专利快速检索-快速检索全球专利，免费商用专利数据库-IPRDB

1. 发明授权

US07102049B2 Process for operating a quench device in an oxygenate-to-olefin production unit 失效
标题翻译：在含氧化合物至烯烃生产单元中操作骤冷装置的方法
公开(公告)号：US07102049B2
公开(公告)日：2006-09-05
申请号：US10603552
申请日：2003-06-25
申请人： Zhong Yi Ding , James Richardson Lattner , David Ritchie Lumgair, Jr. , Jeffrey Alan Kabin , Cor F. Van Egmond
发明人： Zhong Yi Ding , James Richardson Lattner , David Ritchie Lumgair, Jr. , Jeffrey Alan Kabin , Cor F. Van Egmond
IPC分类号： C07C1/00 , C07C7/00
CPC分类号： C07C1/20 , Y02P30/42 , C07C11/02
摘要： The present invention is a process for producing olefin(s) from oxygenates that is more effective than previously known processes at removing carbon dioxide from the effluent stream by operating a quench tower at a pH greater than 7.0.
摘要翻译：本发明是一种从含氧化合物生产烯烃的方法，其比先前已知的通过在大于7.0的pH下操作骤冷塔从流出物流中除去二氧化碳的方法更有效。

2. 发明授权

US07135604B2 Process for separating carbon dioxide from an oxygenate-to-olefin effluent stream 失效
标题翻译：从含氧化合物到烯烃流出物流中分离二氧化碳的方法
公开(公告)号：US07135604B2
公开(公告)日：2006-11-14
申请号：US10603337
申请日：2003-06-25
申请人： Zhong Yi Ding , James Richardson Lattner , David Ritchie Lumgair, Jr. , Jeffrey Alan Kabin
发明人： Zhong Yi Ding , James Richardson Lattner , David Ritchie Lumgair, Jr. , Jeffrey Alan Kabin
IPC分类号： C07C1/00 , C07C7/00
CPC分类号： C07C1/20 , B01D53/1475 , B01D53/265 , B01D53/62 , B01D53/75 , B01D2251/304 , B01D2251/306 , B01D2252/204 , B01D2256/24 , B01D2257/504 , B01D2257/80 , C10G3/49 , C10G2400/20 , Y02C10/04 , Y02P20/152 , Y02P30/20 , Y02P30/40 , Y02P30/42 , C07C11/02
摘要： The present invention is a process for removal of carbon dioxide from a reactor effluent stream comprising water, carbon dioxide and olefin(s), where a portion of the carbon dioxide is removed in a quenching step with a quench medium and more carbon dioxide is removed by contacting the quenched effluent stream with an alkaline stream. A portion of the alkaline stream is added to the quench medium.
摘要翻译：本发明是从包括水，二氧化碳和烯烃的反应器流出物流中除去二氧化碳的方法，其中一部分二氧化碳在淬火步骤中用骤冷介质除去并且除去更多的二氧化碳通过将淬灭的流出物流与碱性流接触。将一部分碱性流加入骤冷介质中。

3. 发明授权

US07005555B2 Process for separating and recycling oxygenate(s) to an oxygenate-to-olefin reactor 失效
标题翻译：将含氧化合物分离和循环到含氧化合物至烯烃反应器的方法
公开(公告)号：US07005555B2
公开(公告)日：2006-02-28
申请号：US10603846
申请日：2003-06-25
申请人： Zhong Yi Ding , James Richardson Lattner , Paul N. Chisholm , Jeffrey Alan Kabin
发明人： Zhong Yi Ding , James Richardson Lattner , Paul N. Chisholm , Jeffrey Alan Kabin
IPC分类号： C07C1/20
CPC分类号： C10G3/49 , B01J8/025 , B01J2219/00006 , C07C1/20 , C10G2400/20 , C10G2400/30 , Y02P30/20 , Y02P30/40 , Y02P30/42 , C07C11/02
摘要： The present invention is a process for producing olefin(s) from oxygenate(s). The process removes oxygenate(s) including carbon dioxide in the bottoms of the quench stream and recycles the oxygenate(s) back to the reactor. Carbon dioxide is removed from the quench bottoms before returning oxygenate(s) in the quench bottoms stream to the reactor.
摘要翻译：本发明是一种从含氧化合物生产烯烃的方法。该方法从骤冷流的底部除去包括二氧化碳在内的含氧化物，并将含氧化合物再循环回反应器。在将骤冷塔底物流中的含氧化合物返回到反应器之前，将二氧化碳从骤冷塔底部排出。

4. 发明授权

US06987208B2 Process for removing oxygenates from an olefinic stream 失效
标题翻译：从烯烃流中除去含氧化合物的方法
公开(公告)号：US06987208B2
公开(公告)日：2006-01-17
申请号：US10761873
申请日：2004-01-21
申请人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
发明人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
IPC分类号： C07C1/20 , C07C7/48
CPC分类号： C07C7/14841 , C07C11/02
摘要： The present invention provides a process for removing oxygenate impurities, e.g., dimethyl ether, from an olefinic product stream by converting the oxygenate impurity to a compound whose boiling point differs by at least about 5° C. from the oxygenate impurity. Typically, the compound is more readily removable from the product stream than the oxygenate impurity.
摘要翻译：本发明提供了通过将含氧化合物杂质转化为沸点与含氧化合物杂质相差至少约5℃的化合物，从烯烃产物流中除去含氧化合物杂质如二甲醚的方法。通常，化合物比含氧化合物杂质更容易从产物流中除去。

5. 发明授权

US06717025B1 Process for removing oxygenates from an olefinic stream 失效
标题翻译：从烯烃流中除去含氧化合物的方法
公开(公告)号：US06717025B1
公开(公告)日：2004-04-06
申请号：US10295066
申请日：2002-11-15
申请人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
发明人： Michael A. Risch , Teng Xu , John Di-Yi Ou , Keith Holroyd Kuechler , James H. Beech , James Richardson Lattner , Cor F. Van Egmond
IPC分类号： C07C7148
CPC分类号： C07C7/14841 , C07C11/02
摘要： The present invention provides a process for removing oxygenate impurities, e.g., dimethyl ether, from an olefinic product stream by converting the oxygenate impurity to a compound whose boiling point differs by at least about 5° C. from the oxygenate impurity. Typically, the compound is more readily removable from the product stream than the oxygenate impurity.
摘要翻译：本发明提供了通过将含氧化合物杂质转化为沸点与含氧化合物杂质相差至少约5℃的化合物，从烯烃产物流中除去含氧化合物杂质如二甲醚的方法。通常，化合物比含氧化合物杂质更容易从产物流中除去。

6. 发明授权

US07060865B2 Recovery of C4 olefins from a product stream comprising C4 olefins, dimethyl ether and C5+ hydrocarbons 失效
标题翻译：从包含C4烯烃，二甲醚和C5 +烃的产物流中回收C4烯烃
公开(公告)号：US07060865B2
公开(公告)日：2006-06-13
申请号：US10292232
申请日：2002-11-12
申请人： Zhong Yi Ding , James Richardson Lattner
发明人： Zhong Yi Ding , James Richardson Lattner
IPC分类号： C07C7/04 , C07C7/11 , C07C41/42 , C07C41/38
CPC分类号： C07C41/38 , C07C41/42 , Y02P30/464 , C07C43/043
摘要： Disclosed is a process for removing DME from a stream containing C4 olefins. The process includes providing a first stream comprising C4 olefins, C5+ hydrocarbons, DME, and methanol. The first stream is separated into a second stream comprising the C4 olefins and the DME and a third stream comprising the C5+ hydrocarbons and the methanol. The second stream is directed to a DME absorption unit, wherein the second stream contacts water under conditions effective to separate the C4 olefins from the DME. Also disclosed is a process including contacting the first stream with water in a methanol removal unit under conditions effective to separate remove the methanol therefrom; distilling the methanol-depleted stream to remove C5+ hydrocarbon components, and contacting the stream with water in a DME removal unit under conditions effective to form an overhead stream comprising the C4 olefins and a bottoms stream comprising the DME.
摘要翻译：公开了从含有C4烯烃的流中除去DME的方法。该方法包括提供包含C4烯烃，C5 +烃，DME和甲醇的第一流。将第一流分离成包含C4烯烃和DME的第二料流和包含C5 +烃和甲醇的第三料流。第二流被引导到DME吸收单元，其中第二流在有效地将C 4烯烃与DME分离的条件下与水接触。还公开了一种方法，包括在有效分离除去甲醇的条件下，使第一流与甲醇去除单元中的水接触; 蒸馏除去甲醇的流以除去C5 +烃组分，并在有效形成包含C 4烯烃的塔顶物流和包含DME的塔底物流的条件下，在DME去除单元中使该物流与水接触。

7. 发明授权

US07740829B2 Synthesis gas production and use 有权
标题翻译：合成气生产和使用
公开(公告)号：US07740829B2
公开(公告)日：2010-06-22
申请号：US11477504
申请日：2006-06-29
申请人： Christopher L. Becker , Frank Hershkowitz , James Richardson Lattner
发明人： Christopher L. Becker , Frank Hershkowitz , James Richardson Lattner
IPC分类号： C01B3/24 , C01B3/26
CPC分类号： B01J8/0438 , B01J8/0453 , B01J8/0457 , B01J8/0492 , B01J8/0496 , B01J2208/00504 , B01J2208/00513 , B01J2208/00522 , B01J2208/0053 , B01J2219/00036 , B01J2219/00038 , B01J2219/00243 , C01B3/382 , C01B3/46 , C01B2203/0233 , C01B2203/0244 , C01B2203/0255 , C01B2203/0261 , C01B2203/0283 , C01B2203/061 , C01B2203/0805 , C01B2203/0844 , C01B2203/0872 , C01B2203/1041 , C01B2203/1052 , C01B2203/1058 , C01B2203/1241 , C01B2203/1288 , C01B2203/142 , C01B2203/143 , C01B2203/82 , C07C29/1518 , C07C31/04
摘要： Synthesis gas is produced according to this invention using a combination of steam reforming and oxidation chemistry. The process incorporates the use of solids to heat the hydrocarbon feed, and to cool the gas product. According to the invention, heat can be conserved by directionally reversing the flow of feed and product gases at intermittent intervals.
摘要翻译：根据本发明使用蒸汽重整和氧化化学的组合制备合成气。该方法包括使用固体来加热烃进料和冷却气体产物。根据本发明，可以通过以间歇间隔定向反转进料和产物气体的流动来保护热量。

8. 发明授权

US08410230B2 Polymerization processes for broadened molecular weight distribution 有权
公开(公告)号：US08410230B2
公开(公告)日：2013-04-02
申请号：US13088622
申请日：2011-04-18
申请人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , Patrick Brant , James Richardson Lattner
发明人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , Patrick Brant , James Richardson Lattner
IPC分类号： C08F2/00
CPC分类号： C08F10/00 , C08F110/06 , C08F2/06 , C08F2/01 , C08F2500/04
摘要： Provided are methods of producing polymers with broadened molecular weight and/or composition distribution in a continuous homogeneous polymerization system utilizing reactor temperature gradients, reactor polymer concentration gradients, monomer concentration gradients, catalyst concentration gradients, and combinations thereof in the polymerization reactor. Such methods are particularly suitable when utilizing metallocene catalysts and other single-site catalysts, which generally produce polymers with narrow molecular weight and composition distribution.

9. 发明授权

US08399586B2 Process for feeding ethylene to polymerization reactors 有权
标题翻译：将乙烯供给聚合反应器的方法
公开(公告)号：US08399586B2
公开(公告)日：2013-03-19
申请号：US12584338
申请日：2009-09-03
申请人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , James Richardson Lattner , Gary D. Mohr
发明人： Gabor Kiss , Robert Patrick Reynolds, Jr. , John W. Chu , James Richardson Lattner , Gary D. Mohr
IPC分类号： C08F2/00 , C08F4/00 , C08F36/00 , C08F110/06 , C08F110/02
CPC分类号： C08F10/02 , C08F110/02 , C08F210/16 , Y02P20/544 , C08F2/06 , C08F2/01 , C08F2500/12 , C08F210/06 , C08F2/00
摘要： A process for feeding ethylene into a polymerization system includes providing a low-pressure ethylene stream, one or more low-pressure C3 to C20 monomer streams, an optional low-pressure inert solvent/diluent stream, and one or more reactors; metering the low-pressure ethylene stream, the one or more low-pressure C3 to C20 monomer streams, and the optional low-pressure inert solvent/diluent stream; blending the metered low-pressure ethylene stream, the metered one or more low-pressure C3 to C20 monomer streams, and the metered low-pressure optional inert solvent/diluent stream to form an ethylene-carrying low-pressure blended liquid feed stream; pressurizing the ethylene-carrying low-pressure blended liquid feed stream to the polymerization system pressure with one or more high-pressure pumps to thrm an ethylene-carrying high-pressure blended reactor feed stream; and feeding the ethylene-carrying high-pressure blended reactor feed stream to the one or more reactors.
摘要翻译：将乙烯进料到聚合体系中的方法包括提供低压乙烯流，一种或多种低压C3至C20单体流，任选的低压惰性溶剂/稀释剂流和一个或多个反应器; 计量低压乙烯流，一个或多个低压C3至C20单体流和任选的低压惰性溶剂/稀释剂流; 混合计量的低压乙烯流，计量的一个或多个低压C3至C20单体流和计量的低压可选惰性溶剂/稀释剂流，以形成携带乙烯的低压混合液体进料流; 使用一个或多个高压泵将携带乙烯的低压混合液体进料流加压至聚合系统压力以加入携带乙烯的高压共混反应器进料流; 并将含乙烯的高压共混反应器进料流输送到一个或多个反应器。

10. 发明授权

US08080610B2 Monomer recycle process for fluid phase in-line blending of polymers 有权
标题翻译：用于流体相在线共混聚合物的单体循环过程
公开(公告)号：US08080610B2
公开(公告)日：2011-12-20
申请号：US12074496
申请日：2008-03-04
申请人： Gabor Kiss , Alan Anthony Galuska , James Richardson Lattner
发明人： Gabor Kiss , Alan Anthony Galuska , James Richardson Lattner
IPC分类号： C08F2/04 , C08F2/06
CPC分类号： C08F6/003 , C08F10/06 , C08F110/06 , C08F210/06 , C08F2/001 , C08F2500/15 , C08F2500/03 , C08F2500/12 , C08F2500/20 , C08F210/16
摘要： A monomer recycle process for fluid phase in-line blending of polymers is provided. In one form, the monomer recycle process includes providing a first group (G1) of one or more reactor trains and a second group (G2) of one or more reactor trains and one or more separators fluidly connected to G1 and one separator fluidly connected to G2; polymerizing in each reactor train of G1 and G2 olefin monomers to form homogenous fluid phase polymer-monomer mixtures wherein each of the G1 and G2 reactor trains have at least one common monomer; passing the reactor effluents from the one or more G1 reactor trains through the one or more G1 separators to separate a monomer-rich phase from a polymer-enriched phase; passing the polymer-enriched phase and the reactor effluents from the one or more G2 reactor trains into the G2 separator (separator-blender) to separate another monomer-rich phase from a polymer-rich blend; recycling to one or more G1 reactor trains the separated monomer-rich phase from the one or more G1 separators; and recycling to one or more G2 reactor trains the separated monomer-rich phase from the G2 separator. The polymer-rich blend is conveyed to a downstream finishing stage for further monomer stripping, drying and/or pelletizing to form a polymer product blend.
摘要翻译：提供了用于聚合物的流体相在线共混的单体再循环方法。在一种形式中，单体再循环方法包括提供一个或多个反应器列的第一组（G1）和一个或多个反应器列的第二组（G2）和与G1流体连接的一个或多个分离器和一个流体连接到 G2; 在G1和G2烯烃单体的每个反应器序列中聚合以形成均相流体相聚合物 - 单体混合物，其中每个G1和G2反应器列具有至少一个共同的单体; 使来自一个或多个G1反应器列的反应器流出物通过一个或多个G1分离器以将富含单体的相与富集聚合相分离; 将聚合物富集相和反应器流出物从一个或多个G2反应器列车通入G2分离器（分离器 - 共混器）中，以从富含聚合物的共混物中分离另一富含单体的相; 将一个或多个G1反应器再循环到一个或多个G1分离器中，从而分离出富含单体的相。并循环到一个或多个G2反应器中，从G2分离器中将分离的富含单体的相进行培养。将富含聚合物的共混物输送到下游整理阶段，以进一步进行单体汽提，干燥和/或造粒以形成聚合物产物混合物。

你已经成功收藏专利！

检索式保存成功!

IPRDB

热门服务

关于我们

友情链接

联系方式