Competing Transport of Malonic and Acetic acids across Commercial and Modified RALEX AMH Anion-Exchange Membranes

被引:4
作者
Karpenko, T. V. [1 ]
Kovalev, N. V. [1 ]
Kirillova, K. R. [1 ]
Achoh, A. R. [1 ]
Melnikov, S. S. [1 ]
Sheldeshov, N. V. [1 ]
Zabolotsky, V. I. [1 ]
机构
[1] Kuban State Univ, Krasnodar 350040, Russia
基金
俄罗斯科学基金会;
关键词
anion-exchange membrane; double-layer membrane; acetic acid; malonic acid; current-voltage characteristic; electrodialysis separation; SELECTIVE ION SEPARATION; LACTIC-ACID; BIPOLAR MEMBRANES; ORGANIC-ACIDS; CITRIC-ACID; FERMENTATION BROTH; ELECTRODIALYSIS; RECOVERY; PERMSELECTIVITY; PURIFICATION;
D O I
10.1134/S2517751622020056
中图分类号
O64 [物理化学(理论化学)、化学物理学];
学科分类号
070304 ; 081704 ;
摘要
The current-voltage characteristics of a Ralex AMH anion-exchange membrane and a Ralex AMH/MF-4SK double-layer membrane in solutions of acetic and malonic acids and the permselectivity coefficients of these acids across the two membranes in a pH range of 1-8 at an electric current density of 0-5 A/dm(2) have been measured. It has been shown that the Ralex AMH anion-exchange membrane exhibits a preferential selectivity with respect to malonic acid in the entire ranges of pH and current densities. The Ralex AMH/MF-4SK double-layer membrane is selective with respect to acetic acid at all pH values and at current densities lower than the limiting electrodiffusion current. At currents above the limiting current, this membrane is selective with respect to malonic acid. The permselectivity coefficient value is explained by the occurrence of two competing processes: the dissociation of water molecules, which accelerates at membrane currents above the limiting current, and the protonation-deprotonation process involving ions and molecules of malonic and acetic acids.
引用
收藏
页码:118 / 126
页数:9
相关论文
共 53 条
[1]   An economic evaluation of the fermentative production of lactic acid from wheat flour [J].
Åkerberg, C ;
Zacchi, G .
BIORESOURCE TECHNOLOGY, 2000, 75 (02) :119-126
[2]  
[Anonymous], 1983, FOOD ACIDS CITRIC LA
[3]   Asymmetric bipolar membrane:: A tool to improve product purity [J].
Balster, J. ;
Sumbharaju, R. ;
Srikantharajah, S. ;
Punt, I. ;
Stamatialis, D. F. ;
Jordan, V. ;
Wessling, M. .
JOURNAL OF MEMBRANE SCIENCE, 2007, 287 (02) :246-256
[4]  
Butler D., 1973, ION EQUILIBRIA
[5]   Surface modification of anion exchange membrane using layer-by-layer polyelectrolytes deposition facilitating monovalent organic acid transport [J].
Chandra, Anusha ;
Bhuvanesh, E. ;
Mandal, Priyabrata ;
Chattopadhyay, Sujay .
COLLOIDS AND SURFACES A-PHYSICOCHEMICAL AND ENGINEERING ASPECTS, 2018, 558 :579-590
[6]   Transport hindrances with electrodialytic recovery of citric acid from solution of strong electrolytes [J].
Chandra, Anusha ;
Tadimeti, Jogi Ganesh Dattatreya ;
Chattopadhyay, Sujay .
CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2018, 26 (02) :278-292
[7]   Switching selectivity of carboxylic acids and associated physico-chemical changes with pH during electrodialysis of ternary mixtures [J].
Chandra, Anusha ;
Tadimeti, Jogi Ganesh Dattatreya ;
Bhuvanesh, E. ;
Pathiwada, Darshak ;
Chattopadhyay, Sujay .
SEPARATION AND PURIFICATION TECHNOLOGY, 2018, 193 :327-344
[8]  
Demina N. G., 2015, Biotekhnologiya, P52
[9]   Demineralization and separation of amino acids by electrodialysis with ion-exchange membranes [J].
Elisseeva, TV ;
Shaposhnik, VA ;
Luschik, IG .
DESALINATION, 2002, 149 (1-3) :405-409
[10]   Utilization of electrodialysis for galacturonic acid recovery [J].
Eszter Molnar ;
Matild Eszterle ;
Kornelia Kiss ;
Nandor Nemestothy ;
Jenoe Fekete ;
Katalin Belafi-Bako .
DESALINATION, 2009, 241 (1-3) :81-85