公开(公告)号：US11772082B1

公开(公告)日：2023-10-03

申请号：US17347620

申请日：2021-06-15

申请人： AVN Corporation

发明人： Madan Mohan Bhasin

IPC分类号： B01J27/224 ,  C07C5/333 ,  B01J37/08 ,  C10G47/02 ,  C10G45/04 ,  B01J35/10 ,  C07D301/06 ,  C10G11/02 ,  B01J35/02 ,  B01J37/02 ,  B01J23/50

CPC分类号： B01J27/224 ,  B01J23/50 ,  B01J35/023 ,  B01J35/1009 ,  B01J35/1014 ,  B01J35/1038 ,  B01J35/1042 ,  B01J37/0203 ,  B01J37/08 ,  C07C5/3335 ,  C07D301/06 ,  C10G11/02 ,  C10G45/04 ,  C10G47/02 ,  C07C2521/08 ,  C07C2521/18 ,  C07C2523/50 ,  C10G2300/202 ,  C10G2300/207

摘要： A catalyst support comprising at least 95% silicon carbide, having surface areas of ≤10 m2/g and pore volumes of ≤1 cc/g. A method of producing a catalyst support, the method including mixing SiC particles of 0.1-20 microns, SiO2 and carbonaceous materials to form an extrusion, under inert atmospheres, heating the extrusion at temperatures of greater than 1400° C., and removing residual carbon from the heated support under temperatures below 1000° C. A catalyst on a carrier, comprising a carrier support having at least about 95% SiC, with a silver solution impregnated thereon comprising silver oxide, ethylenediamine, oxalic acid, monoethanolamine and cesium hydroxide. A process for oxidation reactions (e.g., for the production of ethylene oxide, or oxidation reactions using propane or methane), or for endothermic reactions (e.g., dehydrogenation of paraffins, of ethyl benzene, or cracking and hydrocracking hydrocarbons).

公开(公告)号：US20230405561A1

公开(公告)日：2023-12-21

申请号：US18450902

申请日：2023-08-16

申请人： AVN Corporation

发明人： Madan Mohan Bhasin

IPC分类号： B01J27/224 ,  C07D301/06 ,  B01J35/10 ,  C07C5/333 ,  B01J23/50 ,  B01J37/08 ,  C10G45/04 ,  B01J35/02 ,  C10G11/02 ,  B01J37/02 ,  C10G47/02

CPC分类号： B01J27/224 ,  C07D301/06 ,  B01J35/1038 ,  C07C5/3335 ,  B01J23/50 ,  B01J37/08 ,  C10G45/04 ,  B01J35/1014 ,  B01J35/1009 ,  B01J35/023 ,  B01J35/1042 ,  C10G11/02 ,  B01J37/0203 ,  C10G47/02 ,  C10G2300/207 ,  C07C2521/08 ,  C07C2521/18 ,  C10G2300/202 ,  C07C2523/50

摘要： A catalyst support comprising at least 95% silicon carbide, having surface areas of ≤10 m2/g and pore volumes of ≤1 cc/g. A method of producing a catalyst support, the method including mixing SiC particles of 0.1-20 microns, SiO2 and carbonaceous materials to form an extrusion, under inert atmospheres, heating the extrusion at temperatures of greater than 1400° C., and removing residual carbon from the heated support under temperatures below 1000° C. A catalyst on a carrier, comprising a carrier support having at least about 95% SiC, with a silver solution impregnated thereon comprising silver oxide, ethylenediamine, oxalic acid, monoethanolamine and cesium hydroxide. A process for oxidation reactions (e.g., for the production of ethylene oxide, or oxidation reactions using propane or methane), or for endothermic reactions (e.g., dehydrogenation of paraffins, of ethyl benzene, or cracking and hydrocracking hydrocarbons).