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公开(公告)号：US20140330057A1
公开(公告)日：2014-11-06
申请号：US14265411
申请日：2014-04-30
Applicant: SHELL OIL COMPANY
Inventor： Ivo Johannes DIJS , Arjen NIEUWHOF , Johannes Pieter HAAN , Josiane Marie-Rose GINESTRA , Jozef Jacobus Titus SMITS , Colin John SCHAVERIEN , Leticia ESPINOSA ALONSO , Wouter SPIERING
IPC: C10G1/04
CPC classification number: C10G1/045 , C10B53/02 , C10G33/00 , C10G47/00 , C10G47/24 , C10G47/26 , C10G47/28 , C10L1/02 , Y02E50/14
Abstract: A process for converting a biomass material comprising a) pyrolyzing a biomass material to produce a biomass-derived pyrolysis product; b) mixing at least part of the biomass-derived pyrolysis product and a petroleum-derived hydrocarbon composition, which petroleum derived hydrocarbon composition has a C7-asphaltenes content of equal to or more than 0.2 wt %, based on the total weight of the petroleum-derived hydrocarbon composition, to produce a hydrocarbon-containing mixture; c) dewatering the hydrocarbon-containing mixture to produce a dewatered hydrocarbon-containing mixture; d) contacting the dewatered hydrocarbon-containing mixture with hydrogen in one or more ebullating bed reactors comprising a catalyst at a temperature in the range from 350 to 500° C. to produce a reaction product.
Abstract translation: 一种用于转化生物质材料的方法，包括a）热解生物质材料以产生生物质衍生的热解产物; b）将至少部分生物质衍生的热解产物和石油衍生的烃组合物混合，所述石油衍生的烃组合物具有基于石油的总重量等于或大于0.2重量％的C7-沥青质含量 得到的含烃混合物; c）使含烃混合物脱水以产生脱水的含烃混合物; d）使脱水的含烃混合物与氢在一个或多个沸腾床反应器中接触，所述反应床包含催化剂，温度为350-500℃，以产生反应产物。
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公开(公告)号：US20140115951A1
公开(公告)日：2014-05-01
申请号：US14060134
申请日：2013-10-22
Applicant: SHELL OIL COMPANY
IPC: C10L1/18
CPC classification number: C10L1/1802 , C10G1/002 , C10G1/083 , C10G2300/1011 , Y02P30/20
Abstract: A process for converting a solid biomass material comprising a) providing a pneumatic fluid; b) dispersing the solid biomass material into the pneumatic fluid to prepare a pneumatic dispersion and transporting the pneumatic dispersion to a reactor; and c) contacting the pneumatic dispersion with a catalyst in the reactor to produce a product stream comprising one or more conversion products.
Abstract translation: 一种用于转化固体生物质材料的方法，包括：a）提供气动流体; b）将固体生物质材料分散到气动流体中以制备气动分散体并将气态分散体输送到反应器中; 和c）使所述气动分散体与所述反应器中的催化剂接触以产生包含一种或多种转化产物的产物流。
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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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公开(公告)号：US20170369787A1
公开(公告)日：2017-12-28
申请号：US15540401
申请日：2015-12-24
Applicant: SHELL OIL COMPANY
Inventor： Colin John SCHAVERIEN , Yunming FANG
CPC classification number: C10G1/02 , B01J29/405 , C10B49/10 , C10B49/22 , C10B53/02 , C10B57/06 , C10G3/49 , C10G9/32 , C10G2300/1014 , C10G2300/202 , C10G2400/30 , C10K3/02 , Y02E50/14 , Y02P30/20
Abstract: This invention relates to a process for the conversion of a feedstock comprising a lignin-comprising material, comprising the steps (a) to (c): (a) charging the feedstock to a fluidized bed reactor; (b) pyrolyzing at least part of the feedstock in the fluidized bed reactor while introducing a carrier gas into the reactor, to produce pyrolysis vapours; (c) reacting at least part of the pyrolysis vapours coming from step (b) in a second reactor comprising a catalyst, to produce hydrocarbon products comprising aromatics.
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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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Patent Agency Ranking
6.发明申请PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN 审中-公开来自生物原料的含氧化合物的流体催化裂化工艺公开(公告)号：US20140296592A1
公开(公告)日：2014-10-02
申请号：US14227621
申请日：2014-03-27
Applicant: SHELL OIL COMPANY
Inventor： Wei ZHU , Yinsuo CAI , YiBin LIU , YongShan TU , ChaoHe YANG , Yunying QI , Robert Alexander LUDOLPH , James Lloyd JENKINS , Theodorus Johannes BROK , Colin John SCHAVERIEN , Binghui LI
CPC classification number: C07C7/10 , C07C4/06 , C07C2529/89 , C10G3/42 , C10G11/18 , C10G33/04 , C10G70/06 , Y02P30/20
Abstract: A process for the fluid catalytic cracking of oxygenated hydrocarbon compounds from biological origin. The process comprises (a) contacting a feed comprising the oxygenated hydrocarbon compounds with a fluid catalytic cracking catalyst at elevated temperature to produce a cracked products stream, the feed comprising an amount of sulphur; (b) separating catalyst from the cracked products stream; (c) separating a light fraction from the cracked products stream; and (d) removing hydrogen sulphide from the light fraction by means of an amine treating process. The fluid catalytic cracking process involves the presence or use of water and/or steam and comprises a working-up process of the cracked products stream. In the working-up process, one or more chemical additives for reducing or hindering the formation of foam in amine liquids selected from defoamers and demulsifiers are added to the amine solvent in one or more amine treaters.
Abstract translation: 一种从生物来源对含氧化合物进行流化催化裂化的方法。 该方法包括（a）在升高的温度下将包含含氧烃化合物的进料与流化催化裂化催化剂接触以产生裂化产物流，所述进料包含一定量的硫; （b）从裂化产物流中分离催化剂; （c）从裂化产物流中分离轻馏分; 和（d）通过胺处理方法从轻馏分中除去硫化氢。 流化催化裂化过程涉及水和/或蒸汽的存在或使用，并且包括裂化产物流的处理过程。 在后处理过程中，将一种或多种用于减少或阻碍选自消泡剂和破乳剂的胺液体中的泡沫形成的化学添加剂加入到一种或多种胺处理剂中的胺溶剂中。
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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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10.发明申请PROCESS FOR THE FLUID CATALYTIC CRACKING OF OXYGENATED HYDROCARBON COMPOUNDS FROM BIOLOGICAL ORIGIN 审中-公开来自生物原料的含氧化合物的流体催化裂化工艺公开(公告)号：US20140296594A1
公开(公告)日：2014-10-02
申请号：US14227767
申请日：2014-03-27
Applicant: SHELL OIL COMPANY
Inventor： Theodorus Johannes BROK , Yinsuo CAI , James Lloyd JENKINS , Binghui LI , YiBin LIU , Robert Alexander LUDOLPH , Yunying QI , Colin John SCHAVERIEN , YongShan TU , ChaoHe YANG
CPC classification number: C07C7/20 , C07C4/06 , C07C2529/89 , C10G3/57 , C10G11/18 , C10G33/04 , Y02P30/20
Abstract: A process for the fluid catalytic cracking of oxygenated hydrocarbon compounds from biological origin. The process comprises (a) contacting a feed comprising the oxygenated hydrocarbon compounds from biological origin with a fluid cracking catalyst at a temperature of equal to or more than 400° C. to produce a products stream; (b) separating fluid cracking catalyst from the products stream and separating a fraction comprising one or more C1-C4 hydrocarbon compounds from the products stream; and (c) processing the fraction comprising one or more C1-C4 hydrocarbon compounds in a work-up process, which comprises one or more oil/water separation steps. One or more de-emulsifiers are added to one or more oil/water separation steps.
Abstract translation: 一种从生物来源对含氧化合物进行流化催化裂化的方法。 该方法包括（a）在等于或高于400℃的温度下将包含来自生物来源的氧化烃化合物的进料与流体裂解催化剂接触以产生产物流; （b）从产物流中分离流体裂解催化剂并从产物流中分离包含一种或多种C 1 -C 4烃化合物的馏分; 和（c）在包括一个或多个油/水分离步骤的处理过程中处理包含一种或多种C 1 -C 4烃化合物的馏分。 一种或多种去乳化剂被加入到一个或多个油/水分离步骤中。
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