公开(公告)号：US09073034B2

公开(公告)日：2015-07-07

申请号：US13635642

申请日：2011-03-17

Applicant: Max M. Tirtowidjojo ,  Subrata Sen ,  Christina Zarth ,  Pramod D. Patil

Inventor： Max M. Tirtowidjojo ,  Subrata Sen ,  Christina Zarth ,  Pramod D. Patil

IPC: C07D301/03 ,  F28D7/00 ,  B01J19/24 ,  B01J8/02 ,  C07D301/10

CPC classification number: B01J19/24 ,  B01J8/0242 ,  B01J8/0264 ,  B01J8/0285 ,  B01J2208/00115 ,  B01J2208/00141 ,  B01J2208/00557 ,  B01J2208/00893 ,  B01J2208/02 ,  C07D301/08 ,  C07D301/10

Abstract: At least one method to efficiently produce alkylene oxide from partial oxidation of hydrocarbons using a high efficiency heterogeneous catalyst in a fixed bed enclosed within a reaction vessel, and a reaction vessel constructed to facilitate the same.

Abstract translation: 在封闭在反应容器内的固定床中使用高效多相催化剂，有效地从烃的部分氧化产生环氧烷烃的至少一种方法，以及为促进烯烃氧化反应构成的反应容器。

公开(公告)号：US20060257300A1

公开(公告)日：2006-11-16

申请号：US11430089

申请日：2006-05-09

Applicant: Rasmus Breivik ,  Johan Mogensen ,  Torkil Hansen

Inventor： Rasmus Breivik ,  Johan Mogensen ,  Torkil Hansen

IPC: B01J8/04 ,  B01J10/00

CPC classification number: B01J8/02 ,  B01J8/008 ,  B01J8/0257 ,  B01J8/0278 ,  B01J8/04 ,  B01J8/0453 ,  B01J8/0492 ,  B01J19/0053 ,  B01J19/24 ,  B01J19/26 ,  B01J2208/00548 ,  B01J2208/0061 ,  B01J2208/00831 ,  B01J2208/00849 ,  B01J2208/02 ,  B01J2219/00024 ,  B01J2219/00164 ,  B01J2219/00182 ,  B01J2219/00761 ,  B01J2219/182 ,  B01J2219/24

Abstract: Downflow catalytic reactor having a plurality of catalyst beds in which a mixture of gas and liquid are passed, the region in between subsequent catalyst beds being provided with a distributor system for the distribution and mixing of gas and liquid prior to contact with a subsequent catalyst bed, said region comprising: (a) gas injection line arranged below a catalyst support tray, (b) collector tray adapted to receive gas and liquid, (c) spillway collectors extending above the level of said collecting tray, (d) mixing chamber adapted to receive the gas and liquid descending from said spillway collectors, (e) impingement plate below said mixing chamber, (f) first distributor tray arranged below said impingement plate having a number of apertures throughout and a number chimneys, and (g) second distributor tray arranged below said first distributor tray for the redistribution of gas and liquid prior to contact with the subsequent catalyst bed, wherein the at least one chimney is provided with a distributor device that is able to divide the chimney chamber into at least two chambers.

公开(公告)号：US20240043757A1

公开(公告)日：2024-02-08

申请号：US18462645

申请日：2023-09-07

Applicant: Magëmä Technology LLC

Inventor： Michael Joseph Moore ,  Bertrand Ray Klussmann ,  Carter James White

IPC: C10G45/04 ,  C10G67/06 ,  C10G45/22 ,  C10G45/08 ,  C10G25/02 ,  C10G25/00 ,  B01D3/34 ,  B01J8/04 ,  C10G65/04 ,  C10L1/12 ,  C10L1/14 ,  C10L1/16 ,  B01D53/14 ,  C10G7/00 ,  C10G45/06 ,  C10L1/04 ,  C10G45/02 ,  C10G67/02 ,  B01J8/00 ,  B01J21/04 ,  B01J23/24 ,  B01J23/40 ,  B01J23/74 ,  C10G65/16 ,  B01J8/02 ,  C10G47/02 ,  C10G69/02

CPC classification number: C10G45/04 ,  C10G67/06 ,  C10G45/22 ,  C10G45/08 ,  C10G25/02 ,  C10G25/003 ,  B01D3/343 ,  B01J8/0492 ,  C10G65/04 ,  C10L1/12 ,  C10L1/14 ,  C10L1/1608 ,  B01D53/1481 ,  C10G7/00 ,  C10G45/06 ,  C10L1/04 ,  C10G45/02 ,  C10G67/02 ,  B01J8/008 ,  B01J8/0457 ,  B01J21/04 ,  B01J23/24 ,  B01J23/40 ,  B01J23/74 ,  C10G65/16 ,  B01J8/0278 ,  B01J8/0292 ,  C10G47/02 ,  C10G69/02 ,  C10G2300/302 ,  C10G2300/202 ,  C10G2300/1059 ,  B01J2208/025 ,  C10G2300/207 ,  C10G2300/30 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/70 ,  C10G2300/80 ,  C10L2270/026 ,  C10G2300/107 ,  C10G2300/1077 ,  C10G2300/1048 ,  C10G2400/06 ,  C10L2200/0263 ,  C10L2270/02 ,  C10G2300/205 ,  C10L2200/0438 ,  B01J2208/00557 ,  C10G2300/1044 ,  C10G2300/308 ,  C10G2300/4062 ,  C10G2400/04 ,  C10G2300/208 ,  B01J2208/02 ,  C10G2300/1037 ,  C10G2300/201 ,  C10G2300/206

Abstract: A multi-stage process for the production of an ISO 8217 compliant Product Heavy Marine Fuel Oil from ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a Reaction System composed of one or more reactor vessels selected from a group reactor wherein said one or more reactor vessels contains one or more reaction sections configured to promote the transformation of the Feedstock Heavy Marine Fuel Oil to the Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil has a Environmental Contaminate level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass. A process plant for conducting the process for conducting the process is disclosed that can utilize a modular reactor vessel.

公开(公告)号：US11884883B2

公开(公告)日：2024-01-30

申请号：US17942906

申请日：2022-09-12

Applicant: Magêmã Technology LLC

Inventor： Michael Joseph Moore ,  Bertrand Ray Klussmann ,  Carter James White

IPC: C10G45/04 ,  C10G67/06 ,  C10G45/22 ,  C10G45/08 ,  C10G25/02 ,  C10G25/00 ,  B01D3/34 ,  B01J8/04 ,  C10G65/04 ,  C10L1/12 ,  C10L1/14 ,  C10L1/16 ,  B01D53/14 ,  C10G7/00 ,  C10G45/06 ,  C10L1/04 ,  C10G45/02 ,  C10G67/02 ,  B01J8/00 ,  B01J21/04 ,  B01J23/24 ,  B01J23/40 ,  B01J23/74 ,  C10G65/16 ,  B01J8/02 ,  C10G47/02 ,  C10G69/02

CPC classification number: C10G45/04 ,  B01D3/343 ,  B01D53/1481 ,  B01J8/008 ,  B01J8/0278 ,  B01J8/0292 ,  B01J8/0457 ,  B01J8/0492 ,  B01J21/04 ,  B01J23/24 ,  B01J23/40 ,  B01J23/74 ,  C10G7/00 ,  C10G25/003 ,  C10G25/02 ,  C10G45/02 ,  C10G45/06 ,  C10G45/08 ,  C10G45/22 ,  C10G47/02 ,  C10G65/04 ,  C10G65/16 ,  C10G67/02 ,  C10G67/06 ,  C10G69/02 ,  C10L1/04 ,  C10L1/12 ,  C10L1/14 ,  C10L1/1608 ,  B01J2208/00557 ,  B01J2208/02 ,  B01J2208/025 ,  C10G2300/107 ,  C10G2300/1037 ,  C10G2300/1044 ,  C10G2300/1048 ,  C10G2300/1059 ,  C10G2300/1077 ,  C10G2300/201 ,  C10G2300/202 ,  C10G2300/205 ,  C10G2300/206 ,  C10G2300/207 ,  C10G2300/208 ,  C10G2300/30 ,  C10G2300/302 ,  C10G2300/308 ,  C10G2300/4012 ,  C10G2300/4018 ,  C10G2300/4062 ,  C10G2300/70 ,  C10G2300/80 ,  C10G2400/04 ,  C10G2400/06 ,  C10L2200/0263 ,  C10L2200/0438 ,  C10L2270/02 ,  C10L2270/026 ,  C10L1/1608 ,  C10L2200/0438

Abstract: A multi-stage process for the production of an ISO 8217 compliant Product Heavy Marine Fuel Oil from ISO 8217 compliant Feedstock Heavy Marine Fuel Oil involving a Reaction System composed of one or more reactor vessels selected from a group reactor wherein said one or more reactor vessels contains one or more reaction sections configured to promote the transformation of the Feedstock Heavy Marine Fuel Oil to the Product Heavy Marine Fuel Oil. The Product Heavy Marine Fuel Oil has a Environmental Contaminate level has a maximum sulfur content (ISO 14596 or ISO 8754) between the range of 0.05 mass % to 1.0 mass. A process plant for conducting the process for conducting the process is disclosed that can utilize a modular reactor vessel.

公开(公告)号：US09932531B2

公开(公告)日：2018-04-03

申请号：US15494758

申请日：2017-04-24

Applicant: Battelle Memorial Institute

Inventor： Michael A. Lilga ,  Richard T. Hallen ,  Karl O. Albrecht ,  Alan R. Cooper ,  John G. Frye ,  Karthikeyan Kallupalayam Ramasamy

IPC: C07C2/24 ,  C10G69/12 ,  C10G50/00 ,  B01J8/04 ,  B01J23/755 ,  B01J29/76

CPC classification number: C07C2/24 ,  B01J8/04 ,  B01J21/04 ,  B01J21/12 ,  B01J23/42 ,  B01J23/755 ,  B01J29/072 ,  B01J29/084 ,  B01J29/40 ,  B01J29/7007 ,  B01J29/7615 ,  B01J29/90 ,  B01J35/0006 ,  B01J37/0201 ,  B01J38/02 ,  B01J2208/02 ,  B01J2208/027 ,  C07C1/20 ,  C07C1/24 ,  C07C2/12 ,  C07C5/03 ,  C07C2521/12 ,  C07C2523/755 ,  C07C2529/06 ,  C07C2529/072 ,  C07C2529/14 ,  C07C2529/24 ,  C07C2529/46 ,  C07C2529/68 ,  C07C2529/70 ,  C07C2529/76 ,  C07C2529/85 ,  C10G3/00 ,  C10G45/00 ,  C10G50/00 ,  C10G69/126 ,  C10G2300/1092 ,  C10G2300/4081 ,  C10G2400/02 ,  C10G2400/04 ,  C10G2400/08 ,  Y02P20/52 ,  Y02P20/584 ,  Y02P30/42 ,  C07C11/04 ,  C07C11/02

Abstract: Systems, processes, and catalysts are disclosed for obtaining fuel and fuel blends containing selected ratios of open-chain and closed-chain fuel-range hydrocarbons suitable for production of alternate fuels including gasolines, jet fuels, and diesel fuels. Fuel-range hydrocarbons may be derived from ethylene-containing feedstocks and ethanol-containing feedstocks.

公开(公告)号：US09896395B2

公开(公告)日：2018-02-20

申请号：US15288331

申请日：2016-10-07

Applicant: ExxonMobil Chemical Patents Inc.

Inventor： Larry L. Iaccino ,  Kevin C. P. Leung

IPC: C07C5/327 ,  C07C5/32 ,  C07C5/333 ,  C07C5/373 ,  B01J8/02 ,  B01J29/44 ,  C07C2/76 ,  C07C5/03 ,  C07C7/04 ,  C07C4/22 ,  C07C2/40 ,  C07C2/52 ,  C01B3/26

CPC classification number: C07C5/373 ,  B01J8/02 ,  B01J8/0278 ,  B01J29/40 ,  B01J29/44 ,  B01J29/7038 ,  B01J2208/02 ,  B01J2229/186 ,  B01J2229/40 ,  C01B3/26 ,  C01B2203/0405 ,  C01B2203/043 ,  C01B2203/046 ,  C01B2203/1058 ,  C01B2203/1064 ,  C01B2203/107 ,  C07C2/403 ,  C07C2/52 ,  C07C2/76 ,  C07C4/22 ,  C07C5/03 ,  C07C5/333 ,  C07C7/04 ,  C07C2101/10 ,  C07C2103/68 ,  C07C2529/44 ,  C07C2601/10 ,  C07C2603/68 ,  Y02P20/582 ,  C07C13/15 ,  C07C13/61

Abstract: Processes and systems for making cyclopentadiene and/or dicyclopentadiene include converting acyclic C5 hydrocarbon(s) into CPD in a first reactor to obtain a product mixture, washing the product mixture with a wash oil, separating the washed product mixture in a separation sub-system such as compression train to obtain a C5-rich fraction comprising CPD, dimerizing the C5-rich fraction in a dimerization reactor to obtain a product effluent, followed by separating the product effluent to obtain a DCPD-rich fraction. Wash oil can be recovered and recycled. Multiple-stage of dimerization and separation steps can be used to obtain multiple DCPD-rich fractions of various purity and quantity. C5-rich fractions from various stages of the process may be recycled to the first reactor, or converted into mogas components after selective hydrogenation. C5-rich fractions and mogas components may be optionally separated to produce value-adding chemicals.

公开(公告)号：US20180022667A1

公开(公告)日：2018-01-25

申请号：US15702174

申请日：2017-09-12

Applicant: ExxonMobil Chemical Patents Inc.

Inventor： John S. Buchanan ,  Paul F. Keusenkothen ,  David W. Maher ,  Jaime A. Valencia

IPC: C07C2/76 ,  C07C1/12 ,  B01J37/16 ,  B01J29/78 ,  B01J37/08 ,  B01J23/46 ,  B01J23/58 ,  B01J23/63 ,  B01J23/652 ,  B01J23/656 ,  B01J23/755 ,  B01J23/78 ,  B01J29/70 ,  B01J29/69 ,  B01J29/65 ,  B01J29/48 ,  B01J29/40 ,  B01J29/06 ,  B01J23/889 ,  B01J23/86 ,  B01J23/83 ,  C07C9/04 ,  C07C15/04 ,  C07C15/06 ,  C07C15/08 ,  B01J8/02

CPC classification number: C07C2/76 ,  B01J8/0278 ,  B01J23/462 ,  B01J23/464 ,  B01J23/58 ,  B01J23/63 ,  B01J23/6522 ,  B01J23/6562 ,  B01J23/755 ,  B01J23/78 ,  B01J23/83 ,  B01J23/866 ,  B01J23/8892 ,  B01J29/06 ,  B01J29/405 ,  B01J29/48 ,  B01J29/655 ,  B01J29/69 ,  B01J29/708 ,  B01J29/7084 ,  B01J29/7088 ,  B01J29/7092 ,  B01J29/7096 ,  B01J29/7269 ,  B01J29/7861 ,  B01J29/7869 ,  B01J29/7876 ,  B01J29/7884 ,  B01J29/7892 ,  B01J35/0006 ,  B01J37/08 ,  B01J37/16 ,  B01J2208/02 ,  B01J2229/12 ,  B01J2229/18 ,  B01J2229/37 ,  C07C1/12 ,  C07C9/04 ,  C07C15/04 ,  C07C2529/06 ,  Y02P20/52 ,  C07C15/06 ,  C07C15/08

Abstract: The invention relates to converting non-aromatic hydrocarbon in the presence of CO2 to produce aromatic hydrocarbon. CO2 methanation using molecular hydrogen produced during the aromatization increases aromatic hydrocarbon yield. The invention also relates to equipment and materials useful in such upgrading, to processes for carrying out such upgrading, and to the use of such processes for, e.g., natural gas upgrading.

公开(公告)号：US20170369311A1

公开(公告)日：2017-12-28

申请号：US15542704

申请日：2016-02-04

Applicant: SABIC Global Technologies B.V.

Inventor： Aghaddin MAMEDOV

IPC: C01B3/40 ,  B01J23/889 ,  B01J8/02 ,  B01J35/02 ,  B01J38/12 ,  B01J23/00 ,  B01J23/94

CPC classification number: C01B3/40 ,  B01J8/003 ,  B01J8/02 ,  B01J8/1863 ,  B01J8/26 ,  B01J23/002 ,  B01J23/34 ,  B01J23/755 ,  B01J23/78 ,  B01J23/83 ,  B01J23/8892 ,  B01J23/892 ,  B01J23/94 ,  B01J35/023 ,  B01J38/12 ,  B01J2208/02 ,  B01J2523/00 ,  C01B2203/0238 ,  C01B2203/1041 ,  C01B2203/1058 ,  C01B2203/1082 ,  C01B2203/1241 ,  Y02P20/52 ,  Y02P20/584

Abstract: Methods and systems for converting methane to syngas are provided. Certain exemplary methods and systems involve reacting methane and carbon dioxide with a nickel oxide catalyst in a reaction chamber, thereby providing syngas and a reduced nickel species. The reduced nickel species can be regenerated by oxidation with air in a regeneration chamber, thereby generating a regenerated nickel oxide and heat. The regenerated nickel oxide and heat can be returned to the reaction chamber to drive the syngas reaction.

公开(公告)号：US09835117B2

公开(公告)日：2017-12-05

申请号：US15035390

申请日：2014-11-19

Applicant: HONDA MOTOR CO., LTD.

Inventor： Kohtaro Hashimoto

IPC: F02M27/02 ,  B01J8/02 ,  C10L1/06 ,  B01J31/02 ,  B01J31/22 ,  B01J8/00 ,  C10L1/182 ,  C10L10/10

CPC classification number: F02M27/02 ,  B01J8/001 ,  B01J8/02 ,  B01J8/0221 ,  B01J8/0278 ,  B01J8/0285 ,  B01J31/0247 ,  B01J31/2239 ,  B01J2208/00212 ,  B01J2208/00548 ,  B01J2208/00628 ,  B01J2208/02 ,  B01J2231/70 ,  B01J2531/72 ,  B01J2531/845 ,  C10G2300/104 ,  C10G2300/1044 ,  C10G2300/305 ,  C10G2300/4037 ,  C10G2400/02 ,  C10L1/06 ,  C10L1/182 ,  C10L10/10 ,  C10L2200/0423 ,  C10L2270/023 ,  C10L2290/06 ,  C10L2290/24 ,  C10L2290/58

Abstract: Provided is a fuel reforming system that can convert gasoline into alcohol in a vehicle. Provided is a fuel reforming system (1) equipped with a reformer (15) having a reforming catalyst (152) that uses air to reform gasoline to produce alcohol, a mixer (14) which mixes gasoline and air and supplies the mixture to the reformer (15), and a condenser (16) which separates the gas produced in the reformer (15) into a gas phase and a condensed phase of which reformed fuel is the primary constituent; wherein the fuel reforming system (1) is characterized in that the reforming catalyst (152) is configured including a main catalyst for extracting hydrogen atoms from the hydrocarbons in the gasoline to produce alkyl radicals, and a catalytic promoter for reducing alkyl hydroperoxides produced from the alkyl radicals to produce alcohol.

公开(公告)号：US09738519B2

公开(公告)日：2017-08-22

申请号：US14772746

申请日：2014-03-11

Applicant: SUMITOMO PRECISION PRODUCTS CO., LTD.

Inventor： Makoto Hirakawa ,  Shigeru Mizukawa

IPC: C01B3/38 ,  B01J8/02 ,  B01J8/04 ,  H01M8/0612 ,  H01M8/124

CPC classification number: C01B3/38 ,  B01J8/0465 ,  B01J8/0496 ,  B01J2208/00504 ,  B01J2208/0053 ,  B01J2208/00849 ,  B01J2208/02 ,  C01B3/384 ,  C01B2203/0227 ,  C01B2203/0233 ,  C01B2203/066 ,  C01B2203/0816 ,  C01B2203/0822 ,  C01B2203/0827 ,  C01B2203/1288 ,  C01B2203/1294 ,  H01M8/0618 ,  H01M2008/1293 ,  Y02P20/128

Abstract: A fuel reformer 20 producing a reformed gas by catalysis by using a fuel gas includes a combustion chamber 24, a combustion nozzle 30, an exhausting pipe 15, a gas distribution gap 25, an outer reforming portion 43, a fuel gas introduction pipe 10, and a reformed gas outlet pipe 11. The combustion nozzle 30 is located in the combustion chamber 24. A columnar protruding portion 40 is provided in the combustion chamber 24.