公开(公告)号：US20240166583A1

公开(公告)日：2024-05-23

申请号：US18512747

申请日：2023-11-17

申请人： UOP LLC

发明人： Amit Goyal ,  Gregory J. Schrad ,  Gregory R. Werba ,  Sean Mann ,  Christine Marie Long ,  Cynthia M. Kwik

IPC分类号： C07C7/09 ,  B01D3/14 ,  B01D53/02 ,  C07C7/12

CPC分类号： C07C7/09 ,  B01D3/143 ,  B01D53/02 ,  C07C7/12 ,  B01D2256/24 ,  B01D2257/2025

摘要： Processes and apparatuses for separating chlorides from a butane product stream by removing chlorides from a portion of said feed stream in a rectification section of the separation zone. The rectification section may be in a rectification column which may be combined with a stripper column. Alternatively, a wall may be used to provide the rectification section in a fractionation column. The processes and apparatuses can be used in both new designs and revamped designs.

公开(公告)号：US11905241B2

公开(公告)日：2024-02-20

申请号：US17130260

申请日：2020-12-22

申请人： Gautham Krishnaiah ,  Brian Heasley ,  John Lewis Webb, Jr. ,  Rahul Radhakrishna Pillai ,  Vijender K. Verma ,  Narinder Singh Duggal

发明人： Gautham Krishnaiah ,  Brian Heasley ,  John Lewis Webb, Jr. ,  Rahul Radhakrishna Pillai ,  Vijender K. Verma ,  Narinder Singh Duggal

IPC分类号： C07C7/11 ,  C07C2/12 ,  C07C7/00 ,  C07C7/09 ,  B01J8/02 ,  B01D53/14 ,  B01D53/18

CPC分类号： C07C7/11 ,  B01D53/1406 ,  B01D53/1468 ,  B01D53/1475 ,  B01D53/1487 ,  B01D53/1493 ,  B01D53/18 ,  B01J8/02 ,  C07C2/12 ,  C07C7/005 ,  C07C7/09 ,  B01D2252/10 ,  B01D2252/204 ,  B01D2252/205

摘要： Methods and systems for treating an olefin-containing stream are disclosed. The disclosed methods and systems are particularly suitable for treating an off-gas stream in a refining or petrochemical process, such as from a fluid catalytic cracker (FCC), coker, steam cracker, and the like. The stream is treated in an absorber column to reject lighter stream components and to absorb ethylene and/or propylene into a solvent. The solvent is typically isobutane. The enriched solvent stream from the absorber column is fed to an alkylation reactor, which reacts the dissolved olefin with the isobutane solvent to produce an alkylate product.

公开(公告)号：US20240034699A1

公开(公告)日：2024-02-01

申请号：US18225967

申请日：2023-07-25

申请人： Chevron Phillips Chemical Company, LP

发明人： Steven M. Bischof ,  Gregory G. Hendrickson ,  Uriah J. Kilgore ,  Bruce E. Kreischer ,  Scott G. Morrison ,  Ryan W. Snell ,  Orson L. Sydora

IPC分类号： C07C2/46 ,  C07C7/09 ,  C07C5/327

CPC分类号： C07C2/46 ,  C07C7/09 ,  C07C5/327

摘要： The present disclosure relates to the integration of systems and methods associated with steam cracking, oligomerization reactions, hydrogenation reactions, and aromatization reactions for the production of benzene via the hydrogenation of oligomers produced from ethylene. In some aspects, the disclosed systems and methods utilize one or more of an oligomerization process, a hydrotreating process, and an aromatization process for producing a benzene comprising effluent. In further aspects, the systems and methods disclosed herein utilize one or more selective oligomerization catalyst systems.

公开(公告)号：US11884621B2

公开(公告)日：2024-01-30

申请号：US17705096

申请日：2022-03-25

申请人： EXTERRAN CORPORATION

发明人： Timothy W. Oneal

IPC分类号： B01D3/14 ,  C07C7/09 ,  C07C7/00 ,  B01D3/00 ,  C10L3/10 ,  C07C9/04 ,  F25J1/00

CPC分类号： C07C7/09 ,  B01D3/007 ,  B01D3/143 ,  C07C7/005 ,  C07C9/04 ,  C10L3/10 ,  F25J1/0022

摘要： A process for the separation of a natural gas stream is provided. The process includes receiving an effluent gas flow from a first fractionator operating at a first pressure, splitting the effluent gas flow into a first stream and a second stream, and passing the first stream through a heat exchanger thereby causing a phase change of at least a portion of the first stream from a gaseous state to a liquid state. The process includes inserting the first stream into an upper portion of a second fractionator operating at a second pressure. The second pressure is lower than the first pressure. The process includes inserting the second stream into a lower portion of the second fractionator, and diverting liquids from a lower portion of the second fractionator to the first fractionator.

公开(公告)号：US11845720B2

公开(公告)日：2023-12-19

申请号：US16966129

申请日：2019-01-29

申请人： UNIVERSITÉ CÔTE D'AZUR ,  Centre National de la Recherche Scientifique

发明人： Anne-Sophie Bouville ,  Cyrielle Dieffoldo ,  Xavier Fernandez ,  Stéphane Piquart

IPC分类号： A61K36/00 ,  C07C7/00 ,  A23L27/10 ,  A61K8/9789 ,  A61K8/31 ,  A61Q13/00 ,  B01D3/14 ,  B01D11/02 ,  C07C7/04 ,  C07C7/09 ,  C07C7/10 ,  C07C9/15

CPC分类号： C07C7/005 ,  A23L27/11 ,  A61K8/31 ,  A61K8/9789 ,  A61Q13/00 ,  B01D3/14 ,  B01D11/0288 ,  C07C7/04 ,  C07C7/09 ,  C07C7/10 ,  C07C9/15 ,  A23V2002/00 ,  A61K2800/805

摘要： A heptane composition obtained from a plant source is described, wherein the plant source comprises Commiphora wildii and wherein the heptane composition is obtained by a process of extraction comprising hydrodistilling or steam distilling a resin of Commiphora wildii to obtain an essential oil. A method of using the heptane composition as a solvent for extracting one or more natural products is also described.

公开(公告)号：US20230382826A1

公开(公告)日：2023-11-30

申请号：US18314591

申请日：2023-05-09

申请人： PHILLIPS 66 COMPANY

发明人： Anthony O. Baldridge ,  Matthew J. Wulfers ,  Neal D. McDaniel ,  Robert M. Walston ,  Soumen Kundu ,  Bruce B. Randolph

IPC分类号： C07C6/10 ,  C07C7/09 ,  B01J8/04 ,  B01D5/00 ,  B01D3/14

CPC分类号： C07C6/10 ,  C07C7/09 ,  B01J8/0492 ,  B01D5/006 ,  B01D3/14 ,  C07C2529/40 ,  B01J2208/00017 ,  B01J2208/00539

摘要： The present disclosure relates generally to processes and systems for producing liquid transportation fuels by converting a feed stream that comprises both isopentane and n-pentane, and optionally, some C6+ hydrocarbons. Isopentane and smaller hydrocarbons are separated to form a first fraction while n-pentane and larger components of the feed stock form a second fraction. Each fraction is then catalytically-activated in a separate reaction zone with a separate catalyst, where the conditions maintained in each zone maximize the conversion of each fraction to olefins and aromatics, while minimizing the production of C1-C4 light paraffins. In certain embodiments, the first fraction is activated at a lower temperature than the second fraction. Certain embodiments additionally comprise mixing at least a portion of the two effluents and contacting with either an oligomerization catalyst or alkylation catalyst to provide enhanced yields of upgraded hydrocarbon products that are suitable for use as a blend component of liquid transportation fuels or other value-added chemical products.

公开(公告)号：US20180354872A1

公开(公告)日：2018-12-13

申请号：US15780725

申请日：2016-12-02

申请人： BASF SE ,  Linde AG

发明人： Jan Pablo JOSCH ,  Ragavendra Prasad BALEGEDDE RAMACHANDRAN ,  Philipp GRUENE ,  Steffan RISSEL ,  Martin GEMBALA ,  Ulrike WENNING ,  Anton WELLENHOFER ,  Christine TOEGEL ,  Hendrik REYNEKE

IPC分类号： C07C5/48 ,  C07C7/00 ,  C07C7/08 ,  C07C7/09 ,  C07C7/11 ,  C07C11/167 ,  B01D3/40 ,  B01J19/00

CPC分类号： C07C5/48 ,  B01D3/40 ,  B01J19/0053 ,  B01J2219/00121 ,  B01J2219/00425 ,  C07C7/005 ,  C07C7/08 ,  C07C7/09 ,  C07C7/11 ,  C07C11/167

摘要： A) provision of a feed gas stream a comprising n-butenes;B) introduction of the feed gas stream a comprising n-butenes and an oxygen-comprising gas into a dehydrogenation reactor and oxidative dehydrogenation of n-butenes to butadiene;C) cooling and compression of the product gas stream b in at least one cooling stage comprising a quenching column and in a compression stage comprising a compressor, with the product gas stream b being brought into contact with at least one circulated coolant;D) separation of incondensable and low-boiling gas constituents as gas stream d2 from the gas stream c2 by absorption of the C4-hydrocarbons in at least one circulated absorption medium;E) separation of the C4 product stream d1 by extractive distillation using a solvent which is selective for butadiene into a stream e1 comprising butadiene and the selective solvent and a stream e2 comprising n-butenes;F) distillation of the stream e1 comprising butadiene and the selective solvent to give a stream f1 consisting essentially of the selective solvent and a stream f2 comprising butadiene;wherein the measures (i) to (iii) below are carried out (i) avoidance of formation of explosive gas mixtures by monitoring of the oxygen concentration in the oxygen-comprising gas streams fed into the dehydrogenation zone and control of the mass flows of oxygen-comprising gas streams and gas streams comprising hydrocarbons in such a way that no explosive gas mixtures can be formed; (ii) interruption of the introduction of the oxygen-comprising gas mixture into the dehydrogenation zone when a limit value for the oxygen concentration in the dehydrogenation gas mixture is exceeded; (iii) carrying out of the steps A) to F) in apparatuses which are configured so as to be explosion-protected, where liquid-conveying pipes are configured so as to be explosion-protected and gas conduits are configured so as to be detonation-protected.

公开(公告)号：US09920986B2

公开(公告)日：2018-03-20

申请号：US15284823

申请日：2016-10-04

申请人： Fluor Technologies Corporation

发明人： John Mak

IPC分类号： F25J1/02 ,  C07C7/09 ,  C10G5/06 ,  B01D53/00 ,  F25J1/00 ,  F25J3/02

CPC分类号： F25J1/0231 ,  B01D53/002 ,  C07C7/09 ,  C10G5/06 ,  C10G2300/1025 ,  F25J1/0022 ,  F25J3/0209 ,  F25J3/0233 ,  F25J3/0242 ,  F25J3/0257 ,  F25J2200/02 ,  F25J2200/04 ,  F25J2200/40 ,  F25J2200/70 ,  F25J2200/72 ,  F25J2200/74 ,  F25J2205/02 ,  F25J2205/04 ,  F25J2210/06 ,  F25J2215/02 ,  F25J2220/62 ,  F25J2230/08 ,  F25J2230/60 ,  F25J2235/60 ,  F25J2240/40 ,  F25J2245/02 ,  F25J2260/20 ,  F25J2270/02 ,  F25J2270/08 ,  F25J2270/90 ,  C07C9/04

摘要： Variable N2 content in feed gas ranging from 3 mol % to 50 mol % can be rejected from the process using a feed exchanger that is fluidly coupled with a cold separator and a single fractionation column to produce a nitrogen vent stream and streams that are suitable to be further processed for NGL recovery and LNG production.

公开(公告)号：US09650317B2

公开(公告)日：2017-05-16

申请号：US14635041

申请日：2015-03-02

申请人： FINA TECHNOLOGY, INC.

发明人： Vincent A. Welch ,  James R. Butler

IPC分类号： C07C5/327 ,  C07C5/333 ,  C07C7/09 ,  C01B3/32 ,  C01B3/50 ,  F25J3/06

CPC分类号： C07C7/09 ,  C01B3/24 ,  C01B3/323 ,  C01B3/50 ,  C01B3/506 ,  C01B2203/0233 ,  C01B2203/0266 ,  C01B2203/04 ,  C01B2203/048 ,  C01B2203/0495 ,  C07C5/333 ,  F25J3/063 ,  F25J3/0655 ,  F28B3/00 ,  F28B9/06 ,  Y10S585/921 ,  C07C11/20 ,  C07C15/46 ,  C07C11/18

摘要： Methods and systems for the dehydrogenation of hydrocarbons include a direct contact condenser to remove compounds from an offgas process stream. The reduction of compounds can decrease duty on the offgas compressor by removing steam and aromatics from the offgas. The dehydrogenation reaction system can be applicable for reactions such as the dehydrogenation of ethylbenzene to produce styrene, the dehydrogenation of isoamiline to produce isoprene, or the dehydrogenation of n-pentene to produce piperylene.

公开(公告)号：US20160368841A1

公开(公告)日：2016-12-22

申请号：US15187005

申请日：2016-06-20

申请人： RELIANCE INDUSTRIES LIMITED

发明人： Manoj YADAV ,  Asit Kumar DAS ,  Sukumar MANDAL ,  Amitkumar PAREKH ,  Nilamkumar LIMBASIYA

IPC分类号： C07C7/00 ,  C10G11/18 ,  C07C7/11 ,  C10L3/12 ,  C07C7/04 ,  C07C7/09

CPC分类号： C07C7/005 ,  C07C7/04 ,  C07C7/09 ,  C07C7/11 ,  C10G11/18 ,  C10G70/041 ,  C10G70/043 ,  C10G70/048 ,  C10G70/06 ,  C10G2300/104 ,  C10G2400/20 ,  C10G2400/28 ,  C10L3/12 ,  C10L2290/06 ,  C10L2290/30 ,  C10L2290/541 ,  C10L2290/543

摘要： The present invention provides a process for recovery of propylene and LPG from the fuel gas produced in FCC unit by contacting a heavier hydrocarbon feed with FCC catalyst. The process provides an energy efficient configuration for revamping an existing unit constrained on wet gas compressor capacity or for designing a new gas concentration unit to recover propylene and LPG recovery beyond 97 mole %. The process of the present invention provides an increase propylene and LPG recovery without loading wet gas compressor with marginal increase in liquid loads.

摘要翻译： 本发明提供了一种通过使较重的烃进料与FCC催化剂接触从FCC装置产生的燃料气中回收丙烯和LPG的方法。 该方法提供了一种节能配置，用于改造受限于湿气压缩机容量的现有单元，或设计新的气体浓度单元以回收超过97摩尔％的丙烯和LPG回收率。 本发明的方法提供了增加丙烯和LPG回收率，而不需要加载湿气压缩机，液体负荷略有增加。