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三氯氢硅生产废水资源化回收工艺探索

Process Exploration of Resource Recovery of Trichlorohydrosilicon Production Wastewater
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摘要 三氯氢硅生产过程中产生一股酸性废水,其酸度约为2%,直接中和处理不仅成本高,且形成的高盐废水仍需进一步处理。本研究探索基于酸资源回收、水资源回用的“扩散渗析+特种耐酸膜回收+清液中和回用”的工艺,可有效降低企业的经营成本。研究表明:扩散渗析可将废水酸浓度由2%浓缩至8%,作为盐酸解析单元的原料;扩散渗析产生的淡水酸浓度约为0.5%,经特种耐酸膜装置进一步浓缩后,浓度提高至2%,返回扩散渗析进水单元和原水混合;特种耐膜装置产生的清液酸浓度<0.05%,通过中和后,TDS(Total Dissolved Solids)不高于500 mg·L^(-1),可作为循环水补水。 The production process of trichlorohydrosilicon produces a stream of acidic wastewater with an acidity of about 2%,which is not only costly to treat by direct neutralisation,but also requires further treatment of the high-salt wastewater formed.The study explores the process of‘Diffusion Dialysis+Special Acid Resistant Membrane Recovery+Clear Liquid Neutralisation and Reuse’based on the recovery of acid resources and reuse of water resources,which can effectively reduce the operating costs of enterprises.Research shows that:diffusion dialysis can concentrate the acid concentration of wastewater from 2%to 8%,as the raw material of hydrochloric acid resolution unit;the acid concentration of fresh water produced by diffusion dialysis is about 0.5%,and the concentration is increased to 2%by further concentration of special acid-resistant membrane device,which is returned to diffusion dialysis influent unit and mixed with the raw water;the acid concentration of the clear liquid produced by the special acid-resistant membrane device is less than 0.05%.After neutralisation,the TDS(Total Dissolved Solids)is not higher than 500 mg·L^(-1),which can be used as circulating water make-up water.
作者 韩颖 张威 Han Ying;Zhang Wei(WELLE Environmental Group Co.,Ltd.,Changzhou 213125,China)
出处 《广东化工》 CAS 2024年第11期112-114,共3页 Guangdong Chemical Industry
关键词 三氯氢硅 酸性废水 扩散渗析 酸回收 水回用 Trichlorohydrosilicon acidic wastewater diffusion dialysis acid recovery water reuses
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  • 1李秀华,宋明霞,代罡.氯化氢生产工艺探讨[J].中国氯碱,2004(8):15-16. 被引量:9
  • 2张开仕,曾凤春.聚合硫酸铁铝的制备及混凝效果研究[J].无机盐工业,2005,37(10):44-46. 被引量:12
  • 3王小辉,何佳华.三氯氢硅合成炉尾气的治理[J].中国氯碱,2007(6):39-40. 被引量:9
  • 4傅积责.化工百科全书:有机硅化物[M].北京:化学工业出版社.1994:370.
  • 5周本省.工业水处理技术[M].3版.北京:化学工业出版社,2003.16.
  • 6Hoel J O, Rong H M, Roe T, et at. Method for production of the tri- chlorosilane and silicon for use in the production of trichlorosilane : US,7462341 [ P]. 2008 - 12 -09.
  • 7Anderson G J, Hoel J O, Oye H A. Reactor studies of the trichlo- rosilane process[ C ]//Silicon for the Chemical Industry V 2000, Troms o : Quebec : INFACON Nine ,2001 : 193 - 202.
  • 8Hiroyuki O. Method of producing trichlorosilane having a reduced content of diehlorosilane : US ,5869017 [ P~. 1999 - 02 - 09.
  • 9Andreas B, Rainer W, Hans D B. Method for producing trichlorosi- lane : US ,7056484 [ P]. 2006 - 06 - 06.
  • 10若松智.リクロロミテソ類の回收方法:JP,029428[P].2005-02-03.

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