公开(公告)号：US20170204035A1

公开(公告)日：2017-07-20

申请号：US15324666

申请日：2015-08-03

Applicant: ExxonMobil Chemical Patents Inc.

Inventor： Christopher L. BECKER ,  Jason D. DAVIS ,  Jihad M. DAKKA ,  Kirk C. NADLER

IPC: C07C45/00 ,  B01J19/24 ,  B01J8/04 ,  C07C45/82 ,  B01J8/06

CPC classification number: C07C45/006 ,  B01J8/0492 ,  B01J8/065 ,  B01J8/067 ,  B01J19/242 ,  B01J19/2425 ,  B01J2208/065 ,  B01J2219/24 ,  C07C37/74 ,  C07C45/82 ,  C07C2101/14 ,  C07C2601/14 ,  C07C49/403 ,  C07C39/04

Abstract: Disclosed are processes and systems for making cyclohexanone from a mixture comprising phenol, cyclohexanone, and cyclohexylbenzene, comprising a step of or a device for subjecting at least a portion of the mixture to hydrogenation and a step of or a device for distilling a phenol/cyclohexanone/cyclohexylbenzene mixture to obtain an effluent rich in cyclohexanone.

公开(公告)号：US20170121271A1

公开(公告)日：2017-05-04

申请号：US15342686

申请日：2016-11-03

Applicant: National University of Singapore

Inventor： Saif A. Khan ,  Swee Kun Yap

IPC: C07C209/36 ,  B01J8/04 ,  B01J19/24 ,  B01J8/06

CPC classification number: C07C209/36 ,  B01J8/0492 ,  B01J8/065 ,  B01J19/0046 ,  B01J19/0093 ,  B01J19/2425 ,  B01J2208/06 ,  B01J2219/00286 ,  B01J2219/00306 ,  B01J2219/00353 ,  B01J2219/00418 ,  B01J2219/00587 ,  B01J2219/0072 ,  B01J2219/00747 ,  B01J2219/00783 ,  B01J2219/00792 ,  B01J2219/00813 ,  B01J2219/00833 ,  B01J2219/00835 ,  B01J2219/0086 ,  B01J2219/00869 ,  B01J2219/00871 ,  B01J2219/00891 ,  B01J2219/009 ,  B01J2219/00997 ,  B01J2219/0254 ,  B01J2219/0277 ,  B01J2219/0295 ,  C07C211/46

Abstract: A one-to-many parallelized millireactor system capable of high throughput production in millireactors. Also disclosed is a method for carrying out multi-phase reactions.

公开(公告)号：US09627700B2

公开(公告)日：2017-04-18

申请号：US14533803

申请日：2014-11-05

Applicant: Watt Fuel Cell Corp.

Inventor： Caine M. Finnerty ,  Paul DeWald

IPC: B01J7/00 ,  C01B3/36 ,  H01M8/0612 ,  B01J12/00 ,  B01J19/24 ,  B01J4/00 ,  C01B3/32 ,  C01B3/38 ,  H01M8/04302 ,  H01M8/04007 ,  H01M8/0432 ,  H01M8/0438 ,  H01M8/04791

CPC classification number: H01M8/0631 ,  B01J4/001 ,  B01J4/002 ,  B01J4/005 ,  B01J12/007 ,  B01J19/2425 ,  B01J2219/00006 ,  B01J2219/00058 ,  B01J2219/0006 ,  B01J2219/00069 ,  B01J2219/00135 ,  B01J2219/00159 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00234 ,  B01J2219/00238 ,  C01B3/323 ,  C01B3/386 ,  C01B2203/0261 ,  C01B2203/0283 ,  C01B2203/0405 ,  C01B2203/044 ,  C01B2203/047 ,  C01B2203/066 ,  C01B2203/1633 ,  C01B2203/169 ,  H01M8/04037 ,  H01M8/04302 ,  H01M8/04328 ,  H01M8/04335 ,  H01M8/04373 ,  H01M8/04388 ,  H01M8/04395 ,  H01M8/04798 ,  H01M8/0618

Abstract: Integrated liquid fuel catalytic partial oxidation (CPOX) reformer and fuel cell systems can include a plurality or an array of spaced-apart CPOX reactor units, each reactor unit including an elongate tube having a gas-permeable wall with internal and external surfaces, the wall enclosing an open gaseous flow passageway with at least a portion of the wall having CPOX catalyst disposed therein and/or comprising its structure. The catalyst-containing wall structure and open gaseous flow passageway enclosed thereby define a gaseous phase CPOX reaction zone, the catalyst-containing wall section being gas-permeable to allow gaseous CPOX reaction mixture to diffuse therein and hydrogen rich product reformate to diffuse therefrom. The liquid fuel CPOX reformer also can include a vaporizer, one or more igniters, and a source of liquid reformable fuel. The hydrogen-rich reformate can be converted to electricity within a fuel cell unit integrated with the liquid fuel CPOX reactor unit.

公开(公告)号：US20170022428A1

公开(公告)日：2017-01-26

申请号：US15289301

申请日：2016-10-10

Applicant: General Electric Company

Inventor： Shizhong Wang ,  Wenqing Peng ,  Qijia Fu ,  Zhigang Deng ,  Zhaoping Wu ,  Chuan Lin ,  Yanfei Gu ,  Xiao Zhang ,  Lawrence Bernard Kool

IPC: C10G9/20 ,  C10G9/36 ,  C04B35/622 ,  B01J19/00 ,  B01J19/02 ,  C04B35/505 ,  C10G9/16 ,  C07C4/04

CPC classification number: C10G9/203 ,  B01J19/0026 ,  B01J19/02 ,  B01J19/2425 ,  B01J23/002 ,  B01J2219/00245 ,  B01J2219/0218 ,  B01J2219/0263 ,  B01J2219/0286 ,  C04B35/505 ,  C04B35/62222 ,  C04B2235/3215 ,  C04B2235/3225 ,  C04B2235/3229 ,  C04B2235/3248 ,  C04B2235/79 ,  C07C4/04 ,  C10G9/16 ,  C10G9/18 ,  C10G9/36 ,  C10G2300/1033 ,  C10G2300/1044 ,  C10G2300/1059 ,  C10G2300/107 ,  C10G2300/1074 ,  C10G2300/1077 ,  C10G2300/1081 ,  C10G2300/807 ,  C10G2400/20

Abstract: A method for cracking hydrocarbon, comprises: providing steam and hydrocarbon; and feeding steam and hydrocarbon into a reactor accessible to hydrocarbon and comprising a perovskite material of formula AaBbCcDdO3-δ, wherein 0

Abstract translation: 一种裂解烃的方法，包括：提供蒸汽和烃; 并将蒸气和烃进料到可接近烃的反应器中，并且包含式AaBbCcDdO3-δ的钙钛矿材料，其中0

公开(公告)号：US09504984B2

公开(公告)日：2016-11-29

申请号：US14643726

申请日：2015-03-10

Applicant: P. Scott Northrop

Inventor： P. Scott Northrop

IPC: C01B17/04 ,  C10L3/10 ,  B01J19/00 ,  B01J19/24

CPC classification number: B01J19/2425 ,  B01J2219/00006 ,  B01J2219/00085 ,  C01B17/0408 ,  C01B17/0417 ,  C01B17/0447

Abstract: Techniques for generating elemental sulfur are provided herein. The disclosed methods may include a gas processing system including a processed feed gas. The methods may include a distillation column configured to receive the processed feed gas and to generate a high-pressure acid gas stream. The methods may include a reactor configured to partially combust the high-pressure acid gas stream to generate a limiting reactant. The methods may include a plurality of reactors configured with a shell side and a plurality of reaction tubes, where a reaction between the high-pressure acid gas stream and the limiting reactant produces a partially-reacted high-pressure acid gas containing elemental sulfur. The methods may include a plurality of condensers configured to condense the elemental sulfur. The methods may include a plurality of separators configured to separate out the partially-reacted high-pressure acid gas stream to recover elemental sulfur.

Abstract translation: 本文提供了产生元素硫的技术。 所公开的方法可以包括包括经处理的进料气体的气体处理系统。 所述方法可以包括配置成接收经处理的进料气体并产生高压酸性气流的蒸馏塔。 该方法可以包括反应器，其构造成部分地燃烧高压酸性气体流以产生限制性反应物。 该方法可以包括配置有壳侧和多个反应管的多个反应器，其中高压酸性气体流和限制反应物之间的反应产生含有元素硫的部分反应的高压酸性气体。 所述方法可以包括被配置为冷凝元素硫的多个冷凝器。 该方法可以包括多个分离器，其构造成分离部分反应的高压酸性气流以回收元素硫。

公开(公告)号：US09486775B2

公开(公告)日：2016-11-08

申请号：US14726981

申请日：2015-06-01

Applicant: NOVA Chemicals (International) S.A.

Inventor： Eric Clavelle ,  Edgar Yajure ,  Leslie Wilfred Benum ,  Edward Christopher Foy ,  David Eisenhawer

IPC: B01J19/24 ,  B01J19/02 ,  F16L43/00 ,  C10G9/16 ,  C10G9/20 ,  C10G9/36 ,  G01L7/00 ,  G01N17/00

CPC classification number: C10G9/203 ,  B01J19/02 ,  B01J19/2425 ,  B01J19/243 ,  B01J2219/00033 ,  B01J2219/00164 ,  B01J2219/00243 ,  B01J2219/00247 ,  B01J2219/00254 ,  B01J2219/0277 ,  B01J2219/194 ,  B01J2219/1943 ,  B01J2219/1947 ,  C07C4/04 ,  C10G9/16 ,  C10G9/36 ,  C10G2300/1081 ,  C10G2300/4075 ,  C10G2400/20 ,  F16L43/002 ,  G01L7/00 ,  G01N17/00 ,  G01N17/008 ,  C08F10/00 ,  C08F2/01

Abstract: Some embodiments of the present invention provide components for a serpentine fluid reactor which is optimized for one or more objective functions of interest such as pressure drop, erosion rate, fouling, coke deposition and operating costs. The components are designed by computer modeling the components individually and collectively in which the cross section of flow path is substantially circular under industrial conditions to validate the model design and its operation. Then iteratively the component designs are deformed and the operation of the deformed part(s) is modeled and compared to values obtained with other deformed models until the value of the objective function is optimized (e.g. at an extreme) or the change in the objective function is approaching zero.

公开(公告)号：US20160264414A1

公开(公告)日：2016-09-15

申请号：US15033802

申请日：2014-11-06

Applicant: Watt Fuel Cell Corp.

Inventor： Caine M. Finnerty ,  Paul DeWald

IPC: C01B3/36 ,  H01M8/22 ,  H01M8/0612 ,  B01J19/00 ,  B01J19/24

CPC classification number: C01B3/36 ,  B01J4/001 ,  B01J4/002 ,  B01J4/005 ,  B01J12/007 ,  B01J19/0013 ,  B01J19/24 ,  B01J19/2425 ,  B01J2219/00006 ,  B01J2219/00058 ,  B01J2219/0006 ,  B01J2219/00069 ,  B01J2219/00074 ,  B01J2219/00103 ,  B01J2219/00132 ,  B01J2219/00135 ,  B01J2219/00159 ,  B01J2219/002 ,  B01J2219/00213 ,  B01J2219/00234 ,  B01J2219/00238 ,  B01J2219/24 ,  C01B3/326 ,  C01B3/386 ,  C01B2203/0205 ,  C01B2203/0261 ,  C01B2203/041 ,  C01B2203/066 ,  C01B2203/0833 ,  C01B2203/0838 ,  C01B2203/085 ,  C01B2203/1005 ,  C01B2203/1276 ,  C01B2203/1282 ,  C01B2203/1288 ,  H01M8/0618 ,  H01M8/0631 ,  H01M8/22

Abstract: A liquid fuel reformer (400) includes a fuel vaporizer (415) which utilizes heat from an upstream source of heat, specifically, an electric heater (406), operable in the start-up mode of the reformer (400), and therefore independent of the reforming reaction zone of the reformer, to vaporize fuel in a downstream vaporization zone.

Abstract translation: 液体燃料重整器（400）包括燃料蒸发器（415），该燃料蒸发器（415）利用来自上游热源的热量，特别是可在重整器（400）的起动模式下操作的电加热器（406），因此独立 的重整器的重整反应区，以使下游蒸发区的燃料蒸发。

公开(公告)号：US20160137940A1

公开(公告)日：2016-05-19

申请号：US14976307

申请日：2015-12-21

Applicant: Mark J. Khinkis ,  Aleksandr P. Kozlov

Inventor： Mark J. Khinkis ,  Aleksandr P. Kozlov

IPC: C10L3/00 ,  C01B3/34 ,  B01J19/24

CPC classification number: C10L3/00 ,  B01J12/007 ,  B01J19/2425 ,  B01J19/248 ,  B01J19/249 ,  B01J2219/00081 ,  B01J2219/00085 ,  B01J2219/00087 ,  B01J2219/00099 ,  B01J2219/00157 ,  B01J2219/00159 ,  B01J2219/2453 ,  B01J2219/2458 ,  B01J2219/2462 ,  B01J2219/2479 ,  B01J2219/2482 ,  B01J2219/2486 ,  C01B3/34 ,  C01B2203/0216 ,  C01B2203/0222 ,  C01B2203/0811 ,  C01B2203/1235 ,  C01B2203/1241 ,  C01B2203/148

Abstract: A radiant, non-catalytic recuperative reformer has a flue gas flow path for conducting hot exhaust gas from a thermal process and a reforming mixture flow path for conducting a reforming mixture. At least a portion of the reforming mixture flow path is positioned adjacent to the flue gas flow path to permit heat transfer from the hot exhaust gas to the reforming mixture. The reforming mixture flow path contains substantially no material commonly used as a catalyst for reforming hydrocarbon fuel (e.g., nickel oxide, platinum group elements or rhenium), but instead the reforming mixture is reformed into a higher calorific fuel via reactions due to the heat transfer and residence time. In a preferred embodiment, a portion of the reforming mixture flow path is positioned outside of flue gas flow path for a relatively large residence time.

Abstract translation: 辐射的非催化还原重整器具有用于从热处理和用于引导重整混合物的重整混合物流动路径传导热废气的烟道气流动路径。 重整混合物流动路径的至少一部分定位成与废气流动路径相邻，以允许从热废气到重整混合物的热传递。 重整混合物流动路径基本上不含有用于重整烃燃料（例如，氧化镍，铂族元素或铼）的催化剂的材料，而是通过由于热传递的反应将重整混合​​物重整成更高热量的燃料 和停留时间。 在一个优选实施例中，重整混合物流动路径的一部分位于烟气流动路径的外部，从而具有较大的停留时间。

公开(公告)号：US20160122670A1

公开(公告)日：2016-05-05

申请号：US14896993

申请日：2014-06-10

Applicant: UNIVERSITY OF FLORIDA RESEARCH FOUNDATION, INC.

Inventor： James F. Klausner ,  Joerg Petrasch ,  Nicholas AuYeung ,  Ayyoub Mehdizadeh Momen ,  Rishi Mishra ,  Jinchao Lu ,  David Worthington Hahn ,  Nikhil Sehgal ,  Renwei Mei ,  Benjamin Greek

IPC: C10J3/48 ,  C10J3/72 ,  C10J3/46

CPC classification number: C10J3/48 ,  B01J8/0257 ,  B01J8/0278 ,  B01J8/065 ,  B01J8/067 ,  B01J19/02 ,  B01J19/127 ,  B01J19/2425 ,  B01J2208/00398 ,  B01J2208/00451 ,  B01J2219/0218 ,  B01J2219/0263 ,  C10J3/46 ,  C10J3/721 ,  C10J2300/0969 ,  C10J2300/0976 ,  C10J2300/1292 ,  F24S20/20 ,  Y02E10/41

Abstract: Disclosed herein is a solar reactor comprising a reactor member; an aperture for receiving solar radiation, the aperture being disposed in a plane on a wall of the reactor member, where the plane is oriented at any angle other than parallel relative to the centerline of the reactor member; a plurality of absorber tubes, wherein the absorber tubes are oriented such that their respective centerlines are at an angle other than 90° relative to the centerline of the reactor member; and wherein the aperture has a hydraulic diameter that is from 0.2 to 4 times a hydraulic diameter of at least one absorber tube in the plurality of absorber tubes; and a reactive material, the reactive material being disposed in the plurality of absorber tubes.

Abstract translation: 本文公开了一种包括反应器构件的太阳能反应器; 用于接收太阳辐射的孔，所述孔布置在所述反应器构件的壁上的平面中，其中所述平面相对于所述反应器构件的中心线平行于任何角度; 多个吸收管，其中所述吸收管被定向成使得它们各自的中心线相对于所述反应器构件的中心线成90°以外的角度; 并且其中所述孔的液压直径是所述多个吸收管中的至少一个吸收管的水力直径的0.2至4倍; 和反应性材料，反应性材料设置在多个吸收管中。

公开(公告)号：US20160097002A1

公开(公告)日：2016-04-07

申请号：US14874755

申请日：2015-10-05

Applicant: Lummus Technology Inc.

Inventor： Kandasamy Meenakshi Sundaram

IPC: C10G9/14 ,  C10G9/20 ,  C10G69/06

CPC classification number: C10G9/36 ,  B01J6/008 ,  B01J19/2425 ,  B01J2219/00157 ,  B01J2219/00159

Abstract: Systems and processes for efficiently cracking of hydrocarbon mixtures, such as mixtures including compounds having a normal boiling temperature of greater than 450° C., 500° C., or even greater than 550° C., such as whole crudes for example, are disclosed.

Abstract translation: 烃混合物的有效裂解的系统和方法，例如包括正常沸腾温度大于450℃，500℃，甚至大于550℃的化合物（例如整个原油）的混合物是 披露