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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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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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公开(公告)号：US08632673B2
公开(公告)日：2014-01-21
申请号：US12324418
申请日：2008-11-26
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： 通过在包括氢脱金属部分和加氢脱硫部分的两步法中处理酸性原油来提炼酸性原油的连续方法，两者都以可置换的方式构造，以优化操作条件和 催化剂寿命产生具有低硫和低有机金属杂质的高价值原油。
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4.发明申请Prerefining Process for the Hydrodesulfurization of Heavy Sour Crude Oils to Produce Sweeter Lighter Crudes Using Moving Catalyst System 审中-公开使用移动催化剂体系重酸原油加氢脱硫生产高温轻质原油的预精炼工艺公开(公告)号：US20100018904A1
公开(公告)日：2010-01-28
申请号：US12502590
申请日：2009-07-14
IPC分类号： C10G45/00
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。
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公开(公告)号：US20090139902A1
公开(公告)日：2009-06-04
申请号：US12324418
申请日：2008-11-26
IPC分类号： C10G29/16
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： 通过在包括氢脱金属部分和加氢脱硫部分的两步法中处理酸性原油来提炼酸性原油的连续方法，两者都以可置换的方式构造，以优化操作条件和 催化剂寿命产生具有低硫和低有机金属杂质的高价值原油。
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6.发明授权Process for the sequential hydroconversion and hydrodesulfurization of whole crude oil 有权整个原油顺序加氢转化和加氢脱硫的方法公开(公告)号：US08372267B2
公开(公告)日：2013-02-12
申请号：US12501300
申请日：2009-07-10
IPC分类号： C10G65/00
CPC分类号： B01J35/109 , B01J23/20 , B01J23/26 , B01J23/74 , B01J23/85 , B01J23/883 , B01J23/888 , B01J23/8885 , B01J35/1061 , C10G45/04 , C10G47/02 , C10G65/12
摘要： The invention relates to a method for removing sulfur from crude oils using a catalytic hydrotreating process operating at moderate temperature and pressure and reduced hydrogen consumption. The process produces sweet crude oil having a sulfur content of between about 0.1 and 1.0 wt % in addition to reduced crude density. The method employs least two reactors in series, wherein the first reactor includes a hydroconversion catalyst and the second reactor includes a desulfurization catalyst.
摘要翻译： 本发明涉及使用在中等温度和高压下操作并降低氢消耗的催化加氢处理方法从原油中除去硫的方法。 该方法除了降低粗密度外，还产生硫含量在约0.1至1.0重量％之间的甜油。 该方法采用串联的最少两个反应器，其中第一反应器包括加氢转化催化剂，第二反应器包括脱硫催化剂。
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7.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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8.发明申请Process for the Sequential Hydroconversion and Hydrodesulfurization of Whole Crude Oil 有权整个原油的顺序加氢转化和加氢脱硫工艺公开(公告)号：US20100025293A1
公开(公告)日：2010-02-04
申请号：US12501300
申请日：2009-07-10
IPC分类号： C10G65/00
CPC分类号： B01J35/109 , B01J23/20 , B01J23/26 , B01J23/74 , B01J23/85 , B01J23/883 , B01J23/888 , B01J23/8885 , B01J35/1061 , C10G45/04 , C10G47/02 , C10G65/12
摘要： The invention relates to a method for removing sulfur from crude oils using a catalytic hydrotreating process operating at moderate temperature and pressure and reduced hydrogen consumption. The process produces sweet crude oil having a sulfur content of between about 0.1 and 1.0 wt % in addition to reduced crude density. The method employs least two reactors in series, wherein the first reactor includes a hydroconversion catalyst and the second reactor includes a desulfurization catalyst.
摘要翻译： 本发明涉及使用在中等温度和高压下操作并降低氢消耗的催化加氢处理方法从原油中除去硫的方法。 该方法除了降低粗密度外，还产生硫含量在约0.1至1.0重量％之间的甜油。 该方法采用串联的最少两个反应器，其中第一反应器包括加氢转化催化剂，第二反应器包括脱硫催化剂。
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9.发明申请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：US20100025291A1
公开(公告)日：2010-02-04
申请号：US12502357
申请日：2009-07-14
IPC分类号： C10G45/00
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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10.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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