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公开(公告)号：US10809022B2
公开(公告)日：2020-10-20
申请号：US15843379
申请日：2017-12-15
Applicant: UOP LLC
Inventor： Gregory J. Schrad , James G. Hagen , Sean G. Mueller , Trung Pham , Zhanping Xu
Abstract: Processes for controlling the rate and temperature of cooling fluid through a heat exchange zone in, for example, an alkylation reactor using an ionic liquid catalyst. A cooling fluid system may be used to provide the cooling fluid which includes a chiller and a reservoir. The cooling fluid may pass from the reservoir through the heat exchange zone. A bypass line may be used to pass a portion of the cooling fluid around the heat exchange zone. The amount of cooling fluid may be adjusted, with a valve, based upon the temperature of the cooled process fluid flowing out of the heat exchange zone. Some of the cooling fluid from the chiller may be circulated back to the chiller in a chiller loop.
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公开(公告)号：US10550338B2
公开(公告)日：2020-02-04
申请号：US15710669
申请日：2017-09-20
Applicant: UOP LLC
Inventor： Donald A. Eizenga , Massimo Sangalli , Richard K. Hoehn , Saadet Ulas Acikgoz , Trung Pham
Abstract: We have discovered a process for hydrocracking a distillate stream and separating it into several product cuts including LPG, light naphtha, heavy naphtha and distillate without a stripper column. Additionally, no more than two heaters relying on external utilities are required for reboiling fractionator bottoms.
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公开(公告)号：US10472306B1
公开(公告)日：2019-11-12
申请号：US16023863
申请日：2018-06-29
Applicant: UOP LLC
Inventor： Stanley J. Frey , Chunqing Liu , Trung Pham
Abstract: The present invention relates to a combined C3/C4 splitter with a membrane system. More specifically, the present invention relates to a combined C3/C4 splitter column to separate highly pure propylene product from a liquefied petroleum gas stream, which eliminates a C3 splitter having over 120 trays and the additional equipment that a C3 splitter requires.
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公开(公告)号：US10457878B2
公开(公告)日：2019-10-29
申请号：US15710626
申请日：2017-09-20
Applicant: UOP LLC
Inventor： Donald A. Eizenga , Massimo Sangalli , Richard K. Hoehn , Saadet Ulas Acikgoz , Trung Pham
Abstract: We have discovered a process for hydrocracking a distillate stream and separating it into several product cuts including LPG, light naphtha, heavy naphtha and distillate without a stripper column. Additionally, no more than two heaters relying on external utilities are required for reboiling fractionator bottoms.
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公开(公告)号：US20190100479A1
公开(公告)日：2019-04-04
申请号：US16058784
申请日：2018-08-08
Applicant: UOP LLC
Inventor： Chunqing Liu , Lubo Zhou , Stanley J. Frey , Gregory R. Werba , Carl W. Liskey , Simon E. Albo , Trung Pham
Abstract: A process is provided for separation of light olefins and paraffins and particular for the separation of propylene and propane comprising sending at least one olefin/paraffin stream to a distillation column and a membrane unit to produce an olefin stream comprising at least 92 mol % olefin. In an embodiment of the invention where the membrane unit is placed downstream from the column which can produce propylene streams at polymer grade of over 99.5 mol % propylene.
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Patent Agency Ranking
公开(公告)号：US20160289569A1
公开(公告)日：2016-10-06
申请号：US14674191
申请日：2015-03-31
Applicant: UOP LLC
Inventor： Lance A. Baird , Trung Pham
CPC classification number: C10G3/50 , C07C5/2737 , C07C6/126 , C07C2529/06 , C10B53/02 , C10G1/02 , C10G3/47 , C10G35/04 , C10G2400/30 , Y02E50/14 , Y02P30/20 , C07C15/08
Abstract: Processes for the production of aromatics from a pyrolysis oil. The pyrolysis oil may be obtained from a biomass by fast pyrolysis and may be filtered and upgraded to provide an aromatic rich hydrocarbon product. The aromatic rich hydrocarbon product may be passed to a separation zone to separate non-aromatic hydrocarbons from the aromatics. The remaining aromatics may be separated into aromatic product rich streams based upon the desired aromatics. Isomerization and transalkylation zones may be included to increase the yield depending on the product or desired aromatic. The non-aromatic hydrocarbons may be passed to a reformer to be converted to aromatics and hydrogen.
Abstract translation: 从热解油生产芳烃的方法。 热解油可以通过快速热解从生物质获得，并且可以过滤和升级以提供富含芳烃的烃产物。 可以将富含芳烃的烃产物送入分离区，以从芳族化合物中分离出非芳族烃。 基于所需的芳族化合物，剩余的芳族化合物可以分离成富含芳烃的物流。 可以包括异构化和烷基转移区以根据产物或所需的芳族化合物来提高产率。 非芳族烃可以通入重整器以转化为芳烃和氢。
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公开(公告)号：US20150274613A1
公开(公告)日：2015-10-01
申请号：US14229437
申请日：2014-03-28
Applicant: UOP LLC
Inventor： Trung Pham , Susie C. Martins , Douglas A. Nafis
CPC classification number: C07C7/005 , C07C2/58 , C07C5/41 , C10G11/18 , C10G45/58 , C10G45/68 , C10G69/04 , C10G69/123 , C10G2300/1033 , C10G2300/107 , C10G2400/02 , C10G2400/30 , C07C9/16 , C07C15/08 , C07C11/06
Abstract: An integrated hydrocarbon conversion process is described. The process includes contacting a heavy hydrocarbon feedstock with a hydrocarbon cracking catalyst in a fluidized reactor zone to produce light olefins to form a fluid catalytic cracker (FCC) effluent stream comprising a range of hydrocarbons. The FCC effluent stream is separated to form at least a stream rich in C4 hydrocarbons which comprises isobutane and 1-butene. The stream rich in C4 hydrocarbons is introduced into an alkylation reaction zone where the isobutane and the 1-butene are alkylated to form a reaction product mixture comprising dimethylhexanes and C9+ hydrocarbons. The reaction product mixture is dehydrocyclized to form a stream rich in xylenes.
Abstract translation: 描述了一种综合烃转化方法。 该方法包括在流化反应器区中使重质烃原料与烃裂化催化剂接触以产生轻质烯烃以形成包含一系列烃的流化催化裂化器（FCC）流出物流。 FCC流出物流被分离以形成至少一种富含C4烃的物流，其中包含异丁烷和1-丁烯。 将富含C 4烃的物流引入烷基化反应区，其中异丁烷和1-丁烯被烷基化以形成包含二甲基己烷和C 9+烃的反应产物混合物。 将反应产物混合物脱氢环化以形成富含二甲苯的物流。
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8.发明授权公开(公告)号：US11447436B2
公开(公告)日：2022-09-20
申请号：US17339501
申请日：2021-06-04
Applicant: UOP LLC
Inventor： Chunqing Liu , Trung Pham , Charles P Luebke , Carl Liskey
Abstract: A process and system to control the final product quality in a system for separating olefins and paraffins in a membrane system. A small finishing membrane stage is added to an existing membrane system that takes a slip stream from the product, purifies it to a very high concentration of propylene and blends it back into the product stream.
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9.发明申请公开(公告)号：US20210403397A1
公开(公告)日：2021-12-30
申请号：US17339501
申请日：2021-06-04
Applicant: UOP LLC
Inventor： Chunqing Liu , Trung Pham , Charles P. Luebke , Carl Liskey
Abstract: A process and system to control the final product quality in a system for separating olefins and paraffins in a membrane system. A small finishing membrane stage is added to an existing membrane system that takes a slip stream from the product, purifies it to a very high concentration of propylene and blends it back into the product stream.
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公开(公告)号：US10683246B2
公开(公告)日：2020-06-16
申请号：US16058784
申请日：2018-08-08
Applicant: UOP LLC
Inventor： Chunqing Liu , Lubo Zhou , Stanley J. Frey , Gregory R. Werba , Carl W. Liskey , Simon E. Albo , Trung Pham
Abstract: A process is provided for separation of light olefins and paraffins and particular for the separation of propylene and propane comprising sending at least one olefin/paraffin stream to a distillation column and a membrane unit to produce an olefin stream comprising at least 92 mol % olefin. In an embodiment of the invention where the membrane unit is placed downstream from the column which can produce propylene streams at polymer grade of over 99.5 mol % propylene.
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