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1. 发明授权

US08557087B2 Process for the separation of a hydrocarbon-containing feed stream 有权
标题翻译：用于分离含烃进料流的方法
公开(公告)号：US08557087B2
公开(公告)日：2013-10-15
申请号：US12669132
申请日：2008-07-15
申请人： Denis Mignon
发明人： Denis Mignon
IPC分类号： B01D3/42 , C07C7/04 , G05D7/00 , G05D9/00
CPC分类号： B01D3/4288 , B01D3/425 , B01D3/4283 , C08F210/16 , C08F210/14
摘要： The present invention relates to a process for the separation by distillation of a hydrocarbon-containing feed stream containing olefin monomer, co-monomer and hydrocarbon diluent. The present invention also relates to a distillation system including a distillation column for carrying out the process according to the invention.
摘要翻译：本发明涉及一种通过蒸馏分离含有烯烃单体，共聚单体和烃类稀释剂的含烃进料流的方法。本发明还涉及包括用于实施本发明方法的蒸馏塔的蒸馏系统。

2. 发明申请

US20120178879A1 PROCESS FOR RECYCLING PRODUCT STREAMS SEPARATED FROM A HYDROCARBON-CONTAINING FEED STREAM 有权
标题翻译：回收含有含油料进料流的产品流程的方法
公开(公告)号：US20120178879A1
公开(公告)日：2012-07-12
申请号：US13392531
申请日：2010-09-10
申请人： Denis Mignon , David Vandewiele , Bernard Van Der Schrick , Camille Vercruysse
发明人： Denis Mignon , David Vandewiele , Bernard Van Der Schrick , Camille Vercruysse
IPC分类号： C08L23/02 , B01J19/00
CPC分类号： B01D3/009 , B01D3/146 , B01D5/006 , C07C7/04 , C08J11/02
摘要： The present invention relates to a process for recycling product streams that have been separated from a hydrocarbon-containing feed stream comprising olefin monomer, olefin co-monomer, hydrocarbon diluent and components such as H2, N2, O2, CO, CO2, and formaldehyde. In accordance with the present process a hydrocarbon-containing feed stream is separated into a) a first side stream comprising hydrocarbon diluent and olefin monomer; b) a second side stream which is substantially hydrogen-free and comprises hydrocarbon diluent and olefin monomer, c) a bottom stream comprising substantially olefin-free hydrocarbon diluent, and d) an overhead vapor stream comprising olefin monomer, hydrocarbon diluent and components such as formaldehyde, H2, N2, O2, CO and CO2. The present process further includes recycling said first and said second side streams in a polymerization process for preparing bimodal polyolefin.
摘要翻译：本发明涉及一种从包含烯烃单体，烯烃共聚单体，烃稀释剂和诸如H 2，N 2，O 2，CO，CO 2和甲醛的组分的含烃进料流中分离的产物流的方法。根据本发明方法，将含烃进料流分离为a）包含烃稀释剂和烯烃单体的第一侧流; b）基本上无氢的第二侧流，包括烃稀释剂和烯烃单体，c）包含基本上不含烃的烃稀释剂的底部料流，和d）包含烯烃单体，烃稀释剂和组分如甲醛，H2，N2，O2，CO和CO2。本方法还包括在用于制备双峰聚烯烃的聚合方法中回收所述第一和第二侧流。

3. 发明授权

US08883918B2 Process for recycling product streams separated from a hydrocarbon-containing feed stream 有权
标题翻译：用于回收与含烃进料流分离的产物流的方法
公开(公告)号：US08883918B2
公开(公告)日：2014-11-11
申请号：US13392531
申请日：2010-09-10
申请人： Denis Mignon , David Vandewiele , Bernard Van De Schrick , Camille Vercruysse
发明人： Denis Mignon , David Vandewiele , Bernard Van De Schrick , Camille Vercruysse
IPC分类号： B01D3/00 , C08F2/01 , C08F297/08 , B01D3/14
CPC分类号： B01D3/009 , B01D3/146 , B01D5/006 , C07C7/04 , C08J11/02
摘要： The present invention relates to a process for recycling product streams that have been separated from a hydrocarbon-containing feed stream comprising olefin monomer, olefin co-monomer, hydrocarbon diluent and components such as H2, N2, O2, CO, CO2, and formaldehyde. In accordance with the present process a hydrocarbon-containing feed stream is separated into a) a first side stream comprising hydrocarbon diluent and olefin monomer; b) a second side stream which is substantially hydrogen-free and comprises hydrocarbon diluent and olefin monomer, c) a bottom stream comprising substantially olefin-free hydrocarbon diluent, and d) an overhead vapor stream comprising olefin monomer, hydrocarbon diluent and components such as formaldehyde, H2, N2, O2, CO and CO2. The present process further includes recycling said first and said second side streams in a polymerization process for preparing bimodal polyolefin.
摘要翻译：本发明涉及一种从包含烯烃单体，烯烃共聚单体，烃稀释剂和诸如H 2，N 2，O 2，CO，CO 2和甲醛的组分的含烃进料流中分离的产物流的方法。根据本发明方法，将含烃进料流分离为a）包含烃稀释剂和烯烃单体的第一侧流; b）基本上无氢的第二侧流，包括烃稀释剂和烯烃单体，c）包含基本上不含烃的烃稀释剂的底部料流，和d）包含烯烃单体，烃稀释剂和组分如甲醛，H2，N2，O2，CO和CO2。本方法还包括在用于制备双峰聚烯烃的聚合方法中回收所述第一和第二侧流。

4. 发明申请

US20100264014A1 Process for the Separation of a Hydrocarbon-Containing Feed Stream 有权
标题翻译：用于分离含烃载体原料流的方法
公开(公告)号：US20100264014A1
公开(公告)日：2010-10-21
申请号：US12669132
申请日：2008-07-15
申请人： Denis Mignon
发明人： Denis Mignon
IPC分类号： B01D3/42 , G05D7/00 , G05D9/00
CPC分类号： B01D3/4288 , B01D3/425 , B01D3/4283 , C08F210/16 , C08F210/14
摘要： The present invention relates to a process for the separation by distillation of a hydrocarbon-containing feed stream comprising olefin monomer, co-monomer and hydrocarbon diluent. The present invention also relates to a distillation system comprising a distillation column for carrying out the process according to the invention.
摘要翻译：本发明涉及通过蒸馏分离含有烯烃单体，共聚单体和烃稀释剂的含烃进料流的方法。本发明还涉及包含用于实施本发明方法的蒸馏塔的蒸馏系统。

5. 发明授权

US07060863B2 Multistage reaction system with interstage sparger systems 失效
标题翻译：具有级间分布器系统的多级反应系统
公开(公告)号：US07060863B2
公开(公告)日：2006-06-13
申请号：US10302250
申请日：2002-11-22
申请人： James R. Butler , Denis Mignon
发明人： James R. Butler , Denis Mignon
IPC分类号： C07C2/66
CPC分类号： B01J8/0496 , B01J8/0453 , B01J8/0457 , B01J8/0492 , C07C2/66 , Y10S585/921 , Y10S585/922 , C07C15/02
摘要： A process and system for the vapor phase alkylation of an aromatic substrate in a multi-stage alkylation reaction zone having a plurality of series-connected catalyst beds spaced from one another to provide mixing zones between adjacent catalyst beds. A feedstock containing an aromatic substrate and a C2–C4 alkylating agent is supplied to an inlet side of the reaction zone. The reaction zone is operated at conditions in which the aromatic substrate is in the gas phase and causing vapor phase alkylation of the aromatic substrate as the aromatic substrate and the alkylating agent flow through the reaction zone and pass from one catalyst bed to the next. A quench fluid comprising one or both of the aromatic substrate and the alkylating agent is supplied into the interior of the mixing zone through a plurality of flow paths in which one portion of the flow paths is directed upwardly within the mixing zone and another portion downwardly within the mixing zone. Alkylated product is then recovered from the downstream side of the reaction zone. The quench fluid is supplied to the mixing zone through a plurality of dispersion channels which are spaced laterally from one another and extend transversely across the mixing chamber. At least some of the dispersion channels dispense the quench fluid alternately, upwardly and downwardly within the mixing zone.
摘要翻译：一种用于在多级烷基化反应区中芳族底物气相烷基化的方法和系统，其具有彼此间隔开的多个串联的催化剂床，以在相邻的催化剂床之间提供混合区。将含有芳族底物和C 2 -C 4烷基化剂的原料供给到反应区的入口侧。反应区域在芳香族基质处于气相的条件下进行，芳香族基质作为芳香族基质进行气相烷基化，烷基化剂流过反应区，从一个催化剂床到另一个催化剂床。包含芳族底物和烷基化剂中的一种或两种的骤冷流体通过多个流动路径供应到混合区的内部，其中流动路径的一部分在混合区域内向上指向，混合区。然后从反应区的下游侧回收烷基化产物。骤冷流体通过多个分散通道供应到混合区域，这些分散通道彼此横向间隔开并横向跨越混合室。至少一些分散通道在混合区内交替地向上和向下分配骤冷流体。

6. 发明授权

US06486371B1 Multistage reaction system with interstage sparger systems 失效
标题翻译：具有级间分布器系统的多级反应系统
公开(公告)号：US06486371B1
公开(公告)日：2002-11-26
申请号：US09723650
申请日：2000-11-28
申请人： James R. Butler , Denis Mignon
发明人： James R. Butler , Denis Mignon
IPC分类号： C07C266
CPC分类号： B01J8/0496 , B01J8/0453 , B01J8/0457 , B01J8/0492 , C07C2/66 , Y10S585/921 , Y10S585/922 , C07C15/02
摘要： Vapor phase alkylation of an aromatic substrate in a multi-stage alkylation reaction zone having a plurality of series-connected catalyst beds providing mixing zones between adjacent catalyst beds. An aromatic substrate and a C2-C4 alkylating agent is supplied to an inlet side of a gas phase reaction zone causing vapor phase alkylation of the aromatic substrate as the aromatic substrate and the alkylating agent flow through the reaction zone from one catalyst bed to the next. A quench fluid comprising one or both of the aromatic substrate and the alkylating agent is supplied into the interior of the mixing zone through a plurality of flow paths. One portion of the flow paths is directed upwardly and another portion downwardly within the mixing zone. The quench fluid is supplied to the mixing zone through a plurality of dispersion channels spaced laterally from one another.
摘要翻译：在具有多个串联连接的催化剂床的多级烷基化反应区中芳族底物的气相烷基化提供相邻催化剂床之间的混合区。将芳香族基质和C 2〜C 4烷基化剂供给到气相反应区的入口侧，引起作为芳香族底物的芳香族基质的气相烷基化，烷基化剂从一个催化剂床流到下一个催化剂床。包含芳族底物和烷基化剂中的一种或两种的骤冷流体通过多个流动路径被供给到混合区的内部。流动路径的一部分向上引导，另一部分在混合区域内向下引导。骤冷流体通过彼此横向隔开的多个分散通道供应到混合区域。

7. 发明申请

US20090183789A1 Optimisation of Flow in Transfer Line 审中-公开
标题翻译：传输线流量优化
公开(公告)号：US20090183789A1
公开(公告)日：2009-07-23
申请号：US12280624
申请日：2007-02-21
申请人： Andre Lewalle , Denis Mignon , Sandra Davidts
发明人： Andre Lewalle , Denis Mignon , Sandra Davidts
IPC分类号： F16L41/00
CPC分类号： B01J8/0015 , B01J4/008 , B01J19/2435 , B01J2219/0004 , B01J2219/00166 , B01J2219/00184 , B01J2219/00254 , C08F110/02 , C08F210/16 , F16L41/023 , F16L41/03 , F16L47/32 , Y10S526/918 , Y10S526/92 , Y10T137/85938 , C08F210/06
摘要： The present system discloses a transfer system devised in order to produce optimal flow from the first to the second loop reactor, by connecting the transfer lines to a by-pass line and by separating the connecting points of the transfer lines into the by-pass line by at least 70 cm.
摘要翻译：本系统公开了一种设计用于通过将传输线连接到旁路线并通过将传输线的连接点分离成旁路线而产生从第一到第二环路反应器的最佳流量的传输系统至少70厘米。

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