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1.发明授权Process for the treatment of heavy oils using light hydrocarbon components as a diluent 有权使用轻烃组分作为稀释剂处理重油的方法公开(公告)号：US09260671B2
公开(公告)日：2016-02-16
申请号：US12502357
申请日：2009-07-14
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。
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2.发明授权Integrated hydroprocessing, steam pyrolysis and catalytic cracking process to produce petrochemicals from crude oil 有权综合加氢处理，蒸汽热解和催化裂化过程，从原油生产石化产品公开(公告)号：US09228140B2
公开(公告)日：2016-01-05
申请号：US13847945
申请日：2013-03-20
IPC分类号： C10G69/06 , C10G51/06 , C10G51/04 , C10G45/00 , C10G47/00 , C10G51/02 , C10G55/04 , C10G55/06 , C10G69/04 , C10G9/16 , C10G11/00 , C10G49/00 , C10G67/10 , C10G69/00 , C10G9/00 , C10G9/14
CPC分类号： C10G69/06 , C10G9/16 , C10G11/00 , C10G45/00 , C10G47/00 , C10G49/007 , C10G51/02 , C10G51/04 , C10G51/06 , C10G55/04 , C10G55/06 , C10G67/10 , C10G69/00 , C10G69/04 , C10G2300/201 , C10G2300/308 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： An integrated hydrotreating, steam pyrolysis and catalytic cracking process for the production of olefins and aromatic petrochemicals from a crude oil feedstock is provided. Crude oil and hydrogen are charged to a hydroprocessing zone 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 are catalytically cracked, 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. Catalytically cracked products are produced, which are combined with the mixed product stream and the combined stream is separated, and olefins and aromatics are recovered as product streams.
摘要翻译： 提供了一种用于从原油原料生产烯烃和芳族石油化工的综合加氢处理，蒸汽热解和催化裂化方法。 在有效地产生加氢处理的流出物的条件下，将原油和氢气加入加氢处理区，该加氢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。 重组分被催化裂解，其衍生自一种或多种加氢处理的流出物，蒸汽热解区内的加热流，或混合产物流催化裂解。 产生催化裂化产物，将其与混合产物流混合，并将合并的流分离，并将烯烃和芳族化合物作为产物流回收。
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公开(公告)号：US20130220884A1
公开(公告)日：2013-08-29
申请号：US13865050
申请日：2013-04-17
IPC分类号： C10G69/06
CPC分类号： C10G69/06 , C10G9/36 , C10G21/003 , C10G45/00 , C10G55/04 , C10G67/0463 , C10G2300/201 , C10G2300/308 , C10G2300/4081 , C10G2400/20 , C10G2400/22 , C10G2400/30
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.
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4.发明申请INTEGRATED HYDROTREATING AND STEAM PYROLYSIS PROCESS FOR DIRECT PROCESSING OF A CRUDE OIL 审中-公开用于直接加工原油的综合加氢和蒸汽热解方法公开(公告)号：US20130197285A1
公开(公告)日：2013-08-01
申请号：US13751946
申请日：2013-01-28
申请人： Raheel SHAFI , Julio HASSELMEYER , Abdennour BOURANE , Ibrahim A. ABBA , Abdul Rahman Zafer AKHRAS
发明人： Raheel SHAFI , Julio HASSELMEYER , Abdennour BOURANE , Ibrahim A. ABBA , Abdul Rahman Zafer AKHRAS
IPC分类号： C10G69/06
CPC分类号： C10G69/06 , B01D19/0057 , B01D53/22 , B01D53/526 , B01D2256/16 , B01D2257/7025 , C10G9/16 , C10G45/44 , C10G47/22 , C10G2300/1037 , C10G2300/308 , C10G2300/4075 , C10G2300/42 , C10G2400/20 , C10G2400/30 , Y02C20/20
摘要： An integrated hydrotreating and steam pyrolysis process for the direct processing of a crude oil is provided 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 reduced having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity. Hydroprocessed effluent is thermally cracked in the presence of steam to produce a mixed product stream, which is separated. Hydrogen from the mixed product stream is purified and recycled to the hydroprocessing zone, and olefins and aromatics are recovered from the separated mixed product stream.
摘要翻译： 提供了一种用于直接加工原油的综合加氢处理和蒸汽热解方法，用于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，在有效地产生减少了污染物含量，增加的链烷烃含量，降低的矿山相关指数和增加的美国石油研究所重力的加氢处理流出物的条件下操作。 在蒸汽存在下，加氢处理的流出物被热裂解以产生分离的混合产物流。 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和芳族化合物。
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公开(公告)号：US20110083996A1
公开(公告)日：2011-04-14
申请号：US12819567
申请日：2010-06-21
IPC分类号： C10G65/12
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。
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6.发明授权Integrated hydroprocessing and steam pyrolysis of crude oil to produce light olefins and coke 有权综合加氢处理和蒸汽热解原油生产轻质烯烃和焦炭公开(公告)号：US09228139B2
公开(公告)日：2016-01-05
申请号：US13847918
申请日：2013-03-20
CPC分类号： 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
摘要： 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.
摘要翻译： 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地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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7.发明申请公开(公告)号：US20130233766A1
公开(公告)日：2013-09-12
申请号：US13865032
申请日：2013-04-17
申请人： Raheel SHAFI , Julio HASSELMEYER , Abdennour BOURANE , Ibrahim A. ABBA , Abdul Rahman Zafer AKHRAS
发明人： Raheel SHAFI , Julio HASSELMEYER , Abdennour BOURANE , Ibrahim A. ABBA , Abdul Rahman Zafer AKHRAS
IPC分类号： C10G69/06
CPC分类号： C10G69/06 , C10G9/36 , C10G45/00 , C10G2300/201 , C10G2300/308 , C10G2300/4081 , C10G2400/20 , C10G2400/30
摘要： An integrated hydrotreating and steam pyrolysis process for the direct processing of a crude oil is provided 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 reduced having a reduced content of contaminants, an increased paraffinicity, reduced Bureau of Mines Correlation Index, and an increased American Petroleum Institute gravity. Hydroprocessed effluent is thermally cracked in the presence of steam to produce a mixed product stream, which is separated. Hydrogen from the mixed product stream is purified and recycled to the hydroprocessing zone, and olefins and aromatics are recovered from the separated mixed product stream.
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8.发明申请INTEGRATED HYDROTREATING AND STEAM PYROLYSIS PROCESS INCLUDING HYDROGEN REDISTRIBUTION FOR DIRECT PROCESSING OF A CRUDE OIL 有权一体化加氢和蒸汽热解过程，包括用于直接加工原油的氢再分配公开(公告)号：US20130228495A1
公开(公告)日：2013-09-05
申请号：US13865043
申请日：2013-04-17
IPC分类号： C10G69/06
CPC分类号： C10G69/06 , C10G9/36 , C10G19/00 , C10G45/00 , C10G55/04 , C10G2300/201 , C10G2300/202 , C10G2300/205 , C10G2300/308 , C10G2400/20 , C10G2400/22 , C10G2400/30
摘要： Steam pyrolysis and hydroprocessing are integrated including hydrogen redistribution to permit direct processing of crude oil feedstocks to produce petrochemicals including olefins and aromatics. A feed is initially split into a light portion and a heavy portion, and the heavy portion is hydroprocessed. A hydroprocessed effluent is charged, along with steam, to a convection section of a steam pyrolysis zone. The mixture is heated and passed to a vapor-liquid separation section. A residual portion is removed and light components are charged to a pyrolysis section of the steam pyrolysis zone. A mixed product stream is recovered from the steam pyrolysis zone and it is separated into product including olefins and aromatics.
摘要翻译： 蒸汽热解和加氢处理包括氢再分配，以允许直接加工原油原料以生产包括烯烃和芳烃的石化产品。 进料最初分为轻部分和重部分，重部分进行加氢处理。 将加氢处理的流出物与蒸汽一起装入蒸气热解区的对流段。 将混合物加热并通入气液分离段。 去除残留部分，将轻组分加入到蒸汽热解区的热解段。 从蒸汽热解区回收混合产物流，将其分离成产物，包括烯烃和芳烃。
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9.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
IPC分类号： C10G69/06
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。
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公开(公告)号：US08491779B2
公开(公告)日：2013-07-23
申请号：US12819567
申请日：2010-06-21
IPC分类号： C10G65/12
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。
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