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    Adducts of mid-range vinylidene content polyisobutylene polymer products and methods for making the same
    3.
    发明授权
    Adducts of mid-range vinylidene content polyisobutylene polymer products and methods for making the same 有权
    中等偏二氯乙烯含量聚异丁烯聚合物产品的加合物及其制备方法

    公开(公告)号：US07091285B2

    公开(公告)日：2006-08-15

    申请号：US10896792

    申请日：2004-07-22

    Applicant: C. Edward Baxter, Jr. ,  Christopher Lobue ,  Gilbert Valdez ,  Daniel Herndon ,  Timothy Lowry

    Inventor： C. Edward Baxter, Jr. ,  Christopher Lobue ,  Gilbert Valdez ,  Daniel Herndon ,  Timothy Lowry

    IPC: C08F8/46

    CPC classification number: 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

    Abstract: A reaction product comprising an adduct of a mid-range vinylidene content PIB polymer composition and maleic anhydride, a phenolic compound or a compound having a reactive site for subsequent amination. The PIB composition comprises a relatively low molecular weight, mid-range vinylidene content PIB polymer product wherein 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 mid-range vinylidene content PIB polymer products may be prepared employing a liquid phase polymerization process conducted in a loop reactor at a temperature of at least 60° F. using a BF3/methanol catalyst complex and a contact time of no more than 4 minutes.

    Abstract translation: 一种反应产物，其包含中等偏
    二氯乙烯含量的PIB聚合物组合物和马来酸酐的加合物，酚类化合物或具有用于随后胺化的反应性位点的化合物。 PIB组合物包含相对低分子量的中程偏二氟乙烯含量的PIB聚合物产物，其中存在于产物中的至少约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％。 中等范围的亚乙烯基含量的PIB聚合物产物可以使用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制备，使用BF 3 /甲醇催化剂络合物和 接触时间不超过4分钟。

    Process for preparing polyolefin products
    7.
    发明申请
    Process for preparing polyolefin products 有权
    制备聚烯烃产品的方法

    公开(公告)号：US20050101750A1

    公开(公告)日：2005-05-12

    申请号：US10962920

    申请日：2004-10-12

    Applicant: C. Baxter ,  Gilbert Valdez ,  Christopher Lobue ,  Timothy Lowry ,  Armen Abazajian

    Inventor： C. Baxter ,  Gilbert Valdez ,  Christopher Lobue ,  Timothy Lowry ,  Armen Abazajian

    IPC: C08F2/00 ,  C08F10/00 ,  C08F10/10 ,  C08F110/10 ,  C08F110/14 ,  C08F210/10 ,  C08F4/44

    CPC classification number: C08F10/00 ,  C08F10/10 ,  C08F110/10 ,  C08F110/14 ,  C08F210/10 ,  C08F4/14 ,  C08F2500/20 ,  C08F2500/02 ,  C08F210/08

    Abstract: 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.

    Abstract translation: 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复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任何一种或多种，​​包括支链烯烃如异丁烯，C 3〜C 15直链α-烯烃和C 4 - 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。

    Process for preparing polyolefin products
    8.
    发明授权
    Process for preparing polyolefin products 有权

    公开(公告)号：US06525149B1

    公开(公告)日：2003-02-25

    申请号：US09665084

    申请日：2000-09-20

    Applicant: C. Edward Baxter, Jr. ,  Gilbert Valdez ,  Christopher Lobue ,  Timothy Lowry ,  Armen Abazajian

    Inventor： C. Edward Baxter, Jr. ,  Gilbert Valdez ,  Christopher Lobue ,  Timothy Lowry ,  Armen Abazajian

    IPC: C08F454

    CPC classification number: 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 ,  Y10S526/92 ,  Y10S526/922 ,  C08F4/14 ,  C08F2500/20 ,  C08F2500/02 ,  C08F210/08

    Abstract: 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.

    Process for producing high vinylidene polyisobutylene
    10.
    发明授权
    Process for producing high vinylidene polyisobutylene 有权
    制备高亚乙烯基聚异丁烯的方法

    公开(公告)号：US06683138B2

    公开(公告)日：2004-01-27

    申请号：US10334639

    申请日：2002-12-31

    Applicant: C. Edward Baxter, Jr. ,  Gilbert Valdez ,  Christopher Lobue ,  Timothy Lowry

    Inventor： C. Edward Baxter, Jr. ,  Gilbert Valdez ,  Christopher Lobue ,  Timothy Lowry

    IPC: C08F414

    CPC classification number: 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

    Abstract: 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 0° 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.

    Abstract translation: 一种用于制备低分子量，高反应性聚异丁烯的液相聚合方法。 该方法包括提供含有异丁烯的原料和由BF 3的络合物和络合剂组成的催化剂组合物的步骤。 将原料和催化剂组合物引入到反应区中的残余反应混合物中，其中残余反应混合物，原料和催化剂组合物紧密混合，以便在所述反应区中呈现紧密混合的反应混合物。 将紧密混合的反应混合物保持在其紧密混合的状态，并保持在至少约0℃的温度，同时在反应区中，由此其中的异丁烯聚合形成具有高度末端不饱和度的聚异丁烯 。 产物流从反应区中取出。 控制将原料引入反应区和从反应区抽出产物流，使得在反应区中进行聚合的异丁烯的停留时间不大于约4分钟，由此产物流含有低分子量 重量，高反应性聚异丁烯产物。 优选地，反应可以在其中冷却剂在壳侧循环的管壳式换热器的管侧进行。

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