公开(公告)号：US10053399B2

公开(公告)日：2018-08-21

申请号：US15850233

申请日：2017-12-21

Applicant: ExxonMobil Chemical Patents Inc.

Inventor： Matthew J. Vincent ,  Vijay Nanda

IPC: C07C2/66 ,  B01J8/04

CPC classification number: C07C2/66 ,  B01J8/0453 ,  B01J8/0492 ,  B01J8/0496 ,  B01J2208/00168 ,  B01J2208/00256 ,  B01J2208/00274 ,  C07C2529/08 ,  C07C2529/18 ,  C07C2529/70 ,  Y02P20/582 ,  C07C15/073 ,  C07C15/085

Abstract: The present disclosure relates to a process for production of a monoalkyl aromatic compound by alkylation of alkylatable aromatic compounds with an alkylating agent in a reactor comprising at least a first and a second series-connected alkylation reaction zones and a cooler disposed between the first and the second series-connected alkylation reaction zones. The process comprising a step of cooling at least a portion of an effluent withdrawn from the first alkylation reaction zone before being introduced into the second alkylation reaction zone.

公开(公告)号：US20180229201A1

公开(公告)日：2018-08-16

申请号：US15891941

申请日：2018-02-08

Applicant: Technobell d.o.o. Koper

Inventor： Gabor Toth

IPC: B01J8/06 ,  C07D307/60

CPC classification number: B01J8/067 ,  B01J2208/00017 ,  B01J2208/00132 ,  B01J2208/00221 ,  B01J2208/00256 ,  B01J2208/0053 ,  B01J2208/021 ,  C07D307/60

Abstract: A tubular reactor that produces maleic anhydride from a gas mixture containing n-butane and oxygen includes a first reaction zone including an inlet for the gas mixture and a second reaction zone including an outlet for a reaction gas mixture, a plurality of tubes extending in an axial direction through the first and second reaction zones, a temperature control system, configured for controlling a reaction temperature in each of the reaction zones independently, includes a heat transfer system for each of the reaction zones configured for controlling the temperature of a liquid coolant flowing through one of the reaction zones, and a circulation pumping system configured for controlling flow conditions of the liquid coolant flowing through the reactor and one of the heat transfer systems, and a preheating arrangement configured for preheating the gas mixture such that the gas mixture enters the first reaction zone at a predefined inlet temperature.

公开(公告)号：US09993791B2

公开(公告)日：2018-06-12

申请号：US15338967

申请日：2016-10-31

Applicant: Seerstone LLC

Inventor： Dallas B. Noyes

IPC: B01J8/02 ,  B01J19/22 ,  B01J8/08 ,  C01B31/02 ,  B01J12/00 ,  B01J19/24

CPC classification number: C01B32/26 ,  B01J8/02 ,  B01J8/025 ,  B01J8/087 ,  B01J12/007 ,  B01J19/22 ,  B01J19/24 ,  B01J19/2495 ,  B01J2208/00256 ,  B01J2208/00415 ,  B01J2208/00433 ,  B01J2208/00504 ,  B01J2208/00884 ,  B01J2208/00893 ,  B01J2208/027 ,  B01J2219/00038 ,  B01J2219/00103 ,  B01J2219/00135 ,  B01J2219/00139 ,  B01J2219/00157 ,  B01J2219/24 ,  C01B32/05 ,  C01B32/16 ,  C01B32/25

Abstract: A reactor for producing a solid carbon material comprising at least one reaction chamber configured to produce a solid carbon material and water vapor through a reduction reaction between at least one carbon oxide and at least one gaseous reducing material in the presence of at least one catalyst material. Additional reactors, and related methods of producing a solid carbon material, and of forming a reactor for producing a solid carbon material are also described.

公开(公告)号：US20180073430A1

公开(公告)日：2018-03-15

申请号：US15703042

申请日：2017-09-13

Applicant: 8 Rivers Capital, LLC

Inventor： Brock Alan Forrest ,  Xijia Lu ,  Rodney John Allam ,  Jeremy Eron Fetvedt ,  Miles R. Palmer

IPC: F02C3/28 ,  F02C3/24 ,  F02C3/04 ,  F02C7/22 ,  C10J3/48 ,  C10J3/46 ,  C10K1/00 ,  C01B3/38 ,  B01J8/24 ,  C10K3/02

CPC classification number: F02C3/28 ,  B01J8/24 ,  B01J2208/00256 ,  C01B3/38 ,  C01B2203/0261 ,  C01B2203/0465 ,  C01B2203/0495 ,  C01B2203/0833 ,  C10J3/463 ,  C10J3/466 ,  C10J3/485 ,  C10J2300/0959 ,  C10J2300/1606 ,  C10J2300/1618 ,  C10J2300/1621 ,  C10J2300/165 ,  C10J2300/1653 ,  C10J2300/1662 ,  C10J2300/1846 ,  C10K1/002 ,  C10K1/003 ,  C10K1/004 ,  C10K1/005 ,  C10K1/007 ,  C10K1/04 ,  C10K1/10 ,  C10K1/32 ,  C10K3/026 ,  F02C3/04 ,  F02C3/24 ,  F02C7/22 ,  F05D2220/32 ,  F05D2240/35 ,  Y02E20/18 ,  Y02P20/146

Abstract: The present disclosure relates to a power production system that is adapted to achieve high efficiency power production using partial oxidation of a solid or liquid fuel to form a partially oxidized stream that comprises a fuel gas. This fuel gas stream can be one or more of quenched, filtered, and cooled before being directed to a combustor of a power production system as the combustion fuel. The partially oxidized stream is combined with a compressed recycle CO2 stream and oxygen. The combustion stream is expanded across a turbine to produce power and passed through a recuperator heat exchanger. The expanded and cooled exhaust stream can be further processed to provide the recycle CO2 stream, which is compressed and passed through one or more recuperator heat exchangers in a manner useful to provide increased efficiency to the combined systems.

公开(公告)号：US09663367B2

公开(公告)日：2017-05-30

申请号：US14428589

申请日：2013-09-13

Applicant: ExxonMobil Upstream Research Company ,  Solid Carbon Products LLC

Inventor： Russell J. Koveal, Jr. ,  Terry A. Ring

IPC: C01B31/02 ,  B01J8/18 ,  B01J8/08 ,  B01J8/24 ,  B82Y30/00 ,  B82Y40/00

CPC classification number: C01B31/02 ,  B01J8/08 ,  B01J8/1836 ,  B01J8/24 ,  B01J2208/00256 ,  B01J2208/00752 ,  B01J2208/00761 ,  B01J2208/00893 ,  B82Y30/00 ,  B82Y40/00 ,  C01B31/0233 ,  C01B31/024 ,  C01B32/05 ,  C01B32/162 ,  C01B32/164 ,  Y02P20/129

Abstract: Systems and a method for forming carbon allotropes are described. An exemplary reactor system for the production of carbon allotropes includes a hybrid reactor configured to form carbon allotropes from a reactant gas mixture in a Bosch reaction. The hybrid reactor includes at least two distinct zones that perform different functions including reaction, attrition, catalyst separation, or gas separation.

公开(公告)号：US20170137357A1

公开(公告)日：2017-05-18

申请号：US15268456

申请日：2016-09-16

Applicant: CHINA PETROLEUM & CHEMICAL CORPORATION ,  SHANGHAI RESEARCH INSTITUTE OF PETROCHEMICAL TECHNOLOGY SINOPEC

Inventor： Shuai HU ,  Xin JIN

IPC: C07C41/09 ,  B01J8/04 ,  C07C1/20

CPC classification number: C07C41/09 ,  B01J8/0453 ,  B01J8/0457 ,  B01J8/0492 ,  B01J8/0496 ,  B01J8/065 ,  B01J2208/00256 ,  B01J2208/00548 ,  B01J2208/027 ,  C07C1/20 ,  Y02P20/52 ,  C07C43/043 ,  C07C11/06

Abstract: The present invention relates to a method for preparing dimethyl ether from methanol which is carried out in a reaction device arranged with a plurality of catalyst bed layers connected in series, and comprises: dividing the reactant stream that contains methanol into n substreams, and feeding these different substreams into the reaction device through top feed ports or side feed ports between the catalyst bed layers of the reaction device for methanol-to-dimethyl ether reaction; wherein, the temperature T1 of the substream fed into the first catalyst bed layer is controlled within the following range: 290−50K1≦T1≦150K12−271K1+397.5; where, 1>K1≧0.5, and T1 is in unit of ° C.

公开(公告)号：US20160264496A1

公开(公告)日：2016-09-15

申请号：US15035600

申请日：2014-11-10

Applicant: VERSALIS S.P.A.

Inventor： Armando Galeotti ,  Mirko Oliosi

IPC: C07C5/333 ,  B01J19/24

CPC classification number: C07C5/333 ,  B01J8/001 ,  B01J19/24 ,  B01J2208/00176 ,  B01J2208/00256 ,  B01J2208/00265 ,  B01J2208/00504 ,  B01J2219/00024 ,  B01J2219/00103 ,  C07C15/46

Abstract: An ethylbenzene dehydrogenation plant for producing styrene which comprises a reaction section in which one or more adiabatic reaction apparatuses are positioned in series, and a steam circuit in which there is at least one first steam heat exchange apparatus; said plant being characterized in that it comprises heating equipment in which there is a heating circuit by means of recirculation of the fumes formed during dehydrogenation processes of ethylbenzene to give styrene, wherein said heating equipment comprises the following apparatuses in fluid communication with each other by means of said heating circuit: one or more ultra-heating apparatuses, one or more combustion devices in which at least one steam diffuser, one burner and at least one mixing apparatus are inserted, one or more ventilation device(s).

Abstract translation: 一种用于生产苯乙烯的乙苯脱氢装置，其包括其中一个或多个绝热反应装置串联的反应部分和其中存在至少一个第一蒸汽热交换装置的蒸汽回路; 所述设备的特征在于，其包括加热设备，其中通过在乙苯的脱氢过程中形成的烟气再循环以产生加热回路以产生苯乙烯，其中所述加热设备包括通过装置彼此流体连通的以下装置 所述加热电路：一个或多个超加热装置，一个或多个燃烧装置，其中插入有至少一个蒸汽扩散器，一个燃烧器和至少一个混合装置，一个或多个通风装置。

公开(公告)号：US09422213B2

公开(公告)日：2016-08-23

申请号：US14428298

申请日：2013-09-10

Applicant: THYSSENKRUPP INDUSTRIAL SOLUTIONS AG

Inventor： Melanie Bauer ,  Harald Kömpel ,  Alexander Schulz

IPC: C07C41/09 ,  C07C41/42 ,  B01J19/24

CPC classification number: C07C41/09 ,  B01D3/002 ,  B01D3/009 ,  B01D3/143 ,  B01J8/0457 ,  B01J19/245 ,  B01J2208/00256 ,  B01J2208/065 ,  B01J2219/00006 ,  B01J2219/00103 ,  B01J2219/24 ,  C07C41/42 ,  Y02P20/127 ,  C07C43/043

Abstract: The present disclosure relates to a method and apparatus for producing dimethyl ether by catalytic dehydration of methanol and by distillation of the dehydration product. The method is characterized in that the catalytic dehydration takes place in at least two reaction stages which are connected in series and of which at least the first reaction stage is operated adiabatically, wherein a cooling of the reaction products takes place at least between the first and the second reaction stages.

Abstract translation: 本公开涉及通过甲醇的催化脱水和蒸馏脱水产物生产二甲醚的方法和装置。 该方法的特征在于催化脱水在串联连接的至少两个反应阶段中进行，其中至少第一反应阶段被绝热地进行，其中反应产物的冷却至少在第一和第 第二反应阶段。

公开(公告)号：US20160074825A1

公开(公告)日：2016-03-17

申请号：US14485563

申请日：2014-09-12

Applicant: UOP LLC

Inventor： Syed Basheer Umar ,  Ashim Mandal

IPC: B01J8/18 ,  B01J8/24 ,  B01J38/12 ,  B01J29/90 ,  B01J29/06

CPC classification number: B01J8/1836 ,  B01J8/24 ,  B01J8/28 ,  B01J29/06 ,  B01J29/08 ,  B01J29/40 ,  B01J29/80 ,  B01J29/90 ,  B01J38/12 ,  B01J2208/00132 ,  B01J2208/00256 ,  B01J2208/00991

Abstract: Apparatuses and methods for cooling catalyst are provided. In one embodiment, an apparatus for cooling catalyst includes a catalyst cooler vessel having a catalyst inlet for receiving catalyst. The apparatus includes a gas distributor lance positioned in the catalyst cooler vessel and having a gas outlet configured for injecting gas into the catalyst. The apparatus also includes a heat exchange tube positioned in the catalyst cooler vessel and having an outer surface. The heat exchange tube is configured to transfer heat from the catalyst to a heat exchange fluid. The apparatus further includes a hard surfacing material located on the outer surface of the heat exchange tube.

Abstract translation: 提供了用于冷却催化剂的设备和方法。 在一个实施方案中，用于冷却催化剂的装置包括具有用于接收催化剂的催化剂入口的催化剂冷却器容器。 该装置包括位于催化剂冷却器容器中的气体分配器喷枪，并具有被配置用于将气体注入到催化剂中的气体出口。 该设备还包括位于催化剂冷却器容器中并具有外表面的热交换管。 热交换管构造成将热量从催化剂传递到热交换流体。 该设备还包括位于热交换管的外表面上的硬表面材料。

公开(公告)号：US09149783B2

公开(公告)日：2015-10-06

申请号：US14164866

申请日：2014-01-27

Applicant: Xiamen Ju Sheng Mechanical Engineering Co., Ltd.

Inventor： I-Min Tsai ,  Kun Li ,  Xiaobin Wang ,  Yanzhen Huang ,  Kechang Li ,  Weiming Wu

IPC: B01J19/18

CPC classification number: B01J19/18 ,  B01J8/1836 ,  B01J8/20 ,  B01J8/382 ,  B01J8/386 ,  B01J8/388 ,  B01J2208/00203 ,  B01J2208/00256 ,  B01J2208/003 ,  B01J2208/00548

Abstract: A device for producing ethoxylation derivatives includes an assistant circulation loop with lower starting quantity is added on the base of the main circulation loop, and the assistant circulation pump is started first when slight chain initial dose is added with low flow rate of the ethylene oxide and high growth rate of polyreation; when the amount of reactant gets to the starting quantity of the main circulation pump, the main circulation loop is started with high flow rate of ethylene oxide. The two circulation loops cooperate with each other shorten reaction time and high yield in one batch; a pre-reaction cavity with smaller inner diameter than that of the main body of the reactor is extended from the bottom of the main body of the device, so that lower chain initial dose can start the assistant circulation pump, and then start the assistant circulation loop.

Abstract translation: 用于制备乙氧基化衍生物的装置包括在主循环回路的基底上加入起始量较低的辅助循环回路，并且当轻度链初始剂量加入低环氧乙烷的流速时，首先启动助循环泵， 多重增长率高; 当反应物的量达到主循环泵的起始量时，主循环回路以高的环氧乙烷流速开始。 两个循环回路相互配合，一次缩短反应时间，产率高; 反应器内径小于反应器主体内径的预反应空腔从设备主体的底部延伸出来，从而下链初始剂量可启动辅助循环泵，然后启动辅助循环 循环。