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    Apparatus for dehydrogenation of liquid hydrides
    21.
    发明授权
    Apparatus for dehydrogenation of liquid hydrides 失效
    液体氢化物脱氢装置

    公开(公告)号：US5180560A

    公开(公告)日：1993-01-19

    申请号：US887376

    申请日：1992-05-21

    Applicant: Gamal E. D. Nasser

    Inventor： Gamal E. D. Nasser

    IPC: B01J15/00 ,  B01J19/24 ,  C01B3/00

    CPC classification number: C01B3/0015 ,  B01J15/00 ,  B01J19/245 ,  C01B3/0005 ,  B01J2219/00085 ,  B01J2219/00103 ,  B01J2219/00159 ,  B01J2219/00162 ,  Y02E60/328

    Abstract: An apparatus for the dehydrogenation of liquid hydrides consisting of a chemical reactor (18) to dehydrogenate the heated vaporous hydrides, a pre-heating stage (12a, 12b) to pre-heat the hydride, a vaporization stage (14a, 14b), to vaporize the hydride, a superheating stage (16a, 16b) to superheat the vaporous hydrides and a condensation stage (10a, 10b) to cool the dehydrogenation products. All stages, including the reactor, are designed as plate-shaped hybrid heat exchangers stacked side by side. Two cylindrical storage containers (6a, 6b) for the dehydrogenation products are located at both front ends of the heat exchanger stack. Side plates (30, 32) linked to the storage containers (6a, 6b) function as tie rods, providing the apparatus, in conjunction with the storage containers with the required stability. The spaces (36, 38) between the side plates and the heat exchanger stack hold guide channels for the flow media. In particular, the apparatus is distinguished by its inexpensive design, compactness and low weight.

    Abstract translation: PCT No.PCT / EP88 / 00803 Sec。 371日期：1989年5月3日 102（e）日期1989年5月3日PCT提交1988年9月3日PCT公布。 公开号WO89 / 01823 日本1993年3月9日。一种用于使化学反应器（18）脱氢以使加热的气态氢化物脱氢的预处理阶段（12a，12b），用于预热氢化物的液体氢化物脱氢装置，蒸发阶段 （14a，14b），使氢化物汽化，过热阶段（16a，16b）使过热蒸发的氢化物和冷凝段（10a，10b）冷却脱氢产物。 包括反应器在内的所有阶段被设计成并排堆叠的板状混合式热交换器。 用于脱氢产物的两个圆柱形储存容器（6a，6b）位于热交换器堆叠的两个前端。 连接到存储容器（6a，6b）的侧板（30,32）用作拉杆，与所需的稳定性的储存容器一起提供该装置。 侧板和热交换器堆叠之间的空间（36,38）保持流动介质的引导通道。 特别地，该设备的特征在于其便宜的设计，紧凑性和低重量。

    Reactor for producing gas by means of micro-organisms
    22.
    发明授权
    Reactor for producing gas by means of micro-organisms 失效
    通过微生物生产气体的反应堆

    公开(公告)号：US4604361A

    公开(公告)日：1986-08-05

    申请号：US480104

    申请日：1983-03-29

    Applicant: Roeland H. Peters

    Inventor： Roeland H. Peters

    IPC: B01J15/00 ,  C12M1/40 ,  C12M1/02

    CPC classification number: B01J15/00 ,  C12M21/04 ,  C12M23/34 ,  C12M23/38 ,  C12M29/02 ,  Y02E50/343 ,  Y10S435/813 ,  Y10S435/819

    Abstract: A column reactor, suitable for continuous production of a gaseous reaction product by contacting a liquid reaction medium with a gas-forming agent fixed to a reaction plug comprising a solid substrate provided with a plurality of gas-forming channels. The column reactor overcomes the apparent short circuiting of liquid reaction medium through the reactor by being provided with two or more reaction zones, each zone having its own circulatory by-pass means for liquid reaction medium. To obtain the reaction zones a reaction plug can be divided into two or more spaced apart plug portions. For each reaction zone the circulatory by-pass means provides a portion of the pathway for an internal recirculation current of liquid reaction medium.

    Abstract translation: 一种塔式反应器，适于通过使液体反应介质与固定在包含设置有多个气体形成通道的固体基板的反应塞的气体形成剂接触来连续生产气态反应产物。 塔式反应器通过提供两个或更多个反应区来克服液体反应介质通过反应器的明显短路，每个区域具有用于液体反应介质的其自身的循环旁路装置。 为了获得反应区，反应塞可以分成两个或更多间隔的塞子部分。 对于每个反应区域，循环旁路装置提供了用于液体反应介质的内部再循环电流的路径的一部分。

    Apparatus for solid gas reaction
    23.
    发明授权
    Apparatus for solid gas reaction 失效
    固体气体反应装置

    公开(公告)号：US4348363A

    公开(公告)日：1982-09-07

    申请号：US132992

    申请日：1980-03-24

    Applicant: Toru Akiyama ,  Tsutomu Kamihigoshi ,  Shoji Takagi ,  Tadayuki Maeda

    Inventor： Toru Akiyama ,  Tsutomu Kamihigoshi ,  Shoji Takagi ,  Tadayuki Maeda

    IPC: B01J15/00 ,  B01J19/28 ,  C01B9/08 ,  C01B31/00 ,  B01J8/08 ,  B01J8/16 ,  B01J8/18

    CPC classification number: B01J15/00 ,  B01J19/285 ,  C01B31/005 ,  C01B9/08

    Abstract: Continuous fluorination of carbon is carried out by employing an apparatus for contact reaction of solid powder and reactive gas which comprises a horizontal reactor having a trough provided with weirs (e.g. height: 1 to 6 mm., interval: 5 to 30 cm.) and a vibrating means for vibrating the trough, and in which carbon particles supplied continuously are transported on the trough in a form of thin layer by the vibration of the trough while continuing the reaction by contacting efficiently the carbon particles with a fluorine gas. The contact reaction is efficiently conducted without accumulating the reaction heat to produce the fluorinated carbon in high yields, and the process is useful for the mass production. The apparatus is also useful for various contact reaction of a solid powder and a reactive gas.

    Abstract translation: 碳的连续氟化是通过采用固体粉末和反应性气体接触反应的装置进行的，该装置包括具有设置有堰的槽的水平反应器（例如，高度为1至6mm，间隔为5至30cm），和 用于振动槽的振动装置，其中连续供应的碳颗粒通过槽的振动以薄层的形式在槽上输送，同时通过有效地使碳颗粒与氟气接触来继续反应。 有效地进行接触反应而不积累反应热，以高产率生成氟化碳，该方法对于批量生产是有用的。 该装置还可用于固体粉末和反应性气体的各种接触反应。

    Process for the beneficiation of titaniferous ores utilizing hot wall continuous plasma reactor
    26.
    发明授权
    Process for the beneficiation of titaniferous ores utilizing hot wall continuous plasma reactor 失效
    利用热墙连续等离子体反应器对钛铁矿的受益程序

    公开(公告)号：US3856918A

    公开(公告)日：1974-12-24

    申请号：US34560673

    申请日：1973-03-28

    Applicant: AMERICAN CYANAMID CO

    Inventor： SKRIVAN J ,  CHASE J

    IPC: B01J15/00 ,  C22B4/00 ,  C22B5/12 ,  C22B34/12 ,  H01J37/32 ,  C01G23/04

    CPC classification number: C22B5/12 ,  B01J15/00 ,  B01J2219/0894 ,  C22B4/005 ,  C22B34/1204 ,  H01J37/32 ,  Y10S423/10

    Abstract: There is provided a process for the beneficiation of titaniferous ores utilizing a plasma jet to carry out the high temperature reduction of the oxides of iron with a hydrocarbon gas in a hot wall continuous plasma reactor which enables particulate solids to be recovered. Iron can readily be removed by leaching or magnetic separation of the particulate solids so as to obtain a feed product containing 90-97 percent titania which is eminently suitable as a feed material for manufacturing titanium dioxide pigment by the chloride process.

    Abstract translation: 提供了一种利用等离子体射流来选择含钛矿石的方法，以便在热壁连续等离子体反应器中用烃气体进行铁的氧化物的高温还原，这使得能够回收颗粒状固体。 铁可以容易地通过浸出或磁性分离颗粒固体来除去，从而获得含有90-97％二氧化钛的进料产物，其特别适合作为通过氯化法制备二氧化钛颜料的进料。

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