Introducing an integrated chemical looping hydrogen production, inherent carbon capture and solid oxide fuel cell biomass fueled power plant process configuration

被引:110
作者
Aghaie, Mahsa [1 ]
Mehrpooya, Mehdi [1 ,2 ]
Pourfayaz, Fathollah [1 ]
机构
[1] Univ Tehran, Fac New Sci & Technol, Renewable Energies & Environm Dept, Tehran, Iran
[2] Univ Tehran, Fac New Sci & Technol, Hydrogen & Fuel Cell Lab, Tehran, Iran
关键词
Chemical looping combustion; Carbon capture; Solid oxide fuel cell; Hydrogen production; Power cycle; CO2; CAPTURE; OPTIMAL-DESIGN; NATURAL-GAS; GASIFICATION; SYSTEM; MODEL; POLARIZATION; COMBUSTION; SIMULATION; GENERATION;
D O I
10.1016/j.enconman.2016.07.001
中图分类号
O414.1 [热力学];
学科分类号
摘要
A novel integrated system is proposed which combines biomass gasification, chemical looping combustion, solid oxide fuel cell system and a steam power cycle. Sensitivity analysis is done for effective parameters to analyze the performance of the integrated system and investigation of the optimal operating condition. Because of some restrictions in the integrated system experiments, a chemical process simulator is used for analysis of the hybrid system. Products of this process are high-purity hydrogen and electrical power which are produced by chemical looping and solid oxide fuel cell (and a power cycle) respectively. The net efficiency of the system reaches to 55.8% with 100% carbon dioxide capture. Solid oxide fuel cell operates at 850 degrees C and 12 bar. Chemical looping system uses Calcium oxide metal oxide as oxygen carrier. Also carbonator, calcinator and hydrator reactors operating temperature are 800 degrees C 850 degrees C and 650 degrees C respectively. (C) 2016 Elsevier Ltd. All rights reserved.
引用
收藏
页码:141 / 154
页数:14
相关论文
共 48 条
  • [1] Chemical-Looping Gasification of Biomass for Hydrogen-Enriched Gas Production with In-Process Carbon Dioxide Capture
    Acharya, Bishnu
    Dutta, Animesh
    Basu, Prabir
    [J]. ENERGY & FUELS, 2009, 23 (10) : 5077 - 5083
  • [2] The technical feasibility of biomass gasification for hydrogen production
    Albertazzi, S
    Basile, E
    Brandin, J
    Einvall, J
    Hulteberg, C
    Fornasari, G
    Rosetti, V
    Sanati, M
    Trifirò, F
    Vaccari, A
    [J]. CATALYSIS TODAY, 2005, 106 (1-4) : 297 - 300
  • [3] [Anonymous], 2012, PEM FUEL CELLS THEOR
  • [4] [Anonymous], 2002, OPTIMAL DESIGN OPERA
  • [5] [Anonymous], IRAN ENERGY ENV
  • [6] Polarization effects in electrolyte/electrode-supported solid oxide fuel cells
    Chan, SH
    Xia, ZT
    [J]. JOURNAL OF APPLIED ELECTROCHEMISTRY, 2002, 32 (03) : 339 - 347
  • [7] A complete polarization model of a solid oxide fuel cell and its sensitivity to the change of cell component thickness
    Chan, SH
    Khor, KA
    Xia, ZT
    [J]. JOURNAL OF POWER SOURCES, 2001, 93 (1-2) : 130 - 140
  • [8] Coal gasification integration with solid oxide fuel cell and chemical looping combustion for high-efficiency power generation with inherent CO2 capture
    Chen, Shiyi
    Lior, Noam
    Xiang, Wenguo
    [J]. APPLIED ENERGY, 2015, 146 : 298 - 312
  • [9] An integrated system combining chemical looping hydrogen generation process and solid oxide fuel cell/gas turbine cycle for power production with CO2 capture
    Chen, Shiyi
    Xue, Zhipeng
    Wang, Dong
    Xiang, Wenguo
    [J]. JOURNAL OF POWER SOURCES, 2012, 215 : 89 - 98
  • [10] Three-reactors chemical looping process for hydrogen production
    Chiesa, Paolo
    Lozza, Giovanni
    Malandrino, Alberto
    Romano, Matteo
    Piccolo, Vincenzo
    [J]. INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2008, 33 (09) : 2233 - 2245