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1.发明申请REACTOR AND HEATER CONFIGURATION SYNERGIES IN PARAFFIN DEHYDROGENATION PROCESS 审中-公开石蜡脱氢过程中反应器和加热器组态的协同作用
公开(公告)号：WO2017003786A1
公开(公告)日：2017-01-05
申请号：PCT/US2016/038715
申请日：2016-06-22
Applicant: UOP LLC
Inventor： GATTUPALLI, Rajeswar , YUAN, Quan , SADLER, Clayton C. , VETTER, Michael J. , EGOLF, Bryan J.
CPC classification number: B01J8/087 , B01J8/00 , B01J2208/00132 , B01J2208/00141 , B01J2208/00504 , C10G35/04 , C10G35/12 , F22B29/06 , F24H1/145 , F28D7/00 , F28D7/06
Abstract: An apparatus for heating a process fluid is presented. The apparatus is for improving the foot-print of a fired heater and to reduce the fired heater volume. The apparatus includes a W-shaped process coil to provide for a smaller single-cell fired heater, and a fired heater with a lower profile, providing flexibility in positioning relative to downstream reactors.
Abstract translation: 介绍了一种用于加热过程流体的装置。 该设备用于改善火焰加热器的足迹并减少火焰加热器的体积。 该设备包括W形工艺线圈，以提供更小的单电池燃烧加热器，以及具有更低轮廓的燃烧加热器，相对于下游反应器提供了定位的灵活性。
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公开(公告)号：WO2019089939A1
公开(公告)日：2019-05-09
申请号：PCT/US2018/058726
申请日：2018-11-01
Applicant: UOP LLC
Inventor： DIGIULIO, Christopher , SADLER, Clayton C.
Abstract: Processes for dehydrogenation of a hydrocarbon feedstock are described. The process can be run at lower H 2 /HC ratios and lower RITs while maintaining coke production at the same level as operation at higher H 2 /HC ratios and higher RITs without decreasing the yield per pass. Acceptable levels of coke were achieved when operating the process at low hydrogen to hydrocarbon molar ratio in the range of 0.01 to 0.40 and reactor inlet temperatures in the range of 500° - 645°C.
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公开(公告)号：WO2016100109A1
公开(公告)日：2016-06-23
申请号：PCT/US2015/065193
申请日：2015-12-11
Applicant: UOP LLC
Inventor： SADLER, Clayton C. , WEGERER, David A. , SALAZAR, Juan , CARTER, Elizabeth
CPC classification number: B01D53/8659 , B01D53/02 , B01D53/06 , B01D2257/2045 , B01D2258/0283 , B01D2259/40083 , B01J21/04 , B01J27/13 , B01J35/08 , C10G2300/70
Abstract: A process for adsorbing hydrogen chloride (HCl) from a regeneration vent gas. The regeneration vent gas from a regeneration zone is cooled, and the cooled regeneration vent gas is passed to an adsorption zone that is spaced apart from the regeneration zone. HCl from the regeneration vent gas is adsorbed onto a spent catalyst in the adsorption zone to enrich the spent catalyst with HCl to provide HCl-rich spent catalyst and deplete HCl from the regeneration vent gas to provide HCl-lean regeneration vent gas. The HCl-lean regeneration vent gas is purged as an effluent gas. The HCl-rich spent catalyst is passed to the regeneration zone.
Abstract translation: 从再生排气中吸附氯化氢（HCl）的方法。 来自再生区域的再生排出气体被冷却，并且冷却的再生排出气体被传送到与再生区间隔开的吸附区域。 来自再生排出气体的HCl被吸附到吸附区中的废催化剂上以用HCl富集废催化剂以提供富含HCl的废催化剂并从再生排出气体中除去HCl以提供不含HCl的再生排出气体。 将贫HCl再生排出气体作为流出气体吹扫。 将富含HCl的废催化剂送入再生区。
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4.发明申请
公开(公告)号：WO2014081555A1
公开(公告)日：2014-05-30
申请号：PCT/US2013/068406
申请日：2013-11-05
Applicant: UOP LLC
Inventor： MOSER, Mark D. , SADLER, Clayton C.
Abstract: A process is presented for increasing the aromatics content in a reformate process stream. The process modifies existing processes to change the operation without changing the reactors or heating units. The process includes bypasses to utilize heating capacity of upstream heating units, and passes the excess capacity of the upstream heating units to downstream process streams.
Abstract translation: 提出了一种用于增加重整过程流中的芳烃含量的方法。 该过程修改现有流程以改变操作而不改变反应器或加热单元。 该过程包括旁路以利用上游加热单元的加热能力，并将上游加热单元的剩余容量传递到下游处理流。
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5.发明申请PROCESS FOR CONVERTING A HYDROCARBON STREAM, AND OPTIONALLY PRODUCING A PROCESSED DISTILLATE PRODUCT 审中-公开转化烃流的方法和可选择生产加工的蒸馏产物
公开(公告)号：WO2013138001A1
公开(公告)日：2013-09-19
申请号：PCT/US2013/025662
申请日：2013-02-12
Applicant: UOP LLC
Inventor： SADLER, Clayton C. , GOSLING, Christopher D.
CPC classification number: C10G45/58 , C10G47/26 , C10G65/10 , C10G65/12 , C10G69/04 , C10G2400/02 , C10G2400/30
Abstract: One exemplary embodiment can be a process for converting a hydrocarbon stream. The process can include passing the hydrocarbon stream having one or more C40+ hydrocarbons to a slurry hydrocracking zone to obtain a distillate hydrocarbon stream having one or more C9-C22 hydrocarbons, and passing the distillate hydrocarbon stream to a hydrocracking zone for selectively hydrocracking aromatic compounds including at least two rings obtaining a processed distillate product.
Abstract translation: 一个示例性实施方案可以是用于转化烃流的方法。 该方法可以包括使具有一个或多个C 40 +烃的烃流通过浆料加氢裂化区获得具有一个或多个C 9 -C 22烃的馏出物烃流，并将馏出物烃流送入加氢裂化区，以选择性加氢裂化芳族化合物，包括 至少两个环获得经处理的馏出物。
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Patent Agency Ranking
公开(公告)号：WO2016100111A1
公开(公告)日：2016-06-23
申请号：PCT/US2015/065201
申请日：2015-12-11
Applicant: UOP LLC
Inventor： SADLER, Clayton C. , WEGERER, David A. , LIPPMAN, Matthew
CPC classification number: B01D53/0462 , B01D53/0438 , B01D53/0454 , B01D53/08 , B01D2253/104 , B01D2253/108 , B01D2255/102 , B01D2256/16 , B01D2256/24 , B01D2256/245 , B01D2257/2045 , B01D2257/2064 , B01D2257/2066 , B01D2257/80 , B01D2259/4009
Abstract: Process for adsorbing a species from a feed gas stream. Feed gas stream is introduced to an adsorption zone having a sorbent. Species from the feed gas stream is adsorbed onto the sorbent at an adsorbing temperature to enrich the sorbent with the species and deplete the species from the feed gas stream. Species-lean product gas stream is output. Species-rich sorbent from the adsorption zone is passed to a regeneration zone. Regenerant gas at a regenerating temperature greater than the adsorbing temperature is introduced into the regeneration zone to strip the species from the species-rich sorbent. Regenerated sorbent from the regeneration zone passes to a cooling zone disposed below the regeneration zone. Regenerated sorbent is cooled at a cooling temperature below the regenerating temperature. Cooled sorbent is transferred to the adsorbent zone.
Abstract translation: 从进料气流中吸附物质的方法。 将进料气流引入具有吸附剂的吸附区。 来自进料气流的物质在吸附温度下吸附到吸附剂上，以使物质富集吸附剂并从进料气流中消耗物质。 输出物种贫产品气流。 来自吸附区的物种丰富的吸附剂被传递到再生区。 将再生温度大于吸附温度的再生气体引入再生区，以从物种丰富的吸附剂中剥离物质。 来自再生区的再生吸附剂进入设置在再生区下方的冷却区。 再生吸附剂在低于再生温度的冷却温度下冷却。 冷却的吸附剂转移到吸附剂区域。
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公开(公告)号：WO2015031060A1
公开(公告)日：2015-03-05
申请号：PCT/US2014/050887
申请日：2014-08-13
Applicant: UOP LLC
Inventor： SADLER, Clayton C. , MURTY, Vedula K.
Abstract: A process and apparatus is provided to produce desulfurized diesel at low pressure with high cetane rating. A hydrotreated stream is stripped and fed to a saturation reactor. The saturated stream is stripped again and fractionated to provide diesel product. Unconverted oil may be hydrocracked and stripped with the saturated product.
Abstract translation: 提供了一种方法和设备，用于在低压下生产脱硫柴油，具有高十六烷值。 将加氢处理的物流汽提并进料至饱和反应器。 将饱和物流再次汽提并分馏以提供柴油产品。 未转化的油可以被加氢裂化并用饱和产物汽提。
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公开(公告)号：WO2014074969A1
公开(公告)日：2014-05-15
申请号：PCT/US2013/069379
申请日：2013-11-11
Applicant: UOP LLC
Inventor： FREET, Christian D. , LUEBKE, Charles P. , SADLER, Clayton C.
CPC classification number: C07C2/06 , C07C2/12 , C07C2/18 , C07C7/09 , C07C11/02 , C07C2527/173 , C07C2529/70 , C10G50/00 , C10G57/02
Abstract: A process and apparatus that uses a debutanizer with a side stripper can recover a light stream, an intermediate stream and a liquid stream. One of the intermediate stream and the liquid stream can be recycled to oligomerization or to fluid catalytic cracking.
Abstract translation: 使用脱丁烷剂与侧脱料剂的方法和设备可以回收轻质流，中间流和液体流。 中间料流和液体料流之一可以再循环到低聚或流化催化裂化。
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公开(公告)号：WO2012148829A2
公开(公告)日：2012-11-01
申请号：PCT/US2012/034605
申请日：2012-04-23
Applicant: UOP LLC , MOSER, Mark D. , SADLER, Clayton C. , LAPINSKI, Mark P. , VANDEN BUSSCHE, Kurt M.
Inventor： MOSER, Mark D. , SADLER, Clayton C. , LAPINSKI, Mark P. , VANDEN BUSSCHE, Kurt M.
CPC classification number: C10G35/04 , C07C4/06 , C10G35/06 , C10G61/04 , C10G2300/1044 , C10G2300/4018 , C10G2400/30 , Y02P20/584 , C07C15/02 , C07C15/067
Abstract: A process for reforming a hydrocarbon stream is presented. The process involves increasing the processing temperatures in the reformers. The reformers are operated under different conditions to utilize advantages in the equilibriums, but require modifications to prevent increasing thermal cracking and to prevent increases in coking. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
Abstract translation: 提出了一种重整烃流的方法。 该方法涉及提高改性剂中的加工温度。 改造者在不同的条件下运行，以利用平衡中的优点，但需要修改以防止增加热裂纹和防止焦化增加。 该方法利用普通的催化剂和用于回收生成的所需芳族化合物的常见的下游方法。
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公开(公告)号：WO2011084354A3
公开(公告)日：2011-07-14
申请号：PCT/US2010/059849
申请日：2010-12-10
Applicant: UOP LLC , SADLER, Clayton C. , WIER, Mary Jo , STINE, Laurence O. , NAUNHEIMER, Christopher
Inventor： SADLER, Clayton C. , WIER, Mary Jo , STINE, Laurence O. , NAUNHEIMER, Christopher
Abstract: Systems and processes for hydrocarbon conversion are provided that utilize a plurality of moving bed reactors. The reactors may be moving bed radial flow reactors. Optional mixers that mix a portion of a second hydrocarbon feed with the effluent stream from an upstream reactor, to produce reactor feed streams may be employed, and the reactor feed streams may be introduced at injection points prior to each reactor. Catalyst can be provided from the reaction zone of one reactor to the reaction zone of a downstream reactor through catalyst transfer pipes, and can be regenerated after passing through the reaction zones of the reactors. The moving bed reactors can be stacked in one or more reactor stacks.
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