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公开(公告)号：US20110132806A1
公开(公告)日：2011-06-09
申请号：US12908091
申请日：2010-10-20
申请人： Stacey E. Siporin , David Thomas Ferrughelli , Steven S. Lowenthal , Randolph J. Smiley , Alan Roy Katritzky , Bruce R. Cook
发明人： Stacey E. Siporin , David Thomas Ferrughelli , Steven S. Lowenthal , Randolph J. Smiley , Alan Roy Katritzky , Bruce R. Cook
摘要： A method for the removal of nitrogen compounds from FCC feed or from catalytically cracked distillates including FCC cycle oils by using formaldehyde to selectively couple organic heterocyclic nitrogen species in the FCC feed or FCC distillate to form higher boiling coupling products out of the boiling range of FCC distillate. Removal of the nitrogenous compounds improves the operation of subsequent hydrodesulfurization steps needed for the distillate fraction to conform to low sulfur standards. The formaldehyde is preferably used in the form of paraformaldehyde. The reaction between the nitrogenous compounds in the cycle oil fraction with the formaldehyde is conveniently carried out in the cycle oil pumparound circuit of the FCC main column.
摘要翻译： 一种从FCC原料或催化裂化的馏出物（包括FCC循环油）中除去氮化合物的方法，其中使用甲醛选择性地将有机杂环氮物质在FCC进料或FCC馏出物中偶联，以在沸点范围内形成较高沸点的偶联产物 馏出物 去除含氮化合物改善了馏出物馏分所需的随后加氢脱硫步骤的操作以符合低硫标准。 甲醛优选以多聚甲醛的形式使用。 循环油馏分中的含氮化合物与甲醛的反应在FCC主塔的循环油循环回路中方便地进行。
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公开(公告)号：US08673134B2
公开(公告)日：2014-03-18
申请号：US12908091
申请日：2010-10-20
申请人： Stacey E. Siporin , David Thomas Ferrughelli , Steven S. Lowenthal , Randolph J. Smiley , Alan Roy Katritzky , Bruce R. Cook
发明人： Stacey E. Siporin , David Thomas Ferrughelli , Steven S. Lowenthal , Randolph J. Smiley , Alan Roy Katritzky , Bruce R. Cook
IPC分类号： C10G29/24
摘要： A method for the removal of nitrogen compounds from FCC feed or from catalytically cracked distillates including FCC cycle oils by using formaldehyde to selectively couple organic heterocyclic nitrogen species in the FCC feed or FCC distillate to form higher boiling coupling products out of the boiling range of FCC distillate. Removal of the nitrogenous compounds improves the operation of subsequent hydrodesulfurization steps needed for the distillate fraction to conform to low sulfur standards. The formaldehyde is preferably used in the form of paraformaldehyde. The reaction between the nitrogenous compounds in the cycle oil fraction with the formaldehyde is conveniently carried out in the cycle oil pumparound circuit of the FCC main column.
摘要翻译： 一种从FCC原料或催化裂化的馏出物（包括FCC循环油）中除去氮化合物的方法，该方法是使用甲醛选择性地将FCC原料中的有机杂环氮物质或FCC馏出物结合，从而在FCC沸点范围内形成较高沸点的偶联产物 馏出物 去除含氮化合物改善了馏出物馏分所需的随后加氢脱硫步骤的操作以符合低硫标准。 甲醛优选以多聚甲醛的形式使用。 循环油馏分中的含氮化合物与甲醛的反应在FCC主塔的循环油循环回路中方便地进行。
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3.发明申请Process for flexible vacuum gas oil conversion using divided wall fractionation 有权使用分隔壁分级法进行柔性减压瓦斯油转化的工艺公开(公告)号：US20100018896A1
公开(公告)日：2010-01-28
申请号：US12459730
申请日：2009-07-07
申请人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
发明人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
IPC分类号： C10G57/00
CPC分类号： C10G11/18 , B01D3/141 , B01D3/32 , C10G9/00 , C10G2300/1044 , C10G2300/1074 , C10G2300/4081
摘要： This invention relates to a process for the selective conversion of vacuum gas oil. The vacuum gas oil is treated in a two step process. The first is thermal conversion and the second is catalytic cracking of the products of thermal conversion. The product slate can be varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step. The combined products from thermal and catalytic cracking are separated in a divided wall fractionator.
摘要翻译： 本发明涉及真空瓦斯油的选择性转化方法。 减压瓦斯油以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 可以通过改变热和催化裂化步骤中的条件以及通过在裂化步骤中改变催化剂来改变产品板岩。 来自热和催化裂化的组合产物在分壁分馏器中分离。
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公开(公告)号：US08163168B2
公开(公告)日：2012-04-24
申请号：US12459729
申请日：2009-07-07
申请人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
发明人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
IPC分类号： C10G69/04
CPC分类号： C10G69/06 , C10G11/18 , C10G51/04 , C10G69/02 , C10G69/04 , C10G2300/1074 , C10G2300/4081 , C10G2400/02
摘要： The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt %, based on the hydrocarbon feed. The hydrocarbon feed is treated in a two-step process. The first is thermal conversion and the second is catalytic cracking of the products of the thermal conversion. The present invention results in a process for increasing the distillate production from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step.
摘要翻译： 本发明涉及一种基于烃进料选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 本发明导致用于增加用于流化催化裂化装置的烃进料流的馏出物生产的方法。 通过改变热和催化裂化步骤的条件以及通过改变裂化步骤中的催化剂，可进一步改变本发明产生的产品板条。
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公开(公告)号：US20100018895A1
公开(公告)日：2010-01-28
申请号：US12459729
申请日：2009-07-07
申请人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
发明人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
CPC分类号： C10G69/06 , C10G11/18 , C10G51/04 , C10G69/02 , C10G69/04 , C10G2300/1074 , C10G2300/4081 , C10G2400/02
摘要： The present invention relates to a process for the selective conversion of hydrocarbon feed having a Conradson Carbon Residue content of 0 to 6 wt %, based on the hydrocarbon feed. The hydrocarbon feed is treated in a two-step process. The first is thermal conversion and the second is catalytic cracking of the products of the thermal conversion. The present invention results in a process for increasing the distillate production from a hydrocarbon feedstream for a fluid catalytic cracking unit. The resulting product slate from the present invention can be further varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step.
摘要翻译： 本发明涉及一种基于烃进料选择性转化具有0至6重量％的康拉德森碳残余物的烃进料的方法。 烃进料以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 本发明导致用于增加用于流化催化裂化装置的烃进料流的馏出物生产的方法。 通过改变热和催化裂化步骤的条件以及通过改变裂化步骤中的催化剂，可进一步改变本发明产生的产品板条。
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6.发明授权Process for flexible vacuum gas oil conversion using divided wall fractionation 有权使用分隔壁分级的柔性减压瓦斯油转化工艺公开(公告)号：US08168061B2
公开(公告)日：2012-05-01
申请号：US12459730
申请日：2009-07-07
申请人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
发明人： Martin L. Gorbaty , Bruce R. Cook , David T. Ferrughelli , Jason B. English , Steven S. Lowenthal
IPC分类号： C10G69/04
CPC分类号： C10G11/18 , B01D3/141 , B01D3/32 , C10G9/00 , C10G2300/1044 , C10G2300/1074 , C10G2300/4081
摘要： This invention relates to a process for the selective conversion of vacuum gas oil. The vacuum gas oil is treated in a two step process. The first is thermal conversion and the second is catalytic cracking of the products of thermal conversion. The product slate can be varied by changing the conditions in the thermal and catalytic cracking steps as well as by changing the catalyst in the cracking step. The combined products from thermal and catalytic cracking are separated in a divided wall fractionator.
摘要翻译： 本发明涉及真空瓦斯油的选择性转化方法。 减压瓦斯油以两步法处理。 第一种是热转化，第二种是热转化产物的催化裂化。 可以通过改变热和催化裂化步骤中的条件以及通过在裂化步骤中改变催化剂来改变产品板岩。 来自热和催化裂化的组合产物在分壁分馏器中分离。
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公开(公告)号：US07253330B2
公开(公告)日：2007-08-07
申请号：US10425430
申请日：2003-04-29
申请人： Jihad Mohammed Dakka , Hans K. T. Goris , Georges M. K. Mathys , Stephen Harold Brown , Bruce R. Cook
发明人： Jihad Mohammed Dakka , Hans K. T. Goris , Georges M. K. Mathys , Stephen Harold Brown , Bruce R. Cook
CPC分类号： C07C2/12 , C07C11/02 , C07C2529/85
摘要： In a process for oligomerizing an olefinic hydrocarbon feedstock comprising sulfur-containing molecules, the feedstock is contacted in the absence of hydrogen with a first metal oxide catalyst at a temperature in excess of 150° C. and then is contacted under olefin oligomerization conditions with a second catalyst comprising a crystalline molecular sieve, such as ZSM-22 or ZSM-57.
摘要翻译： 在包含含硫分子的烯属烃原料低聚的方法中，原料在不存在氢气的情况下与第一金属氧化物催化剂在超过150℃的温度下接触，然后在烯烃低聚条件下与 第二催化剂包含结晶分子筛，例如ZSM-22或ZSM-57。
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8.发明授权公开(公告)号：US06180842B2
公开(公告)日：2001-01-30
申请号：US09138130
申请日：1998-08-21
IPC分类号： C10L116
CPC分类号： C10L1/08
摘要： A Fischer-Tropsch derived distillate fraction is blended with either a raw virgin condensate fraction or a mildly hydrotreated virgin condensate to obtain a stable inhibited distillate fuel.
摘要翻译： 将费 - 托衍生的馏出物馏分与原始的原始冷凝物馏分或轻度加氢处理的原始冷凝物混合以获得稳定的受抑制的馏出物燃料。
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公开(公告)号：US07244352B2
公开(公告)日：2007-07-17
申请号：US10359860
申请日：2003-02-07
申请人： Thomas R. Halbert , Craig A. McKnight , John P. Greeley , Bruce R. Cook , Garland B. Brignac , Mark A. Greaney , Robert C. Welch
发明人： Thomas R. Halbert , Craig A. McKnight , John P. Greeley , Bruce R. Cook , Garland B. Brignac , Mark A. Greaney , Robert C. Welch
CPC分类号： C10G67/0418 , C10G67/12 , C10L1/02
摘要： A process for producing a naphtha having a decreased amount of sulfur by selective hydroprocessing a petroleum feedstream comprising cracked naphtha to reduce its sulfur content with minimum loss of octane. The reduced sulfur naphtha stream contains mercaptan sulfur reversion products that are removed preferably by use of an aqueous base solution containing a catalytically effective amount of a phase transfer catalyst.
摘要翻译： 通过选择性加氢处理包含裂化石脑油的石油原料流来制造具有减少硫含量的石脑油的方法，以最小的辛烷值损失降低其硫含量。 还原硫石脑油流含有硫醇硫还原产物，其优选通过使用含有催化有效量的相转移催化剂的碱性水溶液来除去。
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10.发明授权Stability Fischer-Tropsch diesel fuel and a process for its production (LAW725) 有权稳定性费 - 托柴油及其生产工艺（LAW725）公开(公告)号：US06755961B1
公开(公告)日：2004-06-29
申请号：US09625249
申请日：2000-07-25
IPC分类号： C10L116
CPC分类号： C10L1/08
摘要： A Fischer-Tropsch derived distillate fraction is blended with either a raw virgin condensate fraction or a mildly hydrotreated virgin condensate to obtain a stable inhibited distillate fuel.
摘要翻译： 将费 - 托衍生的馏出物馏分与原始的原始冷凝物馏分或轻度加氢处理的原始冷凝物混合以获得稳定的受抑制的馏出物燃料。
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