Energy and the New Reality, Volume 2: C-Free Energy Supply Chapter 4: Biomass Energy L. D. Danny Harvey harvey@geog.utoronto.ca Publisher: Earthscan, UK Homepage: www.earthscan.co.uk/?tabid=101808 This material is intended for use in lectures, presentations and as handouts to students, and is provided in Powerpoint format so as to allow customization for the individual needs of course instructors. Permission of the author and publisher is required for any other usage. Please see www.earthscan.co.uk for contact details. From the Summary For Policymakers of the WG1 Report for the IPCC 5th Assessment Report Table of agreements and disagreements among bioenergy experts Agreements Disagreements Improving the efficiency of traditional uses of bioenergy has both climate and socioeconomic benefits The impact of net social livelihoods of large-scale bioenergy deployment for the global poor is disputed The use of waste and residues, in many cases, can help reducing GHG emissions The fraction of residues that can be sustainably removed is disputed When bioenergy can be used to improve unproductive, or even toxic, marginal lands, this aids the reduction of GHG emissions and does not interfere with food production The area (amount) of land that is marginal, and not informally supporting livelihoods or being biodiversity rich, is not well known Life-cycle analysis of bioenergy needs to include net emissions from soil, processing, direct and indirect effects of land use (change) as well as biophysical factors, such as albedo. The boundaries of analysis are disputed (e.g. inclusion of market-mediated effects, consideration of time frames, climate forcing factors, counterfactuals, etc.) Table of agreements and disagreements (continued) Agreements Disagreements The large-scale use of grain-based and oil-seed food crops for bioenergy production has at best low mitigation effects and may cause net warming, in addition to interfering possibly harmfully with food production and increasing environmental harm from agrochemical use. The full life-cycle impacts of most bioenergy production systems are disputed, including those of energy crops The total resource potential for bioenergy is approximately 100-900 EJ per year in 2050. The maximum sustainable potential for bioenergy is disputed, with some researchers estimating it to be only around 160-270 EJ per year in 2050. Global use of different energy sources for residential and commercial buildings in 2010 35 Residential buildings Commercial buildings Global Energy Use in 2010 (EJ) 30 25 20 15 10 5 0 Electricity Fossil fuels District heat Source: International Energy Agency, Energy Balances Reports for 2010 Biofuels Figure 4.1 Uses of biomass for energy in 2007. Overall contribution: about 10% of total primary energy supply. Source: Sims (2010, in Industrial Crops and Uses, CABI, Wallingford, UK) Figure 4.2a Trends in biomass use by type, with uncertainty bars for the total Biofuel Consumption (Mt/yr) 4000 Industrial Biofuels Domestic Charcoal Domestic Dung Domestic Crops Domestic Fuelwood 3000 2000 1000 0 1900 1925 1950 Year 1975 2000 Figure 4.2b Trends in biomass use by region 3000 North America Latin America Western Europe Eastern Europe/FSU Africa Biofuel Consumption (Mt/yr) 2500 2000 1500 South Asia East Asia 1000 Southeast Asia Oceania 500 0 1900 1925 1950 Year 1975 2000 Advantages of biomass: • • • • • Can be stored Provides rural income & employment Potentially cleaner than coal for most pollutants Can be irrigated and fertilized with sewage water Can be cultivated in such a way as to improve the landscape and remediate soils • Can make use of animal wastes and agricultural residues while providing an effective fertilizer byproduct Disadvantages of biomass energy • Land intensive (efficiency of photosynthesis is ~ 1%, with further losses when biomass is converted to secondary forms of energy) • Can compete with land for food • Complex to initiate and manage • Must be tailored to the biophysical and socioeconomic circumstances of each region Comparison with fossil fuels • Heating value ranges from 14 GJ/t (sugar cane, straw) to 18-20 GJ/t (air-dried wood), compared to 28-31 GJ/t for coal • This makes biomass bulky and more expensive to transport (in both dollar and energy terms) than coal Table 4.3: Biomass energy resource categories Source: Hoogwijk (2003, Biomass and Energy, 25, 119-133) Bioenergy Crops • Annuals • Perennial grasses • Woody Crops (trees) Annuals • Starch-rich crops (maize (corn), wheat, potatoes) (used to produce ethanol) • Sugar-rich crops (sugarcane, sugar beets) (used to produce ethanol) • Oil-rich crops (coconut oil, palm oil, sunflower oil) (used to produce biodiesel) Figure 4.3a Sugarcane (a sugar-rich crop) Source: www.wikipedia.org Figure 4.3b Sugarcane harvesting Source: www.wikipedia.org Figure 4.3c Cut sugarcane stalks Source: www.wikipedia.org Figure 4.4 Palm oil (and oil-rich crop) Sources: Left, Photo by Jeff McNeely in Howarth and Bringezu (2009, Biofuels: Environmental Consequences and Interactions with Changing Land Use, SCOPE); upper right, Stone (2007, Science, vol 317, pp149 ); lower right, Koh and Wilcove (2007, Nature, vol 448, pp993–994) Perennial grasses • Switchgrass (Panicum virgatum)(native to North America) • Miscanthus (native to tropical Africa and tropical and temperate Asia) • Napier grass (native to tropical Africa) • Jatropha curcas (a poisonous weed native to Central America, used in India) Figure 4.5 Switchgrass (Panicum virgatum) Source: US Gov public domain Figure 4.6 Miscanthus sinensus (upper) & Napier grass (Pennisetum pupureum) (lower) Source: www.wikipedia.org Figure 4.7 Close-up of Jatropha (left), and degraded land before (upper right) and after being planted with Jatropha (lower right) in India Source: Left, photo by Jeff McNeely in Howarth and Bringezu (2009, Biofuels: Environmental Consequences and Interactions with Changing Land Use, SCOPE); right, Fairless (2007, Nature, vol 449, pp652–655) Woody crops • Short-rotation coppicing - Willow (Salix) - Poplar (Populus) • Modified conventional forestry - Acacia (N-fixing) - Pine (Pinus) - Eucalyptus Figure 4.8 Harvest of coppice willow and irrigation of new growth with sewage water in Sweden. Source: Dimitriou and Aronsson (2003, Unasylva 56, 221, 47-50) Figure 4.9a Five-year old Acacia plantation Source: Doug Maquire, Oregon State University, www.forestryimages.org Figure 4.9b Eucalyptus plantation in Spain (left) and 4-year old Eucalyptus in Hawaii (right). Source: NREL Photo Exchange, www.nrel.gov/data/pix) Figure 4.9c 14-year old loblolly pine (Pinus taeda) in Georgia, USA Source: Dennis Haugen, www.forestryimages.org Yields of bioenergy crops • Annuals - Sunflower 1.5 t/ha/yr - Maize: 4 t/ha/yr - Sugarcane, sugar beet: 60 t/ha/yr • Grasses - Jatropha: 10-15 t/ha/yr - Miscanthus 10-15 t/ha/yr - Switchgrass 10-25 t/ha/yr - Napier grass 30 t/ha/yr • Trees - Loblolly pine: 4-5 t/ha/yr - Poplar, willow: 10-20 t/ha/yr - Eucalyptus: 10-50 t/ha/yr Agricultural Residues • A variety of residues (stalks, shells, husks, leaves) from a wide variety of crops (such as coconut, maize, cotton, groundnuts, pulses, rice, sugarcane) are produced and used for household energy use in rural areas of developing countries already • Straw is co-fired with coal in Denmark • Bagasse is a fibrous residue produced during the processing of sugarcane into sugar Figure 4.10 Bagasse, a residue from processing of sugarcane Source: Warren Gretz and DOE/NREL Source: Kartha and Larson (2000, Bioenergy Primer, Modernized Biomass Energy for Sustainable Development, United Nations Development Programme, New York) Forestry residues • Primary (left in the field): From thinning of plantations and trimming of felled trees • Secondary (produced during processing): Sawdust, bark, wood scraps from production of marketable wood; bark and black liquor from the production of pulp for paper Processes of extracting energy from biomass • Direct combustion • Pyrolysis (heat to 300-500ºC in near absence of air) • Thermo-chemical gasification (initial pyrolysis, then heating to 800ºC under pressure) • Anaerobic digestion • Fermentation of non-woody biomass • Hydrolysis & fermentation of woody biomass • Transesterification of vegetable oils • Gasification and catalytic production of Fischer-Tropsch liquids • Gasification to produce hydrogen Direct combustion • Cooking with firewood in developing countries, typical cook-stove efficiency is 10-20%, 30-60% with improved stoves (vs. 45-60% with gaseous fuels) • Pellet heating, central Europe in particular • District heating in Sweden, Atlantic Canada • Issues include ash content (which is related to the non-combustible silica in the biomass, which can be high) and K and Ca in the fuel, which can cause agglomeration in boilers Figure 4.11 Traditional wood-burning stove (upper), improved wood-burning stove (middle), and charcoal-burning stove (lower) in Kenya Source: Bailis et al (2003, Environmental Science & Technology 37, 2051–2059) Figure 4.12 A wood-burning hearth in China and its replacement with a biogas-fueled stove Source: Kartha and Larson (2000, Bioenergy Primer, Modernized Biomass Energy for Sustainable Development, United Nations Development Programme, New York) 80 80 70 70 60 60 50 50 40 40 Stove Efficiency 30 30 20 20 Stove Capital Cost 10 10 0 Stove Capital Cost ($) Stove Efficiency (%) Figure 4.13 Cookstove efficiency and cost 0 Increasing Affluence Source: Kammen et al (2001, Policy Discussion Paper for the United Nations Development Program, Environmentally Sustainable Development Group (ESDG) and the Climate Change Clean Development Mechanism (CDM)) Figure 4.14 Biomass pellets (left) and pneumatic delivery by truck (right) Figure 4.15 Pellet-burning stove (left) and furnace (right) Source: www.harmonstoves.com Figure 4.16 Fuel sources for Swedish district heating 70 Heat Produced (TWh/yr) 60 50 Waste Heat Heat Pumps Electric Boilers Biofuels Coal Natural Gas Oil 40 30 20 10 0 1980 1985 1990 1995 Year Source: Swedish Energy Agency (2008, Energy in Sweden 2008, www.stem.se) 2000 2005 Thermo-chemical gasification • Step one: Heat biomass to a temperature of 300-500°C in the near absence of air to drive off the easily vaporized or volatile materials a process called pyrolysis • Step two: heat the remaining residue (char) to 850-900°C in the presence of steam • Step one produces a mixture of CO, H2, CH4, and CO2 (the first 3 of which have energy value) • The gases contain about 2/3 of the energy content of the fuel, which is lost if they are not captured (as is the case in the production of charcoal). If captured, the gases can be used for heating, cooking, generation of electricity, or for cogeneration of useful heat and electricity. • Conversely, the gases can be shifted to consist almost entirely of H2, or can be used to synthesize methanol, dimethyl ether, or Fischer-Tropsch liquids (all of which are potential transportation fuels) • There were no large-scale commercial thermo-chemical gasificationof-biomass facilities anywhere as of early 2006 Figure 4.17a Proportion of original coal and cellulose remaining as solid residues as they are heated in the absence of air (pyrolysis) Fraction of weight remaining 1 0.9 0.8 Coal 0.7 0.6 0.5 0.4 Cellulose 0.3 0.2 0.1 100 300 500 700 900 Temperature (oC) Source: Larson (1993, Annual Review of Energy and Environment 18, 567–630) Gasification rate (percent per minute) Figure 4.17b Rate at which the solid residues (char) from pyrolysis are converted to gas in the presence of steam 40 Poplar 30 Willow 20 Pine 10 Coal 0 500 600 700 800 900 1000 Temperature oC Source: Larson (1993, Annual Review of Energy and Environment 18, 567–630) Figure 4.18 Updraft fixed-bed gasifier (left) and downdraft fixed-bed gasifier (right). Source: Kartha and Larson (2000, Bioenergy Primer, Modernized Biomass Energy for Sustainable Development, United Nations Development Programme, New York) Biological gasification (anaerobic digestion) • Occurs in sanitary landfills (in which waste including organic matter alternates with clay layers, creating anaerobic conditions and temporarily trapping any methane produced from anaerobic decomposition) • The methane is extracted with perforated pipes • The efficiency (heating value of extracted methane over heating value of the organic waste is only ~ 20%) • Can be done with greater efficiency (50-55%) in dedicated digesters Figure 4.19 Collection of biogas from a municipal landfill Source: Ramage and Scurlock (1996, Renewable Energy, Power for a Sustainable Future, Oxford University Press, Oxford, 137-182) Figure 4.20 Dedicated anaerobic digestion of organic solid waste with recovery of biogas, low- & high-temperature heat, and digestate as fertilizer 0.085 t of rejects for dumping Gas treatment 0.040 t ferrous metals 1 t refuse 62.5% dry matter 50% organic matter biogas 125 m3 biogas Preparation Methanization 0.875 t crushed material Refining digestate 0.156 t combustible rejects Combustion Recovery of low-temp heat kWh low-temperature heat kWh high-temperature heat Source: Ramage and Scurlock (1996, Renewable Energy, Power for a Sustainable Future, Oxford University Press, Oxford, 137-182) Anaerobic digestion of animal and sewage wastes • 5 million household cattle-dung digesters in China, 500 large-scale digesters at pig farms and other agro-industrial sites, and 24,000 digesters at sewage treatment plants • 20 million households in China use biogas from digesters for cooking and lighting needs, and 4 million households in India • 5000 digesters in industrialized countries, primarily at livestock processing facilities and municipal sewage treatment plants Figure 4.21 Cattle dung digester in India Source: Kartha and Larson (2000, Bioenergy Primer, Modernized Biomass Energy for Sustainable Development, United Nations Development Programme, New York) Figure 4.22 Digester on a pig farm in England Source: Unknown Figure 4.23a Indian digester design Source: Kartha and Larson (2000, Bioenergy Primer, Modernized Biomass Energy for Sustainable Development, United Nations Development Programme, New York) Figure 4.23b Chinese digester design Source: Kartha and Larson (2000, Bioenergy Primer, Modernized Biomass Energy for Sustainable Development, United Nations Development Programme, New York) Anaerobic digestion of animal wastes in Denmark • 20 centralized plants and 35 farm-scale plants, making it one of the leading industrialized countries in the world • The residue is an effective fertilizer • Yet, these plants process only 3% of the manure produced in Denmark • Processing of 50% of the available manure would allow the complete elimination of oil for heating and of coal for electricity generation Production of ethanol by fermentation of non-woody biomass • Fermentation requires an input rich in sugars • Sugarcane is rich in sucrose sugar (a combination of glucose and fructose) • Potatoes, corn, and wheat contain starch, which consists of long chains of glucose molecules • Initial processing is required to break starch into its constituent sugars before fermentation can occur – this occurs as either wet milling (the grains with starch are soaked in water) or dry milling (the grains are simply ground down) • New facilities are based on dry milling Production of ethanol by hydrolysis and fermentation of woody biomass • Woody biomass is called lignocellulosic biomass • It is a mixture of cellulose (35-50%), hemicellulose (20-35%), and lignin (12-20%) • Cellulose consists of long chains of glucose sugars (it is a polysaccharide) • Hemi-cellulose consists of short, highly branched chains of sugars, mainly xylose (a 5carbon sugar) but also arabinose (5-C), galactose, glucose, and mannose (all 6-C) • Lignin is a resistant heterogeneous substance Table 4.8 Typical composition of different ligno-cellulosic biomass materials, with the sugars composing cellulose and hemi-cellulose and their identification as 5-carbon (5C) or 6-carbon (6C) sugars. Cellulose Glucan (6C) Hemicellulose Xylan (5C) Arabinan (5C) Galactan (6C) Mannan (6C) Lignin Ash Acids Extractives Heating value (GJHHV/tonnedry) Hardwoods EucaHybrid lyptus poplar 49.5 44.7 13.1 10.7 0.3 0.8 1.3 27.7 1.3 4.2 4.3 19.5 18.6 14.6 0.8 1.0 2.2 26.4 1.7 1.5 7.1 19.6 Softwood Pine Corn stover 44.56 37.4 Grass Switchgrass 32.0 21.9 6.3 1.6 2.6 11.4 27.7 0.3 2.7 2.9 19.6 27.5 21.1 2.9 1.9 1.6 18.0 5.8 3.2 8.1 14.9 25.1 21.1 2.8 1.0 0.3 18.1 6.0 1.2 17.5 18.6 Source: Hamelinck et al (2005, Biomass and Bioenergy 28, 384-410), except for corn stover, which is from Sheehan et al (2004, Journal of Industrial Ecology 7, 117–146) Steps in making ethanol from woody biomass • Pretreatment (grinding, following by chemical, physical, or biological removal of lignin) • Breakdown of cellulose – addition of water (hydrolysis) in a weak or strong acid, followed by breakdown with enzymes that are produced by organisms living on about 2% of the material • Fermentation – ethanol is readily produced from 6carbon sugars, but no naturally-occurring organisms convert 5-carbon sugars to ethanol • Concentration of ethanol through distillation Figure 4.24 Integrated production of ethanol, heat and electricity from lignocellulosic biomass Source: Wyman (1999, Annual Review of Energy and the Environment 24, 189–226) Biodiesel from vegetable oils • Vegetable oils almost always contain triacylglycerols (a glycerol with three fatty acid esters) • Transesterification is the process of heating a mixture of 80-90% oil and 10-20% alcohol (typically methanol or ethanol) in the presence of a catalyst • The products are methyl or ethyl esters and glycerin (C3H8O3) • The methyl or ethyl esters can be burned in a diesel engine (unlike the original vegetable oils), while glycerin is used in the cosmetics, ink, lubrication and preservatives industries and is an ingredient in soap Biodiesel (continued) • The major exporters of vegetable oils are Malaysia, Indonesia, Philippines, Brazil and Argentina, with palm oil the dominant crop from these countries used for biodiesel • Biodiesel in Europe is largely made from rapeseed oil, while biodiesel in the US is largely made from soybeans Production of Biodiesel from oily algae • The idea is to grow algae in ponds in the desert (with water transported in, or waste or brackish water used) to make biodiesel • Water requirements per litre of biodiesel would be less than from traditional oilseed crops • CO2 from nearby powerplants could be captured, fed to the algae and sequestered by the algae (by becoming part of the algal mass) Biodiesel from algae (continued) • The cancelled US Aquatic Species Program had concluded that yields of 142,000 litres/ha/yr (4650 GJ/ha/yr) were possible – compared to only 6000 litres/ha/yr from palm oil in Malaysia • A more recent privately-funded assessment concluded that yields of about 100,000 litres/ha/yr could be achieved • This requires a two stage process: first, growing the algae to high mass with a projected photosynthetic efficiency of 5%, then stressing the algae to induce conversion of 35% of the algae mass to oil with continued growth at a projected photosynthetic conversion efficiency of 20%, the latter having been obtained only for short periods of time (typical photosynthesis efficiencies for plants are ~ 1% or less) Biodiesel from algae (continued) • There seem to be lots of potential practical programs that could render the idea uneconomic • Nevertheless, ExxonMobile announced in 2009 that it will spend up to $600 million over 5-6 years developing the technology (with the funding level dependent on results), and other private companies are also working in this technology Table 4.9 Average and maximum measured yields from a microalgae bioreactor-pond system. Projected yields are speculative. Dry biomass (t/ha/yr) Energy in biomass (GJ/ha/yr) Energy in oil (GJ/ha/yr) Measured Average Maximum 38 92 763 1836 422 1014 Projected 200 4100 3200 Source: Huntley and Redalje (2007, Mitigation and Adaptation Strategies for Global Change 12, 573–608) Fischer-Tropsch liquids • Fischer-Tropsch synthesis converts solid hydrocarbons or natural gas into liquids • Biomass is gasified under high temperature and pressure to produce CO and H2 (this differs from the first step in thermo-chemical gasification, discussed earlier, which is carried out in the near-absence of air) • The gases are then sent to a reaction chamber, where catalysts are used to produce chains of various lengths • F-T diesel is cleaner-burning than regular diesel • Overall biomass-to-fuel conversion efficiency of 4652% is expected Fischer-Tropsch liquids (continued) • The process is more expensive using biomass than coal (break-even oil prices of $70-80/barrel and $5055/barrel, respectively, are required) • It can make use of plant material that has too much lignin for production of ligno-cellulosic ethanol • There are still problems related to impurities and fouling of equipment that need to be solved, and there is room for better process integration • Overall, this is a promising method for large-scale production of biofuels from a wide range of biomass sources Solar-driven biomass gasification • In conventional thermo-chemical gasification or F-T synthesis, some of the biomass energy is combusted to produce heat that drives the reactions, and only a portion of the C atoms end up as part of the product gases or liquid fuels • Use of high-temperature heat from solar thermal towers would allow essentially all of the biomass to be converted to fuel, reducing the biomass and land requirements by a factor of 3 (with ethanol yields of ~ 42,000 litres per ha of biomass plantation per yr) • As solar thermal energy can be stored, the production facility would operate 24 hours per day • Biomass would be produced in the regions with highest productivity, then transported by ship or train to semi-arid regions where concentrating solar thermal energy is viable Production of Hydrogen • Hydrogen is one of several fuels that can be produced by thermo-chemical gasification of biomass, but is worth highlighting here because it can also be produced by electrolysis of water using solar- or wind-generated electricity • The overall conversion efficiency from sunlight to biomass will be very small compared to using solar PV – the efficiency of photosynthesis (~ 1%) times the efficiency in conversion from biomass to hydrogen (5060%, or 0.5-0.6) • Thus, if H2 will be the transportation fuel in the future, it makes little sense to make it from biomass • Biomass is interesting as a potential energy source for fuels (such as ethanol or biodiesel) only if H2 turns out not to be viable as a transportation fuel, or to the extent that fuels other than hydrogen are needed (most likely, there will be applications where H2 is best and applications where carbon biofuels are best) Figure 4.25 Biofuel Overview H yd ro g e n (H 2) W a te r g a s sh ift + se p a ra tio n G a sifica tio n DME (C H 3O C H 3 ) S yn g a s C a ta lyse d syn th e sis L ig n o ce llu lo sic b io m a ss A n a e ro b ic d ig e stio n M e th a n o l (C H 3 O H ) F T D ie se l (C xH y) B io g a s P u rifica tio n SNG (C H 4 ) B io o il H yd ro tre a tin g a n d re fin in g B io d ie se l (C xH y) S ugar F e rm e n ta tio n E th a n o l (C H 3 C H 2 O H ) E ste rifica tio n B io d ie se l (a lkyl e ste rs) F la sh p yro lysis H yd ro th e rm a l liq u e fa ctio n H yd ro lysis S u g a r/sta rch cro p s O il p la n ts M illin g a n d h yd ro lysis P re ssin g o r E xtra ctio n Ve g e ta b le o il B io o il (ve g e ta b le o il) Source: Hamelink and Faaij (2006, Energy Policy 34, 3268–3283, http://www.sciencedirect.com/science/journal/03014215 Current production of biofuels, trends and yields Table 4.10 Comparison of biofuel yields (litres per hectare per year) US EU Ethanol from Agricultural Crops Sugar cane Sugar beet 5500 Corn 3100 Wheat 2500 Barley 1100 Ethanol from ligno-cellulosic biomass Corn stover 1100-2200 Miscanthus 7300 Switchgrass 3100-7600 Poplar 3700-6000 Biodiesel from oily plants Palm oil Rapeseed 1200 Sunflower seed 1000 Soybean 500 700 Jatropha Brazil India 6500-7000 5300 Malaysia 6000 700 From the above • Biodiesel from palm oil is the only interesting alternative for biodiesel among those currently available (although biodiesel from algae might give many times the yield) • Ethanol from sugarcane is the best choice, with ethanol from sugarbeets a close second and ethanol from ligno-cellulosic crops perhaps matching yields using sugarcane • However, production of sugarbeets requires more energy inputs than production of sugarcane, while the overall energy balance of lignocellulosic ethanol will be less favorable than that of sugarcane ethanol Figure 4.26a Ethanol production in 2008 France 2% Other 4% China 3% US 51% Brazil 40% Ethanol Production in 2008 Total = 67 billion litres Figure 4.26b Biodiesel production in 2008 Germany 18% Other 23% Italy 3% US 17% Spain 3% Thailand 3% Argentina 10% France 13% Brazil 10% Biodiesel Production in 2008 Total = 12 billion litres Figure 4.27 World biofuels production, 1975-2008 Production (billions litres/yr) 70 60 50 40 Ethanol 30 20 10 0 1975 Biodiesel 1980 1985 1990 1995 Year 2000 2005 2010 Generation of Electricity from Biomass • Co-firing of solid biomass with coal, using steam turbines • Biogas in place of diesel in small (5-100 kW) internal combustion engines • Integrated gasification/combined cycle (BIGCC) • Co-firing of biogas with natural gas • Integrated gasification/fuel cell • Cogeneration in the sugarcane and palm oil industries • Cogeneration in the pulp and paper industry The conventional way to generate electricity from biomass is to burn the biomass to generate steam, then use the steam in a steam turbine. Efficiency is low (typically 2030%) Advanced techniques (still under development) involve thermal gasification of the biomass and use of the gases either in gas/steam turbine combined cycle powerplant or in fuel cells. Waste heat from the steam turbine or fuel cell would provide at least part of the heat required for gasification. Expected overall efficiencies in generating electricity are in the 40-50% range. Recap from Book 1 Chapter 3 (Fig. 3.3): Generation of electricity from a conventional, pulverized-coal powerplant Generator steam High-Pressure Boiler electricity out fossil fuel in Steam Turbine air (O 2) to cooling tower or cold river water CO2 water condensate and/or cogeneration CO2 up the stack sequestered CO2 out Condensor Pump Source: Hoffert et al (2002, Science 298, 981-987) cooling water return flow Recap from Volume 1 Chapter 3 (Fig. 3.6a): Simple-cycle gas turbine and electric generator EXHAUST FUEL COMBUSTOR GAS TURBINE (a) ELECTRICITY GENERATOR COMPRESSOR TURBINE INTAKE AIR Source: Williams (1989, Electricity: Efficient End-Use and New Generation Technologies and Their Planning Implications, Lund University Press) Recap from Volume 1 Chapter 3 (Fig. 3.6c): Combined-cyclepower generation using natural gas COOLING TOWER CONDENSER EXHAUST ELECTRICITY STEAM TURBINE WATER PUMP STEAM FUEL HEAT RECOVERY STEAM GENERATOR (c) GAS TURBINE ELECTRICITY GENERATOR COMPRESSOR TURBINE Source: Williams (1989, Electricity: Efficient End-Use and New Generation Technologies and Their Planning Implications, Lund University Press) Table 4.13 Comparison of a typical natural gas and biogas composition (mole %) and heating value. CH4 Other HC CO2 CO H2 O H2 N2 LHV (MJ/kg) Natural Gas 87.6 10.9 1.2 0.3 47.62 Source: Marbe et al (2004, Energy 29, 1117–1137) Biogas 5.0 12.0 16.0 12.0 11.0 44.0 4.4 Figure 4.28 Flow chart for BIGCC (biomass integrated gasification combined cycle) Exhaust Heat recovery steam generator Steam cycle Electricity Make-up water Generator Gas cooling Biomass Boost compressor Extraction air Pump Gas cleaning Gasifier Intake air Combustor Gas turbine Compressor Electricity Turbine Generator Source: Larson (1993, Annual Review of Energy and Environment 18, 567–630) Table 4.14 Comparison of electrical and total efficiencies (LHV basis) for various cogeneration systems using biomass. BICGG=biogas integration combined cycle. Technology Power (MWe) Steam Atm BIGCC Press BIGCC Biofuel bioler 2-26 6-77 8-104 Electric Efficiency Industry District Heat 0.17 0.27 0.33 0.38 0.38 0.43 Source: Marbe et al (2004, Energy 29, 1117–1137) Total efficiency Industry District Heat 0.87 1.10 0.71 0.76 0.72 0.90 0.87 0.90 Power:Heat Ratio Industry District Heat 0.24 0.33 0.87 1.00 1.12 0.91 Recap from Volume 1 Chapter 3 (Fig. 3.8): Fuel Cell Fuel (H2) Air (Mostly N2 + O2 ) DC Power Eelectron flow Negative ions OR Oxidized Fuel (H2O) CATHODE ELECTROLYTE Fuel distribution plate ANODE Positive ions Nitrogen Sugarcane industry • Sugar refineries require both heat and electricity, and have access to substantial amounts of biomass residue • Today this residue is used to produce on average 30 kWh of electricity per tonne, but the potential is 180-230 kWh/t with biomass gasification/combined cycle • The potential is at least 500 kWh/t if residues on the field, which are currently largely burned off in Brazil, are also used Palm oil industry • Currently produces 25-40 kWh per tonne of fresh fruit bunch that is processed, using a backpressure steam turbine • Could produce 75-160 kWh/t with alternative steam turbines, presumably close to 200 kWh/t with gasification/combined cycle Figure 4.29 Electricity from Sugar Cane Gasifier with STIG and Steam Conservation Biomass integrated gasifierwith combined cycle (BIGCC) CEST with Steam Conservation Condensing Extraction Steam Turbine (CEST) Typical existing factory 0 50 100 150 200 250 kWh of electricity output per ton of cane processed Source: Modified from Kammen et al (2001, Clean Energy for Development and Economic Growth: Biomass and Other Renewable Energy Options to Meet Energy Development Needs in Poor Nations, Policy Discussion Paper) Environmental Issues • • • • Soil fertility and productivity Water use Use of fertilizers, herbicides, and pesticides Atmospheric and water pollutant emissions (biomass production, processing, and end use) • Genetically-modified organisms Environmental Issues (continued) • • • • • • • Removal of heavy metals from soils Utilization of ash and separation of heavy metals Opportunities to treat municipal waste Impact on erosion Impact on biodiversity Indoor air pollution Employment and rural poverty Emissions associated with production and use of ethanol • Burning of sugarcane fields (still occurs) • Greater risk of corrosion of tanks with ethanolgasoline mixtures, increased solubility of petroleum contaminants • No clear benefit compared to gasoline in terms of tailpipe emissions Figure 4.30 Smoke plumes from sugarcane plantations in Brazil that are burned prior to manual harvesting Source: Howarth and Bringezu (2009, Biofuels: Environmental Consequences and Interactions with Changing Land Use), photo by Edmar Mazzi Emissions and spills associated with production and use of biodiesel • Biodiesel is biodegradable and non-toxic, unlike diesel • Biodiesel speeds the rate of degradation of diesel in blends • Lower tailpipe emissions of CO and hydrocarbons, with most of the benefit at 50% biodiesel in biodiesel-diesel blends and a significant increase in NOx emissions only at greater than 50% biodiesel Emissions associated with combustion for heat and/or power • Depend on element ratios in the fuel • Depend on total fuel requirements • Depend on conversion technologies used Figure 4.31 Dry matter to coal element ratios Plant Matter:Coal Concentration Ratio 10 1 0.1 0.01 0.001 B N Na Mg Al P S Cl K Ca Ti V Cr Mn Fe Co Ni Cu Zn As Se Mo Ag Cd Sn SbSmHg Pb Electric resistance, BIGCC Electric resistance, NGCC Pellet boiler Wood boiler Oil boiler Natural gas boiler Heat pump, BIGCC Heat pump, NGCC Primary Energy Used (MJ/MJheat) Figure 4.32a Primary energy used per unit of delivered heat in different home heating systems in Sweden 3.0 2.5 2.0 1.5 1.0 0.5 0.0 Total Hydrocarbons (g/MJ heat) Figure 4.32b Hydrocarbon emissions for different home heating systems in Sweden 500 400 300 200 100 0 Figure 4.32c SOx emissions from different home heating systems in Sweden SOx (g SO2/MJheat) 300 250 200 150 100 50 0 Figure 4.32d NOx emission from different home heating systems in Sweden 900 800 NOx (g NO2/MJheat) 700 600 500 400 300 200 100 0 BIGCC vs Coal for Electricity Generation Table 4.16 Comparison of pollutant emissions (gm/kWh) and CO2 emissions (gmC/kWh) associated with BIGCC using short-rotation willow fuel, and associated with coal powerplants. SO2 NOx Dust CO HC CO2 Crop Production 0.024 0.267 0.029 0.267 0.057 5.85 Willow-BIGCC Crop PowerTransport plant 0.001 0.071 0.006 0.214 0.000 0.029 0.006 0.290 0.002 0.55 Total 0.096 0.487 0.057 0.563 0.059 6.40 Source: Faaij et al (1998, Biomass and Bioenergy 14,125–147, http://www.sciencedirect.com/science/journal/09619534) Coal Powerplant Pulverized IGCC Coal 0.38 0.2 90.3 0.64 0.05 0.07 222 217 Removal of heavy metals from soil and separation from flue gas • Soils in polluted areas tend to have high concentrations of heavy metals, which are absorbed by the plants • Heavy metal concentrations are higher in wood chips and bark than in straw or cereals • Ash can be separated into 4 different fractions, and most of the heavy metals end up in a small fraction of the total ash • The majority of plant nutrients occur in the ash fractions that have minimal concentrations of heavy metals, so these ash fractions can be returned to the soil Figure 4.33 Distribution of wastewater for the irrigation and fertilization of a willow plantation in Sweden Source: P. Aronsson Figure 4.34 Sewage treatment plant (foreground), aeration pond (middle ground), and willow plantation at Enkoping, Sweden Source: Photograph by P. Aronsson in Dimitriou and Aronsson (2003, Unasylva 56, 221, 47-50) Impacts on biodiversity • Positive is short-rotation forestry and grasses replace agricultural crops • Negative if large-scale clearing of tropical forests for soybeans of palm oil, or clearing of the cerrado for sugarcane or soybeans, occurs Figure 4.35 The Brazilian cerrado, potential land for soybean and sugarcane cultivation and home to > 900 species of birds and 300 species of mammals, many threatened with extinction Source: (C) by Luiz Claudio Marigo/naturepl.com Global Warming Impact and Pollutant Emissions of Wood- and Charcoal-based stoves Table 4.18 Emissions (gmC per kg of fuel) associated with different technologies for using biomass for heating, and Cequivalent (in terms of global warming) of non-CO2 emissions (CO, CH4, and NMHCs) Figure 4.36a Ratio of ceramic-stove-to-wood-stove or charcoal-basedto-wood-stove CO2 emissions as computed by various researchers 2.0 CO2 Emission Ratio 1.6 1.2 0.8 0.4 0.0 Ballis Smith Ballis Brocard Smith IPCC Figure 4.36b Ratio of ceramic-stove-to-wood-stove or charcoal-based-to-wood-stove CO emissions 5.0 CO Emission Ratio 4.0 3.0 2.0 1.0 0.0 Ballis Smith Ballis Brocard Smith IPCC Figure 4.36c Ratio of ceramic-stove-to-wood-stove or charcoal-based-to-wood-stove CH4 emissions 6.0 CH4 Emission Ratio 5.0 4.0 3.0 2.0 1.0 0.0 Ballis Smith Ballis Brocard Smith IPCC Figure 4.36d Ratio of ceramic-stove-to-wood-stove or charcoal-based-to-wood-stove NMHC emissions 2.5 NMHC Emission Ratio 2.0 1.5 1.0 0.5 0.0 Ballis Smith Ballis Brocard Smith IPCC Figure 4.36e Ratio of ceramic-stove-to-wood-stove or charcoal-based-to-wood-stove TSP emissions 6.0 TSP Emission Ratio 5.0 4.0 3.0 2.0 1.0 0.0 Ballis Smith Ceramic/Wood Ballis Brocard Smith Charcoal/Wood IPCC Global warming impact of biomass for cooking compared to natural gas • Combustion of solid biomass in various kinds of stove emits CO and NMHCs (which produce ozone), and CH4 and N2O (which are GHGs) • The global warming effect of these emissions (excluding CO2, which is a valid exclusion if the biomass is produced sustainably) is several times that of the CO2 released from the combustion of natural gas, as seen in the next figure Figure 4.37 Efficiency of different cooking fuel/technology combinations, and ratio of total CO2-equivalent GHG emissions to that using natural gas 0.8 0.7 16.0 Efficiency 14.0 Ratio to Gas including CO2 12.0 0.5 10.0 0.4 8.0 0.3 6.0 0.2 4.0 0.1 2.0 0 0.0 GWP Ratio Ratio to Gas excluding CO2 Gas LPG Kerosene Kerosene Eucal-imet Eucal-ivm Eucal-ivc Eucal-3R Acacia-tm Acacia-imet Acacia-ivm Acacia-ivc Acacia-3R Root-tm Root-imet Root-ivm Must-tm Must-imet Must-ivm Must-ivc Rice-tm Rice-ivm Dung-tm Dung-ivm Dung-ivc Dung-Hara Efficiency 0.6 Net Energy Yield Producing and Using Biomass • Biofuels (ethanol, biodiesel) • Solid biomass • Biogas Net Energy Yield of Biofuels • • • • • • Ethanol from corn (kernels) Ethanol from sugarcane Ethanol from woody biomass Ethanol from corn stover Ethanol from sugarcane residue Biodiesel from vegetable oils Figure 4.38 Biofuels and coproducts from corn and soybeans A g r ic u ltu r a l p r o d u c ts B io r e fin e r y P r o d u c ts E t hanol C orn grain W et m illing U se Liquid f uel C orn oil C orn glut en m eal C orn glut en f eed E dible oil If a p p lic a b le A nim al f eed C orn s t ov er C orn s t ov er proc es s E t hanol E lec t ric it y E x port t o pow er grid S oy bean m illing S oy bean m eal S urf ac t ant S oy beans B iodies el B iodies el proc es s S oaps t oc k G ly c erine Source: Kim and Dale (2005b, Biomass and Bioenergy 29, 426–439, http://www.sciencedirect.com/science/journal/09619534) S olv ent Energy Inputs to be considered during the production of biofuel feedstocks • Energy to make fertilizers, herbicides, and pesticides • Energy to produce seeds • Energy for irrigation • Energy used by farm machinery (for soil preparation, seeding, harvesting) • Energy used to make the farm machinery • Energy for drying prior to transportation Energy used during the processing of feedstocks into biofuels • Transportation of workers • Transportation of biomass inputs and of solid wastes • Energy used to manufacture the processing facility • Energy used by the processing facility • Energy used to supply and treat water The key parameter of interest is the Energy Return Over Energy Invested (EROEI) This is the ratio of the energy value of the biofuel and any co-products produced from the biomass, to the total energy input. It should be substantially > 1 if producing the biofuel is to be worthwhile Table 4.19 (upper part) Annual energy inputs used to produce corn or ligno-cellulosic crops, as estimated in different studies, and EROEI up to the point where crop leaves the farm. Results are for a moist corn yield of 8.7 t/ha/yr or a woody crop yield of 13.5 t/ha/yr. Energy required to produce the woody crop is less than half that required to produce the corn crop, so the EROEI for the woody crop is much larger Fertilizer embodied energy (GJ/ha/yr) Herbicide + Insecticide energy (GJ/ha/yr) Direct energy use (GJ/ha/yr) Other energy inputs (GJ/ha/yr) Total energy to produce corn (GJ/ha/yr) Crop yield (kg moist crop/ha/yr) Crop energy yield (GJ/ha/yr) EROEI so far: Corn 9.86 1.07 6.26 2.26 18.65 8746 139.8 7.5 Cellulose 2.49 0.14 4.36 0.43 7.38 13450 242.1 32.8 From the above, 19 GJ of energy inputs are required to produce 140 GJ (8.7 t) of corn, giving an EROEI up to this point of about 7.5. From the lower part of Table 4.19, the 140 GJ of corn energy corresponds with 77 GJ of glucose (the rest being other materials in the corn), which in turn are converted into 62.5 GJ (2943 litres) of ethanol. The energy inputs required to produce the ethanol are • • • • 19 GJ/2943 litres = 6.34 MJ/litre in the production of the corn 6-12 MJ/litre of coal and/or natural gas at the ethanol plant 2 MJ/litre of electricity primary energy 1.5 MJ/litre of other energy inputs (such as to build the ethanol plant and for water treatment) The total energy inputs are thus 16-22 MJ per litre of ethanol produce, but a litre of ethanol contains only 21 MJ of energy. Thus, the energy yield ranges from -1MJ/litre to +5 MJ/litre. However, some products (animal feed) other than ethanol are produced and these save the energy otherwise used to make these products, so an energy credit can be given – up to 4 MJ per litre of ethanol produced. Figure 4.39 A 450 million litre-per-year corn ethanol plant in South Dakota Source: Tollefson (2008, Nature 451, 880–883) Key points, ethanol from corn: • The Energy Return over Energy Invested is justly barely greater than 1.0 (1.5-1.8), and is less than 1.0 for some studies if energy credits for co-products are excluded • The energy used in producing the corn is equal to about one third the energy content of the ethanol that is produced • The fossil fuel energy inputs at the ethanol plant are equal to about half to 2/3 the energy value of the ethanol • This energy in some plants occurs largely as coal (hardly a “green” fuel) • At other plants the energy input is natural gas (which is hardly in abundance) • The net energy gain for ethanol-from-corn depends on energy credits to the meat-production industry (which fuels over-consumption of meat in the western world, with its own long list of environmental and other problems) Ethanol from sugarcane From Table 4.22, an average sugarcane yield in Brazil is ~ 70 t/ha/yr or (in terms of energy value), 430 GJ/ha/yr (about 3 times that of US corn). The energy input per hectare, however, is less than for corn (about 13 GJ/ha/yr vs 18 GJ/ha/yr). Furthermore, because of the high glucose content of sugarcane, the energy requirements required at the ethanol plant are much less (about 5 MJ/litre) than for corn (9-15 MJ/itre). Furthermore, the energy input can be entirely met by burning the residue (called bagasse) that can be burned to produce heat and electricity. The result is an EROEI that averages about 10 today Ethanol from sugarcane (continued) In the future, with advanced electricity production from bagasse (BIGCC), there will be substantial electricity production in excess of the requirements of the ethanol plant, giving an EROEI of ~ 20-40 (depending on future sugarcane crop yields) However, the longterm (decades to centuries) sustainability of current industrial methods of sugarcane production is not clear, particularly if bagasse and other residues are used to supply energy rather than returned to the soil. Even if soil macronutrients (N, P, K) can be replaced with fertilizers, depletion of micro-nutrients could be a problem in the long term. Ethanol from ligno-cellulosic crops • Projected yields are based on expected gains based on current R&D • High EROEIs (~ 6-8) are projected, assuming that biomass residues can be used to supply the ethanol plant energy requirements • However, if the residues need to be returned to the soil to maintain longterm soil productivity, the EROEI would be much smaller Biodiesel from vegetable oils • The main crops are soybeans and canola (in North America esp), sunflower (in Europe), and palm oil (in Indonesia, Malaysia, Thailand) • Soybeans are already used to produce animal meal (but also yield vegetable oils), while canola is a preferred source of vegetable oils (but also provides some animal meal) Market chain reaction: • Production of soybeans to produce oil for biodiesel increases the supply of animal feed as a byproduct • This will be offset by a reduction in the pre-existing soybean production dedicated to production of animal feed • But this also reduces the supply of soy oil for non-energy purposes • So there will be an increase in canola production • The adjustments in non-biofuel soybean production and in canola production will be such (ideally) that there is no net change in the supply of animal feed or in the supply of vegetable oil for non-energy purposes The net result, given the proportions of oil and protein in soybean and canola, and the substitutability between soybean feed and canola feed, is that the energy credit per kg of soybean meal that is produced as a by-product of biodiesel production, is given by Ecredit =1.62 Esoybean – 0.73 Ecanola where Esoybean = energy required to produce and crush soybeans, and Ecanola = energy required to produce and crush canola. As Ecanola > Esoybean, the energy credit for the production of soybean meal as a co-product of biodiesel can be negative! The reason Ecanola > Esoybean in turn is because soybean is a nitrogen-fixing crop and canola is not (so it needs larger N fertilizer inputs, and N production has a high energy requirement) Also note that the negative energy credit from the soybean meal co-product of biodiesel production depends on the fact that soybean meal is the marginal protein meal in the market (that is, increases or decreases in protein meal demand are met with increases or decreases in the production of soybean meal) and that canola oil is the marginal vegetable oil in the market (so changes in the demand for vegetable oil are met with changes in the production of canola oil) Estimated EROEI for biodiesel from oily crops • Canola (rapeseed), 1.0-2.0 • Soybeans,1.4 to 2.2 • Jatropha, 4.6-5.3 in India 0.5-2.7 in Thailand without co-product credits 2-12 in Thailand with co-product credits Note: • A large part of the EROEI for biodiesel from soybeans or canola is due to the energy credit from the co-production of glycerine (11 MJ/litre, compared to about 33 MJ/litre for biodiesel itself) • With large-scale production of biodiesel, more glycerine would be produced than can be used, so its only energy value would be through its combustion for use as a fuel (this would be a small credit) Impact of the production and use of biofuels on GHG emissions • The avoided emissions are the emissions associated with the production and use of the fuels (gasoline and diesel) that the biofuels replace • The direct emissions are the emissions of CO2 from the fossil fuels used in the production of biofuels (substantial coal or natural gas in the case of corn ethanol) and emissions of N2O from the application of N fertilizers • There are additional indirect emissions due to clearing of forests or peatland in order to establish palm oil plantations, or deforestation in the Amazon due to crops displaced by new sugarcane plantations, or changes in land use due to induced changes in the prices of agricultural commodities (in the case of corn ethanol, for example) Range of estimates of the direct impact on GHG emissions of replacing gasoline and diesel with biofuels (Table 4.27) Source: Worldwatch Institute (2006, Biofuels for Transportation: Global Potential and Implications for Sustainable Agriculture and Energy in the 21st Century) for transportation. Source: WWI (2006, Tables 11-1 to 11.3). Biofuel Emission Number feedstock Change of studies Conventional ethanol Corn, E90 +3.3% 1 Corn, E100 -13% to –38% 6 Sugar Beet, E100 -35% to –56% 5 Molasses, E85 -1% to –51% 1 Sugar Cane, E100 -87% to –96% 2 Wheat, E100 -19% to –47% 5 Cellulosic ethanol Wheat straw -57% 1 Corn stover -61% 1 Hay -68% 1 Grass -37% to –73% 4 Waste wood -81% 1 Crop straw -82% 1 Poplar -51% to –107% 2 Biodiesel Rapeseed -21% to –48% 11 Pure plant oil -42% 1 Soybeans -53% to –78% 4 Soybeans +0% to +100% 1 Tallow -55% 1 Waste cooking oil -92% 1 Indirect effect on GHG emissions through induced changes in land use when land formerly used for food or pasture is converted to biofuel production • If corn is devoted to ethanol production, more soybean feed is needed for animals, so the price of soybeans goes up, which encourages expansion of soybean plantations into tropical rainforests • One assessment with a model of the global agricultural economy predicts that replacement of gasoline with US corn-ethanol increases GHG emissions by 100%, rather than reducing them by 20%! GHG debt incurred when grassland, tropical forests, or tropical peatland are converted to biofuels production (Table 4.28) Original land type Indonesian and Malaysian peatland Indonesian and Malaysian lowland tropical forest Brazilian Amazon Brazilian cerrado Brazilian cerrado US central grassland US abandoned farmland Crop and biofuel Initial debt (tC/ha) palm oil biodiesel palm oil biodiesel soybean biodiesel soybean biodiesel sugarcane ethanol corn ethanol corn ethanol 941 Portion of debt assigned to biofuels 87% 191 87% 86 201 39% 319 23 39% 37 45 100% 17 37 19 83% 83% 93 48 Source: Fargione et al (2008, Science 319, 1235–1238) Time required to pay back initial debt (years) 423 EROEI for the use of solid biomass fuels for heating Willow in and New Yorkgas state (Table 4.29) Table 11.34 Energy greenhouse balance of a willow plantation in New York state, US, over a 23-year cycle involving 7 harvestings. Source: Heller et al. (2003). Energy Balance Yield 11.93 odt/ha/yr 236.3 GJ/ha/yr 5435 GJ/ha Input, production with fertilizer Input, production with biosolids Input, transport 96 km by truck EROEI, production only with fertilizers EROEI, production with fertilizers + transport EROEI, production with biosolids + transport Source: Heller et al (2003, Biomass and Bioenergy 25,147–165, http://www.sciencedirect.com/science/journal/09619534) 19.8 GJ/odt 0.358 GJ/odt 0.226 GJ/odt 0.189 GJ/odt 55.3 36.2 47.8 Woody biomass in Norway (Table 4.31), excluding any fertilizer inputs Source: Based on Raymer (2006, Biomass and Bioenergy 30, 605–617, http://www.sciencedirect.com/science/journal/09619534) Biomass supply to Europe (Table 4.33) Biomass Location Biomass Source Transport Mode Scandinavia Forestry residues Forestry residues Forestry residues Forestry residues Shortrotation willow coppice Eucalyptus plantation Chips by ship Chips by trains Pellets by ship Pellets by train 1100 km Scandinavia Scandinavia Scandinavia E Europe Latin America Distance Biomass Energy loss Input GJ/tonnedry delivered 1.6 1.6 EROEI 12.6 1100 km 1.6 4.6 4.3 1100 km 0.5 1.2 16.7 1100 km 0.5 2.5 8.0 Pellets by ship 2000 km 0.1 1.0 9.4 Pellets by ship 11500 km 0.4 1.4 14.1 Source: Hamelinck et al (2005, Biomass and Energy 29, 114–134, http://www.sciencedirect.com/science/journal/09619534) Switchgrass pellets Table 11.40 Energy terms inin theCanada production of(Table 4.35) switchgrass pellets. Source: Samson et al. (2005). Activity Energy (GJ/tonne) Establishment 0.028 Fertilizer+Application 0.460 Mowing 0.034 Bailing 0.197 Transport 0.072 Biofuel production total 0.791 Pellet mill construction 0.043 Pellet mill operation 0.244 Delivery 0.193 Pellet production total 0.480 Overall total Energy supplied EROEI 1.27 18.5 14.6 Source: Samson et al (2005, Critical Reviews in Plant Sciences 24, 461–495) Table 11.41 Energy terms in the production of 30 oven-dry tonnes (ODT)/ha/yr of napier(Table grass in Brazil. Napier grass in Brazil 4.36) Terms in brackets are for the case without application of N fertilizer. Source: Samson et al. (2005). Activity Energy (GJ/ha/yr) Establishment (every 3 yrs) 0.18 N fertilizer 3.69 Other fertilizer 2.29 Lime 4.37 Pesticides 0.02 Mechanical weeding 0.18 Harvest 7.21 Transport (16 km) for processing 1.23 Machinery embodied energy 2.27 Total input: 23.1 (19.4) Energy yield @ 16.44 GJ/ODT 493.2 EROEI 21.3 (25.4) Densification (0.1-0.3 GJ/t) 3-9 Drying (2.6-5.2 GJ/t) 78-156 94-188 Total input: EROEI 2.6-5.2 Source: Samson et al (2005, Critical Reviews in Plant Sciences 24, 461–495) Figure 4.40 Energy required to produce and delivery various fuels for heating in Sweden, as a fraction of the energy content of the fuel 0.18 Energy Input (MJ/MJfuel) 0.16 20 Transportation Production, Harvesting, Processing EROEI 18 16 0.14 14 0.12 12 0.10 10 0.08 8 0.06 6 0.04 4 0.02 2 0.00 0 Source: Gustavsson and Karlsson (2002, Energy Policy 30, 553-574, http://www.sciencedirect.com/ science/journal/03014215) EROEI 0.20 EROEI for the production of gaseous biofuels Figure 4.41 Energy input to make biogas from different biomass materials in Sweden 50 Energy input/output (%) 40 Transport of raw materials Transport of digestate Handling of raw materials Spreading of digestate Biogas plant - electricity Biogas plant - heating 30 20 10 0 Grease Municipal Slaugher Tops & Pig sep. org. - house leaves of manure sludge waste waste sugar beet Straw Source: Berglund and Borjesson (2006, Biomass and Bioenergy 30, 254–266, http://www.sciencedirect.com/science/journal/09619534) Cow manure Ley crops Figure 4.42 Efficiencies in producing fuels from biomass Ethanol from Corn Ethanol from Sugarcane F2006 W2007C Based on Bioenergy Input Only W2007N M2004 Based on total energy input M2004 M2004 Ethanol from wood F2006 from soybeans P2008 from rapeseed P2008 Biodiesel S2005 S2005 soybeans Ethanol from corn & corn stover KD2005a KD2005a KD2005a KD2005a Ethanol+electricity from woody crops HF2005 HF2005 Methanol now Methanol future Fuels from woody crops (HF2006 & TY2008) Ethanol now Ethanol future Hydrogen now Hydrogen future FT diesel now FT diesel future 0.0 0.2 0.4 0.6 Efficiency 0.8 1.0 20 10 P2004 PiP2005 SM2004 F2006 O2005 B2001 O2005 PaP2005 PiP2005 W2001 F2006 C2004 PiP2005 PiP2005 KD2005a KD2005a KD2005a KD2005a HF2006 HF2007 HF2008 HF2009 Methanol now Methanol future Ethanol now Ethanol future Hydrogen now Hydrogen future FT diesel now FT diesel future Percent of Total Energy Input Figure 4.43 Biofuel inputs and output 100 90 80 70 60 50 40 30 Process Energy Input Agricultural Energy Input Bioenergy Input Total Output Energy 0 Biomaterials Figure 4.44 Principle routes for the synthesis of organic chemicals from biomass feedstocks benzene lignin xylene toluene phenols fibers, dyes, solvents intermediates adhesives phenolic resins polymers wood hemicellulose xylose furfural ethylene ethanol cellulose glucose butadiene synthetic rubber polymers starch lactic acid crops acids fats & oils glycerol soaps, detergents Source: Geiser (2001, Materials Matter: Towards a Sustainable Materials Policy, MIT Press, Cambridge) Figure 4.45 Energy requirements to produce PET (from petroleum) and PLA (from biomass) 90 Primary Energy Use (GJ/tonne) 80 Fossil fuel feedstock Process energy 70 60 50 40 30 20 10 0 PET PLA, current PLA, future Source: Detzel et al (2006, in Renewables-Based Technology, John Wiley and Sons, Chichester) Alternative uses of land for reduction of GHG emissions • Production of bio-energy crops (discussed above) • Biological carbon sequestration • Simultaneous bioenergy crop production and biological carbon sequestration • Bioenergy crops and geological carbon sequestration Biological C sequestration • Buildup of above-ground biomass • Buildup of normal soil C • Buildup of biochar Table 4.41 Estimated rates of accumulation of soil carbon due to improved land management that can be sustained over a period of 50 years. System Cropland Biofuel croplands Grasslands Forests Degraded lands Agroforestry Total Global Land Area (Mha) 150 13 47 164 109 21 504 Rate of C Accumulation (tC/ha/yr) 0.3 0.6-1.2 0.5-0.7 1.0-3.0 0.8-3.0 0.3-0.5 Global Total (GtC/yr) 0.045 0.008-0.016 0.024-0.033 0.164-0.492 0.087-0.262 0.006-0.011 0.33-0.86 Source: Lemus and Lal (2005, Critical Reviews in Plant Sciences 24, 1–21 Biochar • Produced through slow pyrolysis (the first step in thermo-chemical gasification, discussed earlier) • Pyrolysis drives off volatile materials (which can be captured and used for energy) • The remaining solid is highly resistant to decomposition • When added to soils, it improves soil fertility, structure, and water retention • However, it might accelerate decomposition of pre-existing soil organic matter From Box 4.2, the avoided CO2 emissions from alternative uses of land are • Improved management within existing land uses: 0.3-3.0 tC/ha/yr • Reforestation: 2-10 tC/ha/yr • Dedicated bioenergy crops displacing coal for electricity generation: 5 tC/ha/yr, plus perhaps another 0.4-2 tC/ha/yr through buildup of soil C with careful management • Brazilian sugarcane ethanol displacing gasoline, 7 tC/ha/yr • H2 + biochar with capture of released CO2: 14 tC/ha/yr • Dedicated production of H2 from biomass with capture and geological sequestration of CO2: 5-7 tC/ha/yr • Avoided deforestation: up to 300 tC/ha/yr Future biomass potential from plantations • Depends on the available land area for plantations • Depends on the productivity (biomass/hectare/year) of the plantation Assuming no expansion of current agricultural and pasture land areas, the only land available for plantations will be surplus agricultural and pasture land. Whether there is any surplus in the future, and how much, depends on • Human population • Phytomass requirements per person • Productivity of agricultural land and of pastureland Figure 4.46 Trend in grain yield averaged over various regions 4000 3500 World All developing 3000 South Asia Yield (kg/ha/yr) Sub-Saharan Africa 2500 2000 1500 1000 500 0 1961 1965 1969 1973 1977 1981 1985 1989 1993 1997 2001 2005 Year Source: Hazell and Wood (2008, Phil. Trans. Royal Soc. B, 363, pp495–515 ) Large increases in the productivity (food/area) of agricultural lands are projected Table 11.50. Projected ratio of agricultural yields 2050 compared to agricultural 1998 according to in 2050 Table 4.43inProjected ratio of yields a range to of 1998 scenarios, in the absence of of scenarios, in the compared according to a range increasing CO2 and climatic change. Source: absence of increasing CO2 and climatic change. WWI (2006). Region North America Western Europe Eastern Europe Former Soviet Union Japan East Asia South Asia Oceania Sub-Saharan Africa Caribbean and Latin America World Yield Ratio 1.6-3.2 0.9-1.9 2.1-4.1 3.2-6.7 2.7-3.0 2.3-3.2 3.7-5.6 2.4-4.6 5.6-7.7 2.8-4.5 2.9-4.6 Source: Worldwatch Institute (2006, Biofuels for Transportation: Global Potential and Implications for Sustainable Agriculture and Energy in the 21st Century) Phytomass requirements per person depend on • Proportion of meat in the diet, and • Inverse feed efficiency for production of animal meat (kg phytomass per kg of meat produced) Recap of Volume 1 Figure 7.12: Phytomass energy flows in the world food system. Source: Wirsenius (2003, Journal of Industrial Ecology 7, 47–80) From Table 4.45: Amount of phytomass (in terms of its energy value) needed to produce 1 kg of food product or 1 kg of protein for human consumption From Table 4.46: Daily phytomass requirements with presentday world average feed intensities (45 kg phytomass/kg meat, 8 kg phytomass/kg dairy product): Affluent: Moderate: Vegetarian: Vegan: 140 MJ/day 64 MJ/day 27 MJ/day 20 MJ/day Current world average: 70 MJ/day Same as above, but with lower feed intensities (due to more use of inhumane industrial-scale production systems) (namely, 30 kg/kg for meat, 5 kg/kg for dairy) Affluent: 96 MJ/day Moderate: 47 MJ/day Vegetarian: 24 MJ/day Vegan: 20 MJ/day With current world average diet: 53 MJ/day From Table 4.47: Current cropland area is 1452 Mha Current pastureland area is 3405 Mha Total land area for food is 4857 Mha Land available for bioenergy plantations with a human population of 8.8 billion: Universal vegetarian diet: 3500-4200 Mha (depending on future agricultural yields) Universal moderate diet: 0-3400 Mha Universal affluent diet: 0 Mha The energy that could be supplied (as biomass), assuming biomass yields of 200 GJ/ha/yr on surplus agricultural land and 100 GJ/ha/yr on surplus pastureland, is: Universal vegetarian diet: 370-500 EJ/yr Universal moderate diet: 0-340 EJ/yr By comparison, total world primary energy demand today is about 500 EJ/yr (Note: energy yields on Brazilian sugarcane plantations are ~ 400 GJ/ha/yr today and are projected to reach 800 GJ/ha/yr in the future) Big increases in the yield of bioenergy crops are projected Table 4.49 Current and projected future yields of switchgrass in different regions of the US, assuming no change in climate Source: Larson (2006, Energy for Sustainable Development 10, 109–126 Costs • Cost of solid fuels: typically $2-4/GJ, vs $2-3/GJ for coal at present • Costs of liquid fuels from biomass: generally less than $1/litre • Capital costs of powerplants using biomass: $2000-4000/kW, vs $600-900/kW for natural gas powerplants (but natural gas is likely to be expensive in the long run) and $1200-1600/kW for coal powerplants without CO2 capture) • Cost of electricity from biomass at $2/GJ: 7-13 cents/kWh Figure 4.47a Present production costs of various liquid fuels Ethanol from cellulose Ethanol from grain (EU) Gasoline (wholesale) Ethanol from corn (US) Ethanol from sugarcane (Brazil) 0 0.2 0.4 0.6 0.8 1 Euros per Litre Gasoline Equivalent Source: Modified from Worldwatch Institute (2006, Biofuels for Transportation Global Potential and Implications for Sustainable Agriculture and Energy in the 21st Century) Figure 4.47b Present biodiesel production costs Diesel fuel Biodiesel from rapeseed (EU) Biodiesel from soybeans (US) Biodiesel from waste grease (US) 0.0 0.2 0.4 0.6 0.8 1.0 Euros per Litre Diesel Equivalent Source: Modified from Worldwatch Institute (2006, Biofuels for Transportation Global Potential and Implications for Sustainable Agriculture and Energy in the 21st Century) Table 4.53 Costs and efficiency of direct combustion steam turbines for generating electricity from biomass, and the resulting cost of electricity assuming 7% financing over 20 years. FB=fluidized bed. Size (MW) 3.4 10 15 50 60 Boiler Tech nology Pile Stoker FB Stoker Stoker Capacity Factor 0.9 0.9 0.9 0.8 0.8 Efficiency 0.16 0.13 0.13 0.24 0.28 Capita l Cost ($/kW) 4235 2875 3116 2191 1946 Operation and Maintenance Costs Fixed Variable ($/kW/yr) (c/kWh) 274 0 270 0 254 0 81 0.95 67 0.75 Cost of Electricity (cents/kWh) Fuel at Fuel at $0/GJ $2/GJ 8.5 12.9 6.9 12.5 7.0 12.5 5.1 8.1 4.3 6.9 Source: Western Governors’ Association (2006) Clean and Diversified Energy Initiative, Biomass Task Force Report, www.westgov.org/wga/initiatives/cdeac/Biomass-full.pdf Heat Credit (cents/ kWh) 6.4 8.7 8.7 3.9 3.1 Figure 4.48 Cost of wood-fired powerplants in Finland Specific investement costs in euros per kW 2000 1500 1000 500 0 0 50 100 150 Installed plant capacity in MW Source: IEA (2003, Renewables for Power Generation, Status and Prospects, 2003 Edition, International Energy Agency, Paris) 200 Figure 4.49a Cost of supplying increasing amounts worldwide of biofuels using Fischer-Tropsch synthesis. A key factor in the cost estimate is the future cost of rural labour, which depends on the degree of economic development and hence on the socio-economic scenario assumed (A1, A2, B1, B2 are from the IPCC SRES report). Gasoline at $1/litre is equivalent to $18/GJ. Current worldwide oil demand is about 160 EJ/yr. 20 Cost of Biofuel ($/GJ) A2 B1 B2 A1 15 10 5 0 0 50 100 150 200 250 300 Technical Potential of Biofuels for Transport (EJ/yr) Source: Hoogwijk et al (2009, Biomass and Bioenergy 33, 26-43, http://www.sciencedirect.com/science/journal/09619534) Figure 4.49b Cost of supplying increasing amounts worldwide of electricity from biomass. Current worldwide electricity demand is ~ 18 PWh/yr Cost of Electricity (cents/kWh) 10 A2 B2 B1 A1 8 6 4 2 0 0 20 40 60 80 Technical Biomass Electricity Potential (PWh/yr) Source: Hoogwijk et al (2009, Biomass and Bioenergy 33, 26-43, http://www.sciencedirect.com/science/journal/09619534)