YSZ-Based Dual-Phase Membrane Reactors for H2 Production by Coupling Water Splitting with CO2 Capture

被引:0
|
作者
Zhang, Youpeng [1 ,2 ]
Zhang, Peng [2 ,3 ]
Ou, Zuqiao [2 ,3 ]
Cao, Zhongwei [2 ]
Feng, Qiuxia [2 ,3 ]
Mu, Shenglong [1 ,4 ,5 ]
Zhu, Xuefeng [2 ,3 ]
Yang, Weishen [2 ,3 ]
机构
[1] Shenyang Univ Chem Technol, Liaoning Prov Key Lab Preparat & Applicat Special, Shenyang 110142, Peoples R China
[2] Dalian Inst Chem Phys, State Key Lab Catalysis, Zhongshan Rd 457, Dalian 116023, Peoples R China
[3] Univ Chinese Acad Sci, Beijing 100049, Peoples R China
[4] Shenyang Univ Chem Technol, Shenyang Key Lab New Funct Coating Mat, Shenyang 110142, Peoples R China
[5] Shenyang Res Inst Ind Technol Adv Coating Mat, Shenyang 110300, Peoples R China
基金
国家重点研发计划; 中国国家自然科学基金;
关键词
HOLLOW-FIBER MEMBRANE; GAS SHIFT REACTION; HYDROGEN SEPARATION; HIGH-TEMPERATURE; STABILIZED ZIRCONIA; CARBON-DIOXIDE; COMPOSITE; METHANE; CONDUCTIVITY; PERMEATION;
D O I
10.1021/acs.iecr.4c02593
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Mixed ionic-electronic conducting (MIEC) membrane reactors are a promising technology for H-2 production through coupling of H2O splitting with CO2 capture. To meet the high reliability requirement to the membrane reactors for an industrial process, it is necessary to develop membrane materials with high mechanical strength and high chemical stability. In this work, a series of x wt % YSZ-(98 - x) wt % La0.7Sr0.27Cr0.4Fe0.6O3-delta-2 wt % CuO (x = 40, 50, 60 and 70; denoted as YL4, YL5, YL6, and YL7, respectively) dual-phase membranes were prepared for coupling water splitting with CO2 capture. The results demonstrate that the mechanical strength of the dual-phase membrane increases significantly with the addition of YSZ and is much higher than that of the single perovskite material LSCF. The conductivity and H-2 production rates increase in the order of YL4 > YL5 > YL6 > YL7. The structure stability of the perovskite phase in dual-phase membranes increases with the content of YSZ phase under the operation condition of membrane reactors. The YL6-based membrane reactor was operated steadily for 290 h, indicating that it is a promising membrane material for H-2 production by coupling water splitting with CO2 capture.
引用
收藏
页码:16367 / 16375
页数:9
相关论文
共 50 条
  • [31] Surface modification of dual-phase ceramic membrane reactor for coupling catalytic CO2 conversion with partial oxidation of methane
    Liu, Yanbo
    Qiao, Wanyu
    Wu, Ning
    Sun, Qiangchao
    Duan, Tong
    Su, Fangchun
    Lu, Xionggang
    Cheng, Hongwei
    JOURNAL OF MEMBRANE SCIENCE, 2024, 692
  • [32] Dual-phase all-polymeric membranes with graft copolymer filler for CO2 capture
    Lee, Jae Hun
    Park, Cheol Hun
    Jung, Jung Pyo
    Kim, Jeong-Hoon
    Kim, Jong Hak
    CHEMICAL ENGINEERING JOURNAL, 2018, 334 : 939 - 947
  • [33] Investigation of molten carbonate electrolysis cells performance for H2 production and CO2 capture
    Audasso, Emilio
    Kim, Kab In
    Accardo, Grazia
    Kim, Han Sung
    Yoon, Sung Pil
    JOURNAL OF POWER SOURCES, 2022, 523
  • [34] High capacity potassium-promoted hydrotalcite for CO2 capture in H2 production
    Halabi, M. H.
    de Croon, M. H. J. M.
    van der Schaaf, J.
    Cobden, P. D.
    Schouten, J. C.
    INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2012, 37 (05) : 4516 - 4525
  • [35] Investigation of molten carbonate electrolysis cells performance for H2 production and CO2 capture
    Audasso, Emilio
    Kim, Kab In
    Accardo, Grazia
    Kim, Han Sung
    Yoon, Sung Pil
    Journal of Power Sources, 2022, 523
  • [36] Pd-Ag tubular membrane reactors for methane dry reforming:: A reactive method for CO2 consumption and H2 production
    Gallucci, F.
    Tosti, S.
    Basile, A.
    JOURNAL OF MEMBRANE SCIENCE, 2008, 317 (1-2) : 96 - 105
  • [37] CO2 capture from H2 plants: implementation for EOR
    Terrien, Paul
    Lockwood, Frederick
    Granados, Ludovic
    Morel, Thomas
    12TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES, GHGT-12, 2014, 63 : 7861 - 7866
  • [38] Coupling CO2 separation with catalytic reverse water-gas shift reaction via ceramic-carbonate dual-phase membrane reactor
    Chen, Tianjia
    Wang, Zhigang
    Liu, Lina
    Pati, Subhasis
    Wai, Ming Hui
    Kawi, Sibudjing
    CHEMICAL ENGINEERING JOURNAL, 2020, 379
  • [39] Poisoning Effect of H2S on CO2 Permeation of Samarium-Doped-Ceria/Carbonate Dual-Phase Membrane
    Chen, Tianjia
    Wu, Han-Chun
    Li, Yongdan
    Lin, Y. S.
    INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2017, 56 (49) : 14662 - 14669
  • [40] Steam-promoted CO2 flux in dual-phase CO2 separation membranes
    Xing, Wen
    Peters, Thijs
    Fontaine, Marie-Laure
    Evans, Anna
    Henriksen, Partow Pakdel
    Norby, Truls
    Bredesen, Rune
    JOURNAL OF MEMBRANE SCIENCE, 2015, 482 : 115 - 119