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公开(公告)号:AU2005200564B2
公开(公告)日:2008-01-10
申请号:AU2005200564
申请日:2005-02-09
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: TONKOVICH ANNA LEE Y , VANDERWIEL DAVID P , GAO YUFEI , WANG YONG , BAKER EDDIE G
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公开(公告)号:AU6643500A
公开(公告)日:2001-03-13
申请号:AU6643500
申请日:2000-08-15
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: WANG YONG , VANDERWIEL DAVID P , TONKOVICH ANNA LEE Y , GAO YUFEI , BAKER EDDIE G
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公开(公告)号:DK0643756T3
公开(公告)日:1999-02-15
申请号:DK93915205
申请日:1993-06-03
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: ELLIOTT DOUGLAS C , SEALOCK L JOHN JR , BAKER EDDIE G
Abstract: A method for converting organic material into a product gas includes: a) providing a liquid reactant mixture containing liquid water and liquid organic material within a pressure reactor; b) providing an effective amount of a reduced metal catalyst selected from the group consisting of ruthenium, rhodium, osmium and iridium or mixtures thereof within the pressure reactor; and c) maintaining the liquid reactant mixture and effective amount of reduced metal catalyst in the pressure reactor at temperature and pressure conditions of from about 300 DEG C. to about 450 DEG C.; and at least 130 atmospheres for a period of time, the temperature and pressure conditions being effective to maintain the reactant mixture substantially as liquid, the effective amount of reduced metal catalyst and the period of time being sufficient to catalyze a reaction of the liquid organic material to produce a product gas composed primarily of methane, carbon dioxide and hydrogen.
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公开(公告)号:AT169663T
公开(公告)日:1998-08-15
申请号:AT93915205
申请日:1993-06-03
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: ELLIOTT DOUGLAS C , SEALOCK L JOHN JR , BAKER EDDIE G
Abstract: A method for converting organic material into a product gas includes: a) providing a liquid reactant mixture containing liquid water and liquid organic material within a pressure reactor; b) providing an effective amount of a reduced metal catalyst selected from the group consisting of ruthenium, rhodium, osmium and iridium or mixtures thereof within the pressure reactor; and c) maintaining the liquid reactant mixture and effective amount of reduced metal catalyst in the pressure reactor at temperature and pressure conditions of from about 300 DEG C. to about 450 DEG C.; and at least 130 atmospheres for a period of time, the temperature and pressure conditions being effective to maintain the reactant mixture substantially as liquid, the effective amount of reduced metal catalyst and the period of time being sufficient to catalyze a reaction of the liquid organic material to produce a product gas composed primarily of methane, carbon dioxide and hydrogen.
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公开(公告)号:CA2137261A1
公开(公告)日:1993-12-23
申请号:CA2137261
申请日:1993-06-03
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: ELLIOTT DOUGLAS C , SEALOCK L JOHN JR , BAKER EDDIE G
Abstract: 2137261 9325639 PCTABS00028 A method for converting organic material into a product gas includes: a) providing a liquid reactant mixture containing liquid water and liquid organic material within a pressure reactor; b) providing an effective amount of a reduced metal catalyst selected from the group consisting of ruthenium, rhodium, osmium and iridium or mixtures thereof within the pressure reactor; and c) maintaining the liquid reactant mixture and effective amount of reduced metal catalyst in the pressure reactor at temperature and pressure conditions of from about 300 ·C to about 450 ·C and at least 130 atmospheres for a period of time, the temperature and pressure conditions being effective to maintain the reactant mixture substantially as liquid, the effective amount of reduced metal catalyst and the period of time being sufficient to catalyze a reaction of the liquid organic material to produce a product gas composed primarily of methane, carbon dioxide and hydrogen.
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公开(公告)号:CA2064464A1
公开(公告)日:1991-02-22
申请号:CA2064464
申请日:1990-08-16
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: SEALOCK L JOHN JR , BAKER EDDIE G , ELLIOTT DOUGLAS C
Abstract: An improved reclamation process for treating petroleum oil and water emulsions derived from producing or processing crude oil is disclosed. The process comprises heating the emulsion to a predetermined temperature at or above about 300 DEG C. and pressurizing the emulsion to a predetermined pressure above the vapor pressure of water at the predetermined temperature. The emulsion is broken by containing the heated and pressurized fluid within a vessel at the predetermined temperature and pressure for a predetermined period of time to effectively separate the emulsion into substantially distinct first, second and third phases. The three phases are then separately withdrawn from the vessel, preferably without any appreciable reduction in temperature and pressure, and at least above a withdraw temperature of about 300 DEG and above the vapor pressure of water at the withdraw temperature.
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公开(公告)号:WO0112323A2
公开(公告)日:2001-02-22
申请号:PCT/US0022422
申请日:2000-08-15
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: WANG YONG , VANDERWIEL DAVID P , TONKOVICH ANNA LEE Y , GAO YUFEI , BAKER EDDIE G
IPC: B01J8/02 , B01J12/00 , B01J19/24 , B01J23/89 , B01J35/00 , B01J35/10 , B01J37/02 , C07B61/00 , C07C1/04 , C07C9/02 , C07C9/04 , C07C9/15 , C10G2/00
CPC classification number: B01J23/8913 , B01J8/0285 , B01J12/007 , B01J19/248 , B01J23/462 , B01J23/75 , B01J35/0006 , B01J35/002 , B01J35/04 , B01J35/10 , B01J35/1009 , B01J37/0221 , B01J37/0238 , B01J37/0244 , B01J2219/32293 , B01J2219/32296 , B01J2219/32408 , B01J2219/32466 , B01J2219/32475 , C07C1/041 , C07C1/0425 , C07C1/0455 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C10G2/33 , C10G2/332
Abstract: The present invention includes Fischer-Tropsch catalysts, reactions using Fischer-Tropsch catalysts, methods of making Fischer-Tropsch catalysts, processes of hydrogenating carbon monoxide, and fuels made using these processes. The invention provides the ability to hydrogenate carbon monoxide with low contact times, good conversion rates and low methane selectivities. In a preferred method, the catalyst is made using a metal foam support.
Abstract translation: 本发明包括费 - 托催化剂,使用费 - 托催化剂的反应,制造费 - 托催化剂的方法,氢化一氧化碳的方法以及使用这些方法制备的燃料。 本发明提供了以低接触时间氢化一氧化碳的能力,良好的转化率和低的甲烷选择性。 在优选的方法中,催化剂使用金属泡沫载体制成。
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公开(公告)号:AU778040B2
公开(公告)日:2004-11-11
申请号:AU6643500
申请日:2000-08-15
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: WANG YONG , VANDERWIEL DAVID P , TONKOVICH ANNA LEE Y , GAO YUFEI , BAKER EDDIE G
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公开(公告)号:NO20092105A
公开(公告)日:2002-04-09
申请号:NO20092105
申请日:2009-05-28
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: WANG YONG , VANDERWIEL DAVID P , TONKOVICH ANNA LEE Y , GAO YUFEI , BAKER EDDIE G
IPC: B01J12/00 , B01J8/02 , B01J19/24 , B01J23/89 , B01J35/00 , B01J35/02 , B01J35/10 , B01J37/02 , B01J37/025 , C07B61/00 , C07C1/04 , C07C9/02 , C07C9/04 , C07C9/15 , C10G2/00
CPC classification number: C10G2/332 , B01J8/0285 , B01J12/007 , B01J19/0093 , B01J19/248 , B01J19/249 , B01J19/2495 , B01J23/8913 , B01J35/0006 , B01J35/04 , B01J35/10 , B01J35/1076 , B01J37/0217 , B01J37/0225 , B01J37/0238 , B01J37/0244 , B01J37/0248 , B01J2219/00783 , B01J2219/00822 , B01J2219/00835 , B01J2219/00844 , B01J2219/0086 , B01J2219/00873 , B01J2219/00984 , B01J2219/2453 , B01J2219/2458 , B01J2219/2462 , B01J2219/32244 , B01J2219/32293 , B01J2219/32296 , B01J2219/32408 , B01J2219/32466 , B01J2219/32475 , C07C1/041 , C07C1/0425 , C07C1/0455 , C07C2523/46 , C07C2523/745 , C07C2523/75 , C10G2/32 , C10G2/33 , C10G2/34 , C10G2/341
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公开(公告)号:CA2381156A1
公开(公告)日:2001-02-22
申请号:CA2381156
申请日:2000-08-15
Applicant: BATTELLE MEMORIAL INSTITUTE
Inventor: GAO YUFEI , BAKER EDDIE G , WANG YONG , VANDERWIEL DAVID P , TONKOVICH ANNA LEE Y
IPC: B01J8/02 , B01J12/00 , B01J19/24 , B01J23/89 , B01J35/00 , B01J35/10 , B01J37/02 , C07B61/00 , C07C1/04 , C07C9/02 , C07C9/04 , C07C9/15 , C10G2/00 , B01J19/00
Abstract: The present invention includes Fischer-Tropsch catalysts, reactions using Fischer-Tropsch catalysts, methods of making Fischer-Tropsch catalysts, processes of hydrogenating carbon monoxide, and fuels made using these processes. The invention provides the ability to hydrogenate carbon monoxide with low contact times, good conversion rates and low methane selectivities. In a preferred method, the catalyst is made using a metal foam support.
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