NEW HIGH-TEMPERATURE ISOTOPIC EXCHANGE FUEL PROCESSING LOOP DESIGN FOR ITER

被引:4
作者
BUSIGIN, A [1 ]
SOOD, SK [1 ]
KALYANAM, KM [1 ]
机构
[1] ONTARIO HYDRO,CANADIAN FUS FUELS TECHNOL PROJECT,TORONTO M5G 1X6,ONTARIO,CANADA
来源
FUSION TECHNOLOGY | 1991年 / 20卷 / 02期
关键词
FUEL CLEANUP; IMPURITY TREATMENT; ISOTOPIC EXCHANGE;
D O I
10.13182/FST91-A29688
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
A new high-temperature isotopic exchange (HITEX) fuel processing loop (FPL) design for the International Thermonuclear Experimental Reactor (ITER) is proposed. The new design has advantages over previous ones that were based on catalytic oxidation or decomposition of impurities; it eliminates the need for impurity oxidation and electrolysis of DTO and does not rely on complicated catalytic decomposition reactions. In the HITEX design, tritium is exchanged out of impurities such as tritiated methane, ammonia, and water by swamping with H-2 and isotopically equilibrating the mixture in a high-temperature reactor. The reactor consists of a horizontal tube with an axial platinum metal hot wire operated at a temperature of 1173 K. The walls of the reactor are cooled to near room temperature to minimize permeation. Downstream from the reactor is a Pd/Ag permeator to separate out hydrogen and impurities. The separated H-2/HT stream is sent to the isotope separation system for tritium recovery.
引用
收藏
页码:179 / 185
页数:7
相关论文
共 13 条
[1]  
Bird R B., 2007, TRANSPORT PHENOMENA
[2]  
Bond G.C., 1962, CATALYSIS METALS
[3]   ITER HYDROGEN ISOTOPE-SEPARATION SYSTEM CONCEPTUAL DESIGN DESCRIPTION [J].
BUSIGIN, A ;
SOOD, SK ;
KVETON, OK ;
DINNER, PJ ;
MURDOCH, DK ;
LEGER, D .
FUSION ENGINEERING AND DESIGN, 1990, 13 (01) :77-89
[4]  
GUYER EC, 1989, HDB APPLIED THERMAL
[5]   THE IMPURITY PROCESSING LOOP FOR THE JET ACTIVE GAS HANDLING PLANT [J].
HEMMERICH, JL ;
DOMBRA, A ;
GORDON, C ;
GROSKOPFS, E ;
KONSTANTELLOS, A .
FUSION TECHNOLOGY, 1988, 14 (02) :557-561
[6]   CATALYSIS ON EVAPORATED METAL FILMS .2. THE EFFICIENCY OF DIFFERENT METALS FOR THE REACTION BETWEEN METHANE AND DEUTERIUM [J].
KEMBALL, C .
PROCEEDINGS OF THE ROYAL SOCIETY OF LONDON SERIES A-MATHEMATICAL AND PHYSICAL SCIENCES, 1953, 217 (1130) :376-389
[7]  
KEMBALL C, 1951, R SOC LONDON P A, V207, P35
[8]  
KERR EC, 1980, APR P TOP M TRIT DAY, P115
[9]   EXPERIMENTAL APPARATUS FOR THE FUEL CLEANUP PROCESS IN THE TRITIUM PROCESS LABORATORY [J].
KONISHI, S ;
INOUE, M ;
YOSHIDA, H ;
NARUSE, Y ;
SATO, H ;
MUTA, K ;
IMAMURA, Y .
FUSION TECHNOLOGY, 1988, 14 (02) :596-601
[10]  
MURDOCH DK, 1989, NET N2P44101A DOC