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    • 1. 发明授权
    • Process for removing contaminants from hot waste gas streams
    • 从热废气流中除去污染物的工艺
    • US3957951A
    • 1976-05-18
    • US499837
    • 1974-08-23
    • Allan E. HokansonRaphael KatzenEdward F. Button
    • Allan E. HokansonRaphael KatzenEdward F. Button
    • B01D53/22B01D53/50B01D53/77C01B17/60C01C1/22C01B17/00
    • C01C1/22B01D53/501
    • A process for removing sulfur dioxide and other contaminants from a hot waste gas stream in which the waste gas stream is cooled to a temperature below 100.degree.F and then passed in sequence through two separate absorption zones utilizing as the absorbent a recirculated aqueous solution of ammonium sulfite-bisulfite salts. Heat is continuously withdrawn from the recirculated salt solution in each zone. The absorbent solution in the first zone has an initial pH of from 6 to 7.2 and a salt concentration of from 1 to 20% by weight. The absorbent solution in the second zone has an initial pH of from 5.2 to 6.5 and a salt concentration, lower than said first zone of, from 0.1 to 5% by weight. The process provides for the efficient absorption and substantial removal of SO.sub.2, SO.sub.3 and particulate contaminants and for the economic recovery and use of heat from stack gases of a variety of industrial and commercial operations.
    • 一种从热废气流中除去二氧化硫和其他污染物的方法,其中将废气流冷却至低于100°F的温度,然后依次通过两个单独的吸收区,作为吸收剂,再循环的铵水溶液 亚硫酸盐 - 亚硫酸氢盐。 在每个区域中从再循环的盐溶液中连续排出热量。 第一区中的吸收剂溶液的初始pH为6至7.2,盐浓度为1至20重量%。 第二区域中的吸收剂溶液的初始pH为5.2至6.5,盐浓度低于所述第一区域的0.1至5重量%。 该过程提供了SO2,SO3和颗粒污染物的有效吸收和实质性去除,以及经济回收和使用来自各种工业和商业操作的烟道气体的热量。