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    • 2. 发明授权
    • Process for working up the wash solution obtained in the washing of
SO.sub.2 -containing off-gases
    • 处理在洗涤SO(HD 2(含B的废气)中获得的洗涤溶液的方法
    • US3954955A
    • 1976-05-04
    • US284709
    • 1972-08-30
    • Herbert Furkert
    • Herbert Furkert
    • C01B17/60C01B17/76C01B17/50
    • C01B17/76C01B17/60
    • In a process which comprises scrubbing an SO.sub.2 -containing gas with an aqueous ammonia solution to form ammonium sulfite and ammonium bisulfite as reaction products, neutralizing said reaction products with sulfuric acid to form SO.sub.2 and aqueous ammonium sulfate, and concentrating the resultant aqueous ammonium sulfate by evaporation, the improvement which comprises:A. heating the concentrated aqueous ammonium sulfate to a temperature of 900.degree.-1250.degree.C in a combustion chamber burning a carbon or sulfur containing fuel, in the presence of sufficient oxygen to maintain an oxygen content of 1-10 vol % in the gas exiting from the combustion chamber, to form a hot split gas consisting essentially of sulfur dioxide, sulfur trioxide, molecular nitrogen, molecular oxygen and water vapor; andB. heat exchanging the hot split gas with the aqueous ammonium sulfate to evaporate the aqueous ammonium sulfate to a concentrate having a water content of less than 55 wt. %, thereby cooling said hot split gas.The split gas can be furhter worked up for any purpose which an SO.sub.2 -containing gas is suitable, e.g., for the production of sulfuric acid.
    • 在包括用氨水溶液洗涤含SO 2的气体以形成亚硫酸铵和亚硫酸氢铵作为反应产物的方法中,用硫酸中和所述反应产物以形成SO 2和硫酸铵水溶液,并将所得的硫酸铵水溶液浓缩 蒸发,其改进包括:
    • 4. 发明授权
    • Process for working up the scrubbing solution obtained in the scrubbing
of So.sub.2 -containing waste gases
    • 处理在洗涤So(hd 2 {b-含有废气中)中获得的洗涤溶液的方法
    • US3950502A
    • 1976-04-13
    • US418273
    • 1973-11-23
    • Herbert Furkert
    • Herbert Furkert
    • C01B17/60C01B17/76C01B17/50
    • C01B17/60C01B17/76
    • Process for working up the scrubbing solution obtained during the scrubbing of SO.sub.2 -containing waste gases, which can also contain SO.sub.3, with the use of ammonia, by evaporation in direct heat exchange with hot cracked gas to a water content of between 15 and 55% by weight, cracking of the thus-evaporated mixture at temperatures of between 900.degree. and 1250.degree. C. with the concomitant combustion of a carbon- and/or sulfur-containing fuel to an SO.sub.2 -containing gas, and processing of the cracked gas, after utilization for evaporation purposes, by contact oxidation to sulfuric acid in accordance with U.S. patent application Ser. 284,709 filed Aug. 30, 1972, characterized in that the scrubbing solution is mixed, prior to or during the evaporation, with a quantity of sulfuric acid sufficient for the liberation of SO.sub.2 from 0-83% of the sulfite and/or bisulfite present in the solution.
    • 在用热裂解气体与热裂解气体直接热交换蒸发至含水量为15%至55%之间的过程中,通过蒸发除去也可以含有SO 3的含SO 2的废气在洗涤期间获得的洗涤溶液的处理方法, ,在900〜1250℃的温度下将这样蒸发的混合物裂解,同时伴随着含碳和/或含硫燃料与含SO 2的气体的燃烧,以及加工裂化气体, 用于蒸发目的后,按照美国专利申请Ser。 284709,1972年8月30日提交,其特征在于,在蒸发之前或期间,将洗涤溶液与足量的硫酸一起混合,所述硫酸足以释放存在于亚硫酸盐中的0-83%的亚硫酸盐和/或亚硫酸氢盐 解决方案。