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Conversion of sulphur di:oxide to sulphur in waste gas - where gas is fed continuously through heated fluidised bed of coal

机译:将二氧化硫转化为废气中的硫-气体通过加热的煤流化床连续供入

摘要

The SO2 content of a gas stream is continuously reduced, where the gas travels at a speed (S) at least 1 foot/second faster than the min. fluidising speed of a bed of fine coal and solid diluent in a reactor fed with the gas; but speed is slow enough to prevent fine material being carried out of the bed. The reaction zone is held at 593-1093 degrees, esp. 704-982 degrees C and coal is fed continuously into the bed; the gaseous prods. are continuously removed for the winning of sulphur. The pref. coal is brown coal; sub-bituminous coal; bituminous coal; and/or anthracite; whereas the filuent is pref. sand.
机译:气流中的SO2含量不断降低,其中气体以至少比最小速度快1英尺/秒的速度(S)传播。在装有气体的反应器中细煤和固体稀释剂床的流化速度;但是速度足够慢,无法阻止细料从床中运出。反应区保持在593-1093度,尤其是。 704-982摄氏度,煤被连续送入煤层;气态的产物。不断去除以赢得硫。偏好。煤是褐煤;亚烟煤烟煤;和/或无烟煤;而稀释剂是优选的。砂。

著录项

  • 公开/公告号FR2373326A1

    专利类型

  • 公开/公告日1978-07-07

    原文格式PDF

  • 申请/专利权人 ALLIED CHEMICAL CORP;

    申请/专利号FR19770036565

  • 发明设计人

    申请日1977-12-05

  • 分类号B01D53/34;B01J8/24;C01B17/04;

  • 国家 FR

  • 入库时间 2022-08-22 21:43:31

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