公开(公告)号：US4792408A

公开(公告)日：1988-12-20

申请号：US37622

申请日：1987-04-13

Applicant: James A. Titmas

Inventor： James A. Titmas

IPC: B01J3/00 ,  B01J3/04 ,  C02F1/02 ,  B01D23/00 ,  B01D29/00 ,  C02F1/72

CPC classification number: B01J3/008 ,  B01J3/044 ,  Y02P20/544

Abstract: A continuously flowing fluid is processed by being fed to the top of a hydraulic downdraft column (17) which is of a height such that the pressure at the bottom thereof will approximately be at the pressure necessary to create supercritical water conditions. The fluid is conducted to the bottom of the column (17) and received in a reaction chamber (21) in which the majority of the fluid is recirculated around an annular baffle plate (24). The material in the reaction chamber (21) is heated to a temperature above that necessary to create supercritical water conditions by an independent reaction taking place in a heating chamber (32). The result is that the fluid will undergo chemical reactions at the supercritical temperature and pressure range and will be of a lower specific gravity than the unprocessed fluid. The material not being recirculated in the chamber (21) is fed to one of two updraft columns (30, 31), a start-up column (30) used to preheat the material in the downdraft column (17) during initiation of the process, and a second column ( 31) isolated from the downdraft column (17) so as not to transmit any heat thereto during normal operation of the process. The temperature of the fluid in the downdraft column (17) is thereby controlled to prevent decomposition of the material until the fluid enters the reaction chamber (21) at which time it is abruptly brought up to the supercritical water temperature.

Abstract translation: 连续流动的流体通过进料到液压下流式塔（17）的顶部来加工，该液压下移塔（17）的高度使得其底部的压力将大致处于产生超临界水条件所需的压力。 流体被引导到塔（17）的底部并且被接纳在反应室（21）中，其中大部分流体围绕环形挡板（24）再循环。 通过在加热室（32）中发生的独立反应，将反应室（21）中的材料加热到高于通过独立反应产生超临界水条件所需的温度。 结果是流体将在超临界温度和压力范围内发生化学反应，并且比未处理的流体具有更低的比重。 在室（21）中不被再循环的材料被供给到两个上升气流柱（30,31）中的一个，用于在开始过程期间预热下吹塔（17）中的材料的启动柱（30） ，以及从下吹塔（17）隔离的第二柱（31），以便在该过程的正常操作期间不传递任何热量。 由此控制下降塔（17）中的流体的温度，以防止材料分解直到流体进入反应室（21），此时其突然升高到超临界水温。

公开(公告)号：US4007321A

公开(公告)日：1977-02-08

申请号：US551494

申请日：1975-02-20

Applicant: Norbert Scholz ,  Georg Friedrich Vock ,  Kurt Erdmann ,  Guenther John ,  Hans Frielingsdorf ,  Wolfgang Gruber ,  Heinz Mueller-Tamm

Inventor： Norbert Scholz ,  Georg Friedrich Vock ,  Kurt Erdmann ,  Guenther John ,  Hans Frielingsdorf ,  Wolfgang Gruber ,  Heinz Mueller-Tamm

IPC: C08F2/00 ,  B01J3/04 ,  B01J8/00 ,  B01J19/18 ,  C08F2/04 ,  C08F6/00 ,  C08F6/06 ,  C08F10/00 ,  C08F110/00 ,  C08F110/02 ,  C08F2/14 ,  C08F6/24

CPC classification number: B01J19/1837 ,  B01J3/044 ,  B01J8/0055 ,  B01J8/007 ,  C08F110/00 ,  C08F10/00 ,  C08F110/02

Abstract: Particulate olefin polymers are prepared by catalytic polymerization of monoolefins in an auxiliary liquid containing the monomers to be polymerized in dissolved form and the particulate polymer product in suspended form. The reaction mixture is recycled in a loop to which the starting materials are fed and from which the particulate polymer formed is removed. The essential features are (a) that a side stream is branched off from the loop, (b) that the side stream is caused to pass through a separating zone in which particulate olefin polymer is separated by centrifugal acceleration at temperatures and pressures in the same range as present in the loop and (c) that the separated particulate olefin polymer is discharged through flashing means.

Abstract translation: 颗粒状烯烃聚合物是通过单链烯烃在含有待溶解形式聚合的单体的辅助液体和悬浮形式的颗粒状聚合物产物进行催化聚合来制备的。 将反应混合物循环在起始原料进料的循环中，从中除去形成的颗粒聚合物。 基本特征是（a）侧流从环分支，（b）使侧流通过分离区，其中通过离心加速在相同温度和压力下分离出颗粒烯烃聚合物 存在于循环中的范围，（c）分离的颗粒状烯烃聚合物通过闪蒸装置排出。

公开(公告)号：US3609296A

公开(公告)日：1971-09-28

申请号：US3609296D

申请日：1970-03-27

Applicant: FUEL ENGINEERING

Inventor： BLAIR JOE B

IPC: B01J3/04 ,  F24H1/10 ,  F27D11/02

CPC classification number: B01J3/044 ,  F24H1/102 ,  F27D11/02 ,  Y10S165/902

Abstract: An autoclave apparatus comprising an autoclave forming a product-receiving chamber having an inlet port in one end and an outlet port in the opposite end and being, further, formed with an access opening. An electrically heated heat exchanger is formed with a chamber which contains heat storage means and such chamber has an inlet in one end and an outlet in the opposite end. Conduits connect the inlet to the autoclave with the outlet from the heat exchanger and the outlet of the autoclave with the inlet to the heat exchanger. Means is provided for supplying gas to the system whereby such system may be pressurized with the gas and such gas circulated through the autoclave and in heatexchange relationship with the heat storage means to heat such gas to an elevated temperature thereby providing an atmosphere in the product-receiving chamber of the desired temperature and pressure.

公开(公告)号：US20180036698A1

公开(公告)日：2018-02-08

申请号：US15787652

申请日：2017-10-18

Applicant: UOP LLC

Inventor： Rajeswar R. Gattupalli ,  Vinayender Kuchana ,  Laura E. Leonard ,  Vighneswara R. Kollati ,  Aziz Sattar ,  Mohamad R. Mostofi-Ashtiani ,  Peter Shafe

IPC: B01J6/00 ,  B01J3/04 ,  C07C2/78

CPC classification number: B01J6/008 ,  B01J3/044 ,  C07C2/78 ,  C07C11/24

Abstract: Methods and apparatus to produce alkynes are described. The method includes combusting fuel and an oxidizer in a combustion zone to create a carrier gas stream, which is accelerated to supersonic speed in an expansion zone. A feedstock material is injected into a feedstock injection zone using two or more pluralities of injection nozzles. The injection nozzles are arranged annularly. The carrier gas stream is transitioned from supersonic speed to subsonic speed to create a shockwave in a reaction zone. The reaction zone is directly connected to the feedstock injection zone, and the shockwave is created adjacent to the feedstock injection zone. The carrier gas stream and the feedstock material are simultaneously mixed and reacted.

公开(公告)号：US20110002816A1

公开(公告)日：2011-01-06

申请号：US12735349

申请日：2009-02-04

Applicant: Marc Parisel ,  Brent Walworth

Inventor： Marc Parisel ,  Brent Walworth

IPC: B01J19/00

CPC classification number: B01J19/2435 ,  B01J3/044 ,  B01J19/0013 ,  B01J2219/00094 ,  B01J2219/00243

Abstract: A tubular reactor for use in polymerisation reactions is described, having a design pressure PR of 40-65 barg, at least a portion of which is oriented vertically and at least part of which vertical portion is surrounded by a concentric jacket for the passage of cooling fluid, wherein the design pressure in barg of the jacket PJ is less than 0.0018.PR2.25. Another aspect of the invention concerns a tubular reactor for use in polymerisation reactions having a design pressure PR of 40-65 barg, at least a portion of which is oriented vertically and at least part of which vertical portion is surrounded by a concentric jacket for the passage of cooling fluid, wherein the actual thickness of the reactor wall is either no more than 2 mm greater and/or no more than 10% greater than the minimum wall thickness required to withstand the design pressure PR as calculated according to the ASME Boiler and Pressure Vessel code.

Abstract translation: 描述了用于聚合反应的管式反应器，其设计压力PR为40-65巴，其至少一部分垂直取向，并且其至少一部分垂直部分被同心夹套围绕以便冷却通过 流体，其中护套PJ的设计压力barg小于0.0018.PR2.25。 本发明的另一方面涉及一种用于聚合反应的管式反应器，其设计压力PR为40-65巴，其设计压力PR至少为40-65巴，其至少一部分垂直取向，并且其至少部分垂直部分被同心夹套围绕，用于 冷却流体的通过，其中反应器壁的实际厚度不得比承受根据ASME锅炉计算的设计压力PR所需的最小壁厚大不超过2mm和/或不超过10％，以及 压力容器代码。

公开(公告)号：US20030161783A1

公开(公告)日：2003-08-28

申请号：US10326286

申请日：2002-12-23

Inventor： Harold A. Huckins

IPC: C01B015/029

CPC classification number: C01B15/029 ,  B01J3/044 ,  B01J8/08 ,  B01J8/228 ,  B01J12/00 ,  B01J19/243 ,  B01J2219/00094 ,  B01J2219/00121 ,  B01J2219/00162

Abstract: The invention relates to a method and apparatus for safely producing hydrogen peroxide by injecting dispersed minute bubbles of hydrogen and oxygen into a rapidly flowing liquid medium. The minute bubbles are surrounded by the liquid medium of sufficient volume for preventing an explosive reaction between the hydrogen and oxygen. The liquid medium is formed of an acidic aqueous solution and a Group VIII metal catalyst. Hydrogen is sparged into the flowing medium for dissolution of the hydrogen in the medium. Oxygen bubbles are reacted with the dissolved hydrogen for producing hydrogen peroxide. Preferably, the liquid medium has a velocity of at least 10 feet per second for providing a bubbly flow regime in the reactor. The invention allows the direct combination of oxygen and hydrogen while preventing propagation of an explosive condition within the reactor. The method and apparatus provide for the safe production of hydrogen peroxide with low manufacturing costs.

Abstract translation: 本发明涉及通过将分散的氢气和氧气的微小气泡注入到快速流动的液体介质中来安全地生产过氧化氢的方法和装置。 微小气泡被足够体积的液体介质包围，以防止氢气和氧气之间的爆炸性反应。 液体介质由酸性水溶液和VIII族金属催化剂形成。 将氢气喷射到流动介质中，以将氢溶解在介质中。 氧气与溶解的氢气反应生成过氧化氢。 优选地，液体介质具有至少10英尺/秒的速度，以在反应器中提供气泡流动状态。 本发明允许氧和氢的直接组合，同时防止反应器内的爆炸性条件的扩散。 该方法和装置以低制造成本提供安全生产过氧化氢。

公开(公告)号：US4068054A

公开(公告)日：1978-01-10

申请号：US711028

申请日：1976-08-02

Applicant: Kenneth W. Willcox

Inventor： Kenneth W. Willcox

IPC: B01J3/04 ,  B01J19/18 ,  C08F2/00 ,  C08F10/00 ,  C10L1/14 ,  C10L1/22 ,  C10L1/24 ,  C08F4/24 ,  C08F2/14

CPC classification number: B01J19/1837 ,  B01J19/002 ,  B01J3/044 ,  C08F10/00 ,  B01J2208/00734 ,  B01J2219/00094 ,  B01J2219/00254 ,  C10L1/14 ,  C10L1/232 ,  C10L1/2437

Abstract: An olefin is polymerized in a hydrocarbon diluent in a turbulent reaction zone to produce particles of polymer which are substantially insoluble in the diluent. Fouling of the reactor by adherence of polymer particles to the walls of the reactor is reduced by adding to the reaction medium a composition which comprises a porphyrin compound, alone or together with a metal alkyl sulfosuccinate. This composition is also useful as an antistatic agent for liquid hydrocarbons and halohydrocarbons.

Abstract translation: 烯烃在湍流反应区中的烃稀释剂中聚合以产生基本上不溶于稀释剂的聚合物颗粒。 通过向反应介质中加入单独或与金属烷基磺基琥珀酸盐一起包含卟啉化合物的组合物来减少聚合物颗粒粘附到反应器壁上的反应器的结垢。 该组合物也可用作液体烃和卤代烃的抗静电剂。

公开(公告)号：US3469414A

公开(公告)日：1969-09-30

申请号：US3469414D

申请日：1968-01-23

Applicant: FUEL ENG

Inventor： SCHMIDT JAMES H ,  HEDSTROM WARREN W

IPC: B01J3/04 ,  F25D17/06 ,  F28D5/00

CPC classification number: B01J3/044

公开(公告)号：US3431081A

公开(公告)日：1969-03-04

申请号：US3431081D

申请日：1963-11-01

Applicant: ICI LTD

Inventor： EDWARDS HARRY ,  KENYON CHARLES FREDERICK

IPC: B01J3/04 ,  B01J4/00 ,  B29B7/60 ,  C08G18/08 ,  B01F3/08

CPC classification number: B01J4/008 ,  B01J3/044 ,  B29B7/603 ,  C08G18/0895 ,  Y10S521/917 ,  Y10T137/2506

公开(公告)号：US20140219047A1

公开(公告)日：2014-08-07

申请号：US14236898

申请日：2012-08-03

Applicant: Holger Blum

Inventor： Holger Blum

IPC: B01F15/02

CPC classification number: B01F15/0216 ,  B01F3/0861 ,  B01F5/0647 ,  B01F5/102 ,  B01F15/0243 ,  B01F15/0291 ,  B01J3/006 ,  B01J3/02 ,  B01J3/044

Abstract: A mixing and metering device for mixing and metering liquid chemicals comprises a circulation pump having a suction port and a pressure port, a pipe coil, the contents volume of which is dimensioned such that the chemicals metered into the device have a residence time sufficient for the chemical reaction, a choke tube which guides the circulation stream exiting from the pipe coil, with formation of a choke point, from the outlet of the pipe coil to a metering conduit which is arranged between the choke tube and the suction port of the circulation pump and at least two metering valves, and also a falling tube which is connected to the choke tube and has a vacuum flange of the mixing and metering device to a vacuum device.

Abstract translation: 用于混合和计量液体化学品的混合和计量装置包括具有吸入口和压力端口的循环泵，管线圈，其内容物的体积被设计成使得计量到装置中的化学品具有足够的停留时间 化学反应，将从管线出口的循环流引导到形成扼流点的扼流管，从管线出口到计量管道，其配置在扼流管和循环泵的吸入口之间 和至少两个计量阀，以及连接到扼流管并且具有混合和计量装置的真空法兰的真空装置的下降管。