Experimental Investigation of Concentration Dependency of Hydrophobic Catalyst Performance in Reaction of Isotope Exchange Between Water Vapor and Hydrogen

被引:4
作者
Tkachenko, V. [1 ]
Ovcharov, A. V. [1 ]
Rozenkevich, M. B. [1 ]
机构
[1] Mendeleyev Univ Chem Technol Russia, IMSEN IFH, Miusskaya Sq 9, Moscow 125047, Russia
关键词
Hydrogen isotopes; catalytic isotope exchange; low and high deuterium concentration; SIMULATION; DETRITIATION; DESIGN;
D O I
10.13182/FST16-130
中图分类号
TL [原子能技术]; O571 [原子核物理学];
学科分类号
0827 ; 082701 ;
摘要
Vapor phase catalytic exchange is an important part of many hydrogen isotope separation processes. Some industrial hydrogen isotope separation processes are performed in a wide deuterium concentration range. The performance of catalysts in hydrogen-water vapor exchange reaction in the upper deuterium concentration limit is poorly investigated. The paper presents results of an investigation of catalytic activity of three catalyst types at the upper and lower limits of the deuterium concentration range. All catalyst experimental rate constants in protium-deuterium exchange demonstrated a tendency to increase with the growth of deuterium concentration. Experimental rate constants of catalysts in protium-tritium and deuterium-tritium exchange were found to remain constant. In this work the authors propose a method to be used for catalyst performance evaluation to obtain catalyst performance data for liquid phase catalytic exchange process models.
引用
收藏
页码:207 / 214
页数:8
相关论文
共 16 条
[1]   MULTI-PURPOSE HYDROGEN ISOTOPES SEPARATION PLANT DESIGN [J].
Boniface, H. A. ;
Gnanapragasam, N. V. ;
Ryland, D. K. ;
Suppiah, S. ;
Castillo, I. .
FUSION SCIENCE AND TECHNOLOGY, 2015, 67 (02) :258-261
[2]   COMPLEX SOFTWARE DEDICATED FOR DESIGN AND SIMULATION OF LPCE PROCESS FOR HEAVY WATER DETRITIATION [J].
Bornea, Anisia ;
Petrutiu, Catalin ;
Zamfirache, Marius .
FUSION SCIENCE AND TECHNOLOGY, 2015, 67 (02) :270-273
[3]  
BRON J, 1973, Z NATURFORSCH A, VA 28, P129
[4]   THE KINETICS OF ISOTOPIC EXCHANGE REACTIONS [J].
BUNTON, CA ;
CRAIG, DP ;
HALEVI, EA .
TRANSACTIONS OF THE FARADAY SOCIETY, 1955, 51 (02) :196-204
[5]   MASS TRANSFER MODEL LIQUID PHASE CATALYTIC EXCHANGE COLUMN SIMULATION APPLICABLE TO ANY COLUMN COMPOSITION PROFILE [J].
Busigin, Anthony .
FUSION SCIENCE AND TECHNOLOGY, 2015, 67 (02) :286-289
[6]  
CRISTESCU I., 2015, JW0FT21 FORSCH KARLS
[7]   Modelling of the process of three-isotope (H, D, T) exchange between hydrogen gas and water vapour on Pt-SDBC catalyst over a wide range of deuterium concentration [J].
Fedorchenko, OA ;
Alekseev, IA ;
Tchijov, AS ;
Uborsky, VV .
FUSION SCIENCE AND TECHNOLOGY, 2005, 48 (01) :120-123
[8]   CATALYSIS ON EVAPORATED METAL FILMS .1. THE EFFICIENCY OF DIFFERENT METALS FOR THE REACTION BETWEEN AMMONIA AND DEUTERIUM [J].
KEMBALL, C .
PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1952, 214 (1118) :413-426
[9]   Analysis of simple kinetic models in heterogeneous catalysis [J].
Lynggaard, H ;
Andreasen, A ;
Stegelmann, C ;
Stoltze, P .
PROGRESS IN SURFACE SCIENCE, 2004, 77 (3-4) :71-137