Use of limestone for SO2 removal from flue gas in the semidry FGD process with a powder-particle spouted bed

被引:241
|
作者
Ma, XX
Kaneko, T
Tashimo, T
Yoshida, T
Kato, K [1 ]
机构
[1] Gunma Univ, Dept Biol & Chem Engn, Kiryu, Gumma 3768515, Japan
[2] Hokkaido Natl Ind Res Inst, Toyohira Ku, Sapporo, Hokkaido 0628517, Japan
关键词
environmental protection; flue gas desulfurization (FGD); particle; slurry; limestone; powder-particle spouted bed;
D O I
10.1016/S0009-2509(00)00090-7
中图分类号
TQ [化学工业];
学科分类号
0817 ;
摘要
Hydrated lime is normally used as SO2 sorbent in spray dry scrubbers, whereas limestone is considered unreactive under conditions prevailing in such a system. However, limestone is more easily available and several times cheaper than hydrated lime. We tried to use limestone to remove SO2 from flue gas in the semidry FGD process with a powder-particle spouted bed. If limestone can be utilized in the process it would be of particular advantage. In the present study, the effects of operating parameters on SO2 removal were investigated, such as Ca/S molar ratio, particle size of SO2 sorbent, apparent residence time of gas in the bed and approach to saturation temperature. The comparison of reactivity with SO2 between limestone and hydrated lime was also made based on their structural properties. The experimental results showed that SO2 removal efficiency of limestone was considerably enhanced in the present process by increasing Ca/S molar ratio and decreasing the approach to saturation temperature and sorbent size. Thus, the present process with limestone as SO2 sorbent may be an attractive alternative to other FGD technologies in terms of removal efficiency, price and availability of sorbent. (C) 2000 Elsevier Science Ltd. All rights reserved.
引用
收藏
页码:4643 / 4652
页数:10
相关论文
共 50 条
  • [1] Influence of gas components on removal of SO2 from flue gas in the semidry FGD process with a powder-particle spouted bed
    Ma, X
    Kaneko, T
    Xu, G
    Kato, K
    [J]. FUEL, 2001, 80 (05) : 673 - 680
  • [2] Removal of SO2 from flue gas using a new semidry flue gas desulfurization process with a powder-particle spouted bed
    Ma, XX
    Kaneko, T
    Guo, QM
    Xu, GW
    Kato, KN
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 1999, 77 (02): : 356 - 362
  • [3] Effects of the operating conditions on SO2 removal from flue gas using a new semidry desulfurization process with a powder-particle spouted bed
    Ma, XX
    Kaneko, T
    Xu, GW
    Kato, K
    [J]. PROSPECTS FOR COAL SCIENCE IN THE 21ST CENTURY, 1999, : 1317 - 1320
  • [4] Use of different sorbents in the semidry FGD process with a powder-particle spouted bed
    Ma, XX
    Nakazato, T
    Xu, GW
    Wang, C
    Nakagawa, N
    Kato, K
    [J]. Circulating Fluidized Bed Technology VIII, 2005, : 786 - 793
  • [5] The effect of operating conditions on SO2 removal in semidry desulfurization process by powder-particle spouted bed
    Guo, QM
    Kato, K
    [J]. KAGAKU KOGAKU RONBUNSHU, 1998, 24 (02) : 279 - 284
  • [6] Removal of SO2 in semi-dry flue gas desulfurization process with a powder-particle spouted bed
    Nakazato, T
    Liu, YY
    Kato, K
    [J]. CANADIAN JOURNAL OF CHEMICAL ENGINEERING, 2004, 82 (01): : 110 - 115
  • [7] A novel dry process for simultaneous removal of SO2 and NO from flue gas in a powder-particle fluidized bed
    Luo, GH
    Yoneda, A
    Kato, K
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 2001, 24 (04) : 361 - 366
  • [8] Process analysis of semidry desulfurization process in powder-particle spouted bed
    Liu, YY
    Kato, K
    [J]. JOURNAL OF CHEMICAL ENGINEERING OF JAPAN, 2000, 33 (02) : 223 - 231
  • [9] Flue gas desulfurization by a powder-particle spouted bed
    Moeini, Mohammad
    Hatamipour, Mohammad Sadegh
    [J]. CHEMICAL ENGINEERING & TECHNOLOGY, 2008, 31 (01) : 71 - 82
  • [10] Simultaneous SO2/NOx removal by a powder-particle fluidized bed
    Gao, SQ
    Nakagawa, N
    Kato, K
    Inomata, M
    Tsuchiya, F
    [J]. CATALYSIS TODAY, 1996, 29 (1-4) : 165 - 169