Research on model of purification of low unsaturated degree polyether polyols with membrane separation |
Authors: YANG Liu1,Ma Weihua1,Qi Li2,Zhong Qin1 |
Units: 1. Department of Chemical Engineering,Nanjing University of Science & Technology,Nanjing 210094,Jiangsu,China; |
KeyWords: polyether polyols; membrane flux; concentration polarization; mathematical |
ClassificationCode: |
year,volume(issue):pagination: 2012,32(4):61-65 |
Abstract: |
Flat membrane ultrafiltration was applied to purification of low unsaturated degree polyether polyols, which flat membrane prepared from polyethersulphone(PES). Crude polyether polyols were used as polyols/hexane miscella in a 1:1 proportion. Based on the studies on operating pressure and flow speed, a mathematic resistance model describing membrane flux as a function of pressure and flow rate was established, and the model parameters were got by fitting the experimental data. The resullts showed that the predicted results of membrane flux as a function were in good agreement with the experimental results well, with a relative error varying between 0.13%~14.02%, and the correlation coefficients were all around 0.99. Using this model, flux change can be predicted and the effective process parameters were prvided for the industrial purification process. |
Funds: |
江苏省科技成果转化专项资金项目(BA2009016);南京理工大学自主科研专项计划资助(2010ZYTS018) |
AuthorIntro: |
杨柳(1987-),女,吉林梨树人,硕士生,从事聚醚多元醇方向的研究. |
Reference: |
[1] 王湛,周翀. 膜分离技术基础[M]. 第二版. 北京:化学工业出版社,2006:4~7. [2] 崔彦杰,刘美,王湛,等. 超滤通量模型的研究进展[J]. 膜科学与技术,2008,28(6):93~98. [3] 曹占平,张景丽,张宏伟. 微滤膜过滤阻力机理及模型研究[J]. 膜科学与技术,2010,30(1):18~23. [4] Tansel B,Bao W Y,Tansl I N. Characterization of fouling kinetics in ultrafiltration systems by resistances in series model[J]. Desalination,2000,129(1):7~14. [5] Neggaz Y,Vargas M L,Dris A O,et al. A combination of serial resistances and concentration polarization models along the membrane in ultrafiltration of pectin and albumin solutions[J]. Separation and Purification Technology,2007,54(1):18~27. [6] Jönsson A S,Jönsson B,Byhlin H. A concentration polarization model for the ultrafiltration of nonionic surfactants[J]. Journal of Colloid and Interface Science,2006,304(1):191~199. [7] Foley G,Garcia J. Ultrafiltration flux theory based on viscosity and osmotic effects: application to diafiltration optimisation[J]. Journal of Membrane Science,2000,176(1):55~61. [8] Curcio S,Calabrò V,Iorio G. Reduction and control of flux decline in cross-flow membrane processes modeled by artificial neural networks[J]. Journal of Membrane Science,2006,286(1~2):125~132. [9] 时钧,袁权,高从楷. 膜技术手册[M]. 北京:化学工业出版社,2001:350~351. [10] 刘茉娥. 膜分离技术[M]. 北京:化学工业出版社,1998:54~58. [11] Todisco S,Tallarico P,Gupta B B. Mass transfer and polyphenols retention in the clarification of black tea with ceramic membranes[J]. Innovative Food Science and Emerging Technologies,2002,3(3):255~262. [12] 程坷伟,许时婴,王璋. 甘薯淀粉生产废液中糖蛋白提取的超滤数学模型[J]. 无锡轻工大学学报,2004,23(6):59~63. |
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