• CSCD核心库收录期刊
  • 中文核心期刊
  • 中国科技核心期刊

ELECTRIC POWER CONSTRUCTION ›› 2015, Vol. 36 ›› Issue (6): 109-113.doi: 10.3969/j.issn.1000-7229.2015.06.018

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Technical Economic Analysis and Optimization of Two-Stage Desulfurization System for CFB Boiler

ZHU Yunfei1, YAN Weiping1, WANG Yupeng1, ZHANG Xiaoling1, MA Fei2   

  1. 1. School of Energy and Power Engineering, North China Electric Power University, Baoding 071003, Hebei Province, China;2. Shanxi Jingyu Power Generation Co., Ltd., Shuozhou 036000, Shanxi Province, China
  • Online:2015-06-01

Abstract:

To reduce the emissions of SO2 from the circulating fluidized bed (CFB) boiler to meet the increasingly stringent emission standards, this paper focused on the two-stage desulfurization system including the limestone desulfurization in the furnace of CFB boiler and the wet limestone-gypsum flue gas desulfurization (FGD). Relying on the investment equipment and operating costs in a 300 MW CFB unit with two-stage desulfurization system, this paper analyzed the impact of SO2 emission limits, sulfur content in coal, unit load, initial investment in desulfurization equipment and annual effective performance time on the economy of CFB-FGD two-stage intensified desulfurization system, finally obtained a reasonable scheme of desulfurization share.

Key words: circulating fluidized bed(CFB) boiler, two-stage intensified desulfurization, desulfurization share, furnace desulfurization, flue gas desulfurization

CLC Number: