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公开(公告)号：US11453829B2
公开(公告)日：2022-09-27
申请号：US16767939
申请日：2018-11-16
摘要： The invention relates to a process for the production of C6-C7 aromatic compounds from a hydrocarbon feedstock of naphtha type comprising a step of fractionating (2) the feedstock in order to obtain an upper stream and a lower stream, a step of catalytic reforming of the upper stream (6) and of the lower stream (9), a step of recombining (15) the reformate effluents obtained, a step of recontacting (16) and a step of stabilizing (19) the stabilized reformate effluents and a step of separating (22) the raffinate in order to recover C6 and C7 hydrocarbon compounds.
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公开(公告)号：US11149211B2
公开(公告)日：2021-10-19
申请号：US16860638
申请日：2020-04-28
摘要： A naphtha reforming reactor system comprising a first reactor comprising a first inlet and a first outlet, wherein the first reactor is configured to operate as an adiabatic reactor, and wherein the first reactor comprises a first naphtha reforming catalyst; and a second reactor comprising a second inlet and a second outlet, wherein the second inlet is in fluid communication with the first outlet of the first reactor, wherein the second reactor is configured to operate as an isothermal reactor, and wherein the second reactor comprises a plurality of tubes disposed within a reactor furnace, a heat source configured to heat the interior of the reactor furnace; and a second naphtha reforming catalyst disposed within the plurality of tubes, wherein the first naphtha reforming catalyst and the second naphtha reforming catalyst are the same or different.
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公开(公告)号：US10941356B2
公开(公告)日：2021-03-09
申请号：US16454839
申请日：2019-06-27
摘要： Increased paraxylene production through the use of a split feed reforming process, wherein hydrotreated naphtha is split into light, middle and heavy fractions. Each fraction is reformed separately to generate streams containing aromatic compounds. These streams can further be processed and can undergo dealkylation, transalkylation, disproportionation, isomerization, and separation steps to maximize paraxylene production. In addition, some streams are recycled or recombined in order to maximize paraxylene production.
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公开(公告)号：US09803507B2
公开(公告)日：2017-10-31
申请号：US15087440
申请日：2016-03-31
IPC分类号： F01K13/02 , C10G69/00 , F01D17/14 , F01K3/18 , H02K7/18 , C10G59/00 , C10G61/00 , C10G63/00 , F01K3/00 , F01K27/00 , C10G53/04 , C10G55/00 , C10G57/00 , C10G61/10 , C07C5/27 , C07C7/00
CPC分类号： F01K13/02 , C07C5/2732 , C07C7/00 , C10G53/04 , C10G55/00 , C10G57/00 , C10G59/00 , C10G61/00 , C10G61/10 , C10G63/00 , C10G69/00 , C10G2300/4006 , C10G2400/04 , C10G2400/30 , F01D17/145 , F01K3/00 , F01K3/185 , F01K27/00 , H02K7/1823 , C07C15/08
摘要： Optimizing power generation from waste heat in large industrial facilities such as petroleum refineries by utilizing a subset of all available hot source streams selected based, in part, on considerations for example, capital cost, ease of operation, economics of scale power generation, a number of organic Rankine cycle (ORC) machines to be operated, operating conditions of each ORC machine, combinations of them, or other considerations are described. Subsets of hot sources that are optimized to provide waste heat to one or more ORC machines for power generation are also described. Further, recognizing that the utilization of waste heat from all available hot sources in a mega-site such as a petroleum refinery and aromatics complex is not necessarily or not always the best option, hot source units in petroleum refineries from which waste heat can be consolidated to power the one or more ORC machines are identified.
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公开(公告)号：US09803505B2
公开(公告)日：2017-10-31
申请号：US15087403
申请日：2016-03-31
IPC分类号： F01D15/10 , F02C6/00 , H02K7/18 , H02P9/04 , F01K13/02 , C10G57/00 , F01D17/14 , F01K3/18 , C10G59/00 , C10G61/00 , C10G63/00 , F01K3/00 , F01K27/00 , C10G99/00 , C10G53/04 , C10G55/00 , C10G61/10 , F02B63/04 , F03G7/08
CPC分类号： F01K13/02 , C10G53/04 , C10G55/00 , C10G57/00 , C10G59/00 , C10G61/00 , C10G61/10 , C10G63/00 , C10G99/00 , C10G2300/00 , C10G2300/4006 , C10G2400/30 , F01D17/145 , F01K3/00 , F01K3/185 , F01K27/00 , H02K7/1823
摘要： Optimizing power generation from waste heat in large industrial facilities such as petroleum refineries by utilizing a subset of all available hot source streams selected based, in part, on considerations for example, capital cost, ease of operation, economics of scale power generation, a number of ORC machines to be operated, operating conditions of each ORC machine, combinations of them, or other considerations are described. Recognizing that several subsets of hot sources can be identified from among the available hot sources in a large petroleum refinery, subsets of hot sources that are optimized to provide waste heat to one or more ORC machines for power generation are also described. Further, recognizing that the utilization of waste heat from all available hot sources in a mega-site such as a petroleum refinery and aromatics complex is not necessarily or not always the best option, hot source units in petroleum refineries from which waste heat can be consolidated to power the one or more ORC machines are identified.
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公开(公告)号：US20100012552A1
公开(公告)日：2010-01-21
申请号：US12176290
申请日：2008-07-18
CPC分类号： C10G35/095 , B01J29/70 , C10G59/02
摘要： One exemplary embodiment can be a process for producing a gasoline. The process can include contacting a feed having a naphtha and recycling at least a portion of the reaction zone effluent to the one or more reforming reaction zones. Generally, the reformate includes no more than about 15%, by volume, benzene, with a UZM-8 catalyst in one or more reforming reaction zones to produce a reaction zone effluent.
摘要翻译： 一个示例性实施方案可以是用于生产汽油的方法。 该方法可以包括使具有石脑油的进料接触并将至少一部分反应区流出物再循环到一个或多个重整反应区。 通常，重整产物在一个或多个重整反应区中包含不超过约15体积％的含有UZM-8催化剂的苯，以产生反应区流出物。
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公开(公告)号：US3776837A
公开(公告)日：1973-12-04
申请号：US3776837D
申请日：1971-10-20
申请人： SHELL OIL CO
发明人： DAUTZENBERG F , ALKEMA H
摘要： HIGH AROMATIC CONTENT MOTOR FUEL IS PRODUCED FROM C5-C8+ NAPHTHA BY SEPARATING THE NAPHTHA INTO A C5-C6 CUT, A SEPARATE C7 CUT AND A C8+ CUT; CATALYTICALLY DEHYDROCYCLIZING THE C7 CUT; CATALYTICALLY REFORMING THE C8+ CUT; AND THEREAFTER COMBINING THE THREE FRACTIONS. IN PREFERRED MODES OF OPERATION, THE C7 CUT IS ALSO SUBJECTED TO CATALYTIC REFORMATION AND THE C5-C6 CUT IS ISOMERIZED BEFORE COMBINATION WITH THE OTHER HYDROCARBON FRACTIONS.
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公开(公告)号：US11478724B2
公开(公告)日：2022-10-25
申请号：US17834339
申请日：2022-06-07
IPC分类号： B01D1/28 , B01D1/26 , B01D3/14 , B01D3/00 , B01D1/00 , B01D9/00 , C07B31/00 , C07B33/00 , C07B35/02 , C07B35/04 , C07B35/08 , C07B37/08 , C07B37/10 , C10B55/00 , C10G7/00 , C10G9/00 , C10G11/00 , C10G31/06 , C10G45/00 , C10G47/00 , C10G49/00 , C10G50/00 , C10G51/00 , C10G53/00 , C10G55/00 , C10G57/00 , C10G59/00 , C10G61/00 , C10G63/00 , C10G65/00 , C10G67/00 , C10G69/00
摘要： The present invention utilizes mechanical vapor compression and/or thermal vapor compression integrating compression loops across multiple process stages. A sequential network of compressors is utilized to increase the pressure and condensing temperature of the vapors within each process stage, as intra-vapor flow, and branching between process stages, as inter-vapor flow. Because the vapors available are shared among and between compressor stages, the number of compressors can be reduced, improving economics. Balancing vapor mass flow through incremental compressor stages which traverse multiple process stages by splitting vapors between compressor stages enables the overall vapor-compression system to be tailored to individual process energy requirements and to accommodate dynamic fluctuations in process conditions.
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公开(公告)号：US11291927B2
公开(公告)日：2022-04-05
申请号：US17374959
申请日：2021-07-13
IPC分类号： B01D1/26 , B01D1/28 , B01D3/14 , B01D3/00 , B01D1/00 , B01D9/00 , C07B31/00 , C07B33/00 , C07B35/02 , C07B35/04 , C07B35/08 , C07B37/08 , C07B37/10 , C10B55/00 , C10G7/00 , C10G9/00 , C10G11/00 , C10G31/06 , C10G45/00 , C10G47/00 , C10G49/00 , C10G50/00 , C10G51/00 , C10G53/00 , C10G55/00 , C10G57/00 , C10G59/00 , C10G61/00 , C10G63/00 , C10G65/00 , C10G67/00 , C10G69/00
摘要： This disclosure provides systems and methods that utilize integrated mechanical vapor or thermal vapor compression to upgrade process vapors and condense them to recover the heat of condensation across multiple processes, wherein the total process energy is reduced. Existing processes that are unable to recover the heat of condensation in vapors are integrated with mechanical or thermal compressors that raise vapor pressures and temperatures sufficient to permit reuse. Integrating multiple processes permits vapor upgrading that can selectively optimize energy efficiency, environmental sustainability, process economics, or a prioritized blend of such goals. Mechanical or thermal vapor compression also alters the type of energy required in industrial processes, favoring electro-mechanical energy which can be supplied from low-carbon, renewable sources rather than combustion of carbonaceous fuels.
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公开(公告)号：US09803511B2
公开(公告)日：2017-10-31
申请号：US15087518
申请日：2016-03-31
IPC分类号： F01K25/08 , C10G69/00 , F01K27/00 , C10G59/00 , C10G61/00 , C10G63/00 , F01K3/00 , F01K13/00 , C10G99/00
CPC分类号： F01K25/08 , C10G59/00 , C10G61/00 , C10G63/00 , C10G69/00 , C10G99/00 , C10G2300/00 , C10G2300/4006 , C10G2400/04 , C10G2400/30 , F01K3/00 , F01K13/00 , F01K27/00
摘要： Optimizing power generation from waste heat in large industrial facilities such as petroleum refineries by utilizing a subset of all available hot source streams selected based, in part, on considerations for example, capital cost, ease of operation, economics of scale power generation, a number of ORC machines to be operated, operating conditions of each ORC machine, combinations of them, or other considerations are described. Subsets of hot sources that are optimized to provide waste heat to one or more ORC machines for power generation are also described. Further, recognizing that the utilization of waste heat from all available hot sources in a mega-site such as a petroleum refinery and aromatics complex is not necessarily or not always the best option, hot source units in petroleum refineries from which waste heat can be consolidated to power the one or more ORC machines are identified.
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