EVALUATING SOLAR DISINFECTION FOR POINT-OF-USE WATER TREATMENT IN NON-TROPICAL CLIMATES by Julia Parsons B.S., Environmental Engineering (2001) Massachusetts Institute of Technology Submitted to the Department of Civil and Environmental Engineering in Partial to Fulfillment of the Requirements for the Degree of Master of Engineering in Civil and Environmental Engineering at the Massachusetts Institute of Technology June 2002 ©2002 Julia C. Parsons All rights reserved The author hereby grants to MIT permission to reproduce and to distribute publicly paper and electronic copies of this thesis document in whole or in part. Signature of Author.................................... .. ................... . . . . . Department o$vil and Environmental Engineering May 10, 2002 C ertified by............................ ...................... ..Daniele(Lan ne Lecturer in Civil and Environmental Engineering Thesis Supervisor td A ccee .............. y....... Oral Buyukozturk Chairman, Departmental Committee on Graduate Students MASSACHUSETTS INSTITUTE OF TECHNOLOGY JUN 3 2002 LIBRARIES BARKER EVALUATING SOLAR DISINFECTION FOR POINT-OF-USE WATER TREATMENT IN NON-TROPICAL CLIMATES by JULIA PARSONS Submitted to the Department of Civil and Environmental Engineering On May 17, 2002 in partial to fulfillment of the requirements for the Degree of Master of Engineering in Civil and Environmental Engineering ABSTRACT SOlar DISinfection (SODIS) is a simple water treatment method using natural solar radiation to inactivate pathogens commonly found in drinking water. This technology involves simply filling transparent PET bottles with contaminated water and exposing the bottles to direct sunlight. SODIS inactivates microorganisms via three mechanisms: (1) DNA alterations by UV, (2) production of photo-oxidative species and (3) thermal inactivation. SODIS works best between 35 0 S and 35'N. Outside of these regions, SODIS works sub-optimally because of the limited availability of solar radiation and the colder climate. In order to assess the applicability of SODIS to colder climates, this study investigated two possible methods of ensuring that SODIS is effective under the conditions of lower temperatures and sunlight intensity: 1) enhancing the heating capacity of the bottle with black paint and 2) increasing the amount of radiation incident on the system using a solar reflector. Additionally, a mathematical model for predicting the expected bottle water temperature of each exposure regime, based on the ambient air temperature, wind, and available solar radiation, was developed. Such a model will be useful in future studies for assessing which type of exposure regime will be most effective. Field studies were conducted in two locations in Haiti: Barasa and Dumay, and in Boston, Massachusetts, between the months of January through March, 2002. Analysis of the data collected showed that clear and half-painted bottles were most effective for microbial inactivation in non-tropical climates (Barasa and Boston). In Dumay, however, significant microbial inactivation was achieved in all bottles because the bottle water temperatures reached were much higher. There was no statistical significance between the amount of inactivation achieved by bottle on a reflector or without a reflector. However, because of the limited amount of data, further studies on the use of solar reflectors are recommended to assess their actual effectiveness. Thesis Supervisor: Daniele Lantagne Title: Lecturer in Civil and Environmental Engineering ACKNOWLEDGEMENTS The author would hereby like to thank the following people for their contribution to this work: My teammates, Sara Elice, Micahel Borucke, Arun Varghese, and my advisor, Daniele Lantagne for all their hard work and support. Gift of Water representatives, Phil Warwick and Matt Cyr, for making this trip possible. My friend, Karl Magdsick, for sharing his technical knowledge and providing emotional support. The Don Don family in Barasa for their hospitality, and Diefu and my little helpers for making sure I had everything I needed in Barasa. Peter Shanahan and Eric Adams for their help in developing the bottle water temperature model. Nathan and Wanda Dieudonne and the Warwick family for their hospitality while I was in transit. Fred Cote from the MIT Edgerton shop, for helping me design and build my solar reflectors. And Amy Smith, for designing and building the phase-change incubator that made this research possible in rural Haiti. 2 TABLE OF CONTENTS I 2 3 4 THE N EED FO R CLEA N W A TER ........................................................................ 6 1.1 Clean W ater in H aiti............................................................................................ 1.1.1 Environm ent of H aiti..................................................................................... 1.1.2 A ssessm ent of w ater resources in H aiti.......................................................... 1.2 G ift of W ater, Inc. ............................................................................................... 1.3 Point-of-use w ater treatm ent options for H aiti................................................... 6 7 9 10 11 A PPLICATION O F SO D IS ................................................................................... 14 2.1 Mechanism s of D isinfection............................................................................... 2.1.1 Therm al Inactivation ................................................................................... 2.1.2 U V Induced DN A Alterations......................................................................... 2.1.3 Photo-O xidative D isinfection........................................................................ 2.2 Required Conditions for SOD IS ......................................................................... 2.2.1 W eather and Clim ate................................................................................... 2.2.2 Turbidity..................................................................................................... 2.2.3 Oxygen ......................................................................................................... 2.2.4 Container M aterial and D esign .................................................................. 2.3 Lim itations ......................................................................................................... 14 14 16 18 19 19 20 20 21 22 RESEA R C H GO A LS..............................................................................................23 3.1 U V enhancem ent .................................................................................................... 3.2 Therm al enhancem ent ....................................................................................... 3.3 Bottle W ater Tem perature model....................................................................... 3.3.1 A bsorption of short-w ave radiation............................................................ 3.3.2 Absorption and emission of long-w ave radiation ....................................... 3.3.3 Convection .................................................................................................. 3.4 Sum mary of Research G oals .............................................................................. 23 25 26 27 29 30 31 RESEA R C H O UTLIN E ......................................................................................... 32 4.1 Location, Clim ate and W ater Supply ................................................................ 4.1.1 B arasa.............................................................................................................. 4.1.2 D um ay ......................................................................................................... 4 .1 .3 B o ston .............................................................................................................. 4.2 Exposure and M onitoring................................................................................... 4.2.1 M icrobial A nalysis ....................................................................................... 32 32 35 36 38 40 3 5 RESU LTS .................................................................................................................43 5.1 Bottle W ater Tem perature ...................................................................................... 43 5 .1 .1 B ara sa .............................................................................................................. 4 3 5.1.2 D um ay ............................................................................................................. 44 5 .1 .3 B o ston .............................................................................................................. 4 5 5.1.4 Sum m ary .......................................................................................................... 46 5.2 M icrobial inactivation ............................................................................................ 47 5.2.1 Barasa .............................................................................................................. 48 5.2.2 D um ay ............................................................................................................. 51 5.2.3 Boston .............................................................................................................. 52 5.2.4 Sum m ary ......................................................................................................... 54 5.3 Evaluation of Results ............................................................................................. 55 5.3.1 Barasa .............................................................................................................. 55 5.3.2 D um ay ............................................................................................................. 55 5.3.3 Boston .............................................................................................................. 56 5.4 Statistical analysis .................................................................................................. 56 5.4.1 Evaluating the Effectiveness of Each Regim e ................................................ 57 5.4.2 Evaluating the U se of Solar Reflectors ........................................................... 60 5.4.3 Sum m ary ......................................................................................................... 61 5.5 Bottle W ater Tem perature Model ........................................................................... 62 6 CO N CLU SIO N S ......................................................................................................67 6.1 Therm al Enhancem ent ............................................................................................ 67 6.2 U V enhancem ent .................................................................................................... 68 6.3 Sum m ary ................................................................................................................ 69 REFEREN CES ................................................................................................................71 APPEN D IX 1: RESEAR CH PLAN ...............................................................................73 APPENDIX 11: DATA SUMMARY AND ANALYSIS ............................................... 88 APPENDIX III: BOTTLE WATER TEMPERATURE MODEL ........................... 113 4 FIGURES AND TABLES 7 Figure 1.1 Map of Haiti (Lonely Planet, 2001).............................................................. 11 Figure 1.2 G W I gravity filtration system .......................................................................... 13 Figure 1.3 SOlar water DISinfection system ............................................................... 14 Figure 2.1 Electromagnetic Spectrum (Modified from PSU, 2001) ............................. 17 Figure 2.2 Formation of pyrimidine dimers in DNA .................................................... 19 Figure 2.3 Effective area for SODIS application. .......................................................... 24 Figure 3.1 Top view of solar reflector used .................................................................. mylar....................24 foil, Right: aluminum Left: aluminum Solar reflectors, Figure 3.2 Figure 4.1 Average daily temperature and radiaiton profiles for Barasa ...................... 33 34 Figure 4.2 Pictures of Barasa community water source................................................ 34 Figure 4.3 Temporary water storage for experiments in Barasa ................................... 36 Figure 4.4 Ambient air temperature profile for Dumay ................................................ Figure 4.5 Average daily temperature and radiation profiles for Boston......................37 38 Figure 4.6 Calendar of research in Barasa .................................................................... 39 Figure 4.7 Calendar of research in Boston .................................................................... Figure 4.8 Kipp & Zonen Solar Radiation Measurement System.................................40 40 Figure 4.9 M icroanalysis equipm ent.............................................................................. 44 Figure 5.1 Bottle water temperature profile for Barasa................................................ 45 Figure 5.2 Bottle water temperature profile for Dumay................................................ 46 Figure 5.3 Bottle water temperature profile for Boston ................................................ 48 Figure 5.4 Percent bacteria kill after 5-hours exposure in Barasa................................ Figure 5.5 Percent bacteria kill after 1-day exposure in Barasa....................................49 50 Figure 5.6 Percent bacteria kill after 2-days exposure in Barasa .................................. 51 Figure 5.7 Percent bacteria kill after 5-hours exposure in Dumay................................ 52 Figure 5.8 Percent bacteria kill after 5-hours exposure in Boston ............................... 53 Figure 5.9 Percent bacteria kill after 1-day exposure in Boston ................................... 54 Figure 5.10 Percent bacteria kill after 2-day exposure in Boston .................................. Figure 5.11 Bottle water temperature and climate conditions in Barasa ...................... 55 64 Figure 5.12 Clear bottle water temperature model....................................................... Table Table Table Table Table Table Table 1.1 1.2 4.1 5.1 5.2 5.3 5.4 Reported cases of water-related illnesses in 1980 (USAID, 1985).................7 Groundwater potentials for selected areas in Haiti (USAID, 1985) .............. 10 35 WaterTurbidity Data for Barasa.................................................................... 58 Statistically significant microbial kill after 5-hour exposure ....................... Statistically significant microbial kill after 1-day exposure ......................... 59 Statistically significant microbial kill after 2-day exposure ......................... 60 63 Beaufort Scale (Petterssen, 1969) .................................................................. 5 1 The Need for Clean Water Access to clean drinking water is one of the world s most daunting development challenges. The United Nations Development Program estimates that 1 billion people today lack access to a safe, adequate water supply (Reed et al., 2000). Clean water is essential to maintaining human health because waterborne pathogens cause diseases such as cholera, typhoid fever, and diarrhea (Cadgil and Shown, 1995). These pathogens usually originate from an infected host (either human or animal) and are transmitted by contaminated water through the fecal-oral route (Maier, 2000). There are over 800 million cases of diarrhea reported each year, of which about 5 million result in death (Wegelin, 1994). Waterborne diseases kill more than 400 developing world children every hour (Cadgil, 1995). Waterborne diseases can be successfully controlled through the protection and treatment of water supplies. However, in the absence of treated water, people draw water from contaminated sources that contain the disease-causing pathogens such as bacteria, viruses, protozoa, and helminthes. Centralized water treatment facilities are common in developed countries but are considered too capital-intensive to be implemented in many developing countries (Cadgil, 1995). In addition, when such infrastructure does exist in developing countries, it is usually limited to urban communities. 1.1 Clean Water in Haiti Haiti is both the poorest and most densely populated country in the western hemisphere (US Dept of State, 1998), and one of the poorest countries in the world. Eighty percent of the population lives below the poverty line (CIA, 2002), and seventy percent lives in rural areas (US Dept of State, 1998). Haiti has been plagued by political unrest for most of its history, and as a result lacks the resources for adequate water and sanitation infrastructure. Diarrhea is the leading cause of mortality in children under five years of age, with an incidence of 47 percent in 6-11 month olds (Pan American Health 6 Org., 2002). As shown in Table 1.1, water related diseases are particularly common in rural areas where potable water is rare (USAID, 1985). Table 1.1 Reported cases of water-related illnesses in 1980 (USAID, 1985) Diarrhea Area Port-au-Prince Gonaives Port-de-Paix Hinche St-Marc Petit-Goave Belladere Jacmel North Dept. South Dept. Population 6,500,000 33,000 15,000 10,000 23,000 7,000 25,000 13,000 560,000 500,000 Cases 6608 255 455 694 851 294 875 320 3145 1909 /1000 10.2 7.7 30.3 69.4 37.0 42.0 350 24.6 5.6 3.8 Intestins Cases 4694 167 2171 738 314 1357 272 152 6819 2380 /1000 7.2 5.1 145 74 13.7 194 109 11.7 12.2 4.8 Typhoid Cases 460 11 114 100 266 2 68 87 141 462 /1000 0.7 0.3 7.6 10.0 11.6 0.3 27.2 6.7 0.3 0.9 1.1.1 Environment of Haiti Haiti shares the island of Hispanola with the Dominican Republic, encompassing 27,750 square kilometers on the western one-third of the island (CIA, 2002). It is located roughly 600 miles south of Florida and 300 miles north of Venezuela, near the center of the West Indies, at 180 to 200 N latitude and 71' to 740 W longitude. It has two large peninsulas (Figure 1.1), called the northern and southern claws, which are separated by the Golfe de la Gon ve. Figure 1.1 Map of Haiti (Lonely Planet, 2001) 7 The name Haiti comes from the Arawak word for 'mountainous land'. This name is more than fitting for Haiti, as 60 percent of all its terrain is on gradients of 20 percent or steeper (Lonely Planet, 2001). The main mountain ranges in Haiti include the Massif de la Hotte on the southern claw, the Massif de la Selle, running west to east just southeast of Port-au-Prince, and the Chaine du Bonnet in the north. Haiti also boasts astounding biodiversity, including 5,000 plant species and 25 endemic bird species. However, only two mammals native to the island still survive in Haiti: the Hispaniolan hutia (mole-like) and the solendon (long-nose rodent). The climate of Haiti is generally hot and humid, with temperatures varying more over the course of a day than from season to season. Highs are generally around 30iC, while nighttime lows can reach 20iC. The summer in Haiti lasts from June to September, and can be slightly hotter than the winter (February to April), though temperatures drop markedly at higher elevations (Weil et al, 1985). Haiti also has a rainy season, which varies with region (in the north, October to May; and in the south, May to October), and a hurricane season, which usually lasts from June through September (Lonely Planet, 2001). Rainfall is usually from the North and East over the mountains. Thus there is more rain in the North and highlands (Weil et al, 1985). One of the most detrimental environmental issues facing Haiti is that of deforestation. Ninety-eight percent of the original tropical forest in Haiti has been deforested for export crops and fuelwood (Lonely Planet, 2001). Deforestation also has detrimental impacts on water quality because of increased erosion of the now-barren hillsides. Erosion has also been the major cause of loss of rich topsoil to the sea, where it chokes the reefs and marine life. However, there are four national parks established in Haiti to preserve what is left of the remaining virgin forest: For t des Pins, in the southeast next to the Dominican border; Parc La Visite, with limestone caves and rainforests 40km southwest of Port-au-Prince; Parc Macaya, at the western end of Haiti's southern claw; and Parc Historique La Citadelle, in the center of the Massif du Nord, near Cap-Ha tien. 8 1.1.2 Assessment of water resources in Haiti Only four percent of the governmental budget is allocated for potable water projects in Haiti, accounting for 15 percent of the total budget for such projects (USAID, 1985). The additional 85 percent of the funding for these projects comes from external assistance. There are two main organizations responsible for managing water resources in Haiti. The Centrale Metropolitaine d Eau Potable (CAMEP) is responsible for supplying water in the metropolitan area and the Service National d Eau Potable (SNEP) is responsible for rural water supply. Both organizations disinfect their water supply with chlorine, but this treatment is irregular and unreliable. CAMEP supplies water to approximately fifty percent of its potential customers and SNEP supplies approximately 39 percent (USAID, 1985). The rest of the population relies on private Haitian water vendors, whose water is from unprotected sources and rarely disinfected, or other local water resources such as wells and surface water. The amount of water in Haiti, including surface water, groundwater, and springs, is believed to be sufficient supply for the entire population (USAID, 1985). However, these resources are limited by lack of access and proper treatment. Groundwater is believed to be abundant, particularly in the coastal plains where it is easy to access (Table 1.2). Groundwater is generally of better quality than surface water, for as water seeps through the soil to the water table, many microorganisms are removed (Lehr, 1980). Additionally, water quality often improves with storage in the aquifer because conditions are not favorable for bacterial survival. A properly constructed well (in addition to proper collection and storage methods) can ensure that the water remains clean and is safe for use. 9 Table 1.2 Groundwater potentials for selected areas in Haiti (USAID, 1985) Region Number of Project Area Number of Project Aquifers Prj__AePec North and North Western Region Artibonite Region Southeast Coastal Region South Coast Region Central Plains Region Total _qu _r Potential No. of Aquifers for which Water flow (tlsec) flow was estimated 7 13 7 500-685 2 3 2 5 2 399-1114 5 3 2 530+ 5 6 1 15-45 22 29 12 1444-1844 Springs (places where groundwater has come to the surface) and surface waters are much more susceptible to bacteriological contamination than groundwater. Therefore, surface water should only be used when groundwater sources are unavailable or inadequate (Lehr, 1980). Surface water flow in Haiti is irregular, with short torrential flows during the rainy season and long periods of dryness - very few rivers have permanent flow (USAID, 1985). However, because groundwater in Haiti is often difficult to access, surface water and springs are the main water source for the Haitian people. 1.2 Gift of Water, Inc. The main religion in Haiti is Christianity, predominantly Roman Catholic (U.S. Department of State, 1998). In Haiti the church is the foundation of the community. The church often coordinates community infrastructure such as schools, government, and facilities. Therefore, the Haitian people have a very high respect for the church and work associated with them. One U.S. based organization that works mainly through the churches in Haiti is Gift of Water, Incorporated (GWI). In 1995, the non-profit Industry for the Poor, Inc. (PI), (now Gift of Water, Inc.) was created by Phil Warwick to investigate clean water options for the people of Haiti. After conducting epidemiological studies in conjunction with the Adopt-A-Village Medical Mission, they developed an in-home gravity water 10 filtration system (Figure 1.2) intended to reduce the presence of bacteria and volatile chemicals in the drinking water. Figure 1.2 GWI gravity filtration system The filter apparatus costs US$15.29, but is subsidized by the program so that each family must only pay approximately US$1.85 or even less (Anarchy, Inc., 2000). Operating expenses for each filter, including chlorination and granular activated carbon, amount to approximately US$0.42 per year. Since being approved by the Haitian Ministry of Health, filters have been placed in seven villages across Haiti (Lantagne, 2001), serving over 22,000 people (Anarchy, Inc., 2000). Because of their extensive contacts and knowledge of Haiti, GWI representatives assisted in choosing appropriate study locations, and making arrangements for travel and research necessary for this study. 1.3 Point-of-use water treatment options for Haiti The estimated cost of providing worldwide water supply coverage in developing countries is US$150 billion (Wegelin, 1994). This cost cannot possibly be met by public funds, which are insufficient to even cover the costs of maintenance of the current infrastructure. An alternative to public water supply for people in developing countries is the use personal household water treatment systems, or point-of-use water treatment systems. 11 The most effective point-of-use water treatment usually consists of two stages: filtration and disinfection. In order to be most effective and appealing to it s users, a point-of-use water purification system should fulfill the following criteria (Lehr et al., 1980; Shultz et al, 1984): * Effective across a range of pathogens; * Robust to changes in water quality; " Effective in appropriate pH and temperature range; * Should not make water toxic or unpalatable; " Safe and easy to handle; " Must provide residual protection against possible recontamination; " Affordable; " Adaptable to local conditions; * Amenable to local production; * Appropriate to local culture and customs; " Comply with national sanitation standards; Current household disinfection mechanisms include boiling water, filtration, and chlorination. However, boiling water requires energy in the form of fuelwood, which can be rare in rural areas of Haiti due to deforestation, and additionally exacerbate deforestation. The use of chlorine is often rejected by users because of the undesirable taste and odor associated with it, as well as because of its cost and unreliable supply and quality. Filtration techniques are also often unaffordable and such systems are subject to leaking and breakage. A more reliable and less expensive water disinfection technique is Solar Disinfection. SOlar DISinfection (SODIS) is a simple water treatment method using natural solar radiation to inactivate pathogens commonly found in drinking water. This technology involves simply filling transparent PET bottles with contaminated water and exposing them to direct sunlight (Figure 1.3). SODIS utilizes the power of the sun to 12 inactivate microorganisms using UV-A radiation and increased temperature. Because this technology is so simple, both in concept and application, it is easily applicable in the developing world where safe water resources are scarce. However, the success of SODIS is dependent on a number of conditions, including climate and water clarity. Figure 1.3 SOlar water DISinfection system The pioneer of solar disinfection technology was Professor Aftim Acra, of the American University of Beruit (SANDEC, 2001). His work motivated the Integrated Rural Energy Systems Association (INRESA) to investigate the application of SODIS through a network project, which was reviewed at a workshop in 1988 organized by the Brace Institute of Montreal. In 1991 the Swiss Federal Institute for Environmental Science and Technology s (EAWAG) Department of Water Sanitation in Developing Countries (SANDEC) undertook extensive laboratory and field tests to analyze the effectiveness and social acceptability of SODIS as a low-cost water treatment method. Currently SANDEC is promoting the use of SODIS by providing information, technical support, and advice on SODIS to institutions in developing countries worldwide (SANDEC, 2001). To date, successful SODIS studies have been completed in Columbia, Bolivia, Burkina Faso, Togo, Indonesia, Thailand, and China. 13 2 Application of SODIS 2.1 Mechanisms of Disinfection The SODIS methodology utilizes both the infrared and ultraviolet spectra of radiation to disinfect water. The infrared spectrum is absorbed to generate heat and increase the bottle water temperature, and the ultraviolet spectrum directly inactivates microorganisms. The infrared spectrum is usually defined as electromagenetic radiation with wavelengths above 1 000nm (10,000 ), and the ultraviolet spectrum is radiation with wavelengths between 4 and 400 nm (40-4000 ) (Koller, 1952), However, the atmosphere absorbs all radiation of wavelengths less than 200 nm (Parrish et al, 1978). Typically the remainder of the ultraviolet spectrum is divided into three portions: UV-C (200 to 290 nm); UV-B (290-320 nm); and UV-A (320-400 nm) (Figure 2.1). Of these, UV-A radiation is most abundant at the earth s surface. ULTRAVIOLET C INFRARED B A VISIBLE 21 40 JO 4 %161 5(J09U Wavcrleig0 & MY - 7 ON4 20100 40001) Anrtra-m Units Figure 2.1 Electromagnetic Spectrum (Modified from PSU, 2001) 2.1.1 Thermal Inactivation The first mechanism of disinfection utilized by SODIS is thermal inactivation of microorganisms. Microorganisms can only function within certain temperature ranges because of limitations of their metabolism. When these temperatures are exceeded, proteins and other macromolecules are denatured and the microorganism loses its ability to function properly (Madigan, 2000). It is possible to disinfect drinking water without 14 reaching boiling temperatures. This process, known as pasteurization, is different from sterilization in that sterilization inactivates all microorganisms, including heat-resistant spores. However, heat-resistant spores are harmless for humans to eat, and thus pasteurized water is sufficient for drinking purposes. For E.coli, a pathogen causing diarrhea, pasteurization occurs above 70 0 C (Wegelin et al, 1994). Microbial inactivation is also possible at temperatures below pasteurization temperatures. Between 20 to 40 0 C, the inactivation rate of fecal coliforms remains constant (Wegelin et al, 1994). Above temperatures of 50 0 C, microbial inactivation is enhanced through the synergistic effects of UV and temperature. At temperatures lower than 20 0 C however, the thermal inactivation effects are negligible and therefore photobiologic effects (i.e. UV and photo-oxidative) are the main modes of disinfection. The temperature of the SODIS system is increased by the absorbance of both long and short wave radiation by the bottle and the water, which then generates heat in the system. Some of this heat is re-emitted as back-radiation from the bottle into the atmosphere. Additionally, the system gains or looses heat through convective exchange with the air. The addition of wind can enhance convective exchange, thus increasing the rate of heating/cooling. In order to prevent rapid cooling, a wind-shield would be desirable to protect the bottles from heat loss, provided the shield does not shade the bottles. Additionally, uneven exposure can cause uneven heating, which causes a thermal gradient and induces circulation in the bottle (Wegelin et al., 1994). Because it is difficult to determine when water reaches pasteurization temperatures without thermometers, a device known as a Temperature Sensor has been developed for use in developing countries (SANDEC, 2001). This device contains soy wax, which melts just below pasteurization temperatures. When the wax melts it drops to the bottom of the indicator, so that even if the water cools again it is obvious that the threshold temperature was reached. 15 2.1.2 UV Induced DNA Alterations Another inactivation mechanism of solar disinfection is the direct effects of UV induced DNA alterations. Ultraviolet radiation is more biologically active than visible light because it is made of higher energy photons (Parrish et al, 1978). When photons are absorbed, all of their energy is transferred to the absorbing atom or molecule, which brings it to an excited state. While in this excited state, changes may occur in the molecule such as rotation, vibration, or changes to the orbital shells. Ultimately, photochemical reactions may be induced if the energy of the absorbed photon is greater than or equal to the activation energy required for a reaction. The typical activation energy for most biological photochemical reactions is between 40 and 100 kcal/mol, making UV light highly effective in causing photobiologic effects because of the amount of energy it contains (Table 2.1). Table 2.1 Energy associated with various ultraviolet wavelengths (Parrish, et al, 1978) UV Band UV-C UV-B UV-A Wavelength Energy (kcal/mol) 200 250 280 300 360 143 114 102 95 79 420 72 The alteration of DNA molecules by UV radiation is the result of photochemical reactions within the cell. The peak amount of energy that can be absorbed by many bacteria corresponds to a wavelength of 260 nm, which is the maximum for absorbance by aromatic amino acid residues and their proteins (Parrish et al, 1978). Therefore, it appears that UV-C and UV-B radiation would be the most effective in the inactivation and killing of bacteria through photochemical alteration of cellular DNA. However, studies have shown that 104-105 times more UV-A radiation (either intensity or exposure time) can have the same inactivation effect as the lower wavelengths. 16 Because DNA has a maximum UV absorbance of approximately 260 nm, exposure to radiation of lower wavelengths causes mutagenesis, resulting in death of the cell (Raven and Johnson, 1996). UV light absorbed by microbial DNA causes the covalent bonding of adjacent bases (commonly thymine-thymine, cystosine-cystosine, and thymine-cystosine), which form pyrimidine dimers (Figure 2.2) (Parrish et al, 1978). DNA replication is prevented by this mutation because nucleotides either cannot properly pair with the thymine dimers, or the dimers are replaced with faulty base pairs. If these mutations are perpetuated they prevent protein synthesis, which blocks metabolism and causes the organism to die. Figure 2.2 Formation of pyrimidine dimers in DNA Additionally, hydrated pyrimidines, cross-linked DNA, DNA strand breakage, local disruption of hydrogen bonds, and changes to RNA can occur when cells are irradiated with UV (Parrish et al, 1978). All of these result in disrupted RNA synthesis and cell replication, likely resulting in death. Cell protein structure; and enzyme activity are also affected by UV irradiation, but in comparison to the effects of DNA disruption, they are negligible. Some microorganisms have adapted to UV exposure by the production of repair enzymes and protective pigments. In most microbial populations the resistant fraction comprises only 0.01 percent, though some studies suggest it can be as high as 10 percent for certain species (Kowalski and Bahnfleth, 2000). In cases of massive exposure, damage is too extensive for these mechanisms to repair. UV-A radiation has also been 17 shown to damage these DNA repair mechanisms (Parrish et al, 1978). For example, the photoreactivating enzyme is both destroyed and activated by UV-A, and excision repair and single strand break repair mechanisms may be inhibited. Additionally, UV-A of about 365nm appears to alter active transport processes, proteins, and other enzyme activities. According to SANDEC News, No. 3, total solar energy of 555 W/m 2 is necessary to induce these lethal UV effects at temperatures between 20-40C. This is equivalent to mid-latitude, midday summer sunshine (Wegelin, 1994). At temperatures of 50'C, only one-third as much energy is required for equivalent disinfection. Therefore, exposure to sunlight of lower intensity for longer periods of time would provide the same amount of total energy as higher intensity sunlight for a shorter period of time. Therefore, for the application of SODIS, the less radiation that is available, the longer exposure time is necessary to achieve sufficient microbial inactivation. Solar radiation also attenuates with depth through water. Therefore, shallower water parcels will be exposed to more intense radiation than deeper parcels. However, circulation induced by the thermal gradient would ensure that each water parcel is exposed to direct radiation (Wegelin et al., 1994). 2.1.3 Photo-Oxidative Disinfection A third mechanism of disinfection that is utilized by the SODIS system is photooxidative disinfection. Highly reactive forms of oxygen, including oxygen free radicals and hydrogen peroxides, are formed in well-oxygenated water when exposed to sunlight (SANDEC, 2001). These species are so reactive that they can cause serious damage to living cells if formed in significant amounts (McKee and McKee, 1999). These reactive forms of oxygen inactivate microorganisms by oxidizing microbial cellular components, such as nucleic acids, enzymes, and membrane lipids (Reed, 1996). This damage results in enzyme inactivation, polysaccharide depolymerization, DNA breakage, and membrane 18 destruction. These mechanisms either prevent proper cell replication or cause mutations, which are propagated through replication. 2.2 Required Conditions for SODIS 2.2.1 Weather and Climate The optimal region for use of SODIS is between 150 and 35 N latitude (Figure 2.3), a region characterized by high solar radiation and limited cloud coverage (the second most optimal region for SODIS is between the equator and 15'N latitude) (SANDEC, 2001). It should be noted that the majority of developing countries lie within this region. According to SANDEC, within this region and during optimal weather conditions (less than 50 percent cloudy), the contaminated water needs to be exposed for 6 hours to achieve total disinfection. If the sky is more than 50 percent cloudy, or the bottle water temperature does not exceed 420 C (necessary to induce synergistic effects), the bottle should be exposed for two consecutive days. PIME MERNDAN a, EQUATOR EQUATC Figure 2.3 Effective area for SODIS application. For practical application of SODIS in developing countries, where there is no accurate way of judging cloud cover or bottle water temperature, an exposure time of two days has been recommended as the standard SODIS procedure (Oates, 2001). Outside of the regions mentioned above, SODIS works sub-optimally because of the limited 19 availability of solar radiation and the colder climate. Often longer exposure can ensure the effectiveness of SODIS under these conditions, as the UV and photo-oxidative effects of the sunlight dominate the disinfection process, as opposed to thermal effects. However, the optimal length of exposure under different conditions has not been extensively investigated in the literature. 2.2.2 Turbidity In order for SODIS to be effective, the water must be relatively clear (turbidity less than 30 NTU) (SANDEC, 2001). This is because suspended particles in the water can absorb solar radiation, thus reducing the depth to which solar radiation penetrates and protecting some microorganisms from radiation. Therefore, water with turbidity greater than 30 NTU would need to be filtered or bottle water temperature of 50'C must be reached in order to achieve pasteurization. In order to overcome the technical burden of exactly measuring turbidity, SANDEC has developed a simple method for determining whether or not water is suitable for SODIS. For this method, a full bottle is placed on top of the white SODIS logo in the shade. If the logo can be seen through the bottle, then the turbidity can be assumed to be less than 30 NTU. If the results are questionable, a higher turbidity should be assumed and the water treated accordingly (SANDEC, 2001). Such treatment may necessitate filtration, though usually allowing particles to settle and decanting the water off the top is sufficient. 2.2.3 Oxygen In order to maximize the production of photo-oxidative species in the water, it is necessary to make sure the water is well aerated. In order to do this, one can shake the bottle when it is only half full, and then fill it completely (SANDEC, 2001). This technique should especially be applied to stagnant waters, such as from cisterns and wells. Reed (1997) recommends repeating this process hourly to ensure aeration is maintained. However, the effectiveness of this repeated agitation has been questioned by 20 Kehoe, et al. (2001). They found that repeated agitation had no effect on the amount of inactivation achieved. 2.2.4 Container Material and Design The most common type of container used for SODIS are PET (PolyEthylene Terepthalate) bottles. These bottles are preferred because they are commonly available, more lightweight and durable than glass, and are more chemically stable than other plastics. However, glass bottles have higher transmittance than plastic bottles (75 percent for glass versus 70 percent for plastic), so some transmittance is lost in using plastic bottles. Plastic bags have an even higher transmittance (90 percent), but are significantly less durable than either glass or plastic bottles and are also difficult to use. PET bottles can easily be distinguished from other bottles because of its clear appearance as compared to PVC, which has a bluish gleam. Additionally, PET bums more easily than PVC and the smell is sweeter than that of PVC. However, one significant drawback to the use of these bottles in comparison to glass is the rate at which they age due to mechanical scratches and the production of photoproducts, which leads to a reduction of UV transmittance (SANDEC, 2001). Because these bottles are commonly available in the developing world, this is not considered a significant problem because aged bottles can be easily replaced. Another concern with the use of PET bottles is the possible formation of photoproducts on the plastic material as a result of UV-irradiation. These photoproducts are the result of the migration of additives out of the material, such as the UV stabilizers that are used to increase the plastics stability (SANDEC, 2001). However, in PET these additives are used less than in PVC (less than one percent of the PET components). Laboratory and field test addressing this concern have shown that these products are generated only on the outer surface of the bottles, and no migration into the water was observed. 21 In addition to the container material, one must also consider the size and shape of container most effective for SODIS. Because UV radiation attenuates with depth (50 percent attenuation at 10 cm with turbidity of 26 NTU), containers with a large exposed surface area to volume ratio are recommended. PET bottles used for SODIS have a suboptimal shape because this ratio is small (SANDEC, 2001). With a water depth of 610cm, the water is not as evenly exposed to radiation as in a flatter container, such as a bag. However, this uneven exposure can cause uneven heating, which causes a thermal gradient and induces circulation in the bottle, which would ensure that each water parcel is exposed to direct radiation at some time (Wegelin et al., 1994). Thus, although containers with a larger exposed area to volume ratio would be more efficient, in the developing world, one must learn to efficiently use whatever is available. 2.3 Limitations Although SODIS seems to be the ideal solution for drinking water disinfection, as it requires no chemicals or technical expertise, it does have limitations. First, SODIS does not improve the chemical water quality, though studies are being undertaken to assess the effectiveness of UV-radiation in arsenic abatement, nor does it change the smell or taste of the water (SANDEC, 2001). The effectiveness of SODIS is also dependent on climate and certain water quality parameters, such as turbidity and dissolved oxygen, as discussed above. However, the user can easily adjust both of these parameters so that SODIS is effective (filtering/settling to reduce turbidity, mixing to increase oxygen). Additionally, SODIS offers only a very limited production capacity because of the limitations to bottle size/shape available, and therefore may not be a feasible solution for generating large quantities of clean water. 22 3 Research Goals In order to assess the applicability of SODIS to colder climates, it is necessary to investigate possible ways of modifying the present system so as to make most efficient use of the available conditions. Though the area in which SODIS should be applicable based on the amount of available sunlight is very broad, some of the locations that fall within this region occasionally experience climate conditions not optimal for SODIS use due to elevation and seasonal variances. For example, the winter season has higher cloud cover associated with colder temperatures, during which SODIS may not be effective. Additionally, at higher altitudes, although sunlight intensity may be stronger, cloud cover is also much more common and temperatures much cooler. Two possible methods to ensure that SODIS is effective under the conditions of lower temperatures and sunlight intensity are: 1) to enhance the heating capacity of the bottle or 2) to increase the amount of radiation incident on the system. The former can be achieved by painting the bottles with black paint, which absorbs solar radiation and converts it to heat energy. The later can be achieved through the use of solar reflectors to gather and focus UV onto the bottle. The purpose of this thesis was to investigate the effectiveness of both of these methods in sub-optimal climate conditions. 3.1 UV enhancement Most metals are good reflectors for both visible and ultraviolet light (Koller, 1952). The efficiency of reflection depends on the cleanliness of the surface and absence of impurities. Aluminum is one of the most commonly used reflective metals because it is relatively inexpensive, easy to use, and resistant to corrosion. It is considered one of the most suitable for UV applications (Parrish, 1978). The shape of the reflector also influences the effectiveness of reflection. Parabolic reflectors are particularly good for focusing light on one point. However, their round shape would not efficiently focus light 23 on the elongated SODIS bottles. Flat reflectors on the other hand, are less efficient because they do not focus the light at all. The reflector used in this study consists of two parallel "slings" of reflective material supported by rope (clothesline) hung between two wooden base pieces (Figure 3.1). One reflector was built using aluminum coated mylar and another was built using materials that would be available in a developing country (aluminum foil supported by a plain brown paper). Each "sling" held three bottles end-to-end (for a total of six bottles per reflector). The reflector should be oriented parallel to the path of the sun (approximately east to west) so as to minimize shadows (Figure 3.2). Supporting Ropes Figure 3.1 Top view of solar reflector used Figure 3.2 Solar reflectors, Left: aluminum foil, Right: aluminum mylar All reflectors use in this study were built at MIT and designed to be transportable, and so had to be light and compact. Therefore, these reflectors consisted of numerous 24 small parts, which were easy to reassemble (see assembly instructions in the research plan in Appendix I) The dimensions of such reflectors could be optimized based on the size of the bottles used, however, the bottle size for each location of this study was not known at the time the reflectors were built. Therefore they may not have been as effective as was possible, though it is estimated that no more than 20 percent effectiveness was lost. 3.2 Thermal enhancement The recommended SODIS procedures call for painting bottles half black to enhance the heat absorbance capacity of the system (SANDEC, 2001). Theoretically, this increases the bottle water temperature by 50C by absorbing extra radiation. However, the amount of temperature increase is dependent on the available amount of radiation to be absorbed and the area and orientation of the surface painted black. This study investigated the thermal enhancing effects of painting bottles both half black and fully black to see if threshold temperatures could be reached despite low ambient air temperatures in areas where radiation is abundant. The bottles were painted using locally available flat black paint, following the procedure outlined in the research plan in Appendix I. The purpose of painting the bottles half black is allow for both thermal enhancement as well as UV disinfection, whereas the fully painted bottle will rely on thermal inactivation alone. Therefore the fully painted bottles must reach the threshold temperature of 50 0C to achieve disinfection. These temperatures were not necessary in the clear and half painted bottles because UV disinfection would be active in these bottles. The main mechanism of heat gain in the SODIS system is the absorbance of solar radiation. Additionally, if the ambient air temperature is greater than the bottle water temperature, some heat gain will be made through natural convection. However, because the amount of convection over two bottles of the same size would be equal, the difference 25 in temperature reached in the fully painted bottle versus the half-painted bottle is mainly dependent on the difference in the amount of radiation absorbed by the different systems. Therefore, it is also possible that the use of a solar collector/reflector could contribute to increased bottle water temperatures by increasing the amount of radiation incident on the bottles. 3.3 Bottle Water Temperature model In addition to evaluating the above techniques for enhancing the effects of SODIS, this project also developed a mathematical model for the bottle water temperature under various conditions. Such a model would be useful for evaluating the suitability of SODIS in a particular locale and the techniques that should be used to enhance its effectiveness. The model is dependent on the local weather conditions over the appropriate period of time: Ta(t) ambient air temperature [K] R(t) total solar radiation [W/m 2] U(t) = wind speed [m/s] In order to achieve an accurate model of the exact bottle water temperature under given conditions, these parameters must be monitored in situ. However, for the purposes of evaluating the effectiveness of SODIS, approximate weather conditions can be generated using a weather model or gathered from a local weather station to estimate best- and worst-case scenarios. The model is also dependant on characteristics of the bottle and the water, including: D = bottle diameter [m] x = bottle thickness [m] kp= thermal conductivity of plastic [W/mK] M = mass of water [g] 26 CN = heat capacity of water [J/gK] This model cannot substitute for in situ field tests to evaluate the actual effectiveness of SODIS. These tests are still necessary to make recommendations for factors that are more site specific, such as exposure time and necessary water pretreatment. However, the results of the model can predict whether thermal enhancement measures would be effective or not. There are four main heat flux components to this model: (1) heat generated by short-wave radiation absorbed by the system (QR), (2) heat gain through absorption of long-wave radiation (QL), (3) heat loss through long-wave radiation from the system (Qb), and (4) heat gain/loss by convection (Qc). Therefore, at each time step the net heat flux into the system (QT) is the sum of these quantities: QT = QR + QL + QC - Qb (Equation 1) The net heat flux can then be used to find the change in bottle water temperature over a single time step: dT = QT C_-M dt (Equation 2) where dt is the length of the time step used, in seconds. It should be noted that in comparison to the mass of the water, the mass of the bottle, and thus the heat capacity of the bottle, is negligible. 3.3.1 Absorption of short-wave radiation The main difference in the bottle water temperature in the painted versus unpainted bottles will be the amount of short-wave solar radiation absorbed (i.e. wavelengths shorter than 3000nm). Each regime will absorb a different amount of solar energy based on the amount of surface area painted black (Figure 3.3). 27 Legend Solar radiation -> SUN Attenuating radiation > Reflection Heat radiation Clear bottle Half-painted Fully painted bottle bottle Figure 3.3 Diagram of short-wave solar radiation absorbed by the different bottle regimes Ideally, the fully painted bottle will absorb all available radiation, and thus the heat flux into the bottle due to solar radiation would be equal to: QR = R-Ax (Equation 3) where Ax is the cross-sectional area of the bottle, over which direct radiation is absorbed. In part this equation will underestimate the heat flux because it does not account for scattered radiation absorbed by the system. However, it is also an overestimate because it assumes 100 percent efficiency. For the half painted bottle not all radiation is absorbed because some radiation is reflected off the unpainted surface. Therefore, for the half painted bottle, the amount of solar radiation absorbed is determined by: QR = (1-s)-R-Ax (Equation 4) where , is the percent of the total solar radiation reflected by the bottle. 28 The water in the clear bottle will also absorb some radiation, which is why the intensity of the radiation attenuates with depth as mentioned in Section 2.1.2. For the clear bottle, there will also be reflection off the clear surface. Therefore, the amount of radiation absorbed by the clear bottle system is calculated by: QR = m-(1-z)-R-Ax (Equation 5) where r9 is percent radiation attenuation. 3.3.2 Absorptionand emission of long-wave radiation In addition to short-wave radiation, long-wave radiation also has the potential affect the amount of heat in the system. The amount of radiation transmitted through the material is dependent on the properties of the material. All the radiation that is transmitted through the plastic will be absorbed by the water. This amount is determined by: QL= aaTa4 -As (Equation 6) where c is the percent of long-wave radiation that is transmitted by the bottle, cY is the Stefan-Boltzman constant (5.67E-8), Ta is the ambient air temperature and A, is the total surface area of the bottle through which radiation can be absorbed. The amount of long-wave radiation lost by the system (often referred to as back radiation) is determined through a similar calculation: Qb= s--Ts 4 -As (Equation 7) Where c is the bottle emissivity, and T, is the bottle surface temperature. 29 3.3.3 Convection The direction of heat flow due to convection is dependent on the thermal gradient across the bottle wall. If the air temperature is warmer than the bottle water temperature, than the direction will be into the bottle, but if the air is cooler than the water, heat flow will be out of the bottle. The rate of this heat flow is enhanced by wind flow over the bottle, which increases the number of parcels of air that come in contact with the bottle (Figure 3.4). Wind*T Figure 3.4. Diagram of convective heat exchange with wind For an open water surface, this heat exchange would be governed by the equation for convective heat loss. However, because the plastic bottle acts as a resistor to heat flow, the equation for conductive heat loss is more applicable Qcond -= X (Equation 7) where Ts is the temperature on the outer surface of the bottle, Tw is the bottle water temperature, kP is the thermal conductivity of the plastic, As is the surface area of the bottle and x is the thickness of the plastic. Ts can be found by equating conductive heat flow through the bottle to convective heat flow across the bottle surface (Figure 3.5): s T Tw Figure 3.5 Diagram of convection and conduction 30 Qconv = h-A-(Ta-Ts) (Equation 9) Qcond = Qconv hA(TaTs) = (Equation 8) (Ts-T)-kp-A X (Equation 10) where h =Nu-ka/D, Nu is the Nusselt number (as calculated in Appendix III), and D is the bottle diameter. Therefore, {((Nu ka/D) -Ta) + (kpT,/x)} { (kp/x)+ (Nu-ka/D) } The Nusselt number is dependent on the type of convection (free versus forced) and the shape of the surface over which convection is occurring. Convection over the end of the bottle will be different than convection over the cylinder. Therefore, different calculations must be made for convection over the end and convection over the cylinder, and then summed to find the total convection. 3.4 Summary of Research Goals The main goal of this thesis was to evaluate SOLar DISinfection for use in nontropical climates. Two methods for enhancing its effectiveness under such conditions were investigated: 1) use of black paint to enhance the thermal effectiveness of the system, and 2) use of solar reflectors to enhance the optical effectiveness of the system. In addition, a simple model for predicting the bottle water temperature was developed and evaluated to supplement in situ studies and pre-determine the type of exposure regime that would be most effective in a given climate. 31 4 Research Outline 4.1 Location, Climate and Water Supply Experiments for this study were carried out during the months of January, February, and March 2002. The month of January was spent conducting studies in two locations in Haiti: the rural community of Barasa and the more urban center of Dumay. Follow-up studies were then conducted throughout February and March in Boston, Massachusetts, USA. All of Haiti falls within the optimal latitudes for application for SODIS, and so the locations in Haiti were chosen based on their disparate weather conditions, which are due mainly to differences in elevation. The process for collecting water from the source and transferring it into the SODIS bottles varied with location and ease of access to the source. In some cases samples were taken directly from the source, but in others an intermediate storage container was used. In all cases, background samples for each run were collected at the same time and in the same manner as the filling of the bottles. Additionally, water turbidity measurements were taken before, during and after sample collection using a Hacho Pocket Turbidimeter (accurate to -1 NTU) to ensure that the water was clear enough for effective SODIS application. 4.1.1 Barasa Barasa is located in the southeastern part of Haiti, near the border of the Dominican Republic. The elevation in Barasa is approximately 1,400 feet. This is a mountainous region, characterized by cooler temperatures but more intense solar radiation than Dumay. The daily weather conditions observed usually consisted of approximately half a day of full sunshine (though it varied between morning and afternoon hours) and half a day of partly cloudy or fully overcast skies. The average daily ambient air temperature peaked at about 28 0C around 1pm, and radiation peaked at around 770 W/m 2 a 12:30pm (Figure 4.1). 32 Climate conditions in Barasa Air temperature m 30 s Radiation 5 25 25 - 800 20- - 600 15 400 0. 0 E) 101/ - 200 5 0 0 10 11 12 13 14 15 16 17 18 hour Figure 4.1 Average daily temperature and radiaiton profiles for Barasa Barasa is located in a rural area where there is no access to running water or electricity. Therefore the people in Barasa do not have access to treated water, except for a few families with the Gift of Water, Inc. filtration system. Their main water supplies are cisterns or a nearby spring, Soos San Louis (Figure 4.2). This spring is difficult to access, not only because of its distance from the community, but also because it is located at the bottom of a steep ravine. The spring is highly contaminated, mainly from the fecal matter of pack animals used to transport water back to community members homes. 33 Figure 4.2 Pictures of Barasa community water source Experiments in Barasa were carried out on the roof of the local school so as to avoid disruption by animals or children. The water used for this study was a combination of water from the spring and a nearby cistern. It was collected in large quantities approximately three times throughout the study and stored in large plastic tubs in an empty classroom of the school (Figure 4.3). The SODIS bottles were then filled using a spigoted bucket, following the shaking procedure recommended in Section 2.2.3 to ensure aeration. The average turbidity of the water was 5.8 NTU (Table 4.1), well below the 30 NTU recommended for SODIS to be effective. However, the turbidity peaked at 16.6 NTU on the third day of sample collection, possibly due to agitation of the water which resuspended settled particles, and would otherwise have been only 3.6 NTU. Figure 4.3 Temporary water storage for experiments in Barasa 34 Table 4.1 WaterTurbidity Data for Barasa Run 1:1/17 1/18 2: 1/20 1/21 3: 1/23 1/24 1 2 3 3.5 3.5 4.1 3.5 4.9 2.9 18.2 16.9 14.8 3.6 6.4 4.5 0.6 0.3 8.6 3.8 2.6 1.1 Average: Average without data from 1/20: 5-hour 1-&2-day 5-hour 1-&2-day 5-hour 1-&2-day Ave 3.7 3.8 16.6 4.8 3.2 2.5 5.8 3.6 4.1.2 Dumay Dumay is located near the city of Port-au Prince, at the base of the southern claw of Haiti. Living conditions in Dumay are much better than in Barasa because of its proximity to the metropolis. Many homes have private wells or are connected to the public water supply. Additionally, treated water is released (on average three times) daily from public access facilities. Those who do not have access to these facilities collect water from local wells and streams. Weather conditions are much hotter in Dumay because it is at a lower elevation (very near sea level) and does not benefit from the trade winds that cross the more mountainous regions. During the 5-hour duration of this experiment the sky was clear, there was little breeze, and sunlight was intense. The ambient air temperature peaked at 470 C at 1pm (Figure 4.2). Radiation measurements from this location are not available due to equipment difficulties, but have been assumed to be on the same order of magnitude of daily radiation in Barasa. Experiments were carried out on the roof of Pastor Nathan Dieudonne s house. 35 Ambient Air Temperature in Dumay 50 454035302 25 0. 20 E S15 10 5 010 11 12 13 14 15 hour Figure 4.4 Ambient air temperature profile for Dumay The water used for this study was collected directly from a local stream found running along the streets in a more rural section of the city. Downstream from the site of sample collection, women were found to be doing their laundry, implying that this is a common water source for the local community. Due to the number of poultry and other animals nearby, it can be inferred that fecal matter also contaminated the stream. The same aeration method as used in Barasa was applied during sample collection. The average turbidity of this source was 25.2 NTU, also below the 30 NTU threshold for effective SODIS application. 4.1.3 Boston Boston is located at 42"N latitude, outside the recommended region for SODIS. Water supply and sanitation is not a problem in Boston, as it is an urban center of the developed world. Most residents have access to a reliable treated water supply or private wells. However, contamination is still a problem for area surface waters due to run off from streets, sewer overflows, and point sources. The source used for this experiment was the Charles River, which flows between the cities of Boston and Cambridge 36 Massachusetts, and past the MIT campus where the experiments were conducted. Turbidity measurements are not available for this source because the equipment was not available. However, all samples did pass the SODIS water clarity test, described in Section 2.2.2. The weather in Boston during the time of this study was typical for the winter season in the northern hemisphere. Cold (near freezing) temperatures were observed, peaking at 12*C around 2:30pm, and overcast skies limited available radiation to less than 400 W/m 2 . Because temperature and radiation measurements were taken less frequently than in Barasa, however, the exact peak radiation is not known (Figure 4.3). Additionally, because experiments were carried out on the roof of a four-story building, it was also subject to a constant breeze, which caused additional cooling of the bottles. Climate Conditions in Boston 14.00 - 1- Air temrperature + Radiat ion 12.00 300 10.00 0 (D 250 8.00 -.- C- - 0 200 .2 -Z- 6.00 150 4.00 -----6.0-7.0-8.- 100 2.00 50 0.00 1 H.O0 11.00 12.00 13.00 14.00 15.00 16.00 17.00 18.00 0 19.(00 hour Figure 4.5 Average daily temperature and radiation profiles for Boston 37 4.2 Exposure and Monitoring Nine different SODIS regimes (outlined in Table 4.2) were tested in Barasa. Duplicates were made of the bottles without a reflector and with the aluminum mylar reflector for quality control. Duplicates were not made of the bottles on the aluminum foil reflector due to lack of space. Each regime was tested over 5-hour, 1-day (7-8 hours), and 2-day (two 7-8 hour) exposure periods. Three complete sampling runs (including all regimes and exposure times) were completed, with the first day of the two-day exposure overlapping with the 1-day exposure (Figure 4.6). Table 4.2 Overview of experimental SODIS regimes and their purposes Without Reflector Reflector 1: Aluminum mylar Reflector 2: Aluminum foil Sunday 15 Monda 16 Regime Clear bottle black paint Fully painted Clear bottle black paint Fully painted Clear bottle black paint Fully painted Tuesday 17 Data label C-a C-b C-c UV1-a UV1-b UV1-c UV2-a UV2-b UV2-c Purpose UV UV and enhanced temperature Enhanced temperature Enhanced UV Enhanced UV and temperature Enhanced temperature Enhanced UV Enhanced UV and temperature Enhanced temperature January 2002 Wednesday Thursday 18 19 Friday 20 5-hour Saturday 21 1-day 2-day (1) 2-day (2) Run 1 22 23 5-hour 24 1-day 2-day (2) 2-d 11) Run_2 25 26 5-hour 27 1-day 28 2-day (2) Run 3 Figure 4.6 Calendar of research in Barasa Only the aluminum foil reflector was used in Boston and Dumay because observations made in Barasa determined there was no significant difference between it and the mylar reflector. Therefore, only seven exposure regimes were tested in Dumay 38 and Boston. Additionally, duplicate bottles were not used, but duplicate microbial samples were taken instead. Only one 5-hour exposure regime was completed in Dumay. Two complete sampling runs, plus additional 1- and 2-day exposures were completed in Boston (Figure 4.7). Sunday Monda Tuesda March 2002 Wednesday Thursda Friday 1 Saturday 2 5-hour 2-day (1) 3 4 5 6 5-hour 2-day (1) 7 1-day 2-day (2) Run 9 8 1-day 2-day (1) Run2 1-day 2-day (2) 1 1-day 2-day (2) Run 3 Figure 4.7 Calendar of research in Boston Temperature data was collected from every bottle hourly in Barasa and Dumay, and at least three times a day in Boston. A CheckTemp electronic thermometer from Hanna Instruments, which has an accuracy of ±0.3'C between -20 to 90C, was used for making these measurements. In order to prevent cross contamination during this process, the thermometer was rinsed with boiled water between samples (see research plan in Appendix I.). Ambient air temperature was also recorded each time bottle water temperature measurements were taken. Radiation data was collected hourly in Barasa using a Kipp & Zonen Solar Radiation Measurement System (Figure 4.8). This device measures total solar radiation between the wavelengths of 300 to 2800nm, which includes most UV-B, UV-A, visible, and some infrared radiation. The instrument detects both incoming direct solar radiation and reflected radiation. It works with a one percent accuracy between the temperatures of -40 to 80 0 C. Radiation data was not collected in Dumay due to equipment malfunction, and was collected with the same frequency as temperature data in Boston. 39 Figure 4.8 Kipp & Zonen Solar Radiation Measurement System 4.2.1 MicrobialAnalysis In order to evaluate the effectiveness of each exposure regime, it is necessary to determine the amount of microbial inactivation achieved. In order to do this, both treated and untreated water samples were analyzed using the membrane filtration test methodology (Figure 4.9). In this test, a measured amount of water is passed through a membrane filter (pore size 0.45 gm), which traps the bacteria contained in the sample on a paper filter (Maier, 2000). This filter is then placed on a thin absorbent pad in a petri dish saturated with a culture media specific to a desired indicator organism. The samples are then incubated at 35*C for 18-24 hours to stimulate growth of microbial colonies present. Figure 4.9 Microanalysis equipment 40 The indicator organisms used in this study were E.coli and Total Coliforms. These bacteria normally occur in the intestines of warm-blooded animals and are thus a commonly used indicator of fecal contamination (Maier, 2000). These organisms are also generally hardier than disease causing bacteria, and therefore their absence is a reliable indicator of the absence of other organisms of real concern. Previous extensive research has shown that the absence of these organisms from 10OmL of drinking water ensures the prevention of bacterial waterborne disease outbreaks. The culture media used was m-coli blue broth from Millipore Corporation, on which E.coli colonies grow blue and Total Coliform colonies grow red. The exact process for the membrane filtration technique used in this study is outlined in the research plan in Appendix I. It was necessary to dilute samples with boiled water so that the number of colonies that grew was countable by hand. In Barasa, the first 5-hour run was uncountable because the samples were not diluted and therefore the plates were overgrown by Total Coliforms. Because the need to dilute samples was not anticipated, proper measuring devices were not available. Therefore, the 1 OmL dilution used in Barasa was estimated as halfway to the 20mL mark on the filtration cup. In both Dumay and Boston, the 20mL mark on the sample filtration cup was used, and is therefore more accurate. However, it is not anticipated that any inaccuracies in dilution will have a large effect on calculations because of the order of magnitude differences between samples being compared. Blanks were run for quality control purposes using sterile water and the boiled water used for dilution. The plates were incubated for 24 hours in a phase change incubator, provided by Amy Smith of the MIT Edgerton Center. This incubator does not require electricity, but instead maintains a constant temperature by taking advantage of the phase-change behavior of a material whose melting point is at the incubation temperature required. Once the material is melted, it keeps a constant temperature until it completely solidifies again (Smith, 2002). Therefore, the only energy input necessary to use this incubator was the heat necessary to initially melt the material - which was done by warming it in a pot of boiling water (see instructions for use in Appendix I). After 24 41 hours of incubation, the E coli and Total Coliform colonies on each plate were counted and normalized to a 1 OOmL sample by multiplying by the dilution factor. The membrane filtration technique gives a measure of the absolute number of bacteria present in the sample, so that the percent kill for each regime could then be calculated. 42 5 Results 5.1 Bottle Water Temperature The bottle water temperature for the different regimes and different locations varied greatly because of the thermal enhancement techniques used and the local weather conditions. However, consistent trends with the time of day were observed within the same regime at the same location over different length exposure periods. Therefore, in order to provide a more representative profile of the average bottle water temperature, the data from all exposures (5-hour, 1-day, 2-day (day 1), and 2-day (day 2)) were combined. Individual daily data and data summaries are provided in Appendix II. Following are the resulting temperature profiles for each location in which the study was conducted. 5.1.1 Barasa Bottle Water temperatures in Barasa did not ever exceed the threshold of 50 0 C required for significant thermal disinfection. The temperatures of the bottles on either reflector were not significantly different (i.e. the standard deviation was less than the accuracy of the thermometer) from their counterparts without a reflector. Therefore, the temperature profiles of all three regimes (and duplicate bottles) were averaged in creating the average daily temperature profile (Figure 5.1). 43 Barasa Temperature profile Ambient -a Half-painted 40 - 38- A Full Painted 36 - *Clear 32 230 0.28 26 24 22 10 12 14 16 18 time of day (hou) Figure 5.1 Bottle water temperature profile for Barasa As illustrated in Figure 5.1, the temperature profile of the half-painted bottles was very similar to that of the fully painted bottles. The bottle water temperature in the clear bottle peaked at around 30 0 C, which is not significantly warmer than the ambient air temperature. The bottle water temperature of both the half-painted and fully painted bottles peaked around 38 0 C, approximately 1 OC higher than the ambient air temperature. Therefore, a temperature increase of 8 0C was achieved by painting the bottles - 3C more than indicated in the literature. All of the bottles reached their peak temperatures approximately one hour later than the peak ambient air temperature and radiation. 5.1.2 Dumay The SODIS experiments carried out in Dumay reached much higher temperatures than those in Barasa. This can be attributed to the much warmer and calmer weather conditions observed in Dumay. However, because only one 5-hour experiment was carried out in Dumay, the data is much less representative than that collected in Barasa. As in Barasa, the water temperature of bottles on the reflector were not significantly 44 different from their counterparts, and therefore these data were grouped in creating the temperature profile for each regime (Figure 5.2). Dumay Temperature Profile ambent 60 =-half painted 55 A 50 0 A A full painted U 40 E 35 30 25 20 10 12 14 16 time of day (hou) Figure 5.2 Bottle water temperature profile for Dumay Unlike in Barasa, in Dumay both the painted and half-painted bottle water temperatures exceeded the threshold temperatures necessary for pasteurization for at least one hour. The peak temperature in the clear bottle was 44.5'C, also high enough to induce synergistic thermal effects. The peak temperature reached in the fully painted bottle was 55 0C and in the half painted bottle it was 51 C. This is therefore an increase of approximately 10*C for the fully painted bottle and 60 C for the half painted bottle. Interestingly, the clear bottle water peak temperature was cooler than that of the ambient air temperature of 470 C. All peak bottle water temperatures were all reached approximately one hour later than the peak ambient air temperature. 5.1.3 Boston Temperatures in Boston were significantly cooler than those in either Barasa or Dumay because of its northern latitude and the time of year. Additionally, temperature 45 was not monitored as regularly as at the other sites, and thus the profile is less defined. Again, there was no significant difference in temperature between the bottles on the reflector and those without and so these data were combined to create a more representative profile. The clear bottles appeared to peak at 1 I0C (Figure 5.3). As in Barasa, the painted and half-painted bottles had very similar temperature profiles, and both peaked at 14 0 C, three degrees warmer than the clear bottle, which is not a significant difference given the accuracy of the equipment. Boston Temperature profile * .........- 15 ambi ent - --------........c le ar --half-p ainted 14 A full pa inted 13 12 IF7 0) I-- 11 10 - 12.13.14.15 -. 9 8 10 11 12 13 14 15 16 17 18 19 time (hour) Figure 5.3 Bottle water temperature profile for Boston 5.1.4 Summary Overall, given sufficient climate conditions, painting the bottles was effective for raising the bottle water temperature in this study. Additionally, the amount the temperature was raised as compared to the clear bottles was greater than was indicated in the literature (which is likely a conservative estimate). The results are inconclusive on the effectiveness of painting the bottles half black versus fully black, for in Dumay the 46 temperature increase was different between the two, whereas in Barasa they were very similar. However, in Barasa the temperature increase in the half and fully painted bottles was not sufficient to induce either synergistic effects or pasteurization. The main difference in climate conditions between Barasa and Dumay was the ambient air temperature and wind speed. It can be assumed that the amount of available solar radiation was the same order of magnitude, though measurements for Dumay are not available. If anything, solar radiation would have been more abundant in Barasa because of its higher elevation. Additionally, the temperature profile for Dumay is less complete than that for Barasa, and thus less reliable. 5.2 Microbial inactivation Unlike the bottle water temperature, the amount of microbial inactivation observed in each regime varied more with the amount of exposure than the location. Thus, data from the multiple runs of each exposure length in each location were grouped in order to provide a more representative data set. Individual data from each run, as well as data summaries, are provided in Appendix II along with the bottle water temperature data. The amount of microbial kill (Nk) was calculated by subtracting the number of colonies present in the bottle sample (N,) from the number in the background sample (Nb) collected at the same time (Equation 8). This number was the divided by the background number, and multiplied by 100 for the percent kill (Pk) (Equation 9). Nk= Nb- Ns Pk =(Nk / Nb )*100 (Equation 8) (Equation 9) In some samples the plates were too overgrown to count individual colonies and were therefore labeled Too Numerous to Count. Therefore, in calculating the percent 47 kill for these samples, the largest number of colonies that was counted for a treated water sample during that run was used in substitution for N. 5.2.1 Barasa The amount of microbial inactivation observed in Barasa varied not only with the exposure regime used, but also with the length of exposure. With 5 hours of exposure 100 percent kill was observed for E.coli in the clear bottle regimes on reflectors (UV 1-a and UV2-a) (Figure 5.4). Additionally, 96 percent kill for E.coli was observed for the clear bottle not on a reflector (C-a). Significant kill was also observed for Total Coliforms in all clear bottle regimes. Additionally, some kill of Total Coliforms was observed in the half painted bottles (C-b, UVI-b and UV2-b). However, it appeared that there was growth of E.coli in these bottles, as indicated by negative percent kill, as well as all fully painted bottles (C-c, UV 1-c and UV2-c). 100 - ----.. ... 5-hour exposure, Barasa .... m TotalColiforms - E.coli 80 60 40 20 0 0 01C -20 -40 -60 -80 -100 C-a C-b C-c UV1-a UV1-b UV1-c UV2-a UV2-b UV2-c bottle regime Figure 5.4 Percent bacteria kill after 5-hours exposure in Barasa 48 For 1-day of exposure, approximately 100 percent kill for E. coli was observed in all clear and half-painted bottle regimes (Figure 5.5). For Total Coliforms, almost 100 percent (approximately 96 percent) kill was observed in the clear bottles, and significant kill was observed in the half painted bottles. No siginificant kill was observed in the fully painted bottles, in fact E.coli growth was again apparent. 1-day exposure, Barasa MTotal G~liforms 100 * E.coli 80 60 a, 40 (.) Cu .0 20 4 0 0 -20 -40 C) T_ I -C-a C-b C-c UV1-a UV1-b UV1-c UV2-a UV2-b UV2-c bottle regime Figure 5.5 Percent bacteria kill after 1-day exposure in Barasa 49 With 2-days of exposure, 100 percent kill for E.coli was observed in all clear and half-painted bottles (Figure 5.6). Over 80 percent kill for Total Coliforms was also observed in all these bottles. While significant kill for E.coli was apparent in the fully painted bottles as well, it was much less significant than for Total Coliforms. 2-day exposure, Barasa * Total O:,iforms n E.coli 90 70 0) C., 4.. n 50 - 30 - 10- 0 m-r -10 - C-a C-b C-c UV1-a UV1-b UV1-c UV2-a UV2-b UV2-c boltle regime Figure 5.6 Percent bacteria kill after 2-days exposure in Barasa 50 5.2.2 Dumay The amount of kill observed after 5-hours of exposure in Dumay was much higher than that observed in Barasa. Greater than 90 percent kill was observed for E.coli in all bottle regimes, reaching 100 percent in all bottles on the reflector and the half painted bottle not on the reflector (Figure 5.7). For Total Coliforms, kill greater than 80 percent was observed in the half painted and fully painted bottle not on the reflector and the half painted bottle on the reflector. Total Coliform kill was also observed in the clear and half painted bottles on the reflector. One and two day tests were not conducted in Dumay. 5-hour exposure, Dumay 100 m Total Coliforms n E.Coli. - 80600 U 0 4020 C, 0 -I C-a C-b C-c UV2-a UV2-b ---I UV/2-c boitle regime Figure 5.7 Percent bacteria kill after 5-hours exposure in Dumay 51 5.2.3 Boston In Boston, 100 percent kill of E.coli was observed in all clear and half-painted bottles after the 5-hour exposure (Figure 5.8). Over 80 percent kill for Total Coliforms was also observed in these bottles. Significant kill was also apparent for E.coli in the fully painted bottles, but there actually appeared to be growth of Total Coliforms, the opposite of what was observed in Barasa. I _ 5-hour exposure, Boston 90 - 70 - * Total Coliforms m E.coli 50- a) U (U .0 30- 0 10-10 -f-- -30 C-a C-b C-c UV2-a UV2-b UV2-c bottle regime Figure 5.8 Percent bacteria kill after 5-hours exposure in Boston 52 After 1-day exposure, 100 percent E.coli kill was observed in both clear bottles and over 90 percent kill was observed in the half-painted bottles (Figure 5.9). For Total Coliforms, the percent kill in the clear bottles was 80 percent, and around 75 percent in the half-painted bottles. Significant E.coli kill was also observed in the fully painted bottles. 1-day exposure, Boston 95- m E.ooli 7555 4) 3515- C-a C-b C-c UV2-a UV2-b UV2-c bottle regime Figure 5.9 Percent bacteria kill after 1-day exposure in Boston 53 For 2-days of exposure, 100 percent kill was observed for E.coli in both the clear and half-painted bottles (Figure 5.10). Additionally, kill greater than 95 percent for Total Coliforms was also observed in these bottles. Significant kill was observed for E.coli in the fully painted bottle without a reflector, but growth of both E.coli and Total Coliforms was actually apparent in the fully painted bottle on the reflector. 2-day exposure, Boston 100 - . . Total Colforms Ecoli 806040200 -20 C-a C-b C-c UV2-a UV2-b UV2-c botle regime Figure 5.10 Percent bacteria kill after 2-day exposure in Boston 5.2.4 Summary Overall, the effectiveness of each exposure regime was related to the length of the exposure time and location. The clear bottle regimes, both with and without a reflector, were most effective. Approximately 100 percent E.coli inactivation in all locations regardless of the duration of the exposure was seen in this regime. Additionally, the half painted bottle regimes consistently showed significant E.coli inactivation as well, though the percent inactivation increased with exposure time. The fully painted bottle regimes were generally not effective, except in Dumay. 54 5.3 Evaluation of Results 5.3.1 Barasa The conditions observed in Barasa were sub-optimal for SODIS application because of cool climate conditions, but abundant solar radiation was available. None of the bottle water temperatures reached 50C necessary for thermal disinfection (Figure 5.11). However, as shown in Figure 5.11, solar radiation was abundant in Barasa, and exceeded the necessary 500 W/m2 for effective UV-related microbial inactivation. This would therefore account for the differences in kill observed in the clear and half-painted bottles, which were exposed to UV radiation, versus the fully painted bottles, which were not exposed to UV radiation. I Bottle Water Temperature and Climate Condlions for Barasa - -- 40 temp Ckear bottle +4-Air He if Painted 35 *R~ diatimn 30 25 600 X60 9- a, FuIly painted A + 20 - --- 0 500 400 15 300 10 200 5 100 0 0 0 10 11 12 13 14 15 16 17 18 time of day (hou) Figure 5.11 Bottle water temperature and climate conditions in Barasa 5.3.2 Dumay The conditions in Dumay were ideal for the application of SODIS because not only was there abundant solar radiation, but the climate was warm as well. Both the half- 55 painted and fully painted bottles exceeded the threshold temperature of 50'C for the onehour required. It is therefore not surprising that significant kill was observed in both of these bottles. Additionally, it can be assumed that the amount of available solar radiation was high, therefore also effecting significant kill in the clear bottle as well. 5.3.3 Boston The conditions in both Boston were again sub-optimal for SODIS application because of limited solar radiation and extremely cold temperatures. However, the trend in microbial inactivation was similar to that observed in Barasa. Significant kill was observed in the clear and half painted bottles, regardless of exposure time, implying that solar radiation was sufficient for bacterial deactivation, whereas there was no significant kill in the fully painted bottles. 5.4 Statistical analysis In order to properly analyze the effectiveness of the different exposure regimes, two different statistical tests were used to detect trends in the data. The two tests used were the Mann-Whitney test and the 2-sample t-test. Both of these tests compute and compare the means of two sample sets and use the sample variances to determine whether or not they are statistically different within a given confidence interval. If the means of the two samples are statistically different, then it is assumed the two sample sets are statistically different within the same confidence interval. Ideally these tests are applied to large sample sets, which are more representative of actual conditions. Unfortunately, the amount of data collected in this study was limited (only 2 data points for each exposure regime per run, therefore 6 total data points per location for each exposure regime). Because the conditions in Boston and Barasa were similar in that they did not exceed the threshold temperature, the two data sets were analyzed individually and grouped. No statistical analysis was conducted on the data collected in Dumay. 56 Statistical analysis was used to evaluate a number of different parameters and determine which regimes were worthy of further investigation. Each test compares two sample sets. The first analysis compared the background microbial concentrations to the concentrations in the treated water of each regime. The purpose of this analysis was to determine if the amount of bacterial kill in each regime was in fact significant, and thus the regime could be considered effective for water treatment. The second analysis compared the clear and half-painted bottle regimes on the two reflectors to their counterparts without a reflector. This analysis was used to determine whether or not the reflector was effective in enhancing microbial deactivation. Finally, the clear and half painted bottle regimes on the two different reflectors were compared in order to determine if there was a significant difference in their effectiveness. 5.4.1 Evaluating the Effectiveness of Each Regime With 5-hours of exposure, only the microbial concentrations in the clear bottle regimes (both with and without the reflector) and the half-painted bottle regime on the aluminum foil reflector were statistically different from the background microbial concentration within a 95 percent confidence interval. Therefore, it can be assumed that these regimes were effective for microbial deactivation with only 5-hours of exposure. However, all of the other half-painted bottle regimes were statistically different from the background microbial concentrations within an 80 percent confidence interval, and thus could also be considered effective exposure regimes, though less so than the others mentioned. None of the fully painted bottle regimes in Boston or Barasa had statistically significant microbial deactivation. 57 Table 5.1 Statistically significant microbial kill after 5-hour exposure Statistically significant microbial kill? Yes No 95% confidence 80 % confidence interval interval No reflector Clear bottle Half-painted bottle V/ Painted bottle Al mylar reflector Clear bottle / Half-painted bottle / Painted bottle Al foil reflector Clear bottle Half-paintedbottle / / Paintedbottle With 1-day of exposure, both the clear bottle regimes (with and without the reflector) and the half-painted bottle regimes on either reflector were statistically different from the background microbial concentration within a 95 percent confidence interval. Thus, with 1-day of exposure these bottle regimes were effective for microbial deactivation. The half-painted bottle regime not on a reflector was also statistically different from the background microbial concentrations, but only within a 90 percent confidence interval, meaning it is also effective for microbial deactivation. Again, the fully painted bottles did not have statistically significant microbial deactivation. 58 Table 5.2 Statistically significant microbial kill after 1-day exposure Statistically significant microbial kill? Yes No (95% confidence interval) No reflector Clear bottle Half-painted bottle Painted bottle Al mylar reflector Clear bottle Half-painted bottle Painted bottle Al foil reflector Clearbottle / Half-paintedbottle Paintedbottle V/ For 2-days of exposure, all clear and half-painted bottle regimes had statistically different microbial concentrations from the background samples, within a 95 percent confidence. Therefore, all these regimes were equally effective for microbial inactivation. The analysis determined that the microbial concentrations in the fully painted bottles were not statistically different form the background concentrations, and thus they were not effective for microbial inactivation. 59 Table 5.3 Statistically significant microbial kill after 2-day exposure Statistically significant microbial kill? Yes No (95% confidence interval) No reflector Clear bottle Half-painted bottle Painted bottle Al mylar reflector Clear bottle V Half-painted bottle / V Painted bottle Al foil reflector Clearbottle V Half-paintedbottle V Paintedbottle Overall, only the clear bottle regimes were consistently effective for microbial inactivation, regardless of exposure time (within those investigated). However, the effectiveness of the half painted bottle regimes seems to increase with exposure time, and it also seems to be enhanced by use of the solar reflectors. Additionally, because the bottle water temperatures in Boston and Barasa did not reach those necessary to either induce synergistic effects or thermal inactivation, it is possible that the half painted bottle regimes would be more effective in only slightly warmer climates. The fully painted bottles were not effective in either Boston or Barasa because threshold temperature for thermal inactivation was not reached and no UV effects could penetrate the system. 5.4.2 Evaluating the Use of Solar Reflectors Data was collected daily in Barasa to compare the amount of radiation incident on a bottle on and off a reflector. Calculations made from these measurements show that the aluminum mylar reflector increased the apparent sunlight intensity an average of 20 percent. According to the above evaluation, it appears that the reflectors do in fact enhance the effectiveness of microbial inactivation in the half painted bottles. However, statistical analysis shows that the microbial concentrations in the clear and half painted bottle regimes are not statistically different between the bottles on the reflector and not, 60 within a 95 percent confidence interval. This analysis was conducted for each of the 5hour, 1-day, and 2-day exposure data sets within the grouped Boston and Barasa data, as well as the two individual location data. Additionally, no statistical difference was detected between the microbial concentrations in the bottles on the two different reflectors. 5.4.3 Summary The validity of this statistical analysis is questionable because the sample set is small and may not be truly representative of the effectiveness of the bottle regimes. Additionally, the data that was collected contained many samples that had 100 percent kill. The presence of these zeros and the lack of a normal distribution of the data greatly skew the mean of the data set. Additional research is necessary to supplement this data for proper statistical analysis. While few conclusions can be drawn from the data available about the effectiveness of the different exposure regimes, it is fairly clear which ones are worthy of further research. Because the bottle water temperatures of the fully painted bottles was not significantly different from that of the half painted bottles, and because there was no significant microbial inactivation in the fully painted bottles, they are not worth further research. The same temperature gains can be achieved in the half painted bottles, while still allowing for UV effects. The clear and half-painted bottle regimes are worthy of further investigation specifically on their effectiveness in non-tropical climates. In particular, because the clear bottle regimes were consistently effective with only 5-hours of exposure, their effectiveness with shorter exposure times and/or less intense radiation should be investigated. Additionally, the same variable seemed to affect the effectiveness of the half-painted bottle regimes. However, because there is an abundance of data on the effectiveness of these two regimes in other locations already, more worthy of further study is the use of solar reflectors to enhance their effectiveness. In investigating the use 61 of these reflectors, not only should the conditions of this study be repeated, but also additional exposure times and sunlight intensities. 5.5 Bottle Water Temperature Model The bottle water temperature model developed as a part of this study was created using a Microsoft Excel spreadsheet (presented in Appendix III). The average air temperature and radiation data collected in Barasa were used as the climatic inputs to the model, and so the outputs were compared to the actual bottle water temperature monitored in Barasa. However, the one-hour time step at which measurements were taken was found to be too large to achieve accurate calculations with the model, and so the data was interpolated at 10 minute time steps. Because the wind speed and direction was not monitored in Barasa, the speed was estimated to be approximately 3.8m/s from observations using the Beaufort scale (Table 5.1). It was assumed that the wind direction was perpendicular to the bottles, which would thus overestimate the amount of convection occurring. 62 Table 5.4 Beaufort Scale (Petterssen, 1969) Beaufort # 0 1 2 General description Calm Light air 8 Slight breeze Gentle Breeze Moderate Breeze Fresh breeze Strong breeze Moderate gale Fresh gale 9 Strong gale 10 Whole gale 11 12 Storm Hurricane 3 4 5 6 7 Specifications Wind speed (m/s) Smoke rises vertically Wind direction shown by smoke drift but not by vanes Wind felt on face; leaves rustle; ordinary vane moved by wind Leaves and twigs in constant motion; wind extends light flag Dust, loose paper, and small branches are moved Small trees in leaf begin to sway Under 0.6 0.6-1.7 Large branches in motion; whistling in telephone wires Whole trees in motion 9.9-12.4 Twigs broken off trees; progress generally impeded Slight structural damage occurs; chimney pots removed Trees uprooted; considerable structural damage Widespread damage 15.3-18.2 1.8-3.3 3.4-5.2 5.3-7.4 7.5-9.8 12.5-15.2 18.3-21.5 21.6-25.4 25.5-29.0 Above 29.0 The short-wave transmissivity of the plastic was calculated from measurements taken in Barasa by placing the end of a plastic bottle around the pyranometer. The meter therefore gave a measure of the percent of radiation that was not reflected or absorbed by the bottle. The painted plastic was completely opaque, but the clear plastic transmitted approximately 90 percent of the radiation. Additionally, measurements were taken to calculate the percent attenuation of radiation through the bottle, which was found to be 80 percent of the total radiation (i.e. only 20 percent of the radiation was transmitted through the full bottle of water). The plastic s transmissivity/emissivity of long-wave radiation could not be calculated because there was no way to measure this radiation. The thermal conductivity of the plastic was found to be 0.2 W/mK (Matweb, 2002). In general, convection was the limiting term to heat transfer in this model. Because convection is small, the surface temperature built up so that it was very close to the bottle water temperature, therefore limiting the rate of conduction, and creating an insulating effect. Additionally, because the long-wave properties of the plastic are 63 unknown, the model was run both with and without these components (Figures 5.12-14). Neglecting long-wave radiation creates a better fit for the clear bottle model, but has little effect on the fit of the half-painted and fully-painted bottle models. a. Clir Battle Water Temperature (K) 330 - Actual 320- Model 310 300 E 290 280 2700 2 4 6 8 Time (hours) b. CIr Bottle Water Temperature (K) 330 - Actual 320 - 310 Model - T 300 E 290 4) 280 2700 2 4 6 8 Time (hours) Figure 5. 12 Clear bottle water temperature model, a) with long-wave radiation, b) without radiation 64 a. Half Painted Bottle Water Temperature (K) 330 - Actual e 320 Model 310 300 290280 270 0 2 4 6 8 Time (hours) b. Half Painted Bottle Water Temperature (K) e 330- Actual 320- Model 2310S300 290 1 280 2700 2 4 6 8 Time (hours) Figure 5.13 Half-painted bottle water temperature model, a) with long-wave radiation, b) without long-wave radiation 65 a. Painted Bdttle Water Temperature (K) 330 33-+- Actual 320 -- _ e C 310IE300- E 290 2802700 2 4 Time (hour) 6 8 b. Painted Bdttle Water Temperature (K) 330 320 C + Actual --- Model 310 300 E 290 280 270 0 2 4 Time (hour) 6 8 Figure 5.14 Painted bottle water temperature model, a) with long-wave radiation, b) without long-wave radiation As illustrated in Figures 5.12, the model consistently overestimates the temperature. However, an underestimate of the bottle water temperature would be more acceptable for SODIS application. Modifying the transmissivity factors for the clear bottle can greatly improve the fit, but it is consistently too high, even when all short-wave radiation is ignored. Additionally, there is no logical basis for this change. It is believed that theses discrepancies are more likely caused by inaccuracies of the material properties than by oversight of additional heat components. Therefore, more research is needed to assess the actual reflective, transmissive, and emissive properties of the plastic in order to make the model more accurate. 66 6 Conclusions 6.1 Thermal Enhancement In order for thermal inactivation alone to be effective for microbial deactivation in the SODIS system, a bottle water temperature of 50 0C must be exceeded for at least one hour. Additionally, reaching this temperature also causes synergistic effects between UV and temperature to be enabled. It has been shown that painting the bottom half of the bottles black can raise the water temperature 5C, depending on the amount of radiation available. In order to test this technique under sub-optimal SODIS conditions, bottles in this study were painted half black so that UV inactivation of bacteria could also take place within the bottle. Additional bottles were fully painted in hopes of absorbing more radiation than the half painted bottles and thus raising the temperature more. Under sub-optimal conditions, there was no significant difference in the amount the bottle water temperature was raised in the half-painted or fully painted bottles. The bottle water temperature of the clear bottles was the same as that of the ambient air temperature. In Barasa, the peak temperature difference between the clear and painted bottles was 80 C - greater than that expected from the literature. However, this only achieved a peak bottle water temperature of 38C, well below the thresholds mentioned above. In Dumay however, which has similar amounts of available solar radiation, a temperature difference of almost 1 00 C was achieved, and the threshold temperature of 50 0C was exceeded in both painted bottles. The difference in the peak temperature achieved can be mainly attributed to the difference in weather conditions, which were cooler and breezier in Barasa, which would cause cooler bottle water temperatures. In order to assess whether or not a thermal enhancement technique would be effective in a specific region, the local weather conditions (air temperature, wind, available solar radiation) must be known. In general, if the ambient air temperature does not reach 45 0C, it can be assumed that the painted bottle water temperature will not reach 50 0C. Additionally, because there was little difference in temperature between the half- 67 painted and fully painted bottle, bottles should only be half painted in order to also allow for synergistic effects with UV. 6.2 UV enhancement The second active disinfection mechanism of SODIS is UV induced DNA alterations, which inhibits proper cellular replication. According to SANDEC News, No. 3, a total sunlight intensity of 555 W/m 2 is necessary to induce these lethal UV effects. In order to increase the sunlight intensity in the system, a reflector was built to gather sunlight from a wider area and focused it on the SODIS bottles. This would not only enhance the UV intensity in the system, but also had the potential to additionally increase the bottle water temperature through increased radiation absorption. Two different reflective materials were used: aluminum mylar and aluminum foil. Aluminum mylar is sturdy and highly reflective, but aluminum foil has similar properties, and is also more commonly available in the developing world. The aluminum mylar reflector increased the apparent sunlight intensity an average of 20 percent. However, the amount of microbial kill observed in bottles on either reflector was not statistically different from that of their counterparts not on a reflector, nor was there a significant difference in bottle water temperature. There are many reasons why the reflector may not have had a significant impact on microbial kill. First of all, the dimensions of the reflector were not optimized to the bottle size because the bottle size to be used in different locations was not known. Additionally, because of material lightness, it was easily misshapen by the wind, often causing partial shading of the bottles. Finally, the amount of ambient solar radiation may have been abundant enough that a 20 percent increase (i.e. 1100 W/m 2 versus 900 W/m 2) did not have significant effect. These results are not consistent with the findings of Kehoe, et al (2001), who observed a significant increase in solar intensities and water temperature, resulting in an increased inactivation rate. However, the efficiency of reflective backing may be higher than that of the reflectors used in this study, thus accounting for the difference in results. Additionally, the Kehoe, et al study was 68 conducted using laboratory simulated solar radiation, which would thus be more evenly distributed than natural sunlight. Further studies are needed in order to properly evaluate the effective use of solar reflectors/reflective bottle backing. Possibly such enhancement techniques would be more obviously effective with shorter exposure times or lesser amounts of ambient solar radiation. In any case, the reflectors did not seem to inhibit microbial deactivation and when used properly can be used without concern of negative impacts on the system. 6.3 Summary Proper assessment of the possible application of SODIS to a region is dependent on a number of factors. Therefore, it is strongly recommended that proper field studies be completed before SODIS is introduced as the primary point-of-use water treatment system in that area. However, in order to make most efficient use of field study time, the following should be noted about thermal enhancement using black paint: 1) There was no significant difference in the bottle water temperatures on the fully painted bottles versus the half painted bottles. Therefore, bottles should only be half painted (if at all) so as to allow for synergistic effects with UV as well. 2) In order for bottle water temperatures in a half painted bottles to reach temperatures of 50 0C necessary to activate synergistic effects, ambient air temperatures need to reach at least 45 0C. If condition (2) is met, than only one hour of exposure is necessary. However, if (2) cannot be achieved, then the bottles should not be painted. In this case, a reflective surface (such as a reflector or reflective bottle backing) may be more effective in achieving increased deactivation by increasing sunlight intensity focused on the bottles. 69 This study evaluated a number of different exposure regimes in non-tropical climates in order to determine which were most effective and worthy of further research. In general, the fully painted bottle regimes were not significantly more effective for reaching the required temperatures than the half painted bottles. Additionally, there have been numerous studies already conducted on the use of the clear and half painted bottle regimes without a reflector. Therefore, it is recommended that the primary focus of future studies focus on the use of such reflectors with the clear and half painted bottle regimes in non-tropical climates. 70 REFERENCES Anarchy, Inc. 2001. Water Projects in Haiti. Massachusetts Institute of Technology M.Eng. Project Report Cadgil, A.J. and L.J. Shown. 1995. To Drink Without Risk: The Use of Ultraviolet Light to Disinfect Drinking Water in Developing Countries. The Solar Cooking Archive. http://solarcooking.org/ultravioletl.htm. Accessed October 31, 2001. CIA. 2002. The World Factbook - Haiti. http://www.odci.gov/cia/publications/factbook/geos/ha.html. Accessed April 14, 2002. Koller, Lewis R. 1952. UltravioletRadiation. John Wiley & Sons, Inc. New York, NY. Kowalski, W.J. and W.P. Bahnfleth. 2000. UVGI Design Basics for Air and Surface Disinfection. Department of Architectural Engineering, Pennsylvania State University. University Park, PA. Lantagne, Daniele. 2001. Personal Communication. September-December 2001. Lehr, J.H., T.E. Gass, W.A. Pettyjohn, and J.DeMarre. 1980. Domestic Water Treatment. McGraw-Hill Book Company. New York. Lonely Planet. 2001. Worldguide, Destination: Haiti. http://www.lonelyplanet.com/destinations/caribbean/haiti/ Accessed November 11, 2001. Madigan, M.T, J.M Martinko, J. Parker. 2000. Brock Biology ofMicroorganisms,9th Edition. Prentice Hall. Upper Saddle River, NJ. Maier, R.M., I.L. Pepper, and C.P. Gerba. 2000. EnvironmentalMicrobiology.Academic Press. San Diego, California. Matweb. 2001. Overview: PET, Unreinforced. http://www.matweb.com/SpecificMaterial.asp?bassum=03300. Accessed April 14, 2002. McKee, T and J.R McKee. 1999. Biochemistry: An Introduction.McGraw-Hill.Boston. Pan American Health Organization. 2002. Regional Core Health Data System - Country Health Profile 2001:Haiti. http://www.paho.org/English/SHA/prflhai.htm. Accessed April 14, 2002. 71 Parrish, J.A., R.R. Anderson, F. Urbach, and D. Pitts. 1978. UV-A. Plenum Press. New York, NY. Petterssen, S. 1969. Introduction to Meteorology. McGraw-Hill Book Company, New York. pp. 305. PSU (Pennsylvania State University). 2001. AerobiologicalEngineering.Graduate School of Architectural Engineering and Department of Biology. http://www.engr.psu.edu/www/dept/arc/server/WJKAEROB.HTML Reed, R.H. 1996. Sol-Air Water Treatment. New Dehli, India. Pp 295-296. 2 2 "d WEDC Conference: Discussion Paper. Reed, R.H., S.K. Mani, and V. Meyer. 2000. Solar photo-oxidative disinfection of drinking water: preliminary field observations. Letters in Applied Microbiology 30(6), pp. 432-436. SANDEC. 2001. SODIS: Solar Water Disinfection. http://www.sodis.ch. Swiss Federal Institute for Environmental Science and Technology. Dtbendorf, Switzerland. Accessed November 11, 2001. Shultz, C.R., Okun, D.A., 1984, Surface Water Treatmentfor Communities in Developing Countries, John Wiley, N.Y. Smith, A. 2002. Personal communication in January 2002. USAID. 1985. Haiti: Country EnvironmentalProfile,A FieldStudy. U.S. Department of State, Bureau of Inter-American Affairs. 1998. Background Notes: Haiti,March 1998. Wegelin, M., S. Canonica, K. Mechsner, F. Persaro, and A. Metzler. 1994. Solar Water Disinfection: Scope of the process and analysis of radiation experiments. Journal of Water Science Research and Technology 43(3): pp. 154-169. Weil, T.E. et al. 1985. Haiti: a country study. US Government Printing Office, Washington, D.C. 72 APPENDIX I: Research plan SODIS Research Plan for Haiti, January 2002 Massachusetts Institute of Technology Researcher: Julia Parsons Advisor: Daniele Lantagne Overview One entire experiment should take 4 days, from initial sample collection to final microbial analysis. It will consist of 3 complete sample runs consisting of 17 bottles, 2 background samples and 2 blanks (21 samples total). The experiment will be run at least 3 times throughout our 15-day stay in Barasa. Bottle Regimes: Regime No reflector Al Mylar reflector: Al foil reflector Label clear (2) 1/2 black (2) all black (2) clear (2) black (2) all black (2) clear (1) black (1) all black (1) C-al and C-a2 C-b2 and C-b2 C-c l and C-c2 UVI-al and UVI-a2 UVi-bi and UVl-b2 UVI-ci and UVI-c2 UV2-a UV2-b UV2-c All supplies will be brought to Haiti from Boston, with the exception of bottles and paint. A detailed schedule, instructions for sample collection, exposure and membrane filtration follow. The same procedures will be used for sampling done in Dumay and Boston as well. 73 Schedule Day 1: Site selection, Bottle selection and preparation, Equipment preparation Run #1 Day 2: SCIa EXPla (5 hours) MF Ia*, begin Il a* Day 3: SClb&c EXPIb&c (1 day, 2 day - dayl) MF1b*, begin Ilb* continue Ila, CCla* Day 4: continue EXPIc (day 2) MFlc*, begin Ilc continue Ilb, CC1b* Day 5: continue 1Ic, CClc* Run #3 Day 8: SC3a, EXP3a (5 hours) MF3a*, begin 13a* Day9:SC3b&c EXP3b&c (1 day, 2 day - dayl) MF3b*, begin 13b* continue 13a, CC3a* Day 10: continue EXP3c (day 2), MF3c*, begin 13c continue 13b, CC3b* Day 11: continue 13c, CC3c* Run #2 Day 5: SC2a, EXP2a (5 hours) MF2a*, begin 12a* Day 6: SC2b&c EXP2b&c (1 day, 2 day - dayl) MF2b*, begin 12b* continue 12a, CC2a* Day 7: continue EXP2c (day 2) MF2c*, begin I2c continue J2b, CC2b* Day 8: continue 12c, CC2c* (SC = sample collection, EXP = exposure, MF = membrane filtration, I= incubation, CC = colony counting, a = 5 hr exposure, b = 1 day exposure, c = 2 day exposure) * in evening 74 Bottle Selection and Preparation Equipment: Towel Wash basin Black paint Labeling marker Drying rack Newspaper Soap Turpentine Paintbrush Aluminum foil and tape Bottle Condition data sheet Sponge and Bottlebrush Preparation: 1) Collect Bottles that meet the following specifications: - 1 liter w/ lid, minimal scratches, dents and deformations 2) Make note of original condition on data sheet (ie. clear, minimal scratches, excessive scratches, deformation, discoloration). Expand on condition in "Notes" section at bottom of page if necessary. 3) Wash bottles using boiled water and non-disinfectant soap. Clean inside by vigorous shaking (use bottlebrush only if necessary - it scratches) and outside using soft sponge. Be careful not to scratch bottle or remove paint. NOTE: if new, unopened bottles are bought from a store, there is no need to wash them because them have been sterilized by the packaging process. ** DO NOT use chemically treated (ie. chlorinated) water or other kind of disinfectant on the bottles at ANY TIME. Using alcohol will increase kill and cause lower apparent microbial concentrations** 4) Dry outside with towel/paper towels and place on end in drying rack 5) Prepare bottles as follows: - 6 fully painted black, 6 black, 6 clear 6) Paint:Line edges of surface to be painted with tape. Paint with paintbrush, being careful not to drip paint on surface that should not be painted. Allow paint to dry by placing on end in drying rack, over newspaper. Coat with additionally layers until opaque (test opaqueness by holding up to light). 7) Label lids as shown above. 75 SODIS Bottle Condition - Haiti, January 2002 Run#: Dates: original condition Bottle Day 5 hr 1 day 2_day_-1_2_day_-2 2 day -1 2 day -2 C-al C-a2 C-b1 C-b2 C-cl C-c2 C-dl C-d2 I I\/1 -91 4 1 I UV1-a2 UJV1-b1l UV1-b2 UV1-cl __________________________________ UV1-c2 UV2-al UV2-a2 UV2-bl UV2-b2 UV2-c1 UV2-c2 -I L _________________________________- Collecting Water samples Equipment: Whirlpack bags Labeling Marker Thermometer Turbidimeter Bottles Turbidity/Radiation data sheet Bottle Condition data sheet Bottle Temperature data sheet Procedure: 1) Note condition of each bottle for appropriate day on data sheet (ie. clear, minimal scratches, excessive scratches, deformation, discoloration). Expand on condition in "Notes" section at bottom of page if necessary. 2) Take all bottles (plus extra) and 4 whirlpack bags to source as early in the day as possible so as to maximize exposure time. 3) Take initial turbidity reading using turbidimeter. Record on Turbidity/Radiation data sheet. 4) Collect first background sample in a whirlpack bag: Label sample bag. Rip off top, open using tabs and be sure bottom is open. Fill to line and whirl closed. Wipe down outer surface and set aside. 5) Rinse inside of bottle with sample water by partially filling & shaking vigorously. 6) Fill first bottle 2/3 full, cap and shake vigorously to aerate. Fill completely (minimizing air space) and record temperature. Cap tightly and set aside. 7) Repeat (6) for rest of bottles. Be careful not to mix up lids. 8) Repeat (4) through (6) for second turbidity reading, background sample, and remaining bottles. NOTE: There is no need to be "sterile" during this procedure because all samples are coming from the same source and will therefore have the same initial microbial concentrations. However, it is necessary to take precautions not to contaminate samples with outside sources. ** ** 77 Reflector Assembly The reflector consists of two parallel "slings" of material (Aluminum coated Mylar or brown paper with Aluminum Foil) hung on rope. Both reflectors are constructed exactly the same way, but using different materials. Each "sling" holds three bottles end-to-end (total = 6 bottles). The reflector should be oriented parallel to the path of the sun (approx East - West) so as to minimize shadows. Samples not utilizing the reflector should be placed at a sufficient distance and orientation away from the reflector so as not to be affected by potential reflection. Materials: Al Mylar: 2' x 3' Wooden bases (2) Wooden "Arms" (6) Duct Tape Brown paper (same as Mylar) Nuts, Bolts, Washers 7' Rope (3) Sand paper (to smooth rough edges) Supporting Ropes Bottles Figure 1. Top view Mylar Bolts Arms Bottles Supporting Ropes Figure 2. End view Arms Supporting Rois -----------------------------------------------------------------------------... ..... ... ... Figure 3. Side View Base 78 Assembly Instructions: 1) Choose a location free of shade (that will remain free of shade) and shielded from wind. If a wind shielded location is not available, you may have to rig up a wind block, as the wind affects bottle temperature and may also adversely affect the reflector. 2) Bolt arms to the inner side of the longer base piece with bolt heads facing outwards. This will allow the Mylar to rest on the ground without interference from the base or bolts. Three arms attach to each base. 3) Tape (using duct tape) one piece of rope to underside of Mylar down middle seam 4) Place the two bases approximately 3 feet apart. Flip over Mylar and position between the two bases. 5) Thread rope through middle arm on each side and through the back rope holes of the base and tie off. Be sure to pull the rope tight, but do not wrinkle Mylar. 6) Thread remaining two rope pieces through the side arms and attach to tie off on both sides as done above. 7) Tape outsides of Mylar to side ropes using duct tape. 8) Readjust ropes and Mylar to get rid of any slack or wrinkles. 9) If necessary, weight down the base with rocks to keep from flipping over. 79 Temperature Monitoring Equipment: Checktemp electronic thermometer Sterile or boiled water (for rinsing thermometers) Squirt bottle Bottle Temperature data sheet ** In order to keep thermometers sterile and avoid contaminating samples, they should be left in the sun during the day and rinsed well with boiled water between samples** Procedure: 1) Take temperature in every bottle every hour (or as often as possible) as long as you are awake, starting at t=0 being when the bottles are first set in the sun. 2) Take ambient air temperature and note weather condition (ie. approximate wind speed) on temperature data sheet. 3) Take reading in first bottle and record on data sheet. ** Only open bottle when ready to take measurement and close immediately after. BE CAREFUL not to shade other bottles while taking temperature readings ** 4) Rinse thermometer with sterile or boiled water. DO NOT wipe dry. 5) Repeat (2) and (3) for remaining bottles. 6) Make any necessary notes on data sheet. 80 SODIS Bottle Temperature - Haiti, January 2002 Date: Exposure Regime: Temperature (oC) Bottle Time sourcef 0 1 2 3 4 5 6 7 8 9 10 12 11 Time Radiation data C-al C-a2 C-b1 C-b2 C-c 1 C-c2 UV1-al UV1 -a2 UV1-b1 UV1-b2 UV1 -cl UV1 -c2 UV2-al UV2-b1 UV2-cl Ambient Notes: 81 Microbial Analysis ** Remember to complete a blank with sterile water at the beginning and end of each sampling round. ** Equipment: Filtration apparatus Petri dishes Filters Sterile Water Candle and matches Paper towels Labeling marker Funnels Media packets Tweezers Alcohol Incubator Plastic trash bag Microbial Analysis data sheet Procedure: 1) Pull back hair, don glasses, use gloves or wipe hands with alcohol 2) Prepare work surface: open plastic bag and wipe down with an alcohol soaked paper towel 3) Wash hands with alcohol 4) Set up filtration apparatus, set out equipment, wipe down outside of samples with alcohol, set out and light candle 5) ** BE CAREFUL not to get alcohol on the LIDS of the bottles but only wipe down the sides to avoid cross contamination ** 6) Prepare media: snap open packet, pour entire packet into petri dish and cover immediately 7) ** PREPARE ALL petri dishes at once in order to minimize time filter is exposed to open air later. ** 8) Sterilize tweezers in candle, pick up and sterilize carbon filter in candle using tweezers, replace in filtration apparatus and wet with sterile water 9) Wash hands with alcohol, sterilize tweezers. 10) Carefully open new filter package, pulling away package and paper, DO NOT touch filter with hands (if so, discard filter) 11) Pick up filter with tweezers and carefully center on filtration apparatus, place new funnel on top of filter. If filter rips - discard filter. 82 12) Carefully pour sample directly from bottle or whirl pack into the funnel, filling to the 100ml (or other appropriate) mark. DO NOT touch container to filter funnel. Close and set rest of sample aside in case it is needed later 13) Pull sample through filter, expelling wastewater into waste bucket or onto ground. 14) Sterilize tweezers 15) Remove filter funnel and pick up filter by edge with tweezers and place in petri dish (held in hand). Avoid air bubbles. Close petri dish immediately and label with sample, exposure and date. 16) Repeat from step 6 until all samples are completed. 17) Incubate samples for 24 hours, along with background and blanks. 18) When done, discard all used funnels, the garbage bag, paper towels and other trash. Empty bottles, wash with soap and boiled water and store under plastic sheet overnight (can also wash the next morning). After 24 hours: Count colonies formed (red = Total and blue = E.Coli) and record on data sheet. Make note of any necessary details (from filtration or counting - e.g. spilled sample?) on data sheet. 83 SODIS Microbial Analysis - Haiti, January 2002 Run #: Dates: 5 hr exposure Sample Total E.Cob. 1-day exposure Sample Total E.Coli. 2-day exposure Sample Total BL1 BL BL1 BG1 BG1 BG1 BG2 BG2 BG2 BG3 BG3 BG3 BL2 BL2 BL2 BL3 BL3 BL3 C-al C-al C-al C-a2 C-a2 C-a2 C-bl C-bl C-bl C-b2 C-b2 C-b2 C-cl C-cl C-cl C-c2 C-c2 C-c2 C-d1 C-dl C-d1 C-d2 C-d2 UV1-al UV-al UV-al UV1-a2 UV-a2 UV-a2 BL4 BL4 BL4 UV1-b1 UV-bl UV-bl UV1-b2 UV-b2 UV-b2 UV1 -c1 UV-cl UV-c1 UV1-c2 UV-c2 UV-c2 UV2-al UV2-a1 UV2-al UV2-a2 UV2-a2 UV2-a2 UV2-bl UV2-bl UV2-bl UV2-b2 UV2-b2 UV2-b2 UV2-c1 UV2-cl UV2-c1 UV2-c2 UV2-c2 UV2-c2 BL5 BL5 BL5 C-d2 __ E.Coli. Notes: 84 Incubator Directions Insulation Petri Dish Wells Thermomete Well Oe Hole for thermometer Lid Pressure release Petri dish brace Handle Figure 1. Top view of phase-change incubator To heat: 1) Place incubator in pot, ensuring space between the incubator and the pot with rocks or other objects so that plastic does not melt. 2) Fill with water up to brim of incubator 3) Boil 15 - 20 minutes, or until contents of incubator has liquefied * NOTE: occasionally lift and "swish" incubator to ensure even distribution of heat * 4) When ready, allow incubator to super cool and start crystallization before filling. * Note: you can "jump start crystallization by touching the side of the incubator * 5) To release pressure from heating open valve and close again. Alternative: Place incubator in direct sun to heat. To use: 1) Place petri dishes inside brace and lower into wells (5 or 6 into each well). If not brace is available use string. 2) Place lid on top. If lid does not sit tightly, cover with a piece of cloth or stuff with extra insulation 3) Insert thermometer through lid and into the thermometer well. 4) Allow samples to incubate for 24 hours. Check temperature occasionally, when it drops below 35 degrees C, reheat. 85 Solar Energy Readings Equipment: Pyranometer Radiation data sheet Bottle Temperature data sheet Pencil Black cloth cloak Procedure: 1) Take normal radiation reading every hour and record on Bottle Temperature data sheet. 2) At peak time (approx. noon) each day take the following measurements: - on reflector - through plastic piece - through full bottle (cloaked in black cloth) - through full painted black bottle (cloaked in black cloth - should be 0) - through full foil wrapped bottle (cloaked in black cloth - should be 0) 3) Cover sides of bottle with black cloth. 4) Place full bottle covered in cloth over pyranometer, record reading on Radiation data sheet. 86 Turbidity & Radiation - Haiti, January 2002 Dates: Day Date Turbidity (NTU) 2 1 3 plain Radiaticn Transmissivity bottle reflector plastic palnted foil 1-1 1-2 1-3 1-4 2-1 2-2 2-3 2-4 3-1 3-2 3-3 3-4 4-1 4-2 4-3 4-4 5-1 5-2 5-3 5-4 6-1 6-2 6-3 6-4 Notes: 87 APPENDIX II: Data Summary and Analysis Barasa.RunI 5-hour: 1117,02 Weather: breezy and sunny in 1 i . Ad Tme 111 35351 5 1n 210 242 237 257 262 250 25.0 MO 230 186 220 245 236 . 995 _ 247 1117102 --- t0 ---- - 2 ?5 - 0i5 a -- CiAab -- 2 5 31.7 29.4 226 293 292 31.0 315 290 258 297 278 314 30.2 295 226 299 290 321 72.2 24 1 21 29 .9 314 295 27.7 292 ------ --- -- 2000 -- 5 -- attle -+- - -- -t-iPe 2 (dtoin c 1000 E ______a____or__ --- -- 0 263 305 265 324 30.7 303 24.3 30.3 29-2 31.0 eA0llel 12 - - -- - -- ---------- -a, - - -- E0 __----_--- -- -- ---- 23 5 32.0 308 343 345 31.1 22.1 30.4 29.6 322 32.1 294 23 5 27.7 28 1 290 28 5 273 25.6 30.0 309 327 31.5 29.7 5-r. Radiation and Temperature data -- -- 253 299 280 309 31 8 29.3 249 29.6 26 0 31 0 320 29.7 21.0 24.6 24-0 26.0 25.8 24.0 21 2 25.2 252 269 266 24.0 205 24 3 246 25.9 25 5 242 212 24.3 245 256 249 240 207 253 252 26 4 26.0 25.0 21 3 244 237 256 258 --- 300 Cb V-lIV-i U--lU2a a w Ambin 231 0 970 7350 33.0 1335 14 35 135 16 35 2 3 A sunny and calm ahemoon mming, h 4 4 time (ho-ur? Evaluao on reacred lbeslold radiation Acer I il Run 1-1 Runl-2 Total E.Col Total I BG 5 2500 109 2500 UV0-c 2505 2500 2500 2500 2500 256 2500 25 0 IUV2- 2500 250 2 42 2500 2500 2500 2500 2500 UVI-a UV1-b UV2-sJ Barasa, Run 2500 2 2500 did not 52 exceed '% kill rag Ave__ 250130 2500 292 2 2 C-a C-b Ic-c 1 1'2 hour. EColi Total 05 0 0 0 2500 1 L for approxmately 2500 2500 96 2500 2500 2 2500 2500 V1 2500 2505 2500 2500 2500 274 2500 25 1514 1025 2500 2500 2 2500 2500 21 2500 2500 1 20 0 5-hr. 1jr7002 0 25M 2500 250 temp E.Col Total E.Col threshold - - - - Bacterial Kilt - - - - - - -- - - - -- - 959 0 0 0 C 8904 9992 0 0 3944 0 0 0 9919 0 I -- 00 _ --- ------ -_ T. 9 7 ... 7 0 7 2 5-hour: 1/2003 Weather: Sunniy and calm Temperature data RadiatIon Time 9140 1200 0 8240 .00 n 7515 250 2 526. 300 3 294.0 4.00 4 125_0 5 5 UV1-1 1: 2 259 209 30.0 28 274 183 261 294 30.4 296 276 275 301 300 203 277 226 0 C-A2 C-al Ambient UV1-2 UV2-a 273 298 284 265 235 289 279 25.0 22.0 1/201/02 5-hr.Temperature C-bI 18.8 195 270 19 102 203 318 31.0 2 26.0 C-63 1-V2 UV- 216 364 410 400 36.1 30.3 199 312 360 37.6 353 32.7 188 308 363 393 37 3 34.1 2.9 29.7 29.5 27.9 25.5 5000 - 0 - 200 Bacterial till I Sample BL aG C-a C-b C-c UV1-A UV1-b UV1-c UV2-a U uV2c __ ~ Total temperature 200 20 Total 0 385 0 2500 2500 0 0 400 0 0 240 2 threshold radiatin was exceeded ~ 63 120 20.7 34.2 40.3 30.7 35.7 30.9 batte tedbottle o---Pa -a- adiaion 5 6 Kil1, 0 2500 2500 2500 2500 330 2500 2500 145 0 42.5 364 28.7 5 0 hours ela E Cob Total E Col E.Coll Total 0 0 0 391 2500 396 10,40 1002 0 2040 0 000 -5402 2500 2500 2500 0.00 -5402 2500 2500 2500 0 9700 100.0 325 0 5 000 987 2500 10 0.00 -281.5 1490 2500 2500 0 76.90 100.0 578 0 0 46,70 1000O 1333 0 165 2.80 24M0 13601 % 469 21.7 30.7 34.1 36.2 32 7 273 900 --- A 3 221 423 Half-painted 400 0 ---- -- - ----- 1 not met. but fang nSI E.Coll a 2500 1580 2500 2500 320 2500 2500 1010 - - 50 ---50 0 Evaluation Threshold _-- UV1-c2 UV-o -W-Ambient Clear BOttle - ------- --- E C-ct C-c2 091-01 092-b 0 215 20.1 008 196 21 4 274 335 32.2 33.3 34.5 416 374 37 7 373 36 9 39 1 41 0 394 37,3 353 330 396 370 34.0 31 4 27.8 36.2 34 29.9 269 and Radiation data 0 250 214 336 369 343 301 256 1/2&W0 12000 60 OD 000 21100 - - 60 0 - - - - - -- 2 5-hr. Bactoria! Kill -- - -- - -- - ---- =- WE Coll - 69_2 88 22 4 320 303 34 35 319 24.0 30.0 25.1 22.3 30.3 20.6 Barasa. Run 3 5-hour 1f23t2002 Weather: Mostly sunny.0rzy 0 1I 2~ [ in the altarnOO50 _m__Rad__t__ 5500 10001 112O 8370 5620 1200 100 6500 7400 200 300 2500 T 3 4 51 204 28.5 193 181 235 1d3 235 250 26 265 273 310 092 287 298 250 301 281 099 292 272 32 313 29.0 4 192 275 200 282 32.4 347 33.6 313 338 329 30.5 123502 5-hr 1 19.0 26.0 l'- 29.8 17 31.4 29.0 30L5 . .. - "Y'1- ' C 212 20.8 214 32.6 346 358 408 43.7 41.0 425 464 40.8 403 468 40.3 355 I IC"C2 I,--I-'* 20.0 1MM 19.0 322 293 295 35. 358 34.6 394 392 382 373 397 393 34' 357 33 w' 189 29.3 2)5 280 336 330 373 384 34 5 382 36.3 336 22.1 358 40.7 428 414 362 -V 3.4 3.0 - 202 32.4 407 453 442 3.1 210 326 41.2 455 443 381 189 29.91 39.2 38. 37.2 Temperature and Radiation data 000 0 -3102.- ~ O -- . __-__-_ _-- ---- -1 clear a. .I -- _ - Battles - Half-Painted 00 Bottles -PaintedBatles Radiation 10 -- +00 5 I 3 22 0 exceeded Ealua0on. Univ (bows) r Bacterial Kill Run3-2 Run3- jTotal Sample IL BG II 0 0 340 25W 0 0 60 400 270 2500 2500 3 2500 1u1- 30 2500 C-3 30 UV Saraoa. Run I-day: 1/1V2 0 240 0 110 2"0 2500 120 0 78 2500 135 135 1480 0 0 0 and oartly 2500 1360 10 946 100 926 100 0 O 0 ;-e 11i0IX1-[43u6nmo. 65.00 T 2 01 11"0 2 00 3 00 4 00 1 2 3 4 S 00! 6o ' 2 m C-al 23 2851 2938 900 00 92000 770,10 4537 W 28100 8400 C-a2 10 3 246 279 316 31 2 315 280 270 18s SQ Cl ieC ;4 -.-- --- -- .-----..-- 20 1 8 55 19.5 256 29 1 33 0 31 5 265 248 18.8 1. 1 19.1 298 34 7 398 396 390 339 25.1 21L0 31.3 30.5 29.2 26.0 52 19's 275 31 8 371 369 35 3 306 1 21 S 355 382 427 400 354 294 2 20 2 288 340 38.7 367 314 268 . . 1. 19.8 295 360 412 40.5 402 34 9 2 20.2 30.4 34.7 39.6 38.95 35.3 302 00 reached 0 _t_! 20 threshold radiation or 4 hours, did Bacter ial Kill rot 2 25 3 timfe (hour) Total Total E.Co Average Total E.Cod % E.Col 0 1 0 05 0 2500 C-d 2500 2500 0 20 2500 2525 0 1 2500 2500 C-C 2500 0 0 2500 2500 0 0 2500 2500 0 10 2500 2500 0 05 2500 UVI-b UVI-C 150 240 2500 47 2500 2500 2500 47 2500 61 2500 2500 2500 988 1370 2500 ki 38.2 40.5 38.9 35.7 30.8 . 17.9 220 251 278 28.1 2193 270 - 1 18'o 215 243 25.5 263 262 248 8. 19.0 d1 21.8 24.7 27.2 27.2 27.3 25.9 tattle 45 Half-pain a -a 0: -- +- Radiation battle ed I Ono0 5 ata 9-day Bacterial Kill dy ll Tlat 0 UV1- 4 1/2 RunI-2 20-5 32.8 exceed threshold tem__ 2500 75 2500 2500 C-b 35 olo~ot16111510 Ruin-1 0 22 35 0 3850 41 0 378 316 28.8 -0o0 -- _ - t5 1 21.7 380 384 41 9 406 355 295 C~l,11 -080~Ambient .- Te _--_-Painted .. as 1 1&.6 279 323 379 368 353 31 2 ~~100000 - ----- 0 C-a --- -- - 20 194 EClear SL BG ---- 4-------- 00 1-day Radiation and Temperature data ____ .... o 153 19 3 264 284 308 29.7 27.0 24.0 U 18 2 237 2617 298 297 296 272 1/18102 0 Sample --- ------- 19 -1387 cloudy Temperature data Evaluathon Kill - 100 0 866 335 - - - I 620 1 Oeezy Wealtr: 0 Bacte" 9/23002 54hr E.Coll 0 0 2500 550 460 0 0 2500 _- K_ Total ME.II Total 0 9M C-c 0Uv1-a Ca % Av80996 Total E.Coli 0 25 x 1040 E.CT I 1al ______ 9756 100 0 0 0 96.06 45 29 996 0 Eco T - 0 2a - 0 100 99 9a , _ 89 Barasa Run 2 1-day: 1121/02 Weather: &c"y.aftemoon momningovercast and sunny and :aim Temperaltro data Tim. Radiation AmbanI C-al C-a2 UV1-I 0 10 :G 5300 217 1 1486 194 1 01/ 0 2501 8 565 1a 117 196 2 1200 380.00 222 197 196 715 3 ' 00 850200 280 241 247 271 4 270 74100 237 278 272 285 O 300 55700 278 29 1 28.1 284 6 400 277 00 257 2881 27 4 286 15300 26.0 2741 254 24 3 UV1-2 UV2-& 195 21 1 268 287 283 258 23-5 I a C-b1 19 2 19 8 21 6 26 27 1 27 9 26 0 238 190 UV1-b2 C-b2 UVI-b 201 2/5 202 222 219 252 30.3 350 357 393 376 394 354 354 32.0 3.5 19 7 204 220 303 362 38 1 369 342 18. 193 20.7 25.8 27.9 2&4 26.9 24.9 21 4 222 249 338 365 352 301 26 5 UV2-b I 21 7 225 257 339 372 361 31 6 273 C-cl C-c2 UVI-cl UV1-c2 200 198 204 209 205 200 21.5 21 a 22.4 210 244 246 311 232 372 354 370 374 397 388 388 383 39.1 398 380 364 301 338 360 32.9 304 287 20.9 21.5 239 32.7 37.0 37.3 33.9 30-1 UV2-c 205 223 254 334 360 366 325 285 c 20-3 21.2 23.7 32-1 37-8 38.3 352 31.3, C-dl C-d2 179 180 182 184 191 192 22.5 224 252 251 267 266 270 267 272 263 C-d 17.9 18.3 19.2 22.5 252 26.7 272 26.8 1/21/02 1-day Temperature and Radiation date 3s0 -mo-- 2'0 ___ - . -- . o00 110 -- 1 Run2-1 Total BL 3 2 lRun2-2 0 tle Radiation E.Coll 0 Total 1680 2500 E-Cofi |Tota1l 1 0 0 0 E.C01 25,41 _G TO 2500 160 290 2070 1580 2500 430 2500 0 2500 155 0 710 a 1605 0 430 2500 60 0 0 2500 250 2500 1965 UV2-b 50 200 2570 UV2-c 2 07o 2500 290 1640 1400 UV7-b UV2-a Baraba, Run 1280 2500 0 UVI8 UV-c 1 %Kill EColl Total 1 113546, 0 88.40 1000(l 65 17.20 94 51 000 1340 0oc0 43GS 0 A~vrage 0 5I 2500 C-a C-b C c C-d 5 1 it- (htouris temperature not met. but hreshold radiation was exceeded for 3 hours Bacterlal kill Sample ClearBettie AE Halt-pamnted bottle -1-Patmed bot .. 1 0 Evalual-i Thfestiold --w- Amnbent --- - - 110 1505 Q 00 j500 som 1000016 000 90100 -W52 0 1070 --- 00 200 1 1 -5:T - -- -2700 9380 35. 112IM2 I-oay Bacterial KIM -- ~ -.-- -- - 10 I -- - 00 " 1 009380 100.00 970 000 000 3 1-day: 1/242002 Morning sunny and breezy. aftemocin overcast A r- R di weathw 2 1 2 3 4 5 6 7 i i a050.00 atn Tmre_ 1070 1100 120) n 95000 90100 05000 221.00 145 00 5000 / 00 100 2.00 3 0 470 500 30d bi 21 t C-4 221 254 174 222 258 28 1 287 274 257 230 276 204 228 17 240 33 5 322 2? 4 252 210 1. 4 281 windy 203 261 303 307 298 274 247 22 0 5206 270 306 318 309 28.5 257 22.8 208 204 26.6 330 32.1 32 0 292 2 3 23 3 183 262 313 354 362 336 298 257 196 255 31 35.6 385 33.9 320 259 19.3 24.8 28.4 30-2 30.0 28.0 25.6 2e 8 22.7 324 390 378 349 309 275 239 231 345 399 41 0 383 336 295 252 231 321 37,0 387 375 335 292 255 C-d1 UV2-c ic -,I 180 C-r218 !UV1-cilUV1-c2 7 22.4 20.4 215 216 214 30.3 3S.8 37.7 36.7 33.1 29-2 25-2 203 34,3 367 333 30,0 274 237 250250 327 32.5 365 365 37.4 365 34 7 336 308 29 7 261 25.9 310 37.2 330 350 303 268 233 322 292 380 37.0 37 38 1 319 283 248 34.9 35.7 32. 28. 24.9 C-d2 1- :10_ Z' 0 -- ---------- --- S0--- --- 283 277 26.7 27.5 272 25.9 24.1 280 270 259 24.4 27,8 27.0 25.9 24.3 14 time (hours) valuat/n exceeed diI,on iav0S t/reSnold /1 BL BG C-a C-b C-c C-d UV1-a UVI-b UV1-c UV2-a UV2-b UV2-c Total 3 Total ECoOI 1 2500 30 250 2500 2500 4C 7 25/3/ 5C 56C 250C 0 870 0 0 110 170 0 0 250 0 0 2500 E.Coll 0 2500 tO 160 2500 2500 0 20 2500 Tott % 05 0 25M0 500 0 0 205 20 0 l155 1305 2500 2500 _ 14C To__250C E.C] 20 0 16C 7 a % KIM Col Total 0 130 C 5 Pained 1/2 oursl,did 11ot xceed thre5hold texnperature eaow Rut3-2 iRu3-1 Samp t for Bottles Radiation --- .- ___ -_ 00 Bacterial Kill Bottles Cleat lelct - Half-Paited1Bodies -- - E 10 S2500 , 50 560 250C 0 0 1330 0 0 25DO 1123)02 5-hr Bacterial LCKII Kil 120 100% O918 to Sao 8 .161 ._C02 ______ 0 69 ITI 4 100 99 2 2W 996 100 0 -466 98 100 77 6 100 0 .4w 992 - --- in - . > 72 172 20.8 20.7 247 24.2 Ambient 00000 - C-d 171 205 23.7 1/24/02 1-day Tenperature and Radiation data 1150.. 7 172 Y 90 6-rsa. Run I 2-dy- 905s-0832 da.U T.r,p.rt Tim. AoIC-1oi Rd.I-3An3 i C-al C-bl 0UVI-52 1s 0005.1 0,-2 U0. iC-b2 C-ic 9 UV-03 220 205 |-41 UV9-4 uv1-t C-2 25 7 22 22. 2 9M67 2 30.5 4 3 37-2 |21 s2 5 d 232 238 UC-2 cC21 5 28 2131 21 9 29.5 304 31 5 29 ' 283 325 24.8 07 280 233 239 243 24 5 34.0 352 36S 3210 324 900 0 310 33290 9 361 S 220 239Q 230 008 220 2539' 2 25 7 230207' 26 3 25 1, 38 3 3.13 39 37 9 704 2716 29 23 31 2 20 2".40 28.3 9 33 35 36.) 365 256 35 329 303555 11 210 27 296 294 297 40 40 120 324 31 7 294 3 3|3 3 325 28 33 345 33 27.a 273 2107 2' 289 3 20080 0 299 21 r 246 21 29.0 16 2. A.. 2 247 26 3 25 7 19 200 24 2z0 240 243 239 247 253 293 7 235 96 0 204 20 7 20 6 2310 21 0 21.3 23 7 '00 094 19 2.0 238 233 225 2 2.5 242 250 22 5 225 215 a! 000 00 0 212 20 2 203 2 21 19 7 202 22.3 28.7 207 239 239 215 261 25 23 23 21.6 222 20 a 232 21 70 20 30. 0 91 1200 221 225 342 383 35.8 31 4 388 324 33 5 30 5 30 5 349 205 26 A 27 3 249 24 0 10 7500 231 399 L2 9 35 35 0 378 359 38 0 33 8 34 S 401 25. 30.2 255 014 275 345 2000 002 0 1 23' 28.4 351 33' 394 2 34 360 38.3 357 36 7 U2 3434 27 292 2723 2 3 10 00 170 22 3 279 334. 332 358 302 354 32.4 314 31 0 2 5 331 329 250 1 20 26 3 271 13 230 26 1 302 2.4 300 308 335 1.7 32 5 30 250 20 25.1 239 0 235 3 25 ____ c _ 2a 4 2, 215 521. 32Z7 313 34 2421 2.1 2 14 5 Temperature I 09-19102 2-day and 251, 25,0 27.3 252 19 I 20.2 22.5 2451 29.1 255 25.2 2 &.4 243 Radiation Data - -Hall PIr4 - __ 3 20 'I a 253 270 283 21 05 99 227 A- F $acteri% Kill C. C- rG.25.4 S 0 :B. 250o 2 255M C-d 5 "35 .L5 2500 U07- ____ 1.3 _ 2 25 2500 2 T _ _l 2 25W 23-- 25 95 AurM U.s Vaa.050.95,9 93 05 a 0 2975 2500 280 25030 - 4- 3 9935 0 0 8 255 25035 - c275 4 2500 .-- ..-5- ---- - 0 C 0470 30 0 5 2 20 -c T E.V 2500 ___ .. ___.- _ ._-_-__ 2 3 .A - 220 0 0 50 1000 M 00 120c0 4 000 200 3 5 7 S 1O R0d09 250,0 3f0 0 8500 741 0 557 0 C0 6'0127 53 0 500 & 0030 450 0 8503 11 00 0 070 97 l000 '52 0 0 0200 2300 083 0! 3 4 00 5 0 0 940 500 22 5 22 5 290 26 5 292 259 29 264 285 261 ----- 25200 C 00-4 UV- 1000.0 Iv:+ UV2.s 3D 355 530J and 31 310 39. 328 j a 35 28 3. 2500 30 3 890 0 3500 01205 3. 0 39940 06208 2500 2 030 2300 780 2200 370 2500 470 2900 325 00884.94 2500 530 2508 0 2500 0 50 5 700 2500 0 200 905 039 00 389 55 4000 0 00 0000 000 50 32.8 - - -- 10000 05.036ui 098.--0,i _ 0375207E0000 745 22.9 -2 ----- __ - 720 500 7 0 2500 0 32. 29.2 d -4 2500 090 22.8 0 0 70004 0 0 850 328 37 8 371 285 293 c-0 _______________Pa ... - 2500 0 900 35.0 33 2323 27 data Radiaion . 8-9_0 0540 0 'C 3.2 Temparature - sm52103-9 60. C 2 26.6 297 259 -s jso~~. -- 719 19.7' 1. 1/21-22/02 6G i jc C-02 Uv505 0v-2 UV2-- c b UV2-b C-2 0145UV1-bl UV-b2 C-b9 l C-2 [U91. 0111 2 02-. 25.2 29.5 209e 00 20.3 09 28.4 099 2094 95 05999188 193 89091 0 217 212 209 200 19 9 9.0 19 7 98 212 292 217 20.1 5 1931 083 084 0 185 12 5 233 23 25.5 21 6 20 230 21.0 236 234 04 21521 21 2082.86 200 19 4 1!, 2 22 35.2 307 3 2 356 399 5.9 32.0 354 38 32.5 276 25.7 298 298 238 235 Z5 7 27 9 280 49.3 34.7. 44 35 302300 49.7 275 420 330 25.634348 30.2 3268 26 7 259 269 23 7 3.8. 48.8 429 340 37 1 364 33 42.0 422 339 364 372 21.3 21.8 67 20 11 27 5 273 .34. 37.7 37 1 29 8 333 342 34. 37.5 365 298 343 34 27. 20'S 292 251 285 2' 218 2951 322 7 0 28 25 301 308 2P.2 322 29 258 292 242 305 242 225 250 24. 24 282 0 9 195 19.0 1 57 186 I.3 to. 1985 197 14 is .3 I .4 18A 183 7 9 7 9 24 39.1 327 330 253 309 30 327 33 312 350 293 298 270 21.0 2. 263 240 24 3 27 32 396 33 31 3 9 31 384 40.8 359 4079 34 8 349 2.7 30.4 305 302 274 278 31 0 402 40 40 9 300 Al 9 A, 0 40.8 44.7 391 4 2 3.f 39 7 3a 0 3.2 331 31 9 1 296 258 30 48.2 42.2 31 365 42 9 42 1 42.0 35. 7 39 43 8 5 3 3 390 337 3.4 3122 30. 309 267 AmbAN- C-SO 20 71 000 9508 I _0 --- ------ - 00 _ _ _ _ - . 5 - 91 223 23.7 K) 88 88 ~88 I 8 ~8 8 d 88 8 I 8 fHi I I ia 2 I. Jo opa U "N ti U u -~ ~ 418 j 8 8 8 18 .fr ~A8H88U8 888888881 1 Barasa - Miaroibal let TNTCo data summary 2500 S-how ___ BG C-a ic-a 2500 C-c 2500 250C C-d UVI-b 292 25-X 2500 1580 2500 2500 2500 320 2500 316 96 2500 2500 2500 2 2500 25M 2500 256 UV2-c WV2-. UV2-b 25001 2dlution. radiation: 0 2500 2500 200 25001 2500 250 49C 2500 330 2500 2500 48, 2500 1010 2500 250C 'CIE 0 385 0 0 2500 2500 25kC 2500 2500 2500 250C 42 S28 250c 2500 25M0 250C UV1-a eak 2500 2500 2500 2500 109 2500 2500 2500 2 2500 CC-c C-d UV1-a UV1-b UV1-c UV2-a UV2-b UV2-c diluon:o peak ~o 7J101rn1 aE . 96 -107 -I68 .124 -11- -- 0 0 1430 0 0 1070 100m b l40l battle re am -551 -711 100 3: 862 1-day exposure, Barasa E.Coll 40 -- i 20 0 0 15. 0 - 100- C-b . C -4 0 UV0 Uv bottle regime 0 A Runl-i Sample Total BG C-a C-b C-c C-d 2500 5 50 2500 2500 UV1-b 6.35 UV1-c UV2-3 2500 Run2-1 Total lRual-2 E.ColiTotal 0 L 0 2500 0 0 135 2500 C 250 E.Co1 0 2500 0 0 2500 120 0 2500 2500 2500 195 95 0 101 250 25 2500 2500 0 2500 2500 910 2500 0 I Aver Run3.2 Run3.1 Aun2-2 Total E.Coll Total E.Col Total E.Cofl Total 0 0 0 0 0 0 0 690 2500 070 2500 130 2500 1690 2500 0 466 0 130 10 0 0 30 575 0 0 0 0 0 900 0 611 2500 2500 2370 730 1720 790 2500 310 2500 2500 2637 3320 470 380 2500 0 530 0 0 UV2-c 2500 50 peak r 0 700 110 0 505 2500 0 :01- 110 2500 114 10 1: 790 3 575 % Kill St.Dev, Total EColl Total EColi 0 0 0 2-day a1 77 5 -5 100 100 41 25 0 400 347 0 0 239 84 0 0 0 21 0 0 2500 ______ 1275 99 10 0 100 71 1 408 2500 Radiation Ambient C-a 21.38 348.33 23.66 631.14 1.00 26.50 765.50 2.00 28.00 762.13 3.00 26.90 589.00 4.00 26.03 453.86 5.00 25.08 202.29 6.00 22.86 7.00 93.86 0.00 998 100 0 1732 3 C-d C-c C-b 19.41 24.14 27.69 33.22 35.99 35.58 34.02 30.28 18.3 21.0 23.3 26.7 28.5 28.4 27.8 25.6 19.5 24.5 28.5 34.1 37.4 36.0 34.9 31.2 - S 60 -- U-- 40 -. 100 -- UVl-a 19.3 23.2 25.6 29.1 30.2 28.8 26.7 24.2 17.96 20.06 21.85 24.63 26.35 26-52 26.58 25.47 UV2-b UV2-a UV1-c UV1-b 21.1 19.2 20.5 21.36 30.8 24.5 26.4 27.53 32.5 25.7 30.8 31.38 38.7 29.4 37.0 36.52 40.0 29.8 38.2 37.90 37.3 28.4 35.5 35.34 34.2 26.6 31.6 31.60 29.5 24.2 27.1 27.31 --- C-d - 00060000 700.00 5500 @3 40 0.00 -400.00 300.00 25.00 - - 15.00 5,00 0.00 0.00 200.00 0.000 2.00 c A -UV1a --- UV1 UV2-a UV2-a UV 2-C -Radiation -00-00 1.00 Ambient C-a 900.00 45.00 3.00 4.00 A.5.00 I. 6.00 7.00 -A C-b C, CAd UVI. u b UV- UV2-. battle regime 9 Temperature & Radiation I- -,c exposure, Barass Barasa - temperature data summary Time -oU1421 9M0 0 0 964 1136 0 2500 0 1395 0 0 827 1043 318 335 0 90 0 0 250_ :0m0 10m0 20m0 adiation; 590 2500 00 U02-b dilotiov: 20m11 E.Coli E.Co(1 Uv2- ___ -595 2-day - 0- 100 -121 99 C 2500 290 70 2500 1580 2500 1400 2500 0 1680 1: 920 radiation: 305! S280 5-hour exposure, Harass - TNTC -2500=77 % Kill SL.ev. IAvee Runl3-2 Ro3-1 Total E.Coll Total ECollTotal F-Can Total E.Coll Total E.Coll 1 0 0 0 0 0 0 1 90 0 130 2500 1395 870 2500 690 2500 100 0 96 114 90 0 0 10 30 0 0 98 36 32 25 1125 0 1592 0 10 S0 250 27 0 949 0 110 2500 2500 2500 1770 2500 140 0 0 0 1049 140 2500 1332 170 2500 1290 2500 100 0 96 0 76 91 0 0 0 40 0 110 0 60 100 0 1193 0 995 20 0 0 0 710 0 -39 1932 0 960 2500 150 500 00 25 2500. 25 100 94 141 50 100 39 0 0 1372 a1530 560 0 -28 1011 0 2500 1795 2500 250 _____ 10 111m 14 m 3: 950 2: 950 Total E.Coli 0 BG 96 I Run22 Run2-1 Runi-2 E.Coll Total E.Coll Total 0 0 1 0 2500 2500 2500 2500 25N9 0 0 47 75 20 1640 2500 0 2500 2500 2500 2500 2500 2500 2500 2500 2500 2500 2550 0 200 47 0 1501 1 250 0 2500 240 2500 2500 2500 2500 2500 250 2500 2500 Total 9L 20 2: 9t4 1: 735 % Kll 2500 472C 24C St.DeO. lAvrge I 0 0oa 0 0 01 0 0 S.Co W06 0 858 3401 25sf 900 2500 34 169-7 1006 53 0 60 29 01 1778 1667 1291 40C 0 270 833 c 2500 2300 2500 460 2500 2150 0 1075 c 1807 2500 360 2500 25W0 1 9c 1 1196 G 245 0 30 0 240 1290 31 035 172a 10 1110 0 c 1113 2500 2500 220 25001 2500 25M0 1783 290 51 0 1082 11 0 21 Z2 1954 120 33C :0 1390 -22 0 2500 0 396 5 2500 21 RunlSample n3-2 IOun2-2 -1 I i.CoTlTOW I 0 0 -1 2500 1L 0.00 8.00 hour 93 Mvb UV2 Boston, Rlun I 5-houc: 3/1102 TemrPeratur data . 0 Rad alon 9:30 TIm 5 UV-a a AMbento 3 12 -40 2.30 475 1a ;12 186 184 175 80 C-b 75 73 182 18 246 232 3/1/02 5-hr. Radiation and 25 .4 ~ ~ Eavauon the1stok raactid 0 BL 600 115 09-8 Boston, Run 5 E.Cod 0 1000 0 40 100 35 35 1200 UV-41 K 2 15 1 :5 bottle Radia-on 5 1 5 1 Painted 10 0-2 Total E.C.i C-C Uv-5 23.7 not e xceea thfishold lemp d4l Runt-2 Sampl/ Total C-. C-b 5s apparoxknately. 22.7 247 Clear bo.ft OIme (hour) 4ata4nor4or Bacterlali K/il Run1-1 BG 1 217 F- i len-.-.-t. -t- 05 5 . 237 226 --- D c UV-c 9 24.9 24.1 251 Temperature data .-~ e~- ~ 1--- iC- Ib UV-b ~1 178 182 0 8o 50 1300 1600 55 0 0 20 0 95 0 0 175 8 35 ECnI 20 275 -51 97 96 00 90 0 -83 98 1 _ isFC_ 2.1 52.5 a 425 128 Ka 0 0 82.5 0 50 1370 Total 0 75 35 125 44.8rdad %kill Avera, E.Co Total -- - - 45 100 95 106 71 6 ( $ 2 5-hioor: 3/5/02 Ternperalure data TIn. 51 Ambieni 512 69 56 560 21 Uv-* 1C-a 1Radilatlo 915 0 3/5/02 52 . 90 10-0 IUV-b C-b 80 ! 54 109 6.1 14. 48 53 151 158 edbWile Hall /an-Paledbo -- =2 -R---- -a--i-on s o 2 Ev4h4a171 ThrlsholdradlataIon was 1 as lirn (hours) 12 exceedd kill Run2-2 Run2Samnp I SL 5.9 85.5 5-hr.Temperaturs and Radiation data a 8aceral I-4 C-o 54 ,3 '4.7 Total BG 0 c 16c0 C-C 40 UV- 144 79 0 Aoo. 0 7T1.1 85 0 0 40 7Q 1201) Coco UVI-a uivi.tl c 0 100 C-d E.Co 0 1400 35 110 1400 55 14001 20 C-a C-b Total E.Coll s 20 72s 0 Total 0 70 0 0 110 5 ECob 000 214Q 3 5 0 9804 9036 35 300 140 KA age .Coh 1400 28 135 1400 97"1 135 1.00! hr.Bacterial 4&S2 0 1M0 Wal 10000 5000 1786 ""- 10000 Ion 0 50. Kim I 1 EC o 3 o 93 00 a 94 Boston, Run 1 1-day: 32/02 Weather: hazy. treezy Temperature data Time 9:30 397 10.6 7.5 7.9 7.7 4 1 30 5.30 178 20 9.9 8.1 14,3 9.3 143 92 14.3 9.3 8 8.31 IC-c lb IUV-b IC-b a UV-a C-al Radiation Ambient 0 170 8.5 175 10.1 10 5 8.4 IUV-c C-d [c 8.5 16.8 18.8 75 162 9.9 10.7 10.3 12.0 9.6 91 17.3 10.3 16.5 3/2102 1-day Radiation and Temperature data 20 0 -- - 18o - - -600 Ambient -- - -- Clear bottle '4 0 - -- C3 440 0 . - - 0 - 2 1 Painted bottle -- Radiation 5 4 3 -*- oo -a ----- --- --- - Halt-painted bottle ___ __----- ---- - --- -- - ------ _------ ------------------- time (hour) Evaluation did no exceed threshold temp or radiation 3/2/02 1-day Bacterial Kill Bacterial Kill Run1-1 Sample BG C-a C-b C-c C-d UV1-a 1200 35 55 1200 UV1-b UV1-c E.Coli Total E.Coli 0 750 875 70 1275 1210 37.5 92.5 1300 0 160 0 10 25 80 5 0 70 0 750 115 80 1350 1220 40 130 1400 0 75 0 0 55 80 0 0 35 0 750 60 60 1200 E.Colt Total Total E.Coli Total BIL 120 kill 1% Average Runl-2 0 117.5 0 5 40 80 25 88 91 -70 -61 95 0 88 52.5 -73 100 96 66 60- 32 98 100 55 _ (L-. _ 4- Boston, Run 2 1-day: 3/6/02 Weather: hazy, breezy Temperature data Time Radiation Ambient IC-a UV-a [a 9:00 115 0 54 5.6 0 4 12:30 250 8.4 8.3 82 IC-b lb IUV-b 5.5 8.3 5.7 5.5 9.8 IC-c 5.6 10.2 10.5 55 IUV-c Ic IC-d 5.6 5.6 5.4 10.4 10.7 10.6 7.0 3/6/02 1-day Temperature and Radiation data 400 120 100 - - -- - - e --. .. Ambient aClear Bottle Half-painted bottle so -- ---- 4 S2000 M- - -- 05 Painted bottle n________Radiation _____________ -_________. 3 -- 200 -- 1 15 25 2 3 35 4 45 time (hours) Evaluation did not exceed threshold temp or radiation Bacterial kill Sample BL BG C-a C-b C-c C-d UV1-a UV1-b UV1-c Total E.Coll 0 1400 20 170 650 1600 15 125 1000 Average Run2-2 Run2-1 Total 0 60 0 0 20 110 0 0 60 E.Colt 0 1200 45 130 850 1600 25 85 1600 Total 5 70 0 0 5 100 0 % Kilt E.Coli 0 0 1300 33 150 750 1600 20 105 45 1300 Total E.Coli 3 65 0 97.50 100.00 0 88.46 100.00 13 42.31 80.77 105 -23.08 -61.54 0 98.46 100.00 0 91 92 100.00 53 0.00 19.23 3/6/02 1-day Bacterial Kill 120042 10.00 ___ -- 40.00 40.00 2 --- -CL> 20-_ 00.00 DO2~__ _ 95 Boston. extra 1-day 1-day: 3/7102 Run3-1 Total Sample BL BG Run3-2 _ E.Coli Average Total E.Coli Total % Kill Total E.Coli 0 0 0 0 0 C-a C-b C-c C-d UV-a UV-b 1300 0 100 800 1100 20 40 10 0 0 10 30 0 0 1100 30 75 1050 1000 15 30 30 0 5 5 15 1200 15 0 925 1050 18 35 20 0 3 8 23 0 0 99 93 23 13 99 97 100 88 63 -13 100 100 UV-c 1250 15 1200 5 1225 10 -2 50 88 0 3/7/02 1-day Bacterial Kill E.Coli 0 -00 I0 C-a C-E C-n OTata Cd UV-a dye v Boston. extra 1-day 1-day: 3/8/2002 Weather: overcast and windy Time 0 9 15 12:15 2:15 5 6:15 9 Radiation Ambient C-a UV-a a 70 7.10 6.60 6.60 123 7.30 8.50 8.60 85 6.3 7.8 8.3 0 6.7 6.7 6.3 C-b 6.6 UV-b b 6.60 8.60 8.3 6.60 920 8.7 6.4 6.6 8.1 6.5 6.6 8.9 5.5 6.4 6.3 C-c UV-c c 6.60 6.60 9.10 9.60 8.4 9 1 6.4 6S4 C-d 6.6 9.4 8.8 6.4 6.60 7.50 7.2 6.3 3/8/02 1-day Temperature and Radiation data B00 --------7 00 ---- 500 - 4.00 --- 3700 100 - - -- - -- -- - - - - -------- - ---- ------ _ ---- _--__-__-_-__--- --- - __-_ ----- - Ambient Clear Bottles Half-Painted Bottles --- Painted Bottles --Radiation -- - -- - 000 1 0 2 3 4 5 6 7 8 10 9 Evaluation. did not exceed threshold temp or radiation Bacterial Kill Run4-1 Sample B Total Run4-2 _ EColi Total IAverage Total E.Coll BG C-a C-b 0 2000 800 1000 0 70 5 0 0 1400 1000 1000 45 0 10 C-c C-d 1000 1000 60 55 1400 1600 45 65 UV1-a UV1-b UV1-c 1000 0 0 1700 900 1000 0 800 1000 5 1000 10 1200 1300 900 1000 800 35 1600 55 1200 0 % Kill Total E.ColI 0 57.5 2.5 47.059 95.652 5 41.176 91.304 3/8/02 5-hr Bacterial Kill E.Coli 52.5 60 7.5 41,176 86.957 45 29412 21.739 0 29.412 8,6957 23.529 -4.348 47.059 100 120 __ _ -L _ 60 -- - a - 40. 20 0 . 0 - - > --M0-1 > n 96 Boston. Run 1 2-day: 1,1-2/02 Weather: and Partly cloudy breezy Temperature data C-cl UVI-ul c Cd1 UV1-b b UVI-al a L Time _ Radiation Ambient IC-al 1 930 112 74 691 6.8 89 7.0 8.0 93 8 1 2 12 3C 640 17 5 178 174 17.4 233 266 25.0 236 27 5 24.1 224 283 179 17.9 23 1 250 475 180 18.1 3 130 4 530 4 59 81 89 8.9 93 11 0 10.2 a5 123 3 19 2 19 5 19 11 2 192 930 397 6 170 179 17 5 144 15.2 14.8 166 186 17.6 16 1 169 7 53X 20 180 95 93 9.4, 10.1 10.5 10.3 100 104 5 19.5 19.2 19.1 5 300 E 00 al Panted Paind time Evaluat-on barely reached theshold radiation. 6 4 2 0 (hr) di not exceed temp threshold Run-2 Run-I 0 115 0 0 15 100 6(70 25 60 60o 1400 UV1-b [UV1-c 12-Col Total E.Coil 0 C-a C-b C-c C-d uV1-a 11-2/02 2-day Bacterial Kill [ Kill BL BG 98 bent n ons -- 100 Total 10.2 19.3 19 40 so Sample 16.3 1451 921 18 7 12 7 800 50 200 Bac taraia 62 138 Temperature and RadIation data 3/1-2/02 - C-d 8.7 25.6 25.4 10.4 15 65 0 0 FAXI 7D -0 1000 45 40 1000 1400 35 45 0 75 0 - 0 100 100 5 60526 0 0 60 37 110 0 --- - - - - o- 0 95 - - - - i2 - - -1053 100 0 79 0 100 105 0 u 653157 60 SIX ioO E.Coll E.Coll Boston, Run 2 2-dayl 3/5-/02 Weather: moring overcast and windy, attemoon 5unny and calm data Radiation Ambient C-al Time 69 5 2 512 910 0' I60 56 107 09 0 17 6 s 2 6.9 18. 115 90 3 4 1-230 250 j 92 Temperature UV1-1 a 58 11.3 1 1 .3 100 C-b2 UV1-b b 5.5 6.8 68 11-0 145 183 25 14 .0 18.5 187 182 .6 109 126 C-cl UV1-cl c 6.8 6.2 16.4 136 1.2 52 206 36 188 18.2 9.8 12.5 2.0 18.5 88-8 6.2 Cd 93 7 7 25 17.1 2.4 18.5 11.2 188' 95 3/5-6/02 Temperature and Radiation data 'M 0 -1--Ambient 34 Clear Bottles Mta 400 - 20 Evalualon- Theshokl lemplrature Bacterial kill Run2-1 Sample Total BL BG not met, but threshold 4 3 2 time (hr) 1 0 radiation was exceeded /50-02 2-day Bacterial Kii Run2-2 Total E.Coli 0 1_00 0 E.Coli E.Coli E.Coi 0 70 1400 0 65 15 0 0 10001 0 30 1200 1200 5 0 35 35 0 0 30 0 10000 50 2857 113 -60.71 6 10000 0100 00 148 -110.71 0 55 C-a C-b 1470I 25 25 C-c 1400 C-d UVI-a 2500 65 190 9 UV1-b UV1-c 455 2500 0 40 265 1000 0 65 - no - ---- -xll - - o a.400 2 00- - D0 D 97 Boston, Run 3 2-day: 1124-2512002 overcast and windy Weather: Morning surny and oreezy. alernmot 0 1 2 3 4 TMne a Radiation Ambient C-al IUVI-1 R6 78 144 870 186 184 71 70 102 90 73 122 87 810 63 85 8.3 83 67 0 6.15 15 9 5 2 15 2 5 3/7,1102 20 0 - C-b2 16.5 9.6 8.4 6.3 92 191 98 8 6.4 C-cl UV1-b b RB 93 182 95 84 9.0 18.9 10.4 9.1 6.4 186 109 94 64 UV<leC 87 64 18.3 106 92 84 Cd 9.0 1.3 10.a; 74 1851 9 .8 75 6.4 83 2-day Temperature and Radiation data -- - - - - - - - 9.3 - - ---- - -- .30, xcii AM 4 93 EVa3lraton ercoeded hiesnhold radiation. did not exceed threshold BG C-a C-b C-c C-d UV1-a UVI-b UV1-c temoerature __-1_n_-2 jRun3-2 E.Coli E.Coll E.ColI Total E.Coll 0 0 0 0 D 20 30 1100 10 13C0 10 0 0 75 1 30 10C 0 0 75 0 95 625 7 5 10 1250 5 1250 -2E 25 20 1400 30 12N) 0j 102 0 75 0 HS; 10C U 75 215 -7 3785 20 1300 55 1300i Bacterial Killu Rurt3-l Sample Total 8L 0 5 tme (t) 0 3rr-& 02 2-day ftCle lal Kil 12 0 -- - - - - - - - - - - a N - W 2o u -Y u -a - 98 Boston - Microbial 5-hour 1 n1-1 Sample BL Data sumninary Rus-I i BG C-a C-0 C-c 115 5 F101 o 40 C-d 1 35 1UV2-a 35 UV2-b UV2-c 1200 peak radiation: - 0 50 ISO 1400 95 1000 -9 200 2 0 Runt-I 0 1370 Total 0 75C 75 750 C-a C-0 !C-c 60 50 0 115 0 80 55 1350 60 1220 .) 40 1200 120. UV2-a 35 55 1200 UV2-b UV2< 144 35 110 301400 7012DC 20 110 45 14001 14001 0 130 35 1400 A___ e %Klt Total ECo Total 10 5 0 S3 1 0 244 99 0 0 90 0 11DO 109 0 44 74 25 134-3 31 45 0 0 24 f58 -23 c a 98 a 5-hour exposure, Boston E.Collj 0 1350 1100 40 0 0 75 3 Tota!LE.Col 0 0 -40 94 -22 "TNTC Run2-1 jToral 0 E.Coll 0 1 0 0 1400 20 10 25 170 73 1000 l _= 901 :2 7 98 100 47 11 100 100 621 4Q-0.. 650 0 1600 5 15 0 125 % KIll jPutt4-~JAsera LRun4-t JRtmO-2 Averg Kill IRun3-1 !21741RnE.Coll Total E.Colt Total E.Coll To01 E.Col ITotal E.Coli Total E.Coll Total 0 0 5 0 0 45 70 1400 1C 1100 30 2000 7C 1300 1 79 0 259 5 1000 0 800 0 0 0 30 74 3 10 327 0 1000 0 75 5 1000 0 100 16 28 45 I038 Ic 1050 1000 60 1400 5 000 -4 65 1290 15 1000 55 1600 100 1100 C 1000 0 244 c 00 1000 C 15 so 0 20 75 2 1000 10 308 C 30 40 0 1! 1200 3-- 16001 55 125 45 1250 401 -2 Run2-2 EColl1 Total 0 0 60 1200 45 0 0 130 20 850 110 1600 25 0 0 85 60 1600 , ________ - 250027' 2: RunT-2 0 BG Cd4 C C 50 0 0 55 0 1: Sample Total 4E.ColI SL 0 1600 0 Run2-2 E.Coll iTotaliE.Coll c0 75 1400 1000 C 35, 20 0125 50 45 0 1000 Ru2-1 -2 Total TOIaL E.Coil 0. 0 5 0 0 1I 8001 1238 1-day E.Col 0a 65 99 2 95 571 -i 991 971 67 1 5 04 552- 1v2-b UV2-c 1 1% Run41 0 C-b exposure, Boston T 5 30 - - 0 20 - 0 2- v2+ v bottle regirne 2-day Run3-2 Avera Run3-1 Run2-2 Run1-2 Run2-1 Run1-1 Sample Total IECol Total EColl Total IEColI Total E.Coli Total E.Coll Total E.Coll Total 0 0 0 0 0 0 0 0 0 0 01 0 0 L 10 1100 30 1133 55 1400 85 1300 600 115 1000 75 1400 BG 0 36 30 0 75 15 0 25 0 0 45 25 C-a 0 25 0 30 0 95 0 75 0 54 C-S 00 0 40 5 1250 10 1117 65 1200 35 1250 60 1400 500 15 1000 C-c 30 1400 20 1517 1400 100 1400 110 2500 190 1200 35 1200 C c 41 0 75 0 5 c a5 1 0 55 C I5 UV2-a 75 0 149 0 215! 0 0 40 0 455 3 0 45 UV2-b 20 1250 55 1300 30 1300 255 1000 60 2500 70 400 00 UV2-c E-Coll 0 0 - all 20 mA dilution % KHi Total 0 62 0 0 32 81 0 0 875 2-day exposure, Boston E.Coll 95 1 100 100 49 -34 0, 07 I00 -10 -35 97 c 100 40 -31 - 20 100 i C.M 6- C. LN2 a LPv2-b bottle rogirne " Boston - temperature data summary Time Radiation Ambient C-a 9.00 313 8.48 350 3.00 11.90 280 5.00 10.93 8 8.00 0.00 10.62 13.55 12.78 11.08 10.7 13.3 12.4 10.8 UV1-b UV1-a C-d C-c C-b 10.0 11.1 10.5 9.8 10.41 14.66 13.47 11.84 10.1 11.1 10.5 9.8 9.70 9.34 9.32 9.32 UV1-c 10.3 14.9 13.7 12.1 -1-Ambient Temperature & Radiation C-a 4001 100 30--*--C-d 14.00 3o-+- UV-a 12.00 2501 1.00 200 Et -C-b UV-b 1 5 -UV-C - Radialton 6.00 F100 50 0 - '50 2 00 0.00 0.00 1.00 ,0- - -- 2.00 3.00 5.00 4.00 Time (hr) 6.00 7.00 8.00 99 ulvz Dumay 5-hour: 1/26/02 Tamperature data 00 1 2 3 4 5 C-b a 253 349 409 447 46.0 45.4 24.8 337 38.4 41 5 430 43.1 28.3 42.3 44.2 471 448 340 10:00 11 12:00 100 2.00 3:00 UV-a C-a Ambient Time 0 1/26/02 25.3 34.9 40.9 44.7 253 39.4 465 50,9 46.0 524 45.4 51.7 UV-b 26.2 38.9 45.4 49.5 b IUV-c C-c 26.4 41.8 50.2 267 436 51 7 561 498 51.1 53.3 56.8 55.1 48.0 49.9 55.2 53.1 51. 0 - 53.8 bien -- Ax Clear botle . --- - E 200 - - 50.0 5-hr. Radiation and Temperature data - oa C 26.0 399 48.3 51.5 25.8 39.2 46.0 H - Hall-painted bottle - - - Painted bottle 00 0 1 Sample BL BG C-a C-b C-: UV-a UV-b UV-c j 0 2500 2500 272 556 520 102 624 0 250M 136 0 98 0 0 2 1 temperature for three hours. 1/2 painted for 2 hours I % Kill Average E.ColI E.Coll Total E.Coll Total 0,5 0 1 0 2500 2500 2500 2500 0 9416 146 2500 156 2500 100 89.44 0 264 0 256 94.52 137 494 176 432 9996 396 1 1510 2 2500 1 89.96 99,96 251 2 400 1537.5299.94 1562 1 2500 ju1 Runl-2 Total E.Coli Total 4 3 time (hour) Evaualion. Dained Sotle exceeded threshold Bacterial Kill________ 2 80.24 Kill 1126M8 5-hr. Bacterial K . I ~ Tta 0t 2C 100 0 - 20 - - - 100 C V.uvl-e U lG a- t -. Vn 2-2 JIM 00 340 3-1 02041-20 R .;l0 B 2 Rn2-2 Tota CAW-ms -1 Ru B..we Ru_ ft- C-c UVI+b UV2-6 0 0 240 2400 0 0 2400 40M 05 A-ply0 00 2 20 5 2 2400 -a 0 20 1 60 4001 200 200 2000 04 260 27 5 0 0 7420 1 400 0 w 440 4 225.00 __=0 35 _ 14. 15 0 10 76un10 " . M"d-a 3Md QuAid I0 goumrt 0 0 11 k= lm Ran m m RnMen-Wan. . 0 0 6 oe 0%3 0D0 '360 3 1 'po 00100 C 0% o'im a HaCndne G U1a 0t"0 Otim ilid I.020 374 340 4 UVI o W.W. 09 2 39 0 26. 100 00 0 0 0 a 2 OG V 1.r 4 LLtira 228 53 55 a UV2-. 0 a 0 __ ,qual W 0 _ 0UP 09 BG 4 374 34 M -sn 3rmcuar,,w 3 0.029 G-44ri . _ Cotum n 2 UV2 0 ia 3r0dQuWrU. ow0 W6 0 M H.: b NO 0 000424 20.070 P -m p 040. 000 l Wer % wltr0 ttie I 0 2.00 " 04.2 -0(~~~~~~ o0. | 9 7J 0704440 '01 0 QV2.0 Ipp4 % toer9D% MOO 3Q.O.0 0o 0020a4. w R.0k A.Wly. C421 It 440400040r8200 .420 DO ._ -Whibny 00 0,0400 444007402202e a0w0' 404900 09 M-aan 56nu ING-uAl. ow 5 6 3 2 3"8 to- BG 3dQameMxma 04 0.40 AM"Wal P1Wk 2Q04405N. toc G o.oo a r 0.2C0n000r24 : J40 74 C.0700004 022000 . 392 ".-vau 100 4 2Sapei 21 UV7 Il 2.l V lum 0opu olum pu~st Co _ D-Ir" 1turtwo. "eA' M es 0 10.0 .. UV2-. nV 1.1unu Mein 0 400 0 MeereW-Walth S-n so I ft'll, Ian Messin LIP. C-. 4a UV2-a M.- I 002.00 7040244 - 0 0 _ 340.UU o. Mean DON ; 00 0 VW F2 Sml ".: N,4 ,,1"l 1. c Ann bG 0.9 Clmnf _m N . .0 4 9200204 - 00 0 ti-Il Hr S-m2 Med.up3850,so R.a -- A0 nK Anay "np I - 420320 M_.,ia 0724. 0.00 o Crdrr UV m - .o2 o .,j. N 2,00 40200040 00020000 0.4007744 M00m 5V2 0 M7Nt-u00n2 IPnk Ansky inpu C.W-m 3140 3U0 4 - ti N 14-stul1s .. M0di N BG " 2 00 302 228 A..&"se 0 106 52 0 704. . . 0,l C_lnv I 1--a 02 w44477D 0090400 Men-Whhney fak. A20y00047404 440oI:Inu Colm 1 i" Znpu Cnn 54 0 0G M__eum o0 U11 220 ,tAsiel, I-ml 9-au . S24[C H, | H a C- C41.nce "'Nt C"'Nrt" C'Am 72 I06 mnput 744070 iiri 07 0".,rpUmv awtiftes Min-mu An2y00 2 o w 2 3 0424802924402 M 24 2420 420 400 40 40 f 2420 444. 2800 It G46 00 24 20 2800 h 46 3 4 2 004: m 000u004404400. 70'00 a 8G _______________G_________ 0 | 0 04 0rw0 0 QWor Sampl. K R 00k 20044 .M 0 Itpu oidlne G.4-m [ = 091~ 12 290 so 5 0 a 0 C. I .1"G 240 0 200 2 240 0 2 0 320 20 140 2400 2.1 10 0 IUV- VV- UV2+1. C-tI _11V1-leUV3-,l ~-eUV11 IC- 1UIV114040 11400 200 2400 2400 200 40 2400 000 I111 2-2 0 0 0 0 0 M 0 0 6 -05 0 2400 1 C-6 0 o 200 -|UV2- 0 0 81, 504000 0000-1 0-2-0. 00.51 400U0 3. U C- -26 0 -smm LV2- 1,, 0 1 3rdQ__in MU-m I 0 0 Man-Witnt. R-nk An-lymb. 01 227 w0 O ." _0 at 1U6.0 t.W . . 320mOO J+trmen-wmany mat fi tut colma" v. UVi C-t 20 I In.utC AMYIN;s -lm Smp Al R nk DM . 0 6,IN'o C It a.mianNmt 20240 0 0. M~da cv 0 0 0 2 M.. 7 -Whh.7y F.- 6-m1 00l. 6195.0o 21 0 0 042C0n2.30 2.400 1.20D 3 0 0 R A0-% R-n Sm I--u 0 ,86 15.0 0.0 -o -1O.00 2,400 M"dal . V 10 222 99%'4p.e 2,400.D f28rp k ; 0 10 , . 0 u2-0 &5% 4 0 2 0 M- .- M70 DdL.i ...5m1 181.0 0.G An2ly7i N M Anaysa Me:",J004 E~epaaRar 42aH: W-ga N G C2 Lo . im 64 2 , 0 G 00222.7na 0.tunn io|lo50 44np.40 An-y"- 0 - 0.04o0 1.40000 t" Fink 5S42 0 0 ~nyjL R-nk _ 0 0 r95%.% 0 am 0 0 0 A.Wlys 0.00 0 '1 0 0 0 U.n-WhItal" R..k Ank,"la t-r96% MppW 96% an S. m i 5-1 k0 Ft um260 " 0 kva 0.01) k.40D03 442 0.0 76 0 2 UM 02020 0 2 7] 07020 a o t dr002.8 3r400u20. 400 000o00 424d200 v2.00 -955 7.200 2A00 1.4.20 w a "3w 00 00.3 Dill .j42 -p 2 0 a 0 0 M.n-VWoNIly R-It 1-~ue ka 95% Mpe 95% M.dan DIN Fitt. S-m1 FMAn SW-n 10 0 w a NO6 0.00 _ 186 21.1 0.0 AnaVmte A 0 QCKrbe MNum 700 A 2 00 0222 .4,4.0a 700. ,20,7042 00m0.. Medien 01M. kank S-m' 2.12o 0 . 30 2. 17 Dm. .m2 m 0m 220 k2200 2,40C .0 r9b%uppW95% 0.02V BG C", ; 0 R'&rX oMeola 2Sml o 002200 -it0 02.00 02030 BG H..Nu. inpt clum,1 4 aG 2,0 70 00 a 400 00 s m 1.3L* I,4ttx 2.440 ~ 22 0 1,70 s BG 2.MO N Dt Sm " n M"n o o%2o20 ,4200 00 Q-4i. .02 2.2400 2 0 0 M VI 223 ,330 0 2 2.400 2 ,4 4W W 2."w -oe 5 pp.r0595% 2,29W. 0 343 -u HaKSm 2.02- 14 0' I iltum 35 3rdck QurieMa-ium 1t u-wl Mcdhan 2.400 2.AOO 1 ow OW0 1.300 56 93 275 2.4OU 4.n At- yI F S,. P'.n- - Baism e9% "W"'r95% 2,Z %000 W5 n0000 .1.2. 0 1.32 5 Median ~ ~ Q00 0n 2. o 0040I0OG044 4.2" .20 2 " -S-mu P-n 1H. MdI"Jr, DIN,. - 0 2 G |a oeult 240 1w1! M.0-0 M -. 4,32 202~ 2,370.00_ Inp.1 C.1l' opo2454. 228 M5 24 0 yo HRak Anly Mn-wwhtinmt, 95% P--., :Ie 66% uppw M6 6_m2 M.M', (IN -r,. buI "I.' 0 Wl t 390 9a.0 W 1 413G uv..a 00 .0.0.48 -n. I, 442 4 Moolan~~~ An 240400 0.0 4 2 lu ll-, plict.leVi-iov. Anwiyso 2 [ 400y4440 02202.2 -" - 4 323.3 0 A.MVyO. R-nkp-ee ueM-Whh.ne R-kSr2 26 0.204 .0. A-"*. 3r' '0 A.Wlywk, 22. L_ urt 2, 215 'Wh"e R-1, . 2.400 2.400 1 00 I0 V4 ,. 00,39'5 1c m- 0 0 ItIG 00m 00.402040002220.02440 0 0 NW 2 0 Dl 000042.414. I4 Wqua t 0 I O H.: Not u C .is " _no sulullft 01-1rpave tnAum W- C M 3aN" M 09002m4. G-023 M- 003 02 N UVlb UV2. Iwlk 000 VR,-0 0202447m 2 1a DIMn - S-90 M P-mp 2 ,qm - 'mu IVChll WuiiMOW 3rd Qmnfte MautImI i 200 No a 0 0 0 4 G.n1 ; M'u Cun2u . UV2-o "Mw 0 L. ........ UVSlam Uvi-il UV24 R o:MdINan Dill O etsacW4" 1 irspot~~~~~l c+ UVOMWW. SU42 SI09 UV2-b A-"%st 40 40mp.e .. A43N2 000402000M. W0.2ow. DU.40074 hok C- 0 : 2 Cot0 0pt . 0 Men-Whart-y psu 991090955 1090 00 .00 001 G1001 1110 E00 '00000 099- 10,0 00 0 000t9 it A96 1 500011 . L 0-9 999 0001050 7.1 0 POP5 10 1 _-1e %soges %SS 1909, 5t F01 90093 Pe n o q -" sees leddo Sq So9 , . 0 1 1 I 00 09 0 .a 00 0 . 050 M 007MS 9 010 1i 090 99r090 0 e .7 9go 900 001 000 05101 10060 900 551 1 00 0 CA0 5 9 60 -9 950-.1 ?,An; u00105 000' 600 o000 0 0 mme dd 00 9 -1 0S0100 %We 00 0m L 9IS0 Nl 919CC nA 9s e 3 600En n9 0 - 100S0.. uaooa ilt5 n )7A 091011550 9 .950d -IIt~o" j OON D 55095n001 R-En on i E0 0005 03 0 59950090 0 50-09 ce 'N5 00 3IIZ2 0 'sh' S01 10- t 00 000 0 0000 PIPE=6 190W 0-00 0 9 50595 5556900060 aa 6 - nd---amoeeno '0-0 -n I P i99510 00 am ;109 In0z'0 Cog 6055995195000-010550" SO000 9900 0500 o~i 7rg 6ev5t D00'0 000 W"56600001 955193me ELt 9 0 0 G~s -q 09100 00090 .550 000 . 9 5 0000 5905 1W, g 50650E 1 0055 PIS 000 s 11 WOL 90. v 6I90 990000 000 .-. V.-090 o arl 591 v9 0n 0000 00 1 05 000 a -Z-Aan .A a DL JJrsG 010 u MS 5- 94 U." PTS AO0 N -AP-d [_WTV1 F ,d- 'An I O 0AR8 5 9105 0000 000 On P0ric 5t0 10e 95901 a0 9055 o01 5 X00 000 0 - 6q I 6n9555 -~~-n" - cG c e 31 - 9M.00 -M KO 0 -.O A I gi uioA " "'7 e o 56 9 000 O9 009000-z 10150 Jed %96. -0 9-90 -46 000997 '-eLS -Wm Woemn 00 190 00 z 000-1, %S6 00 9 -4 16 -0001 0 o S 00 600 51 4- 5 1 55500511015165151500959 ~e0 PIC N CI 906 ."I- 9z cm ; 0900 C 10 1 n0. 'rm9.5)"O0 51 99n 90 1 8 00010 1E %5s' '56ggsaal - e 4 0 -- 0059 0080 .,,dA .~ Lwswa 00CR00 am 009 0 9Z - a, -swa aupow m'- II 60 09 00 j 09~j4 G H M",'" 50 0 0 zft 0 09 09". 9550i 0 000 z qofj ) Wdoos" " 0 I0060;N5 s O O A.UM-n 01n D0 5 a_.. w -4 t U W " n 5 WO 0 0065 -3 An 0 5 SWBAW.V Ul. "l 09 0-&Z 009 Pog 005 00 0050 0000 005u" 0 00-009 %q6 I W0 -0CL JAdd 00-019' %9sol nit 92 S 000 100. wowU W LUPtS Z-9 -d MO' 0007 Oat3 0"'? 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(;O--4.1 NA034e, 8561( N61,8 OA 82.8y1 #AE 8870.0.87 28 N88.818888886 -l013 0146800 w26 ~ 11 95 _ S6 _ __0 ~ BA08801 8.06 7116208688 ,'8 6008780 MME? 50868, 16 08l U-7. 8388y68 830M 6 8 136820 F 106 0 4.212 11611 880246696 660881.-"p ,88% Me~ 18 80 81.0 0.30,21 611080 . 0 8l 25 1801 0 5 8 1818 [2111,8.1202888'"'A I-ME'830(1060800 073 286 007 11 S. Ell 7,186 -802 1l0 Bottle Water temperature Model Constants dt[s]= T, KJ= m]= x [m[ z 600 291 15 D L= 0.08 0 0005 021 Ajrml= 2 A_ jm [ A1 [m2I = t 1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 9.10 9 20 9 30 9.40 9 50 1000 1010 1020 1030 1040 10.50 11 00 11 10 11 20 11 30 11.40 11 50 1200 12 10 12 20 1230 12.40 1250 13 00 1310 13,20 '13 30 13 40 13:50 14:00 14 10 14:20 1430 14.40 1450 15,00 15 10 15-20 15.30 15:40 1550 16:00 16.10 16:20 1630 1640 16.50 1700 0.05:3 k, [W/mK] 0 017 C [J/qKJ clear black half 09 01 0 7 lmisiFvlty 11( 02 4.2 '[ 0 0.1 0.2 rulleuivily QaCjUIations lully painted bomte 10t time step time Migl= 0005 T[oCI T. [K) 1860 193 19.9 20.5 21 2 21 8 22 2 22.5 22.9 233 23 6 240 25.6 27.2 28 8 30 3 31.9 33 5 33 3 33 1 32.9 32.6 32.4 322 31 4 30.6 29 8 29 0 28.2 274 27.0 26 7 26.3 25.9 25.6 252 24 5 23 8 23 1 22 4 21.7 21.0 21.1 21.1 21.2 21.3 21 3 21 4 R [J/s- I U [nvsJ Q 3 80 23.56 29 1. 15 650 00 3 80 23.7 291 78 60.0 3 80 23.96 292.42 650 0 3 80 24 17 293 05 6500 293 68 3.80 24.38 650.0 3 80 24.59 294. 32 650.0 3 80 2481 294 95 650 00 3 80 24 93 700 0 29S 32 3.80 2505 7500 295 68 3 80 25.18 296.05 800.0 296 42 3.80 2530 850.0 3 80 2543 296 78 900.0 25.55 3.80 297.15 95000 26.10 3.80 298.73 941.8 26 66 3 80 300.32 933 7 3 80 27.23 301.90 925 5 27 80 3 80 303 48 9173 2839 3 80 305.07 909 2 28,98 3 80 30665 901 00 3.80 28.90 306.43 892.5 306 22 884 0 3 80 2882 3.80 2874 30600 875 5 28.66 3 80 305.78 867.0 3 80 28 57 305.57 858.5 3.80 2849 305.35 850 00 28.20 3 80 745 2 304 55 2790 3 80 640.3 303 75 27.61 3 80 302 95 535 5 3 80 27.32 302 15 430.7 3 80 27.03 301.35 325.8 2674 3 80 300 55 221 00 2661 3 80 2083 300 18 26.48 195.7 3 80 299 82 3 80 26.35 183,0 299.45 2623 3 80 299 08 170 3 26.10 3 80 298.72 1577 25.97 3.80 298 35 14500 3 80 25.73 297.65 130.8 25.48 3 80 296 95 1167 25.25 3 80 29625 102.5 25.01 88.3 3.80 295.55 2477 3.80 74 2 294.85 3.80 24.54 294.15 60.00 52.7 3.80 24.56 294 22 45 3 3.80 2458 294 28 24.60 3.80 38 0 294 35 3.80 2463 30 7 294 42 380 2465 23 3 294 48 3 801 2467 294.551 1600 1Qa,o Q.(P Qk-P 3.70 21 22 -17 51 21 82 -2 70 21.71 -13.08 22 11 -589 22.16 -1091 22 45 -902 2256 -13 22 2276 -11.73! 2284 -14 16 2301 -13.90 23 12 -15 '18 2326 -8771 2343 -6.51 2388 -791 24.42 -684 24 92 -742 25.45 -6,92 25.98 -17:31 26.45 -19.98 26.44 -1799 26.32 -19 05 26.27 -18 11 26.17 -18,49 26.11 -21 32 26.00 -19.72 2569 -17 88 25.38 -16 19 25.08 -1440 24 77 -12.68 24.47 -842 24 19 -854 2408 -8.09 23.95 -8 02 2383 -7,70 23.71 -7.55 2359 -920 23.46 -9.49 2324 -887 2301 -886 22.79 -8.44 22 57 -8.30 22 36 -351 22 16 -236 22 16 0.64 -2 95 2219 0.52 -2 34 22 20 0 39 -2561 -2211 22.24 0.27 10.92, 10.92 10 92 10 92 1092 1092 11.76 1260 13 44 14.28 15.12 1596 15 82 1569 1555 1541 15.27 15 14 1499 1485 14.71 14 57 14 42 1428 12,52 10 76 9 00 7 24 5 47 3.71 3.50 3.29 3 07 2.86 2 65 244 2.20 1 96 1.72 1 48 1 25 1 01 0 88 0 76 kltar 1, dT, [K] Tr,, 1 ]KJ T 291.15 2 45 293.60 17.16 -445 -0 64 292.9/ 1 53 294 49 10,68 0.12 0.02 294.51 7 47 1 07 295 57 0 '34 295.91 2 37 5 11 0.73 296.64 0 24 296 88 1.68 404 0 58 297 46 2.42 0 35 29780 3 63 0 50 298 31 2 77 0 40 298 70 1 39 300 09 9 73 1 71 301 80 11 95 1 49 303.29 10. 45 11 45 1 64 30493 1 54 306,47 1079 1 60 308 07 11 2J 0 13 0. 02 308 09 -2,75 -039 30 / 70 307 58 -087 -0 12 -2.10 -0,30 307 28 -1 29 -018 307.09 -026 306 83 -1.82 -661 -094 305 89 -676 -097 304 92 -665 -095 303.97 -6 72 -096 303 01 -6.67 -0.95 302.06 -669 -0,96 301 10 -0.36 300 75 -2.50 -0.41 300 34 -284 -0.37 299 97 -2.61 -2.77 -0.40 299.57 -038 29919 -2 66 -2 73 -039 298 80 -4.74 -068 298 12 -076 297 37 -5.29 -070 296.67 -4 91 -0.74 295 93 -5 17 -499 -0.71 295 22 -5 11 -073 294 49 -003 294.45 -0.23 0.12 294.57 0 82 001 294.59 010 009 294 67 0.60 004 294 711 0 26 0.07 294 78 0 49 20.45 1982 21 34 21 36 22 42 22.76 2349 23 73 24.31 2465 25. 16 25 55 16 94 2865 3014 31 78 33.32 34.92 34 94 34.55 34.43 34 13 33.94 3368 3274 31 77 3082 2986 2891 27 95 27.60 27.19 26.82 26.42 2604 2565 2497 24.22 23.52 22.78 22.07 21.34 21.30 21.42 21 441 21 52 21 56 21 63 9 83 9 83 9 83 9 8:3 9 83 9 8-i 10 58 11 34 12 10 12.85 1361 14 36 1424 14 12 13.99 13 87 13 75 13 62 13 49 13 24 13 11 12.98 12 8b 11 27 9 68 8 10 6 51 4 93 3 34 3 15 2 96 2 77 2 58 2 38 2 19 I 98 1 76 1 55 1.34 1 12 091 0 80 0 69 0.57 0 46 0 35 024 0 52 -261 -496 -6 68 -794 -8 86 -9 77 -10 84 -11.80 -1268 -1351 -1430 -1398 -12 73 -11 84 -11 21 -1077 -104,) -11 76 49 17 05 17 1 1 /.90 18 23 1851 18 76 19 0 1 1924 1946 19.68 1989 20 11 20 35 20 6r6 2099 21 36 21 76 22. 17 22 50 -14 14 12 -15 84' - I/ 02A 825 ;2 92 - 17 86 -18 42 -19 30 -2003 2283 21,61 -20 16 -19 86 2:1 32 -19.24 "1 99 -18.40 21 62 -17.01 21.24 -15.59 20.92 -14.51 20.66 20 43 -13.68 -13 021 20 23 -12 51 2005 - 12 37 19 89 -12 49 19 72 -12 50 19.64 -1245 19 34 -12.35 1915 -1221 1894 -11.36 1874 -1007 18.58 16 2295 -1.03 -1 21 -1 38 -1 F4 d f, JK] T.,,. [K] T f ["CI 29115 2062 2 52 292 67' 17 61 22 54 2 02 295 69 14 13 24 18 297.33 1 66 11 53 298 71 25 56 9 63 :38 2674 8 21 1 18 299.89 27 77 1.04 300 92 7 26 1 00 301 92 28 // 6.98 29.71 6 F55 0 94 302 86 0 89 30 75 3060 6 23 31.45 0 86 304 60 601 32 29 0 83 305 44 5 84 33 11 0 82 306.26 5 73 0 89 307 15 34 00 6 25 35 10 1 10 308.25 7 70 3635 1.25 :309 0 8 73 3770 9 47 1 35 310.85 312 28 1001 39 13 1 43 6z 77 40 313 10 39 1 .48 41 82 1 21 314 97 8 46 42 62 0.79 :315 77 5.64 43 10 3 42 049 316.26 4337 1 88 0 2/1 316 52 4348 316 63 0 77, 4348 0 00 316 6:1 -0 0:3 43 08 -278 -0.40 316 21 4233 -527 -0.75 :315 48 41 32 -1.01 314 47 -706 -1.19 313 28 4013 -8 35 38.80 -1 32 311 95 -9 27 37 38 310 53 -994 -1.42 36.17 -849 -1 21 309 32 35 16 -1 01 308.31 -7.06 3430 -604 -086 307 45 33 F4 -0,76 306 69 -5 31 3286 -068 306,01 -4 78 305 38 3223 -440 -0 63 31 98 -065 34(73 -4.5S 3087 -071 304 02 -4 96 30 12 -075 303 27 -5.24 2934 -545 -078 302 49 28 54 -560 -080 301.69 27.73 -082 300 88 -571 2705 300 20 -4 7'6 -068 2656 -048 299 /1 2737 0.81 300 52 5.64 0 74 301 26 28.11 6 17 28 78 068 301 93 4 73 29 40 4 31 0 62 :302 ss 1r, 0ah [C] 18 51 18 71 18 89 19 oG6 (J,(1 ttle Q, 4 37 4.37 4 37 437 4 37 4 37 4 70 5 04 538 S71 605 6 33 6 31 6.27 622 6.16 6 11 6,0r 6 00 5 94 5 88 5 83 5 77 5 71 5,01 4 30 3.60 289 2.19 119 140 1 31 1.23 1.14 1 06 097 0,88 078 069 059 0.50 0,40 0.35 0 30 0 26 0 21 016 0 11 Qof dT.]KJ OTI 0 52 1649 12 1 5 -iI 9, 16.88 10 16 2 66 1721 8 67 7 57 -3 68 17 4 17 75 I6 78 -4 4 -499 17 06 6 20 5 80; -i604 18.19 -6 42 1839 5 29 491 -7.07 18 67 4 64 -7.63 18 74 -8 13 18.91 4 44 4 30 -857 190/ -7 93 19 22 " 28 4 -6 j 19 42 7 02 -548 1969 8.28 -4 79 20 00 9 18 -4 32 2035 9 83 -400 20 72 10 31 -5 28 21 12 8 50 5 CA -764 21.44 3,63 -934 21 65 S12 -10 57 21 79 1 03 -1144 21.87 0 24 -1206 21.91 -1299 21 91 -1 69 -13,96 21 84 -359 -1448 21.>9 -4.96 -1467 21 49 -5 95 -1462 21.26 -667 -1441 -21 00 -7 18 -1368 2073 -640 -12.77 2049 -! 46 -12.08 20.29 -4 78 -11 56 2011 -4,30 -11 15 1995 -3 95 -10 83 1980 -j 69 -1086 19 67 -3 92 -11 13 1952 -4 38 -11 29 1936 -4 71 -11 36 1919 -495 -11.38 19 01 -f" 12 - 11 35 18 8A -5 24 -10.62 1864 -4 35 -943 1849 -3 04 647 --096 18 43 -1 13 1862 !)08 -1 29 1880 4 71 - 1 45 1897 4 36 T,,, [K] T JoC] .J1 IS 1 74 291 891 1.45 1 24 1 08 0 97 0 89 0 83 294 34 0 76 0 70 0 66 300 10 0 63 0.61 0 75 1.00 118 302 295 58 296 66 297 63 298 51 299 34 300 80 301 46 302 10 71 19 74 21 19 22 4L 23 51 24 48 2 ) 36 2( 26 Tj 27 6* 28 11 28 9v 29 6 31 1, 32 ',0 1 21 1 40 1 47 309 84 36 69 311 05 311 87 312 38 303 93 30 7H 11141 31056 -0 95 -1 01 -0.91 -078 -0.68 -0.61 -056 309 60 308 58 :107.66 302 64 301.93 301.20 300 45 299 83 299 39 1.00. 18 300.90 301.27 :302.20i -OW 90 306 88 306.20 305.59 305 02 304 50 312 69 3 1? 84 312 87 312"63 -0,8t 0 53 3/ 38 70" 39 13 39 54 39.C,9 39 72 3948 3896 3826 37 41 36 45 35 43 34 51 33 73 3305 3244 31 8,1 31 35 -0.61 -0 71 -056 -0.63 0 67 -0 71 -0 73 -0.75 -062 -043 0 78 0 73 0 67 0 62 r PM lWli 46 304 47 305 65 306 96 30&37 0 81 0 52 0 301 0 15 0 03 -024 m 19 30 16 29 49 28 78 28 05 27.30 2668 26 24 27003 27 75 28 42 2905 ~C M 0CD B ga 0 0. 0 3D W/ Definition of terms Constant Inputs: dt = time step interval (hours] T, = initial water temperature [K] D = bottle diameter [m] x = bottle thickness [m] As, = 2r(D/2)L = total surface area of bottle cylinder [mi] 2 Ase = -(D/2) 2 = total surface area of bottle end [M ] A= D*L = cross sectional area of bottle [M 2] M mass of water [g] kr= thermal conductivity of plastic [W/mK] Measured Inputs: Ta = ambient air temperature at each time step [K] 2 R = net radiation measurements at surface for each time step [W/m ] U = wind speed at each time step [m/s] Calculated: Q_ amount of long-wave radiation going into th e system QL = EaTs (Ase+Asc) where a = Stefan-Boltzman constant (5.67-10-) T3 = ambient air temperature ,= amount of heat generated by radiation absorbed by bottle Q, = ERA, where Eis the percent of radiation absorbed by the system (clear = 80%, half painted = 90%, painted = 100%) 0, amount of heat lost by back radiation QU = EcOTs 4(Ase+Asc) where TSa OT = = a = Stefan-Boltzman constant (5.67-10-) surface temperature (calculated in attached spreadsheets) net heat flux into bottle Or = Q,+Q+QL ~ b dT = change in temperature for each time step for either painted or clear bottles) dT = (QT/CM)*dt Tn = final temperature for each time step (for either painted or clear bottles) T, = T, + dT 114 Painted bottles: conduction/convection Constants k, jW/mKj D Iml x[m) A. A = 02 0 08 x 0 0005 = 0 005 = 0,0528 - (thermal conduclivity (bottle diameter) (bOttle thickness) ul the plaslic) L mi -. 2 (rool imnension( caffiationi; (free fime sic T. 1 2 3 4 5 6 7 8 9 10 11 12 13 14 [K] 291.15 29360 29297 29449 294 51 295.57 295.91 296 64 296.88 297.46 29780 298 31 29870 300.09 15! 301.80 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 303.29 304 93 306.47 308.07 308 09 30770 307 58 307 28 307.09 30683 305 89 304.92 303.97 30301 302 06 301.10 300 75 300 34 299 97 299.57 299 19 29880 298 12 297.37 296 67 29593 29522 294 49 294.45 294,57 294.59 294.67 294.71 294.78 T, [K] Tt [K j 291 47 291 31 292.1 292 85 292 73 292,85 293 37 293 93 294 294 25 294 63 295.1 295 13 295 52 295.5 296 07 295 87 296.37 296 23 296.85 296 6 2972 2969/ 29764 291 94 298 32 299 53 299 81 301 11 301 45 302 69 302 99 30428 304.6 30586 306 16 306.4 307.31 306 33 307 21 306 11 306,9 305 89 306 73 30568 30648 30546 306 27 304.95 305 89 304 15 305.02 303 35 304.14 302 55 303.26 301 75 30238 300 95 301 5 300 37 300 73 300 300 37 299 63 299 99 299.27 299 62 2989 29924 298.53 298 86 298 298.4 297.3 297.71 2966 296 98 295.9 29628 295.2 29556 294.5 29486 294 18 294.33 294.25 29435 294.32 29444 294.38 294.48 294.45 294 56 294.52 294.61 14728 221 03 v [m'/s] a [(m'/sjk [W/M; 1E-05 1E-05 3E-05 0 0247 3E-05 0 0248 3E-05 0 0248 3E-05 0 0249 3E-05 0 0249 0,025 3E-05 3E-05 0 025 0 025 3E-05 3E-05 0 025 3E-05 00251 3E-05 0. 0251 3E-05 0.0251 3E-05 0 0252 3E-05 0 0253 3E-05 0 0254 3E-05 0 0255 3E-05 0.0256 3E-05 0.0257 3E-05 0 0258 3E-05 0,0258 3E-05 0.0258 3E-05 0 0258 3E-05 0 0258 3E-05 0 0257 3E-05 0 0257 3E-05 0.0257 3E-05 0.0256 1E-05 3E-05 9E-06 9E-06 9E-06 9E-06 9E-06 1 E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E.05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 0.0255 3E-05 00255 1E-05 3E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-05 1E-06 1E-05 1E-05 1E-05 3E-05 1E-05 3E-05 9E-06 9E-06 9E-06 9E-06 9E-06 3E-05 3E-05 9E-06 9E-06 2E-06 3E-05 3E-05 3E-05 3E-05 3E-05 3E-05 3E-05 3E-05 3E-05 0 0254 0.0254 0 0253 0 02 53 0. 0253 0.0252 0 0252 0 0252 00251 00251 0 025 0.025 0 0249 0 0249 0 0249 0 0249 0 0249 0 0249 0 0034 0.0034 0 0034 0 0034 0 0034 0 0034 0 0034 0 0034 0.0034 0 0033 0.0033 0 0033 0 0033 0 0033 0 0033 0.0033 0 0033 0 0033 0.0033 0 0033 00033 0 0033 0 0033 00033 0 0033 0 0033 0 0033 0.0033 0 0033 0.0033 0 0033 0,0033 0 0034 0.0034 0 0034 0.0034 0.0034 0.0034 0 0034 0.0034 0.0034 0 0034 0 0034 3E-05 3E-05 0.0249 0 0034 00198 0 0045 1E-05 3E-05 3E-05 3E-05 convection over end) lover cy (forced convechon over end) in1er) a Nu . T,.,, o, 10,,, 1 jU[m/s Ret i [K"} jPr Ra, jNu,. IT.,,. 10. INU,, 832345 199 1I 11066 0 0034 0.3231 21137 5 8649 291 15 0.0029 4 /419 291 15 0,0244 00301 1094 0 0034 0 325 96930 8319 293 59 -00 19 6 94 1 293 59 -0 17, -0 208 818521 198.27 1094 818529 198.:'7 0 0034 0.325 15009 5 4471 292 96 -0 002 4.372 292 96 -0 0 17 -0 02 1085 4 800123 197 4:3 -0.014 6 4132 294 49 -0 118 145 -0 48 0 0034 0.3263 70995 7 7331 294 0. 3267 0 :3277 0.3282 0.3289 0.3292 0 3298 0.3302 0.3307 03314 0:3331 0 3:43 0 3366 0 3383 0.3399 0 3411 0.341 0 3407 0 3405 0 3402 0 :34 0 3396 0 3387 03378 0 3369 0.3359 0 335 03341 0,3337 0 3333 0 3329 0 :3325 0 3321 03315 0.3308 0 3299 0 3291 0 3283 03274 0 3268 0,3268 0 3269 0 327 0.3271 0-3271 0.148 31841 57987 47590 68962 60907 72840 71041 78490 43988 31837 37513 '31628 33351 30262 74127 85644 77549 82340 78643 805J3 93443 87748 80774 74299 67114 60024 40451 41260 39390 39323 37998 37508 46085 48109 45551 46125 44485 44348 18949 12754 15914 12632 13787 11892 1E 408 6 4332 7.3806 7.0528 7.6885 7 4698 7 7905 7 7462 1 9315 6 9353 6 4487 6 6969 6.4475 6 5291 6 3916 7.8571 8.1293 7.9398 8 0525 7 9648 8 0089 8 2949 8.1691 8.0077 7.8488 7.6609 7.4612 6 8108 6.8413 6 7675 6 7638 6.7102 6 6894 7.01 7.0774 6.9869 7.0048 6.9446 6.9374 5.7341 5.2642 5 5209 5 2538 5. 3532 5 1869 48 763 294 51 295 57 29591 296.64 296 88 297 45 297.8 298.3 298 7 300 09 301.8 303 29 304 93 30647 308.06 308.08 307.69 307.56 307 27 307.08 306.82 305 88 30491 303 96 303 302.05 301.1 300.74 300 34 299.96 299 57 299 19 298 8 298 12 297.36 296 66 295 93 29521 294 48 294.45 294.57 294.58 294.67 294 71 290.46 -0 005 52481 294 51 -0011 6 0954 295 57 -0 009 5 8024 295.91 -0014 6 3732 296 64 -0.0 12 6. 1767 296.88 -0 015 6 4651 297 -5 -0 015 6 4253 297.8 -0.017 6 5922 298.3 -0 008 5 6974 298.7 -0.006 5 2624 300 09 -0 007 5 4843 301 8 -0.006 5 2616 303 29 -0007 5.3346 304 93 -0 006 52119 306.47 -0019 6.5261 308.07 -0 023 6 7713 308.08 -002 6 6005 307 69 -0 022 6.702 :307 57 -002 6 623 307 27 -0,021 6 6627 307.08 -0.025 6 9206 306 82 -0 023 6.807 3.05 88 -0.02 66614 :304 91 -0018 6 5182 303 96 -0015 6 3491 303.01 -0.013 6 1694 :302 os 301 1 -0 008 5.5861 -0 008 5 6134 300 74 -0.008 5 5473 300 34 5,544 299 96 -0 007 -0 007 5.496 299 57 -0 007 5 4774 299.19 -0.009 5 7643 298 8 -0 009 58246 298.12 -0 008 5.7435 297.37 -0 008 5 7594 296.66 -0 008 5. 7055 295 93 -0.006 5.699 29521 -0.003 4 626 294 48 -0 002 4.2098 294 45 -0 002 4 4369 294.57 -0 002 4 2006 294 59 -0 002 4 2885 29467 -0 002 4 1416 294 71 44 5 290 83 -8.674 -0 044 -0 054 -0 091 -0 116 -0 074 -0091 -0 12 0 103 -0 13 .() 12! U 14/ -0 127 -0 16 -0 157 806333 197 17 799125 196.51 795620 196 19 791081 195. 7 788593 195 54 784750 195 19 781876 194 92 *0 179 778:387 194 b9 -0 089 -0061 0078 -0 03 -0 065 -0 059 -0 072 -0 054 -0 067 -o 169 -0 208 -0 203 -0 249 -0 1/8 -0218 -0.191 -0 23f. 772962 761451 19408 .0 146 -0 072 -0 05 -0 0 -0 179 -0184 -0.22 -0.226 -022 -027 -0.199 -0 244 -0 176 -0216 -0 155 -0.191 -0 134 -0.165 -0 114 -014 -0 068 -0 084 -007 -0 086 -0 065 -008 -0 064 -0.079 -0 061 .0075 -0,06 -0,074 .0076 -0.094 -0 079 -0 098 -0 073 -0.09 -0 073 -0 089 -0.068 -0.084 -0067 -0 082 -0.023 -0 028 -0014 -0017 -0019 -0 023 -0014 -0017 -0016 -0019 0.013 -0016 -83 33 -100 7 749103 737917 726561 715870 708241 708897 710918 712052 713781 715128 717724 723683 729816 736001 742325 748734 754456 757176 760103 762925 765854 768747 772356 777796 783632 789335 795274 801197 805642 805495 804709 804364 803717 803279 4E+06 192 99 191 8 190 71 18959 188 52 187 75 18782 18802 188 14 18831 18845 18871 1893 18991 190 52 191 14 191.77 192 32 192.58 192 86 193 13 19341 193.68 194.02 19454 195.08 19561 196 16 196 7 197.11 197 1 197,02 196.99 196 93 196.89 309,66 (over cylinder) T . INu,. , Nu, T IQ,, Uu 291 3 0 2933 160 39 291.3 3 0792 3 6657 292 91 -14. 4 -17 31 292 91 -1 :384 -2.68 292 86 -0.2 14 1t9 41 292.86 1.035 158 74 293 98 -10 8b -12 93 293 98 -5 835 1082 8 294 28 -0467 158 53 294 28 -4 !Xj 10762 295 15 -0 864 15801 295.15 -9.068 -108 -7 5 -8.928 -0.714 1t7 76 295.56 1073 295.56 1 045 157 42 296, 12 -1098 -13.07 1068 8 296 12 10665 296.42 -0.928 V])7.24 296 42 -9 749 -11 61 -14 -1.12 156 96 296 9 -11 /6 10629 296.9 -1 099 1!J 74 297 25b -11 54 -1374 1060.2 297 26 -15 3 297 7 -12 83 1057 297 7 -1 224 1'6 48 -0 695 156 06 298 36 7 2q3 -8 681 1051 9 298.36 -6 453 1041.1 299 84 -0 516 15 21 299 54 1029 4 301 49 -0 626 154 26 301.49 -6 575 -76428 10188 :303.02 -0542 153 39 303 02 -5.695 -6 779 -7 35 1007 9 304 64 -0 588 152 5 304 64 -6 144 0 548 151 65 306 2 -5 754 -685 997.62 3062 990 23 307 39 -1 368 151 04 307 39 -14.37 -1711 990 87 307.31 -1 578 151.09 307 .31 -1. 57 -19'_1"1 -14 441 91 -1777 992 83 306 99 -1 422 151 25 306 99 .1: 993 92 :306 83 -1 505 151 34 306 83 -1, 81 -1882 15 03 -17 89 9956 306.56 -1 432 151 48 306 56 996.9 :306 36 -1 461 151 59 306.36 -15.34 -18.26 151 8 305 99 -17 68 -2 10f 999 41 305.99 -1 684 1005 1 30511 -1. 558 152 27 :05 11 -16.36 -1948 -1 413 152 76 :304 22 -14 BA -17 66 1011 304 22 -16 -1 28 153.25 303 33 -13 44 1017 303 33 -1 139 153.74 302 45 11 96 -14 2:3 1023 302 45 1029 1 301.56 -1.003 154 23 301 56 -10 53 -12 54 1034 5 300 77 -0.667 154.67 300 77 -7.00 1 -8 335 1037.1 300.41 -0 6/6 15488 30041 -7 099 -8.451 10:398 300 02 -0.641 155 11 300 02 -6 728 -8 009 10425 299 65 -0.635 155 32 2996) -6 672 -7 943 -0.61 155.54 299 27 -6 404 -7 624 1045,2 299 27 1047 9 298 89 -0 598 155 76 298 89 -6 279 -7 4751 1051.31 298.44 -0729 156 03 298 44 -7 652 -9 109 -7 89 -9 392 10564 297 75 -0751 156.44 297 75 1061.9 297.02 -0.702 15687 297 02 -7 372 -8 777 10672 296 32 -0 702 157,29 296 32 -7 371 -8 775 1072.7 295,6 -0 668 157. 73 295 6 -7 016 -8 352 10/8 1 294.89 -0 658 158.16 294.89 -6.904 -8219 1082 2 294 35 -0.278 15848 294 35 -2 921 -3.478 1082.1 294.36 -0 187 15847 294.36 -1,967 -2 342 1081.4 294 46 -0.2,34 15842 294 46 -2 409 -2 927 1081 294 49 -0 186 15839 294 49 -1 953 -2 325 10804 294.57 -0 203 15835 294 57 -2 13j -2 541 1080 294 62 -0.176 158.31 294 62 -1.843 -2.194 -1963 -23371 -187 247 43 201 78 2761 8 201 78 IT.. jor _ 291 22 3.6958 293 25 -17 51 292 91 -2 Z 294 23 -1:3 08 9439 -5 889 29536 .1091 -9 02 '295 73 296 38 -13 22 296 65 -11 73 '97 18 -14 16 297 53 -139 298 -15.48 298 53 -8771 299 96 -6 515 301 64 -7906 :303 16 -6845 :304 78 -7 423 30 33 -6916 30 7:3 -17 31 307 69 -1998 307 34 -17 99 307,2 -1905 306.91 -18 11 306 72 -1849 306 41 -21 32 305.49 -1972 304 57 -17.88 303 65 -16 19 -144 302 13 301 81 -12.68 300.94 -8,419 300.58 -8.537 -8.09 300 18 299.81 -8 023 299.42 -7.699 299 04 -7.549 298.62 -9203 297.94 -949 297 19 -8 866 296 49 -8 864 29576 -8.436 295 05 -8.301 294.42 -3.506 294.41 -2 359 294.51 -2.95 294 54 -2.342 294.62 -2.56 294 66 -221 246 21 -24381 Half-painted bottles: conduction/convection C onstants k, [WrriK = 0.2 D 1m] = 0.08 x(m] = 5E-04 A_ = 0.005 A=0 053 (thermal conductivity or the plastic) (bottle diameter) (bottle thickness) Calculat an5 (tree time step T [K] T. [KJ T4K] v [m/s a [ljts 1 291 15 291.5 291.3 9E-06 3E-05 2 293.67 292.1 292.9 9E-06 3E-05 3 29569 292.7 294.2 9E-06 3E-05 4 29733 293.4 295 3 1E-05 3E-05 294 296.4 1E-05 3E-05 5 298,71 6 29989 2946 2973 1E-05 3E-05 298 1E-05 3E-05 7 300.92 295. 1 8 301.92 295.5 298 7 1E-05 3E-05 1E-05 3E-05 299.4 9 30286 2959 300 1E-05 3E-05 10 303.75 296.2 11 304.60 2966 3006 1E-05 3E-05 297 301.2 1E-05 3E-05 12 30544 13 30626 297.9 3021 IE-05 3E-05 303.3 1E-05 3E-05 299.5 15 14 307 15 30825 301 1 304 7 1E-05 3E-05 16 309.50 3027 3061 1E-05 3E-05 17 310.85 304.3 307 6 1E-05 3E-05 18 31228 3059 3091 1E-05 3E-05 19 313.77 306 5 310.2 1E-05 3E-05 20 31497 3063 3106 1E-05 3E-05 21 31577 306.1 3109 1E-05 3E-05 22 31625 305.9 311 1 1E-05 3E-05 23 31652 3057 311 1 1E-05 3E-05 311 1E-05 3E-05 24 316 63 3055 305 3108 1E-05 3E-05 25 316 63 26 31623 304.2 310.2 1E-05 3E-05 27 315.48 3034 309.4 1E-05 3E-05 28 314.47 302.6 3085 1E-05 3E-05 29 313,28 301 8 307.5 1E-05 3E-05 301 3065 1E-05 3E-05 30 311 95 31 31053 300.4 3054 1E-05 3E-05 300 304 7 1E-05 3E-05 32 309 32 304 1E-05 3E-05 33 308.31 2996 34 30745 299.3 303.4 1E-05 3E-05 35 306.69 298,9 3028 1E-05 3E-05 36 306.01 2985 302,3 1E-05 3E-05 298 301 7 1E-05 3E-05 37 30538 301 1E-05 3E-05 38 304.73 2973 39 304.02 2966 3003 1E-05 3E-05 40 30327 2959 2996 1E-05 3E-05 41 302.49 295.2 2988 1E-05 3E-05 42 301.69 294.5 298.1 1E-05 3E-05 43 300.88 294.2 297.5 1E-05 3E-05 44 300.20 2943 2972 1E-05 3E-05 297 1E-05 3E-05 45 299.71 294 3 46 30052 294 4 297.5 1E-05 3E-05 47 301.26 2945 2979 1E-05 3E-05 48 301.93 2945 298.2 1E-05 3E-05 49 30255 147.3 2249 2E-06 1E-05 (Wirmli 0025 0.025 0 025 0025 0 025 0025 0.025 0.025 0025 0 025 0025 0.025 0025 0026 0.026 0.026 0026 0.026 0026 0,026 0026 0.026 0,026 0026 0026 0026 0.026 0.026 0.026 0026 0026 0.026 0.026 0.026 0.025 0025 0025 0.025 0,025 0.025 0.025 0025 0.025 0.025 0.025 0025 0.025 0.025 002 co i ection) 0,,1 Q.t T,,. Nu,, a,,. Nut. T~.. Ra [K'] Pr 0 01 0 003 0.323 2113/ 5.865 291 2 0003 4 742 291 2 0.024 -0.22 -0.179 293 7 -0.02 7.017 0003 0 325 1E+05 8 403 293.7 -0485 -0.396 295.7 8 224 -0045 2957 9,735 2E t05 0.327 0 003 0.003 0.328 2EA 5 10 42 2973 -0 064 8842 297 3 -0 574 0702 0003 0329 3E+05 1082 2987 -0079 9 21 2987 0711 -0 87 0:33 3E4OF 11 07 299,8 -0091 9 442 2998 -0.816 -0.998 0003 0 003 0331 3E #05 11 31 3009 -0. 1Oi 9655 300 9 -0 921 -1.126 0 003 0332 4E+05 11 57 301 9 -0 117 9895 301.9 -1 049 -1 282 0003 0333 4E+05 11 78 302,8 -0 13 1009 3028 -1 166 -1.425 0.003 0.333 4E+05 11 97 3037 -0.142 1026 3037 -1 276 -1 559 0.003 0.3:34 4E+05 12.13 304 5 -0 153 1041 304.5 -1 381 -1 688 0.003 0,335 5E+05 12.27 30F.4 -0.164 1054 305 4 -1 483 -1 811 0003 0.336 4E+05 12.16 306.2 -0 16 1044 3062 -1 445 -1.766 0003 0.33/ 4E+05 11 83 307 1 -0 143 10 14 307 1 -1.292 -1 578 0.003 0.338 4E+05 11 57 308.2 -0 132 9894 30872 -1 185 -1 449 0003 0.34 3E+05 11.36 3094 -0 124 9.702 309.4 -1 112 -1.36 0.003 0341 3E+05 11 19 310.8 -0.118 9 547 3108 -1 062 -1.298 0003 0 343 3E05 11.05 3122 -0 115 9.421 312 2 -1 027 -1 257 0.003 0344 3E+05 11.33 313.7 -0,132 9.675 3137 -1 19 -1 455 0.003 0344 4E+05 11.83 3149 -0 166 1013 314 9 -1.494 -1 825 0003 0 345 4E+05 12.15 315 7 -019 10.43 3157 -1 71/ -2.098 0003 0345 5E05 12.36 316.2 -0.208 10 2 316 2 -1.877 -2.293 -1 99 -2.43 -0.22 10 75 3164 0.003 0.345 5E+05 12 51 3164 126 3165 -0 228 1084 316.5 -2 066 -2.523 0 003 0:345 5E+05 -267 0003 0345 5E+05 1276 316,5 -0242 10.99 3165 -2 187 0003 0.344 6E+05 1291 316 1 -0.252 11.12 3161 +2.285 -2.79 -23 -2808 0.003 0343 6E+05 1296 315.4 -0 254 11 17 3154 0.003 0.342 6E+05 1296 314.3 -0249 11 17 3144 -2254 -27b1 164 -2.642 2 313.2 11 12 12.9 3132 -0239 0003 0.341 6E+05 034 5E+05 12.81 311 8 -0.226 11.03 311 9 -2044 -2495 0.003 0.003 0.339 5E+05 12.61 3104 -0 205 1085 3104 -1852 -2 282 0.003 0 338 5Ei05 12,38 3092 -0 184 1063 309.2 -1662 -2029 0.003 0,338 4E+05 12.19 3082 -0168 1046 3082 -1.52 -1 856 0,003 0.337 4E+05 12.04 3074 -0.157 10.33 3074 -1.412 -1 725 0003 0.336 4E+05 11 92 306 6 -0 147 10 22 306,61 -1328 -1 623 0003 0336 4E+05 11.83 3059 -014 10 13 3059 -1262 -1.542 0003 0 335 4E+05 11 82 305.3 -0138 10.12 305.3 -1 243 -1.519 0.003 0 334 4E+05 11.88 304.7 -0139 1018 304.7 -1 255 -1.534 304 -1.255 -1.534 0.003 0.334 4E+05 11.91 3039 -0 139 10.21 0003 0333 4E+05 11.93 3032 -0.138 1023 3032 -1 246 -1 523 4 -1232 -1 505 302 1023 -0137 3024 11.94 4E+05 0332 0003 0003 0.331 4E+05 11.94 301 6 -0 134 1023 301 6 -1.212 -1.481 0003 0331 4E+05 11.76 300.8 -0123 1006 3008 -1 108 -1 354 033 4E+05 11 43 300.1 -0,106 9.764 3002 -0954 .1 167 0,003 0.33 3E+05 11 16 299.7 -0.094 9 522 2997 -0844 -1 033 0.003 11.5 300.5 -0.11 9.835 3005 -0.993 -1213 0.33 4E+05 0.003 10 1 301 2 -1.131 -1 383 -0.126 0.003 0331 4E+05 11 79 301. -0.14 10.31 301 9 -1.26 -1 54 0.003 0.331 4E+05 1203 301.9 -104 0004 0 166 9E+07 47 18 298 1 -8,961 4303 2985 -8603 (forced rOnvectiont O., 01c T.. Nu,. Of. Nu,.. T.. Nu,. U [m/s Re 0 3 80 33294 39.9 84.26 291 2 0 039 31 34 291.2 0408 0486 380 32729 3965 83.28 293 6 -0 191 31. 15 293.6 -2.005 -2 387 31 2955 -3 7.8 -4474 380 32269 3944 82 48 295 5 -0 358 81 8 297 1 -0478 3087 297 1 -5024 -5981 3.80 31883 39.27 3,80 31550 39 11 81.22 2984 -0.566 3075 2984 -5 94 -7,071 807 2996 -0629 3065 299.6 -6 604 -7862 3.80 31256 38 97 -864 0 26 300 6 -0,691 3057 3006 -7257 dO 3 80 31011 38 8 380 30797 3876 7988 301.5 -0764 30.49 301 5 -8026 -9 555 3.80 30595 3866 79.52 3024 -083 3042 302 4 -8714 -1037 380 :10403 3857 79.18 303 3 -089 30 15 3033 -9344 -11 12 -11 82 380 30218 3848 7884 304.1 -0.946 30129 304 1 -9 93 38 4 7852 304 9 -0999 30 22 3049 -1049 -1249 380 30039 380 29775 38 2 ? 7804 3058 -0977 30 13 305 8 -1026 -12.21 30 306 7 -9365 -11 15 3 80 29418 3809 774 3067 -0892 3.80 29041 37,91 76,71 307.8 -0.831 29 86 307 8 -8728 -1039 309 1 -8 274 -9 851 2972 -0788 309 1 76 37.71 28654 380 3,80 28262 37.52 75.28 310 .5 -0 757 29.57 310.5 -7953 -9468 380 27872 37.32 74,55 311 9 -0 736 29.42 311 9 -7 72 -9 198 380 27598 3717 74 04 3134 -0.824 2931 313.4 -8657 -1031 3.80 27474 37 11 73.81 3145 -0 986 2927 314.5 -1 3 -122 3.80 2/403 3707 73 68 3152 -1 099 29.24 315 2 -11 54 -13.74 380 27389 3706 73 62 3157 -1 179 2922 315 7 -12 38 -1474 736 315.9 -1.234 29 22 315 9 -12.96 -1543 380 27363 37.05 316 -13 35 -159 316 -1 272 29.23 3.80 27176 3706 7363 316 -13 97 -16.63 316 -1,33 29 25 3.80 2/439 3709 7375 3 80 27588 37.17 7403 3155 1 379 2931 315.5 -14.48 .1724 3.80 27784 37.27 74.39 3148 -1.388 2939 314.8 -145/ -17.35 3.80 28016 3739 74.82 3138 -1368 2947 '113.8 -14.37 -171 -166 753 312.6 -1 328 2957 3126 -13.94 3.80 28275 3752 -159 3.80 28558 37.67 75.82 311 3 -1.272 2968 311 3 -13 3 37.8 76.32 309.9 -1 18 29 78 309 9 -12.39 -14 75 380 28829 3 80 29046 3791 7672 3088 -1 085 2986 308 8 -11 39 -13.56 o80 29239 3801 77.07 307.8 -1.012 29.93 3078 -1063 -1266 307 -10 05 -11 96 30 307 -0957 3,80 29413 38,09 7739 380 29574 38 17 7768 3062 -0913 3005 306.2 -9.584 -11.41 3 80 29725 3824 7795 305 6 -0877 3011 305.6 -9,213 1097 30 17 304.9 -9 116 -10,85 380 29895 3833 7826 3049 -0.868 380 30095 3842 7862 3043 -0.876 3024 3043 -9201 -10.95 3032 3036 -9.216 -1097 83/ -0 303.6 79 51 38 30306 3.80 304 3028 -9 18 -10 93 79.4 3028 -0874 380 30527 38 63 380 30755 3874 7981 :302 1 -0.867 3048 302.1 -9.108 -1084 3.80 30990 38 85 80 2:1 301 3 -0 858 30.56 301 3 -901 -1073 -10 -08 3062 300.5 -8404 380 31170 38 93 80 55 300.5 380 31268 3898 80.72 299.8 -0712 30.66 299.8 -7478 -8.902 0 0 0.3 299.7 0 0 299 7 0 0 0.00 0 0 03 300. 0 0 3005 0 0 0.00 0 0 03 301 3 0 0 301 3 0 0 0.00 0 0 03 101 9 0 0 301 9 0 0 0 00 0 0 5 302 0,3 0 3025 0 0 0 000 T.... 291 2 2936 2956 2972 298 5 299.7 3007 301 7 302 6 1035 2043 3052 306 306 9 308 3093 310.6 312 1 3135 314 7 3154 315 9 3162 316 1 3162 3158 315 1 3141 3129 311 6 3102 309 308 3072 3064 305 8 305 1 304.5 3038 303 302.2 301 4 3006 300 299 7 300 3012 301.9 300-4 Q14 05t1 -2 606 -4 959 -6 683 -7 941 -8 859 -9 766 -10.84 -11 8 -12 68 - 1 14 3 -1398 -12 /3 11 84 -10 77 -10 45 -1 76 -14 14 -15.84 17.03 -1786 -18 42 -19J -20 0+ -201I -19.8t -19 24 -184 -1701 -15 59 -14 51 -13 68 -130 -12 51 -12 37 -12.49 -12 5 -12 45 -12 35 -1221 -11 :36 -1007 1 033 -1 .313 .1.383 -1.54 -104 Clear bottles: conduction/convection Constants (thermal conduCtIvy of the plastic) k, [W/tK} = 0.2 (bottle diameter) D [ml = 0.08 0 0005 (bottle thickness) xn] 0.005 A, A_ 0.0528 Calculations I Nu, OTa IRao Q_ jNuge T.-,h lQt, IsI F [WIm I [K-] Pr T. [KI T. [K] T,[K] I[m is a 291.15 291.47 291 31 9E-06 3E-05 0 0247 0 0034 0.3231 21137 5 8649 291 15 00029 4 7439 291 15 0 0244 0 030 29289 292 1 292.49 9E-06 3E-05 0.0248 0 0034 0 3246 5115S 7 1609 292.88 -0009 5 899 292 88 -0 075 -0 0931 29434 292.73 29354 9E-06 3E-05 0.0248 0 0034 0.3258 102148 8.4264 294 33 -0021 7.038 294 33 -0184 -0226 29558 29337 294,47 9E-06 3E-05 0.0249 0 0034 0 327 137927 90611 295 56 -0031 7 6121 295 56 -0 275 -0.337 294 29533 1E-05 3E-05 0.025 0 0(134 0.328 162991 9 4402 296 64 -0 039 7 9558 296.64 -0 346 -0.424 296.66 297.63 294.63 29613 1 E-05 3E-05 0.025 0 0034 0.3289 180515 9 6826 297.6 -0 045 8.1759 29761 0 402 -0 492 29851 295 1:3 296.82 1E-05 3E-05 0.0251 0. 0034 0 3297 20092C 9 9439 298.49 -0 053 84133 298 49 0 467 -C 572 299 34 295.5 297.42 1E-05 3E-05 0.0251 0 0034 0.3304 225637 10 236 299 31 -0.062 8 6787 299 32 -0 549 -0 672 30010 29587 297.98 1E-05 3E-05 0 0252 0 0034 0.3311 24562E 10.45G5 300.06 -0 069 8 8794 300 07 -0619 -0 '84 1063 300 76 -0.076 9 0379 300 7/ -0681 -0 833 300 8029623 29852 1E-05 3E-05 0.0252 0 0033 0 3317 262214 301.46 296.6 29903 1E-05 3E-05 0.0252 0 0033 0.3322 276332 10772 301 42 -0082 9 1678 301 43 -0737 -0 901 30210 296.97 29953 1E-05 3E-05 0.0253 0 0033 0 3328 288645 10 897 302.05 -0 088 9 2778 302 061 -0 787 -0 9G3 302 71 297.94 300.33 1E-05 3E-05 0,0253 0 0033 0.333/ 264125 10 658 302.67 -008 9 06:J9 302681 0717 -087/ ' -0 688 0 335 2131921 10 1 12 303 43 -0 063 8 5669 03 44 -0 52 14 30346 299.53 301,49 1 E-05 3E-05 0 0254 0 0033 15 30447 301.11 302.79 1E-05 3E-05 0 0255 0 0033 0 3364 177248 96687 304.44 -0.052 8 1641 30445 -0458 -0 562 0 389 -0.477 8456 305.63' 7 -0044 16 30565 30269 304.17 1E-05 3E-05 0.0256 0 0033 0.3378 151941 9 3174 305 63 17 306 96 304.28 305.62 1E-05 3E-05 0.0257 0. 0033 0 3394 134175 9.046 306 94 -0.039 7 5998 306.95 -0 344 -0422 18 30837 30586 307.11 1 E-05 3E-05 0.0258 0 0033 0 3409 12174E 8 8415 308 35 -0036 7 .4148 308 35 031fi -0 38F, 19 309.84 306.54 308.19 1E-05 3E-05 0.0259 0 0032 0 342116846 9.4051 309 81 -0 05 7 9255 309 82 -0 443 -0543 20 311 05 30633 30869 1E-05 3E-05 0.0259 0 0032 0.3425 222827 10254 311.01 -0078 8 6969 311 02 -0 698 -0 855 -0.1 9 1528 311 82 0 895 -1 09') 21 311.87 30611 308.99 1E-05 3E-05 0 0259 0.0032 0 3428, 26980S 10 755 311.82 22 312.38 30589 309.14 1E-05 3E-05 0 0259 0.0032 0 34291303377 11 075 312 33 -0116 94454 312 33 ..1 041 -1 274 -0.128 9.641 312.63 -1 148 -1 404 23 31269 305,68 309 18 1E-05 3E-05 0 0259 0.0032 0 34291327411 11.29 312.62 24 31284 30546 309.15 1E-05 3E-05 00259 0.0032 0 3429 344638 11 436 312.77 -0 136 9 7748 312 78 -1 224 -1 497 -1 .4 -1.6)8 25 31287 304.95 30891 1E-05 3E-05 0 0259 0.0032 0.3427 371634 11 655 312.8 -0 149 9 9746 312.81 26 312.63 304.15 308.39 1E-05 3E-05 0.0259 0 0032 0 3422 40173C 11 884 312 55 -0 162 10.184 312 56 1 403 .1 78/ 27 31211 30335 307.73 1E-05 3E-05 0 0258 0.0032 0.3415 420490S 12.02 312 03 -0.169 10 308 312 04 .1 528 -1 866 -1.535 -1 894 28 311.41 302.55 30698 1E-05 KE-05 0.0258 0 0033 0.3407 430981 12 091 311 32 -0. 172 10.374 311 33 29 310.56 301.75 306 15 1E-05 3E-05 0 0257 0.0033 0 3399 435318 12 118 310.47 -0 171 10398 31048 -1 5411 - 86'1 - 1 r1 -1 845 309 51 10 392 -0 167 52 12 111 309 30 309 60 300.95 305.28 1E-05 3E-05 0 0257 0.0033 0.339 435035 31 308,58 300.37 304.47 1E-05 3E-05 0.0256 0.0033 0.3382 419256 11.994 308.5 -0157 10,284 30b 51 -1 415 -1 729 300 303.83 1 E-05 3E-05 0 0256 0 0033 0. 3375 396196 11.82 307.59 -0144 10 125 307.6 .1.298 1 587 32 307.66 33 306.88 299.63 30326 1E-05 3E-05 0 0255 0.0033 0 3369 379034 11 685 306.82 -0135 10 002 306 83 -1212 -1 481 34 30620 29927 302.73 1 E-05 3E-05 0 0255 0.0033 0 3363 36621 C 11.581 306.14 -0.127 9 9065 306. 15 -1.146 -1 401 35 305.59 298.9 302.24 1E-05 3E-05 0.0255 0.0033 0 3358 356563 11 501 305 53 -0122 98331 305 53 -1 096 -1 339 36 305.02 298.53 301.78 1E-05 3E-05 0 0254 0 0033 0. 3353 349236 11.438 30496 -0118 9 7759 304.97 -1 056 -1 291 298 301.25 1E-05 3E-05 0.0254 0.0033 0 3347 353228 11 469 30444 -0 118 9 8033 30444 -1058 -1 294 37 304.50 38 303.93 297.3 30062 1E-05 3E-05 0.0253 0 0033 0 334 365348 11 563 303 87 -0121 9.8897 303 88 -1.089 -1 :311 1 105 -1 351 39 303.31 296.6 29995 1E-05 3E-05 0 0253 0.0033 0.3333 37435 11.631 303.25 -0 123 9 9515 303 26 -1 136 40 302 64 295 9 299 27 1E-05 3E-05 0 0252 0.0033 0 3325 381076 11.68 302 57 -0 124 9.9959 :302 58 -1 113 -1.36 41 301.93 295.2 298.56 1E-05 3E-05 0 0252 0. 0033 0.3317 386135 11.715 301.87 -0124 10028 301 88 -1.113 42 301.20 294.5 297.85 1E-05 3E-05 0.0251 0.0034 0.3309 389971 11.74 301 14 -0 123 10.051 301 15 -1108 -1 354 43 300.45 294 18 297.32 1E-05 3E-05 00251 0 0034 0 3303 368807 11.573 300 39 -0.113 9.8978 300 4 -1 02 -1.246 0.33 330167 11.253 299.78 -0 098 9 6057 299.79 -088 -1 077 44 299.83 294,25 297.04 1E-05 3E-05 0 0251 0 0034 11 299.35 -0087 9 3747 299 36 -0 782 -0.956 45 299.39 294.32 296.86 1E-05 3E-05 00251 0 0034 0.3298 301650 46 300.18 294.38 297.28 1E-05 3E-05 00251 0 0034 0 3303 341179 11.347 300 12 -0.103 96921 300 13 -0 923. -1129 47 300.90 294.45 297.68 1E-05 3E-05 00251 0 0034 0.33071 376959 11.639 300.84 -0.118 9.9513 300 85 -1.057 -1 292 48 301.57 294.52 298.05 1E-05 3E-05 0.0252 0 0034 033111 409302 11.886 301.51 -0.131 10 184 301 52 -1 184 -1.44/ 002 00044 0 1655 9E+07 47244 297.75 -8947 43 092 298 13 -85 91 -103.8 49 30220 14728 224.74 2E-06 1E-05 time st 1 2 3 4 5 6 7 8 9 10 11 12 13 U IT. JQT1 T, 01, INu,, Q,, Nu,, 1JT,.,. 80' 332941 39901 84 263 291 17 0 0389131.337 291 17 0.4081 0 48 5 29284 008 31.197 -1 3180 32867 39712 83 525 292 84 -0 0961 3 80 32501 39,547 82 887 294.24 -0 195 31 075 294 24 -2 048 -2 43E 3 80 32179 39401 82 325 29544 -0 268 :0 967 29544 -2681 -3 345 -4.01 -:3368 296.5 .0 321 iC) 869 196 3 80 31890 39268 81 816 -4 !, -378 -036 '30 779 291 45 3 80 31624 39 146 8 1 349 297.45 3 80 31398 39 041 80 948 298 31 -0 40t) 31 701 29d 31 -4 256 -06C 827 74 11 -4 '99 46 634 -0 30 3 80 31205 38 961 80.607 299. 11 3 80 31026 38 867 8029 299 85 -0 505 30 72 299 85 - 5 303 79 99 300 53 -0 3)44 30 513 300 '3 - 5 /1 3 80 30858 38 788 -6 066i 3 80 30698 38 712 79.704 301 1 / -0578 30 457 301 1-/ :3 80 30543 38.638 79 428 301 79 -0 60 30 403 30t 79 -6:34 -7 60~i 3 80 30301 38523 78 994 302 4:1 -0564 30 J17 302 43 -5 923 -7 051 3 80 29952 38 354 78.365 301 23 -0 464 30 19' 3W3 23 -4 871 -5 799 29575 38.171 77 683 304 27 -01 394 30 055 3(42/ -4 134 -4 921 380 2918 37 978 76 969 305 48 0.345 29 912 30548 -3622 -4 312 3 80 28783 37 778 76 237 306811 0 312 '9763 30681 -3 272 -3 895 .580 28381 37 576 75 498 308 22 -0289 29613 308 '2 -3 0:18 -' 617 3.80 28099 37 432 74.975 309 65 -0 379 29 505 309 65 -3 9791 -4 77 380 27970 37 366 74 735 :00 78 -0 542 29456 '10 78 -5 6961 -678 -066 2942/ 311 54 -6 928 -8 248 3 80 27893 37.327 74.593 311 54 380 27855 37.3071 74 522 31201 0 74.1 29412 312 01 -7808 .9 296 380 27844 37 301 74.501 312.29 -0 803 29408 312 29 -8 43:3 -1004 3 80 27852 37.3061 74 518 31241 -0845 29.411 312 41 -8.871 -10 56 7913 37:i37 74 63 312 42 -0.908 'N 4'3' 312 42 -9 532 .11 35 380 0 974 29 486 312 14 -10 22 -12 17 -8047 37.406- 74 8/9 ,312 14 3 80 3 80 28218 37 49N4 75 196 311 61 -1 009 29.551 311 61 -10 59 -1261 28417 37 594 /5 564 310.9 - 1 022 29626 3109 -10.73 -1) 78 3 80 380 28638 37706 75 97 310 05 -1 019 29.709 310 05 -107 -12 74 12 "it) 3.80 28876 7 825 76 408 309 1 -1.005 29.798 309 1 -10.55 308 1 -0 956 29881 308 1 -10 04 - 11 95 3.80 29099 37936 76815 3.80 29278 38025 77 142 30722 -0 895 29947 307.22 -9 394 -11 18 -10 6 3.80 29441 38 10', Y7 438 306.46 -0 848 30 006 306.46 -8 906 .0e 13 30061 3058 -8 534 -10 16 380 29591 38 179 77 712 :305.8 380 29733 38.248 77 969 3015 2 -0 7bl, 30 113 305.2 -8 244 -9815 380 29869 38314 78215 304 64 -0 763 30 162 30464 -8015 -9 542 380 30025 38 39 78497 304.11 -0766 30218 30411 -8.039 -957 3.80 30214 38481 78.836 303 54 -0784 :30.286 303.54 -8231 -9 799 3,80 30414 38.577 79.196 30291 -0 795 30,357 30291 -8 '344 -9 934 -10 -08 30.431 302 24 -8 401 3.80 30624 38 677 79 573 302 24 30843 38.78 19 963 301.53 -0801 30508 301.53 -8415 -10.02 3.80 -10 -8.4 -0 8 30 5W7 300 8 31068 38 887 80 365 300 8 380 31238 38966 80 666 300.08 -075 30.646 300 08 -7875 -9 376 380 31328 39 008 80.825 299 5 -0.668 30677 299.5 - 7 018 -8 355 0 0 0 0 3 299 39 0 299 39 0 0 0 0 0 3 30018 0 0 300 18 01 0 000 00 0 0 0 0 300.9 0 3 1) 300 9 01 C' 0 00 0 00 0 0 0 3 301 57 0 301 57 0 0 0 0 00 0.3 302.21 01 0 302. 2 01 0 01 1m/s1 3 294.28 129:1 2 661 "96 5/ 3 682 -4 434 292 86 297 3 P931 4 ,199 "1 0418 299 9t, / , 300 6 301,. -8 / 125 301192 -8 5 1 7 928 33 -6 48/ 304 3O ' 48' 305 5; -4 789 303 88 4 117 308 29 -4 '109 73 :310 9 7 6,36 311 6 9 343 312 17 10 17 :312 461 - 11 -4 312 59 -12 06 31261 - 12 99 :112 35 -1395S 1448 :111 82 :111 II -14 67 310 26 -14 62 309 31 -1441 308 3 -113 68 307 41 -1; 77 :306 64 -12 08 305 9/ -11 56 :305 :36 -11 :304 81 - 10 8:3 304 28 1086 303.71 303 08 302 41 I 1 36 301 7 11 38 30. 97 -I11 35 300 24 -10 62 299 64 -9 4 32 299.31 - 0 956 -129 :300 15 300 87 301 54 1 447 300 071 103 8, 306 m U El -- Definition of terrms T! average of water ai and temperatures V (T. T = (T.-T,2 where T. is the water temperature at and TA!s ma average a;r teriperatura 1E-07x - 2E-05 y Ott ar viscosity dependart on ten-perature v 300 2E-05 350 2E-05 400 3E-05 450 3E-05 (15-7)T. - 2E -5 0 V t - air thermal dffusivity dependant on temperai (misl T, 30C 2E-05 350 3E-05 400 4--05 450 SE-CS ic= (2E-7)T, - 3E-5 4 000 500 thermal conductivity (dependant on emper_ TK [W'mK7 30 0 0263 350 003 0038 4 45C 00373 (7E-5)T,+ 0043 volume expansion coefficient s~ ~- - - y= 2E 07 - 3E-05 000003 0 OC'2 tO 0 = air 200 _ 200 o300 OW 500 400 500 (Tr) 0 04 y 003 7E-05x + 0.0043 - 02 0 0 tCC 20 300 Pr = Prandtl number Pr = V" Fa, = Rayteigh number where g Is acceleration due to gravity and D ;s the characrerstic length of the geometry (bottle diameter) = Nusselt number for free onvection over ine end of tne bottle Nu,, 825 Nu, =, Q17C N1. Nu, = Nusseit number for Nu = 6 + CL 492; P0)) free convection over the cyinder 17 559zPr +(0.W "] l~ Re 0 = Reynold's number Reo = (UD)/v where U is the average wind speed over the Nu. = Nusselt nuter for forced convection Nu,= 03387R&"'Pra (1 +-(0 0468&Pr)n " time step rrvsl end Nusseft numDer for forced convection over the cylinder Nu = t .3 + 062Re PrO 1 45 [1+(0. 4/Pr) 820 Nu, = T, surface temperature T, =atuKTJl,(s'L-)j L L = over the } Sa+Ny,, x 0 L rate of heat transfer 0= (T.-TAkh x where A, is the total surface area (of end or cylinder) kq is the thermal conductivity of the plastic and x is the thickness of the bottle = average T,. Or = surface temperature total rate of heat transfer (sum of forcedifree convection over ends cylinder) Or= 0. +0 Source for Pr, Re. Ra. and Nu: Incropera, F.P. and D.P DeWitt 1996 Fundamentals of Heat and Mass Transfer. Fourth Edition. John Wtey & Sons, New York, NY 118 -~ -~ -~--. plots of model v. real data for data collected in Barasa Painted Model Time Actual 295.91 293.9 0 298.70 302.8 1 308.07 308.6 2 306.83 310.9 31 301.10 308.9 4 298.80 305.2 5 294 49 301.7 6 294.78 298 7 1diffStDevl 2.01 -4.10 -0.53 -4.07 -7.80 -6.40 -7.21 -3.22 Painted Bottle Water Temperature (K) 1 3 0 3 6 5 2 3 Clear StDev1 diff1 IModel Time Actual 4 5.91 298.51 292.61 0 3 4.41 302.71 298.3 1 6 8.04 309.84 301.8 2 7 9.27 312.87 303.6 3 4 5.08 308.58 303 5 4 2 3.10 304.50 301.4 5 1 1.65 300.45 298,8 6 4 6.20 302 20 296 71 4 Half StDev1 diff1 Model Time Actual 4 6.12 300.92 294.8 0 2 2.46 306.26 303.8 1 3 4.57 313.77 2 309.2 4 5.63 316.63 311 3 0.53 0 310 310.53 4 1 -0 92 306.3 305.38 5 1 -1 52 300.88 302.4 6 7 298.4 302.55 4.15 31 1 2 0 Actal - 32(, 310 E _ 290 6 4 2 0 Time (hour) Clear Bottle Water Temperature (K) - 330 - S 320 -- - -- 310 Actua Model - 4) 300 0. - E 290 - 280 . ----- 270 0 2 4 Time (hours) 8 6 Half Painted Bottle Water Temperature (K) 330 --- dtua - .320 Mdei 3 10 C 3CC S 290 280 270 0 4 6 8 Time (hours) 119