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21. 发明申请

US20120022307A1 CO-PROCESSING SOLID BIOMASS IN A CONVENTIONAL PETROLEUM REFINING PROCESS UNIT 有权
标题翻译：常规石油精炼加工单元中加工固体生物质
公开(公告)号：US20120022307A1
公开(公告)日：2012-01-26
申请号：US12867214
申请日：2009-06-29
申请人： Steve Yanik , Paul O'Connor , Robert Bartek
发明人： Steve Yanik , Paul O'Connor , Robert Bartek
IPC分类号： C10G1/00 , B01J8/08 , C07C1/20
CPC分类号： C09K3/00 , C10G1/002 , C10G1/08 , C10G11/00 , C10G11/18 , C10G2300/1014 , C10G2300/1037 , C10G2300/4056 , C10G2400/02 , C10G2400/04 , C10G2400/08 , C10G2400/20 , C10G2400/28 , Y02P30/20
摘要： Preparing solid biomass particles for catalytic conversion includes agitating solid biomass particles and providing a biomass-catalyst mixture to a conventional petroleum refinery process unit. The biomass-catalyst mixture includes the solid biomass particles and a catalyst. Agitating solid biomass particles includes flowing a gas to provide a velocity to at least a portion of the solid biomass particles sufficient to reduce their sizes. Co-processing a biomass feedstock and a conventional petroleum feedstock includes liquefying at least a portion of a biomass-catalyst mixture and co-processing at least a portion of the liquefied biomass feedstock and a conventional petroleum feedstock in a conventional petroleum refinery process unit. The biomass feedstock includes a plurality of solid biomass particles and a catalyst, which is liquefied to produce a liquefied biomass feedstock.
摘要翻译：制备用于催化转化的固体生物质颗粒包括搅拌固体生物质颗粒并向传统的炼油工艺单元提供生物质 - 催化剂混合物。生物质 - 催化剂混合物包括固体生物质颗粒和催化剂。搅拌固体生物质颗粒包括使气体流动以提供足以减小其尺寸的至少一部分固体生物质颗粒的速度。共同处理生物质原料和常规石油原料包括液化生物质 - 催化剂混合物的至少一部分，并在常规的炼油工艺单元中共同处理至少一部分液化生物质原料和常规石油原料。生物质原料包括多个固体生物质颗粒和催化剂，其被液化以产生液化生物质原料。

22. 发明申请

US20100113849A1 BIOMASS CONVERSION PROCESS 有权
标题翻译：生物量转换过程
公开(公告)号：US20100113849A1
公开(公告)日：2010-05-06
申请号：US12612378
申请日：2009-11-04
申请人： Robert Bartek , Steve Yanik , Paul O'Connor
发明人： Robert Bartek , Steve Yanik , Paul O'Connor
IPC分类号： C10G1/00 , B01J8/04
CPC分类号： C10L1/04 , C10G1/08 , C10G1/083 , C10G2300/1011 , C10G2300/4006 , C10G2300/708 , Y02E50/14 , Y02P30/20
摘要： A process is disclosed including: contacting solid biomass with a first catalyst stream in a first reaction zone operated at a temperature T1 (from about 250 to about 400° C.), for conversion of a portion of the solid biomass and forming a first gaseous product stream; downwardly passing unconverted biomass to a second reaction zone for contact with a second catalyst stream charged to the second reaction zone operated at a temperature T2, for conversion to form a second gaseous product stream and a spent catalyst; burning coke off the spent catalyst in a regenerator to form a regenerated catalyst; charging a portion of the regenerated catalyst to each of the first and second reaction zones, as the first and second catalyst streams, respectively; upwardly passing the second gaseous product stream to the first reaction zone; and removing both first and second gaseous product streams from the first reaction zone.
摘要翻译：公开了一种方法，包括：使第一催化剂流与第一反应区在温度T1（约250至约400℃）下操作，以使一部分固体生物质转化并形成第一气态产品流; 向下通过未转化的生物质到第二反应区，以与加入在温度T2下操作的第二反应区的第二催化剂流接触，以转化以形成第二气态产物流和废催化剂; 在再生器中燃烧焦炭废催化剂以形成再生催化剂; 将一部分再生催化剂分别装入第一和第二反应区中的第一和第二反应区，作为第一和第二催化剂流; 向上通过第二气态产物流到第一反应区; 以及从所述第一反应区域除去第一和第二气态产物流。

23. 发明申请

US20110197496A1 PRODUCING FUEL AND SPECIALTY CHEMICALS FROM GLYCERIDE CONTAINING BIOMASS 审中-公开
标题翻译：从含有生物质的甘油生产燃料和特种化学品
公开(公告)号：US20110197496A1
公开(公告)日：2011-08-18
申请号：US12997284
申请日：2009-06-30
申请人： Paul O'Connor , Steve Yanik
发明人： Paul O'Connor , Steve Yanik
IPC分类号： C10L1/04 , C07C1/20
CPC分类号： C10G1/08 , C10G1/002 , C10G3/42 , C10G3/50 , C10G11/00 , C10G29/20 , C10G45/58 , C10G47/00 , C10G51/026 , C10G69/04 , C10G69/123 , C10G2300/1014 , C10G2400/04 , C10G2400/08 , C10L1/02 , C10L1/023 , C10L1/026 , Y02E50/13 , Y02P30/20
摘要： A method for catalytically cracking a triglyceride-containing biomass can include the steps of (i) catalytically cracking triglycerides in a biomass-catalyst mixture, at a temperature below about 300° C., to produce a first oil and a cellulosic portion and (ii) catalytically cracking cellulose in the cellulosic portion, at a temperature between about 300 and about 600° C., to produce a second oil. Another method for catalytically cracking a triglyceride-containing biomass includes catalytically cracking triglycerides in a biomass-catalyst mixture, at a temperature between about 300 and about 600° C., where the catalyst comprises an acidic or basic catalyst, to produce an oil comprising aromatics.
摘要翻译：用于催化裂解含甘油三酯的生物质的方法可以包括以下步骤：（i）在低于约300℃的温度下在生物质 - 催化剂混合物中催化裂解甘油三酸酯，以产生第一油和纤维素部分，）在约300至约600℃的温度下在纤维素部分中催化裂解纤维素，以产生第二种油。用于催化裂解含甘油三酯的生物质的另一种方法包括催化裂化生物质 - 催化剂混合物中的甘油三酯，温度在约300至约600℃之间，其中催化剂包含酸性或碱性催化剂，以产生包含芳族化合物的油。

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