Process for the internal coating of contact tubes
    3.
    发明授权
    Process for the internal coating of contact tubes 失效
    接触管内部涂层的工艺

    公开(公告)号:US4415485A

    公开(公告)日:1983-11-15

    申请号:US300298

    申请日:1981-09-08

    CPC分类号: B05C7/04 B05D7/222

    摘要: The previously carried out internal coating of contact tubes not only required very much manual labor and was very time consuming, but it was also unsatisfactory in regard to adhesion of the contact liquid to the surface and homogenity of the catalyst. By the simultaneous action of heat on the liquid interface in the tubes during the lowering of the liquid level as well as by a specially suited apparatus for this purpose which operates according to the principle of communicating tubes there is provided the possibility of a good adhesion to the surface as well as the formation of a homogeneous layer at very little operating expense.

    摘要翻译: 先前进行的接触管的内部涂层不仅需要非常多的手工劳动,并且非常耗时,而且对于接触液体对表面的粘附和催化剂的均匀性也是不令人满意的。 通过在液面降低期间在管中的液体界面上的热同时作用以及根据连通管的原理的特别适合的用于该目的的设备,提供了对 表面以及以非常小的操作费用形成均匀的层。

    Process for the production of hydrogen cyanide
    4.
    发明授权
    Process for the production of hydrogen cyanide 失效
    生产氰化氢的方法

    公开(公告)号:US4320104A

    公开(公告)日:1982-03-16

    申请号:US183955

    申请日:1980-09-03

    IPC分类号: C01C3/02

    CPC分类号: C01C3/0233

    摘要: By introducing the reaction gas mixture of hydrocarbons and ammonia at increased velocity through an inlet tube with one or more openings in a customary reaction tube in the hydrocyanic acid-methane-ammonia (BMA) process the yield of HCN is increased considerably.

    摘要翻译: 通过在氢氰酸 - 甲烷 - 氨(BMA)方法的常规反应管中通过具有一个或多个开口的入口管以增加的速度引入烃和氨的反应气体混合物,HCN的产率显着增加。

    Apparatus for the internal coating of contact tubes
    6.
    发明授权
    Apparatus for the internal coating of contact tubes 失效
    接触管内涂装置

    公开(公告)号:US4471712A

    公开(公告)日:1984-09-18

    申请号:US508133

    申请日:1983-06-27

    CPC分类号: B05C7/04 B05D7/222

    摘要: The previously carried out internal coating of contact tubes not only required very much manual labor and was very time consuming, but it was also unsatisfactory in regard to adhesion of the contact liquid to the surface and homogenity of the catalyst. By the simultaneous action of heat on the liquid interface in the tubes during the lowering of the liquid level as well as by a specially suited apparatus for this purpose which operates according to the principle of communicating tubes there is provided the possibility of a good adhesion to the surface as well as the formation of a homogeneous layer at very little operating expense.

    摘要翻译: 先前进行的接触管的内部涂层不仅需要非常多的手工劳动,并且非常耗时,而且对于接触液体对表面的粘附和催化剂的均匀性也是不令人满意的。 通过在液面降低期间在管中的液体界面上的热同时作用以及根据连通管的原理的特别适合的用于该目的的设备,提供了对 表面以及以非常小的操作费用形成均匀的层。

    Process for the production of hydrogen cyanide
    7.
    发明授权
    Process for the production of hydrogen cyanide 失效
    生产氰化氢的方法

    公开(公告)号:US4289741A

    公开(公告)日:1981-09-15

    申请号:US133358

    申请日:1980-03-24

    IPC分类号: C01C3/02

    CPC分类号: C01C3/0233

    摘要: The known hydrocyanic acid-methane-ammonia (BMA) process for the production of hydrogen cyanide can now be carried out with liquified gases namely through the presence of additional hydrogen at the beginning of the reaction. The atomic ratio of carbon to nitrogen and hydrogen is from 1:1:7.1 to 1:1.33:13. As additional hydrogen there is the portion of hydrogen present coming out of the reaction "hydrocarbon+NH.sub.3 ". Otherwise the reaction conditions are the same as in the known BMA process.

    摘要翻译: 用于生产氰化氢的已知氢氰酸 - 甲烷 - 氨(BMA)方法现在可以用液化气体进行,即在反应开始时通过存在另外的氢气来进行。 碳与氮和氢的原子比为1:1至7.1:1.33:1。 作为另外的氢,存在从反应“烃+ NH 3”出来的部分氢。 否则反应条件与已知的BMA方法相同。

    Process for the production of hydrogen cyanide
    8.
    发明授权
    Process for the production of hydrogen cyanide 失效
    生产氰化氢的方法

    公开(公告)号:US4387081A

    公开(公告)日:1983-06-07

    申请号:US304049

    申请日:1981-09-21

    IPC分类号: B01J23/00 C01C3/02

    CPC分类号: C01C3/0233

    摘要: In order to be independent of the situation in regard to methane and natural gas and at the same time to obtain a heating gas there is employed in the hydrocyanic acid-methane-ammonia process (the BMA process) in place of methane an alkanol or alkanediol having 2-4 carbon atoms, preferably ethyl alcohol, and this is reacted with ammonia in a C:N ratio of 0.8:1 to 2:1. Optionally additional hydrogen can be present.

    摘要翻译: 为了独立于甲烷和天然气的情况,同时获得加热气体,采用氢氰酸 - 甲烷 - 氨法(BMA法)代替烷烃或链烷二醇 具有2-4个碳原子,优选乙醇,并且其与C:N比为0.8:1至2:1的氨反应。 可选地,可以存在另外的氢。