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    INTEGRATED HYDROPROCESSING AND FLUID CATALYTIC CRACKING FOR PROCESSING OF A CRUDE OIL
    3.
    发明申请
    INTEGRATED HYDROPROCESSING AND FLUID CATALYTIC CRACKING FOR PROCESSING OF A CRUDE OIL 有权
    用于加工原油的综合加氢和流体催化裂化

    公开(公告)号：US20130248421A1

    公开(公告)日：2013-09-26

    申请号：US13847749

    申请日：2013-03-20

    Applicant: Ibrahim A. ABBA ,  Raheel SHAFI ,  Abdennour BOURANE ,  Essam SAYED

    Inventor： Ibrahim A. ABBA ,  Raheel SHAFI ,  Abdennour BOURANE ,  Essam SAYED

    IPC: C10G69/04 ,  C10G51/06

    CPC classification number: C10G69/04 ,  C10G11/18 ,  C10G45/02 ,  C10G51/06 ,  C10G2300/70 ,  C10G2400/20

    Abstract: 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.

    Abstract translation: 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研究所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。

    INTEGRATED SOLVENT DEASPHALTING, HYDROTREATING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL
    5.
    发明申请
    INTEGRATED SOLVENT DEASPHALTING, HYDROTREATING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL 有权
    用于直接加工原油的集成溶剂去除，加氢和蒸汽热解过程

    公开(公告)号：US20130233768A1

    公开(公告)日：2013-09-12

    申请号：US13865062

    申请日：2013-04-17

    Applicant: Abdennour BOURANE ,  Raheel SHAFI ,  Essam SAYED ,  Ibrahim A. ABBA ,  Abdul Rahman Zafer AKHRAS

    Inventor： Abdennour BOURANE ,  Raheel SHAFI ,  Essam SAYED ,  Ibrahim A. ABBA ,  Abdul Rahman Zafer AKHRAS

    IPC: C10G69/06 ,  C10G67/04

    CPC classification number: C10G55/04 ,  C10G9/36 ,  C10G21/003 ,  C10G45/00 ,  C10G67/0463 ,  C10G67/049 ,  C10G69/06 ,  C10G2300/201 ,  C10G2300/308 ,  C10G2300/4081 ,  C10G2400/20 ,  C10G2400/30

    Abstract: A process is provided that is directed to a steam pyrolysis zone integrated with a solvent deasphalting zone and a hydrotreating zone to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. The integrated solvent deasphalting, hydrotreating 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 for producing a deasphalted and demetalized oil stream and a bottom asphalt phase; charging the deasphalted and demetalized oil stream and hydrogen 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; thermally cracking the hydroprocessed effluent 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.

    Abstract translation: 提供了一种方法，其涉及与溶剂脱沥青区和加氢处理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。 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，加氢处理和蒸汽热解过程包括：用有效量的溶剂将原油装入溶剂脱沥青区，用于产生脱沥青和脱金属的油料流， 底部沥青相; 将脱沥青和脱金属的油流和氢气加氢到加氢处理区，在有效地产生具有降低的污染物含量，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公司重力的加氢处理流出物的条件下操作; 在蒸汽存在下对加氢处理的流出物进行热裂解以产生混合产物流; 分离混合产物流; 净化从混合产物流中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。

    INTEGRATED HYDROTREATING, SOLVENT DEASPHALTING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL
    7.
    发明申请
    INTEGRATED HYDROTREATING, SOLVENT DEASPHALTING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL 审中-公开
    一体化加氢处理，溶剂脱硫和蒸汽热解法直接加工原油

    公开(公告)号：US20130197284A1

    公开(公告)日：2013-08-01

    申请号：US13751646

    申请日：2013-01-28

    Applicant: Abdennour BOURANE ,  Raheel SHAFI ,  Essam SAYED ,  Ibrahim A. ABBA ,  Abdul Rahman Zafer AKHRAS

    Inventor： Abdennour BOURANE ,  Raheel SHAFI ,  Essam SAYED ,  Ibrahim A. ABBA ,  Abdul Rahman Zafer AKHRAS

    IPC: C10G69/06

    CPC classification number: 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

    Abstract: 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.

    Abstract translation: 提供了一种方法，其涉及与加氢处理区和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油化学品。 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，该加氢处理区在有效产生具有降低的污染物含量，降低的污染物含量，降低的矿物相关指数局和减少的矿物相关指数减少的加氢处理流出物的条件下操作 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精油流进行热裂解以产生混合产物流; 分离混合产物流; 净化从混合产物流中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。

    Integrated hydroprocessing and fluid catalytic cracking for processing of a crude oil
    8.
    发明授权
    Integrated hydroprocessing and fluid catalytic cracking for processing of a crude oil 有权
    综合加氢处理和流化催化裂化加工原油

    公开(公告)号：US09096806B2

    公开(公告)日：2015-08-04

    申请号：US13847749

    申请日：2013-03-20

    Applicant: Ibrahim A. Abba ,  Raheel Shafi ,  Abdennour Bourane ,  Essam Sayed

    Inventor： Ibrahim A. Abba ,  Raheel Shafi ,  Abdennour Bourane ,  Essam Sayed

    IPC: C10G69/04 ,  C10G51/06 ,  C10G11/18 ,  C10G45/02 ,  C10G69/14

    CPC classification number: C10G69/04 ,  C10G11/18 ,  C10G45/02 ,  C10G51/06 ,  C10G2300/70 ,  C10G2400/20

    Abstract: 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.

    Abstract translation: 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研究所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。

    INTEGRATED HYDROPROCESSING AND STEAM PYROLYSIS OF CRUDE OIL TO PRODUCE LIGHT OLEFINS AND COKE
    10.
    发明申请
    INTEGRATED HYDROPROCESSING AND STEAM PYROLYSIS OF CRUDE OIL TO PRODUCE LIGHT OLEFINS AND COKE 有权
    原油的氢化和蒸汽热解产生光油和焦炭

    公开(公告)号：US20130248416A1

    公开(公告)日：2013-09-26

    申请号：US13847918

    申请日：2013-03-20

    Applicant: Raheel SHAFI ,  Abdennour BOURANE ,  Abdul Rahman Zafer AKHRAS ,  Essam SAYED ,  Ibrahim A. ABBA

    Inventor： Raheel SHAFI ,  Abdennour BOURANE ,  Abdul Rahman Zafer AKHRAS ,  Essam SAYED ,  Ibrahim A. ABBA

    IPC: C10G69/06 ,  C10G51/06

    CPC classification number: C10G69/06 ,  C10B57/045 ,  C10G9/005 ,  C10G9/16 ,  C10G49/007 ,  C10G51/06 ,  C10G69/00 ,  C10G2300/201 ,  C10G2300/308 ,  C10G2400/20 ,  C10G2400/22 ,  C10G2400/30 ,  Y02P20/132

    Abstract: An integrated hydrotreating, steam pyrolysis and coker process for the direct processing of a crude oil is provided to produce olefinic and aromatic petrochemicals, and petroleum coke. Crude oil and recycled coker liquid product are charged to a hydroprocessing zone operating under conditions effective to produce a hydroprocessed effluent which is thermally cracked in the presence of steam to produce a mixed product stream. The residual liquid fraction recovered upstream of the thermal cracking unit or within the thermal cracking unit is thermally cracked under conditions effective to produce coke and coker liquid product. The coker liquid product is recycled to the step of hydroprocessing while the petroleum coke is recovered. Hydrogen from the mixed product stream is purified and recycled to the hydroprocessing zone, and olefins, aromatics and pyrolysis fuel oil are recovered from the separated mixed product stream.

    Abstract translation: 提供了一种用于直接加工原油的综合加氢处理，蒸汽热解和焦化工艺，以生产烯烃和芳香族石油化学品和石油焦炭。 将原油和再循环焦化液体产物装入加氢处理区，该加氢处理区在有效产生加氢处理流出物的条件下运行，该加氢处理流出物在蒸汽存在下被热裂解以产生混合产物流。 在热裂解单元上游或在热裂解装置中回收的剩余液体馏分在有效生产焦炭和焦化液体产物的条件下被热裂解。 在回收石油焦时，将焦化液体产物再循环至加氢处理步骤。 将来自混合产物流的氢气纯化并再循环至加氢处理区，并从分离的混合产物流中回收烯烃，芳烃和热解燃料油。

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