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

IPC: C10G1/00 ,  C10L1/02

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。

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

IPC: B01J38/40 ,  B01J38/12

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。

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。