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13 条记录 (耗时 0.045 秒)

    Method of humidifying a gas
    1.
    发明授权
    Method of humidifying a gas 失效
    加湿气体的方法

    公开(公告)号：US4705654A

    公开(公告)日：1987-11-10

    申请号：US863519

    申请日：1986-05-15

    申请人： Kensuke Niwa ,  Hisayoshi Fujita ,  Yoshihiko Saito ,  Hiroshi Makihara ,  Ritsuo Hashimoto ,  Younosuke Hoshi ,  Katsutoshi Murayama

    发明人： Kensuke Niwa ,  Hisayoshi Fujita ,  Yoshihiko Saito ,  Hiroshi Makihara ,  Ritsuo Hashimoto ,  Younosuke Hoshi ,  Katsutoshi Murayama

    IPC分类号： B01F3/04

    CPC分类号： B01F3/04078

    摘要： A wetted wall type method of humidifying gas with a liquid which is composed, or mainly composed, of water wherein the liquid flows down a heated vertical wall to form a wetted wall and gas flows along the wetted wall in contact with the liquid on the wetted wall to increase the humidity contained in the gas, comprises supplying a greater amount of liquid than the amount of liquid used or evaporated for increasing the humidity, and recirculating the liquid which is not evaporated from an outlet of the wetted wall to a liquid supply portion, the amount of the flowing liquid being adapted to satisfy the following equation:q

    摘要翻译： 用液体加湿气体的润湿壁式方法，其中液体由水组成或主要由水组成，其中液体沿着加热的垂直壁流动以形成湿壁，并且气体沿着与被润湿的液体上的液体接触的润湿壁流动 以增加包含在气体中的湿度，包括供给比用于或蒸发的用于增加湿度的液体量更多的液体，并且将未蒸发的液体从润湿壁的出口再循环到液体供应部分 流动液体的量适合满足以下等式：q <5.99×105 GAMMA 2.12（1）其中q是W / m2K中的热通量，其中W =瓦特，K =以开尔文为单位的温度，GAMMA是 相对于每单位湿宽度的水质量，以kg / ms计算流动水量。

    Process for synthesizing methanol with an optimal temperature profile using a concentric pipe reactor
    2.
    发明授权
    Process for synthesizing methanol with an optimal temperature profile using a concentric pipe reactor 失效
    使用同心管式反应器合成具有最佳温度曲线的甲醇的方法

    公开(公告)号：US4767791A

    公开(公告)日：1988-08-30

    申请号：US928665

    申请日：1986-11-06

    申请人： Yoshimitsu Nakajima ,  Kensuke Niwa ,  Kazuhiro Morita ,  Hiroshi Makihara

    发明人： Yoshimitsu Nakajima ,  Kensuke Niwa ,  Kazuhiro Morita ,  Hiroshi Makihara

    IPC分类号： B01J8/06 ,  C07C29/152 ,  C07C27/06

    CPC分类号： B01J8/067 ,  C07C29/152 ,  B01J2208/00212 ,  B01J2208/00274

    摘要： A process for synthesizing material uses an exothermic reactor which comprises a coolant shell, two concentric pipes provided within the shell, a catalyst bed packed between inner and outer ones of the concentric pipes, an introduction tube connected to the inner pipe through which a starting fluid is introduced, and a communication path enabling the fluid after the passage of the inner pipe to be passed through the catalyst bed in a direction opposite to the direction of the passage through the inner pipe, the coolant shell having an inlet and an outlet for a coolant arranged in such a way that the flow of the coolant is parallel to the flow of the fluid within the catalyst bed. The coolant on the outside and the starting fluid on the inside of the catalyst bed cools the bed in such a way as to produce a temperature distribution along the bed that follows a maximum reaction rate line (M in FIG. 1) relating the concentration of the methanol to the temperature of the starting fluid.

    摘要翻译： 合成材料的方法使用放热反应器，其包括冷却剂壳体，设置在壳体内的两个同心管，包含在内部和外部同心管之间的催化剂床，连接到内部管的引入管，通过该引入管，起始流体 以及能够使内管通过后的流体在与内管的通道方向相反的方向通过催化剂床的连通路径，冷却剂壳具有入口和出口， 冷却剂布置成使得冷却剂的流动平行于催化剂床内的流体的流动。 外部冷却剂和催化剂床内部的起始流体以这样的方式冷却床，以便产生沿着床的温度分布，该温度分布遵循最大反应速率线（图1中的M），其与 甲醇至起始流体的温度。

    Reaction vessel
    3.
    发明授权
    Reaction vessel 失效
    反应容器

    公开(公告)号：US4938930A

    公开(公告)日：1990-07-03

    申请号：US96810

    申请日：1987-09-10

    申请人： Toshikazu Shinkawa ,  Daisaku Shozen ,  Kazuto Kobayashi ,  Hiroshi Makihara ,  Kensuke Niwa ,  Kazuhiro Morita ,  Masaaki Kuwa ,  Murayama Katsutoshi

    发明人： Toshikazu Shinkawa ,  Daisaku Shozen ,  Kazuto Kobayashi ,  Hiroshi Makihara ,  Kensuke Niwa ,  Kazuhiro Morita ,  Masaaki Kuwa ,  Murayama Katsutoshi

    IPC分类号： C07C29/15 ,  B01J8/06 ,  C07C27/00 ,  C07C29/152 ,  C07C31/04 ,  C07C67/00

    CPC分类号： B01J8/067 ,  C07C29/152 ,  B01J2208/0007 ,  B01J2208/00212 ,  B01J2208/0053

    摘要： A reaction vessel has a catalytic core, with an inlet for a first gas and for a second gas. The first and second gasses react in an exothermic reaction during passage through the catalytic core. The first gas passes through conduits which extend through the catalytic core, so as to be preheated and also so as to cool the catalytic core so that the catalyzed reaction proceeds in a preferred temperature range. The gasses are mixed at one end of the vessel in a mixing chamber, and are drawn through the catalytic core into a gathering chamber, from which the reacted gasses exit. A cooling chamber is provided for introduction of a cooling fluid about the periphery of the catalytic core, for drawing away any excess heat during operation.

    摘要翻译： PCT No.PCT / JP85 / 00227 Sec。 371日期1985年12月12日第 102（e）1985年12月12日日期PCT提交1985年4月23日PCT公布。 出版物WO85 / 04820 日期为1985年11月7日。反应容器具有催化剂芯，其具有用于第一气体和第二气体的入口。 第一和第二气体在通过催化核心期间在放热反应中发生反应。 第一气体通过延伸穿过催化芯的导管，以便被预热，并且也可以冷却催化剂芯，使得催化反应在优选的温度范围内进行。 气体在容器的一端在混合室中混合，并通过催化剂芯被抽吸到聚集室中，反应气体从该聚集室中排出。 提供冷却室，用于在催化芯的周围引入冷却流体，以在操作期间抽出多余的热量。

    Method for converting a plastic waste into oil in a stainless steel reactor
    5.
    发明授权
    Method for converting a plastic waste into oil in a stainless steel reactor 失效
    在不锈钢反应器中将塑料废物转化为油的方法

    公开(公告)号：US06504068B1

    公开(公告)日：2003-01-07

    申请号：US08870623

    申请日：1997-06-06

    申请人： Wataru Matsubara ,  Hiroshi Makihara ,  Kazuto Kobayashi ,  Masaki Iijima

    发明人： Wataru Matsubara ,  Hiroshi Makihara ,  Kazuto Kobayashi ,  Masaki Iijima

    IPC分类号： C07C100

    CPC分类号： C10G1/10 ,  Y10S208/952

    摘要： A method of converting a plastic waste into oil by decomposing the plastic waste by a reaction using water in a supercritical or near supercritical region as a reaction medium. In this method, the reaction is conducted by using a tubular continuous reactor. The present invention further provides an apparatus therefor. Moreover, the present invention provides a method of converting a plastic waste into oil by conducting the reaction after hydrogen chloride is removed by performing the pyrolysis of the plastic waste in the case that the plastic waste contain chlorine. The present invention further provides an apparatus for performing this method.

    摘要翻译： 通过使用超临界或近超临界区域中的水作为反应介质的反应分解塑料废物来将塑料废物转化为油的方法。 在该方法中，通过使用管状连续反应器进行反应。 本发明还提供了一种装置。 此外，本发明提供了在塑料废物含有氯的情况下，通过进行塑料废物的热分解而在除去氯化氢之后通过进行反应来将塑料废物转化为油的方法。 本发明还提供了一种用于执行该方法的装置。

    Plate thickness measuring method and apparatus
    6.
    发明授权
    Plate thickness measuring method and apparatus 失效
    板厚测量方法及装置

    公开(公告)号：US4564296A

    公开(公告)日：1986-01-14

    申请号：US305374

    申请日：1981-09-24

    申请人： Yoshitada Oshida ,  Hiroshi Makihara ,  Nobuhiko Aoki

    发明人： Yoshitada Oshida ,  Hiroshi Makihara ,  Nobuhiko Aoki

    IPC分类号： G01B11/00 ,  G01B11/06 ,  H01L21/66

    CPC分类号： G01B11/06

    摘要： A plate thickness measuring method and apparatus, is provided wherein a fine pattern is projected on the front and rear surfaces of an object to be measured via object lenses oppositely provided on the front and rear surfaces of the object to be measured in its thickness. The image of the projected pattern on the object to be measured is formed via said object lenses, and the contrast of the formed pattern image is detected. Then the object lenses are moved slightly to achieve the maximum of the contrast, or to perform an automatic focusing control. The thickness of the object to be measured can then be estimated from the difference of the positions of the object lenses at which the maximum contrast, or the focused condition, are obtained.

    摘要翻译： 提供了一种板厚测量方法和装置，其中精细图案通过相对设置在被测量物体的前表面和后表面上的物镜在其厚度上投影在被测量物体的前表面和后表面上。 通过所述物镜形成待测物体上的投影图案的图像，并且检测形成的图案图像的对比度。 然后物镜稍微移动以达到对比度的最大值，或进行自动对焦控制。 然后可以从获得最大对比度或聚焦条件的物镜的位置的差异来估计被测量物体的厚度。

    Oil-forming method of chlorine-containing plastic refuse
    7.
    发明授权
    Oil-forming method of chlorine-containing plastic refuse 失效
    含氯塑料垃圾的成油方法

    公开(公告)号：US5728910A

    公开(公告)日：1998-03-17

    申请号：US735420

    申请日：1996-10-22

    申请人： Wataru Matsubara ,  Hiroshi Makihara ,  Shigeo Hasegawa

    发明人： Wataru Matsubara ,  Hiroshi Makihara ,  Shigeo Hasegawa

    IPC分类号： A62D3/00 ,  B09B3/00 ,  C08L27/06 ,  C10G1/10 ,  C07C1/00 ,  C07C1/26 ,  C07C7/152

    CPC分类号： C10G1/10 ,  Y10S208/952 ,  Y10S585/935

    摘要： To present an oil-forming method of chlorine-containing plastic refuse capable of obtaining oily product free from chlorine content, while suppressing apparatus corrosion by efficiently capturing hydrogen chloride generated by decomposition of chlorine-containing plastics, the oil-forming method of chlorine-containing plastic refuse is characterized by decomposing chlorine-containing plastic refuse using water in supercritical region as reaction medium and forming into oil, wherein silver nitrate of 0.8 to 2.0 times the reaction equivalent amount of hydrogen chloride generated by decomposition of chlorine-containing plastic refuse is added in the water as reaction medium to decompose and form into oil, and generated hydrogen chloride is removed in a form of silver chloride.

    摘要翻译： 为了提供能够获得没有氯含量的油性产品的含氯塑料垃圾的成油方法，同时通过有效地捕获由含氯塑料分解产生的氯化氢来抑制设备腐蚀，含氯的成油方法 塑料垃圾的特点是在超临界区域使用水分解含氯塑料垃圾作为反应介质并形成油，其中加入硝酸银为含氯塑料垃圾分解产生的反应当量的氯化氢的0.8〜2.0倍 在水中作为反应介质分解并形成油，产生氯化氢以氯化银的形式除去。

    Thermal cracking method for producing olefins from hydrocarbons
    9.
    发明授权
    Thermal cracking method for producing olefins from hydrocarbons 失效
    用烃制造烯烃的热裂解方法

    公开(公告)号：US4520224A

    公开(公告)日：1985-05-28

    申请号：US473761

    申请日：1983-03-09

    申请人： Yoshihiko Kamimura ,  Toshiro Okamoto ,  Naoyuki Takahashi ,  Hiroshi Makihara ,  Michio Oshima

    发明人： Yoshihiko Kamimura ,  Toshiro Okamoto ,  Naoyuki Takahashi ,  Hiroshi Makihara ,  Michio Oshima

    IPC分类号： C10G47/00 ,  C07C1/00 ,  C07C4/04 ,  C07C11/02 ,  C07C67/00 ,  C10G47/22 ,  C07C4/02

    CPC分类号： C10G47/22 ,  C10G2400/20 ,  Y02P30/40

    摘要： A thermal cracking method for producing olefins from hydrocarbons which comprises the steps of mixing said hydrocarbons with a mixed gas of methane and hydrogen in a methane/hydrogen mol ratio of 0.2 or more; prior to reaction carrying out a thermal cracking reaction under conditions such that the total concentration of methane and hydrogen is at least 40 mol % or more at the outlet of a reactor, the partial pressure of said hydrogen is 3 bars or more, the temperature at the outlet of the reactor is from 800.degree. to 1200.degree. C., and the residence time in the reactor is from 5 to 300 milliseconds; and quenching the reaction product discharged through the outlet of the reactor.

    摘要翻译： 一种用于从烃生产烯烃的热裂解方法，包括以下步骤：甲烷/氢摩尔比为0.2或更高的甲烷和氢气的混合气体; 在反应之前进行热裂解反应的条件下，在甲烷和氢的总浓度在反应器出口处至少为40摩尔％以上的条件下，所述氢的分压为3巴或更高， 反应器的出口为800〜1200℃，反应器中的停留时间为5〜300毫秒; 并使通过反应器出口排出的反应产物骤冷。