See discussions, stats, and author profiles for this publication at: https://www.researchgate.net/publication/308306859 REMOVAL OF COLOUR FROM WASTEWATER USING LOCALLY AVAILABLE CHARCOAL Conference Paper · February 2014 CITATION READS 1 3,592 4 authors, including: Niamul Md. Bari H. M. Rasel Rajshahi University of Engineering & Technology Rajshahi University of Engineering & Technology 83 PUBLICATIONS 297 CITATIONS 37 PUBLICATIONS 279 CITATIONS SEE PROFILE SEE PROFILE Some of the authors of this publication are also working on these related projects: Treatment of Industrial Wastewater for the Removal of Colour by using Locally Available Low Cost Adsorbent View project All content following this page was uploaded by Niamul Md. Bari on 19 September 2016. The user has requested enhancement of the downloaded file. Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development (ICCESD-2014), 14~16 February 2014, KUET, Khulna, Bangladesh, ISBN: 978-984-33-6373-2 (CD-Rom) REMOVAL OF COLOUR FROM WASTEWATER USING LOCALLY AVAILABLE CHARCOAL Md. Niamul Bari1 , Mst. Sulekha Khatun2, H.M. Rasel1 and Fatema Khatun3, Department of Civil Engineering, Rajshahi University of Engineering & Technology *Corresponding Author’s E-mail: niamulbari@yahoo.com ABSTRACT Adsorption technique is used for the effective removal of dyes. Because of the high cost of some conventional adsorbents, locally available Charcoal is used as adsorbent in this study. The aim of this study is to investigate the use of Charcoal as an alternative adsorbent for the removal of dyes present in textile effluents. One-factorat-a time (OFAT) method is used for the experimental design considering three independent parameters viz., particle size, particle dose and shaking time. The particle size of charcoal is varying from 0.075 to 1.8 mm. The charcoal doses are 2, 4, 6, 8 and 10 mg/100 ml of methylene blue solution are used and centrifuged at 10000 rpm for 3, 6, 9, 12 and 15 minutes. The results show that the effective particle size of charcoal is 0.3 to 0.6 mm and the charcoal dose is 6 mg/100 ml and the mixing time is 15 minutes for the 100% removal of colour having methylene blue concentration of 10 mg/l. Keywords: charcoal, colour removal, local absorbent, optimum dose, particle size. 1. Introduction The world-wide high level of production and use of dyes generates colored wastewater, which give cause of environmental concern. Almost every industry uses colouring matter to colour their products. Of various pollutants contained in industrial wastewater, colour is considered to be very important from the aesthetic point of view and is stated as visible pollutant. Textile companies, dye manufacturing industries, paper and pulp mills, tanneries, electroplating factories, distilleries food companies and a host of other industries discharge colored wastewater which are released into nearby land or rivers without any treatment (Amin, et al., 2008). Textile processes produce multi component wastewater which can be difficult to treat (Jaya and Arumai, 2008). This wastewater can cause serious environmental problems due to their high color, large amount of suspended solids, and high chemical oxygen demand (Jaya and Arumai, 2008). Discharging of color or dyes into water resources even in a small amount can affect the aquatic life and the food web. Dyes can also cause allergic dermatitis and skin irritation and may lead to carcinogenic and other disorders. The methods of color removal from industrial effluents include biological treatment, coagulation, adsorption, chemical oxidation, hyper filtration and reverse osmosis are generally not feasible due to economic considerations. Moreover, the conventional methods of sewage treatment, such as primary and secondary treatment systems are not suitable for the treatment of effluents containing dye molecules because these molecules are very complex in nature and are stable to heat and light. Nowa-days, there are more than 10,000 dyes available commercially (Nigam, et al., 2000), most of which are not easy to biodegrade because of their stability toward light and oxidation; also these dyes are resistant to aerobic digestion (Gupta, et al., 2003) due to their complex aromatic molecular structure and synthetic origin (Seshdari, et al., 1994). Adsorption is an effective method of lowering the concentration of dissolved dyes in the effluent resulting in color removal. The process of adsorption has an edge over the other methods due to it sludge free clean operation and complete removal of dyes even from dilute solution (Malik, 2003). 1375 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development The most efficient and commonly used adsorbent is commercially activated carbon which is expensive and has re-generation problem. Therefore, development of low cost alternative adsorbent has been the focus of recent research. Various adsorbents have been tried for the removal of different types of synthetic dyes. Perhaps, activated carbon is the most widely used adsorbent because of its extended surface area, microporous structure, high adsorption capacity and high degree of reactivity. However, commercially available activated carbons are very expensive (Malik, 2003). Consequently, the high cost of the activated carbon, coupled with the problems associated with regeneration, has necessitated the search for alternate adsorbents. A wide variety of low cost materials such as agricultural by product (Kadirvelu et al., 2000), waste coir pith (Namasivayam et al., 2001), Indian rosewood sawdust (Garg et al., 2004), pine sawdust (Özacar and Şengil, 2005), banana pith (Namasivayam et al., 1998), rice husk (Lee, et al., 1999), orange peel (Namasivayam et al., 1996) and pea shells charcoal (Sumanjit et al., 2007) are used as low cost alternatives to activated carbon. The present study investigates the adsorption methods to remove dyes from effluent using cheaper source of adsorbent, namely charcoal, which is locally available in plenty in Bangladesh. 2. Materials and Methods 2.1. Collection and preparation of adsorbents In this study, locally available charcoal is used as adsorbent. The locally available charcoal was collected and ground in different finer particle. The charcoal particles are graded using sieve and preserved in the closed container for subsequent use. The particle sizes used for the experiment are shown in Table 1. Table 1: Particle Sizes of Charcoal Samples Sample no. 1 2 3 4 5 2.2. Preparation of dye solution Sieve no. Particle sizes 16 30 50 100 200 1-1.8 mm 0.6 – 1 mm 0.3 – 0.6 mm 0.15 – 0.3 mm 0.075 – 0.15 mm Methylene blue is a heterocyclic aromatic chemical compound with molecular formula: C16 H18ClN3S. It was chosen because of its known strong adsorption onto solids and widely use in dying industry. The dye is regarded as acutely toxic, but it can have various harmful effects. Methylene blue (LOBA Company, India) was collected from commercial market. The stock solution of dye was prepared by dissolving 10 mg of methylene blue in 1000 ml of distilled water. 2.3. Experimental Procedure The Spectrophotometer was used for the determination of methylene blue removal from aqueous solution by measuring optical density. Removal of colour of methylene blue is determined by comparing the optical density of treated sample with the optical density of aqueous solution of methylene blue. Colour removal is expressed in percentage. One-factor-at-a time (OFAT) method is used for the experimental design considering three independent parameters viz., particle size, particle dose and shaking time. The particle sizes of charcoal shown in Table 1 are used in different doses are 2, 4, 6, 8 and 10 mg/100 ml of methylene blue solution for each charcoal sample. The dye solutions with charcoal doses are kept for 24 hours for soaking. The soaked samples are centrifuged at 10000 rpm (Khadijah, et al., 2009) for 3, 6, 9, 12 1376 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development and 15 minutes for each sample of each dose. After centrifuging the solution is filtered with Whatman Number 1 filter paper and optical density of supernatant is measured with UV/VIS spectrophotometer at 225 nm (Rita and Rattan, 2009). Figure 1 shows the experimental process. Figure 1: Sample preparation, centrifuging and filtration of sample 3. Results and Discussions Charcoal of five different particle sizes is used as absorbent of methylene blue for aqueous solution. The doses of each charcoal sample were varied as 2, 4, 6, 8 and 10 mg/100 of methylene blue solution. The mixing time is also varied for every dose of each charcoal sample of 3, 6, 9, 12 and 15 minutes. All experiments are conducted in triplicate. The colour removal results in terms of percentage for each experiment are presented in Table 2. Table 2: Removal of Color from Methylene Blue Solution Sample Sample-1 (1-1.8 mm) Sample-2 (0.6-1mm) Sample-3 (0.3-0.6 mm) Sample-4 (0.15-0.3 mm) Sample-5 (0.075-0.15 mm) Mixing time (min) 3 6 9 12 15 3 6 9 12 15 3 6 9 12 15 3 6 9 12 15 3 6 9 12 15 2 42 60 64 69 76 15 34 40 47 66 92 93 94 94 99 68 78 78 72 99 51 52 65 70 76 4 35 52 63 82 83 11 20 20 64 65 88 91 94 98 99 63 64 68 72 72 54 56 57 63 88 1377 Dose (mg/100 ml) 6 21 47 58 72 88 27 28 63 65 74 93 98 98 99 100 65 65 67 74 91 47 52 56 82 89 8 22 31 51 52 85 21 23 56 57 57 95 97 98 98 98 64 69 75 76 80 32 56 67 72 73 10 18 26 28 45 67 21 43 54 68 81 95 96 98 98 98 47 48 59 66 73 36 48 64 66 84 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development 3.1. Effect of mixing time The effect of mixing time on colour removal with five charcoal samples of different particle sizes are examined and the trends of colour removal with mixing time for each sample are presented in Figure 2 to 6. The charcoal doses of 2, 4, 6, 8 and 10 mg per 100 ml of methylene blue solution (10 gm/L) are used for each charcoal sample. Colour removal (%). 100 Sample-1 80 60 40 2mg/100ml 4mg/100ml 6mg/100ml 8mg/100ml 10mg/100ml 20 0 0 3 6 9 12 Mixing time (min) 15 18 Figure 2: Colour removal with mixing time for charcoal sample-1 100 Colour removal (%). Sample-2 80 60 40 2 mg/100 ml 4 mg/100 ml 6 mg/100 ml 8 mg/100 ml 10 mg/100 ml 20 0 0 3 6 9 12 Mixing time (min) 15 Figure 3: Colour removal with mixing time for charcoal sample-2 1378 18 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development 110 Colour removal (%). Sample-3 100 2 mg/100 ml 4 mg/100 ml 6 mg/100 ml 8 mg/100 ml 10 mg/100 ml 90 80 0 3 6 9 12 Mixing time (min) 15 18 Figure 4: Colour removal with mixing time for charcoal sample-3 Colour removal (%). 100 Sample-4 80 2 mg/100 ml 4 mg/100 ml 6 mg/100 ml 8 mg/100 ml 10 mg/100 ml 60 40 0 3 6 9 12 Mixing time (min) 15 18 Figure 5: Colour removal with mixing time for charcoal sample-4 Colour removal (%). 100 Sample-5 80 60 2mg/100ml 4mg/100ml 6mg/100ml 8mg/100ml 10mg/100ml 40 20 0 3 6 9 12 Mixing time (min) 15 Figure 6: Colour removal with mixing time for charcoal sample-5 1379 18 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development From the Figure 2 to 6 show the similar trend of colour removal with respect to mixing time. The removal of colour was increased with the increase of mixing time. However, the removal trends for every charcoal sample that are observed from the figures are not linear with time. The reason of this non linearity of colour removal might be determined by the kinetic study of the experiment. Moreover, the highest colour removal was obtained at 15 minutes mixing time for all samples of every dose. 3.2. Effect of particle size Locally available five charcoal samples with different particle sizes (Sample-1, 1 to 1.8 mm; Sample2, 0.6 to 1 mm; Sample-3, 0.3 to 0.6 mm; Sample-4, 0.15 to 0.3 mm and Sample-5, 0.075 to 0.15 mm) are used as absorbent for the removal of colour from the aqueous solution of methylene blue with the concentration of 10 mg/L. The previous experiment shows that the maximum removal of colour is obtained at the mixing time of 15 minutes. Therefore, the effect of particle size of charcoal on colour removal is presented for 15 minutes mixing time in Figure 7. The Figure 7 shows that nature of colour removal by different charcoal samples with various particle sizes. The highest removal of colour from methylene blue aqueous solution is obtained to be for the Sample-3 with the particle sizes varying within 0.3 to 0.6 mm. The total removal of colour is achieved with the charcoal sample having particle size within 0.3 to 0.6 mm. Colour removal (%). 110 100 90 80 70 2mg/100ml 4mg/100ml 6mg/100ml 8mg/100ml 10mg/100ml 60 50 40 0 1 2 3 Sample 4 5 6 Figure 7: The effect of particle size of charcoal on colour removal 3.3. Effect of adsorbent dose The highest removal of colour from methylene blue solution is obtained against the charcoal dose of 6 mg/100 ml for all samples except Sample-2. The highest removal efficiency (100%) is observed for Sample-3 with dose of 6 mg/100 ml. Furthermore, the highest removal is obtained for Sample-3 in any doses of charcoal compared to the other samples. The colour removal efficiency is presented in Figure 8. 1380 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development Colour removal (%). 110 100 90 80 70 60 Sample-1 Sample-4 50 40 0 2 Sample-2 Sample-5 4 6 8 Charcoal dose (mg/100ml) Sample-3 10 12 Figure 8: The effect of absorbent dose on colour removal 4. Conclusions It is observed from the experiment that the efficiency of colour removal varies with the variation of adsorbent particle size, adsorbent dose and mixing time. The experimental results show that the effective particle size of charcoal for using as absorbent of methylene blue is varying from 0.3 to 0.6 mm. For the total removal of colour, the charcoal dose to be 6 mg/100 ml and the mixing time is 15 minutes. It is evident that the locally available charcoal is effective in removal of methylene blue and can provide an economical solution for removal of such colour from the aqueous solution. From 74 to 100 % colour removal efficiency can be achieved having methylene blue concentration of 10 mg/l for any size of charcoal particle. The locally available charcoal can be proved as good, effective and eco friendly adsorbent. 5. References Amin NK, Removal of reactive dye from aqueous solutions by adsorption activated carbons prepared from sugarcane bagasse pith, Desalination, 223, 152-161, 2008. Garg VK, Kumar R, Gupta R, Removal of malachite green dye from aqueous solution by adsorption using agro-industry waste, a case study of Prosopis cineraria, J Dyes and Pigments, 62, 1-10, 2004. Gupta VK, Ali I and Mohan D, J. Colloid Interface Science, 265, 257, 2003. Jaya Paul and Arumai Dhas, Study on removal of COD and colour from textile wastewater using limestone and activated carbon, MSc Thesis, University Sains Malaysia, 2008. Kadirvelu K, Palonival M, Kalpana R, Rajeswari S, Activated carbon from an agricultural byproduct, for the treatment of dyeing industry wastewate, Bioresource Technology, 74, 263-265, 2000. Khadijah O, Lee KK and Mohd Faiz F, Abdullah, Isolation, screening and development of local bacterial consortia with azo dyes decolourising capability, Malaysian Journal of Microbiology, 5(1), 25-32, 2009. Lee CK, Low KS, Gan PY, Removal of some organic dyes by Acid Treated Spent Bleaching Earth, Environ. Technol., 20, 99-104, 1999. 1381 Proceedings of the 2nd International Conference on Civil Engineering for Sustainable Development Malik PK, Use of activated carbons prepared from sawdust and rice husk for adsorption of acid dyes, a case study of Acid Yellow 36. Dyes and Pigments, 56, 239-249, 2003. Namasivayam C, Muniasamy N, Gayatri K, Rani M and Ranganathan K, Removal of dyes from aqueous solution by cellulosic waste orange peel, Bioresource Technology, 57, 37-43, 1996. Namasivayam C, Radhika R, Suba S., Uptake of dyes by a promising locally available agricultural solid wastes: coir pith, Waste Management, 21, 381–7, 2001. Namasivayam C, Prabha D, Kumutha M, Removal of Direct Red and Acid Brilliant Blue by Adsorption on to Banana Pith, Bioresource Technology 64 (1), 77-79 (3), 1998. Nigam P, Armour G, Banat IM, Singh D and Marchant R, Physical removal of textile dyes and solid-state fermentation of dye-adsorbed agricultural residues, Bioresour. Technol. 72, 219– 226, 2000. Özacar M and Şengil İA, Adsorption of metal complex dyes from aqueous solutions by pine sawdust, Bioresour. Technol., 96(7), 791-795, 2005. Rita Kant and Rattan VK, Adsorption of dye Green B from a textile industry effluent using two different samples of activated carbon and static batch method and continuous process, Indian Journal of Chemical Technology, 16, 240-244, 2009. Seshdari S, Bishop PL and Agha AM, Waste Manag., 15,127, 1994. Sumanjit, Walia TPS, Kaur R., Removal of health hazards causing acidic dyes from aqueous solutions by the process of adsorption, Online J Health Allied Scs. 6, 3(3) 1-10, 2007. 1382 View publication stats