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111. 发明申请

WO2016142808A1 AN INTEGRATED PROCESS FOR CONVERSION OF WASTE PLASTICS TO FINAL PETROCHEMICAL PRODUCTS 审中-公开
标题翻译：废弃塑料转化为最终石油化工产品的综合工艺
公开(公告)号：WO2016142808A1
公开(公告)日：2016-09-15
申请号：PCT/IB2016/051136
申请日：2016-03-01
申请人： SABIC GLOBAL TECHNOLOGIES, B.V.
发明人： NARAYANASWAMY, Ravichander , RAMAMURTHY, Krishna Kumar , STANISLAUS, Alexander , JAVEED, Mohammad
IPC分类号： C10G1/10 , C10G9/36 , C10G45/02 , C10G47/00 , C10G69/06
CPC分类号： C10G65/00 , C10B53/07 , C10B57/06 , C10G1/02 , C10G1/10 , C10G9/36 , C10G45/02 , C10G47/00 , C10G69/06 , C10G2300/1003 , C10G2300/201 , C10G2300/202 , C10G2300/301
摘要： An integrated process for the conversion of waste plastics to high value products. The integrated process allows for operation with a hydroprocessing reactor which provides simultaneous hydrogenation, dechlorination, and hydrocracking of components of a hydrocarbon stream to specifications which meet steam cracker requirements.
摘要翻译：将废塑料转化为高价值产品的综合过程。整合过程允许使用加氢处理反应器进行操作，其提供烃流体组分的同时氢化，脱氯和加氢裂化，以满足满足蒸汽裂化器要求的规格。

112. 发明申请

WO2016102249A1 PROCESS FOR PRODUCING LPG AND BTX 审中-公开
标题翻译：生产液化石油气和BTX的工艺
公开(公告)号：WO2016102249A1
公开(公告)日：2016-06-30
申请号：PCT/EP2015/079824
申请日：2015-12-15
申请人： SABIC GLOBAL TECHNOLOGIES B.V.
发明人： OPRINS, Arno Johannes Maria , DAVIES, Andrew , WARD, Andrew Mark , WONG, M Kae Shin , ARAMBURO, Luis , MAIKEL, Van Iersel
IPC分类号： C10G65/00 , C10G65/10 , C10G65/18
CPC分类号： C10G67/02 , C10G65/00 , C10G65/10 , C10G65/18 , C10G69/02 , C10G2300/301 , C10G2400/20 , C10G2400/26 , C10G2400/28 , C10G2400/30
摘要： The invention relates to a process for producing LPG and BTX, comprising a) subjecting a mixed hydrocarbon feedstream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; b) separating the first hydrocracking product stream to provide at least a light hydrocarbon stream comprising at least C2 and C3 hydrocarbons, a middle hydrocarbon stream comprising C4 and/or C5 hydrocarbons and a heavy hydrocarbon stream comprising at least C6+ hydrocarbons and c) subjecting the heavy hydrocarbon stream to second hydrocracking to produce a second hydrocracking product stream comprising BTX, wherein the second hydrocracking is more severe than the first hydrocracking, wherein at least part of the middle hydrocarbon stream is recycled back to the first hydrocracking in step a).
摘要翻译：本发明涉及一种生产LPG和BTX的方法，其包括：a）在第一加氢裂化催化剂存在下使混合烃进料流进行第一加氢裂化以产生第一加氢裂化产物流; b）分离第一加氢裂化产物流以提供至少包含至少C 2和C 3烃的轻质烃流，包含C 4和/或C 5烃的中间烃流和包含至少C 6 +烃的重质烃流，和c）重烃流进行第二加氢裂化以产生包含BTX的第二加氢裂化产物流，其中第二加氢裂化比第一加氢裂化更严格，其中在步骤a）中至少部分中间烃流被循环回第一加氢裂化。

113. 发明申请

WO2016102248A1 PROCESS FOR PRODUCING C2 AND C3 HYDROCARBONS 审中-公开
标题翻译：生产C2和C3烃的方法
公开(公告)号：WO2016102248A1
公开(公告)日：2016-06-30
申请号：PCT/EP2015/079821
申请日：2015-12-15
申请人： SABIC GLOBAL TECHNOLOGIES B.V.
发明人： OPRINS, Arno Johannes Maria , DAVIES, Andrew , WARD, Andrew Mark , WONG, Kae Shin , ARAMBURO, Luis , VAN IERSEL, Maikel
IPC分类号： C10G65/00 , C10G65/10 , C10G65/18
CPC分类号： C10G65/10 , C10G65/00 , C10G65/18 , C10G2400/20 , C10G2400/26 , C10G2400/28 , C10G2400/30
摘要： The invention relates to a process for producing C2 and C3 hydrocarbons, comprising a) subjecting a mixed hydrocarbon feedstream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; b) separating the first hydrocracking product stream to provide a light hydrocarbon stream comprising C4- hydrocarbons and c) subjecting the light hydrocarbon stream to C4 hydrocracking in the presence of a C4 hydrocracking catalyst to obtain a C4 hydrocracking product stream comprising C2 and C3 hydrocarbons.
摘要翻译：本发明涉及一种生产C2和C3烃的方法，包括a）在第一加氢裂化催化剂存在下使混合烃进料流进行第一加氢裂化以产生第一加氢裂化产物流; b）分离第一加氢裂化产物流以提供包含C4-烃的轻质烃流，和c）在C4加氢裂化催化剂存在下使轻质烃物流进行C4加氢裂化以得到包含C 2和C 3烃的C 4加氢裂化产物流。

114. 发明申请

WO2016102247A1 PROCESS FOR PRODUCING C2 AND C3 HYDROCARBONS 审中-公开
标题翻译：生产C2和C3烃的方法
公开(公告)号：WO2016102247A1
公开(公告)日：2016-06-30
申请号：PCT/EP2015/079818
申请日：2015-12-15
申请人： SABIC GLOBAL TECHNOLOGIES B.V.
发明人： OPRINS, Arno, Johannes, Maria , DAVIES, Andrew , WARD, Andrew, Mark , WONG, M Kae Shin , ARAMBURO, Luis , MAIKEL, Van Iersel
IPC分类号： C10G65/00 , C10G65/10 , C10G65/18
CPC分类号： C10G65/18 , C10G47/20 , C10G65/00 , C10G65/10 , C10G2300/1048 , C10G2400/20 , C10G2400/26 , C10G2400/28
摘要： The invention relates to a process for producing C2 and C3 hydrocarbons, comprising a) subjecting a mixed hydrocarbon stream to first hydrocracking in the presence of a first hydrocracking catalyst to produce a first hydrocracking product stream; and b) subjecting the first hydrocarbon product stream to C4 hydrocracking optimized for converting C4 hydrocarbons into C3 hydrocarbons in the presence of a C4 hydrocracking catalyst to obtain a C4 hydrocracking product stream comprising C2 and C3 hydrocarbons.
摘要翻译：本发明涉及一种生产C2和C3烃的方法，包括：a）在第一加氢裂化催化剂存在下使混合烃物流进行第一加氢裂化以产生第一加氢裂化产物流; 和b）在C4加氢裂化催化剂存在下使第一烃产物流经C4优化用于将C 4烃转化为C 3烃的C4加氢裂化，得到包含C 2和C 3烃的C 4加氢裂化产物流。

115. 发明申请

WO2016019403A2 PRODUCTION OF OILFIELD HYDROCARBONS 审中-公开
标题翻译：生产油田油气
公开(公告)号：WO2016019403A2
公开(公告)日：2016-02-04
申请号：PCT/ZA2015/050002
申请日：2015-07-22
申请人： SASOL TECHNOLOGY PROPRIETARY LIMITED
发明人： DE WET, Ewald, Watermeyer
CPC分类号： C10G57/00 , C10G47/00 , C10G57/02 , C10G65/00 , C10G65/12 , C10G65/14 , C10G2300/1022
摘要： A process (20) to produce olefinic products suitable for use as or conversion to oilfield hydrocarbons includes separating (42) an olefins-containing Fischer-Tropsch condensate (64) into a light fraction (68), an intermediate fraction (82) and a heavy fraction (94), oligomerising (44) at least a portion of the light fraction (68) to produce a first olefinic product (72) which includes branched internal olefins, and carrying out either one or both of the steps of (i) dehydrogenating (50) at least a portion of the intermediate fraction (82) to produce an intermediate product (84) which includes internal olefins and alpha-olefins, and synthesising (52) higher olefins from the intermediate product which includes internal olefins and alpha-olefins to produce a second olefinic product (86), and (ii) dimerising (52) at least a portion of the intermediate fraction to produce a second olefinic product (86). At least a portion of the heavy fraction (94) is dehydrogenated (58) to produce a third olefinic product (96) which includes internal olefins. Also provided is a process (30) to produce paraffinic products suitable for use as or conversion to oilfield hydrocarbons which includes separating (110) a Fischer-Tropsch wax (124) into at least a lighter fraction (126, 128) and a heavier fraction (130), hydrocracking (120) the heavier fraction (130) to provide a cracked intermediate (144), and separating (122) the cracked intermediate (144) into at least a naphtha fraction (148), a heavier than naphtha paraffinic distillate fraction (150) suitable for use as or conversion to oilfield hydrocarbons, and a bottoms fraction (152) which is heavier than the paraffinic distillate fraction (150).
摘要翻译：制备适用于或转化为油田烃的烯烃产物的方法（20）包括将含烯烃的费 - 托缩合物（64）（42）分离成轻馏分（68），中间馏分（82）和重馏分（94），低聚（44）轻馏分（68）的至少一部分以产生包含支链内烯烃的第一烯烃产物（72），并且执行以下步骤之一或两者：（i）使中间馏分（82）的至少一部分脱氢（50）以产生包括内烯烃和α-烯烃的中间产物（84），并从中间产物合成（52）高级烯烃，其包括内烯烃和α-烯烃，烯烃以产生第二烯烃产物（86），和（ii）将所述中间馏分的至少一部分二聚化（52）以产生第二烯烃产物（86）。重馏分（94）的至少一部分被脱氢（58）以产生包含内烯烃的第三烯烃产物（96）。还提供了一种生产适合用作或转化成油田烃的链烷烃产物的方法（30），其包括将费 - 托蜡（124）分成至少较轻馏分（126,128）和较重馏分（130），加氢裂化（120）较重的馏分（130）以提供裂化的中间体（144），并将裂解的中间体（144）分离成至少一个比石脑油石蜡馏分重的至少一个石脑油馏分（148）适用于或转化为油田碳氢化合物的级分（150）和比石蜡馏分馏分（150）重的塔底馏分（152）。

116. 发明申请

WO2015114008A1 CONVERSION OF BIOMASS OR RESIDUAL WASTE MATERIAL TO BIOFUELS 审中-公开
标题翻译：生物量或残留废物转化为生物燃料
公开(公告)号：WO2015114008A1
公开(公告)日：2015-08-06
申请号：PCT/EP2015/051709
申请日：2015-01-28
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： URADE, Vikrant, Nanasaheb , DEL PAGGIO, Alan, Anthony , PANCHAGNULA, Madhusudhan, Rao , CHILKOOR SOUNDARARAJAN, Laxmi, Narasimhan , GOPAL, Srikant
IPC分类号： C10G45/44 , C10G3/00
CPC分类号： C10G3/50 , C10G3/42 , C10G3/44 , C10G45/44 , C10G65/00 , C10G2300/1014 , C10G2300/202 , C10G2400/04 , Y02P30/20
摘要： The present invention provides a process for producing liquid hydrocarbon products from solid biomass and/or residual waste feedstocks, said process comprising the steps of : a) hydropyrolysing the solid feedstock in a hydropyrolysis reactor vessel in the presence of molecular hydrogen and one or more deoxygenation catalyst, producing a product stream comprising partially deoxygenated hydropyrolysis product, H 2 O, H 2 , CO 2 , CO, C 1 - C 3 gases, char and catalyst fines; b) removing said char and catalyst fines from said product stream; c) hydroconverting said partially deoxygenated hydropyrolysis product in a hydroconversion reactor vessel in the presence of one or more hydroconversion catalyst and of the H 2 O, CO 2 , CO, H 2 , and C 1 - C 3 gas generated in step a), producing a vapour phase product comprising substantially fully deoxygenated hydrocarbon product, H 2 O, CO, CO 2 , and C 1 - C 3 gases; d) condensing the vapour phase product of step d) to provide a liquid phase product comprising substantially fully deoxygenated C4+ hydrocarbon liquid and aqueous material and separating said liquid phase product from a gas phase product comprising H 2 , CO, CO 2 , and C 1 - C 3 gases; e) removing the aqueous material from the substantially fully deoxygenated C4+ hydrocarbon liquid; and f) hydroprocessing at least a portion of the substantially fully deoxygenated C4+ hydrocarbon liquid in a hydroprocessing reactor vessel in the presence of hydrogen and one or more hydroprocessing catalysts, each hydroprocessing catalyst comprising at least one reduced metal on a solid support, in order to provide an upgraded liquid hydrocarbon stream.
摘要翻译：本发明提供了一种从固体生物质和/或残余废物原料生产液体烃产物的方法，所述方法包括以下步骤：a）在分子氢和一种或多种脱氧剂的存在下在加氢热解反应器容器中氢化热解固体原料催化剂，产生包含部分脱氧加氢热解产物H 2 O，H 2，CO 2，CO，C 1 -C 3气体，炭和催化剂细粉的产物流; b）从所述产品流中除去所述焦炭和催化剂细粉; c）在一种或多种加氢转化催化剂和步骤a）中产生的H 2 O，CO 2，CO，H 2和C 1 -C 3气体的存在下，在加氢转化反应器容器中加氢转化所述部分脱氧加氢热解产物，产生包含基本上完全脱氧的烃产物，H 2 O，CO，CO 2和C 1 -C 3气体; d）冷凝步骤d）的气相产物以提供包含基本上完全脱氧的C4 +烃液体和水性材料的液相产物，并将所述液相产物与包含H 2，CO，CO 2和C 1 -C 3气体的气相产物分离 ; e）从基本上完全脱氧的C4 +烃液体中除去水性物质; 以及f）在氢气和一种或多种加氢处理催化剂的存在下，在加氢处理反应器容器中加氢处理基本上完全脱氧的C4 +烃液体的至少一部分，每种加氢处理催化剂在固体载体上包含至少一种还原金属，以便提供一种升级后的液态烃流。

117. 发明申请

WO2015077390A1 A PROCESS FOR THE CATALYTIC CONVERSION OF MICRO CARBON RESIDUE CONTENT OF HEAVY HYDROCARBON FEEDSTOCKS AND A LOW SURFACE AREA CATALYST COMPOSITION FOR USE THEREIN 审中-公开
标题翻译：一种重油碳氢化合物微量碳含量的催化转化方法及其低表面积催化剂组合物的使用方法
公开(公告)号：WO2015077390A1
公开(公告)日：2015-05-28
申请号：PCT/US2014/066493
申请日：2014-11-20
申请人： SHELL OIL COMPANY , SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
发明人： GINESTRA, Josiane Marie-Rose , SHERWOOD, David Edward , KOMAR, David Andrew
IPC分类号： C10G45/08 , B01J37/08 , B01J23/883 , B01J27/19 , B01J35/10 , B01J37/00 , C10G45/60 , C10G47/04
CPC分类号： B01J27/19 , B01J35/1019 , B01J35/1061 , B01J35/108 , B01J37/0009 , C10G45/08 , C10G45/60 , C10G47/04 , C10G65/00
摘要： An improved process for the hydroconversion of micro carbon residue content of heavy hydrocarbon feedstocks by the use of a catalyst composition that is especially useful in the conversion of micro carbon residue of such feedstocks. The catalyst composition is a low surface area composition that further has a specifically define pore structure the combination of which provides for its enhance micro carbon residue conversion property.
摘要翻译：通过使用特别可用于转化这些原料的微量碳残余物的催化剂组合物来改进重质烃原料的微量碳残余物含量的改进方法。催化剂组合物是低表面积组合物，其进一步具有特别限定的孔结构，其组合提供其增强的微碳残余物转化性质。

118. 发明申请

WO2015001520A1 PROCESS FOR THE REFINING OF CRUDE OIL 审中-公开
标题翻译：原油精炼工艺
公开(公告)号：WO2015001520A1
公开(公告)日：2015-01-08
申请号：PCT/IB2014/062855
申请日：2014-07-04
申请人： ENI S.P.A.
发明人： BELLUSSI, Giuseppe , PICCOLO, Vincenzo , MALANDRINO, Alberto Maria Antonio , FABIO, Valentina , RISPOLI, Giacomo Fernando
IPC分类号： C10G45/02 , C10G47/26 , C10G49/12 , C10G65/12 , C10G65/14 , C10G65/16 , C10G7/00 , C10G7/06
CPC分类号： C10G65/00 , C10G7/00 , C10G7/06 , C10G45/02 , C10G47/26 , C10G49/12 , C10G65/12 , C10G65/14 , C10G65/16 , C10G2300/202 , C10G2300/308
摘要： Process for the refining of crude oil comprising at least one atmospheric distillation unit for separating the various fractions, a sub-atmospheric distillation unit, a conversion unit of the heavy fractions obtained, a unit for enhancing the quality of some of the fractions obtained by actions on the chemical composition of their constituents and a unit for the removal of undesired components, characterized in that the sub-atmospheric distillation residue is sent to one of the conversion units, said conversion unit comprises at least one hydroconversion reactor in slurry phase, into which hydrogen or a mixture of hydrogen and ¾S, is fed, in the presence of a suitable dispersed hydrogenation catalyst with dimensions ranging from 1 nanometer to 30 microns.
摘要翻译：用于精炼原油的方法包括至少一个用于分离各种馏分的常压蒸馏装置，亚常压蒸馏装置，所得重馏分的转化装置，用于提高通过动作获得的一些馏分的质量的装置关于其组分的化学组成和用于除去不期望的组分的单元，其特征在于，将所述次大气压蒸馏残余物送入一个转化单元，所述转化单元包含至少一个浆料相中的加氢转化反应器，其中氢或氢和¾S的混合物在适当的分散氢化催化剂存在下进料，其尺寸范围为1纳米至30微米。

119. 发明申请

WO2014149247A1 HYDROPROCESSING THERMALLY CRACKED PRODUCTS 审中-公开
标题翻译：氢化热裂纹产品
公开(公告)号：WO2014149247A1
公开(公告)日：2014-09-25
申请号：PCT/US2014/015907
申请日：2014-02-12
申请人： LUMMUS TECHNOLOGY INC.
发明人： ARORA, Arun , MUKHERJEE, Ujjal, K. , LOUIE, Wai Seung , GREENE, Marvin, I.
IPC分类号： C10G65/02 , C10L1/14
CPC分类号： C10G65/10 , C10G65/00 , C10G65/12 , C10G65/18 , C10G2300/1059 , C10G2400/02 , C10G2400/04 , C10L1/04 , C10L1/06 , C10L1/08
摘要： Embodiments herein relate to a process flow scheme for the processing of gas oils and especially reactive gas oils produced by thermal cracking of residua using a split flow concept. The split flow concepts disclosed allow optimization of the hydrocracking reactor severities and thereby take advantage of the different reactivities of thermally cracked gas oils versus those of virgin gas oils. This results in a lower cost facility for producing base oils as well as diesel, kerosene and gasoline fuels while achieving high conversions and high catalyst lives.
摘要翻译：本文的实施方案涉及用于使用分流式概念处理残油的热油裂解产生的瓦斯油，特别是反应性瓦斯油的工艺流程。所公开的分流流概念允许优化加氢裂化反应器严重性，从而利用热裂解瓦斯油与原始瓦斯油的反应性不同。这导致用于生产基础油以及柴油，煤油和汽油燃料的低成本设备，同时实现高转化率和高催化剂寿命。

120. 发明申请

WO2014095815A1 INTEGRATED GAS-TO-LIQUID CONDENSATE PROCESS 审中-公开
标题翻译：集成的气体 - 液体冷凝过程
公开(公告)号：WO2014095815A1
公开(公告)日：2014-06-26
申请号：PCT/EP2013/076839
申请日：2013-12-17
申请人： SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V. , SHELL OIL COMPANY
发明人： HOEK, Arend , SCHOLTEN, Wilhelmus Johannes Franciscus , AL-SHARSHANI, Ali Mohammed Ali Shahab
IPC分类号： C10G2/00 , C10G65/00 , C10G45/02 , C10G47/00 , C10G65/14 , C10G65/02
CPC分类号： C10G2/332 , C01B3/34 , C01B2203/0216 , C01B2203/0255 , C01B2203/062 , C01B2203/1241 , C10G45/02 , C10G47/00 , C10G65/00 , C10G65/02 , C10G65/14 , C10G67/00 , C10L1/04 , C10L1/06 , C10L1/08 , C10L2200/0492 , C10L2270/023 , C10L2270/026 , C10L2290/42 , C10L2290/543
摘要： A process is provided to prepare middle distillates products, the process at least comprising the following steps : (a) providing a feed stream comprising a natural gas and a condensate and separating the feed stream into a natural gas feed stream and a condensate feed stream; (b) preparing a mixture of carbon monoxide and hydrogen from the natural gas feed stream obtained in step (a); (c) preparing a paraffin product stream by performing a Fischer-Tropsch reaction using carbon monoxide and hydrogen obtained in step (b); (d) separating the paraffin product stream of step (c), thereby obtaining a heavy Fischer-Tropsch product stream comprising hydrocarbons of C20 and above including the majority of the paraffinic wax components of the Fischer-Tropsch reaction in step (c) and a light Fischer- Tropsch product stream comprising hydrocarbons with a distribution in the range C5 to C20; (e) separating the light Fischer-Tropsch product of step (d), thereby obtaining a first paraffinic product fraction having hydrocarbons in the range from C5 to C8, a second paraffinic product fraction having hydrocarbons in the range from C9 to C13, and a third paraffinic product fraction having hydrocarbons in the range from C14 to C20; (f) subjecting the heavy Fischer-Tropsch product stream of step (d) to a hydrocracking/hydroisomerization step thereby obtaining an at least isomerised Fischer- Tropsch product stream; (g) hydrotreating the condensate feed stream of step (a) and the first product fraction of step (e), thereby obtaining a hydrotreated product stream; (h) combining the at least isomerised Fischer- Tropsch product stream of step (f) with the hydrotreated product stream of step (g) to provide a distillate feed stream; and (i) performing a distillation step on the distillate feed stream, wherein the distillation step provides for isolation of middle distillate products; wherein the steps (b), (c) and (f) occur substantially concurrently with step (g).
摘要翻译：提供了一种制备中间馏分产物的方法，该方法至少包括以下步骤：（a）提供包含天然气和冷凝物的进料流，并将进料流分离成天然气进料流和冷凝物进料流; （b）从步骤（a）中获得的天然气进料流中制备一氧化碳和氢气的混合物; （c）通过使用步骤（b）中获得的一氧化碳和氢进行费 - 托反应来制备石蜡产物流; （d）分离步骤（c）的链烷烃产物流，从而得到包含C20及以上烃的重的费 - 托产物流包括步骤（c）中费 - 托反应的大部分链烷烃蜡组分和轻的费 - 托产物流，其包含分布在C5至C20范围内的烃; （e）分离步骤（d）的光费 - 托产物，从而得到具有C5至C8范围内的烃的第一链烷烃产物级分，具有C 9至C 13的烃的第二链烷烃产物馏分和具有C14至C20范围内的烃的第三链烷烃产物级分; （f）使步骤（d）的重费 - 托产物物流进行加氢裂化/加氢异构化步骤，从而获得至少异构化的费 - 托产物流; （g）加氢处理步骤（a）和步骤（e）的第一产物级分的冷凝物进料流，从而获得加氢处理的产物流; （h）将步骤（f）的至少异构化的费 - 托产物流与步骤（g）的加氢处理产物流混合以提供馏出物进料流; 和（i）对所述馏出物进料流进行蒸馏步骤，其中所述蒸馏步骤提供中间馏分产物的分离; 其中步骤（b），（c）和（f）基本上与步骤（g）同时发生。

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