Mechanism and kinetics of high-temperature flue gas desulfurization with magnesia tailings as a desulfurization sorbent

被引:0
作者
Li H. [1 ]
Fu L. [1 ,2 ]
Yang H. [1 ]
Xu G. [1 ]
Bai D. [1 ]
机构
[1] Institute of Industrial Chemistry and Energy Technology, Shenyang University of Chemical Technology, Shenyang
[2] School of Chemical Engineering, University of Science and Technology Liaoning, Anshan
来源
Gao Xiao Hua Xue Gong Cheng Xue Bao/Journal of Chemical Engineering of Chinese Universities | 2023年 / 37卷 / 06期
关键词
calcination; desulfurization; diffusion; Magnesite; micro fluidized bed; sulfation;
D O I
10.3969/j.issn.1003-9015.2023.06.016
中图分类号
学科分类号
摘要
High-temperature flue gas desulfurization using magnesite tailings as a sorbent has economic and environmental benefits. In order to assess the feasibility, the reaction mechanism and kinetic characteristics of high-temperature flue gas desulfurization using magnesite tailings as the sorbent were studied via a micro fluidized bed reaction analyzer (MFBRA). The dynamics of magnesite calcination and sulfation, and the evolution of the inner pore structure of magnesite particles were studied. The results show that the reaction process includes a calcination reaction of magnesite to MgO, and a sulfation reaction between MgO and SO2 to form MgSO4. The calcination reaction rate is faster than the sulfation reaction. Decomposition of magnesite is fast at beginning that resulted in quick increase of MgO and also the sulfation reaction between MgO and SO2. The amount of nascent MgO consumed by the sulfation reaction is low and the available MgO is excessive. After that period the sulfation reaction rate increases, thereby the formation of MgSO4 increases accordingly. The increased MgSO4 covers MgO surface that leads to a reduction of sulfation rate. The calcination rate of MgCO3 reduces in the later stage and the internal pore formation slows down with dense MgSO4 layer covers small pores. Consequently, the sulfation reaction rate tends to be controlled by the diffusion through the MgSO4 layer, leaving some MgCO3 and MgO unreacted at the end of the operation. © 2023 Zhejiang University. All rights reserved.
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页码:1007 / 1016
页数:9
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共 35 条
  • [1] CHEN P., Properties, classification and utilization of coal in China, Journal of Fuel Chemistry and Technology, 30, 1, pp. 71-71, (2002)
  • [2] National Statistical Yearbook 2020
  • [3] ZHAO Y C, MA S M, YANG J P, Et al., Status of ultra-low emission technology in coal-fired power plant, Journal of China Coal Society, 40, 11, pp. 2629-2640, (2015)
  • [4] CHEN L, WANG C B, YAN G J., Research progress of SO<sub>2</sub> removal with limestone in CFB boilers, Chemical Industry and Engineering Progress, 38, 5, pp. 2451-2460, (2019)
  • [5] OZDEMIR K, SERINCAN M F., A computational fluid dynamics model of a rotary regenerative heat exchanger in a flue gas esulfurization system, Applied Thermal Engineering, 143, pp. 988-1002, (2018)
  • [6] ZHU Y L, ZHAO Y H, ZHANG S, Et al., The research on desulfurization technology in coal-fired power plant, Tianjin Chemical Industry, 32, 2, pp. 1-3, (2018)
  • [7] MENG Q H., Research and application on increasing desulfurization efficiency of circulating fluidized bed boiler, Energy Conservation Technology, 34, 1, pp. 68-72, (2016)
  • [8] CHEN L, WANG Z M, WANG C B., Limestone calcination kinetics in simultaneous calcination and sulfation under CFB conditions, CIESC Journal, 68, 12, pp. 4615-4624, (2017)
  • [9] WANG H M., Analysis and optimization of desulfurization system in circulating fluidized bed boiler, Inner Mongolia Coal Economy, 12, pp. 33-34, (2019)
  • [10] WANG C, CHEN L, JIA L, Et al., Simultaneous calcination and sulfation of limestone in CFBB, Applied Energy, 155, pp. 478-484, (2015)