Process for dehydrating gas with sulfuric acid
    1.
    发明授权
    Process for dehydrating gas with sulfuric acid 失效
    用硫酸脱气的方法

    公开(公告)号:US4023938A

    公开(公告)日:1977-05-17

    申请号:US568341

    申请日:1975-04-15

    摘要: In the removal of water from a gas by contact with sulfuric acid, the improvement which comprises supplying the sulfuric acid in finely divided form having a surface of about 10.sup.4 to 10.sup.7 m.sup.2 /h at a concentration of about 95 to 99% and a temperature of about 35.degree. to 80.degree. C and with a contact time of about 0.2 to 2 seconds, whereby the residual moisture content of the gas is reduced to about 30 to 250 mg of H.sub.2 O/Nm.sup.3. Preferably the sulfuric acid is sprayed through a constriction into a vessel through which the gas is passed. The large sulfuric acid surface area permits high levels of dehydration to be achieved with far less sulfuric acid than heretofore believed possible and with small vessels and minimal contact times. Contact may be effected serially in several stages with the spent acids combined, brought up to initial concentration and recirculated.

    摘要翻译: 在通过与硫酸接触从气体除去水时,其改进包括以约95至99%的浓度提供具有约104至107m 2 / h表面的细碎形式的硫酸和温度 约35℃至80℃,接触时间约0.2至2秒,从而将气体的残留水分降低至约30至250mg的H 2 O / Nm 3。 优选地,硫酸通过收缩部喷射到气体通过的容器中。 大的硫酸表面积允许以比迄今所认为可能的少得多的硫酸和小容器和最小的接触时间来实现高水平的脱水。 接触可以在几个阶段中连续进行,废酸组合,达到初始浓度并再循环。

    Process for producing sulfuric acid from waste acid and iron sulfate
    4.
    发明授权
    Process for producing sulfuric acid from waste acid and iron sulfate 失效
    从废酸和硫酸铁生产硫酸的方法

    公开(公告)号:US4163047A

    公开(公告)日:1979-07-31

    申请号:US811798

    申请日:1977-06-30

    CPC分类号: C01B17/901 Y10S423/02

    摘要: A process for the recovery of sulfuric acid from waste sulfuric acid containing iron sulfate and from solid iron sulfate of high water content of crystallization which consists essentially of:A. concentrating waste sulfuric acid to an acid concentration of 25-55 weight percent, based upon the suspension, by removing water therefrom;B. mixing the concentrated acid of Step A with recycled concentrated sulfuric acid obtained from Step E to form a resultant acid mixture of acid concentration of 30-65 weight percent, based upon the suspension;C. adding said solid iron sulfate of high water content of crystallization to the acid mixture of Step B thereby obtaining iron sulfate of low water content of crystallization;D. separating the iron sulfate of low water content from the resultant sulfuric acid solution of Step C;E. concentrating the separated sulfuric acid solution of Step D to an acid concentration of 45-70 weight percent, based on salt-free acid, and recycling at least a portion thereof to Step B; andF. thermally decomposing the iron sulfate from Step D to produce iron oxide and sulfur dioxide.

    摘要翻译: 一种从含硫酸铁的废硫酸和硫酸高固含量的硫酸中回收硫酸的方法,该方法主要包括:

    Working up spent sulphuric acid simultaneously with sulphate salts
    5.
    发明授权
    Working up spent sulphuric acid simultaneously with sulphate salts 失效
    与硫酸盐同时处理废硫酸

    公开(公告)号:US4153628A

    公开(公告)日:1979-05-08

    申请号:US836465

    申请日:1977-09-26

    摘要: Spent sulphuric acid, either alongside or mixed with contaminated metal salts such as iron sulphate heptahydrate, is regenerated to fresh acid by countercurrent contact with gases from cleavage of the sulphate salts, such gases containing SO.sub.3 which effects build up of the acid concentration. The built up acid is evaporated in another stage to obtain pure acid. The metal sulphate solids are subjected to high temperature cleavage, generating SO.sub.3 which effects the previous concentration. Cleavage also produces some SO.sub.2 which is converted to SO.sub.3 by wet catalysis.

    摘要翻译: 与受污染的金属盐(如七水硫酸铁)一起或与其混合的硫酸可以通过与硫酸盐裂解的气体逆流接触而再生成新鲜的酸,这些气体含有SO 3,从而产生酸浓度。 在另一个阶段将积聚的酸蒸发得到纯酸。 金属硫酸盐固体经受高温裂解,产生影响先前浓度的SO 3。 裂解还产生一些SO2,其通过湿催化转化为SO 3。