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1. 发明授权

US5689015A Method for the production of ether and alkylate from a paraffin feedstock 失效
标题翻译：从石蜡原料生产醚和烷基化物的方法
公开(公告)号：US5689015A
公开(公告)日：1997-11-18
申请号：US613267
申请日：1996-03-08
申请人： Harold R. Hunt , Mark D. Scharre , Warren M. Ewert
发明人： Harold R. Hunt , Mark D. Scharre , Warren M. Ewert
IPC分类号： C07C9/16 , C07C41/06
CPC分类号： C07C9/16 , C07C41/06
摘要： A process for the production of ethers and alkylate from a paraffin feedstock. The process includes a novel arrangement of dehydrogenation, isomerization, separation, etherification and alkylation to provide such products.
摘要翻译：从石蜡原料生产醚和烷基化物的方法。该方法包括脱氢，异构化，分离，醚化和烷基化的新颖布置以提供这样的产物。

2. 发明授权

US5750798A Method for making ether from a paraffin feedstock 失效
标题翻译：从石蜡原料制造乙醚的方法
公开(公告)号：US5750798A
公开(公告)日：1998-05-12
申请号：US573219
申请日：1995-12-13
申请人： Mark D. Scharre , Warren M. Ewert , Harold R. Hunt
发明人： Mark D. Scharre , Warren M. Ewert , Harold R. Hunt
IPC分类号： C07C41/06
CPC分类号： C07C41/06
摘要： A process for the production of ethers from a paraffin feedstock. The process includes a novel arrangement of dehydrogenation, isomerization, hydroisomerization, separation and etherification to provide a novel method for the production of ethers from a paraffin feedstock.
摘要翻译：一种从石蜡原料生产醚的方法。该方法包括脱氢，异构化，加氢异构化，分离和醚化的新颖布置，以提供从石蜡原料生产醚的新方法。

3. 发明授权

US4876410A Catalyst support, and catalyst for olefin dimerization 失效
标题翻译：催化剂载体和烯烃二聚化催化剂
公开(公告)号：US4876410A
公开(公告)日：1989-10-24
申请号：US271135
申请日：1988-11-14
申请人： Warren M. Ewert , Donald H. Kubicek , Charles A. Drake
发明人： Warren M. Ewert , Donald H. Kubicek , Charles A. Drake
IPC分类号： B01J23/04 , B01J27/232 , B01J37/00 , C07C2/24
CPC分类号： C07C2/24 , B01J23/04 , B01J27/232 , B01J37/0009 , C07C2523/04 , C07C2527/232
摘要： Catalyst supports, catalyst systems, methods for the preparation thereof, and dimerization process therewith are provided catalyst supports are prepared from an alkali metal carbonate, water, alcohol, and optionally at least one carbonaceous compound. Catalyst systems comprise at least one elemental alkali metal deposited on the catalyst support. Optionally, the catalyst system further comprises at least one promoter.
摘要翻译：提供了催化剂载体，催化剂体系，其制备方法及其二聚过程，催化剂载体由碱金属碳酸盐，水，醇和任选的至少一种含碳化合物制备。催化剂体系包含沉积在催化剂载体上的至少一种元素碱金属。任选地，催化剂体系还包含至少一种助催化剂。

4. 发明授权

US06380451B1 Methods for restoring the heat transfer coefficient of an oligomerization reactor 有权
标题翻译：恢复低聚反应器传热系数的方法
公开(公告)号：US06380451B1
公开(公告)日：2002-04-30
申请号：US09474306
申请日：1999-12-29
申请人： Bruce E. Kreischer , Warren M. Ewert , Ronald D. Knudsen
发明人： Bruce E. Kreischer , Warren M. Ewert , Ronald D. Knudsen
IPC分类号： C07C208
CPC分类号： B08B9/08 , B01J19/002 , B01J2219/00252 , C07C2/08 , Y02P20/52 , Y02P20/582 , Y10S585/95
摘要： The specification discloses a method for cleaning an oligomerization reactor after making a higher olefin in the reactor. An olefin is reacted in the presence of a catalyst comprising an aluminum alkyl to form an olefin reaction product. For example, ethylene can be trimerized in the reaction to produce 1-hexene. The reaction also causes a co-product residue of the catalyst to form on the interior surface of the reactor. The interior surface of the reactor is then contacted with an alcohol under conditions effective to remove at least a substantial amount of the catalyst residue from the interior surface of the reactor. The catalyst-removing step can be carried out by combining an alcohol with the process medium used in the reactor. The combined medium can be used to remove both the accumulated polymer co-product and the accumulated catalyst residue from the reactor.
摘要翻译：该说明书公开了在反应器中制备高级烯烃之后清洗低聚反应器的方法。烯烃在包含烷基铝的催化剂的存在下反应以形成烯烃反应产物。例如，乙烯可以在反应中进行三聚，以产生1-己烯。该反应还导致催化剂的副产物残余物在反应器的内表面上形成。然后在有效地从反应器的内表面除去至少大量催化剂残余物的条件下，将反应器的内表面与醇接触。催化剂除去步骤可以通过将醇与反应器中使用的加工介质结合来进行。组合的介质可用于从反应器中除去累积的聚合物共同产物和累积的催化剂残余物。

5. 发明授权

US4810688A Catalyst support and catalyst for olefin dimerization 失效
标题翻译：用于烯烃二聚化的催化剂载体和催化剂
公开(公告)号：US4810688A
公开(公告)日：1989-03-07
申请号：US112802
申请日：1987-10-23
申请人： Warren M. Ewert , Donald H. Kubicek , Charles A. Drake
发明人： Warren M. Ewert , Donald H. Kubicek , Charles A. Drake
IPC分类号： B01J23/04 , B01J27/232 , B01J37/00 , C07B61/00 , C07C1/00 , C07C2/08 , C07C2/24 , C07C11/02 , C07C67/00 , B01J32/00
CPC分类号： C07C2/24 , B01J23/04 , B01J27/232 , B01J37/0009 , C07C2523/04 , C07C2527/232
摘要： Catalyst supports, catalyst systems, method for the preparation thereof, and dimerization process therewith are provided catalyst supports are prepared from an alkali metal carbonate, water, alcohol, and optionally at least one carbonaceous compound. Catalyst systems comprise at least one elemental alkali metal deposited on the catalyst support. Optionally, the catalyst system further comprises at least one promoter.

6. 发明授权

US08344198B2 Process to decrease or eliminate corrosion from the decomposition of halide containing olefin catalysts 有权
标题翻译：减少或消除含卤化烯烃催化剂分解腐蚀的方法
公开(公告)号：US08344198B2
公开(公告)日：2013-01-01
申请号：US10800471
申请日：2004-03-15
申请人： Warren M. Ewert , Bruce E. Kreischer , Ronald D. Knudsen
发明人： Warren M. Ewert , Bruce E. Kreischer , Ronald D. Knudsen
IPC分类号： C07C2/08 , B08B9/00
CPC分类号： C07C7/005 , B01J31/0244 , B01J31/143 , B01J31/181 , B01J31/4015 , B01J2231/20 , B01J2531/62 , C08F110/14 , C10G50/00 , C10G2300/1092 , C10G2300/44 , C10G2300/802 , C10G2400/22 , Y02P20/582 , Y02P20/584 , C08F2500/02
摘要： A processes is provided to inhibit or limit the decomposition of a halide-containing olefin oligomerization catalyst system during recovery of an oligomerization product. The process includes deactivation of an olefin oligomerization catalyst system present in an olefin oligomerization reactor effluent stream by contact with an alcohol under conditions that minimize potential for deactivated catalyst system decomposition. Such conditions include minimization of the water content of the deactivation agent and concentration of the deactivation agent.
摘要翻译：提供了在回收低聚产物期间抑制或限制含卤烯烃低聚催化剂体系的分解的方法。该方法包括使烯烃低聚反应器流出物流中存在的烯烃低聚催化剂体系通过与醇的接触来使在失活的催化剂体系分解的潜力最小化的条件下失活。这些条件包括减活化剂的水含量的最小化和失活剂的浓度。

7. 发明授权

US07718838B2 Olefin production process 有权
标题翻译：烯烃生产过程
公开(公告)号：US07718838B2
公开(公告)日：2010-05-18
申请号：US11637407
申请日：2006-12-12
申请人： William M. Woodard , Warren M. Ewert , Harvey D. Hensley , Mark E. Lashier , Glyndal D. Cowan , Jeffrey W. Freeman , Ralph V. Franklin , Ronald D. Knudsen , Richard L. Anderson , Lyle R. Kallenbach , Bruce E. Kreischer
发明人： William M. Woodard , Warren M. Ewert , Harvey D. Hensley , Mark E. Lashier , Glyndal D. Cowan , Jeffrey W. Freeman , Ralph V. Franklin , Ronald D. Knudsen , Richard L. Anderson , Lyle R. Kallenbach , Bruce E. Kreischer
IPC分类号： C07C2/26
CPC分类号： B01J31/122 , B01J31/0231 , B01J31/04 , B01J31/143 , B01J31/181 , B01J2231/20 , B01J2531/62 , C07C2/30 , C07C2527/08 , C07C2527/10 , C07C2527/126 , C07C2527/135 , C07C2531/02 , C07C2531/14 , C07C2531/22 , Y02P20/584 , C07C11/107
摘要： A process is provided to stabilize and/or reactivate an olefin production catalyst system which comprises contacting an olefin production catalyst system, either before or after use, with an aromatic compound.
摘要翻译：提供了一种稳定和/或重新活化烯烃生产催化剂体系的方法，其包括将烯烃生产催化剂体系在使用前或使用后与芳族化合物接触。

8. 发明授权

US07157612B2 Olefin production process 有权
标题翻译：烯烃生产过程
公开(公告)号：US07157612B2
公开(公告)日：2007-01-02
申请号：US10872250
申请日：2004-06-18
申请人： Warren M. Ewert , William M. Woodard , Harvey D. Hensley , Mark E. Lashier , Glyndal D. Cowan , Jeffrey W. Freeman , Ralph V. Franklin , Ronald D. Knudsen , Richard L. Anderson , Lyle R. Kallenbach , Bruce E. Kreischer
发明人： Warren M. Ewert , William M. Woodard , Harvey D. Hensley , Mark E. Lashier , Glyndal D. Cowan , Jeffrey W. Freeman , Ralph V. Franklin , Ronald D. Knudsen , Richard L. Anderson , Lyle R. Kallenbach , Bruce E. Kreischer
IPC分类号： C07C2/26 , C07C2/30
CPC分类号： B01J31/122 , B01J31/0231 , B01J31/04 , B01J31/143 , B01J31/181 , B01J2231/20 , B01J2531/62 , C07C2/30 , C07C2527/08 , C07C2527/10 , C07C2527/126 , C07C2527/135 , C07C2531/02 , C07C2531/14 , C07C2531/22 , Y02P20/584 , C07C11/107
摘要： A process is provided to stabilize and/or reactivate an olefin production catalyst system which comprises contacting an olefin production catalyst system, either before or after use, with an aromatic compound.
摘要翻译：提供了一种稳定和/或重新活化烯烃生产催化剂体系的方法，其包括将烯烃生产催化剂体系在使用前或使用后与芳族化合物接触。

9. 发明授权

US06455648B1 Olefin production 有权
标题翻译：烯烃生产
公开(公告)号：US06455648B1
公开(公告)日：2002-09-24
申请号：US09474067
申请日：1999-12-29
申请人： Jeffrey W. Freeman , Warren M. Ewert , Bruce E. Kreischer , Ronald D. Knudsen , Glyndal D. Cowan
发明人： Jeffrey W. Freeman , Warren M. Ewert , Bruce E. Kreischer , Ronald D. Knudsen , Glyndal D. Cowan
IPC分类号： C08F478
CPC分类号： B01J31/04 , B01J31/0244 , B01J31/122 , B01J31/143 , B01J2231/20 , B01J2531/62 , C07C2/30 , C07C2/32 , C07C2527/132 , C07C2531/02 , C07C2531/04 , C07C2531/12 , C07C2531/22
摘要： A process is provided which comprises preparing an olefin oligomerization or trimerization catalyst system and producing olefins in the presence of the olefin oligomerization or trimerization catalyst system and a solvent, wherein said catalyst system preparation comprises the steps of first contacting a chromium source and a pyrrole-containing compound to form a chromium/pyrrole mixture; second, contacting said chromium/pyrrole mixture with a metal alkyl to form a catalyst system; and then contacting said catalyst system with an alpha-olefin, preferably ethylene.
摘要翻译：提供了一种方法，其包括在烯烃低聚或三聚催化剂体系和溶剂的存在下制备烯烃低聚或三聚催化剂体系和生产烯烃，其中所述催化剂体系制备包括以下步骤：首先使铬源和吡咯 - 以形成铬/吡咯混合物; 第二，使所述铬/吡咯混合物与烷基金属接触以形成催化剂体系; 然后使所述催化剂体系与α-烯烃（优选乙烯）接触。

10. 发明授权

US5235121A Method for reforming hydrocarbons 失效
标题翻译：烃类重整方法
公开(公告)号：US5235121A
公开(公告)日：1993-08-10
申请号：US739823
申请日：1991-08-02
申请人： Francis M. Brinkmeyer , Warren M. Ewert , Homer M. Fox , D. F. Rohr, Jr.
发明人： Francis M. Brinkmeyer , Warren M. Ewert , Homer M. Fox , D. F. Rohr, Jr.
IPC分类号： C10G35/085
CPC分类号： C10G35/085
摘要： The present invention provides a method and apparatus for reforming a hydrocarbon feedstock in the presence of steam using a steam-active reforming catalyst The present invention can generally be used in conjunction with any steam-active reforming processes wherein the hydrocarbon reforming and catalyst regeneration operations are conducted simultaneously and the catalyst is regenerated using a steam-diluted oxygen (or air) regeneration medium. In the present invention, catalyst regeneration effluent gas is advantageously reused in the reforming operation to provide at least a portion of the steam environment required for reforming the hydrocarbon feedstock. Free oxygen is preferably removed from the regeneration effluent gas before the regeneration effluent gas is brought into contact with the hydrocarbon feedstock.
摘要翻译：本发明提供了一种使用蒸汽活性重整催化剂在蒸汽存在下重整烃原料的方法和设备。本发明通常可与任何蒸汽活性重整方法一起使用，其中烃重整和催化剂再生操作是同时进行催化剂，并使用蒸汽稀释的氧（或空气）再生介质来再生催化剂。在本发明中，催化剂再生废气有利地在重整操作中重新使用以提供重整烃原料所需的至少一部分蒸汽环境。在再生废气与烃原料接触之前，游离氧优选从再生流出气中除去。

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