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1. 发明申请

WO2010062462A3 IMPROVED HEAT PUMP FOR HIGH PURITY BOTTOM PRODUCT 审中-公开
标题翻译：改善高纯度底漆产品的热泵
公开(公告)号：WO2010062462A3
公开(公告)日：2010-07-29
申请号：PCT/US2009058726
申请日：2009-09-29
申请人： UOP LLC , SECHRIST PAUL A , WEGERER DAVID A
发明人： SECHRIST PAUL A , WEGERER DAVID A
IPC分类号： B01D3/00 , C02F1/04 , F25B30/00
CPC分类号： B01D3/322 , B01D3/4266
摘要： An apparatus for reducing the energy consumption of a distillation column (10) is disclosed. The apparatus draws off an intermediate vapor stream (60) from the rectification section (20) of the distillation column (10), where the vapor stream is compressed and used to reboil a portion of the bottoms stream. The compressed vapor stream transfers energy to the bottoms stream, thereby condensing a portion of the vapor stream while vaporizing the bottoms stream.
摘要翻译：公开了一种用于降低蒸馏塔（10）的能量消耗的装置。该设备从蒸馏塔（10）的整流段（20）中抽出中间蒸气流（60），蒸馏物流被压缩并用于再沸一部分底部物流。压缩的蒸汽流将能量转移到塔底物流，从而在蒸发塔底物流的同时冷凝蒸汽流的一部分。

2. 发明申请

WO2009064543A2 SPLITTER WITH MULTI-STAGE HEAT PUMP COMPRESSOR AND INTER-REBOILER 审中-公开
标题翻译：具有多级热泵压缩机和内部再生器的分体器
公开(公告)号：WO2009064543A2
公开(公告)日：2009-05-22
申请号：PCT/US2008078295
申请日：2008-09-30
申请人： UOP LLC , WEGERER DAVID A , SECHRIST PAUL A
发明人： WEGERER DAVID A , SECHRIST PAUL A
IPC分类号： B01D3/00 , B01D53/00 , C07C4/06 , C10G11/00
CPC分类号： B01D3/14 , C07C7/04 , Y10S203/04 , Y10S203/08 , Y10S203/20 , Y10S203/90 , C07C11/06
摘要： A splitter system is disclosed that produces a product stream from a mixed stream of two materials. A multi-stage heat pump compressor is used in combination with a bottoms reboiler and an intermediate reboiler resulting in reduced utility consumption. The intermediate reboiler enables use of a lower temperature heat source relative to the bottoms reboiler heat source. The first stage of the multi-stage heat pump compressor delivers pressurized overhead vapor to the intermediate reboiler and the second stage provides pressurized overhead vapor to the bottoms reboiler. The disclosed design and method lessens the heat pump compressor power consumption and trim condenser duty for a propylene/propane splitter system by over 20%. A third stage of compression upstream of the overhead trim condenser may be used for purposes of making the column pressure and temperatures independent of the trim condenser temperature.
摘要翻译：公开了一种从两种材料的混合流产生产物流的分流器系统。多级热泵压缩机与底部再沸器和中间再沸器组合使用，导致降低的功耗。中间再沸器使得能够使用相对于底部再沸器热源的较低温度的热源。多级热泵压缩机的第一级将加压的塔顶蒸气输送到中间再沸器，第二级向底部再沸器提供加压的顶部蒸气。所公开的设计和方法将丙烯/丙烷分配器系统的热泵压缩机功率消耗和修整电容器负荷降低20％以上。顶置式冷凝器上游的第三级压缩可用于使柱压力和温度与修整冷凝器温度无关。

3. 发明申请

WO2010077439A3 TEMPERATURE CONTROLLED ADSORPTION FOR DEHYDRATION OF WATER RICH STREAMS 审中-公开
标题翻译：温度控制吸附水分流失
公开(公告)号：WO2010077439A3
公开(公告)日：2010-08-26
申请号：PCT/US2009063849
申请日：2009-11-10
申请人： UOP LLC , DUNNE STEPHEN R , WEGERER DAVID A
发明人： DUNNE STEPHEN R , WEGERER DAVID A
IPC分类号： B01D15/00 , C02F11/12 , C10L1/32 , C12P7/08
CPC分类号： C10L1/32 , B01J20/28011 , B01J20/2803 , B01J20/28042 , B01J20/3042 , B01J20/3204 , B01J20/3206 , B01J20/3238 , B01J20/3408 , C10G25/003 , C10G25/03 , C10G33/04
摘要： A process for dehydration of a water rich stream, the process comprising providing a process stream to at least one temperature controlled adsorber that is undergoing adsorption, where the at least one temperature controlled adsorber has adsorption flow passages containing an adsorptive material coating and heat transfer flow passages and producing a dehydrated effluent stream. There may be at least one temperature controlled adsorber undergoing a regeneration cycle and at least one undergoing a bed to bed interchange cycle. The process stream is passed through the adsorption flow passages, where water is adsorbed by the adsorptive material coating, and a heat of adsorption is generated. The heat of adsorption is removed by passing a cooling fluid through the heat transfer flow passages. The process stream can be a process stream for producing motor fuel grade ethanol.
摘要翻译：一种用于使富水流脱水的方法，该方法包括向至少一个经受吸附的温度控制的吸附器提供工艺物流，其中至少一个温度控制的吸附器具有含有吸附材料涂层和传热流的吸附流动通道并产生脱水流出物流。可能存在至少一个经历再生循环的温度控制的吸附器和至少一个经历床以进行交换循环的床。工艺物流通过吸附流动通道，其中吸附材料涂层吸收水分，产生吸附热。通过使冷却流体通过传热流动通道来除去吸附热。工艺流可以是生产汽油燃料级乙醇的工艺流。

4. 发明申请

WO2012148834A3 PROCESS FOR INCREASING AROMATICS PRODUCTION 审中-公开
公开(公告)号：WO2012148834A3
公开(公告)日：2013-01-24
申请号：PCT/US2012034610
申请日：2012-04-23
申请人： UOP LLC , GAJDA GREGORY J , WIER MARY JO , LAPINSKI MARK P , WEGERER DAVID A , VANDEN BUSSCHE KURT M , MOSER MARK D
发明人： GAJDA GREGORY J , WIER MARY JO , LAPINSKI MARK P , WEGERER DAVID A , VANDEN BUSSCHE KURT M , MOSER MARK D
IPC分类号： C10G63/04 , C10G35/04 , C10G59/02 , C10G61/02
CPC分类号： C10G35/04 , C10G35/06 , C10G35/065 , C10G35/085 , C10G59/06 , C10G2300/1044 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.

5. 发明申请

WO2009015140A3 USE OF OLEFIN CRACKING TO PRODUCE ALKYLATE 审中-公开
标题翻译：使用烯烃裂解生产烷基酯
公开(公告)号：WO2009015140A3
公开(公告)日：2009-05-14
申请号：PCT/US2008070752
申请日：2008-07-22
申请人： UOP LLC , SENETAR JOHN J , WEGERER DAVID A , TOWLER GAVIN P
发明人： SENETAR JOHN J , WEGERER DAVID A , TOWLER GAVIN P
IPC分类号： C07C2/04
CPC分类号： C10G29/205 , C10G57/005
摘要： A process for producing a feedstock for gasolines having very little aromatic concentrations is disclosed. The present process uses by-product olefins and alkanes to produce an alkylate for use in gasoline blending.
摘要翻译：公开了一种生产芳香族浓度很低的汽油的原料的方法。本发明方法使用副产物烯烃和烷烃来生产用于汽油混合的烷基化物。

6. 发明申请

WO2012148878A3 PROCESS FOR INCREASING AROMATICS PRODUCTION 审中-公开
标题翻译：增加芳香剂生产的过程
公开(公告)号：WO2012148878A3
公开(公告)日：2013-02-21
申请号：PCT/US2012034742
申请日：2012-04-24
申请人： UOP LLC , GAJDA GREGORY J , VANDEN BUSSCHE KURT M , MOSER MARK D , WEGERER DAVID A
发明人： GAJDA GREGORY J , VANDEN BUSSCHE KURT M , MOSER MARK D , WEGERER DAVID A
IPC分类号： C10G61/02 , C10G35/04 , C10G59/02
CPC分类号： C10G59/00 , C10G2300/1044 , C10G2400/02 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译：介绍了一种重整烃流的方法。该过程涉及将石脑油原料流分成至少两个原料流，并将每个原料流送入分离重整器。重整器在不同的条件下运行以利用不同烃组分的反应性质的差异。该方法使用共同的催化剂，并且回收所产生的所需芳族化合物的常见下游方法。

7. 发明申请

WO2012148811A3 PROCESS FOR INCREASING AROMATICS PRODUCTION 审中-公开
标题翻译：增加生产力的过程
公开(公告)号：WO2012148811A3
公开(公告)日：2013-02-14
申请号：PCT/US2012034443
申请日：2012-04-20
申请人： UOP LLC , WEGERER DAVID A , VANDEN BUSSCHE KURT M , MOSER MARK D
发明人： WEGERER DAVID A , VANDEN BUSSCHE KURT M , MOSER MARK D
IPC分类号： C10G61/02 , C10G35/04 , C10G59/02
CPC分类号： C10G59/00 , C10G2300/1044 , C10G2400/02 , C10G2400/30
摘要： A process for reforming a hydrocarbon stream is presented. The process involves splitting a naphtha feedstream to at least two feedstreams and passing each feedstream to separation reformers. The reformers are operated under different conditions to utilize the differences in the reaction properties of the different hydrocarbon components. The process utilizes a common catalyst, and common downstream processes for recovering the desired aromatic compounds generated.
摘要翻译：提出了一种重整烃流的方法。该方法包括将石脑油进料流分成至少两个进料流并将每个进料流通过分离重整器。改性剂在不同条件下运行，以利用不同烃组分的反应性质的差异。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。

8. 发明申请

WO2008042613A3 ABSORPTION RECOVERY PROCESSING OF LIGHT OLEFINS FREE OF CARBON DIOXIDE 审中-公开
标题翻译：不含二氧化碳的轻质烯烃吸收回收工艺
公开(公告)号：WO2008042613A3
公开(公告)日：2008-06-12
申请号：PCT/US2007079028
申请日：2007-09-20
申请人： UOP LLC , SCHULTZ MICHAEL A , TOWLER GAVIN P , WEGERER DAVID A , BRADY JOHN P , LECHNICK WILLIAM J
发明人： SCHULTZ MICHAEL A , TOWLER GAVIN P , WEGERER DAVID A , BRADY JOHN P , LECHNICK WILLIAM J
IPC分类号： C10G11/00 , C10G11/18
CPC分类号： C07C7/005 , B01D53/1475 , B01D53/77 , B01D2256/24 , B01D2257/504 , C07C7/11 , C10G9/206 , C10G2400/20 , Y02C10/06 , Y02P20/152 , Y02P20/51 , Y02P20/52 , Y02P30/40 , Y02P30/442 , C07C11/06 , C07C11/04
摘要： Processing schemes and arrangements for the amine treatment of high olefin content (e.g., ethylene-rich) carbon dioxide-containing streams such as for the effective separation and removal of carbon dioxide therefrom are provided. Corresponding or associated processing schemes and arrangements for the catalytic cracking of a heavy hydrocarbon feedstock (212) and obtaining light olefins substantially free of carbon dioxide via absorption-based product recovery (236) are also provided.
摘要翻译：提供了用于胺处理高烯烃含量（例如富含乙烯）含二氧化碳的料流的加工方案和设置，例如用于有效分离和除去二氧化碳。还提供了用于重质烃原料（212）的催化裂化和通过基于吸收的产物回收（236）获得基本上不含二氧化碳的轻质烯烃的相应或相关的处理方案和装置。

9. 发明申请

WO2008039906A2 ABSORPTION RECOVERY PROCESSING OF FCC-PRODUCED LIGHT OLEFINS 审中-公开
标题翻译： FCC生产的轻质烯烃的吸收回收工艺
公开(公告)号：WO2008039906A2
公开(公告)日：2008-04-03
申请号：PCT/US2007079675
申请日：2007-09-27
申请人： UOP LLC , WEGERER DAVID A , SCHULTZ MICHAEL A
发明人： WEGERER DAVID A , SCHULTZ MICHAEL A
IPC分类号： C10G9/00
CPC分类号： C10G21/14 , C10G9/32 , C10G55/06 , C10G70/06 , C10G2300/202 , C10G2300/44 , C10G2400/20 , C10G2400/22
摘要： Processing schemes and arrangements are provided for the processing a heavy hydrocarbon feedstock (212) via hydrocarbon cracking processing with selected hydrocarbon fractions being obtained via absorption-based product recovery.
摘要翻译：提供加工方案和装置用于通过烃裂化处理来处理重质烃原料（212），其中通过基于吸收的产物回收获得选定的烃馏分。

10. 发明专利

RU2698814C1 СТУПЕНЧАТОЕ РАЗМЕЩЕНИЕ КАТАЛИЗАТОРА В СПОСОБЕ НА ОСНОВЕ КАТАЛИТИЧЕСКОЙ РЕАКЦИИ 未知
公开(公告)号：RU2698814C1
公开(公告)日：2019-08-30
申请号：RU2018117449
申请日：2016-10-12
申请人： UOP LLC
发明人： EGOLF BRYAN J , HORN IAN G , WEGERER DAVID A , WERBA GREGORY R
IPC分类号： C10G35/04 , C10G35/06 , C10G59/02
摘要： Изобретениеотноситсяк способуриформинга, вкотором: углеводородныйпоток 105, имеющийв своёмсоставеуглеводороды, содержащиеот 5 до 12 атомовуглерода, вводятв зонуриформинга, содержащуюкатализаторриформинга, приэтомзонариформингавключаетв себяпоменьшеймеречетыререакторариформинга, причёмкаждыйреакторриформингахарактеризуетсяопределённымнаборомрабочихусловийриформингадляполучениявыходящегопотока 125 риформатаи последнийреакторриформингасодержитменьшекатализатора, чемпредпоследнийреакторриформинга, причемпервыйреактор 145 риформингаработаетпритемпературеот 480°C до 560°C, второйреактор 150 риформингаработаетпритемпературеот 510°C до 560°C, третийреактор 175 риформингаработаетпритемпературеот 520°C до 560°C, ачетвёртыйреактор 205 риформингаработаетпритемпературеот 540°C до 560°C изначениечасовойобъемнойскоростижидкости (LHSV) впервомреакторе 145 риформингасоставляетот 8,5 чдо 20 ч, значение LHSV вовторомреакторе 150 риформингасоставляетот 8,5 чдо 12 ч, значение LHSV втретьемреакторе 175 риформингасоставляетот 6,5 чдо 8,5 ч, азначение LHSV вчетвёртомреакторе 205 риформингасоставляетот 12 чдо 30 ч. Использованиепредлагаемогоспособапозволяетувеличиватьоктановоечислобензинабезизлишнегоувеличениясодержанияароматическихсоединенийв бензине. 7 з.п. ф-лы, 1 ил., 2 табл., 1 пр.

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