Computation and comparison of Pd-based membrane reactor performances for water gas shift reaction and isotope swamping in view of highly tritiated water decontamination

被引:5
|
作者
Santucci, Alessia [1 ]
Rizzello, Claudio [2 ]
Tosti, Silvano [1 ]
机构
[1] CR ENEA Frascati, Assoc ENEA Euratom Fus, I-00044 Frascati, RM, Italy
[2] Tesi Sas, Rome, Italy
关键词
Highly tritiated water; Pd-based membrane reactor; Water gas shift; Isotopic swamping; PERMCAT REACTOR;
D O I
10.1016/j.fusengdes.2013.05.080
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
In a D-T fusion machine, due to the possible reaction between tritium and oxygen, some potential sources of highly tritiated water (HTW) can be identified. Therefore, a dedicated detritiation process has to be assessed either for economic and safety reasons. In this view, the use of a Pd-based membrane reactor performing isotopic exchange reactions can be considered since hydrogen isotopes exclusively permeate the Pd-Ag membrane and their exchange over the catalyst realizes the water detritiation. In this activity, the treatment of highly tritiated water, generated by an ITER-like machine (i.e. 2 kg of stoichiometric HTO containing up to 300g of tritium), via a Pd-membrane reactor is studied in terms of decontamination capability. Especially, a parametric analysis of two processes (water gas shift and isotopic swamping) performed in a Pd-based membrane reactor is carried out by using two mathematical models previously developed and experimentally verified. Particularly, the effect of the reactor temperature, the membrane thickness, the reaction pressure and the protium sweep flow-rate is investigated. Moreover, a comparison in terms of the decontamination factor and the number of reactors necessary to detritiate the HTW are provided. Generally, the results reveal a higher decontamination capability of the WGS reaction respect with the IS (maximum DF values of about 120 and 1.6 in the case of WGS and IS, respectively). However some drawbacks, mainly related with the formation of tritiated species, can occur by performing the WGS. (C) 2013 Euratom-ENEA Association sulla Fusione. Published by Elsevier B.V. All rights reserved.
引用
收藏
页码:2413 / 2416
页数:4
相关论文
共 50 条
  • [41] High pressure palladium membrane reactor for the high temperature water-gas shift reaction
    Augustine, Alexander S.
    Ma, Yi Hua
    Kazantzis, Nikolaos K.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2011, 36 (09) : 5350 - 5360
  • [42] Dimethyl ether reforming in a mesoporous γ-alumina membrane reactor combined with a water gas shift reaction
    Park, Sang-Jun
    Lee, Dong-Wook
    Yu, Chang-Yeol
    Lee, Kwan-Young
    Lee, Kew-Ho
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (05) : 1416 - 1420
  • [43] Hydrogen production in a Pore-Plated Pd-membrane reactor: Experimental analysis and model validation for the Water Gas Shift reaction
    Sanz, R.
    Calles, J. A.
    Alique, D.
    Furones, L.
    Ordonez, S.
    Marin, P.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (08) : 3472 - 3484
  • [44] Experimental Study of an Intensified Water-Gas Shift Reaction Process Using a Membrane Reactor/Adsorptive Reactor Sequence
    Chen, Huanhao
    Cao, Mingyuan
    Zhao, Linghao
    Ciora, Richard J., Jr.
    Liu, Paul K. T.
    Manousiouthakis, Vasilios, I
    Tsotsis, Theodore T.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2018, 57 (41) : 13650 - 13660
  • [45] Palladium based micro-membrane for water gas shift reaction and hydrogen gas separation
    Karnik, SV
    Hatalis, MK
    Kothare, MV
    MICROREATION TECHNOLOGY, 2001, : 295 - 302
  • [46] Inert membrane reactor model: Enhanced hydrogen production from the water gas shift reaction.
    Enick, RM
    Cugini, AV
    Rothenberger, KS
    McIlvried, HG
    ABSTRACTS OF PAPERS OF THE AMERICAN CHEMICAL SOCIETY, 1999, 218 : U635 - U635
  • [47] Effect of Pressure on High-Temperature Water Gas Shift Reaction in Microporous Zeolite Membrane Reactor
    Kim, Seok-Jhin
    Xu, Zhi
    Reddy, Gunugunuri K.
    Smirniotis, Peter
    Dong, Junhang
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (03) : 1364 - 1375
  • [48] A catalytic hollow fibre membrane reactor for combined steam methane reforming and water gas shift reaction
    Gil, Ana Gouveia
    Wu, Zhentao
    Chadwick, David
    Li, K.
    CHEMICAL ENGINEERING SCIENCE, 2015, 137 : 364 - 372
  • [49] Water-gas shift reaction in a Pd membrane reactor over Pt/Ce0.6Zr0.4O2 catalyst
    Bi, Yadong
    Xu, Hengyong
    Li, Wenzhao
    Goldbach, Andreas
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2009, 34 (07) : 2965 - 2971
  • [50] Catalytic Pd0.77Ag0.23 alloy membrane reactor for high temperature water-gas shift reaction: Methane suppression
    Pati, Subhasis
    Jangam, Ashok
    Wang Zhigang
    Dewangan, Nikita
    Hui, Wai Ming
    Kawi, Sibudjing
    CHEMICAL ENGINEERING JOURNAL, 2019, 362 : 116 - 125