System for the liquid-phase removal of a component from the gas stream especially the absorption of sulfur trioxide in sulfuric acid
    1.
    发明授权
    System for the liquid-phase removal of a component from the gas stream especially the absorption of sulfur trioxide in sulfuric acid 失效
    用于从气体流中液相移除组分的系统特别是在硫酸中吸收三氧化硫

    公开(公告)号:US3780499A

    公开(公告)日:1973-12-25

    申请号:US3780499D

    申请日:1971-10-12

    发明人: DORR K GRIMM H KOLA R

    IPC分类号: B01D53/14 C01B17/80 C01B17/90

    摘要: A process for the removal of gaseous components from a gas stream by liquid-phase absorption of the component in the treatment of the gas with a liquid, especially the absorption of sulfur trioxide from a gas stream obtained by the contactcatalysis oxidation of sulfur dioxide in the production of sulfuric acid, makes use of a uniflow vertical venturi absorber followed by a turbulencing device or horizontal venturi absorber and a counterflow column absorber or tower. The absorbing liquid is sulfuric acid.

    摘要翻译: 一种通过在用液体处理气体中液体吸收组分从气流中除去气体组分的方法,特别是从通过二氧化硫的接触催化氧化获得的气流中吸收三氧化硫 在生产硫酸时,使用一个单向垂直文丘里吸收器,随后是湍流装置或水平文丘里吸收器和逆流柱吸收塔或塔。 吸收液体是硫酸。

    Absorber for sulfur trioxide
    2.
    发明授权
    Absorber for sulfur trioxide 失效
    吸收三氧化硫

    公开(公告)号:US3788043A

    公开(公告)日:1974-01-29

    申请号:US3788043D

    申请日:1971-10-12

    发明人: DORR K GRIMM H KOLA R

    摘要: In a contact process for transforming sulfur dioxide to sulfur trioxide, between the contact stages there is provided an interstage absorber for removing sulfur trioxide for the gases emerging from a previous stage. The gases are passed by a venturi system in intimate contact with sulfuric acid into a settling chamber in which sulfuric acid is collected in the sump and then, by another gas/liquid contactor or reagitator, into a further settling chamber with an outlet at its upper end.

    摘要翻译: 在将二氧化硫转化为三氧化硫的接触方法中,在接触阶段之间,提供了用于从前一阶段出现的气体中除去三氧化硫的级间吸收剂。 气体通过与硫酸紧密接触的文氏管系统进入沉淀室,其中将硫酸收集在贮槽中,然后通过另一种气/液接触器或反应器进入另一沉淀室,在其上部具有出口 结束。

    Method of removing so{11 {11 and h{11 so{11 {11 mist from a gas stream
    3.
    发明授权
    Method of removing so{11 {11 and h{11 so{11 {11 mist from a gas stream 失效
    除去气体的方法[11] {11和H {11 SO {11 {11气体从气体流

    公开(公告)号:US3853502A

    公开(公告)日:1974-12-10

    申请号:US28710472

    申请日:1972-09-07

    CPC分类号: B01D53/507 C01B17/74

    摘要: A method of removing sulfur trioxide (SO3) and surfuric-acid mist from the end gas of a contact-catalysis process for the production of sulfuric acid involves intimately contacting the dry end gas, containing SO3 and/or sulfuric acid mist, with a water-diluted sulfuric-acid treating solution to increase the water-vapor content of the end gas in accordance with the vapor pressure of water in the dilute acid. The liquid phase, consisting of sulfuric acid present in the treating solution, formed by dissolution of SO3 in water and present as the sulfuric acid mist, is removed or separated from the gas which is released into the atmosphere substantially free from sulfuric acid or SO3.

    摘要翻译: 从用于生产硫酸的接触催化过程的末端气体中除去三氧化硫(SO 3)和磺酸雾的方法包括使含有SO 3和/或硫酸雾的干燥末端气体与水紧密接触 稀释的硫酸处理溶液,以根据稀酸中水的蒸气压来增加末端气体的水汽含量。 由SO3溶解在水中形成并以硫酸雾形式存在的处理溶液中存在的硫酸的液相从释放到基本上不含硫酸或SO 3的气氛中的气体中除去或分离。

    Process of catalytically reacting so2 to form so3 and of producing sulfuric acid
    4.
    发明授权
    Process of catalytically reacting so2 to form so3 and of producing sulfuric acid 失效
    催化SO2反应形成SO3和生产硫酸的方法

    公开(公告)号:US3780166A

    公开(公告)日:1973-12-18

    申请号:US3780166D

    申请日:1969-07-08

    IPC分类号: C01B17/765 C01B17/76

    CPC分类号: C01B17/7655

    摘要: A PROCESS OF CATALYTICALLY REACTING SO2-CONTAINING GAS TO FORM SO3 IN A CATALYTIC PLANT INCLUDING A PLURALITY OF CATALYST STAGES AND IN WHICH SO3 IS CONDENSED BETWEEN CATALYST STAGES FORMING SULFURIC ACID, CHARACTERIZED IN THAT:

    (A) THE SO3-CONTAINING GAS LEAVING THE FIRST OF TWO SUCCESSIVE STAGES IS TRANSFERRED ALONG A CLOSED FLOW PATH INTO THE SECOND OF SAID TWO STAGES; (B) A PARTIAL STREAM IS SEPARATED FROM SAID TRANSFERRED STREAM AND COOLED, AND SO3 IS CONDENSED FROM THE PARTIAL STREAM; (C) SAID PARTIAL STREAM FOLLOWING SAID CONDENSING IS COMBINED WITH THE BALANCE OF SAID TRANSFERRED STREAM AND AND THE COMBINED STREAM IS INTRODUCED INTO THE SECOND CATALYST STAGE.