-
公开(公告)号：US09809759B2
公开(公告)日：2017-11-07
申请号：US15061560
申请日：2016-03-04
Applicant: ExxonMobil Chemical Patents Inc.
Inventor： Paul F. Keusenkothen , Frank Hershkowitz , Gary D. Mohr , Changmin Chun , Jeffrey W. Frederick
CPC classification number: C10G9/18 , B01J4/004 , B01J8/0423 , B01J8/0438 , B01J8/0442 , B01J8/0453 , B01J8/0457 , B01J19/02 , B01J19/2485 , B01J2208/00106 , B01J2208/00309 , B01J2208/00327 , B01J2208/00495 , B01J2208/0053 , B01J2208/00911 , B01J2219/0004 , B01J2219/00117 , B01J2219/00121 , B01J2219/00139 , B01J2219/00155 , B01J2219/00159 , B01J2219/0281 , B01J2219/182 , B01J2219/185 , B01J2219/1923 , B01J2219/194 , B01J2219/1943 , B01J2219/1947 , C07C4/04 , C10G9/26 , F23L15/02 , Y02E20/348
Abstract: The present disclosure relates to reactor components and their use, e.g., in regenerative reactors. A process and apparatus for utilizing different wetted areas along the flow path of a fluid in a pyrolysis reactor, e.g., a thermally regenerating reactor, such as a regenerative, reverse-flow reactor, is described.
-
公开(公告)号：US09751027B2
公开(公告)日：2017-09-05
申请号：US15047361
申请日：2016-02-18
Applicant: Cameron International Corporation
Inventor： Rafiqul Khan , Joseph Min-Hsiun Lee , Gary W. Sams
IPC: B01D17/00 , C10G31/00 , B01D17/04 , C10G31/08 , B01D17/02 , B01D17/12 , B01D19/00 , B01D21/00 , B01D21/02 , B01D21/24 , B01J4/00 , C10G33/06 , B08B9/093
CPC classification number: B01D17/04 , B01D17/0214 , B01D17/12 , B01D19/0036 , B01D21/0042 , B01D21/0087 , B01D21/10 , B01D21/2416 , B01D21/2472 , B01J4/004 , B01J2204/002 , B01J2204/005 , B01J2219/182 , B01J2219/1943 , B08B9/0933 , C02F1/00 , C10G31/08 , C10G33/06 , C10G2300/4081 , C10G2300/805
Abstract: A method and system for controlling an interface emulsion layer within an oil treatment vessel includes injecting a water flow through a plurality of radial eductors arranged about a radial eductor manifold located in the brine water layer. Each radial eductor is oriented vertically to the radial eductor manifold and the horizontal axis of the oil treatment vessel. The water flow through the plurality of radial eductors causes a swirling flow pattern in a volume of water around each radial eductor that is effective for promoting a collapse of the interface emulsion layer. The water flow through each radial eductor, which may be a recycled water flow, may be in a range of about 1 to 5 feet per minute.
-
公开(公告)号：US20170210708A1
公开(公告)日：2017-07-27
申请号：US15501187
申请日：2015-08-07
Applicant: SABIC GLOBAL TECHNOLOGIES B.V.
CPC classification number: C07C407/00 , B01J4/004 , B01J10/002 , B01J19/0006 , B01J19/2425 , B01J19/248 , B01J2219/00094 , B01J2219/00166 , B01J2219/00177 , C07C37/08 , C07C45/53 , C07C39/04 , C07C49/08 , C07C409/10
Abstract: An apparatus for oxidation of a C8-C12 alkylbenzene reactant to a C8-C12 alkylbenzene hydroperoxide product, the re-actor can comprise: a flow reactor comprising a reactant inlet, an oxidate product outlet, wherein the reactor is configured to provide a liquid flow from the reactant inlet to the product outlet, a gas inlet configured to introduce an oxygen-containing gas into the reactor and an inlet sparger configured to flow gas bubbles comprising the oxygen-containing gas within the liquid flow, and wherein: the inlet sparger is configured to flow the gas bubbles having a diameter of 1.0 mm to 5.0 mm over a gas bubble residence time from 1 to 200 seconds, and/or the inlet sparger configured to flow the gas bubbles such that greater than or equal to 80% of the gas bubbles do not coalesce into larger bubbles over a gas bubble residence time of 1 to 200 seconds.
-
公开(公告)号：US09687805B2
公开(公告)日：2017-06-27
申请号：US14908044
申请日：2014-07-15
Applicant: NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
Inventor： Kentarou Morita , Kazuki Murahashi , Eiichi Yamada , Yuzuru Kato , Yoshiyuki Saiwai , Atsushi Murata
CPC classification number: B01J8/22 , B01J4/004 , B01J8/1827 , B01J2208/00902 , B01J2208/00911 , C10G2/342 , C10G2/343 , C10G2/344
Abstract: The present invention includes a reactor main body (4) that is formed into a tubular shape having an axis (O) as the center and accumulates a slurry (S); a gas supply line (10) for incorporating a synthesis gas (G) into the reactor main body (4), and a sparger part (5) that is disposed in a lower portion within the reactor main body (4), communicates with the gas supply line (10), and sprays the synthesis gas (G). The sparger part (5) includes a header tube (15) in which a plurality of openings are formed so as to be separated from each other in a first direction and which sprays the synthesis gas (G) from the openings, and a pair of wall surface parts that protrude from the header tube (15), on opposing sides of the plurality of openings and in a direction orthogonal to the first direction.
-
公开(公告)号：US09643146B2
公开(公告)日：2017-05-09
申请号：US14093155
申请日：2013-11-29
Applicant: UOP LLC
Inventor： Jonathan Andrew Tertel , Quan Yuan , Stephen R. Addison
CPC classification number: B01J10/002 , B01J4/004 , B01J4/008 , C10G19/02 , C10G2300/202
Abstract: A unit for processing a liquid/gas phase mixture, a mercaptan oxidation apparatus, and a method of processing a liquid/gas phase mixture are provided. In an embodiment, a unit for processing a liquid/gas phase mixture includes a vessel that is adapted to receive the liquid/gas phase mixture and a distributor that is disposed in the vessel. The distributor is adapted for flow of the liquid/gas phase mixture into the vessel, and the distributor includes a first outlet pipe that is horizontally disposed within the vessel. The first outlet pipe includes top orifices and bottom orifices that are spaced along the first outlet pipe, and the first outlet pipe is in fluid communication with the vessel through the top orifices and the bottom orifices. The top orifices have a smaller cross-sectional area than the bottom orifices.
-
Patent Agency Ranking
公开(公告)号：US20170081257A1
公开(公告)日：2017-03-23
申请号：US14858526
申请日：2015-09-18
Applicant: Chevron Phillips Chemical Company LP
Inventor： Bruce E. KREISCHER
CPC classification number: C07C2/32 , B01J4/004 , B01J4/02 , B01J8/22 , B01J8/222 , B01J19/1806 , B01J19/1818 , B01J19/1825 , B01J19/1856 , B01J19/1862 , B01J19/1881 , B01J2208/00044 , B01J2208/00141 , B01J2208/00176 , B01J2208/00212 , B01J2208/00265 , B01J2208/00274 , B01J2208/00283 , B01J2208/00911 , B01J2219/00056 , B01J2219/00083 , B01J2219/00094 , B01J2219/00108 , B01J2219/0011 , B01J2219/00195 , B01J2219/00211 , B01J2219/00229 , B01J2219/00238 , C07C2/30 , C07C2/88 , C07C2523/26 , C07C2523/755 , C07C2527/135 , C07C2531/12 , C07C2531/14 , C07C2531/24 , C07C11/02 , C07C11/107
Abstract: A process includes periodically or continuously introducing an olefin monomer and periodically or continuously introducing a catalyst system or catalyst system components into a reaction mixture within a reaction system, oligomerizing the olefin monomer within the reaction mixture to form an oligomer product, and periodically or continuously discharging a reaction system effluent comprising the oligomer product from the reaction system. The reaction system includes a total reaction mixture volume and a heat exchanged portion of the reaction system comprising a heat exchanged reaction mixture volume and a total heat exchanged surface area providing indirect contact between the reaction mixture and a heat exchange medium. A ratio of the total heat exchanged surface area to the total reaction mixture volume within the reaction system is in a range from 0.75 in−1 to 5 in−1, and an oligomer product discharge rate from the reaction system is between 1.0 (lb)(hr−1)(gal−1) to 6.0 (lb)(hr−1)(gal−1).
-
67.发明申请PNEUMATICALLY AGITATED IONIC LIQUID ALKYLATION USING VAPORIZATION TO REMOVE REACTION HEAT 有权使用蒸发去除反应热的气动化学离子液体烷基化公开(公告)号：US20160263547A1
公开(公告)日：2016-09-15
申请号：US14656950
申请日：2015-03-13
Applicant: Chevron U.S.A. Inc.
Inventor： Donald Henry Mohr , Huping Luo , Clifford Michael Lowe , Hye Kyung Cho Timken , Krishniah Parimi , Michael John Girgis , Bong-Kyu Chang
CPC classification number: B01J19/246 , B01J4/002 , B01J4/004 , B01J19/0013 , B01J19/2405 , B01J19/2465 , B01J19/26 , B01J2219/00047 , B01J2219/00103 , B01J2219/00108 , B01J2219/0011 , B01J2219/182 , B01J2219/185 , B01J2219/1943 , B01J2219/24 , C07C2/58 , C07C2527/125 , C07C9/16
Abstract: Systems and apparatus for ionic liquid catalyzed hydrocarbon conversion, such as alkylation, using vaporization to remove reaction heat from an ionic liquid reactor and to provide mixing therein, wherein hydrocarbon vapors are withdrawn from the ionic liquid reactor and the withdrawn hydrocarbon vapor is recovered by a hydrocarbon vapor recovery unit in fluid communication with the ionic liquid reactor for recycling condensed hydrocarbons to the ionic liquid reactor. Processes for ionic liquid catalyzed alkylation are also disclosed.
Abstract translation: 用于离子液体催化的烃转化的系统和装置，例如烷基化，使用蒸发来除去离子液体反应器的反应热并提供其中的混合，其中烃蒸气从离子液体反应器中取出并且取出的烃蒸气通过 烃蒸气回收单元与离子液体反应器流体连通，用于将冷凝的烃再循环到离子液体反应器。 还公开了用于离子液体催化烷基化的方法。
-
公开(公告)号：US20160160129A1
公开(公告)日：2016-06-09
申请号：US14908044
申请日：2014-07-15
Applicant: NIPPON STEEL & SUMIKIN ENGINEERING CO., LTD.
Inventor： Kentarou MORITA , Kazuki MURAHASHI , Eiichi YAMADA , Yuzuru KATO , Yoshiyuki SAIWAI , Atsushi MURATA
IPC: C10G2/00
CPC classification number: B01J8/22 , B01J4/004 , B01J8/1827 , B01J2208/00902 , B01J2208/00911 , C10G2/342 , C10G2/343 , C10G2/344
Abstract: The present invention includes a reactor main body (4) that is formed into a tubular shape having an axis (O) as the center and accumulates a slurry (S); a gas supply line (10) for incorporating a synthesis gas (G) into the reactor main body (4), and a sparger part (5) that is disposed in a lower portion within the reactor main body (4), communicates with the gas supply line (10), and sprays the synthesis gas (G). The sparger part (5) includes a header tube (15) in which a plurality of openings are formed so as to be separated from each other in a first direction and which sprays the synthesis gas (G) from the openings, and a pair of wall surface parts that protrude from the header tube (15), on opposing sides of the plurality of openings and in a direction orthogonal to the first direction.
Abstract translation: 本发明包括反应器主体（4），其以轴线（O）为中心形成管状，并积聚有浆料（S）; 用于将合成气（G）并入反应器主体（4）中的气体供给管线（10）和设置在反应堆主体（4）内的下部的喷洒部（5）与反应器主体 气体供给管线（10），喷射合成气体（G）。 喷射器部分（5）包括集管（15），其中多个开口形成为沿着第一方向彼此分离并且从开口喷射合成气（G），并且一对 所述壁表面部分从所述集管（15）突出，在所述多个开口的相对侧上并且在与所述第一方向正交的方向上。
-
公开(公告)号：US20160158669A1
公开(公告)日：2016-06-09
申请号：US15047361
申请日：2016-02-18
Applicant: Cameron International Corporation
Inventor： Rafiqul Khan , Joseph Min-Hsiun Lee , Gary W. Sams
CPC classification number: B01D17/04 , B01D17/0214 , B01D17/12 , B01D19/0036 , B01D21/0042 , B01D21/0087 , B01D21/10 , B01D21/2416 , B01D21/2472 , B01J4/004 , B01J2204/002 , B01J2204/005 , B01J2219/182 , B01J2219/1943 , B08B9/0933 , C02F1/00 , C10G31/08 , C10G33/06 , C10G2300/4081 , C10G2300/805
Abstract: A method and system for controlling an interface emulsion layer within an oil treatment vessel includes injecting a water flow through a plurality of radial eductors arranged about a radial eductor manifold located in the brine water layer. Each radial eductor is oriented vertically to the radial eductor manifold and the horizontal axis of the oil treatment vessel. The water flow through the plurality of radial eductors causes a swirling flow pattern in a volume of water around each radial eductor that is effective for promoting a collapse of the interface emulsion layer. The water flow through each radial eductor, which may be a recycled water flow, is preferably in a range of 1 to 5 feet per minute.
Abstract translation: 用于控制油处理容器内的界面乳液层的方法和系统包括将水流注入位于盐水水层中的径向喷射器歧管周围的多个径向喷射器。 每个径向喷射器垂直于径向喷射器歧管和油处理容器的水平轴线定向。 通过多个径向喷射器的水流在每个径向喷射器周围的水体积中产生旋转流动模式，其有效促进界面乳剂层的塌陷。 通过每个径向喷射器（其可以是循环水流）的水流优选在1至5英尺/分钟的范围内。
-
公开(公告)号：US09302239B2
公开(公告)日：2016-04-05
申请号：US14345490
申请日：2012-09-18
Applicant: Joung Ha Kim , Ju Dong Lee , Jae Ho Yun , Ho Kyeong Kim , Sang Min Kim , Seung Beom Hong , Ta Kwan Woo , Seung Hee An
Inventor： Joung Ha Kim , Ju Dong Lee , Jae Ho Yun , Ho Kyeong Kim , Sang Min Kim , Seung Beom Hong , Ta Kwan Woo , Seung Hee An
IPC: B01J19/00 , B01J19/18 , B01J4/00 , B01J10/00 , B01J8/00 , B01J8/08 , B01J8/18 , C07C9/00 , C07C9/02 , C07C9/04 , C10L3/00 , C10L3/06 , C10L3/10 , C01B3/02 , C01B3/32 , C01B6/00
CPC classification number: B01J10/00 , B01J4/004 , B01J19/0066 , B01J19/18
Abstract: According to an embodiment of the present invention, a gas-liquid circulating type gas hydrate reactor, includes: a reactor body configured to be supplied with gas and water to generate a gas hydrate; and a bubble generator configured to be disposed around a lower portion of the reactor body, wherein the gas supplied from the lower portion of the reactor body is jetted into the reactor body through the bubble generator. The gas-liquid circulating type gas hydrate reactor in accordance with the present invention makes it possible to jet gas at a high speed by using the bubble generator disposed at the low portion of the reactor body so as to promote the reaction of water and gas which are accommodated in the reactor body while forming a water stream at the lower portion of the reactor body that enables a smooth agitation of the water and the gas.
Abstract translation: 根据本发明的实施例，气液循环式气体水合物反应器包括：反应器主体，被配置为供应气体和水以产生气体水合物; 以及气泡生成器，其构造成围绕反应器主体的下部设置，其中从反应器主体的下部供应的气体通过气泡发生器被喷射到反应器主体中。 根据本发明的气液循环式气体水合物反应器使得可以通过使用设置在反应器主体的低部分处的气泡发生器高速喷射气体，从而促进水和气体的反应， 容纳在反应器主体中，同时在反应器主体的下部形成水流，能够平稳地搅拌水和气体。
-
-
-
-
-
-
-
-
-
Search Results
144
records
(took 0.021 seconds)
