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公开(公告)号：EP3478801A1
公开(公告)日：2019-05-08
申请号：EP17733710.2
申请日：2017-06-19
发明人： UMANSKY, Benjamin, S. , GUPTA, Himanshu , NELSON, John, D. , HUGHART, Cindy, J. , CHENG, Jane, C. , LEVINE, Steven, W. , BROWN, Stephen, H. , MARUT, Todd, P. , DANKWORTH, David, C. , SOLED, Stuart, L. , DEGNAN, Thomas, F. , FALKINER, Robert, J. , HARANDI, Mohsen, N. , HENAO, Juan, D. , ZHANG, Lei , BAI, Chuansheng , DOUGHERTY, Richard, C.
IPC分类号： C10G67/14 , B01J27/185 , B01J35/10 , C10G31/09 , C10G45/16
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公开(公告)号：EP3464517A1
公开(公告)日：2019-04-10
申请号：EP17726473.6
申请日：2017-05-19
发明人： UMANSKY, Benjamin, S. , ALDOUS, Keith, K. , GLEESON, James, W. , BLOK, Edward, J. , DEMMIN, Richard, A.
IPC分类号： C10G67/04
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公开(公告)号：EP2588567A2
公开(公告)日：2013-05-08
申请号：EP11734194.1
申请日：2011-06-24
CPC分类号： C10G65/12 , B01D3/141 , B01D3/143 , C10G2300/1011 , C10G2300/1055 , C10G2300/202 , C10G2300/301 , C10G2300/304 , C10G2300/4006 , C10G2300/4012 , C10G2300/4018 , C10G2400/04 , C10L1/08 , Y02P30/20
摘要： A divided wall column can allow for fractionation of multiple streams while maintaining separate product qualities. Effluents from multiple stages of a reaction system can be processed in a single divided wall column. The divided wall column can produce multiple cuts from each separated area, as well as at least one output from a common area. At least one reaction stage can advantageously have a continuous liquid phase environment.
摘要翻译： 分隔壁柱可以允许多个流的分馏，同时保持单独的产品质量。 来自反应系统多个阶段的污水可以在单个分隔壁柱中处理。 分隔墙柱可以从每个分隔区域产生多个切口，以及来自公共区域的至少一个输出。 至少一个反应阶段可有利地具有连续的液相环境。
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公开(公告)号：EP2880131B1
公开(公告)日：2016-11-02
申请号：EP13750418.9
申请日：2013-07-26
CPC分类号： C10G51/04 , C10G11/05 , C10G45/08 , C10G69/02 , C10G69/04 , C10G69/06 , C10G2300/1074 , C10G2300/307 , C10G2400/02 , C10G2400/04
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公开(公告)号：EP2880131A1
公开(公告)日：2015-06-10
申请号：EP13750418.9
申请日：2013-07-26
CPC分类号： C10G51/04 , C10G11/05 , C10G45/08 , C10G69/02 , C10G69/04 , C10G69/06 , C10G2300/1074 , C10G2300/307 , C10G2400/02 , C10G2400/04
摘要： An integrated thermal and catalytic process for improving the yield of middle distillate from heavy petroleum oil feeds comprises cracking the heavy portion (345 °C+) of the feed in a thermal conversion zone, followed by hydrotreating the thermally cracked product and the lighter portion of the feed and then separating the hydrotreated product into a bottoms fraction which is passed to a catalytic cracking step.
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公开(公告)号：EP2782673A1
公开(公告)日：2014-10-01
申请号：EP12795237.2
申请日：2012-11-16
发明人： UMANSKY, Benjamin, S. , TRACY, William, J. , HELTON, Terry, Eugene , MCCARTHY, Stephen, J. , KALYANARAMAN, Mohan , OLIVERI, Christopher, G. , HILBERT, Timothy, Lee
IPC分类号： B01J37/18 , B01J37/20 , B01J29/068 , B01J27/049 , B01J38/56 , B01J23/28 , B01J23/30 , B01J23/38 , B01J38/48 , B01J29/70 , B01J29/72 , C10G65/04
CPC分类号： B01J37/20 , B01J23/89 , B01J23/8993 , B01J29/0325 , B01J29/0333 , B01J29/126 , B01J29/143 , B01J29/44 , B01J29/46 , B01J29/67 , B01J29/68 , B01J29/7415 , B01J29/7461 , B01J29/7492 , B01J29/7615 , B01J29/7661 , B01J29/7692 , B01J29/85 , B01J29/90 , B01J38/10 , B01J38/58 , B01J38/74 , B01J2229/42 , C10G45/10 , C10G45/12 , C10G65/043 , C10G2300/4031 , C10G2300/703
摘要： Methods are provided for liquid phase activation of dewaxing and/or hydrofinishing catalysts that include a molecular sieve or other acidic crystalline support. The methods are compatible with activating the catalysts as part of a catalyst system that also includes a hydrotreating catalyst.
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7.发明公开PROCESS AND SYSTEM TO CONVERT LIGHT OLEFINS TO DIESEL AND OTHER DISTILLATES 审中-公开方法和系统的轻烯烃的柴油和馏分油其他转换
公开(公告)号：EP2513264A2
公开(公告)日：2012-10-24
申请号：EP10795582.5
申请日：2010-12-15
CPC分类号： C10G57/02 , C10G29/205 , C10G50/00 , C10G57/00 , C10G57/005 , C10G2300/1088 , C10G2300/1096 , C10G2300/301 , C10G2300/307 , C10G2400/02 , C10G2400/04 , C10G2400/08
摘要： The present invention provides a process for producing a hydrocarbon fuel composition that includes introducing an olefin feed composition including light olefins to an oligomerization catalyst to yield an intermediate composition including olefins having at least four carbon atoms, introducing the intermediate composition and a second feed of aromatic compounds (e.g., a feed including from 2 to 99.9% benzene or other alkylatable aromatics) to an aromatic alkylation catalyst to yield a fractionation feed to provide a composition which can be further refined to provide one or more hydrocarbon fuel compositions.
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公开(公告)号：EP3274425A1
公开(公告)日：2018-01-31
申请号：EP16711943.7
申请日：2016-03-10
发明人： UMANSKY, Benjamin, S. , HOO, Tech-Mui , DEMMIN, Richard, A. , CHEN, Fengrong , GLEESON, James, W. , DOU, Suisheng, M. , MELLI, Tomas, R. , CLARK, Michael, C.
CPC分类号： C10G67/02 , C10G47/14 , C10G47/16 , C10G65/12 , C10G2300/301 , C10G2300/302 , C10G2300/304 , C10G2400/10 , C10M101/02
摘要： A process for producing high yields of higher quality (API Group II, Group III′) lubricating oil basestock fractions which allows the production of two or more types of high quality lubes in continuous mode (no blocked operation mode) without transition times and feed or intermediate product tankage segregation. Two consecutive hydroprocessing steps are used: the first step processes a wide cut feed at a severity needed to match heavy oil lube properties. The second step hydroprocesses a light oil after fractionation of the liquid product from the first step at a severity higher than for the heavy oil fraction. The two hydroprocessing steps will normally be carried out in separate reactors but they may be combined in a single reactor which allows for the two fractions to be processed with different degrees of severity.
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公开(公告)号：EP2879785A1
公开(公告)日：2015-06-10
申请号：EP13752733.9
申请日：2013-08-05
发明人： RAMOS, Antonio, O. , KORSTEN, Hans, G. , HUANG, Yi, En , NADARAJAH, Chithranjan , UMANSKY, Benjamin, S.
IPC分类号： B01J8/00
CPC分类号： B01J8/0015 , B01J8/002 , B01J8/003 , B01J2208/00752
摘要： Methods, devices and processes for effectively loading catalysts into reactor vessels. In particular methods, devices and processes for effectively loading catalysts into fixed bed reactors utilizing inducted vibrational energy to improve catalyst loading performance, thereby resulting in improved flow distribution through the catalyst beds at designed operating conditions. The methods herein are particularly effectively for improving the performance of new or existing catalyst bed configurations of vertically-oriented two-phase hydroprocessing fixed bed reactors.
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公开(公告)号：EP2561046A1
公开(公告)日：2013-02-27
申请号：EP11718584.3
申请日：2011-04-22
发明人： UMANSKY, Benjamin, S. , KALYANARAMAN, Mohan , HILBERT, Timothy, L. , LOPEZ, Carlos, N. , ZHANG, Lei
CPC分类号： C10G45/02 , B01D3/141 , C10G45/58 , C10G45/64 , C10G65/043 , C10G2300/202 , C10G2300/304 , C10G2300/4018 , C10G2400/04 , C10L1/08
摘要： A diesel fuel product with beneficial cold flow properties can be produced. A suitable feedstock for forming a diesel boiling range product can be hydrotreated to have a sulfur content of at least about 100 wppm and then dewaxed. This two stage process can allow for production of an arctic or winter diesel without use of high pressures. Optionally, a divided wall column fractionator can be used to allow a single separation stage to handle the effluent from both the hydroprocessing and the dewaxing stages.
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