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公开(公告)号：US20130118059A1
公开(公告)日：2013-05-16
申请号：US13677124
申请日：2012-11-14
Applicant: Shell Oil Company
Inventor： Jean Paul LANGE , Colin John SCHAVERIEN , Nicolaas Wilhelmus Joseph WAY , Johan Willem GOSSELINK , John William HARRIS , Andries Quirin Maria BOON , Andries Hendrik JANSSEN , Leticia ESPINOSA ALONSO
CPC classification number: C10G1/006 , C10G1/002 , C10G1/042 , C10G3/50 , C10G11/18 , C10L1/02 , Y02P30/20
Abstract: A process for conversion of a cellulosic material comprising a) a liquefaction step, comprising contacting a cellulosic material with a liquid solvent at a temperature of equal to or more than 200° C.; or contacting a cellulosic material with a liquid solvent at a temperature of equal to or more than 100° C. in the presence of a catalyst, to produce a final liquefied product; b) a catalytic cracking step, comprising contacting at least part of the final liquefied product with a fluidized catalytic cracking catalyst at a temperature of equal to or more than 400° C., to produce one or more cracked products.
Abstract translation: 一种转化纤维素材料的方法，包括a）液化步骤，包括在等于或大于200℃的温度下使纤维素材料与液体溶剂接触; 或在催化剂存在下，在等于或大于100℃的温度下将纤维素材料与液体溶剂接触，以产生最终的液化产物; b）催化裂化步骤，包括使至少部分最终液化产物与等于或大于400℃的温度下的流化催化裂化催化剂接触，以产生一种或多种裂化产物。
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Patent Agency Ranking
公开(公告)号：US20130167430A1
公开(公告)日：2013-07-04
申请号：US13729227
申请日：2012-12-28
Applicant: SHELL OIL COMPANY
Inventor： John William HARRIS , Ye-Mon CHEN
CPC classification number: C10L1/1802 , B01F5/00 , B01J8/24 , B01J29/082 , B01J29/084 , B01J29/088 , B01J29/18 , B01J29/40 , B01J29/50 , B01J29/60 , B01J29/70 , B01J29/7034 , B01J29/7042 , B01J29/7046 , B01J29/80 , B01J29/90 , B01J2208/00902 , B01J2219/00024 , C10G1/08 , C10G3/57 , C10G2300/1011 , C10G2300/4056 , Y02P30/20 , Y10T29/49718 , Y10T137/87652
Abstract: A process for converting a solid biomass material comprising (a) mixing the solid biomass material with a fluid to form a fluidized biomass stream; and (b) propagating the fluidized biomass stream into the riser reactor via one or more delivery aperture(s); wherein the solid biomass material has a particle size distribution with a mean particle size diameter, and wherein the delivery aperture has a diameter equal to or more than three times the mean particle size diameter of the particle size distribution of the solid biomass material.
Abstract translation: 一种用于转化固体生物质材料的方法，包括（a）将固体生物质材料与流体混合以形成流化的生物质流; 和（b）通过一个或多个输送孔将流化的生物物流传播到提升管反应器中; 其中所述固体生物质材料具有平均粒度直径的粒度分布，并且其中所述输送孔的直径等于或大于所述固体生物质材料的粒度分布的平均粒度直径的三倍。
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公开(公告)号：US20150094201A1
公开(公告)日：2015-04-02
申请号：US14563479
申请日：2014-12-08
Applicant: SHELL OIL COMPANY
Inventor： Andries Hendrik JANSSEN , Andries Quirin Maria BOON , John William HARRIS , Nicolaas Wilhelmus Joseph WAY , Colin John SCHAVERIEN , Johan Willem GOSSELINK
CPC classification number: B01J38/40 , B01J29/90 , B01J38/12 , B01J38/14 , B01J38/30 , C10B49/22 , C10B53/02 , C10G1/08 , C10G1/083 , C10G3/57 , C10G11/18 , C10G2300/1011 , C10G2300/708 , Y02E50/14 , Y02P20/145 , Y02P30/20 , Y02P30/446
Abstract: A process for regenerating a coked catalytic cracking catalyst which the carbon-containing deposits on the catalyst contains at least 1 wt % bio-carbon, based on the total weight of carbon present in the carbon-containing deposits is provided. Such coked catalytic cracking catalyst is contacted with an oxygen containing gas at a temperature of equal to or more than 550° C. in a regenerator to produce a regenerated catalytic cracking catalyst, heat and carbon dioxide.
Abstract translation: 提供了一种基于存在于含碳沉积物中的碳的总重量，使催化剂上的含碳沉积物含有至少1重量％生物碳的再结晶催化裂化催化剂的方法。 这样的焦化催化裂化催化剂在再生器中在等于或高于550℃的温度下与含氧气体接触，以产生再生的催化裂化催化剂，热和二氧化碳。
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公开(公告)号：US20130276360A1
公开(公告)日：2013-10-24
申请号：US13868455
申请日：2013-04-23
Applicant: SHELL OIL COMPANY
Inventor： Andries Quirin Maria BOON , Johan Willem GOSSELINK , John William HARRIS , Andries Hendrik JANSSEN , Martin Jean Pierre Cornelis NIESKENS , Easwar Santhosh RANGANATHAN , Colin John SCHAVERIEN , Nicolaas Wilhelmus Joseph WAY
IPC: C10G1/06
CPC classification number: C10G1/065 , B01J8/32 , B01J8/388 , C10G1/002 , C10G1/08 , C10G3/42 , C10G3/57 , C10G11/18 , C10G69/04 , C10G2300/1011 , Y02P30/20
Abstract: A process for converting a solid biomass material, comprising contacting the solid biomass material and a hydrocarbon co-feed with a catalytic cracking catalyst at a temperature of more than 400° C. in a riser reactor to produce one or more cracked products, wherein the solid biomass material is introduced to the riser reactor at a location downstream of the location where the hydrocarbon co-feed is introduced to the riser reactor.
Abstract translation: 一种用于转化固体生物质材料的方法，包括在提升管反应器中在大于400℃的温度下使固体生物质材料和烃共进料与催化裂化催化剂接触以产生一种或多种裂化产物，其中 将固体生物质材料引入到提升管反应器中的烃共进料引入提升管反应器的位置下游的位置处。
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公开(公告)号：US20130178672A1
公开(公告)日：2013-07-11
申请号：US13733713
申请日：2013-01-03
Applicant: Shell Oil Company
Inventor： Ye-Mon CHEN , John William HARRIS , Martin Jean Pierre Cornelis NIESKENS , Easwar Santhosh RANGANATHAN , Colin John SCHAVERIEN
IPC: C10G1/00
CPC classification number: C10G1/002 , C10G1/08 , C10G3/49 , C10G3/57 , C10G3/62 , C10G11/18 , C10G11/182 , C10G51/026 , C10G2300/1014 , C10G2400/20 , Y02P30/20
Abstract: A process for making a distillate product and one or more C2-C4 olefins from a FCC feedstock containing a cellulosic material and a hydrocarbon co-feed is provided.
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公开(公告)号：US20150337207A1
公开(公告)日：2015-11-26
申请号：US14816322
申请日：2015-08-03
Applicant: SHELL OIL COMPANY
Inventor： Ye-Mon CHEN , John William HARRIS , Martin Jean Pierre Cornelis NIESKENS , Easwar Santhosh RANGANATHAN , Colin John SCHAVERIEN , Robert Alexander LUDOLPH
CPC classification number: C10G1/002 , C10G1/08 , C10G3/49 , C10G3/57 , C10G3/62 , C10G11/18 , C10G11/182 , C10G51/026 , C10G2300/1014 , C10G2400/20
Abstract: A process for making a distillate product and one or more C2-C4 olefins from a FCC feedstock containing a cellulosic material and a hydrocarbon co-feed is provided.
Abstract translation: 提供了一种从含有纤维素材料和烃共进料的FCC原料制备馏出物产物和一种或多种C 2 -C 4烯烃的方法。
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