个人信息Personal Information
教授
博士生导师
硕士生导师
性别:男
毕业院校:布朗大学
学位:博士
所在单位:能源与动力学院
学科:热能工程. 化学工程. 材料表面工程
联系方式:www.guoflab.com
电子邮箱:feiguo@dlut.edu.cn
Mass transfer during membrane distillation treatment of wastewater from hot-dip galvanization
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论文类型:期刊论文
发表时间:2020-03-18
发表刊物:SEPARATION AND PURIFICATION TECHNOLOGY
收录刊物:EI、SCIE
卷号:235
ISSN号:1383-5866
关键字:Membrane distillation; Hot-dip galvanizing; Diffusion coefficient; Acid recovery; Porous membrane
摘要:Hot-dip galvanized products are widely applied in many fields in China. The treatment of the wastewater containing acid and many metal ions from the hot-dip galvanizing industry is an important environmental issue. In this paper, we experimentally investigated the membrane distillation technique to treat the wastewater from the hot-dip galvanizing industry, and determined the factors that affect the membrane distillation performance. The transport behavior of multi-components (i.e. HCl and H2O) through the porous membranes was studied in detail. The results indicate that it is promising to use the air gap membrane distillation configuration to treat the wastewater and recover hydrochloric acid. The increase of the feed temperature leads to the increase of the permeate flux in general. The presence of FeCl2 and the acidity of the feed affects the acidity of the permeate. FeCl2 in the feed can enhance the acidity of the permeate significantly, especially when the acidity of the feed is low. The adding of 9.5 wt% FeCl2 in the feed can increase the acidity of the permeate by about 10 times when the acidity of the feed is 6 wt%. The overall metal ion (Fe2+) rejection ratio is higher than 99.99% by membrane distillation technique.