Startup methods analysis of a cryogenic distillation system with two interlinked columns for hydrogen isotope separation

被引:2
|
作者
Chen, Min [1 ]
Luo, Junhong [1 ]
Li, Peilong [1 ]
Hu, Cun [2 ]
Yu, Bin [1 ]
Jiang, Fei [1 ]
Wang, Jingchuan [1 ]
Yao, Weizhi [1 ]
An, Yongtao [1 ]
Bai, Jiao [1 ]
Shi, Yan [1 ]
Song, Jiangfeng [1 ]
Luo, Wenhua [1 ,3 ]
机构
[1] China Acad Engn Phys, Inst Mat, POB 9071, Mianyang 621907, Sichuan, Peoples R China
[2] Southwest Petr Univ, Sch Chem & Chem Engn, Chengdu 610500, Sichuan, Peoples R China
[3] Sci & Technol Surface Phys & Chem Lab, POB 9072-35, Mianyang 621908, Sichuan, Peoples R China
关键词
Hydrogen isotopes; Cryogenic distillation; Dynamic simulation; Startup method; DYNAMIC SIMULATION;
D O I
10.1016/j.fusengdes.2023.113721
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
Effective startup methods are crucial for the successful operation of a distillation facility. In order to design a viable startup method for a cryogenic distillation demonstration system with two interlinked columns for hydrogen isotope separation, which is under construction at Institute of Materials, China Academy of Engi-neering Physics, Aspen Plus and Aspen Dynamics were employed in combination to generate a dynamic nu-merical model for the startup analysis. Total four conventional startup methods were analysed. The most time -effective method was identified and the other of the four startup methods were found to be able to lead to successful startup results but with varied operation complexity and length of time to reach the steady state. The effective startup method that involved in charging the two distillation columns with equilibrated hydrogen isotope mixtures respectively, took only 50.36 h to reach the target steady state. And the identified method would be employed into the cryogenic distillation demonstration system to check its startup efficient.
引用
收藏
页数:8
相关论文
共 50 条
  • [31] Equilibrium Modeling for Hydrogen Isotope Separation by Cryogenic Adsorption
    张东辉
    周理
    苏伟
    孙艳
    Chinese Journal of Chemical Engineering, 2006, (04) : 526 - 531
  • [32] Equilibrium modeling for hydrogen isotope separation by cryogenic adsorption
    Zhang Donghui
    Zhou Li
    Su Wei
    Sun Yan
    CHINESE JOURNAL OF CHEMICAL ENGINEERING, 2006, 14 (04) : 526 - 531
  • [33] Analysis of the isotopes hydrogen mixtures from cryogenic distillation separation using gas chromatography
    Preda, Anisoara
    Pearsica, Claudia
    Bornea, Anisia
    Vasut, Felicia
    Zamfirache, Marius
    ASIAN JOURNAL OF CHEMISTRY, 2008, 20 (08) : 6263 - 6268
  • [34] THEORETICAL CALCULATION OF SEPARATION LENGTH IN ISOTOPE SEPARATION WITHIN PACKED DISTILLATION-COLUMNS
    KAMYNSKY, VA
    GYORGADSE, NA
    KOVTUN, VP
    ISOTOPENPRAXIS, 1978, 14 (09): : 321 - 324
  • [35] EXPERIMENTAL-STUDY FOR SEPARATION CHARACTERISTICS OF CRYOGENIC DISTILLATION-COLUMNS WITH AN H-D-T SYSTEM
    YAMANISHI, T
    ENOEDA, M
    OKUNO, K
    HAYASHI, T
    AMANO, J
    NARUSE, Y
    SHERMAN, RH
    FUSION TECHNOLOGY, 1991, 20 (04): : 419 - 424
  • [36] An analytic model for a 13C isotope separation process by cryogenic distillation
    Dumitrache, Dan Calin
    Inoan, Iulia
    De Schutter, Bart
    JOURNAL OF PROCESS CONTROL, 2014, 24 (05) : 463 - 474
  • [37] Steady-State simulation of cryogenic distillation used for helium isotope separation
    Chen, Huan
    Jia, Peng
    Qu, Qianxi
    Dai, Niannian
    Wang, Liguo
    Shi, Yaran
    Guo, Rendong
    Xu, Dong
    Li, Laifeng
    CRYOGENICS, 2024, 139
  • [38] HYDROGEN ISOTOPE DISTILLATION IN A FUSION REACTOR SYSTEM
    WILKES, WR
    TRANSACTIONS OF THE AMERICAN NUCLEAR SOCIETY, 1974, 19 (OCT27): : 20 - 20
  • [39] Dynamic simulation of a cryogenic batch distillation process for hydrogen isotopes separation
    Chen, Min
    Li, Peilong
    Hu, Cun
    Luo, Junhong
    Wen, Ming
    Yu, Bin
    Jiang, Fei
    An, Yongtao
    Shi, Yan
    Song, Jiangfeng
    Luo, Wenhua
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2022, 47 (23) : 11955 - 11961
  • [40] Optimal design of cryogenic distillation columns with side heat pumps for the propylene/propane separation
    Alcantara-Avila, J. Rafael
    Gomez-Castro, Fernando I.
    Segovia-Hernandez, J. Gabriel
    Sotowa, Ken-Ichiro
    Horikawa, Toshihide
    CHEMICAL ENGINEERING AND PROCESSING-PROCESS INTENSIFICATION, 2014, 82 : 112 - 122