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A Study on the Physicochemical Characteristics of Tannery Effluent Collected from Chennai
1.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 03 | Mar-2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 6.171 | ISO 9001:2008 Certified Journal | Page 24 A study on the physicochemical characteristics of tannery effluent collected from Chennai M. Muthukkauppan1, P. Parthiban2 1,2Department of Chemistry, CRD, PRIST University, Tamilnadu, India ---------------------------------------------------------------------***--------------------------------------------------------------------- Abstract - In the present study, the tannery effluent collected from a tannery industry in Chennai was characterized for basic parameters. The effluent was grey colored with a disagreeable odor, acidic in pH, with high organic and inorganic load indicating high Electrical Conductivity (EC), Biological OxygenDemand(BOD),Chemical Oxygen Demand (COD), Total Dissolved Solids (TDS), total hardness, chlorides and sulphates. The physicochemical parameters were, determined as per the standards prescribed by Bureau of Indian Standards (BIS). Key Words: Tannery effluent BOD, COD, TDS 1. INTRODUCTION Tannery effluent is one of the most polluting industrial wastes. Leather production requireslarge amount ofwater- 35 liters of water is consumed per kilogram of raw material processed. The effluent generated by tannery is estimatedat about 75,000m3/day (1). For processing 7,00,000 tons of hidesand skins per annum, about 4,00,000 tonsofchemicals are needed. Not more than 20% of the chemicals are absorbed by leather; the remainder flows out with the effluent. Effluent from tannery is the most polluting and has high concentration of proteins, chlorides, trivalent chromium, nitrogen, sulphate, sulphides, COD, BOD and suspended solids (2). Volume and characteristics of wastewater discharged vary from processto process, tannery to tannery and from time to time. The operations in a tannery are done in batches and discharge of wastewater is intermittent. Wastewater from beam house operations like soaking, liming, deliming, bathing etc., is alkaline and contains decomposable organic matter, hair, lime,TSS,TDS,sulphides and BOD. This is mainly due to the poor quality of calcium hydroxide and other chemicals used in excess without proper control. The major public concern over tanneries has traditionally been about odours and water pollution from untreated discharges. Other issues have arisen more recently from the increasing use of synthetic chemicals such as pesticides, solvents, dyes, finishing agents and new processing chemicals, which introduce problems of toxicity and persistence. The present study on the tannery effluent from a tannery industry in Chennai was aimed to analyse the characteristics of the effluent as per the standards of BIS, and to study the nature of pollutants present in the effluent. 2. MATERIALS AND METHODS 2.1 Sample Collection The effluent was collected from a tannery at Chennai, Tamil Nadu, India. The tannery is producing semi-finished tanned leathers. The effluent samples from the raw composite stream were collected in a two litre polythene containers and were brought to the laboratory with due care. 2.2 Physico Chemical Characterization of Tannery Effluent The physicochemical parameters of the effluent such as color, odor, pH, Electrical Conductivity (EC), Total Dissolved Solids (TDS), Total Hardness, Biological Oxygen Demand (BOD), Chemical Oxygen Demand (COD), Sulphates and chlorides were determined as per the standards prescribed by Bureau of Indian Standards (BIS). Color Color is measured by visual comparison of the sample. Odor The sample was filled half the volume of a wide mouthed stoppered bottle, closed, shake vigorously for 5seconds,and then quickly observe the odor. The true odorofthesampleat the mouth of the bottle was recorded as agreeable or disagreeable. pH After calibrating, the instrument with a buffer solutionofpH near that of the sample was checked as per the instructions. Electrical Conductivity Reagents: Standard potassium chloride solution: Dissolve 0.7456 g of anhydrouspotassium chloride (0.01N) in distilledwaterand make up to 1000ml at 25 °C. The specific conductance ofthis solution at 25°C is 1,408 μs/Cm. Procedure: About 50 ml of standard potassium chloride solution was taken and measured the electrical conductivity at room temperature for calibration. After calibration, 50 ml of the effluent sample was analyzed for the electrical conductivity and expressed as μs/Cm.
2.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 03 | Mar-2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 6.171 | ISO 9001:2008 Certified Journal | Page 25 Total Dissolved Solids The evaporating dish washeated in an oven at 180°Cforone hour, cooled in the desiccators, weighed and stored in the desiccators. A 100 ml of the sample was filtered using pre- weighed Whatmann No.40 filter paper and the weight of the filterable residue was determined. Pipette the 100 ml of sample on to a pre-weighed evaporatingdishandplacedona hot air oven. After complete evaporation of water from the residue, the evaporating dish is removed and weighed after cooling in desiccator. Total Hardness Principle: Eriochrome black –T dye when added to water containing calcium and magnesium solution becomes wine red at pH10.0 when this is titrated with EDTA calcium and magnesium will get complexed. At the end of complex formation, solution turns blue from wine red, which is indicated as the end point. Reagents: i) Patton and Reeder indicator solution: 1g of Patton and Reeder reagent was dissolved in 100 ml of distilled water EBT indicator: 0.5 g of EBT indicator and45g of hydroxylamine hydrochloride were dissolvedin100mlof spirit. ii) Standard calcium solution: 0.1 g of CaCO3 was dissolved in 100 ml of dil HCl (1ml = 0.4008 g of Ca). iii) Buffer solution: 70 g of Ammonium chloride was added to 570 ml of 30 % ammonium solution in water and make up to 1 liter using distilled water. iv) 1N Sodium hydroxide: 40 g of NaOH was dissolved in 1 litre of distilled water. v) 0.001M EDTA solution: 3.75 g of Disodium ethylenediamine Tetra-acetatedihydrate was dissolved in distilled water and make up to 1 liter. Procedure: To 25 ml of sample in 250ml conical flask, add 25 ml of distilled water, 10 ml of buffer solution and 5 drops of eriochrome black T. The mixture was titrated against EDTA solution till it turns from wine red to blue. ca equivalent to 1ml of EDTA solution was calculated. Biological Oxygen Demand Principle: The method consists of filling with sample, to overflowing, an airtight bottle of the specified size and incubating it atthe specified temperature for 3 days. Dissolved oxygen is measured initially and after incubation, and the BOD is computed from the difference between initial and final DO. Because the initial DO is determined shortly after the dilution is made, all oxygen uptakes occurring after this measurement is included in the BOD measurement. Reagents: i) Manganous sulphate solution: 480g of MnSO4.4H2O wasdissolved in distilledwater,filtered and make up to 1000ml. ii) Alkaline Iodide Solution: 500g of Sodium hydroxide and 135gmofsodiumiodidewere dissolved in distilled water and make up to 100ml. iii) Starch Indicator: 2g of Starch and 0.2g of salicylic acid were dissolved in 100ml of hot water. iv) Stock sodium thiosulphate solution: 25g of Sodium thiosulphate was dissolved in distilled water and make up to 1000ml 1.0g of sodium hydroxidewasadded as preservative. v) Standard sodium thiosulphate solution: 250ml of Stock solution was dissolved in distilled water and make up to 1000ml. Procedure: To the sample contained in 300ml BOD bottle, add 2 ml of manganese sulphates solution followed by 2 ml of alkaline iodide solution were added. The content was thoroughly mixed and allowed to precipitate to settle. After settling, the stopper was removed and 2ml of Conc. sulphuric acid was added through the sides. The stopper was replaced and the bottle was shaken thoroughly to dissolve the liberated iodine. 200ml of solution was titrated against sodium thio sulphate solution after adding 3-4 drops of starch indicator. End point is dark blue to colorless. The Procedure was done during 0 h of incubation and after 72 h of incubation. Chemical Oxygen Demand Principle: Most type of organic matter is oxidized by a boiling mixture of chromic and sulphuric acids. A sample is refluxed in a strongly acid solution with a known excess of potassium dichromate (K2Cr2O7). After digestion, the remaining unreduced K2Cr2O7 is titrated with ferrous ammonium sulphate to determine the amount of K2Cr2O7 consumed and the oxidisable matter is calculated in terms of oxygen equivalent. Reagents: i) 0.25 N Standard potassium dichromate solution: 12.259 g of K2Cr2O7 was dissolved in distilled water and diluted to 1000ml.
3.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 03 | Mar-2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 6.171 | ISO 9001:2008 Certified Journal | Page 26 ii) Sulphuric acid reagent: 0.55 g of Silver sulphate was dissolved in 100 ml of conc. H2SO4. iii) Ferroin indicator solution: 1.485 g of 1,10-Phenanthroline monohydrate and 695 mgof FeSO4 . 7H2O were dissolved in distilled water and dilute to 100 ml. iv) 0.25 N Standard Ferrous Ammonium Sulphate (FAS): 98 g Fe(NH4)2 (SO4)2.6 H2O was dissolved in distilled water. 20 ml Conc. H2SO4 wasadded, cooled, and dilutedto1000ml. This solution was standardized against standard K2Cr2O7. v) Mercuric sulphate, (HgSO4) and vi) Potassium hydrogen phthalate (KHP) Procedure: Take 50 ml sample in a 250 ml BOD bottles. Add 1 g HgSO4 and very slowly add 5ml sulphuric acid reagent. 25 ml of 0.25 N K2Cr2O7 solutionwasadded and mixed. The flask was attached to condenser and turn on cooling water. Add remaining Sulphuric acid reagent (70 ml) to open end of condenser. Continue swirling and mixing while adding the sulphuric acid reagent. Disconnect reflux condenser and dilute mixture to about twice itsvolume with distilledwater. Cool to room temperature and titrate excess K2Cr2O7 with FAS, using ferroin indicator. Although the quantity offerroin indicator is not critical, use the same volume me for all titrations. The first sharp color change from blue green to reddish brown is considered as end point. The blue green may reappear. In the same manner, reflux and titrate a blank containing the reagentsand a volume of distilledwaterequal to that of sample. Sulphate Principle: Sulfate ion (SO4 2-) precipitated in acetic acid medium with barium chloride to form barium sulphate (BaSO4). Light absorbance of the BaSO4 suspension is determined and the sulphate ion concentration is determined by comparison of the reading with a standard curve. Reagents: i) Conditioning reagent 1: Added a 0.3g of gelatin in 100ml distilled water and warmed it on hot plate till it dissolves. Kept the gelatin solution for about 12 hrs,or overnight preferably at 4 °C. After bringing the solution to room temperature, 3.0g of barium chloride is added to gelatin solution and dissolvedbymixing.Theturbid solution is kept standing for 2 hrs and mixed before use. ii) Conditioning reagent 2: Mixed 50ml glycerol with a solution containing 30ml concentrated hydrochloric acid, 300ml distilled water, 100ml 95%ethyl /isopropyl alcohol and 75g of sodium chloride. iii) Stock sulphate solution: Dissolved 0.1479 g anhydrous sodium sulphate in distilled water and make up to 1 litre. (1ml = 0.1 mg SO4 2-). iv) Standard Sulphate solution: Prepared a seriesof standards by diluting the stock solution to cover the range 1 to 40 mg/l (5, 10, 20 and 40 mg/l). v) Hydrochloric acid (1:9) and, vi)Barium chloride crystals. Procedure: In 100 ml of sample 20 ml of conditioning reagent and a spatula of BaCl2 were added for 60 sec. The absorbance at 420 nm after 30 sec was noted. Chloride Principle: In a neutral or slightly alkaline solution,potassiumchromate can indicate the end point of the silver nitrate titration of chloride. Silver chloride is precipitated before red silver chromate is formed. Reagents: i) Potassium chromate indicator solution: Dissolved 50 g of Potassium chromate in a little distilled water. Silver nitrate solution was added until a definite red precipitate is formed. Let it stand for 12 hours, filter and dilute to 1 liter with distilled water. ii) 0.014 N Standard silver nitrate: Dissolved 2.395 g of silver nitrate in distilled water and diluted to 1 litre. iii) 0.0141 N Standard sodium chloride solution: Dissolved 824.0 mg of sodium chloride in distilledwaterand diluted to 1 litre. iv) Aluminum hydroxide suspension: Dissolved 1.25 g of aluminum potassium sulphatein1litreof distilled water. Procedure: Standardisation of silver nitrate: Pipetted out a 20 ml of standard sodium chloride and transferredintoaconicalflask and 1 ml of potassium chromate indicator solution was added. Titrated with silver nitrate solution to a pinkish yellow end point. Analysis of chloride: Took 100ml sample and 1 ml of potassium chromate indicator, titrated with standard silver nitrate solution to obtain a pinkish yellow end point. Parallely, performed a blank titration using water.
4.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 03 | Mar-2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 6.171 | ISO 9001:2008 Certified Journal | Page 27 3. RESULTS AND DISCUSSIONS 3.1 Physicochemical Characterization of Leather Effluent The physicochemical characteristics of the untreated tannery effluent have revealed that it is acidic, with high BOD, COD, organic particulate matter, unpleasantodourand colour. The raw effluent was observed with dark ash coloured, which might be derived from tanning processes. Unpleasant odour may be due to microbial growth or the decomposition of organic substance present in it (3, 4). The pH of the tannery effluent was highly acidic (5.8 to 6.6) and did not meet the general standards recommended by CPCB (1995) for the discharge of effluentsinto land or irrigational purpose. Discharge of such untreated effluents with such a low pH into ponds, rivers or on lands for have direct impact over zooplankton and fishes, since low pH level may affect the physiology of fishes (5). Electrical conductivity is a numerical expression of the ability of water sample to carry an electric current. The number depends on the total concentrations of the ionised substances dissolved in water and to the temperature at which the measurement is made. Theconductivityoftannery effluent in the present study was found tobeveryhighwhich may be due to the presence of inorganic substancesandsalts that show good conductivity (6). According to Kataria et al., (7) high electrical conductivity level may be due to higher concentration of acid-base and salt in water. Table -1: List of methods used for physicochemical characterization High level of total suspended solids present in the tannery effluent could be attributed to their accumulation during the processing of finished leather. Moreover, presence of total suspended solids leads to turbidity resulting in poor penetration of light inthe aquatic system, thereby affects the photosynthetic activity (3). Further the settlingofsuspended particleson soil and soil fauna,mightleadtovariousdamages like change in soil porosity, soil texture, water holding capacityononehand (8) and clogging ofgillsandrespiratory surfaces of fishes on the other hand (9). Biochemical Oxygen Demand is one of the important parameters used in water pollution studies to evaluate the impact of wastewaters on receiving waters. The present study has revealed the high levels of biological oxygen demand in the tannery effluents (793 mg/1) indicating high organic load. Present investigation is in agreement with the studies on tannery effluent (10), sugar mill effluent, sago effluent (4) and distillery effluent (11). According to Poole et al. (12), increase in BOD is a reflection of microbial oxygen demand, whichleadsto depletion ofdissolved oxygen.Under such a condition, no aquatic life can survive,exceptanaerobic microorganisms. Further, the presence oforganicmatterwill promote anaerobic action leading to the accumulation of toxic compounds in water bodies (3) Chemical Oxygen Demand is the best method for the determination of total oxygen demand by organic material present in the effluent. In the present investigation,highlevel of COD was recorded (2479 mg/L) which did not meet the standard prescribed by CPCB (1995) for effluent discharge into inland surface water (permissiblelimit:250mg/1).This indicates that the effluent is unsuitable for the existence of the aquatic organisms. Raj et al. (13) recorded higher values of COD for the treated tannery effluent of a tannery industry in Chrompet, Chennai. Ions, especially calcium, sulphate, magnesium and sodium impart hardness to water. The results revealed that the concentrations of ions were more than the prescribed limit by CPCB (1000mg/L). According to Lehr et al.(14),thewater is very hard if the value is beyond 180 mg/L. In the present study,the valuerangesnear 2870 mg/L, whichindicatedthat the water hardness was very high. Table -2: Physicochemical characterization of raw tannery effluent S.No. Characteristics Units Observations 1 Color - Grey 2 Odor - Disagreeable 3 pH - 0.8 4 EC µS/cm 12659 5 TDS mg/L 3059 6 BOD mg/L 895 7 COD mg/L 2381 8 Total Hardness mg/L 1460 9 Chlorides mg/L 1592 10 Sulphates mg/L 1338
5.
International Research Journal
of Engineering and Technology (IRJET) e-ISSN: 2395-0056 Volume: 05 Issue: 03 | Mar-2018 www.irjet.net p-ISSN: 2395-0072 © 2018, IRJET | Impact Factor value: 6.171 | ISO 9001:2008 Certified Journal | Page 28 High levels of chlorides in the tannery effluent could be attributed to the soaking process involved (15). More over high contentof ions,hardnesspresent in the tannery effluent might be due tomixingof tannery effluentswith the aqueous system from the different sources of processing within the tannery. The results of the present investigation revealed the acidic pH, increased total hardness, high TDS, BOD, and COD of the tannery effluent. The present study also revealed that, the tannery effluent was highly polluted and do not satisfy the prescribed limits of the CPCB (1995). Hence, it is imperative to adopt technologies that could reduce or degrade the tannery effluent effectively. According to McEldowney et al. (16), the most appropriate method for pollution control depends on various factors linked to the nature and type of pollution with environmental statutes, cost benefit analysis and commodity acceptance, Since no single technology can satisfy allthese requirements, combinedtreatmentstrategies could be an option. 4. CONCLUSIONS Tanning is an integral part of the process of converting raw hides and skins into finished leather. Tanning is a complicated and laboriousprocessthat caninvolveover130 different chemicals, depending on the type of raw material used and the finished product. In most developingcountries, tannery effluents are discharged into sewers or inland surface waters and/or brought onto the land with irrigation water. The high concentrations of solid substances such as chloride and sulphate salts as indicated by high total hardness, TDS, BOD, and COD in the tested tannery effluent will affect the quality of water and may cause bad taste and odor. Discharge of untreated tannery effluents into the sewer system causes deposition of calcium carbonate and choking of the sewer. Hence, a better approach than the traditional methods is to destroy the pollutantsif possible, or at least to transform them to innocuous substances is necessary. Bioremediation is an option that offers the possibility to destroy or render harmlessvariouscontaminantsoftannery effluent using natural biological activity, and therefore, further study is under progress using greener biomethod. REFERENCES (1) Sahasranaman,. A. and Buljan, J. (2000). Environment management in Indian tanneriesin 34th, LERIQ:27-30. (2) Kadam, R.V. (1990). Treatment of tannery wastes. Indian. J. Env. Prot., 10: 212-216. (3) Goel, P.K. (2000). Water pollution causes, effects and control. New Age International (P) Ltd., Publ. New Delhi. 269. (4) Panneerselvam, A. (1998). Studies on sago industry effluent and its bioremediation using the white rot fungus Phanerochaete chrysosporium (Thirds). Ph.D. Thesis, University of Madras. (5) Geetha, M. et al (1996). Effect of low pH on phosphates activity of a freshwater teleost fish Cyprinuscarpio.Ind. J. Environ. Prot., 17(1): 51-54. (6) Robinson, R.A. and Stokes, R.H. (1959). Electrolyte solutions. 2nd ed. V-Academic Press, New York. 466. (7) Kataria, H.O. and Jain, O.P. (1995). Physico-chemical analysis of river Ajnar. Ind. J. Environ. Prot. 12 (9): 64- 67. (8) Narasimha, G., Babu, G.V.A.K. and Reddy, B.R. (1999). Cellulolytic activity of fungal culturesisolated fromsoil contaminated with effluentscotton spinningindustry.J. of Environ. Biol., 20(3): 235-239. (9) Alabaster, J.S., and Llyod, R. (1980). Water quality criteria for freshwater fish, Butterworths. London. (10) Gokulakrishnan, K. (2003). A study on the solid and liquid waste treatment and disposal in the tanning industries of Tiruchirappalli. Ph.D. thesis. Bharathidasan University, Tiruchirappalli. (11) Prabakar, K. (1999). StudiesonBioremediationofsugar and distillery effluent. Ph.D. Thesis, University of Madras. (12) Poole, N.J., Wildish, D.J. and Kristmanson, D.D. (1978). The effects of the pulp and paper industry on the aquatic environment. Cur. Rev. Environ. Con., 8 : 153. (13) Raj, E.M., et al. (1996). Studies on treated effluent characteristicsof a few tanneries at Chrompet, Madras. Ind. J. Environ. Prot., 6: 252-254. (14) Lehr, J.H., Tyler, E.G., Wayne, A.P. and Jack, D. (1980). Domestic water treatment.McGrawHillBookCompany, New York. (15) Athappan, M., Sethuraman, P.R.K. and Kannan, N. (1992). A study on the pollution of river Vaigai at Madurai. Ind. J. Environ. Prot., 12: 818-823. (16) McEldowney, S., Hardman, D.J. and Waile. S. (1993). Pollution: Ecology and Bioreatment. Longman, Scientific and Technical Publ: 1-321. McGraw Hill Book Company, New York.
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