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1. 发明授权

US5013424A Process for the simultaneous hydrogenation of a first feedstock comprising hydrocarbonaceous compounds and having a non-distillable component and a second feedstock comprising halogenated organic compounds 失效
标题翻译：用于同时氢化包含烃类化合物并具有不可蒸馏组分的第一原料和包含卤化有机化合物的第二原料的方法
公开(公告)号：US5013424A
公开(公告)日：1991-05-07
申请号：US559820
申请日：1990-07-30
申请人： Robert B. James, Jr. , Tom N. Kalnes , Steven P. Lankton
发明人： Robert B. James, Jr. , Tom N. Kalnes , Steven P. Lankton
IPC分类号： A62D3/00 , A62D3/37 , A62D101/22 , A62D101/24 , B01J23/44 , B01J23/88 , C10G1/00 , C10G45/02 , C10G65/04 , C10G65/12 , C10M175/00 , C10N40/08 , C10N40/22
CPC分类号： A62D3/37 , C10G45/02 , A62D2101/22 , A62D2101/24 , A62D2203/02
摘要： A process for the production of hydrogenated, distillable hydrocarbonaceous product from a feed comprising hydrocarbonaceous compounds and having a non-distillable component, and a feed comprising halogenated organic compounds by means of contacting the feed comprising hydrocarbonaceous compounds and having a non-distillable component with a hot hydrogen-rich gaseous stream to increase the temperature of this feed stream to vaporize at least a portion of the distillable hydrocarbonaceous compounds thereby producing a distillable hydrocarbonaceous product which is immediately hydrogenated in an integrated hydrogenation zone. The feed comprising halogenated organic compounds is contacted in a second hydrogenated hydrocarbonaceous product and at least one water-soluble inorganic halide compound.
摘要翻译：一种从包含烃类化合物并具有不可蒸馏组分的原料生产氢化，可蒸馏的含烃产物的方法，以及包含卤化有机化合物的进料，其通过使包含烃类化合物的进料与含有不可蒸馏组分的物质接触，热的富氢气流以增加该进料流的温度以蒸发至少一部分可蒸馏烃类化合物，从而产生可在一体化氢化区中立即氢化的可蒸馏烃类产物。包含卤代有机化合物的进料在第二氢化烃产物和至少一种水溶性无机卤化物化合物中接触。

2. 发明授权

US5302282A Integrated process for the production of high quality lube oil blending stock 失效
标题翻译：生产高品质润滑油混合料的综合工艺
公开(公告)号：US5302282A
公开(公告)日：1994-04-12
申请号：US846114
申请日：1992-03-05
申请人： Tom N. Kalnes , Steven P. Lankton , Robert B. James, Jr.
发明人： Tom N. Kalnes , Steven P. Lankton , Robert B. James, Jr.
IPC分类号： C10G67/00 , C10G67/04 , C10M175/02
CPC分类号： C10G67/00 , C10G2400/10
摘要： A process for the production of high quality lube oil blending stock from atmospheric fractionation residue and waste lubricants by means of contacting the waste lubricant with a hot hydrogen-rich gaseous stream to increase the temperature of this feed stream to vaporize at least a portion of the distillable hydrocarbonaceous compounds thereby producing a distillable hydrocarbonaceous stream which is immediately hydrogenated in an integrated hydrogenation zone. The vaporization of the waste oil is also conducted in the presence of an asphalt residue which is produced in the integrated process. The resulting effluent from the integrated hydrogenation zone provides at least one high quality lube oil blending stock stream.
摘要翻译：一种通过将废润滑剂与富含氢气的气流接触以提高该进料流的温度以汽化至少一部分的方法，从大气分馏残渣和废润滑剂生产高质量润滑油混合料的方法可蒸馏的烃类化合物，从而产生可在一体化的氢化区中立即氢化的可馏出的烃类物流。废油的蒸发也是在一体化过程中生产的沥青残渣的存在下进行的。来自整合氢化区的所得流出物提供至少一种高品质润滑油混合原料流。

3. 发明授权

US5244565A Integrated process for the production of distillate hydrocarbon 失效
标题翻译：生产馏出油的综合工艺
公开(公告)号：US5244565A
公开(公告)日：1993-09-14
申请号：US813522
申请日：1991-12-26
申请人： Steven P. Lankton , Tom N. Kalnes , Robert B. James, Jr.
发明人： Steven P. Lankton , Tom N. Kalnes , Robert B. James, Jr.
IPC分类号： C10G65/00
CPC分类号： C10G65/00
摘要： A process for the production of distillate hydrocarbon from atmospheric fractionation residue and waste lubricants by means of contacting the waste lubricant with a hot hydrogen-rich gaseous stream to increase the temperature of this feed stream to vaporize at least a portion of the distillable hydrocarbonaceous compounds thereby producing a distillable hydrocarbonaceous stream which is immediately hydrogenated in an integrated hydrogenation zone. The vaporization of the waste oil is also conducted in the presence of a vacuum fractionation residue which is produced in the integrated process. The resulting effluent from the integrated hydrogenation zone and a distillable hydrocarbon stream recovered from the atmospheric fraction residue is catalytically converted to produce lower molecular weight hydrocarbon compounds.
摘要翻译：通过使废润滑剂与富含氢气的气态流接触以提高该进料流的温度以蒸发至少一部分可蒸馏烃类化合物，从大气馏分残余物和废润滑剂生产馏出物烃的方法，由此产生可在一体化的氢化区中立即氢化的可蒸馏烃物流。废油的汽化也是在一体化过程中产生的真空分馏残渣的存在下进行的。来自整体氢化区的所得流出物和从大气馏分残余物回收的可馏出烃流被催化转化以产生较低分子量的烃化合物。

4. 发明授权

US5064450A Gas absorber method and apparatus 失效
标题翻译：气体吸收剂的方法和装置
公开(公告)号：US5064450A
公开(公告)日：1991-11-12
申请号：US636784
申请日：1991-01-02
申请人： Steven P. Lankton , Robert B. James, Jr.
发明人： Steven P. Lankton , Robert B. James, Jr.
IPC分类号： B01D47/06 , B01D53/18
CPC分类号： B01D53/18 , B01D47/06
摘要： A gas absorber for removing at least one gaseous component from a flowing gas stream by contacting the gas stream with a lean liquid stream to absorb at least a portion of the gaseous component to produce a rich liquid stream comprising the gaseous component and a flowing gas stream having a reduced concentration of the gaseous component which absorber comprises: (a) a double wall forming an annulus having a means for restricting fluid flow into the bottom of the gas absorber from the bottom of the annulus and a means for passing fluid out of an upper section of the annulus into the gas absorber; (b) an inlet for the lean liquid stream having a locus in the upper end of the gas absorber; (c) an inlet for the flowing gas stream; (d) an outlet for the rich liquid stream having a locus in the lower end of the gas absorber; (e) an outlet for the flowing gas stream having a reduced concentration of the gaseous component; and (f) at least one inlet communicating with the lower end of the annulus which inlet is used to introduce a lean liquid stream at least a portion of which flows upwardly through the annulus and overflows from the top of the annulus and thereby protecting at least a portion of the outer wall from contact with the flowing gas stream.

5. 发明授权

US5176816A Process to produce a hydrogenated distillable hydrocarbonaceous product 失效
标题翻译：生产氢化蒸馏烃类产品的方法
公开(公告)号：US5176816A
公开(公告)日：1993-01-05
申请号：US862146
申请日：1992-04-02
申请人： Steven P. Lankton , Robert B. James, Jr.
发明人： Steven P. Lankton , Robert B. James, Jr.
IPC分类号： C10G45/02 , C10G49/22
CPC分类号： C10G49/22 , C10G45/02
摘要： An integrated process for the production of a hydrogenated distillable hydrocarbonaceous product from a temperature-sensitive hydrocarbonaceous stream containing a non-distillable component by the utilization of a hot hydrogen flash zone and a secondary separation zone to achieve a high yield of hydrogenated distillable hydrocarbonaceous product.
摘要翻译：一种用于通过利用热氢闪蒸区和二次分离区从含有不可蒸馏组分的温度敏感烃流产生氢化可蒸馏烃产物以实现高产率的氢化可蒸馏烃类产物的综合方法。

6. 发明授权

US5057125A Process for the treatment of vent gas containing organic halide compounds 失效
标题翻译：用于处理含有机卤化物的排放气体的方法
公开(公告)号：US5057125A
公开(公告)日：1991-10-15
申请号：US522719
申请日：1990-05-14
申请人： Steven P. Lankton , Richard T. Maurer , Robert B. James, Jr.
发明人： Steven P. Lankton , Richard T. Maurer , Robert B. James, Jr.
IPC分类号： B01D53/00 , B01D53/04
CPC分类号： B01D53/04 , B01D53/002 , B01D2257/20
摘要： A process for the removal of organic halide compounds from an effluent waste gas wherein the waste gas is sequentially compressed to separate water vapor and organic halide compounds, and to contact the resulting compressed gas having a reduced concentration of organic halide compounds with an adsorbent to produce an effluent waste gas containing essentially no detectable quantities of organic halide compounds.
摘要翻译：一种从流出废气中除去有机卤化物的方法，其中依次压缩废气以分离水蒸气和有机卤化物，并将所得的具有降低的有机卤化物浓度的压缩气体与吸附剂接触以产生基本上不含可检测量的有机卤化物的流出废气。

7. 发明授权

US08404916B1 Process for separating and/or introducing a flush material in an adsorption separation system 有权
标题翻译：用于在吸附分离系统中分离和/或引入冲洗材料的方法
公开(公告)号：US08404916B1
公开(公告)日：2013-03-26
申请号：US13310954
申请日：2011-12-05
申请人： Jeffrey L. Pieper , Cynthia K. Zimmerman , Stephen W. Sohn , Steven P. Lankton
发明人： Jeffrey L. Pieper , Cynthia K. Zimmerman , Stephen W. Sohn , Steven P. Lankton
IPC分类号： C07C7/12
CPC分类号： C07C7/12 , C10G25/12 , C07C9/00
摘要： Embodiments of the present invention provide, for an adsorption separation system for separating normal paraffins from a hydrocarbon feed stream, a process for switching the adsorption separation from a triple split desorbent system to a dual split desorbent system, and vice versa. Switching occurs by separating and/or introducing a second flush material in the adsorption separation system. This switching can occur during normal operations.
摘要翻译：本发明的实施方案提供了用于从烃进料流中分离正链烷烃的吸附分离系统，用于将吸附分离从三分裂解吸系统切换到双分离解吸系统，反之亦然。通过在吸附分离系统中分离和/或引入第二冲洗材料进行切换。这种切换可能在正常操作期间发生。

8. 发明申请

US20110319698A1 PROCESS FOR UPGRADING SWEETENED OR OXYGEN-CONTAMINATED KEROSENE OR JET FUEL, TO MINIMIZE OR ELIMINATE ITS TENDENCY TO POLYMERIZE OR FOUL WHEN HEATED 有权
标题翻译：升级清洁或氧化污染的凯龙或喷射燃料的过程，以最小化或消除其在加热时聚合或加热的趋势
公开(公告)号：US20110319698A1
公开(公告)日：2011-12-29
申请号：US13154572
申请日：2011-06-07
申请人： Stephen W. Sohn , Steven P. Lankton , Joao Jorge da Silva Ferreira Alves
发明人： Stephen W. Sohn , Steven P. Lankton , Joao Jorge da Silva Ferreira Alves
IPC分类号： C07C7/00 , C10G29/00 , C10G45/00
CPC分类号： C10G31/06 , C10G7/00 , C10G2300/1051 , C10G2300/202 , C10G2400/08
摘要： A process is presented for the removal of oxygen from a hydrocarbon stream. The oxygen can react and cause polymerization of the hydrocarbons when the hydrocarbon stream is heated. Controlling the removal of the oxygen from the hydrocarbon stream produces a hydrocarbon stream that is substantially free of oxygen and has a reduced activity for generating undesired compounds.
摘要翻译：提出了从烃流中除去氧气的方法。当烃流被加热时，氧可以反应并引起烃的聚合。控制从烃流中除去氧气产生基本上不含氧气并且具有降低的活性以产生不需要的化合物的烃流。

9. 发明申请

US20100292519A1 AROMATIC ALKYLATION PROCESS WITH REDUCED BYPRODUCT FORMATION 有权
标题翻译：具有减少产物形成的芳香烷基化方法
公开(公告)号：US20100292519A1
公开(公告)日：2010-11-18
申请号：US12467622
申请日：2009-05-18
申请人： Patrick J. Bullen , Steven P. Lankton , Robert J. Schmidt
发明人： Patrick J. Bullen , Steven P. Lankton , Robert J. Schmidt
IPC分类号： C07C2/00
CPC分类号： C07C6/126 , C07C7/1485 , C07C2521/04 , C07C2521/08 , C07C2529/08 , C07C2529/70 , C07C15/073 , C07C15/085 , C07C15/02
摘要： Byproduct formation in aromatic alkylation processes is reduced when different polyalkylated aromatic compounds are first fractionated into separate streams enriched in these respective polyalkylated aromatic compounds, and the separate streams are sent to different transalkylation reaction zones, which may or may not be in the same reactor. The different transalkylation reaction zones allow for greater control of the transalkylation of the respective polyalkylated aromatic compounds, such as diisopropylbenzene (DIPB) and triisopropylbenzene (TIPB) that accompany the alkylation of benzene with propylene in a process for cumene production.
摘要翻译：当将不同的多烷基化芳族化合物首先分馏成富含这些各自的多烷基化芳族化合物的分离的流中时，芳族烷基化方法中的副产物形成降低，并且将分离的物流送入不同的烷基转移反应区，其可以是或不在同一个反应器中。不同的烷基转移反应区可以更好地控制各种多烷基化芳族化合物如二异丙基苯（DIPB）和三异丙基苯（TIPB）在烷基化反应过程中伴随苯与丙烯烷基化反应的烷基转移。

10. 发明授权

US07525003B2 Process for producing ethylbenzene 有权
标题翻译：生产乙苯的方法
公开(公告)号：US07525003B2
公开(公告)日：2009-04-28
申请号：US11752508
申请日：2007-05-23
申请人： Michael A. Schultz , Steven P. Lankton , Constante P. Tagamolila
发明人： Michael A. Schultz , Steven P. Lankton , Constante P. Tagamolila
IPC分类号： C07C15/073 , C07C2/64
CPC分类号： C07C15/073 , C07C2/66 , C07C6/126
摘要： This ethylbenzene process involves contacting, in an alkylation zone, a first benzene recycle stream and an ethylene feed stream with an alkylation catalyst to form ethylbenzene. In a transalkylation zone, a polyethylbenzene recycle stream and a second benzene recycle stream are contacted with a transalkylation catalyst to form additional ethylbenzene. The effluents are passed into a dividing wall distillation column where a benzene overhead and a benzene side draw are removed and recycled. An ethylbenzene stream product stream is also removed. The remainder, largely polyethylbenzene and tar, is passed to a polyethylbenzene column for separation. The separated polyethylbenzene is recycled to the transalkylation reactor.
摘要翻译：该乙苯方法包括在烷基化区中与烷基化催化剂接触第一苯再循环流和乙烯进料流以形成乙苯。在烷基转移区中，将聚乙苯再循环流和第二苯再循环流与烷基转移催化剂接触以形成另外的乙苯。流出物被送入分离塔蒸馏塔，其中苯塔顶馏出物和苯侧馏分被除去并再循环。还除去乙苯料流产物流。其余的，主要是聚乙苯和焦油，被送到聚乙苯塔进行分离。将分离的聚乙苯再循环至烷基转移反应器。

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