Position:Home >> Abstract

Experiment study on advection multi-effect vacuum membrane distillation(ME-VMD)process
Authors: Zhang Yonggang, Peng Yuelian, Ji Shulan 
Units: Beijing Key Laboratory for Green Catalysis and Separation, College of Environmental and Energy Engineering, Beijing University of Technology, Beijing 100124, P. R. China
KeyWords: advection; multi-effect; vacuum membrane distillation; gained output ratio; thermal efficiency; transmembrane flux
ClassificationCode:TQ028.8
year,volume(issue):pagination: 2016,36(6):11-18

Abstract:
 An experimental investigation was carried out by using advection multi-effect vacuum membrane distillation (ME-VMD) system containing hydrophobic PTFE hollow fiber membrane and PTFE capillary heat exchanger. The effect of feed temperature, feed velocity and vacuum degree on the transmembrane flux, thermal efficiency and gained-output-ratio (GOR) were investigated. The experimental results show that the temperature difference loss increases with the increase of feed temperature, and decreases with the increase of the effect number. The best effect number has a direct relationship with the feed temperature. High feed temperature, low flow rate and the high vacuum degree contribute to the improvement of transmembrane flux, water yield and GOR. The thermal efficiency increases with the increase of feed temperature and vacuum degree and declines with the increase of feed velocity. When the feed temperature, the feed velocity and the absolute pressure at the permeate side is 90℃, 0.30m/s and 3kPa, respectively, four effect ME-VMD can be used, and the GOR can get to 2.15. 

Funds:

AuthorIntro:
第一作者简介:张永刚(1976-),男,山东德州人,博士研究生,研究方向为膜蒸馏技术及应用,E-MAIL:yongganga@126.com.?通讯作者,E-mail:pyl@bjut.edu.cn

Reference:
 [1] El-Bourawi M S, Ding Z, Ma R, et al. A framework for better understanding membrane distillation separation process [J]. J Membr Sci, 2006, 285 (1-2) :4-29.
[2] Alkhudhiri A, Darwish N, Hilal N. Membrane distillation:A comprehensive review [J]. Desalination, 2012, 287:2-18.
[3] Drioli E,Wu Y.Membrane distillation:an experimental study [M]. Desalination, 1985, 53:339-340.
[4] Lawson K W , Lioyd D R. Membrane distillation [J]. J Membr Sci,1997, 124 (1): 1-25.
[5] 赵晶,武春瑞,吕晓龙.膜蒸馏海水淡化过程研究:三种膜蒸馏过程的比较[J].膜科学与技术,2009,29(1):83-89.
[6] 张猛,高启君,文晨,吕晓龙.减压多效膜蒸馏过程试验研究 [J]. 水处理技术,2102,38(6):57-62.
[7] 秦英杰,刘立强,何菲,等.内部热能回收式多效膜蒸馏用于海水淡化及浓盐水深度浓缩[J].膜科学与技术,2012,32(2):52-57.
[8] Zhang Y, Peng Y, Ji S, et al. Review of thermal efficiency and heat recycling in membrane distillation processes. Desalination, 2015,367, 223-239. 
[9] 刘学晶,李保安.减压膜蒸馏热量回收研究[J]. 化学工业与工程, 2012, 3
(2):38-42.
[10] Camacho L M,Dumée L, Zhang J h , et al. Advances in Membrane Distillation for Water Desalination and Purification Applications [J].Water, 2013, 5, 94-196.
[11 Khayet, M, Membranes and theoretical modeling of membrane distillation: a review [J].Adv Colloid Interface Sci, 2011, 164, 56-88.
[12] Fan H W, Peng Y L. Application of PVDF membranes indesalination and comparison of the VMD and DCMD processes [J].Chemical Engineering Science, 2012,79:94-102.
 

Service:
Download】【Collect

《膜科学与技术》编辑部 Address: Bluestar building, 19 east beisanhuan road, chaoyang district, Beijing; 100029 Postal code; Telephone:010-80492417/010-80485372; Fax:010-80485372 ; Email:mkxyjs@163.com

京公网安备11011302000819号