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184 条记录 (耗时 0.014 秒)

    Nitrogen fixation by plasma and catalyst
    93.
    发明授权
    Nitrogen fixation by plasma and catalyst 失效
    通过等离子体和催化剂固氮

    公开(公告)号：US4451436A

    公开(公告)日：1984-05-29

    申请号：US442367

    申请日：1983-02-01

    申请人： Louis R. O'Hare

    发明人： Louis R. O'Hare

    IPC分类号： B01J12/00 ,  B01J19/08 ,  C01B21/32 ,  C01C1/04 ,  C01B21/20

    CPC分类号： C01B21/32 ,  B01J12/002 ,  B01J19/088 ,  C01C1/0405 ,  C01C1/0494 ,  B01J2219/0894 ,  Y02P20/52 ,  Y10S422/904

    摘要： A system and a method of nitrogen fixation is disclosed in which nitrogen and other gases such as oxygen are electrically activated and reacted on a catalyst-like material to provide a fixed nitrogen product in such a way that the reactant gases are first placed into an excited state by a single electrode electric discharge acting on a gas stream and then by means of the stream the reactants are contacted on the catalyst-like material on which they are then combined and the product compounds which are thereby formed are shielded by the same catalytic material from ultra violet radiation generated by the electric excitation, said shielding being to prevent subsequent disassociation of the product compounds, and the gas stream emerging on the downstream side of the catalyst carries the products to an absorption bed on which they are absorbed and concentrated and then reacted with a periodic flow of hydrogen to provide ammonia. In an alternate embodiment the products absorbed on the bed are first desorbed and then reacted with hydrogen.

    摘要翻译： 公开了一种固氮系统和方法，其中氮气和其它气体如氧被电活化并在催化剂样材料上反应以提供固定氮产物，使得反应气体首先被置于激发态 通过作用在气流上的单个电极放电，然后通过该流将反应物与催化剂样材料接触，然后将它们组合，由此形成的产物化合物被相同的催化材料 通过电激发产生的紫外线辐射，所述屏蔽是防止产物化合物随后的分离，并且出现在催化剂下游侧的气流将产物运送到吸收床，吸收床被吸收并吸收并浓缩 与周期性氢气反应以提供氨。 在另一个实施方案中，吸附在床上的产物首先被解吸，然后与氢反应。

    High temperature reactor
    95.
    发明授权
    High temperature reactor 失效
    高温反应釜

    公开(公告)号：US4217479A

    公开(公告)日：1980-08-12

    申请号：US893898

    申请日：1978-04-06

    申请人： Werner J. Borer ,  Volker Nobbe ,  Hugo Spalinger

    发明人： Werner J. Borer ,  Volker Nobbe ,  Hugo Spalinger

    IPC分类号： B01J6/00 ,  B01J12/00 ,  C03B3/02 ,  C03B5/02 ,  H05H1/32 ,  H05B7/10

    CPC分类号： C03B5/025 ,  B01J12/002 ,  B01J6/005 ,  C03B3/026 ,  H05H1/32 ,  B01J2219/0894 ,  Y10S422/906

    摘要： A high temperature reactor is fitted with a plasma gun at an anode chamber and is provided with a graphite cathode. The reactor is cooled by means of pipes in the refractory lining of the reactor, and rests on essentially horizontal bearings. The charge to be melted e.g. oxides or oxide mixtures is fed from above at an angle .alpha. at most 90.degree. to the main axis of the reactor in the direction of the plasma stream, and the molten product is tapped off at an exit port which is also close to the entry port of the plasma stream so that the plasma stream covers and therefore heats the area around the exit port.

    摘要翻译： 高温反应器在阳极室配有等离子体枪，并设有石墨阴极。 反应器通过反应器的耐火衬里中的管道冷却，并且搁置在基本上水平的轴承上。 要熔化的电荷例如 氧化物或氧化物混合物从上方以等离子体流的方向与反应器的主轴成α°至多90度的角度进料，并且熔融产物在也接近进入口的出口处被分离 的等离子体流，使得等离子体流覆盖并因此加热出口周围的区域。

    Plasma apparatus for carrying out high temperature chemical reactions
    99.
    发明授权
    Plasma apparatus for carrying out high temperature chemical reactions 失效
    用于实施高温化学反应的等离子体装置

    公开(公告)号：US3840750A

    公开(公告)日：1974-10-08

    申请号：US34269973

    申请日：1973-03-19

    申请人： PLASMACHEM

    发明人： DAVIS R ,  MEYER T ,  BLIZZARD R

    IPC分类号： B01J12/00 ,  C01G1/06 ,  C22B4/00 ,  C22B4/08 ,  H01J37/32 ,  H05H1/34 ,  C22D7/08 ,  B01K1/00

    CPC分类号： C22B4/005 ,  B01J12/002 ,  B01J2219/0894 ,  C01G1/06 ,  C22B4/08 ,  H01J37/32 ,  H05H1/34

    摘要： In the process of carrying out high temperature, chemical reactions including reductins for producing elemental metal powders, especially refractory metals; chlorinations for producing halogens and for chemical synthesis in general using a plasma genertor, the reactant or reactants feed material is introduced into the reaction zone of the apparatus and the effluent from the reaction zone is directed into a quenching zone through a selectively variable passageway or orifice in a manner that permits in the reduction process separation of the desired reaction product from the effluent hot gas stream and the continuous collection of the reaction product in a collection zone wherein in some instances, the reaction product is of a selected characteristic, controlled by the maintenance of certain operational parameters, including a selected differential fluid pressure in the reaction and collection zone as well as reaction and collection zone temperatures. Apparatus for carrying out the high temperature chemical reactions is disclosed.