Salt splitting with radiation grafted PVDF membranes

被引:20
作者
Tzanetakis, N
Taama, WM
Scott, K [1 ]
Varcoe, J
Slade, RS
机构
[1] Univ Newcastle Upon Tyne, Dept Chem & Proc Engn, Newcastle Upon Tyne NE1 7RU, Tyne & Wear, England
[2] Univ Surrey, Dept Chem, Guildford GU2 7XH, Surrey, England
关键词
electrohydrolysis; ion-exchange membrane; salt splitting; PVDF; radiation grafted;
D O I
10.1016/S0011-9164(02)01020-2
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Sulphonated PVDF cation-exchange membranes have been formulated for the splitting of sodium sulphate by electrohydrolysis. Three membranes with different degree of grafting were tested in a two-compartment membrane cell. The effect of flow rate, current density and salt concentration on the performance of each membrane is described. The different flow conditions in front of the membranes did not significantly affect the current efficiency. Productivity was greater at higher current densities, although a slight decrease in the current efficiency was observed. The SPVDF with a 22.7% degree of grafting performed slightly better than the other cation-exchange membranes. The new materials gave acceptable selectivity; low electrical resistance; and excellent chemical, thermal, and mechanical stability. They resulted in superior performance to the commercially available Nafion(R) 117, enabling an increase of approximately 20% in current efficiencies and sodium transport rates.
引用
收藏
页码:275 / 282
页数:8
相关论文
共 11 条
[1]   Nitric acid and sodium hydroxide generation by electrodialysis using bipolar membranes [J].
Cherif, AT ;
Molenat, J ;
Elmidaoui, A .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1997, 27 (09) :1069-1074
[2]   EFFECT OF TURBULENCE ON LIMITING CURRENT IN ELECTRODIALYSIS CELLS [J].
COWAN, DA ;
BROWN, JH .
INDUSTRIAL AND ENGINEERING CHEMISTRY, 1959, 51 (12) :1445-1448
[3]   Evaluation of a ceramic-polymer composite cation-selective membrane for sodium salt splitting [J].
Girard, F ;
Izquierdo, R ;
Quenneville, E ;
Bah, ST ;
Paleologou, M ;
Meunier, M ;
Ivanov, D ;
Yelon, A .
JOURNAL OF THE ELECTROCHEMICAL SOCIETY, 1999, 146 (08) :2919-2924
[4]   THE BEHAVIOR OF ION-EXCHANGE MEMBRANES IN ELECTROLYSIS AND ELECTRODIALYSIS OF SODIUM-SULFATE [J].
JORISSEN, J ;
SIMMROCK, KH .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1991, 21 (10) :869-876
[5]   Salt splitting using ceramic membranes [J].
Kurath, DE ;
Hollenberg, GW ;
Jue, JF ;
Smith, J ;
Virkar, AV ;
Balagopal, S ;
Sutija, DP .
SEPARATION SCIENCE AND TECHNOLOGY, 1997, 32 (1-4) :557-572
[6]  
MARTIN AD, 1992, ICHEME S SER, V27
[7]   Enhancement of the current efficiency for sodium hydroxide production from sodium sulphate in a two-compartment bipolar membrane electrodialysis system [J].
Paleologou, M ;
Thibault, A ;
Wong, PY ;
Thompson, R ;
Berry, RM .
SEPARATION AND PURIFICATION TECHNOLOGY, 1997, 11 (03) :159-171
[8]   Behaviour of Nafion® 350 membrane in sodium sulfate electrochemical splitting:: continuous process modelling and pilot scale tests [J].
Rakib, M ;
Moçotéguy, P ;
Viers, P ;
Petit, E ;
Durand, G .
JOURNAL OF APPLIED ELECTROCHEMISTRY, 1999, 29 (12) :1439-1448
[9]   Electrohydrolysis recycling of waste iodide salts into hydriodic acid for the chemical conversion of biomass into liquid hydrocarbons [J].
Robinson, JM ;
Mechalke, EJ ;
Rogers, TE ;
Holland, PL ;
Barber, WC .
JOURNAL OF MEMBRANE SCIENCE, 2000, 179 (1-2) :109-125
[10]  
Seerak I.J., 1935, T ELECTROCHEM SOC, V68, P493