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Recycling of wastewaters of textile dyeing industries using advanced treatment technology and cost analysis - Case studies

机译:使用先进处理技术和成本分析的纺织印染废水回收利用-案例研究

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Textile dyeing industries in Tirupur and Karur of Tamil Nadu (India) usually discharge effluents ranging between 80 and 200 m(3)/t of production. Dyeing is performed either by conventional winch process or by advanced soft flow reactor process. Hypochlorite, the commonly used bleaching chemical is being gradually phased out by alkaline hydrogen peroxide solution that generates less effluent and fewer solids in the effluents. Coloring of yarn/cloth takes place in the presence of high concentration of sodium chloride or sodium sulphate (25-75 kg/m(3)) in dye solutions. Dye bath wastewaters and wash waters are the process effluents of dyeing industry which are collected separately or together and follow the advanced treatment for maximum recycling of recovered waters. Dye bath water after treating by sand and nanofiltrations (N-F), the permeate is used in process for dye bath preparation and the reject of about 20-30% is sent to multi effect evaporator (MEE)/solar evaporation pond (SEP). Wash waters treated using a sequence of physicochemical and biological unit processes are passed into two stages reverse osmosis (RO) membrane systems and then the permeate is reused in the processes. The rejects about 15-20% of the inlet volume is subject either to nanofiltration for salt recovery or sent to evaporators. The final rejects from nanotilter systems is directed to multi effect evaporator system where condensed waters are recovered. The removal of total dissolved solids (TDS), chemical oxygen demand (COD), chloride and sodium are in the range of 80-97%, 91-97%, 76-97% and 96%, respectively. Multiple effect evaporators out flows of about 2-3% of the effluent volume are allowed for solar evaporation and the solids are disposed off. The cost of operation of MEE is about INR 400/m(3) of the rejects. The cost of water recovery is about INR 60-80/m(3) including commissioning and maintenance whereas price of raw-water in Tirupur is about INR 100/m(3). (c) 2006 Elsevier B.V. All rights reserved.
机译:泰米尔纳德邦(印度)的蒂鲁普和卡鲁尔的纺织品染色工业通常排出的废水量为80至200 m(3)/ t。染色可以通过常规绞盘工艺或通过先进的软流反应器工艺进行。次氯酸盐,一种常用的漂白剂,正在被碱性过氧化氢溶液逐步淘汰,碱性过氧化氢溶液在废水中产生的废水更少,固体也更少。纱线/布料的染色是在染料溶液中存在高浓度氯化钠或硫酸钠(25-75 kg / m(3))的情况下进行的。染浴废水和洗涤水是印染工业的过程废水,它们分别或一起收集,并经过高级处理,以最大程度地回收利用回收的水。经过沙子和纳米过滤(N-F)处理后的染料浴水,渗透液用于染料浴的制备过程,约20-30%的废料被送到多效蒸发器(MEE)/太阳能蒸发池(SEP)。使用一系列物理化学和生物单元过程处理过的洗涤水进入两个阶段的反渗透(RO)膜系统,然后将渗透物重新用于过程中。约15-20%入口体积的废品需进行纳滤以回收盐分或送入蒸发器。来自纳米倾斜器系统的最终废品被引导至多效蒸发器系统,在该系统中回收冷凝水。总溶解固体(TDS),化学需氧量(COD),氯化物和钠的去除率分别为80-97%,91-97%,76-97%和96%。允许多效蒸发器流出约2-3%的废水,以进行太阳能蒸发,并将固体清除掉。 MEE的运营成本约为400卢比/ m(3)废品。包括调试和维护在内的水回收成本约为60-80印度卢比/ m(3),而蒂鲁普的原水价格约为100印度卢比/ m(3)。 (c)2006 Elsevier B.V.保留所有权利。

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