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循环流化床烟气脱硫模拟中试试验研究

冯斌 李大骥 周志良 吴颖海 杨军

东南大学学报(自然科学版)2001,Vol.31Issue(2):72-76,5.
东南大学学报(自然科学版)2001,Vol.31Issue(2):72-76,5.

循环流化床烟气脱硫模拟中试试验研究

Experimental Research on a Pilot-Scale Circulating Fluidized Bed for Flue Gas Desulfurization

冯斌 1李大骥 1周志良 2吴颖海 1杨军1

作者信息

  • 1. 东南大学热能工程研究所, 南京 210096
  • 2. 江苏省昆山市环保局管理处, 昆山 215300
  • 折叠

摘要

Abstract

At present, SO2 pollution control of coal combustion is an urgenttask in the field of air pollution control in China. An experimental research was carried on the simulated pilot-scale test facility of Circulating Fluidized Bed for Flue Gas Desulfurization (CFB-FGD) whose diameter is 600mm and nominal flow rate of the flue gas is 2 000 m3/h in Thermal Engineering Research Institute of Southeast University. The Ca/S molar ratio and the reaction temperature have great influence on the efficiency of desulfurization, but the influences of the flow rate and SO2 inlet concentration are not obvious. So the result indicates that CFB-FGD technology is applicable for the variation of the boiler’s load and the coal used.

关键词

循环流化床烟气脱硫/模拟中试/Ca与S的摩尔比/烟气流量/入口SO2浓度/反应温度/反应湿度

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引用本文复制引用

冯斌,李大骥,周志良,吴颖海,杨军..循环流化床烟气脱硫模拟中试试验研究[J].东南大学学报(自然科学版),2001,31(2):72-76,5.

东南大学学报(自然科学版)

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