Influence of Steam Injection during Calcination on the Reactivity of CaO-Based Sorbent for Carbon Capture

被引:88
作者
Champagne, Scott [1 ]
Lu, Dennis Y. [2 ]
Macchi, Arturo [1 ]
Symonds, Robert T. [2 ]
Anthony, Edward J. [2 ]
机构
[1] Univ Ottawa, Dept Chem & Biol Engn, Ottawa, ON K1N 6N5, Canada
[2] Nat Resources Canada, CanmetENERGY, Ottawa, ON K1A 1M1, Canada
关键词
HIGH-TEMPERATURE STEAM; LOOPING CYCLE REACTOR; CO2; CAPTURE; CALCIUM-OXIDE; PILOT-SCALE; HYDRATION; CAPACITY; DIOXIDE; CARBONATION/CALCINATION; REACTIVATION;
D O I
10.1021/ie3012787
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Calcium looping is an emerging CO2 capture technology based on cyclic calcination/carbonation reactions using calcium-based sorbents. Steam is typically present in flue/fuel gas streams from combustion or gasification and in the calciner used for sorbent regeneration. The effect of steam in the calciner on sorbent performance has received little attention in the literature. Here, experiments were conducted using a thermogravimetric analyzer (TGA) to determine the effect of steam injection during calcination on sorbent reactivity during carbonation. Two Canadian limestones, Cadomin and Havelock, were tested, and various levels of steam (up to 40%) were injected in the sorbent regeneration process for 15 calcination/carbonation cycles. All concentrations of steam examined were found to increase sorbent reactivity for carbonation for both sorbents. In these experiments, 15% steam concentration with calcination had the largest impact on carrying capacity for both sorbents. Steam changes the morphology of the sorbent while calcination is occurring, probably causing a shift from smaller to larger pores, resulting in a structure which increases carrying capacity. It was also demonstrated that steam addition produced a larger impact on sorbent reactivity for carbonation than for calcination.
引用
收藏
页码:2241 / 2246
页数:6
相关论文
共 28 条
  • [1] Separation of CO2 from flue gas:: A review
    Aaron, D
    Tsouris, C
    [J]. SEPARATION SCIENCE AND TECHNOLOGY, 2005, 40 (1-3) : 321 - 348
  • [2] Conversion limits in the reaction of CO2 with lime
    Abanades, JC
    Alvarez, D
    [J]. ENERGY & FUELS, 2003, 17 (02) : 308 - 315
  • [3] Determination of the critical product layer thickness in the reaction of CaO with CO2
    Alvarez, D
    Abanades, JC
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2005, 44 (15) : 5608 - 5615
  • [4] Solid looping cycles: A new technology for coal conversion
    Anthony, Edward J.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2008, 47 (06) : 1747 - 1754
  • [5] The Effect of Steam on the Fast Carbonation Reaction Rates of CaO
    Arias, B.
    Grasa, G.
    Abanades, J. C.
    Manovic, V.
    Anthony, E. J.
    [J]. INDUSTRIAL & ENGINEERING CHEMISTRY RESEARCH, 2012, 51 (05) : 2478 - 2482
  • [6] CALCIUM OXIDE-CARBON DIOXIDE SYSTEM IN PRESSURE RANGE 1-300 ATMOSPHERES
    BAKER, EH
    [J]. JOURNAL OF THE CHEMICAL SOCIETY, 1962, (FEB): : 464 - &
  • [7] 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] Influence of High-Temperature Steam on the Reactivity of CaO Sorbent for CO2 Capture
    Donat, Felix
    Florin, Nicholas H.
    Anthony, Edward J.
    Fennell, Paul S.
    [J]. ENVIRONMENTAL SCIENCE & TECHNOLOGY, 2012, 46 (02) : 1262 - 1269
  • [10] High temperature CO2 capture using calcium oxide sorbent in a fixed-bed reactor
    Dou, Binlin
    Song, Yongchen
    Liu, Yingguang
    Feng, Cong
    [J]. JOURNAL OF HAZARDOUS MATERIALS, 2010, 183 (1-3) : 759 - 765