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1. 发明申请

WO2012021341A3 PRODUCING 1-BUTENE FROM AN OXYGENATE-TO-OLEFIN REACTION SYSTEM 审中-公开
标题翻译：从氧化剂到烯烃反应体系生产1-丁烯
公开(公告)号：WO2012021341A3
公开(公告)日：2012-06-07
申请号：PCT/US2011046351
申请日：2011-08-03
申请人： UOP LLC , MONTALBANO JOSEPH A , KRUPA STEVEN L , SENETAR JOHN J , GREGOR JOSEPH , BOZZANO ANDREA G , SANDHU GARY
发明人： MONTALBANO JOSEPH A , KRUPA STEVEN L , SENETAR JOHN J , GREGOR JOSEPH , BOZZANO ANDREA G , SANDHU GARY
IPC分类号： C07C2/86 , C07C1/20 , C07C4/06 , C07C11/08
CPC分类号： C07C41/06 , C07C1/20 , C07C4/02 , C07C4/04 , C07C5/03 , C07C11/04 , C07C11/06 , C07C11/08 , Y02P30/42 , C07C43/046 , C07C11/02
摘要： 1-butene is recovered as a purified product from an MTO synthesis and especially from an integrated MTO synthesis and hydrocarbon pyrolysis system in which the MTO system and its complementary olefin cracking reactor are combined with a hydrocarbon pyrolysis reactor in a way that facilitates the flexible production and recovery of olefins and other petrochemical products, particularly butene-1 and MTBE.
摘要翻译：作为纯化产物从MTO合成中回收1-丁烯，特别是从集成的MTO合成和烃热解系统中回收，其中MTO系统及其互补烯烃裂解反应器以便于柔性生产的方式与烃热解反应器组合并回收烯烃和其他石化产品，特别是丁烯-1和MTBE。

2. 发明申请

WO2012021343A2 INTEGRATION OF A METHANOL-TO-OLEFIN REACTION SYSTEM WITH A HYDROCARBON PYROLYSIS SYSTEM 审中-公开
标题翻译：甲醇与烯烃反应体系与烃类热分解系统的整合
公开(公告)号：WO2012021343A2
公开(公告)日：2012-02-16
申请号：PCT/US2011046357
申请日：2011-08-03
申请人： UOP LLC , BOZZANO ANDREA G , GREGOR JOSEPH , SENETAR JOHN J
发明人： BOZZANO ANDREA G , GREGOR JOSEPH , SENETAR JOHN J
IPC分类号： C07C2/86 , C07C1/20 , C07C4/06 , C07C11/08
CPC分类号： C07C1/20 , C07C4/06 , C07C7/04 , C07C7/163 , C07C7/167 , Y02P30/42 , C07C11/04 , C07C11/06 , C07C11/08
摘要： An integrated MTO synthesis and hydrocarbon pyrolysis system is described in which the MTO system and its complementary olefin cracking reactor are combined with a hydrocarbon pyrolysis reactor in a way that facilitates the flexible production of olefins and other petrochemical products, such as butene-1 and MTBE.
摘要翻译：描述了一种综合的MTO合成和烃热解系统，其中MTO系统及其互补烯烃裂解反应器与烃热解反应器结合，促进烯烃和其它石化产品如丁烯-1和MTBE的柔性生产。

3. 发明申请

WO2012087732A2 IMPROVED QUENCH TOWER CATALYST RECOVERY 审中-公开
标题翻译：改进的QUENCH塔催化剂回收
公开(公告)号：WO2012087732A2
公开(公告)日：2012-06-28
申请号：PCT/US2011065076
申请日：2011-12-15
申请人： UOP LLC , MONTALBANO JOSEPH A , SENETAR JOHN J , KAUFF DANIEL A , SANDHU GURJIT S
发明人： MONTALBANO JOSEPH A , SENETAR JOHN J , KAUFF DANIEL A , SANDHU GURJIT S
IPC分类号： B01J38/48 , B01J19/24 , B01J37/06 , B01J38/06
CPC分类号： C07C1/20 , B01D47/06 , C07C7/00 , Y02P20/584 , Y02P30/42 , C07C11/02
摘要： A process and apparatus is presented for the removal of solid particles from a gas stream. The process and apparatus includes adding a second stream of liquid that is sprayed over the openings in trays in a quench tower. The second spray stream provides for a veil of liquid to wash out solid particles from the vapor stream.
摘要翻译：介绍了一种从气流中除去固体颗粒的方法和设备。该方法和设备包括添加第二液流，该第二液流喷射在骤冷塔中托盘中的开口上。第二喷雾流提供液体的膜以从蒸气流中洗出固体颗粒。

4. 发明申请

WO2011115737A3 OLEFIN CRACKING CATALYST AND MANUFACTURING PROCESS 审中-公开
标题翻译： OLEFIN CRACKING催化剂和制造方法
公开(公告)号：WO2011115737A3
公开(公告)日：2011-12-15
申请号：PCT/US2011026033
申请日：2011-02-24
申请人： UOP LLC , VOSKOBOYNIKOV TIMUR V , QUICK MICHAEL H , SENETAR JOHN J
发明人： VOSKOBOYNIKOV TIMUR V , QUICK MICHAEL H , SENETAR JOHN J
IPC分类号： B01J29/06 , B01J37/06 , B01J37/10 , C07C4/06 , C10G11/18
CPC分类号： B01J37/10 , B01J29/035 , B01J29/06 , B01J37/06 , B01J2229/36 , B01J2229/37 , B01J2229/42 , C10G11/02 , C10G11/05 , C10G11/10 , C10G2300/1081 , C10G2300/1088 , C10G2400/20 , Y02P30/40
摘要： A new catalyst and method of preparing the catalyst is presented. The catalyst is a molecular sieve used for cracking olefins, and has improved selectivity to increase propylene yields and to reduce the amount of aromatics and methane produced. The catalyst been ion-exchanged to reduce the alkali composition in the catalyst.
摘要翻译：提出了一种新的催化剂和制备催化剂的方法。催化剂是用于裂化烯烃的分子筛，并且提高了丙烯产率的选择性和减少芳族化合物和甲烷产生量。催化剂被离子交换以降低催化剂中的碱组成。

5. 发明申请

WO2009015118A3 INTEGRATION OF OLEFIN CRACKING WITH METATHESIS TO INCREASE LIGHT OLEFINS PRODUCTION 审中-公开
标题翻译：结合元素分析的烯烃裂解增加轻质烯烃生产
公开(公告)号：WO2009015118A3
公开(公告)日：2009-04-16
申请号：PCT/US2008070713
申请日：2008-07-22
申请人： UOP LLC , SENETAR JOHN J , GLOVER BRYAN K
发明人： SENETAR JOHN J , GLOVER BRYAN K
IPC分类号： C07C4/02 , C07C6/04
CPC分类号： C07C4/06 , C07C6/04 , C07C11/04 , C07C11/06 , C10G2400/20
摘要： A process for increasing the propylene yields for hydrocarbon cracking processes. The process includes adding using alkylation of the C4s coming from the hydrocarbon cracker, and passing larger olefins to an olefin cracking unit.
摘要翻译：一种提高烃裂解过程丙烯收率的方法。该方法包括使用来自烃裂化器的C4的烷基化加入，并将较大的烯烃通入烯烃裂化单元。

6. 发明申请

WO2007079323A2 OLEFIN PRODUCTION VIA OXYGENATE CONVERSION 审中-公开
标题翻译：通过氧化转化生产烯烃
公开(公告)号：WO2007079323A2
公开(公告)日：2007-07-12
申请号：PCT/US2006061876
申请日：2006-12-11
申请人： UOP LLC , PUJADO PETER R , VORA BIPIN V , SENETAR JOHN J , MILLER LAWRENCE W
发明人： PUJADO PETER R , VORA BIPIN V , SENETAR JOHN J , MILLER LAWRENCE W
CPC分类号： C07C1/20 , C07C11/02 , C07C29/151 , C07C41/01 , C10G2300/4081 , C10G2400/20 , C10G2400/22 , C07C31/04 , C07C43/043
摘要： An improved processing for the production of light olefins via oxygenate conversion processing is provided. Synthesis gas conversion (22) such as to produce an effluent (24) including at least methanol can be integrated with oxygenate conversion processing (40) such as to produce an oxygenate conversion reactor effluent (42) including at least light olefins and dimethyl ether. At least a portion of the oxygenate conversion reactor effluent (42) can be contacted with such produced methanol (35) to effect recovery of dimethyl ether from the oxygenate conversion reactor effluent (42).
摘要翻译：提供了通过含氧化合物转化处理来生产轻质烯烃的改进处理。合成气转化（22）以产生包括至少甲醇的流出物（24）可与含氧化合物转化处理（40）整合，以便产生至少包含轻质烯烃和二甲醚的含氧化合物转化反应器流出物（42）。可以使至少一部分含氧化合物转化反应器流出物（42）与这样产生的甲醇（35）接触以实现从含氧化合物转化反应器流出物（42）回收二甲醚。

7. 发明申请

WO2012021345A3 INTEGRATION OF A METHANOL-TO-OLEFIN REACTION SYSTEM WITH A HYDROCARBON PYROLYSIS SYSTEM 审中-公开
标题翻译：甲醇与烯烃反应体系与烃类热解系统的整合
公开(公告)号：WO2012021345A3
公开(公告)日：2012-06-14
申请号：PCT/US2011046370
申请日：2011-08-03
申请人： UOP LLC , SENETAR JOHN J
发明人： SENETAR JOHN J
IPC分类号： C07C2/86 , C07C1/20 , C07C4/06 , C07C11/08
CPC分类号： C07C11/04 , C07C1/20 , C07C4/02 , C07C4/04 , C07C11/06 , C07C11/08 , Y02P30/42 , C07C11/02
摘要： An integrated MTO synthesis and hydrocarbon pyrolysis system is described in which the MTO system and its complementary olefin cracking reactor are combined with a hydrocarbon pyrolysis reactor in a way that facilitates the flexible production of olefins and other petrochemical products, such as butene-1 and MTBE.
摘要翻译：描述了一种整合的MTO合成和烃热解系统，其中MTO系统及其互补烯烃裂化反应器与烃热解反应器组合以便于灵活生产烯烃和其他石化产品如丁烯-1和MTBE 。

8. 发明申请

WO2004094355A3 SELECTIVE DIMETHYLETHER RECOVERY AND RECYCLE IN A METHANOL-TO-OLEFIN PROCESS 审中-公开
标题翻译：甲醇到烯烃过程中的选择性二甲基甲烷回收和回收
公开(公告)号：WO2004094355A3
公开(公告)日：2004-12-23
申请号：PCT/US2004012415
申请日：2004-04-22
申请人： UOP LLC , SENETAR JOHN J
发明人： SENETAR JOHN J
IPC分类号： C07C41/34 , C07C43/04 , C07C41/42
CPC分类号： C07C41/34 , Y02P30/42 , C07C43/043
摘要： An improved methanol-to-olefin (MTO) product recovery scheme is provided which enables substantial reduction in the amount of light olefins that are undesirably captured in a dimethylether (DME) recycle stream when a portion of the methanolic feed to the MTO reaction zone is used as the scrubbing solvent in a primary DME absorption zone in order to recycle this DME oxygenate by-product to the MTO reaction zone. In accordance with the present invention, a liquid solvent stream recovered from the primary DME absorption zone is subjected in a stripping zone to light olefin stripping conditions sufficient to lift a substantial portion of the light olefins that are absorbed in the DME solvent without stripping a significant portion of this methanol solvent, thereby increasing the recovery of desired light olefins while simultaneously diminishing the amount of light olefins carried by the DME recycle stream back to MTO conversion step.
摘要翻译：提供了一种改进的甲醇 - 烯烃（MTO）产物回收方案，当一部分到MTO反应区的甲醇进料的一部分是在二甲醚（DME）循环流中时，能够显着减少在二甲醚（DME）再循环流中不期望地捕获的轻质烯烃的量用作初级DME吸收区中的洗涤溶剂，以便将该DME含氧化合物副产物再循环到MTO反应区。根据本发明，从初级DME吸收区回收的液体溶剂流在汽提区进行轻质烯烃汽提条件，足以提升大部分在DME溶剂中吸收的轻质烯烃，而不剥离显着的部分该甲醇溶剂，从而增加所需轻质烯烃的回收率，同时将由DME再循环流携带的轻质烯烃的量减少回MTO转化步骤。

9. 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。

10. 发明申请

WO2007111744A3 OXYGENATE CONVERSION TO OLEFINS WITH ENHANCED CARBONYL RECOVERY 审中-公开
标题翻译：氧化碳转化为烯烃与增强碳回收
公开(公告)号：WO2007111744A3
公开(公告)日：2007-12-06
申请号：PCT/US2006062264
申请日：2006-12-18
申请人： UOP LLC , SENETAR JOHN J
发明人： SENETAR JOHN J
IPC分类号： C07C2/00
CPC分类号： C07C1/20 , C10G2300/42 , C10G2400/20 , Y10S585/91 , C07C11/02
摘要： Improved processing of an oxygenate-containing feedstock involving increased or enhanced removal or recovery of carbonyls, particularly, acetaldehyde via either or both application of a more stringent stripping regime or addition of a sulfite-containing material.
摘要翻译：包含含氧化合物的原料的改进处理涉及增加或增强羰基化合物的去除或回收，特别是通过更严格的汽提方法或添加含亚硫酸盐的材料中的一种或两种来进行乙醛。

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