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1. 发明申请

WO2013112968A1 INTEGRATED HYDROTREATING, SOLVENT DEASPHALTING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL 审中-公开
标题翻译：用于直接加工原油的综合加氢，溶剂去除和蒸汽热解方法
公开(公告)号：WO2013112968A1
公开(公告)日：2013-08-01
申请号：PCT/US2013/023335
申请日：2013-01-27
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , BOURANE, Abdennour , SHAFI, Raheel , SAYED, Essam , ABBA, Ibrahim, A. , AKHRAS, Abdul Rahman, Zafer
发明人： BOURANE, Abdennour , SHAFI, Raheel , SAYED, Essam , ABBA, Ibrahim, A. , AKHRAS, Abdul Rahman, Zafer
IPC分类号： C10G9/16 , C10G55/04 , C10G69/06 , B01D53/24 , B01D19/00 , B01D17/02
CPC分类号： C10G69/06 , B01D17/0217 , B01D19/0057 , B01D53/526 , B01D2256/16 , B01D2257/7025 , C10G9/36 , C10G19/00 , C10G21/003 , C10G55/04 , C10G67/0463 , C10G2400/20 , C10G2400/30 , Y02C20/20
摘要： A process is provided that is directed to a steam pyrolysis zone integrated with a hydrotreating zone and a solvent deasphalting zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. The integrated hydrotreating, solvent deasphalting and steam pyrolysis process comprises charging the crude oil to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent reduced having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity; charging the hydroprocessed effluent to a solvent deasphalting zone with an effective amount of solvent to produce a deasphalted and demetalized oil stream and a bottom asphalt phase; thermally cracking the deasphalted and demetalized oil stream in the presence of steam to produce a mixed product stream; separating the mixed product stream; purifying hydrogen recovered from the mixed product stream and recycling it to the hydroprocessing zone; recovering olefins and aromatics from the separated mixed product stream; and recovering pyrolysis fuel oil from the separated mixed product stream.
摘要翻译：提供了一种方法，其涉及与加氢处理区和溶剂脱沥青区整合的蒸汽热解区，以允许原油原料直接加工以生产包括烯烃和芳族化合物的石化产品。综合的加氢处理，溶剂脱沥青和蒸汽热解过程包括将原油装入加氢处理区域，该加氢处理区域有效地产生减少含有污染物含量的加氢处理流出物，增加的链烷烃含量，减少的矿山相关指数和增加的美国石油学院重力; 将加氢处理的流出物用有效量的溶剂装入溶剂脱沥青区，以产生脱沥青和脱金属的油料流和底部沥青相; 在蒸汽存在下对脱沥青和脱金属油流进行热裂解以产生混合产物流; 分离混合产物流; 净化从混合产物流回收的氢并将其再循环到加氢处理区; 从分离的混合产物流中回收烯烃和芳族化合物; 并从分离的混合产物流中回收热解燃料油。

2. 发明申请

WO2011005476A2 ALTERNATIVE PROCESS FOR THE TREATMENT OF HEAVY CRUDES IN A COKING REFINERY 审中-公开
标题翻译：用于处理炼焦炼油厂重金属的替代方法
公开(公告)号：WO2011005476A2
公开(公告)日：2011-01-13
申请号：PCT/US2010/039332
申请日：2010-06-21
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , SHAFI, Raheel , HAMAD, Esam, Z. , KRESSMANN, Stephane, Cyrille , MOSES, Julio, Hasselmeyer
发明人： SHAFI, Raheel , HAMAD, Esam, Z. , KRESSMANN, Stephane, Cyrille , MOSES, Julio, Hasselmeyer
IPC分类号： C10G69/06
CPC分类号： C10G69/06 , C10G2300/1033 , C10G2300/202 , C10G2300/205 , C10G2300/206 , C10G2300/308 , C10G2300/4006 , C10G2300/4081
摘要： The present invention relates to a process for the pretreatment of heavy oils using a catalytic hydrotreating process prior to introduction to a refinery. More specifically, the invention relates to the use of an HDM reactor and an HDS reactor in order to improve the characteristics of the heavy oil, such that when the oil is introduced into the refinery, the refinery can achieve improved throughputs, increased catalysts life, increased life cycles, and a reduction in overall operation costs.
摘要翻译：本发明涉及在引入炼油厂之前使用催化加氢处理方法预处理重油的方法。更具体地，本发明涉及HDM反应器和HDS反应器的用途，以改善重油的特性，使得当油被引入炼油厂时，炼油厂可以实现提高的生产量，增加的催化剂寿命，增加生命周期，降低整体运营成本。

3. 发明申请

WO2010009082A1 A PREREFINING PROCESS FOR THE HYDRODESULFURIZATION OF HEAVY SOUR CRUDE OILS TO PRODUCE SWEETER LIGHTER CRUDES USING MOVING CATALYST SYSTEM 审中-公开
标题翻译：用于使用移动催化剂体系来制造重要的发光体的重油原油的预处理方法
公开(公告)号：WO2010009082A1
公开(公告)日：2010-01-21
申请号：PCT/US2009/050473
申请日：2009-07-14
申请人： SAUDI ARABIAN OIL COMPANY , SHAFI, Raheel , HAMAD, Esam, Z. , KRESSMANN, Stephane, Cyrille , ALZAID, Ali, Hussain
发明人： SHAFI, Raheel , HAMAD, Esam, Z. , KRESSMANN, Stephane, Cyrille , ALZAID, Ali, Hussain
IPC分类号： C10G65/12 , C10G45/18 , C10G47/28
CPC分类号： C10G65/12 , C10G45/18 , C10G47/28
摘要： A pre-refining catalytic hydrotreating process for the desulfurization, demetallization, and upgrading of heavy, sour crude oils operating at a moderate temperature and pressure through the utilization of moving catalyst bed technology.
摘要翻译：一种预处理催化加氢处理方法，用于通过利用移动催化剂床技术在适度的温度和压力下进行脱硫，脱金属和升级的重质酸性原油。

4. 发明申请

WO2009073436A3 PROCESS FOR CATALYTIC HYDROTREATING OF SOUR CRUDE OILS 审中-公开
标题翻译：用于原油原油催化加氢处理的方法
公开(公告)号：WO2009073436A3
公开(公告)日：2009-10-29
申请号：PCT/US2008084513
申请日：2008-11-24
申请人： SAUDI ARABIAN OIL CO , KRESSMANN STEPHANE CYRILLE , SHAFI RAHEEL , HAMAD ESAM Z , DABBOUSI BASHIR OSAMA , ARAMCO SERVICES CO
发明人： KRESSMANN STEPHANE CYRILLE , SHAFI RAHEEL , HAMAD ESAM Z , DABBOUSI BASHIR OSAMA
IPC分类号： B01J8/04 , C10G45/02 , C10G65/04
CPC分类号： C10G65/04 , B01J2219/00038 , C10G45/02 , C10G49/002 , C10G65/12
摘要： A continuous process for upgrading sour crude oil by treating the sour crude oil in a two step process that includes a hydro-demetallization section and a hydro-desulfurization section, both of which are constructed in a permutable fashion so as to optimize the operating conditions and catalyst lifespan to produce a high value crude oil having low sulfur and low organometallic impurities.
摘要翻译：通过两步处理包括加氢脱金属段和加氢脱硫段的两步法处理含硫原油的连续工艺，二者均以可置换的方式构造，以优化操作条件并且催化剂寿命以生产具有低硫和低有机金属杂质的高价值原油。

5. 发明申请

WO2015084779A1 INTEGRATED SOLVENT-DEASPHALTING AND FLUID CATALYTIC CRACKING PROCESS FOR LIGHT OLEFIN PRODUCTION 审中-公开
标题翻译：用于轻油生产的综合溶剂 - 去除和流体催化裂化工艺
公开(公告)号：WO2015084779A1
公开(公告)日：2015-06-11
申请号：PCT/US2014/068034
申请日：2014-12-02
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , SHAFI, Raheel , BOURANE, Abdennour , AL-GHRAMI, Musaed, Salem , ABUDAWOUD, Raed
发明人： SHAFI, Raheel , BOURANE, Abdennour , AL-GHRAMI, Musaed, Salem , ABUDAWOUD, Raed
IPC分类号： C10G55/06 , C10G11/18 , C10G21/00
CPC分类号： C07C4/06 , C07C7/10 , C07C2529/08 , C07C2529/40 , C07C2529/80 , C10G11/18 , C10G21/003 , C10G55/06
摘要： The process described herein broadly comprehends an integrated process that permits the use of straight run residual fractions as a feedstock to produce lighter olefins including propylene. A blend of natural gas condensate and/or naphtha, and heavy oil residue(s), is catalytically cracked to produce a light olefin-rich product stream. In particular, the light natural gas condensate and/or naphtha stream is used as both solvent in a solvent-deasphalting unit and a portion for the feedstock to a fluidized catalytic cracking process. In addition, blending a heavy boiling hydrocarbon stream with a light natural gas condensate or naphtha stream enables efficient cracking in fluidized catalytic cracking process processes while sustaining the heat balance within the cracking unit.
摘要翻译：本文所述的方法广泛地包括允许使用直馏残余馏分作为原料来生产包括丙烯的轻质烯烃的综合方法。将天然气冷凝物和/或石脑油与重油残余物的混合物进行催化裂化以产生轻质富烯烃产物流。特别地，轻质天然气冷凝物和/或石脑油流用作溶剂脱沥青单元中的两种溶剂，以及用于原料的部分用于流化催化裂化过程。此外，将重沸腾的烃流与轻质天然气冷凝物或石脑油流混合使得能够在流化催化裂化过程中有效地开裂，同时保持裂化装置内的热平衡。

6. 发明申请

WO2013142563A3 INTEGRATED HYDROPROCESSING AND FLUID CATALYTIC CRACKING FOR PROCESSING OF A CRUDE OIL 审中-公开
标题翻译：原油加工中的一体化加氢处理和流体催化裂化
公开(公告)号：WO2013142563A3
公开(公告)日：2013-12-19
申请号：PCT/US2013033083
申请日：2013-03-20
申请人： SAUDI ARABIAN OIL CO , ARAMCO SERVICES CO , ABBA IBRAHIM A , SHAFI RAHEEL , BOURANE ABDENNOUR , SAYED ESSAM
发明人： ABBA IBRAHIM A , SHAFI RAHEEL , BOURANE ABDENNOUR , SAYED ESSAM
IPC分类号： C10G11/18 , B01J8/18 , C10G51/06 , C10G69/04
CPC分类号： C10G69/04 , C10G11/18 , C10G45/02 , C10G51/06 , C10G2300/70 , C10G2400/20
摘要： An integrated hydroprocessing and fluid catalytic cracking process is provided for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals. Crude oil and hydrogen are charged to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity. The hydroprocessed effluent is separated into a low boiling fraction and a high boiling fraction. The low boiling fraction is cracked in a first downflow reactor of a fluid catalytic cracking unit in the presence of a predetermined amount of catalyst to produce cracked products and spent catalyst, and the high boiling fraction is cracked in a second downflow reactor of the fluid catalytic cracking unit in the presence of a predetermined amount of catalyst to produce cracked products and spent catalyst. Spent catalyst from both the first and second downflow reactors are regenerated in a common regeneration zone, and first and second cracked product streams are recovered.
摘要翻译：提供综合加氢处理和流体催化裂化工艺以直接处理原油以生产烯烃和芳族石油化学品。将原油和氢气加入加氢处理区，该加氢区在有效产生具有降低的污染物含量，增加的链烷烃含量，降低的矿业局相关指数和增加的美国石油学会引力的加氢处理流出物的条件下操作。加氢处理的流出物被分离成低沸点馏分和高沸点馏分。低沸点馏分在预定量的催化剂存在下在流化床催化裂化装置的第一个下流式反应器中裂化，产生裂化产物和废催化剂，高沸点馏分在流化催化剂的第二个下流式反应器中裂化在预定量的催化剂的存在下使裂化单元产生裂化产物和废催化剂。来自第一和第二下流式反应器的废催化剂在共同的再生区中再生，并且回收第一和第二裂化产物流。

7. 发明申请

WO2013142617A1 INTEGRATED HYDROPROCESSING, STEAM PYROLYSIS AND SLURRY HYDROPROCESSING OF CRUDE OIL TO PRODUCE PETROCHEMICALS 审中-公开
标题翻译：一体化水解，蒸汽热解和浆料加氢处理生产石油化工
公开(公告)号：WO2013142617A1
公开(公告)日：2013-09-26
申请号：PCT/US2013/033181
申请日：2013-03-20
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , SAYED, Essam , SHAFI, Raheel , AKHRAS, Abdul Rahman, Zafer , BOURANE, Abdennour , ABBA, Ibrahim, A.
发明人： SAYED, Essam , SHAFI, Raheel , AKHRAS, Abdul Rahman, Zafer , BOURANE, Abdennour , ABBA, Ibrahim, A.
IPC分类号： C10G9/16 , C10G65/08 , C10G65/12 , C10G69/06 , C10G70/02
CPC分类号： C10G69/06 , B01D17/0217 , B01D19/0057 , B01J21/04 , B01J27/051 , B01J27/0515 , B01J35/1014 , B01J35/1042 , B01J35/1047 , B01J35/1061 , C10G9/16 , C10G47/26 , C10G49/12 , C10G65/08 , C10G65/12 , C10G65/14 , C10G69/00 , C10G70/02 , C10G2300/201 , C10G2300/308 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： Crude oil is charged to a hydroprocessing zone in the presence of hydrogen operating under conditions effective to produce a hydroprocessed effluent, which is thermally cracked in the presence of steam in a steam pyrolysis zone to produce a mixed product stream. Heavy components, which are derived from one or more of the hydroprocessed effluent, a heated stream within the steam pyrolysis zone, or the mixed product stream catalytically cracking, are charged to a slurry hydroprocessing zone to produce a slurry intermediate product which is then thermally cracked. Olefins and aromatics are recovered from the separated mixed product stream as product.
摘要翻译：在有效地产生加氢处理流出物的氢气存在下，将原油装入加氢处理区，氢气处理流出物在蒸汽热解区的蒸汽存在下被热裂解以产生混合产物流。来自一种或多种加氢处理流出物，蒸汽热解区内的加热流或混合产物流催化裂化的重质组分被加入到浆料加氢处理区中以产生浆料中间产物，然后热裂化。从作为产品的分离的混合产物流中回收烯烃和芳族化合物。

8. 发明申请

WO2013112966A1 INTEGRATED SOLVENT DEASPHALTING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL 审中-公开
标题翻译：用于直接加工原油的综合溶剂去除和蒸汽热解方法
公开(公告)号：WO2013112966A1
公开(公告)日：2013-08-01
申请号：PCT/US2013/023333
申请日：2013-01-27
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , BOURANE, Abdennour , SHAFI, Raheel , SAYED, Essam , ABBA, Ibrahim, A. , AKHRAS, Abdul Rahman, Zafer
发明人： BOURANE, Abdennour , SHAFI, Raheel , SAYED, Essam , ABBA, Ibrahim, A. , AKHRAS, Abdul Rahman, Zafer
IPC分类号： C10G67/04 , C10G55/04 , C10G9/16 , C10G47/22 , B01D45/12 , C10G21/00 , C10G47/34 , B01D17/02 , B01D19/00 , B01D53/24
CPC分类号： C10G55/04 , C10G9/16 , C10G21/003 , C10G47/22 , C10G47/34 , C10G67/04 , C10G67/049
摘要： A process is provided that is directed to a steam pyrolysis zone integrated with a solvent deasphalting zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. The integrated solvent deasphalting and steam pyrolysis process for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals comprises charging the crude oil to a solvent deasphalting zone with an effective amount of solvent to produce a deasphalted and demetalized oil stream and a bottom asphalt phase; thermally cracking the deasphalted and demetalized oil stream in the presence of steam to produce a mixed product stream; separating the mixed product stream; recovering olefins and aromatics from the separated mixed product stream; and recovering pyrolysis fuel oil from the separated mixed product stream.
摘要翻译：提供了一种方法，其涉及与溶剂脱沥青区一体化的蒸汽热解区，以允许直接处理原油原料以生产包括烯烃和芳族化合物的石化产品。用于直接加工原油以生产烯烃和芳族石油化学品的综合溶剂脱沥青和蒸汽热解方法包括用有效量的溶剂将原油装入溶剂脱沥青区，以产生脱沥青和脱金属油流和底沥青相; 在蒸汽存在下对脱沥青和脱金属精油流进行热裂解以产生混合产物流; 分离混合产物流; 从分离的混合产物流中回收烯烃和芳族化合物; 并从分离的混合产物流中回收热解燃料油。

9. 发明申请

WO2010009077A2 PROCESS FOR THE TREATMENT OF HEAVY OILS USING LIGHT HYDROCARBON COMPONENTS AS A DILUENT 审中-公开
标题翻译：使用光油组分作为稀释剂处理重油的方法
公开(公告)号：WO2010009077A2
公开(公告)日：2010-01-21
申请号：PCT/US2009050466
申请日：2009-07-14
申请人： SAUDI ARABIAN OIL CO , SHAFI RAHEEL , HAMAD ESAM Z , KRESSMANN STEPHANE CYRILLE , ALZAID ALI HUSSAIN
发明人： SHAFI RAHEEL , HAMAD ESAM Z , KRESSMANN STEPHANE CYRILLE , ALZAID ALI HUSSAIN
IPC分类号： C10G65/12
CPC分类号： C10G65/12 , C10G2300/202 , C10G2300/205 , C10G2300/802
摘要： The present invention relates to a process for the treatment of heavy oils using a catalytic hydrotreating process. More specifically, the invention relates to the presence of light hydrocarbon components in conjunction with the heavy oils for improved treatment of the heavy oils utilizing moderate temperature and pressure.
摘要翻译：本发明涉及使用催化加氢处理方法处理重油的方法。更具体地说，本发明涉及轻质烃组分与重油结合的用途，用于利用适度的温度和压力来改进对重油的处理。

10. 发明申请

WO2013142563A2 INTEGRATED HYDROPROCESSING AND FLUID CATALYTIC CRACKING FOR PROCESSING OF A CRUDE OIL 审中-公开
标题翻译：用于加工原油的综合加氢和流体催化裂化
公开(公告)号：WO2013142563A2
公开(公告)日：2013-09-26
申请号：PCT/US2013/033083
申请日：2013-03-20
申请人： SAUDI ARABIAN OIL COMPANY , ARAMCO SERVICES COMPANY , ABBA, Ibrahim, A. , SHAFI, Raheel , BOURANE, Abdennour , SAYED, Essam
发明人： ABBA, Ibrahim, A. , SHAFI, Raheel , BOURANE, Abdennour , SAYED, Essam
IPC分类号： C10G11/18
CPC分类号： C10G69/04 , C10G11/18 , C10G45/02 , C10G51/06 , C10G2300/70 , C10G2400/20
摘要： An integrated hydroprocessing and fluid catalytic cracking process is provided for the direct processing of a crude oil to produce olefinic and aromatic petrochemicals. Crude oil and hydrogen are charged to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity. The hydroprocessed effluent is separated into a low boiling fraction and a high boiling fraction. The low boiling fraction is cracked in a first downflow reactor of a fluid catalytic cracking unit in the presence of a predetermined amount of catalyst to produce cracked products and spent catalyst, and the high boiling fraction is cracked in a second downflow reactor of the fluid catalytic cracking unit in the presence of a predetermined amount of catalyst to produce cracked products and spent catalyst. Spent catalyst from both the first and second downflow reactors are regenerated in a common regeneration zone, and first and second cracked product streams are recovered.
摘要翻译：提供了一种综合的加氢处理和流化催化裂化方法，用于直接加工原油以生产烯烃和芳族石油化学品。将原油和氢气加入加氢处理区，在有效产生具有降低的污染物含量，增加的链烷烃含量，降低矿山相关指数的美国石油协会重力的加氢处理流出物的条件下操作。加氢处理的流出物被分离成低沸点馏分和高沸点馏分。低沸点馏分在流化床催化裂化装置的第一下流式反应器中在预定量的催化剂存在下裂化，产生裂化产物和废催化剂，高沸点馏分在流化催化剂的第二下流反应器中裂化在预定量的催化剂存在下开裂单元以产生裂化产物和废催化剂。来自第一和第二下流式反应器的废催化剂在普通再生区再生，回收第一和第二裂化产物流。

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