中科微点-全球专利检索

  1. Login
  2. Sign Up

Search Results

419 records (took 0.02 seconds)

    Reactor or heat exchanger with improved heat transfer performance
    21.
    发明授权
    Reactor or heat exchanger with improved heat transfer performance 有权
    具有改善传热性能的反应器或换热器

    公开(公告)号：US07695695B2

    公开(公告)日：2010-04-13

    申请号：US11654529

    申请日：2007-01-18

    Applicant: Sang Baek Shin ,  Sang Phil Han ,  Ye Hoon Im ,  Young Bae Kim ,  Jung Hoon Chang ,  Sang Oeb Na ,  Won Am Lee

    Inventor： Sang Baek Shin ,  Sang Phil Han ,  Ye Hoon Im ,  Young Bae Kim ,  Jung Hoon Chang ,  Sang Oeb Na ,  Won Am Lee

    IPC: B01J19/00 ,  F28D7/10

    CPC classification number: B01J8/067 ,  B01J2208/00194 ,  B01J2208/00221 ,  B01J2208/0023 ,  B01J2208/025 ,  F28D7/0091 ,  F28F9/22

    Abstract: A shell-and-tube reactor or heat exchanger comprises first tubes, through the inside of which a first object for heat transfer with a heat transfer medium is passed, some of the first tubes being provided in a zone in which a flow of the heat transfer medium (parallel flow) parallel to the axis of the tubes is present; and a second tube, through the inside of which the first object is not passed, the second tube being provided in said zone such that it is parallel to the axis of the first tubes. A method for producing an oxide comprises using said shell-and-tube reactor or heat exchanger, and causing a catalytic vapor-phase oxidation reaction in first tubes, through the inside of which the first object for heat transfer with the heat transfer medium is passed.

    Abstract translation: 管壳式反应器或热交换器包括第一管，其中通过内部的第一传热介质的传热物体通过，一些第一管被设置在热交换区域中 存在平行于管轴的转印介质（平行流）; 以及第二管，其第一物体的内部不通过，所述第二管设置在所述区域中，使得其平行于第一管的轴线。 一种生产氧化物的方法包括使用所述管壳式反应器或热交换器，并且在第一管中引起催化气相氧化反应，通过其内部，传热介质的第一物体通过 。

    PROCESS FOR PRODUCING MONOSILANE
    23.
    发明申请
    PROCESS FOR PRODUCING MONOSILANE 失效
    生产单体的方法

    公开(公告)号：US20090155156A1

    公开(公告)日：2009-06-18

    申请号：US12088286

    申请日：2006-06-19

    Applicant: Raymund Sonnenschein ,  Peter Adler ,  Yuriy Kasatkin ,  Adolf Petrik ,  Leonid Schwarzmann

    Inventor： Raymund Sonnenschein ,  Peter Adler ,  Yuriy Kasatkin ,  Adolf Petrik ,  Leonid Schwarzmann

    IPC: C01B33/08 ,  B01J19/00

    CPC classification number: C01B33/043 ,  B01D3/009 ,  B01J8/0085 ,  B01J8/009 ,  B01J8/025 ,  B01J8/0285 ,  B01J8/0426 ,  B01J8/0438 ,  B01J8/0453 ,  B01J8/048 ,  B01J8/0484 ,  B01J8/0492 ,  B01J8/0496 ,  B01J8/065 ,  B01J8/067 ,  B01J19/30 ,  B01J19/32 ,  B01J2208/00176 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00247 ,  B01J2208/00274 ,  B01J2208/00283 ,  B01J2208/0053 ,  B01J2208/00884 ,  B01J2208/021 ,  B01J2219/30475 ,  B01J2219/32466 ,  B01J2219/3325 ,  C01B33/10773 ,  Y02P20/127 ,  Y10S203/06

    Abstract: The present invention relates to a plant and a process for the continuous production of monosilane and tetrachlorosilane by catalytic dismutation of trichlorosilane at an operating temperature and a pressure of from 1 to 50 bar abs. in a plant according to claim 1, in which—trichlorosilane (A) is preheated in a heat exchanger (7), and fed to the 10 countercurrent reactor (1) which is provided with catalyst (3),—product mixture formed in the countercurrent reactor (1) is at least partly condensed by means of the condenser (5) at a temperature in the range from −25 to 50° C. with the condensate flowing back into the countercurrent reactor (1),—the product phase which is not condensed in the condenser (5) is passed to the 15 condensation unit (8) which is operated at a temperature in the range from −40 to −110° C.,—the volatile product phase from the condensation unit (8) is fed to the distillation column (9) which is operated at a temperature in the range from −60 to −170° C. and monosilane (C) is discharged at the top of the distillation column (9), 20—the SiCl4-containing bottoms from the countercurrent reactor (1) are brought to a temperature in the range from 60 to 110° C. in the vaporizer unit (6) and—bottom product from the vaporizer (6) is conveyed via a heat exchanger (7) into the double wall (2) of the countercurrent reactor (1) and the SiCl4-containing product stream (B) is discharged at a level in the upper region of the reactor (1).

    Abstract translation: 本发明涉及一种在操作温度和1至50巴绝对压力下通过三氯硅烷的催化分解连续生产甲硅烷和四氯硅烷的设备和方法。 在根据权利要求1的设备中，其中在热交换器（7）中预热三氯硅烷（A），并送入设有催化剂（3）的10逆流反应器（1）， - 形成在 逆流反应器（1）通过冷凝器（5）至少部分地在-25至50℃的温度范围内冷凝，冷凝物流回到逆流反应器（1）中，产物相位 在冷凝器（5）中未冷凝的冷凝单元（8）在-40至-110℃的温度范围内运行， - 来自冷凝单元（8）的挥发性产物相 进料到在-60至-70℃范围内操作的蒸馏塔（9）中，并且甲硅烷（C）在蒸馏塔（9）的顶部排出，20- SiCl 4 - 来自逆流反应器（1）的含底部物质在蒸发器单元（6）中的温度范围为60至110℃，-toto 来自蒸发器（6）的产物经由热交换器（7）输送到逆流反应器（1）的双壁（2）中，并且含SiCl4的产物流（B）在上部区域中被排出 的反应器（1）。

    Carbon monoxide conversion process and reactor
    25.
    发明授权
    Carbon monoxide conversion process and reactor 有权
    一氧化碳转化过程和反应器

    公开(公告)号：US07481857B2

    公开(公告)日：2009-01-27

    申请号：US11453001

    申请日：2006-06-15

    Applicant: Thomas Rostrup-Nielsen ,  Erik Løgsted-Nielsen

    Inventor： Thomas Rostrup-Nielsen ,  Erik Løgsted-Nielsen

    IPC: B01J8/00

    CPC classification number: C01B3/501 ,  B01J8/009 ,  B01J8/067 ,  B01J2208/00212 ,  B01J2208/00221 ,  C01B3/16 ,  C01B2203/0283 ,  C01B2203/041 ,  C01B2203/0475 ,  C01B2203/0888 ,  C01B2203/0894 ,  F28D3/02 ,  F28D3/04 ,  Y02P20/52

    Abstract: Process and reaction unit for isothermal shift conversion of a carbon monoxide containing feed gas, the process comprising the steps ofintroducing the feed gas in a reaction unit into reactor tubes with a fixed bed of a shift conversion catalyst in a reaction zone;contacting the feed gas with the catalyst at conditions being effective in carbon monoxide shift conversion reaction with steam reactant to hydrogen and cooling the reaction by indirect heat exchange with a cooling agent by passing the cooling agent in a falling film along shell side of the reactor tubes and removing heated cooling agent from the falling film;passing hydrogen when it is formed by the shift conversion reaction through a hydrogen selective membrane to a permeate zone;withdrawing hydrogen from the permeate zone and carbon monoxide depleted feed gas from the reaction zone.

    Abstract translation: 含有一氧化碳的进料气体的等温转化转化的工艺和反应单元，该方法包括以下步骤：将反应单元中的进料气体引入反应器管中，在反应区中用固定床的转化转化催化剂; 使进料气体与催化剂接触，条件是有效地与蒸汽反应物进行一氧化碳转化反应转化为氢气，并通过与冷却剂间接热交换冷却反应物，通过将冷却剂沿着反应器管的壳侧通过降膜 并从降膜除去加热的冷却剂; 当通过通过氢选择性膜的移位转换反应形成至渗透区时，使氢气通过; 从渗透区抽出氢气和从反应区域排出一氧化碳的进料气体。

    Process for the production of polymers using a loop reactor
    26.
    发明授权
    Process for the production of polymers using a loop reactor 失效
    使用环管反应器生产聚合物的方法

    公开(公告)号：US07473744B2

    公开(公告)日：2009-01-06

    申请号：US11265450

    申请日：2005-11-02

    Applicant: Harold Chenoweth ,  Jeffrey Tilley

    Inventor： Harold Chenoweth ,  Jeffrey Tilley

    IPC: C08F2/00 ,  B01J19/24

    CPC classification number: C08F110/02 ,  B01J8/067 ,  B01J19/0013 ,  B01J19/2435 ,  B01J2208/00221 ,  B01J2219/00063 ,  B01J2219/00094 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00238 ,  C08F2400/02 ,  Y10S526/918 ,  C08F2/06 ,  C08F2/00

    Abstract: A polymer can be prepared using a loop reactor and process including feeding a process stream through the loop reactor and maintaining the loop reactor at a steady state by controlling a flow of coolant fluid to maintain a temperature in the loop reactor at a preset point. The temperature in the loop reactor may be maintained at a preset point by using a coolant fluid flow controller and valve unit having a substantially linear response over the normal operating range of the controller and valve unit. The normal operating range of the controller and valve unit may be sufficient to provide a flow range not limiting to the throughput of the loop reactor.

    Abstract translation: 聚合物可以使用环管反应器和方法制备，包括通过环流反应器进料工艺流，并通过控制冷却剂流体的流动将环管反应器维持在稳定状态，以将回路反应器中的温度保持在预设点。 通过使用在控制器和阀单元的正常操作范围内具有基本线性响应的冷却剂流体流量控制器和阀单元，可将回路反应器中的温度保持在预设点。 控制器和阀单元的正常操作范围可能足以提供不限制回路反应器的生产量的流量范围。

    Reactor for testing catalyst systems
    29.
    发明授权
    Reactor for testing catalyst systems 失效
    用于测试催化剂体系的反应器

    公开(公告)号：US07402288B2

    公开(公告)日：2008-07-22

    申请号：US10478684

    申请日：2002-06-05

    Applicant: Gerhard Olbert ,  Torsten Mattke ,  Matthias Kummer ,  Thomas Ruehl ,  Frank Rosowski

    Inventor： Gerhard Olbert ,  Torsten Mattke ,  Matthias Kummer ,  Thomas Ruehl ,  Frank Rosowski

    IPC: B01J19/24 ,  F27B15/14 ,  F28D7/16 ,  G01N31/10

    CPC classification number: G01N31/10 ,  B01J8/067 ,  B01J2208/00168 ,  B01J2208/00221 ,  B01J2208/0023 ,  B01J2208/00256 ,  B01J2208/021 ,  B01J2219/00009 ,  B01J2219/00745 ,  B01J2219/00747 ,  B01J2219/00777 ,  C40B30/08 ,  C40B40/18 ,  F28D7/0066 ,  F28D7/0091

    Abstract: A reactor for testing catalyst systems which has a plurality of catalyst tubes (2) which are arranged parallel to one another in the interior space of the reactor and whose ends are welded into tube plates and also has caps (3) at each end of the reactor which each bound a cap space (4), with a fluid reaction medium (5) being fed via one cap space (4) into the catalyst tubes (2), flowing through the catalyst tubes (2) and being discharged via the other cap space (4), and is also provided with a heat exchange medium circuit in which the heat exchange medium (6) is fed in at one end of the reactor, flows through the intermediate space between the catalyst tubes (2) and flows out at the other end of the reactor, wherein the catalyst tubes (2) are arranged in two or more catalyst tube regions (7) which are thermally separate from one another, is proposed.

    Abstract translation: 一种用于测试催化剂体系的反应器，其具有多个催化剂管（2），所述多个催化剂管（2）在所述反应器的内部空间中彼此平行地布置，并且其端部被焊接到管板中，并且在所述反应器的每一端具有盖（3） 反应器，每个反应器结合盖空间（4），流体反应介质（5）经由一个盖空间（4）进入催化剂管（2），流过催化剂管（2）并经由另一个排出 盖子空间（4），并且还设置有热交换介质回路，其中热交换介质（6）在反应器的一端进料，流过催化剂管（2）之间的中间空间并流出 在反应器的另一端，其中催化剂管（2）布置在彼此热分离的两个或更多个催化剂管区域（7）中。

    Maximum reaction rate converter system for exothermic reactions
    30.
    发明授权
    Maximum reaction rate converter system for exothermic reactions 有权
    用于放热反应的最大反应速率转换器系统

    公开(公告)号：US07371361B2

    公开(公告)日：2008-05-13

    申请号：US10904315

    申请日：2004-11-03

    Applicant: Shashi P. Singh ,  David P. Mann ,  Anant Pisut

    Inventor： Shashi P. Singh ,  David P. Mann ,  Anant Pisut

    IPC: C01C1/04 ,  C01B3/16

    CPC classification number: C01C1/0423 ,  B01J8/008 ,  B01J8/067 ,  B01J23/462 ,  B01J2208/00212 ,  B01J2208/00221 ,  B01J2208/00513 ,  B01J2208/00548 ,  B01J2219/00238 ,  C01C1/0441 ,  C01C1/0482 ,  Y02E60/364 ,  Y02P20/52

    Abstract: An ammonia converter system and method are disclosed. The reactor can alter the conversion of ammonia by controlling the reaction temperature of the exothermic reaction along the length of the reactor to parallel the equilibrium curve for the desired product. The reactor 100 can comprise a shell 101 and internal catalyst tubes 109. The feed gas stream enters the reactor, flows through the shell 101, and is heated by indirect heat exchange with the catalyst tubes 109. The catalyst tubes 109 comprise reactive zones 122 having catalyst and reaction limited zones 124 that can comprise inert devices that function to both separate the reactive zones, increase heat transfer area, and reduce the temperature of the reaction mixture as the effluent passes through the catalyst tube 109.

    Abstract translation: 公开了一种氨转化器系统和方法。 反应器可以通过控制沿着反应器长度的放热反应的反应温度平行所需产物的平衡曲线来改变氨的转化率。 反应器100可以包括壳体101和内部催化剂管109。 进料气流进入反应器，流过壳体101，并通过与催化剂管109的间接热交换加热。 催化剂管109包括具有催化剂和反应限制区124的反应区122，其可以包含用于分离反应区的惰性装置，增加传热面积，并且当流出物通过催化剂管时降低反应混合物的温度 109。

Patent Agency Ranking