Circuit breaker and driving mechanism thereof
    11.
    发明授权
    Circuit breaker and driving mechanism thereof 失效
    断路器及其驱动机构

    公开(公告)号:US5451731A

    公开(公告)日:1995-09-19

    申请号:US322363

    申请日:1994-10-13

    CPC分类号: H01H33/168 H01H33/14

    摘要: In a double-break type circuit breaker having resistor contacts which are to be connected in parallel with main contacts in not only closing operation but also breaking operation, the resistor contacts are opened by a force due to loading of elastic members in the breaking operation and the elastic members are loaded for storing the driving force In the closing operation.

    摘要翻译: 在具有电阻触点的双断路型断路器中,不仅在闭合动作中与主触点并联而且断开操作,所以电阻触点由于在断开操作中的弹性部件的加载而被打开, 在关闭操作中,弹性构件被装载用于存储驱动力。

    Gas circuit breaker
    12.
    发明授权
    Gas circuit breaker 失效
    气体断路器

    公开(公告)号:US5387773A

    公开(公告)日:1995-02-07

    申请号:US100302

    申请日:1993-08-02

    摘要: In a stationary contact unit of a gas circuit breaker, an arc-quenching cylinder for passing an arc-quenching insulation gas is formed in a substantially semicircular shape, and the stationary contact unit is supported by an insulation frame which is disposed beneath the dent part of the semicircular portion of the arc-quenching cylinder. The insulation frame is prevented from the degradation of dielectric strength between the stationary contact unit and a grounded tank, and the size of the gas circuit breaker is decreased.

    摘要翻译: 在气体断路器的固定接触单元中,用于使灭弧绝缘气体通过的消弧筒形成为大致半圆形,并且固定接触单元由设置在凹部下方的绝缘框架支撑 的弧形圆弧的半圆形部分。 防止绝缘框架降低固定接触单元和接地箱之间的介电强度,并且减小气体断路器的尺寸。

    Method for the catalytical production of acrylonitrile
    13.
    发明授权
    Method for the catalytical production of acrylonitrile 失效
    丙烯腈催化生产方法

    公开(公告)号:US4205010A

    公开(公告)日:1980-05-27

    申请号:US718513

    申请日:1976-08-30

    摘要: Acrylonitrile can be catalytically produced with a high yield by bringing, at an elevated temperature, preferably of 300.degree. to 470.degree. C., a reaction feed containing propylene, ammonia and molecular oxygen into contact with a catalyst consisting of an oxide composition of the empirical formula: Mo.sub.a Co.sub.b Fe.sub.c X.sub.d O.sub.e wherein X denotes at least one atom of an element selected from phosphorus, arsenic, antimony and bismuth and wherein the ratio a:b:c:d:e is in a range of 12:4 to 9:1 to 5:0.01 to 0.07:39.5 to 52.7, said catalyst being prepared by providing an aqueous mixture containing molybdenum-, cobalt- and iron-containing compounds and a phosphorus-, arsenic-, antimony- or bismuth-containing compound, converting the aqueous mixture into a dried solid mixture and calcining the solid mixture at a temperature of at least 550.degree. C.

    摘要翻译: 丙烯腈可以通过在升高的温度,优选在300-470℃下,使含有丙烯,氨和分子氧的反应进料与由经验的氧化物组成的催化剂接触而以高产率催化制备 式:MoaCobFecXdOe其中X表示选自磷,砷,锑和铋中的元素的至少一个原子,其中a:b:c:d:e的比率在12:4至9:1至5:1的范围内。 0.01至0.07:39.5至52.7,所述催化剂通过提供含有含钼,钴和铁的化合物和含磷,砷,锑或铋的化合物的含水混合物制备,将含水混合物转化为 干固体混合物并在至少550℃的温度下煅烧固体混合物

    Method for the catalytic production of acrylonitrile
    14.
    发明授权
    Method for the catalytic production of acrylonitrile 失效
    催化生产丙烯腈的方法

    公开(公告)号:US4097518A

    公开(公告)日:1978-06-27

    申请号:US733771

    申请日:1976-10-19

    IPC分类号: B01J23/882 C07C120/14

    摘要: High-yield catalytic production of acrylonitrile at an elevated temperature, from a reaction mixture containing propylene, ammonia and molecular oxygen, utilizing a catalyst comprising an oxide composition having the empirical formula Mo.sub.a Co.sub.b Fe.sub.c X.sub.d O.sub.e wherein X denotes at least one atom of an element selected from among calcium, tungsten, chromium, zirconium, titanium, zinc, manganese, and tin and the atomic ratio a:b:c:d:e is in the range of 12:4 to 10:1 to 6:0 to 1.0:40 to 70, said catalyst being prepared by providing an aqueous mixture containing compounds of the elements, drying the aqueous mixture, and calcining the dried solid product at a temperature of at least 500.degree. C.

    摘要翻译: 使用包含具有经验式MoaCobFecXdOe的氧化物组合物的催化剂,从含有丙烯,氨和分子氧的反应混合物高温催化生产丙烯腈,其中X表示选自钙的元素的至少一个原子 ,钨,铬,锆,钛,锌,锰和锡,原子比a:b:c:d:e在12:4至10:1至6:0至1.0:40至70的范围内 所述催化剂通过提供含有元素化合物的水性混合物,干燥含水混合物和在至少500℃的温度下煅烧干燥的固体产物来制备。