公开(公告)号：US20240335822A1

公开(公告)日：2024-10-10

申请号：US18575675

申请日：2022-07-01

Applicant: JGC CATALYSTS AND CHEMICALS LTD.

Inventor： Hirosato YAMAZAKI

IPC: B01J25/00 ,  B01J37/02 ,  C07C209/48

CPC classification number: B01J25/00 ,  B01J37/0201 ,  C07C209/48

Abstract: A sponge cobalt catalyst composition contains water, an oxoacid, and a sponge cobalt catalyst. The oxoacid contains W or Mo, and part or all of the oxoacid is adsorbed to the sponge cobalt catalyst.

公开(公告)号：US20180169632A1

公开(公告)日：2018-06-21

申请号：US15899988

申请日：2018-02-20

Applicant: China Petroleum & Chemical Corporation ,  Beijing Research Institute of Chemical Industry, China Petroleum & Chemical Corporation

Inventor： Wei Dai ,  Haibin Jiang ,  Shuliang Lu ,  Xiaohong Zhang ,  Guoqing Wang ,  Jinliang Qiao ,  Hui Peng

IPC: B01J25/02 ,  C07C1/04 ,  B01J31/28 ,  B01J31/34 ,  C07C29/141 ,  C07C1/06 ,  B01J25/00 ,  B01J37/00

CPC classification number: B01J25/02 ,  B01J25/00 ,  B01J31/28 ,  B01J31/34 ,  B01J37/0009 ,  B01J2231/643 ,  C07B35/02 ,  C07B35/04 ,  C07B35/06 ,  C07C1/0435 ,  C07C1/066 ,  C07C29/141 ,  C07C2525/00 ,  C07C2525/02

Abstract: A supported catalyst and preparation method thereof, the catalyst comprising an organic polymer material carrier and Raney alloy particles supported on the organic polymer material carrier, wherein substantially all of the Raney alloy particles are partially embedded in the organic polymer material carrier. The catalyst can be used in hydrogenation, dehydrogenation, amination, dehalogenation or desulfuration reactions.

公开(公告)号：US20170362163A1

公开(公告)日：2017-12-21

申请号：US15541733

申请日：2016-01-26

Applicant: Evonik Degussa GmbH

Inventor： Stephan Kohlstruk ,  Anne Rittsteiger ,  Alexander Martin Rüfer ,  Norbert Schlüter ,  Sven Schneider ,  Sabrina Sowka ,  Guido Streukens ,  Stefan Röder ,  Monika Berweiler

IPC: C07C209/52 ,  B01J35/02 ,  B01J25/02 ,  C07C209/48 ,  B01J37/00 ,  C07C2601/14

CPC classification number: C07C209/52 ,  B01J25/00 ,  B01J25/02 ,  B01J35/023 ,  B01J35/026 ,  B01J37/0018 ,  B01J37/0063 ,  B01J37/0081 ,  B01J2523/00 ,  C07C209/48 ,  C07C2601/14 ,  C07C211/36 ,  B01J2523/31 ,  B01J2523/67 ,  B01J2523/845 ,  B01J2523/847

Abstract: Process for preparing isophoronediamine, characterized in thatA) isophoronenitrile is subjected directly in one stage to aminating hydrogenation to give isophoronediamine in the presence of ammonia, hydrogen, a hydrogenation catalyst and possibly further additions, and in the presence or absence of organic solvents; orB) isophoronenitrile is first converted fully or partly in at least two or more than two stages to isophoronenitrile imine, and this isophoronenitrile imine is subjected to aminating hydrogenation to give isophoronediamine as a pure substance or in a mixture with other components and/or isophoronenitrile, in the presence of at least ammonia, hydrogen and a catalyst.

公开(公告)号：US20170044123A1

公开(公告)日：2017-02-16

申请号：US15302702

申请日：2014-04-10

Applicant: Archer Daniels Midland Company

Inventor： Kenneth Stensrud ,  Chi-Cheng Ma

IPC: C07D307/12 ,  A23L27/30 ,  C07G3/00 ,  B01J25/00 ,  C07C29/60 ,  C07C29/132

CPC classification number: C07D307/12 ,  A23L27/34 ,  A23V2002/00 ,  B01J23/72 ,  B01J25/00 ,  C07C29/132 ,  C07C29/60 ,  C07D307/20 ,  C07D493/04 ,  C07G3/00 ,  C07C31/24 ,  C07C31/22 ,  C07C31/26

Abstract: Disclosed herein are methods for synthesizing 1,2,5,6-hexanetetrol (HTO), 1,6 hexanediol (HDO) and other reduced polyols from C5 and C6 sugar alcohols or R glycosides. The methods include contacting the sugar alcohol or R-glycoside with a copper catalyst, most desirably a Raney copper catalyst with hydrogen for a time, temperature and pressure sufficient to form reduced polyols having 2 to 3 fewer hydoxy groups than the starting material. When the starting compound is a C6 sugar alcohol such as sorbitol or R-glycoside of a C6 sugar such as methyl glucoside, the predominant product is HTO. The same catalyst can be used to further reduce the HTO to HDO.

Abstract translation: 本文公开了用于从C5和C6糖醇或R糖苷合成1,2,5,6-己烷乙醇（HTO），1,6-己二醇（HDO）和其它还原的多元醇的方法。 所述方法包括使糖醇或R-糖苷与铜催化剂接触，最理想的是具有氢气的拉尼铜催化剂一段时间，足以形成比起始原料少2-3个羟基的还原多元醇的温度和压力。 当起始化合物是C6糖醇如C6糖如山梨糖醇或R-糖苷如甲基葡糖苷时，主要产物是HTO。 可以使用相同的催化剂进一步将HTO还原成HDO。

公开(公告)号：US20170029393A1

公开(公告)日：2017-02-02

申请号：US15302709

申请日：2014-04-10

Applicant: Archer Daniels Midland Company

Inventor： Kenneth Stensrud ,  Chi-Cheng Ma ,  Kevin Martin

IPC: C07D307/12

CPC classification number: C07D307/12 ,  B01J23/462 ,  B01J23/72 ,  B01J25/00 ,  B01J27/053 ,  B01J27/16 ,  B01J27/20 ,  C07C29/132 ,  C07C29/60 ,  C07G3/00 ,  C07C31/26 ,  C07C31/22 ,  C07C31/24

Abstract: Disclosed herein are methods for synthesizing 1,2,5,6-hexanetetrol (HTO), 1,6 hexanediol (HDO) and other reduced polyols from C5 and C6 sugar alcohols or R glycosides. The methods include contacting the sugar alcohol or R-glycoside with a copper catalyst, most desirably a Raney copper catalyst with hydrogen for a time, temperature and pressure sufficient to form reduced polyols having 2 to 3 fewer hydoxy groups than the starting material. When the starting compound is a C6 sugar alcohol such as sorbitol or R-glycoside of a C6 sugar such as methyl glucoside, the predominant product is HTO. The same catalyst can be used to further reduce the HTO to HDO.

公开(公告)号：US08945219B1

公开(公告)日：2015-02-03

申请号：US12151841

申请日：2008-05-08

Applicant: Maximilian A. Biberger

Inventor： Maximilian A. Biberger

IPC: A61F2/28 ,  A61F2/54

CPC classification number: F28C3/16 ,  A61L2/18 ,  B01J2/16 ,  B01J19/0013 ,  B01J19/088 ,  B01J25/00 ,  B01J25/02 ,  B01J35/04 ,  B01J37/0018 ,  B01J37/0027 ,  B01J37/06 ,  B01J37/349 ,  B01J2219/0805 ,  B01J2219/0879 ,  B01J2219/0894 ,  B22F9/12 ,  B22F2203/13 ,  B22F2999/00 ,  F28D7/024 ,  F28D7/08 ,  F28D15/00 ,  F28F27/00 ,  Y10S623/92 ,  Y10S623/923 ,  Y10T137/0391 ,  Y10T137/2076 ,  Y10T156/15 ,  B22F2202/13

Abstract: A method of introducing an additive to a biological material using a supercritical fluid is disclosed. The method comprises placing the biological material in a processing chamber, adding an additive to the supercritical fluid to form a supercritical fluid-additive mixture, adding the supercritical fluid-additive mixture to the processing chamber, and pulsing the mixture in the processing chamber. A processing system for introducing an additive to a biological material using a supercritical fluid in accordance with the present invention comprises a processing chamber for housing the biological material, a vat for storing a processing fluid, a pump, a heating element, an inlet port, and a flow path.

Abstract translation: 公开了一种使用超临界流体将添加剂引入生物材料的方法。 该方法包括将生物材料放置在处理室中，向超临界流体中加入添加剂以形成超临界流体添加剂混合物，将超临界流体添加剂混合物加入到处理室中，并将混合物脉冲在处理室中。 根据本发明的使用超临界流体向生物材料引入添加剂的处理系统包括用于容纳生物材料的处理室，用于储存处理流体的桶，加热元件，入口端口， 和流路。

公开(公告)号：US08735317B2

公开(公告)日：2014-05-27

申请号：US13375560

申请日：2010-06-15

Applicant: Vladimir Zalmanovich Mordkovich ,  Lilia Vadimova Sineva ,  Igor Grigorievich Solomonik ,  Vadim Sergeevich Ermolaev ,  Eduard Borisovich Mitberg

Inventor： Vladimir Zalmanovich Mordkovich ,  Lilia Vadimova Sineva ,  Igor Grigorievich Solomonik ,  Vadim Sergeevich Ermolaev ,  Eduard Borisovich Mitberg

IPC: B01J21/18 ,  B01J27/20 ,  B01J25/00 ,  B01J23/00 ,  B01J23/02 ,  B01J23/06

CPC classification number: B01J25/00 ,  B01J23/75 ,  B01J23/78 ,  B01J23/83 ,  B01J23/864 ,  B01J23/8896 ,  B01J23/8913 ,  B01J29/06 ,  B01J29/084 ,  B01J37/0009 ,  B01J37/0205 ,  B01J37/0221 ,  B01J37/04 ,  C10G2/332 ,  C10G2/333 ,  C10G2300/70

Abstract: The present invention relates to petrochemistry, gas chemistry, coal chemistry, particularly the invention relates to a catalyst for synthesis of hydrocarbons from CO and H2 and a preparation method thereof. The catalyst is pelletized and comprises at least Raney cobalt as active component in an amount of 1-40% by weight based on the total weight of the catalyst, metallic aluminium in an amount of 25-94% by weight based on the total weight of the catalyst and a binder in an amount of 5-30% by weight based on the total weight of the catalyst. The present invention provides the catalyst stability to overheating and high productivity of hydrocarbons C5-C100 for synthesis of hydrocarbons from CO and H2.

Abstract translation: 本发明涉及石油化学，气体化学，煤化学，特别涉及用于从CO和H 2合成烃的催化剂及其制备方法。 催化剂被造粒，并且至少包含阮内钴作为活性组分，其量为基于催化剂总重量的1-40重量％，金属铝的量为25-94重量％，基于 催化剂和基于催化剂总重量的5-30重量％的粘合剂。 本发明提供催化剂对于从CO和H 2合成烃的碳氢化合物C5-C100的过热稳定性和高生产率。

公开(公告)号：US08669295B2

公开(公告)日：2014-03-11

申请号：US13131028

申请日：2009-11-26

Applicant: Qiang Fu ,  Xiaoxin Zhang ,  Yibin Luo ,  Xuhong Mu ,  Baoning Zong

Inventor： Qiang Fu ,  Xiaoxin Zhang ,  Yibin Luo ,  Xuhong Mu ,  Baoning Zong

IPC: C07C27/00

CPC classification number: C07C41/01 ,  B01J23/78 ,  B01J23/80 ,  B01J23/825 ,  B01J23/835 ,  B01J23/8472 ,  B01J23/868 ,  B01J23/8892 ,  B01J25/00 ,  B01J29/46 ,  B01J35/002 ,  B01J37/0009 ,  B01J37/03 ,  B01J37/06 ,  C07C1/043 ,  C07C29/154 ,  C07C2521/02 ,  C07C2521/04 ,  C07C2521/06 ,  C07C2523/02 ,  C07C2523/06 ,  C07C2523/10 ,  C07C2523/22 ,  C07C2523/26 ,  C07C2523/34 ,  C07C2523/72 ,  C07C2523/745 ,  C07C2523/755 ,  C07C2529/40 ,  C07C2529/85 ,  Y02P20/52 ,  C07C31/04 ,  C07C43/043 ,  C07C11/04 ,  C07C11/06

Abstract: The present invention provides a process for preparing methanol, dimethyl ether, and low carbon olefins from syngas, wherein the process comprises the step of contacting syngas with a catalyst under the conditions for converting the syngas into methanol, dimethyl ether, and low carbon olefins, characterized in that, the catalyst contains an amorphous alloy consisting of a first component Al and a second component, said second component being one or more elements or oxides thereof selected from Group IA, IIIA, IVA, VA, IB, IIB, IVB, VB, VIB, VIIB, VIII, and Lanthanide series of the Periodic Table of Elements, and said second component being different from the first component Al. According to the present process, the syngas can be converted into methanol, dimethyl ether, and low carbon olefins in a high CO conversion, a high selectivity of the target product, and high carbon availability.

Abstract translation: 本发明提供从合成气制备甲醇，二甲醚和低碳烯烃的方法，其中该方法包括在合成气转化为甲醇，二甲醚和低碳烯烃的条件下使合成气与催化剂接触的步骤， 其特征在于，所述催化剂含有由第一成分Al和第二成分组成的非晶合金，所述第二成分为选自IA，IIIA，IVA，VA，IB，IIB，IVB，VB中的一种或多种元素或氧化物 ，VIB，VIIB，VIII和元素周期表的镧系元素，所述第二成分与第一成分Al不同。 根据本方法，合成气可以在高CO转化率，目标产物的高选择性和高碳可利用性下转化为甲醇，二甲醚和低碳烯烃。

公开(公告)号：US20140058182A1

公开(公告)日：2014-02-27

申请号：US13766369

申请日：2013-02-13

Applicant: Aggregate Energy, LLC

Inventor： Gert Sandstede ,  Thomas Lehmann

IPC: C10G3/00 ,  B01J27/055 ,  B01J31/06

CPC classification number: C10G3/46 ,  B01J21/18 ,  B01J21/185 ,  B01J23/882 ,  B01J23/883 ,  B01J23/888 ,  B01J25/00 ,  B01J25/02 ,  B01J27/055 ,  B01J31/06 ,  B01J35/0033 ,  B01J35/023 ,  B01J37/0018 ,  B01J37/0036 ,  B01J37/04 ,  B01J37/06 ,  B01J37/20 ,  B01J2231/643 ,  B82Y30/00 ,  C10G3/45 ,  C10G3/47 ,  C10G3/50 ,  C10G2300/1014 ,  C10G2300/1018 ,  C10G2300/70 ,  Y02P30/20

Abstract: A process for hydrogenation of oxygen-containing organic products, oil refinery products or mixtures thereof, wherein the process comprises bringing the organic products, oil refinery products, or mixtures thereof into contact with a catalyst according to claim 1 in the presence of hydrogen gas at a temperature in the range of 200 to 500° C. and at a pressure in the range of 10 to 1000 bar.

Abstract translation: 含氧有机产物，炼油产品或其混合物的氢化方法，其中所述方法包括使有机产物，炼油产品或其混合物与根据权利要求1的催化剂在氢气存在下接触 温度范围为200〜500℃，压力为10〜1000巴。

公开(公告)号：US08524631B2

公开(公告)日：2013-09-03

申请号：US12152109

申请日：2008-05-09

Applicant: Maximilian A. Biberger

Inventor： Maximilian A. Biberger

IPC: B01J23/755 ,  B01J23/745 ,  B01J23/75 ,  B01J23/80 ,  B01J23/85 ,  B01J23/86 ,  B01J23/88 ,  B01J23/881 ,  B01J23/882 ,  B01J23/883

CPC classification number: F28C3/16 ,  A61L2/18 ,  B01J2/16 ,  B01J19/0013 ,  B01J19/088 ,  B01J25/00 ,  B01J25/02 ,  B01J35/04 ,  B01J37/0018 ,  B01J37/0027 ,  B01J37/06 ,  B01J37/349 ,  B01J2219/0805 ,  B01J2219/0879 ,  B01J2219/0894 ,  B22F9/12 ,  B22F2203/13 ,  B22F2999/00 ,  F28D7/024 ,  F28D7/08 ,  F28D15/00 ,  F28F27/00 ,  Y10S623/92 ,  Y10S623/923 ,  Y10T137/0391 ,  Y10T137/2076 ,  Y10T156/15 ,  B22F2202/13

Abstract: A method of producing a catalyst material with nano-scale structure, the method comprising: introducing a starting powder into a nano-powder production reactor, the starting powder comprising a catalyst material; the nano-powder production reactor nano-sizing the starting powder, thereby producing a nano-powder from the starting powder, the nano-powder comprising a plurality of nano-particles, each nano-particle comprising the catalyst material; and forming a catalyst precursor material from the nano-powder, wherein the catalyst precursor material is a densified bulk porous structure comprising the catalyst material, the catalyst material having a nano-scale structure.