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1. 发明申请

US20030032740A1 Process for preparing polyolefin products 有权
标题翻译：制备聚烯烃产品的方法
公开(公告)号：US20030032740A1
公开(公告)日：2003-02-13
申请号：US10208234
申请日：2002-07-30
申请人： Texas Petrochemicals LP
发明人： C. Edward Baxter JR. , Gilbert Valdez , Christopher Lobue , Timothy Lowry , Armen Abazajiah
IPC分类号： C08F002/00
CPC分类号： C08F10/00 , C08F10/10 , C08F110/10 , C08F110/14 , C08F210/10 , C08F4/14 , C08F2500/20 , C08F2500/02 , C08F210/08
摘要： A novel liquid phase polymerization process for preparing a polyolefin product having preselected properties is disclosed. The process includes the steps of providing a liquid feedstock which contains an olefinic component and a catalyst composition consisting of a stable complex of BF3 and a complexing agent therefor. The feedstock may comprise any one or more of a number of olefins including branched olefins such as isobutylene, C3 to C15 linear alpha olefins and C4 to C15 reactive non-alpha olefins. The feedstock and the catalyst composition are introduced into a residual reaction mixture recirculating in a loop reactor reaction zone provided in the tube side of a shell and tube heat exchanger at a recirculation rate sufficient to cause intimate intermixing of the residual reaction mixture, the added feedstock and the added catalyst composition. The heat of the polymerization reaction is removed from the recirculating intimately intermixed reaction admixture at a rate calculated to provide a substantially constant reaction temperature therein while the same is recirculating in said reaction zone. The conditions in the reactor are appropriate for causing olefinic components introduced in said feedstock to undergo polymerization to form the desired polyolefin product in the presence of the catalyst composition. A product stream containing the desired polyolefin product is withdrawn from the reaction zone. The introduction of the feedstock into the reaction zone and the withdrawal of the product stream from the reaction zone are controlled such that the residence time of the olefinic components undergoing polymerization in the reaction zone is appropriate for production of the desired polyolefin product.
摘要翻译：公开了一种用于制备具有预选性质的聚烯烃产品的新型液相聚合方法。该方法包括提供含有烯烃组分的液体原料和由稳定的BF 3络合物及其络合剂组成的催化剂组合物的步骤。原料可以包括许多烯烃中的一种或多种，包括支链烯烃如异丁烯，C 3 -C 15直链α-烯烃和C 4 -C 15反应性非α-烯烃。将原料和催化剂组合物引入到在壳管式热交换器的管侧中设置的环管反应器反应区中再循环的残留反应混合物，其循环速率足以引起残余反应混合物的密集混合，加入的原料和添加的催化剂组合物。将聚合反应的热量从循环的紧密混合的反应混合物中除去，其速率被计算为在其中提供基本上恒定的反应温度，同时在该反应区中再循环。反应器中的条件适合于在催化剂组合物存在下使引入所述原料的烯烃成分进行聚合以形成所需的聚烯烃产物。从反应区取出含有所需聚烯烃产物的产品流。控制将原料引入反应区和从反应区中引出产物流，使得在反应区中进行聚合的烯烃组分的停留时间适于生产所需的聚烯烃产物。

2. 发明申请

US20040225083A1 Apparatus for preparing polyolefin products and methodology for using the same 有权
公开(公告)号：US20040225083A1
公开(公告)日：2004-11-11
申请号：US10758168
申请日：2004-01-15
申请人： Texas Petrochemicals, LP
发明人： C. Edward Baxter JR. , Daniel Herndon , James G. Wakeland , Russel E. Reid SR. , Gilbert Valdez
IPC分类号： C08F002/00
CPC分类号： B01J19/2425 , B01J8/007 , B01J8/20 , B01J19/2405 , B01J19/2465 , B01J2208/00212 , B01J2208/00283 , B01J2219/00006 , B01J2219/00038 , B01J2219/00085 , B01J2219/0011 , B01J2219/00272 , C08F6/02 , C08F10/00 , C08L23/00
摘要： Apparatus for olefin polymerization includes a plurality of shell and tube olefin polymerization reactors, each of which has an olefin polymerization reaction mixture inlet connection and a crude polyolefin product outlet connection. Each reactor is equipped with a recirculation system including a pump arranged to circulate a reaction mixture through the tube side of the reactor independently of the introduction of olefin polymerization reaction mixture into the reactor. The apparatus also includes an inlet reaction mixture distribution manifold and an outlet polymerization reaction mixture collection manifold interconnecting the reactors for operation in parallel. The apparatus also includes catalyst composition and catalyst modifier inlets for each reactor arranged such that a catalyst modifier to may be introduced into each reactor at a rate which is independent of the introduction of catalyst composition. The apparatus further incorporates a crude polyolefin product catalyst removal and wash system including a plurality of settler vessels, associated piping and an inlet for a catalyst killing agent. This crude polyolefin product catalyst removal and wash system operates to receive crude polyolefin product from the crude polyolefin product outlet and remove residual catalyst therefrom.

3. 发明申请

US20030040587A1 Mid-range vinylidene content polyisobutylene polymer product and process for producing the same 有权
标题翻译：中等偏乙烯含量的聚异丁烯聚合物产品及其制备方法
公开(公告)号：US20030040587A1
公开(公告)日：2003-02-27
申请号：US10102279
申请日：2002-03-19
申请人： Texas Petrochemicals LP
发明人： C. Edward Baxter JR.
IPC分类号： C08F002/00
CPC分类号： C08F110/10 , C08F10/00 , C08F10/10 , C08F110/14 , C08F210/10 , Y10S525/911 , C08F2/14 , C08F4/14 , C08F2500/08 , C08F2500/20 , C08F2500/02 , C08F210/08 , C08F2/01
摘要： A relatively low molecular weight, mid-range vinylidene content PIB polymer product and a process for making the same. At least about 90% of the PIB molecules present in the product comprise alpha or beta position isomers. The vinylidene (alpha) isomer content of the product may range from 20% to 70% thereof and the content of tetra-substituted internal double bonds is very low, preferably less than about 5% and ideally less than about 1-2%. The midrange vinylidene content PIB polymer products are prepared by a liquid phase polymerization process conducted in a loop reactor at a temperature of at least 60null F. using a BF3/methanol catalyst complex and a contact time of no more than 4 minutes.
摘要翻译：相对低分子量，中等范围的亚乙烯基含量的PIB聚合物产物及其制备方法。存在于产品中的至少约90％的PIB分子包含α或β位异构体。产物的亚乙烯基（α）异构体含量可以在20％至70％的范围内，四取代的内部双键的含量非常低，优选小于约5％，理想地小于约1-2％。通过使用BF 3 /甲醇催化剂络合物和不超过4分钟的接触时间，在至少60°F的温度下在环管反应器中进行的液相聚合方法制备中等偏二氯乙烯含量的PIB聚合物产物。

4. 发明申请

US20040225084A1 Apparatus for preparing polyolefin products and methodology for using the same 有权
标题翻译：用于制备聚烯烃产品的设备及其使用方法
公开(公告)号：US20040225084A1
公开(公告)日：2004-11-11
申请号：US10758499
申请日：2004-01-15
申请人： Texas Petrochemicals, LP
发明人： C. Edward Baxter JR. , Daniel Herndon , James G. Wakeland , Russel E. Reid SR. , Gilbert Valdez
IPC分类号： C08F002/00
CPC分类号： B01J19/2425 , B01J8/007 , B01J8/20 , B01J19/2405 , B01J19/2465 , B01J2208/00212 , B01J2208/00283 , B01J2219/00006 , B01J2219/00038 , B01J2219/00085 , B01J2219/0011 , B01J2219/00272 , C08F6/02 , C08F10/00 , C08L23/00
摘要： Apparatus for olefin polymerization includes a plurality of shell and tube olefin polymerization reactors, each of which has an olefin polymerization reaction mixture inlet connection and a crude polyolefin product outlet connection. Each reactor is equipped with a recirculation system including a pump arranged to circulate a reaction mixture through the tube side of the reactor independently of the introduction of olefin polymerization reaction mixture into the reactor. The apparatus also includes an inlet reaction mixture distribution manifold and an outlet polymerization reaction mixture collection manifold interconnecting the reactors for operation in parallel. The apparatus also includes catalyst composition and catalyst modifier inlets for each reactor arranged such that a catalyst modifier to may be introduced into each reactor at a rate which is independent of the introduction of catalyst composition. The apparatus further incorporates a crude polyolefin product catalyst removal and wash system including a plurality of settler vessels, associated piping and an inlet for a catalyst killing agent. This crude polyolefin product catalyst removal and wash system operates to receive crude polyolefin product from the crude polyolefin product outlet and remove residual catalyst therefrom.
摘要翻译：用于烯烃聚合的设备包括多个壳和管烯烃聚合反应器，每个反应器具有烯烃聚合反应混合物入口连接和粗聚烯烃产物出口连接。每个反应器配备有循环系统，其包括泵，其被布置成使反应混合物循环通过反应器的管侧，而与将烯烃聚合反应混合物引入反应器中无关。该装置还包括入口反应混合物分配歧管和出口聚合反应混合物收集歧管，其将反应器互连以并行操作。该装置还包括用于每个反应器的催化剂组合物和催化剂改性剂入口，其布置成使催化剂改性剂以不同于引入催化剂组合物的速率引入每个反应器中。该装置还包括粗聚烯烃产物催化剂去除和洗涤系统，其包括多个沉降器容器，相关联的管道和用于催化剂杀伤剂的入口。该粗聚烯烃产物催化剂去除和洗涤系统用于从粗聚烯烃产物出口接收粗聚烯烃产物并从其中除去残留的催化剂。

5. 发明申请

US20040176552A1 Process for producing mid-range vinylidene content polyisobutylene polymer products 审中-公开
标题翻译：生产中等范围的亚乙烯基含量聚异丁烯聚合物产品的方法
公开(公告)号：US20040176552A1
公开(公告)日：2004-09-09
申请号：US10803721
申请日：2004-03-18
申请人： Texas Petrochemicals LP
发明人： C. Edward Baxter JR.
IPC分类号： C08F002/00
CPC分类号： C08F110/10 , C08F10/00 , C08F10/10 , C08F110/14 , C08F210/10 , Y10S525/911 , C08F2/14 , C08F4/14 , C08F2500/08 , C08F2500/20 , C08F2500/02 , C08F210/08 , C08F2/01
摘要： A process for making a relatively low molecular weight, mid-range vinylidene content PIB polymer product comprising a liquid phase polymerization process conducted in a loop reactor at a temperature of at least 60null F. using a BF3/methanol catalyst complex and a contact time of no more than 4 minutes. At least about 90% of the PIB molecules present in the product comprise alpha or beta position isomers. The vinylidene (alpha) isomer content of the product may range from 20% to 70% thereof, and the content of tetra-substituted internal double bonds is very low, advantageously no more than about 10%, preferably less than about 5% and ideally less than about 1-2%.
摘要翻译：使用BF 3 /甲醇催化剂络合物制备相对低分子量的中等范围的亚乙烯基含量的PIB聚合物产物的方法，其包括在环流反应器中在至少60°F的温度下进行的液相聚合方法，接触时间不超过4分钟。存在于产品中的至少约90％的PIB分子包含α或β位异构体。产物的亚乙烯基（α）异构体含量可以在20％至70％的范围内，四取代的内部双键的含量非常低，有利地不超过约10％，优选小于约5％，理想的是小于约1-2％。

6. 发明申请

US20030096924A1 Process for producing high vinylidene polyisobutylene 有权
公开(公告)号：US20030096924A1
公开(公告)日：2003-05-22
申请号：US10334639
申请日：2002-12-31
申请人： Texas Petrochemicals LP
发明人： C. Edward Baxter JR. , Gilbert Valdez , Christopher Lobue , Timothy Lowry
IPC分类号： C08F002/00
CPC分类号： B01J19/2425 , B01J19/243 , B01J19/2465 , B01J2219/00063 , B01J2219/00065 , B01J2219/00069 , B01J2219/00099 , B01J2219/00114 , B01J2219/00166 , C08F10/00 , C08F10/10 , C08F110/10 , C08F110/14 , C08F210/10 , C08F4/14 , C08F2500/20 , C08F2500/02 , C08F210/08
摘要： A liquid phase polymerization process for preparing low molecular weight, highly reactive polyisobutylene. The process includes the steps of providing a feedstock containing isobutylene and a catalyst composition made up of a complex of BF3 and a complexing agent. The feedstock and the catalyst composition are introduced into a residual reaction mixture in a reaction zone where the residual reaction mixture, the feedstock and the catalyst composition are intimately intermixed so as to present an intimately intermixed reaction admixture in said reaction zone. The intimately intermixed reaction admixture is maintained in its intimately intermixed condition and kept at a temperature of at least about 0null C. while the same is in the reaction zone, whereby the isobutylene therein is polymerized to form polyisobutylene having a high degree of terminal unsaturation. A product stream is withdrawn from the reaction zone. The introduction of feedstock into the reaction zone and the withdrawal of the product stream from the reaction zone are controlled such that the residence time of the isobutylene undergoing polymerization in the reaction zone is no greater than about 4 minutes whereby the product stream contains a low molecular weight, highly reactive polyisobutylene product. Preferably the reaction may be conducted on the tube side of a shell-and-tube exchanger in which a coolant is circulated on the shell side.

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