Studies on permeation, rejection, and transport of aqueous poly(ethylene glycol) solutions using ultrafiltration membranes

被引:4
作者
Jaya, N.
Arthanareeswaran, G.
Mohan, D. [1 ]
Raajenthiren, M.
Thanikaivelan, P.
机构
[1] Anna Univ, Membrane Lab, Dept Chem Engn, AC Coll Technol, Madras 600025, Tamil Nadu, India
[2] Cent Leather Res Inst, Ctr Leather Apparel & Accessories Dev, Madras 600020, Tamil Nadu, India
关键词
ultrafiltration; poly(ethylene glycols); permeate flux; rejection; mass transfer coefficient; POLYURETHANE BLEND MEMBRANES; CELLULOSE-ACETATE; MASS-TRANSFER; PERFORMANCE; PREDICTION; POLYMERS; WATER; FLOW;
D O I
10.1080/01496390701206231
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
The permeate flux and retention of aqueous solutions of poly(ethylene glycols) (PEG) with different molecular weights ranging from 4000 to 35,000 Da have been investigated using various compositions such as 100/0, 90/10, 80/20, and 70/30 wt% of cellulose acetate (CA)/sulfonated poly (etheretherketone) (SPEEK) ultrafiltration blend membranes. The factors affecting the rejection rate and permeate flux such as molecular weight of PEGs, concentration of the solute, composition of the membranes, and transmembrane pressures have been studied. It is seen that the increase in the concentration of PEG results in the decreased permeate flux and increased rejection for increasing CA content in the membranes. A similar observation in the flux and rejection was made for increasing the molecular weight of PEGS. Further, the mass transfer, diffusion, and true retention coefficients of the solute have been studied with different operating variables like molecular weight and concentration of PEGS. An increase in the molecular weight of PEGS results in the decrease of mass transfer and diffusion coefficients and increase of the true retention coefficient. A reverse trend is observed with increasing concentrations of PEG.
引用
收藏
页码:963 / 978
页数:16
相关论文
共 28 条
[1]   Transport of formic acid through anion exchange membranes by diffusion dialysis and electro-electro dialysis [J].
Akgemci, EG ;
Ersöz, M ;
Atalay, T .
SEPARATION SCIENCE AND TECHNOLOGY, 2004, 39 (01) :165-184
[2]   Studies on cellulose acetate and sulfonated poly(ether ether ketone) blend ultrafiltration membranes [J].
Arthanareeswaran, G ;
Srinivasan, K ;
Mahendran, R ;
Mohan, D ;
Rajendran, M ;
Mohan, V .
EUROPEAN POLYMER JOURNAL, 2004, 40 (04) :751-762
[3]   THE ANTI-FOULING ACTION OF POLYMERS PREADSORBED ON ULTRAFILTRATION AND MICROFILTRATION MEMBRANES [J].
BRINK, LES ;
ELBERS, SJG ;
ROBBERTSEN, T ;
BOTH, P .
JOURNAL OF MEMBRANE SCIENCE, 1993, 76 (2-3) :281-291
[4]  
Cheryan M., 1986, Ultrafiltration handbook
[5]  
CHRISTOPHER TC, 2002, J ENV ENG, V128, P399
[6]   ULTRAFILTRATION OF LIPOPROTEINS THROUGH A SYNTHETIC MEMBRANE - IMPLICATIONS FOR FILTRATION THEORY OF ATHEROGENESIS [J].
COLTON, CK ;
LEES, RS ;
WILSON, DE ;
FRIEDMAN, S .
JOURNAL OF CLINICAL INVESTIGATION, 1972, 51 (09) :2472-+
[7]  
Flory P J., PRINCIPLES POLYM CHE
[8]   CONCENTRATION POLARIZATION IN A REVERSE-OSMOSIS TEST CELL [J].
JONSSON, G ;
BOESEN, CE .
DESALINATION, 1977, 21 (01) :1-10
[9]  
JONSSON G, 1986, MEMBRANES MEMBRANE P, P179
[10]   FOULING OF CELLULOSE-ACETATE TUBULAR REVERSE-OSMOSIS MODULES TREATING INDUSTRIAL WATER IN TOKYO [J].
KIMURA, S ;
NAKAO, SI .
DESALINATION, 1975, 17 (03) :267-288