Integration of a Ca-looping system for CO2 capture in an existing power plant

被引:33
作者
Martinez, I. [1 ]
Murillo, R. [1 ]
Grasa, G. [1 ]
Abanades, J. C. [2 ]
机构
[1] ICB CSIC, Inst Carboquim, C Miguel Luesma Castan 4, Zaragoza 50018, Spain
[2] INCAR, CSIC, E-33011 Oviedo, Spain
来源
10TH INTERNATIONAL CONFERENCE ON GREENHOUSE GAS CONTROL TECHNOLOGIES | 2011年 / 4卷
关键词
post-combustion CO2 capture; Ca-looping cycle; REACTOR; CYCLE;
D O I
10.1016/j.egypro.2011.02.043
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
This work analyses a Ca-looping system that uses CaO as regenerable sorbent to capture CO2 from the flue gases generated in an existing supercritical power plant. The CO2 is captured by CaO in a CFB carbonator while coal oxycombustion provides the energy required to regenerate the sorbent. Part of the energy introduced into the calciner can be transferred to a new supercritical steam cycle to generate additional power. Two case studies based on a scenario of low solid circulation rate between reactors have been integrated with the new supercritical steam cycle. Efficiency penalties, mainly associated with the energy consumption of the ASU, CO2 compressor and auxiliaries, can be as low as 7.5 percentage points of net efficiency when working with low CaCO3 make-up flows and integrating the Ca-looping with a cement plant that makes use of the solid purge. 70 % of the CO2 generated in the existing plant is captured under these conditions, with an overall CO2 capture in the process over 86 %. Different scenarios with high circulation rates between reactors could be also proposed to achieve a determined CO2 capture efficiency. In this case the optimal thermal integration for the new scenarios should be evaluated as the energy availability in the process streams and the consumptions of the main equipments in the process would be different. (C) 2011 Published by Elsevier Ltd.
引用
收藏
页码:1699 / 1706
页数:8
相关论文
共 17 条
  • [1] Fluidized bed combustion systems integrating CO2 capture with CaO
    Abanades, JC
    Anthony, EJ
    Wang, JS
    Oakey, JE
    [J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2005, 39 (08) : 2861 - 2866
  • [2] Modelling of a fluidized bed carbonator reactor to capture CO2 from a combustion flue gas
    Alonso, M.
    Rodriguez, N.
    Grasa, G.
    Abanades, J. C.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2009, 64 (05) : 883 - 891
  • [3] [Anonymous], CONTRIBUTION WORKING
  • [4] Solid looping cycles: A new technology for coal conversion
    Anthony, Edward J.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (06) : 1747 - 1754
  • [5] EFFECT OF THE PRODUCT LAYER ON THE KINETICS OF THE CO2-LIME REACTION
    BHATIA, SK
    PERLMUTTER, DD
    [J]. AICHE JOURNAL, 1983, 29 (01) : 79 - 86
  • [6] The calcium looping cycle for large-scale CO2 capture
    Blamey, J.
    Anthony, E. J.
    Wang, J.
    Fennell, P. S.
    [J]. PROGRESS IN ENERGY AND COMBUSTION SCIENCE, 2010, 36 (02) : 260 - 279
  • [7] Application of the Random Pore Model to the Carbonation Cyclic Reaction
    Grasa, Gemma
    Murillo, Ramon
    Alonso, Monica
    Abanades, J. Carlos
    [J]. AICHE JOURNAL, 2009, 55 (05) : 1246 - 1255
  • [8] Process analysis of CO2 capture from flue gas using carbonation/calcination cycles
    Li Zhen-shan
    Cai Ning-sheng
    Croiset, Eric
    [J]. AICHE JOURNAL, 2008, 54 (07) : 1912 - 1925
  • [9] Metz B, 2005, SPECIAL REPORT CARBO
  • [10] Heat requirements in a calciner of CaCO3 integrated in a CO2 capture system using CaO
    Rodriguez, N.
    Alonso, M.
    Grasa, G.
    Abanades, J. Carlos
    [J]. CHEMICAL ENGINEERING JOURNAL, 2008, 138 (1-3) : 148 - 154