公开(公告)号：EP4232525B1

公开(公告)日：2024-08-07

申请号：EP21815279.1

申请日：2021-10-26

IPC分类号： C10B53/02 ,  C10B47/44 ,  C10J3/62 ,  C10J3/46 ,  C10J3/84 ,  C10J3/66 ,  C10J3/50

CPC分类号： C10B53/02 ,  C10B47/44 ,  C10J3/66 ,  C10J3/62 ,  C10J2300/095620130101 ,  C10J2300/091620130101 ,  C10K3/005 ,  C10K3/008 ,  C10J2300/160920130101 ,  C10J2300/120720130101 ,  C10J2300/125320130101 ,  C10J3/14 ,  Y02E50/10 ,  Y02P20/145

公开(公告)号：EP3745065B1

公开(公告)日：2023-06-07

申请号：EP20401026.8

申请日：2020-05-02

发明人： Kohler, Hubert ,  Gschoßmann, Günther

IPC分类号： F26B3/20 ,  C10G1/02 ,  F26B3/24 ,  F26B9/08 ,  C10J3/46 ,  C10K3/00

公开(公告)号：EP2582778B1

公开(公告)日：2023-06-07

申请号：EP11796075.7

申请日：2011-06-09

发明人： MARKER, Terry, L. ,  FELIX, Larry, G. ,  LINCK, Martin, B. ,  MEYER, Howard, S. ,  LEPPIN, Dennis

IPC分类号： C10L3/08 ,  C01B3/16 ,  C01B3/34 ,  C10J3/46 ,  C10K1/02 ,  C10K3/04 ,  C10L3/10 ,  C10B49/10 ,  C10B53/02 ,  C10G3/00 ,  B01J37/20 ,  B01J23/883 ,  B01J37/02

公开(公告)号：EP4143274A1

公开(公告)日：2023-03-08

申请号：EP21796935.1

申请日：2021-04-30

申请人： Fulcrum Bioenergy, Inc.

发明人： TIVERIOS, Peter, G. ,  MACIAS, James, E. ,  LUCAS, Stephen, H. ,  RICH, Lewis, L. ,  THOMSON, Gregor, A.

IPC分类号： C10G2/00 ,  C10G47/00 ,  C10J3/46

公开(公告)号：EP4136196A1

公开(公告)日：2023-02-22

申请号：EP21789290.0

申请日：2021-04-13

申请人： Eastman Chemical Company

发明人： DEBRUIN, Bruce, Roger ,  EKART, Michael, Paul ,  TRAPP, William, Lewis

IPC分类号： C10J3/46 ,  C10J3/72

公开(公告)号：EP3215457B1

公开(公告)日：2022-08-24

申请号：EP15774635.5

申请日：2015-10-06

发明人： OSTUNI, Raffaele ,  SKINNER, Geoffrey Frederick ,  FILIPPI, Ermanno

IPC分类号： C01B3/38 ,  C01B3/02 ,  C10J3/46 ,  C10J3/72

公开(公告)号：EP3986987A1

公开(公告)日：2022-04-27

申请号：EP20825112.4

申请日：2020-02-26

申请人： Aries Gasification, LLC

发明人： KELFKENS, Renus ,  DAVIS, Brandon

IPC分类号： C10J3/46 ,  B01J8/18 ,  C10K1/02 ,  C02F11/10

公开(公告)号：EP3819357A1

公开(公告)日：2021-05-12

申请号：EP20206377.2

申请日：2020-11-09

申请人： Indian Oil Corporation Limited

发明人： MUKTHIYAR, Sadhullah ,  SAIDULU, Gadari ,  BHUYAN, Manoj Kumar ,  GUPTA, Kamlesh ,  SAU, Madhusudan ,  KAPUR, Gurpreet Singh ,  RAMAKUMAR, Sankara Sri Venkata

IPC分类号： C10G11/18 ,  C10J3/46 ,  C10K3/04 ,  C01B3/56 ,  C01B3/44

摘要： The present invention relates to a process for production of high yield of hydrogen by carrying out the dry reforming of the dry gas generated from the process itself by utilizing the same catalyst for cracking and producing high yield of light olefins such as ethylene, propylene and butylenes from residue feedstocks.

公开(公告)号：EP3666858A3

公开(公告)日：2020-08-19

申请号：EP19176804.3

申请日：2009-09-28

申请人： The Ohio State University

发明人： FAN, Liang-Shih ,  LI, Fanxing

IPC分类号： C10J3/00 ,  B01J2/28 ,  B01J21/04 ,  B01J21/06 ,  B01J23/745 ,  B01J35/02 ,  B01J37/00 ,  B01J37/12 ,  B01J37/16 ,  C04B35/626 ,  C04B35/628 ,  C04B35/63 ,  C04B35/636 ,  C10J3/12 ,  C10J3/46 ,  C10J3/72 ,  F23C99/00

摘要： A method of preparing ceramic composite particles comprising the steps of, mixing a metal oxide with at least one ceramic material to form a mixture; granulating said mixture by adding a binding material; drying said granulated mixture; processing said dried, granulated mixture into particle form such that the length of said particles is greater than about 200 μm; heat treating said particles at a temperature of from about 500 to about 1500°C; and reducing and oxidizing said particles.

公开(公告)号：EP3566770A2

公开(公告)日：2019-11-13

申请号：EP19183725.1

申请日：2013-12-18

申请人： Reliance Industries Limited

发明人： Daggupati, Sateesh ,  Mandal, Sukumar ,  Das Asit, Kumar ,  Sapre, Ajit Vishwanath

IPC分类号： B01J23/04 ,  B01J27/232 ,  B01J27/25 ,  B01J29/40 ,  C10J3/46 ,  B01J29/08 ,  B01J37/02

摘要： An improved process for the catalytic gasification of a carbonaceous feedstock in a dual fluidized bed reactor for producing synthesis gas is disclosed. The disclosure uses γ-alumina as a catalyst support and heat carrier in the gasification zone (102). The gasification zone (102) is operated at 700 - 750 °C to prevent substantial conversion of γ-alumina to α-alumina, which would manifest in the enablement of high catalyst loading and high recyclability. The catalyst is an alkali metal, preferably K 2 CO 3 , so that conversion proportional to total K 2 CO 3 to solid carbon ratio is achieved with as high K 2 CO 3 loading as 50 wt% on the solid support. The combustion zone (140) is operated at 800° - 840° C, to prevent any conversion of the γ-alumina to α-alumina, so that catalyst recyclability of up to 98% is achieved between two successive cycles.