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公开(公告)号：US08864976B2
公开(公告)日：2014-10-21
申请号：US12157971
申请日：2008-06-13
IPC分类号： C10G73/02 , C10G45/62 , B01J29/74 , B01J29/03 , B01J29/04 , C10G65/08 , B01J35/00 , C10G65/04 , B01J23/44 , B01J21/06 , B01J37/00
CPC分类号： C10G65/043 , B01J21/063 , B01J23/44 , B01J29/0325 , B01J29/043 , B01J29/7461 , B01J35/0026 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C10G45/62 , C10G65/08 , C10G73/02 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/4018 , C10G2400/10
摘要： Integrated hydroprocessing methods using high activity, low density catalysts are provided. The high activity catalysts allow for blocked operation when processing lube range feedstocks of widely varying characteristics, such as wax content, without having to substantially change the configuration or operating conditions of the process train. Instead, the different feedstocks can be accommodated by varying the reaction temperature in the process train.
摘要翻译： 提供了使用高活性，低密度催化剂的综合加氢处理方法。 当处理广泛变化的特性（例如蜡含量）的润滑剂范围原料时，高活性催化剂允许堵塞操作，而不必基本上改变工艺列车的构型或操作条件。 相反，可以通过改变过程列中的反应温度来适应不同的原料。
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公开(公告)号：US20090005627A1
公开(公告)日：2009-01-01
申请号：US12157971
申请日：2008-06-13
IPC分类号： C07C7/148
CPC分类号： C10G65/043 , B01J21/063 , B01J23/44 , B01J29/0325 , B01J29/043 , B01J29/7461 , B01J35/0026 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C10G45/62 , C10G65/08 , C10G73/02 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/4018 , C10G2400/10
摘要： Integrated hydroprocessing methods using high activity, low density catalysts are provided. The high activity catalysts allow for blocked operation when processing lube range feedstocks of widely varying characteristics, such as wax content, without having to substantially change the configuration or operating conditions of the process train. Instead, the different feedstocks can be accommodated by varying the reaction temperature in the process train.
摘要翻译： 提供了使用高活性，低密度催化剂的综合加氢处理方法。 当处理广泛变化的特性（例如蜡含量）的润滑剂范围原料时，高活性催化剂允许堵塞操作，而不必基本上改变工艺列车的构造或操作条件。 相反，可以通过改变过程列中的反应温度来适应不同的原料。
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公开(公告)号：US08864975B2
公开(公告)日：2014-10-21
申请号：US12157968
申请日：2008-06-13
IPC分类号： C10G73/02 , C10G45/62 , C10G65/08 , B01J29/74 , B01J29/03 , B01J29/04 , C10G65/04 , B01J35/00 , B01J21/06 , B01J37/00 , B01J23/44
CPC分类号： C10G65/043 , B01J21/063 , B01J23/44 , B01J29/0325 , B01J29/043 , B01J29/7461 , B01J35/0026 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C10G45/62 , C10G65/08 , C10G73/02 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/4018 , C10G2400/10
摘要： Integrated hydroprocessing methods using high activity, low density catalysts are provided. The high activity catalysts allow for lower temperature operation, which reduces catalyst degradation, while the low density of the catalysts means a corresponding reduction in the amount of metal needed to fill a reactor volume. The methods allow for flexible processing of feedstocks with a variety of wax contents.
摘要翻译： 提供了使用高活性，低密度催化剂的综合加氢处理方法。 高活性催化剂允许较低的温度操作，这降低催化剂降解，而催化剂的低密度意味着填充反应器体积所需的金属量的相应减少。 这些方法允许用各种蜡含量对原料进行灵活处理。
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公开(公告)号：US20080314797A1
公开(公告)日：2008-12-25
申请号：US12157968
申请日：2008-06-13
IPC分类号： C10G65/02
CPC分类号： C10G65/043 , B01J21/063 , B01J23/44 , B01J29/0325 , B01J29/043 , B01J29/7461 , B01J35/0026 , B01J37/0009 , B01J2229/20 , B01J2229/42 , C10G45/62 , C10G65/08 , C10G73/02 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2300/4018 , C10G2400/10
摘要： Integrated hydroprocessing methods using high activity, low density catalysts are provided. The high activity catalysts allow for lower temperature operation, which reduces catalyst degradation, while the low density of the catalysts means a corresponding reduction in the amount of metal needed to fill a reactor volume. The methods allow for flexible processing of feedstocks with a variety of wax contents.
摘要翻译： 提供了使用高活性，低密度催化剂的综合加氢处理方法。 高活性催化剂允许较低的温度操作，这降低催化剂降解，而催化剂的低密度意味着填充反应器体积所需的金属量的相应减少。 这些方法允许用各种蜡含量对原料进行灵活处理。
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5.发明申请公开(公告)号：US20170157553A1
公开(公告)日：2017-06-08
申请号：US15433168
申请日：2017-02-15
IPC分类号： B01D53/14 , B01F3/04 , B01F5/04 , E21B43/40 , C01B17/16 , C01B17/04 , C10L3/10 , B01D53/18 , B01D45/16
CPC分类号： B01D53/1406 , B01D45/16 , B01D53/1425 , B01D53/1462 , B01D53/1468 , B01D53/18 , B01D53/62 , B01D2252/20431 , B01D2256/245 , B01D2257/30 , B01D2257/80 , B01F3/04021 , B01F5/0463 , C01B17/0408 , C01B17/167 , C01B32/50 , C10L3/101 , C10L3/103 , C10L3/104 , C10L2290/12 , C10L2290/541 , E21B43/16 , E21B43/164 , E21B43/40 , Y02C10/04 , Y02C10/06 , Y02P20/152
摘要： Systems and methods for separating CO2 and H2S from a natural gas stream are provided herein. The system includes a first loop of co-current contacting systems configured to remove H2S and CO2 from a natural gas stream and a second loop of co-current contacting systems configured to remove the H2S from the CO2.
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公开(公告)号：US5866621A
公开(公告)日：1999-02-02
申请号：US851863
申请日：1997-05-06
CPC分类号： C10G2/342 , B01J8/0065 , B01J8/226
摘要： Particulate solids and gas are removed from a three phase hydrocarbon synthesis slurry of solid catalyst particles, gas and liquid, by successively passing slurry from a slurry body through solids and gas disengaging zones in fluid communication, with the solids disengaging zone upstream of the gas disengaging zone. This is accomplished using a solids and gas disengaging downcomer immersed in the slurry wherein solids are disengaged in a quiescent zone adjacent the slurry body, from which the solids reduced slurry passes through an enclosed cup in which gas is disengaged and removed. The bottom of the cup terminates in a downwardly depending downcomer which hydraulically feeds the densified, solids and gas reduced slurry to the bottom of the reactor or to filtration.
摘要翻译： 颗粒状固体和气体从固体催化剂颗粒（气体和液体）的三相烃合成浆液中通过连续地将浆料从淤浆体通过流体连通的固体和气体分离区域而被从气相分离的上游固体分离区域中除去 区。 这是使用浸入浆料中的固体和气体分离降液管来实现的，其中固体在邻近淤浆体的静止区域中脱离，固体还原浆液从该悬浮液通过封闭的杯，气体被分离和除去。 杯的底部终止于向下的降液管，其将致密化的，固体和气体减少的浆液液压地进料到反应器的底部或过滤。
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公开(公告)号：US20150354321A1
公开(公告)日：2015-12-10
申请号：US14766621
申请日：2013-09-30
申请人： Nicholas F. URBANSKI , Robert D. DENTON , Charles J. MART , Tracy A. FOWLER , EXXONMOBIL UPSTREAM RESEARCH COMPANY
CPC分类号： E21B36/001 , F28D1/022 , F28D1/0435 , F28D1/047 , F28D15/00 , F28F2250/08
摘要： The present disclosure provides a subwater heat exchanger that includes a duct, first coils, a first impeller and a second impeller. The duct is configured to receive a first fluid. The first coils are inside of the duct and are configured to receive a second fluid that is heated or cooled by the first fluid. The first impeller is inside of the duct that is configured to initiate flow of the first fluid around the first coils. The second impeller is inside of the duct and is substantially in line with the first impeller along a duct lateral axis of the duct.
摘要翻译： 本公开提供了一种次水热交换器，其包括管道，第一线圈，第一叶轮和第二叶轮。 所述管道构造成接收第一流体。 第一线圈位于管道的内部并且被构造成接收由第一流体加热或冷却的第二流体。 管道内部的第一叶轮配置成启动第一流体围绕第一线圈的流动。 第二叶轮在管道的内部，并且沿着管道的管道横向轴线基本上与第一叶轮成一直线。
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公开(公告)号：US20150240717A1
公开(公告)日：2015-08-27
申请号：US14427246
申请日：2013-09-30
CPC分类号： F02C3/22 , B01D53/22 , B01D2257/304 , B01D2257/504 , C01B3/04 , C01B3/34 , C01B2203/0205 , C10L3/10 , C10L3/103 , C10L3/104 , C25B1/02 , F02C3/20 , F02C3/24 , F02C3/30 , F05D2220/75 , F25J3/0209 , F25J3/0233 , F25J3/0266 , F25J2200/02 , F25J2200/76 , F25J2205/20 , F25J2215/04 , F25J2260/80 , Y02C10/10 , Y02C10/12 , Y02E20/16 , Y02E60/364 , Y02P20/13 , Y02P20/152
摘要： A system and methods for increasing a combustibility of a low BTU natural gas are provided herein. The method includes increasing the adiabatic flame temperature of the low BTU natural gas using heavy hydrocarbons, wherein the heavy hydrocarbons include compounds with a carbon number of at least two. The method also includes burning the low BTU natural gas in a gas turbine.
摘要翻译： 本文提供了一种用于提高低BTU天然气的可燃性的系统和方法。 该方法包括使用重质烃增加低BTU天然气的绝热火焰温度，其中重烃包括碳数至少为2的化合物。 该方法还包括在燃气轮机中燃烧低BTU天然气。
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9.发明申请METHOD AND DEVICE FOR SEPARATING HYDROCARBONS AND CONTAMINANTS WITH A HEATING MECHANISM TO DESTABILIZE AND/OR PREVENT ADHESION OF SOLIDS 审中-公开用加热机构分离碳氢化合物和污染物来降解和/或防止固体粘附的方法和装置公开(公告)号：US20150159947A1
公开(公告)日：2015-06-11
申请号：US14516726
申请日：2014-10-17
申请人： Jaime A. Valencia , Harry W. Deckman , Charles J. Mart , James T. Wilkins , Paul Scott Northrop
发明人： Jaime A. Valencia , Harry W. Deckman , Charles J. Mart , James T. Wilkins , Paul Scott Northrop
CPC分类号： F25J3/067 , B01D3/42 , C07C7/05 , C10L3/102 , C10L3/104 , C10L3/107 , C10L2290/543 , C10L2290/545 , C10L2290/58 , C10L2290/60 , F25J1/0022 , F25J3/0209 , F25J3/0233 , F25J3/0266 , F25J3/061 , F25J3/0635 , F25J3/08 , F25J2200/02 , F25J2200/30 , F25J2200/50 , F25J2200/74 , F25J2205/04 , F25J2205/20 , F25J2220/66 , F25J2235/60 , F25J2280/02 , F25J2280/40 , F25J2290/12 , F25J2290/40 , Y02C10/12
摘要： The present disclosure provides a method for separating a feed stream in a distillation tower which includes separating a feed stream in a stripper section into an enriched contaminant bottom liquid stream and a freezing zone vapor stream; contacting the freezing zone vapor stream in the controlled freeze zone section with a freezing zone liquid stream at a temperature and pressure at which a solid and a hydrocarbon-enriched vapor stream form; directly applying heat to a controlled freeze zone wall of the controlled freeze zone section with a heating mechanism coupled to at least one of a controlled freeze zone internal surface of the controlled freeze zone wall and a controlled freeze zone external surface of the controlled freeze zone wall; and at least one of destabilizing and preventing adhesion of the solid to the controlled freeze zone wall with the heating mechanism.
摘要翻译： 本公开提供了一种用于分离蒸馏塔中的进料流的方法，其包括将汽提部分中的进料流分离成富集的污染物底部液体流和冷冻区蒸气流; 在控制的冷冻区段中的冷冻区蒸汽流与形成固体和富含烃的蒸气流的温度和压力下与冷冻区液体流接触; 将受控冻结区段的受控冻结区域的热量直接加热到受控冻结区域壁的受控冷冻区内表面和受控冷冻区域外部表面中的至少一个的加热机构 ; 以及使用加热机构去除稳定和防止固体与受控冷冻区域壁粘合中的至少一种。
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10.发明申请Selective Hydrogenation of Alkynyl-Containing Compounds and Polyunsaturated Compounds 有权含炔基的化合物和多不饱和化合物的选择性氢化公开(公告)号：US20130204055A1
公开(公告)日：2013-08-08
申请号：US13571120
申请日：2012-08-09
IPC分类号： C07C5/09
摘要： A selective hydrogenation process that is particularly effective in selectively hydrogenating alkynl compounds, such as acetylene or methyl acetylene, over alkenyl compounds, such as ethylene, is described. The process utilizes a slurry conversion unit for heat efficiency purposes during the conversion of acetylene into ethylene.
摘要翻译： 描述了在链烯基化合物如乙烯上选择性氢化炔烃化合物如乙炔或甲基乙炔特别有效的选择性氢化方法。 在乙炔转化为乙烯期间，该方法利用用于热效率目的的浆料转化单元。
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