集成膜工艺处理碱减量废水及回用
周慧婷, 杜春慧, 吴春金, 吴礼光
浙江工商大学环境科学与工程学院, 杭州310018
Treatment and reuse of alkali reduction wastewater with integrated membrane technique
ZHOU Huiting, DU Chunhui, WU Chunjin, WU Liguang
College of Environmental Science and Engineering, Zhejiang Gongshang University, Hangzhou 310018, China
摘要 研究了超滤-纳滤组合膜工艺在碱减量废水处理中的应用,发现采用该工艺可以有效地降低碱减量废水中的化学需氧量(COD),COD 去除率可达到80%以上。对膜透过液回用于碱减量过程可能对涤纶减量效果的影响进行了实验分析,探讨了温度、时间、碱度、乙二醇含量等条件对涤纶减量率的影响。结果表明:温度、时间、碱浓度的增加均可以提高涤纶的减量率;乙二醇含量的累积,也可促进涤纶减量过程。采用该工艺可以实现对苯二甲酸、水、碱、乙二醇的回收及综合利用。
关键词 :
膜分离技术 ,
碱减量废水 ,
涤纶 ,
减量率
Abstract :In this work, ultrafiltration- nanofiltration integration membrane technique was applied in alkali reduction wastewater treatment. The results indicated that chemical oxygen demand (COD) of alkali weight reduction wastewater was effectively decreased by this process, and COD removal rate reached over 80%. Meanwhile, the effect of reused wastewater on the polyester reduction process was also analyzed, with main factors, such as temperature, time, alkalinity, and ethylene glycol content (accumulated) discussed in detail. The polyester reduction rate increased with the increase of temperature, process time and alkali concentration. The accumulating ethylene glycol content could also promote the reduction effect of the polyester. The recovery and comprehensive utilization of terephthalic acid, water, alkali and ethylene glycol could be realized by this technique.
Key words :
membrane separation technique
alkali reduction wastewater
polyester
reduction rate
收稿日期: 2015-05-01
基金资助: 国家自然科学基金项目(51103130)
通讯作者:
吴春金(通信作者),副教授,研究方向为环境功能材料及膜分离技术,电子信箱:wuchunjin99@sina.com
E-mail: wuchunjin99@sina.com
作者简介 : 周慧婷,硕士研究生,研究方向为环境功能材料及膜分离技术,电子信箱:zhouhuitin@sina.com
引用本文:
周慧婷, 杜春慧, 吴春金, 吴礼光. 集成膜工艺处理碱减量废水及回用[J]. 科技导报, 2015, 33(14): 70-73.
ZHOU Huiting, DU Chunhui, WU Chunjin, WU Liguang. Treatment and reuse of alkali reduction wastewater with integrated membrane technique. Science & Technology Review, 2015, 33(14): 70-73.
链接本文:
http://www.kjdb.org/CN/10.3981/j.issn.1000-7857.2015.14.012 或 http://www.kjdb.org/CN/Y2015/V33/I14/70
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