CaO carbonation kinetics determined using micro-fluidized bed thermogravimetric analysis

被引:45
作者
Li, Ye [1 ]
Li, Zhenshan [1 ]
Wang, Hui [1 ]
Cai, Ningsheng [1 ]
机构
[1] Tsinghua Univ, Dept Energy & Power Engn, Minist Educ, Key Lab Thermal Sci & Power Engn, Beijing 100084, Peoples R China
基金
中国国家自然科学基金; 欧盟地平线“2020”;
关键词
Micro-fluidized bed thermogravimetric analysis (MFB-TGA); CaO carbonation reaction; Kinetics; HIGH-TEMPERATURE; CO2; CAPTURE; PRODUCT LAYER; DIRECT SULFATION; MODEL; STEAM; COMBUSTION; HYDROGEN; SORBENT; ENERGY;
D O I
10.1016/j.fuel.2019.116823
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
A micro-fluidized bed thermogravimetric analysis (MFB-TGA) method based on real-time mass measurement of solid sample inside a fluidized bed was developed. This technique was used to measure the fast reaction kinetics of CaO carbonation in calcium looping with similar characteristics of a strong mass and heat transfer in the fluidized bed reactor. The effects of particle size, temperature, and CO2 concentration on the fast reaction kinetics of CaO carbonation were investigated. The experimental data measured upon MFB-TGA were interpreted with a K-L two-phase fluidized bed model to evaluate the effect of gas exchange between the bubble phase and the emulsion phase on the carbonation kinetics. We concluded that the kinetics of CaO carbonation measured by MFB-TGA were faster than those measured via regular TGA. The reaction rate constant (ks) was 8.0 x 10(-10) m(4)/(mol.s), the activation energy of the carbonation reaction was near zero, and the reaction was first order when the CO2 concentration was within 50 vol% (1 bar). This MFB-TGA method provides a new experimental idea and method for measuring gas-solid reaction kinetics occurring inside fluidized bed reactors.
引用
收藏
页数:8
相关论文
共 50 条
  • [1] Conversion limits in the reaction of CO2 with lime
    Abanades, JC
    Alvarez, D
    [J]. ENERGY & FUELS, 2003, 17 (02) : 308 - 315
  • [2] 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
  • [3] Capture of CO2 from combustion gases in a fluidized bed of CaO
    Abanades, JC
    Anthony, EJ
    Lu, DY
    Salvador, C
    Alvarez, D
    [J]. AICHE JOURNAL, 2004, 50 (07) : 1614 - 1622
  • [4] Undesired effects in the determination of CO2 carrying capacities of CaO during TG testing
    Alonso, M.
    Criado, Y. A.
    Abanades, J. C.
    Grasa, G.
    [J]. FUEL, 2014, 127 : 52 - 61
  • [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] CaCO3 Crystallite Evolution during CaO Carbonation: Critical Crystallite Size and Rate Constant Measurement by In-Situ Synchrotron Radiation X-ray Powder Diffraction
    Biasin, A.
    Segre, C. U.
    Strumendo, M.
    [J]. CRYSTAL GROWTH & DESIGN, 2015, 15 (11) : 5188 - 5201
  • [7] Investigation of CaO-CO2 reaction kinetics by in-situ XRD using synchrotron radiation
    Biasin, A.
    Segre, C. U.
    Salviulo, G.
    Zorzi, F.
    Strumendo, M.
    [J]. CHEMICAL ENGINEERING SCIENCE, 2015, 127 : 13 - 24
  • [8] 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
  • [9] Kinetics of the Oxidation of a Co-precipitated Mixture of Cu and Al2O3 by O2 for Chemical-Looping Combustion
    Chuang, S. Y.
    Dennis, J. S.
    Hayhurst, A. N.
    Scott, S. A.
    [J]. ENERGY & FUELS, 2010, 24 (07) : 3917 - 3927
  • [10] The calcium looping cycle for CO2 capture from power generation, cement manufacture and hydrogen production
    Dean, C. C.
    Blamey, J.
    Florin, N. H.
    Al-Jeboori, M. J.
    Fennell, P. S.
    [J]. CHEMICAL ENGINEERING RESEARCH & DESIGN, 2011, 89 (6A) : 836 - 855