Study on mathematical model of sweeping gas multiple-effect membrane distillation process |
Authors: YANG Dan,GAO Qijun*,LU Xiaolong*,WU Chunrui,CHEN Huayan,WANG Xuan, JIA Yue |
Units: State Key Laboratory of Hollow Fiber Membrane Materials and Processes, Institute of Biological and Chemical Engineering, Tianjin Polytechnic University, Tianjin 300387, China |
KeyWords: sweeping gas; multiple-effect membrane distillation; heat recovery; GOR; mathematical model |
ClassificationCode:TQ028.8 |
year,volume(issue):pagination: 2014,34(5):58-64 |
Abstract: |
A novel sweeping gas multiple-effect membrane distillation process (SGMEMD) was designed based on the high energy consumption of sweeping gas membrane distillation (SGMD) process. The process was set up for the first time with a special latent-heat recovery system where the vapors got condensed and the feed was heated up simultaneously. Thus the latent-heat could be recovery gradually and effectively. The empirical formulas of membrane distillation permeate flux J and heat recovery rate η that describes sweeping gas multi-effect membrane distillation processes (SGMEMD) were presented using curve fitting method, which was according to results of single factor experiment that the effects of sweeping gas flow velocity, feed circulation volumetric flow, feed in temperature and the feed concentration on performance of SGMEMD process were investigated. Based on the empirical formulas, semi theoretical model of GOR was also established. The empirical formulas and semi theoretical model had a high precision in predicting the J and GOR of SGMEMD process, which had been validated by L9(34)orthogonal experiment. Compared to results of experiment, the calculated value of J and GOR relative deviation were within 8.0 %. |
Funds: |
国家自然科学基金项目(21176188,21106100),高等学校博士学科点专项科研基金(20111201110004) |
AuthorIntro: |
杨丹(1989—),男,天津市人,硕士研究生,研究方向为新型膜蒸馏过程研究.*联系人, |
Reference: |
[1].Qtaishat M,Matsuura T,Kruczek B,et al. Heat and mass transfer analysis in direct contact membrane distillation. Desalination[J]. Desalination,2008,219(1-3):272-292. [2].吕晓龙. 膜蒸馏过程探讨[J]. 膜科学与技术,2011,30(3):1-10. [3].李玖明,朱海霖,郭玉海,等. 真空膜蒸馏处理垃圾渗沥液反渗透浓水的研究[J]. 水处理技术,2013,39(7):89-91,95. [4].刘乾亮,马军,王争辉,等. 直接接触式膜蒸馏工艺处理高浓度氨氮模拟废水中操作条件的影响[J].环境工程学报,2012,6(7):2237-2241. [5].吕晓龙. 一种气扫式膜蒸馏方法[P]. 中国发明专利:200910245021.9,2009-12-23. [6].陈华艳,李欢,吕晓龙. 气扫式膜蒸馏传质传热过程[J]. 化工学报,2009,60(2):304-309. [7].Khayet M,Cojocaru C,Baroudi A. Modeling and optimization of sweeping gas membrane distillation[J]. Desalination,2012,287:159-166. [8].Alkhudhiri A,Darwish N,Hilal N. Membrane distillation: A comprehensive review[J]. Desalination,2012,287:2-18. [9].El-Bourawi M S,Ding Z,Ma R,et al. A framework for better understanding membrane distillation separation process[J]. J Membr Sci,2006,285:4-29. [10].Fiorini P,Sciubba E. Thermoeconomic analysis of a MSF desalination plant[J]. Desalination,2005,182:39-51. [11].夏清,陈常贵. 化工原理(上)[M]. 天津:天津大学出版社,2007. |
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