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The document discusses establishing a zero discharge system for treating textile effluent. Key points include: - Zero discharge means recovering all process water for reuse with no effluent discharge. - Design considerations include effluent quantity/quality variation, suitable unit processes, and durability. - Textile effluent is characterized by high BOD, COD, TDS, and trace metals from chemicals used. - A zero discharge system requires assessment, pilot testing, pipeline design, and handling abnormal situations. - Processes include primary treatment to remove solids, biological treatment using MBRs, and secondary treatment using reverse osmosis. - Tertiary treatment uses evaporation to
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- 1. Zero Discharge Possibility in Textile Processing Industry
- 2. Introduction Zero discharge implies that the process water utilized in pretreatment, bleaching and dyeing operations is recovered for reuse to an extent that there is no discharge of effluent into the environment.
- 3. Design Considerations 1. Quantity of the effluent to be treated. 2. Variation of quantity and quality with time 3. Unit processes suitable for achieving desired purposes for the given effluent. 4. The upper and lower limits of performance of each unit process. 5. The durability of the system to be adopted. 6. The feasibility of establishing suitable collection and conveyance system
- 4. Qualitative Analysis of Textile Effluent • Typical BOD5 : COD values lie between 1:2.5 and 1:5. • Organic load from pretreatment: BOD5 values: Desizing - up to 140 kg O2 per tonne of material alkaline boiling out of polyester – cotton blend fabrics - 210 kg/t. • High COD values because of the organic or inorganic reducing agents used. • High TDS due to large quantities of salts used in dye baths • Trace metals like Cu, Zn, Pb, Ni, Cd (few μgrams per gram) • Chemicals : wetting agents, soda ash, peroxides, bleaching powder, common salt, acids, dye stuffs, soap oil and, fixing and finishing agents
- 5. Characteristics of effluents from different sectors of textile industry Characteristics Cotton Synthetic Wool Scouring pH 8-12 7-9 3-10 BOD 150-750 150-200 5000-8000 COD 200-2400 400-650 100000-200000 Alkalinity 180-7300 550-630 80-100 Phenol 0.03-1 - - Oils and Grease 4.5-30 - 2000-2500 SS 35-1750 50-150 5000-6000 TDS 2100-7100 1060-1080 100000-130000
- 6. Requirements to establish a zero discharge system 1. Assessment of existing treatment based on available information 2. The chosen treatment system i) should be able to produce effluent with desired quality ii) should not produce any harmful substances on its own. 3. Conduct pilot plant test runs 4. Full-scale design should only be based on the combined effluent characteristics of all member units. 5. Pipeline design for effluent transport and return of treated effluent to the member units from the CETP
- 7. 6.Identification of processes that generate the effluent alongwith the chemicals and their quantities utilized 7. Listing energy conserving measures to reduce operating costs. 8. Conducting levelling survey is very much essential to design the pipeline – both for implementing gravity flow as well as for pumped flow. 9. The system should consider ways of handling undesirable situations : i) feed with undesirable quality, ii) power failure, iii) periods of maintenance iv) flooding.
- 8. Collection and Conveyance 1. Available location for the treatment facility, extend of land available, and the possibility for further expansion 2. Levelling survey to estimate the latitude, longitude and, height of each member unit and that of the proposed CETP 3. Estimation of quantity of effluent generated per day in each member unit 4. Estimating the available storage capacity of effluent storage tanks at each member unit 5. Provision for removal of debris, grits, and suspended solids should be given at each member unit
- 9. 6. Capacity of the pipeline material to withstand the temperature range of effluent 7. Durability of the material of construction of the pipeline. 8. Proposed pipeline route with a list of existing natural and man-made impediments 9. Accessibility to road, availability of electric power, provision for secured landfill, proximity to urban population and archaeological treasures 10. Implementation of gravity flow and/or pumped flow depending on the prevailing environmental conditions.
- 10. Treating Segregated and Combined Raw Effluent 1. Treating only the quantity of effluent generated in that process. 2. Due to segregation, each type of effluent has to be stored in separate tanks at each member units, and passed through a separate pipeline to the CETP. 3. Employment of different unit processes and equipments 4. As the temperature of the dye bath is around 70-80°C, it takes more time for natural cooling when compared with combined raw effluent.
- 11. 5.The organics content of the recovered water utilizing combined raw effluent is comparatively lower than in the case of segregation. 6. When dye bath is directly treated with an evaporator there might be a problem in colour removal since chlorine is used. The only disadvantage with handling combined raw effluent is that a large volume has to be handled. However, considering the benefits, it is always desirable to treat combined raw effluent instead of engaging segregation.
- 12. Unit Processes 1. Removal of grits and suspended solids 2. Removal of oil & grease 3. Equalization 4. Adjustment of pH 5. Reduction of BOD/COD 6. Removal of colour 7. Recovery of reusable water 8. Treatment of reject (from reverse osmosis system/blow out from evaporator) 9. Solid waste disposal and management.
- 14. 1. Removal of grits and suspended solids 2. Removal of oil & grease 3. Equalization 4. Adjustment of pH 5. Reduction of BOD/COD 6. Removal of colour
- 15. Selection of Biological Process: i) Simple Aeration ii) Activated Sludge Process with/without aeration iii) Aerobic/anaerobic digestion with Fluidised Bed Bioreactor (FBBR) iv) Membrane Bioreactor (MBR)
- 16. Problems associated with Conventional Biodegradation Process 1. Most dyestuffs are non-biodegradable 2. High TDS (8000-10000ppm) retards microbial growth 3. Low F/M ratio 4. Low biological activity 5. Different biodegradability of different dye stuffs 6. Higher sludge production 7. Inefficient nutrient removal from raw effluent which encourages microbial growth on RO membrane used in secondary treatment
- 17. Membrane Bioreactor Involves conventional activated sludge process with the use of ultrafiltration or, microfiltration membrane which helps to maintain higher levels of MLSS concentration
- 18. Retention of active microorganisms, extra cellular enzymes generated by these micro- organisms for degradation of the organics present in the effluent, organics resulting from cell-lysis, and other heavy molecular weight organics typical of textile effluent. Thus, overall efficiency of BOD-COD removal is increased
- 19. Submerged MBRs are generally used in textile waste-water treatment. It incorporates two zones: 1. Anoxic 2. Aerobic
- 20. Advantages: 1. Reduces the foot print 2. Improves BOD/COD reduction 3. Eliminates the need for a secondary clarifier 4. Removes suspended solids 5. Gives uniform output of effluent 6. Can be operated at higher MLSS concentration 7. Reduces shocks Disadvantage: High capital investment
- 21. Removal of colour and turbidity: 1. Chlorination 2. Ozonation 3. Activated Carbon Filter (ACF) 4. Pressure Sand Filter (PSF) and ACF used to remove turbidity
- 23. Secondary Treatment Generally reverse osmosis membranes are employed
- 24. Design Considerations 1. Should be able to operate with the desired TDS level typical of the effluent. 2. Should be able to withstand membrane scaling caused by various constituents in the effluent. 3. It is essential to utilize highly optimized system in place. 4. In order to reduce membrane fouling and backwash frequency, fouling resistant membranes may be utilized. 5. Mixing desired quantity of permeate with the feed and recirculating it through the membrane system is another option to maintain system performance.
- 26. Tertiary Treatment Objective of a tertiary treatment system is to treat the reject generated by the reverse osmosis system. The tertiary system employs an evaporator that utilizes steam as heating source, produces reusable water in the form of condensate, and generates blow down and salt as by products.
- 27. Design Considerations 1. For good maintenance, an evaporator has to be cleaned regularly. 2. The design of secured landfill should take into account disposal of the salt recovered from the evaporator. 3. The evaporator design should consider utilization of waste heat from the steam. 4. The blow down from evaporator has to be treated with a solar evaporation pond.
- 29. Tirupur Textile industry: An Overivew • Leading cotton knitwear industrial cluster • Favorable climatic conditions • Experienced rapid growth in the last two decades Operation of textile industry No. of units Knitting and stitching 4900 Dyeing and bleaching 736 Printing 300 Embroidery 100 Other 200 TOTAL 6250
- 30. Issues • Ground water quality in Tirupur was significantly affected due to the discharge of large quantities of textile dye effluent into the Noyyal river • Contamination of Orathupalayam Dam causing serious environmental degradation in the downstream areas of Erode and Karur.
- 31. Observations and Measures • Treated effluent regularly analysed for : pH, TSS, TDS, COD, BOD, Chloride, Sulphate, and trace metals • Found that the TDS levels in Noyyal is now oscillating in the range of 3,400 to 4,200 ppm • Attempts were made to evaporate the effluent using solar energy
- 32. • Trials conducted for implementing reverse osmosis system • Pilot study was carried out for a week using Vibratory Shear Enhanced Process (VSEP) reverse osmosis • Produced reusable water with a Total Dissolved Solids (TDS) < 500 mg/L • Also, eliminates chemicals in the pretreatment process
- 35. Present scheme of effluent treatment at MPCETP, Tirupur • Raw effluent passed to equalization tank ▫ Aeration • Clariflocculator ▫ Sludge to evaporation Ponds ▫ Treated effluent to sand bed
- 36. Implementation of Zero-Discharge a)Reverse Osmosis (R.O) system for treating 2000 m/day of textile dye effluent for recovery of pure water for reuse in textile wet processing. b)Nano-Filtration (N.F) assembly for salt recovery from R.O. reject and its reuse in dyeing/other industries. c)Multiple Effect Evaporator for recovery of reusable water from 200 m/day of reject from nano filtration assembly.
- 37. d) Solar pond for evaporation of mother liquor from Multiple Effect Evaporator, and separation of salts. e) Windmills for power generation to cater to the needs of the reverse osmosis, nanofiltration, and other electrical appliances of the Common Effluent Treatment Plant In addition, currently existing private forest of 5 acres will be expanded to 20 acres in order to promote environmental benefits.
- 38. Thank You