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1.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1775 TREATMENT OF SUGAR INDUSTRY WASTEWATER BY UPFLOW ANAEROBIC SLUDGE BLANKET REACTOR Saba Mohammad Ayub1, Rachana M Madiwalar2, Rohit I Gaddikerimath3, Soumya S Shingennavar4, Rahul. R. Bannur5 1,2,3,4B.E Student, Dept. of Civil Engineering, S.G. Balekundri Institute of Technology, Belagavi-590010 (Karnataka). 5Assistant Professor, Dept. of Civil Engineering, S.G. Balekundri Institute of Technology, Belagavi-590010 (Karnataka). ---------------------------------------------------------------------***---------------------------------------------------------------------- Abstract - In India we have about 380 sugar industries; also it is world’s second biggest sugar producer. The production of sugar was estimated to be around 26million tonnes and Indian sugar mills generate 0.16 to 0.76 m3 of wastewater for every tonne of cane crushed by them. The sugar industry wastewater contains high amount of COD, BOD, TS and pH which is highly acidic in nature. In present study a laboratory scale Hybrid Up flow anaerobic sludge blanket reactor was constructed for treating sugar industry wastewater by using polypropylene pall rings as filter media. The reactor is being operated at different hydraulic retention time that is 72, 64, 56, 48, 40, 32, 24, 16 and 8 hours. Also we aim to obtain the optimum HRT of the reactor. COD feed concentration was 5400mg/l and 78% of COD removal was achieved at 48hour HRT. Key words: BOD (Biochemical Oxygen Demand), COD (Chemical Oxygen Demand), TS (Total Solids), HRT (Hydraulic Retention Time). INTRODUCTION Sugar is made from sugarcane, and was discovered thousands of years ago in New Guinea. The route was then traced to India and Southeast Asia. India was the first to begin with the production of sugar following the process of pressing sugarcane to extract juice and boil it to get crystals. The government of India in 1950-51 made serious industrial development plans and has set many targets for production and consumption of sugar. These plans by the government projected the license and installment capacity for the sugar industry in its Five Year Plans. India is well known as the original home of sugar and sugarcane. India is the world's second biggest sugar producer. India's share in global sugar production in 2022 is forecast at 15 per cent at around 32 million tonnes. Sugar production in the period 2015-16 is estimated to be around 26million tonnes, about 2 million tonnes less than last year. The drop has been mainly due to extended dry weather in Maharashtra and Karnataka. Consumption in 2015-16 was estimated to be 25 MT. The country had produced 28.1MT of sugar in 2015. Maharashtra, the country's leading sugar producing state, has projected sugar output to decline to 8.6MT in the 2015-16.marketing year, compared with 10.5MT last year. In India there are about 380 sugar factories, of which 105 are in Uttar Pradesh. TABLE 1: EFFLUENT GENERATIONS IN VARIOUS, UNITS OF SUGAR FACTORY. Karnataka Sugar Industry ranks 3rd in terms of its contribution of sugar in the total sugar production in the country. Karnataka stands 4th in the country in the cultivation of sugarcane. The Sugar Industry in Karnataka has around 41 sugar factories which are distributed all over the state. Biological Wastewater Treatment Method. It is a process that seems simple on the surface since it uses natural processes to help with the decomposition of organic substances, but in fact, it’s a complex, not completely understood process at the intersection of biology and biochemistry. Biological treatments rely on bacteria, nematodes, or other small organisms to break down organic wastes using normal cellular processes. Wastewater typically contains a buffet of organic matter, such as garbage, wastes, and partially digested foods. It may also contain pathogenic organisms, heavy metals, and toxins. The goal of biological wastewater treatment is to create a system in which the results of decomposition are easily collected for proper disposal. Process Mill house Boiling house Boiler house(Blowdown) Pump cooling water Sulphur furnaces Lime hydrator Excess Condensate Final effluent Spray Pond over flow
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International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1776 Aerobic and Anaerobic In biological treatment processes, it is important to briefly discuss the terms aerobic and anaerobic. Aerobic, as the title suggests, means in the presence of air (oxygen); while anaerobic means in the absence of air (oxygen). These two terms are directly related to the type of bacteria or microorganisms that are involved in the degradation of organic impurities in a given wastewater and the operating conditions of the bioreactor. Therefore, aerobic treatment processes take place in the presence of air and utilize those microorganisms (also called aerobes), which use molecular/free oxygen to assimilate organic impurities i.e. convert them in to carbon dioxide, water and biomass. The anaerobic treatment processes, on other hand take place in the absence of air (and thus molecular/free oxygen) by those microorganisms (also called anaerobes) which do not require air (molecular/free oxygen) to assimilate organic impurities. The final products of organic assimilation in anaerobic treatment are methane and carbon dioxide gas and biomass. Hybrid Upflow Anaerobic Sludge Blanket(UASB) reactor Karnataka Sugar Industry ranks 3rd in terms of its contribution of sugar in the total sugar production in the country. Karnataka stands 4th in the country in the cultivation of sugarcane. The Sugar Industry in Karnataka has around 41 sugar factories which are distributed all over the state. Aerobic digester that combines a UASB reactor with anaerobic filters. This combination is an advanced form enabling improved solid retention time in the treatment of wastewater. This wastewater can be built up in the secondary chamber and must be removed daily or an explosion is imminent to occur. Upflow Anaerobic Sludge Blanket Reactor Wastewater Treatment is a wastewater treatment system using biology that without using of air or oxygen. It aimed to remove organic pollution in wastewater, slurries and sludge. Anaerobic microorganisms convert organic pollutants into a “biogas” which contains methane and carbon dioxide. Statement of Problem In India, sugar Industry is one of the major agro based industries. Treatment and safe disposal of sugar industry waste water has been cause of concern for many decades because of its high pollution potential. Anaerobic treatment has gained importance in better treatment of sugar industry wastewater. The sugar industry effluent contains high chemical oxygen demand (COD). As per central pollution control board (CPCB) the typical value for COD is 250mgL and pH of 5.5 to 9.0 for discharging the treated effluents to inland surface water. Considering all the problems above a low cost efficient treatment is essential for sugar industry. Objectives: Treatment of Sugar Industry wastewater by Upflow Anaerobic Sludge Blanket Reactor. a. To obtain the variation of BOD content with respect to different HRT at different levels. b. To obtain the variation of COD with respect to different HRT at different levels. c. To obtain the variation of pH with respect to different HRT at different levels. d. To obtain the variation of Total Solids with respect to different HRT at different levels. e. To obtain the optimum Hydraulic Retention time (HRT). Fabrication of Materials A laboratory scale Upflow Anaerobic sludge blanket reactor was fabricated. The overall height of the reactor is 1220mm. The effective volume of the reactor is 18.2 liters and the effective height is 1070mm with a free board of 75mm. A 10% of fresh cow dung slurry was seeded to the reactor to generate bacteria in it. Sampling ports were given to the reactors as shown in the figure. The sampling ports were fixed at various levels 25 %, 50 % and 75 % of overall height of the reactor and they are placed at 75mm from top as well as 75mm distance from bottom to arrest the packing material and reduce the choking problems at inlet as well as outlet. Packing material According to literature review and previous studies use of packing materials has proven to be more efficient for treatment of wastewater. We have selected Polypropylene pall rings as packing material for the present study. The diameter of pall rings is 20mm and height is 14mm. Details of the reactor Table 2: Design details of UASB Reactor Total height 1220mm Effective height 1145mm Inner diameter 142.4mm Outer diameter 150.4mm Thickness 4mm Diameter of Pall rings 20mm Height of Pall rings 14mm
3.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1777 Fig 1: Schematic Diagram of UASB Reactor Results: 1) Parameters at 100% level of reactor Table 3: 100% level HRT in Hours pH TS in mg/l COD in mg/l BOD in mg/l 72 6.5 320 5250 1440 64 6.6 390 4980 1410 56 6.53 650 4880 1355 48 8.8 790 4520 1300 40 8.6 780 4690 1290 32 7.6 760 4820 1360 24 6.3 690 4940 1390 16 6.53 750 5100 1420 8 6.59 780 5200 1440 Chart 1.1: BOD AT 100% LEVEL Chart 1.2: COD AT 100% LEVEL Chart 1.3: TS AT 100% LEVEL Chart 1.4: pH AT 100% LEVEL 1200 1300 1400 1500 8 16 24 32 40 48 56 64 72 BOD(mg/L) HRT(hrs) BOD at 100% level BOD at 100% level 4000 4200 4400 4600 4800 5000 5200 5400 8 16 24 32 40 48 56 64 72 COD(mg/L) HRT (hrs) COD AT 100% LEVEL COD at 100% level 0 100 200 300 400 500 600 700 800 900 8 16 24 32 40 48 56 64 72 TS(mg/L) HRT(hrs) TS AT 100% LEVEL TS at 100% level 0 1 2 3 4 5 6 7 8 9 10 8 16 24 32 40 48 56 64 72 pH HRT (hrs) pH AT 100% LEVEL ph
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International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1778 2) Parameters at 75% level of reactor Table 4: 75% LEVEL Chart 2.1: BOD AT 75% LEVEL Chart 2.2: COD AT 75% LEVEL Chart 2.3: TS AT 75% LEVEL Chart 2.4: pH AT 75% LEVEL 3) Parameters at 50% level of reactor Table 5: 50% LEVEL 0 200 400 600 800 1000 1200 1400 1600 8 16 24 32 40 48 56 64 72 BOD(mg/L) HRT BOD AT 75% LEVEL BOD AT 75% level 0 1000 2000 3000 4000 5000 6000 8 16 24 32 40 48 56 64 72 COD(mg/L) HRT(hrs) COD AT 75% LEVEL COD at 75% level 0 200 400 600 800 1000 8 16 24 32 40 48 56 64 72 TS(mg/L) HRT (hrs) TS AT 75% LEVEL TS at 75% level 0 2 4 6 8 10 8 16 24 32 40 48 56 64 72 pH HRT (hrs) pH AT 75% LEVEL Ph HRT in Hours pH TS in mg/l COD in mg/l BOD in mg/l 72 6.51 380 5100 1420 64 6.56 450 4800 1350 56 7.41 580 4580 1300 48 9 780 4200 1100 40 8.4 760 4320 1150 32 7.9 780 4825 1260 24 7.45 750 4980 1290 16 7.44 740 5000 1340 8 6.5 740 5400 1390 HRT in Hours pH TS in mg/l COD in mg/l BOD in mg/l 72 6.57 360 5200 1421 64 6.74 420 4850 1400 56 7.5 529 4600 1360 48 8 723 4450 1150 40 7.9 720 4700 1200 32 7.51 712 4835 1245 24 7.3 720 4980 1380 16 6.7 722 5150 1445 8 6.4 725 5120 1488
5.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1779 Chart 3.1: BOD AT 50% LEVEL Chart 3.2: COD AT 50% LEVEL Chart 3.3: TS AT 50% LEVEL Chart 3.4: pH AT 50% LEVEL 4) Parameters at 25% level of reactor Table 6: 25% LEVEL Chart 4.1: BOD AT 25% LEVEL Chart 4.2: COD AT 25% LEVEL 0 500 1000 1500 2000 8 16 24 32 40 48 56 64 72 BOD(mg/L) HRT BOD AT 50% LEVEL 50 4000 4200 4400 4600 4800 5000 5200 5400 8 16 24 32 40 48 56 64 72 COD(mg/L) HRT(hrs) COD AT 50% LEVEL COD at 50% level 0 500 1000 8 16 24 32 40 48 56 64 72 TS(mg/L) HRT (hrs) TS AT 50% LEVEL TS at 50% level 0 2 4 6 8 10 8 16 24 32 40 48 56 64 72 pH HRT (hrs) pH AT 50% LEVEL Ph 1100 1150 1200 1250 1300 1350 1400 1450 1500 8 16 24 32 40 48 56 64 72 BOD(mg/L) HRT (hrs) BOD AT 25% LEVEL BOD AT25% LEVEL 4000 4200 4400 4600 4800 5000 5200 5400 8 16 24 32 40 48 56 64 72 COD(mg/L) HRT(hrs) COD AT 25% LEVEL COD at 25% level HRT in Hours Ph TS in mg/l COD in mg/l BOD in mg/l 72 6 360 5320 1459 64 6.5 400 4900 1440 56 6.59 426 4720 1410 48 8.9 489 4500 1300 40 8.5 478 4650 1245 32 7.2 467 4780 1266 24 6.9 472 4950 1392 16 6.69 480 5100 1430 8 6.44 495 5200 1436
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International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1780 Chart 4.3: TS AT 25% LEVEL Chart 4.4: pH AT 25% LEVEL Conclusions The industrial wastewater was treated itself repeatedly in UASB Reactor, which means it involves simple, reliable, biological process. The UASB Reactor works in anaerobic condition. Handling of the excess sludge is not a problem because the amount of sludge produced can be utilized. Therefore, the proposed biological treatment process appears to be promising wastewater treatment with respect to the removal of COD and BOD. From our results at 75% level of reactor we observed that: COD is reduced from 5400 mg/l to 4200 mg/l at 48 hours of HRT. BOD is reduced from 1500 mg/l to 1100mg/l at 48 hours of HRT. pH is increased from 6.37 to 9 at 48 hours of HRT. TS is increased from 300mg/l to 780mg/l at 48 hours of HRT. Hence optimum HRT of UASB Reactor is 48 hours. The efficiency of COD removal is 78%, and BOD is 73%. Hence the sugar industry wastewater can be efficiently treated by UASB Reactor. Scope for future study In future this reactor can be studied: By changing the filter media. By changing wastewater. By providing a mesh to separate the levels. By varying the HRT. By varying the dimensions of the reactor. By varying the parameters of the reactor. By varying the concentration of the reactor. REFERENCES 1. Hampannavar, Shivyogimath.C.B; “Anaerobic treatment of sugar industry wasterwater by upflow anaerobic sludge blanket reactor at ambient tempreture”. Research schoolar basaweshwar engineering collage bagalkot, Karnataka. 2. K.Kaviyarasan; “Application of uasb reactor in industrial wastewater treatment – a review” international journal of scientific & engineering research, volume 5, issue 1. (2014) 3. Herbert H.P fang and H.K chui, “Maximum cod loading capacity in uasb reactor at 37⁰c”. 4. A.S.Tanksali, “Treatment of sugar industry wastewater by upflow anaerobic 9osludge blanket reactor” Bldea’s V.P.P.G.H college of engineering and technology,bijapur, karnataka,india. Corres.Author: anutanksali@gmail.Com, 5. Hina rizvi, Nasir Ahmad, Farhat Abbas, “UASB reactor treating municipal wastewater”. Arabain journal of chemistry.(2015) 6. P. Araya, G. Aroca, Rchamy. “Anaerobic treatment of effluent from an industrial polymer synthesis plant” 7. Arvind Kumar Mungray and Pradeep Kumar “Fate of anionic surfactant in 38m/day USAB based municipal wastewater treatment plant” Indian institute of technology, Roorkee india (2009) 8. Anupam Kumar Verma “Characterization of sewage and design of a UASB reactor for its treatment” -Sanjy Gandhi Postgraduate Institute of Medical Science, Lucknow, India Siddhant Kumar- southwest national private researchcentre, texas biomedical research centre(2013) 9. Herbert H. P. Fang; “UASB treatment of wastewater with concentrated mixed VFA” (volatile fatty acid) 10. K.Karthikeyan, j.Kandasamy “Upflow Anaerobic Sludge Blanket (UASB) reactor in wastewater treatment” -associate professor, school of civil and enviengineering (2009) 11. Eliasroza –Floresyear “Biodegradation of mixture of phenolic compounds in an UASB sludge blanket reactor ”(1996) 12. Prasad Gaikwad, Pradip Borate, Pratish Kate, Vishal Borawake, Anand Raut, prof Bansode S.S “Anaerobic lagoon treatment for sugar industries wastewater” (2016) 0 200 400 600 8 16 24 32 40 48 56 64 72 TS(mg/L) HRT (hrs) TS AT 25% LEVEL TS at 25% level 0 2 4 6 8 10 8 16 24 32 40 48 56 64 72 pH HRT (hrs) PH AT 25% LEVEL Ph
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International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 06 Issue: 09 | Sep 2019 www.irjet.net p-ISSN: 2395-0072 © 2019, IRJET | Impact Factor value: 7.34 | ISO 9001:2008 Certified Journal | Page 1781 13. Sowmeyan “Treatment of sugar industry wastewater by anaerobic method” –Periyar Maniammai University, tamilnadu, india, swaminathan-indian geneticist and informational administrator(2007) 14. Saurabh Saini “Assement of physico-chemical characteristics of sugar industry effluents” - international institute of information technology,hydrabad, shailja pant-departmental of microbiology, dolphin(p.G) institute of biomedical and natural science, mandvalladehradun, india(2014 15. K. S. Jayantha,t. K. Ramanujam chemical engineering department,indian institute of technology madras, india. “Start-up criteria for A upflow anaerobic sludge blanket (UASB) reactor” 16. E.V.Ramasamy centre for pollution control and energy technology, pondicherry university, kalapet, pondicherry 605 014, india, S.Gajalakshmi, R.Sanjeevi, M.N.Jithesh, S.A.Abbasi.“Feasibility study on the of treatment on dairy wastewater with upflow anaerobic sludge blanket reactor”. 17. Y.Saatciae.I.Arslanav.Konarb Department of environmental engineering, university of firat, elazig 23119, turke department of biology, university of firat, elazig 23119, turkey. “Removal of total lipids and fatty acids from sunflower oil factory effluent by UASB reactor” 18. .Molder and blonskaya (1999)“treatment of organic matter using UASB reactor”. 19. Chinnaraj and venkoba rao (2006) “ implementation of an UASB anaerobic digester at bagasse based pulp and paper industry”. 20. Bodik ;(2000) “anaerobic treatment of the municipal wastewater under psychrophilic conditions” BIOGRAPHIES Saba Mohammad Ayub is B.E. Student, Dept. of Civil Engineering in S.G. Balekundri Institute of Technology, Belgavi 590010, Karnataka India. Rachana M Madiwalar is B.E. Student, Dept. of Civil Engineering in S.G. Balekundri Institute of Technology, Belgavi 590010, Karnataka India. Rohit I Gaddikerimath is B.E. Student, Dept. of Civil Engineering in S.G. Balekundri Institute of Technology, Belgavi – 590010, Karnataka India. Soumya S Shingennavar is B.E. Student, Dept. of Civil Engineering in S.G.Balekundri Institute of Technology, Belgavi – 590010, Karnataka India. Prof. Rahul R Bannur is working as Assistant Professor, Dept. of Civil Engineering in S.G. Balekundri Institute of Technology, Belgavi – 590010, Karnataka India.
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