Stabilization of cross-linked silane group containing polymers with phenomic stabilizers
    32.
    发明授权
    Stabilization of cross-linked silane group containing polymers with phenomic stabilizers 失效
    具有苯基稳定剂的交联硅烷基聚合物的稳定化

    公开(公告)号:US07842772B2

    公开(公告)日:2010-11-30

    申请号:US11823022

    申请日:2007-06-26

    IPC分类号: C08L43/04 C08K5/13 C08K5/372

    摘要: The present invention relates to a composition for cross-linking and stabilization of a polymer containing hydrolysable silane groups comprising a sulphonic acid as a silanol condensation catalyst characterized in that it comprises a stabilizer which is neutral or acidic, does not contain ester groups and is a compound according to formula (I): wherein R is an unsubstituted or substituted aliphatic or aromatic hydrocarbyl radical which may comprise heteroatoms, R′ is a hydrocarbyl radical, R″ is a hydrocarbyl radical and R′ and/or R″ being a bulky radical, X1, X2 or X3 is the same or different H or OH, whereby at least X1, X2 or X3 is OH, and n is 1 to 4; or a compound according to formula (II): R′″—(S)p—R′″  (II) wherein R′″ is an aliphatic hydrocarbyl radical and p is 1 to 6; or a mixture of any of such compounds, to a stabilized polymer comprising the above stabilizers and to a process for cross-linking and stabilization of silane group containing polymers in the presence of the above mentioned stabilizers.

    摘要翻译: 本发明涉及一种用于交联和稳定含有可水解硅烷基团的聚合物的组合物,其包含磺酸作为硅烷醇缩合催化剂,其特征在于其包含中性或酸性,不含酯基的稳定剂,并且为 根据式(I)的化合物:其中R是可以包含杂原子的未取代或取代的脂族或芳族烃基,R'是烃基,R“是烃基,R'和/或R”是大体积的基团 X1,X2或X3是相同或不同的H或OH,其中至少X1,X2或X3是OH,n是1至4; 或根据式(II)的化合物:R“” - (S)p -R'“(II)其中R'”是脂族​​烃基,p是1-6; 或任何这些化合物的混合物与包含上述稳定剂的稳定化聚合物,以及在上述稳定剂存在下交联和稳定含硅烷基团的聚合物的方法。

    Method for preparing an ethylene-silane copolymer
    33.
    发明授权
    Method for preparing an ethylene-silane copolymer 有权
    乙烯 - 硅烷共聚物的制备方法

    公开(公告)号:US07834115B2

    公开(公告)日:2010-11-16

    申请号:US11940764

    申请日:2007-11-15

    IPC分类号: C08F2/01

    摘要: The present invention relates to an improved method for preparing an ethylene-silane copolymer comprising hydrolysable silane groups by radical-initiated polymerisation of ethylene and an olefinically unsaturated silane compound, such as vinyl trimethoxysilane (VTMS). Said method is performed in a multi-zone reactor comprising two or more reaction zones, wherein advantageously essentially all of the silane compound is introduced into the first reaction zone to provide a higher conversion of silane monomer into polymer.

    摘要翻译: 本发明涉及通过自由基引发的乙烯聚合和烯属不饱和硅烷化合物如乙烯基三甲氧基硅烷(VTMS)制备包含可水解硅烷基团的乙烯 - 硅烷共聚物的改进方法。 所述方法在包含两个或更多个反应区的多区反应器中进行,其中有利地基本上所有的硅烷化合物都被引入到第一反应区中以提供更高的硅烷单体转化为聚合物。

    Removal of Hydrocarbons from an Aqueous Stream
    34.
    发明申请
    Removal of Hydrocarbons from an Aqueous Stream 有权
    从水流中去除碳氢化合物

    公开(公告)号:US20100282591A1

    公开(公告)日:2010-11-11

    申请号:US12808368

    申请日:2008-12-22

    IPC分类号: C02F1/04 C02F1/26

    摘要: The present application concerns a process for the removal of hydrocarbons from an aqueous stream, which process may include conducting a phenol-containing water stream into a separation column, separating the phenol-containing water in the column using heat to form an overhead portion and a bottoms portion, and collecting the overhead portion as well as the bottoms portion. Further, the process may include adding an eluent to an aqueous stream, thereby forming an aqueous mixture, subsequently conducting the aqueous mixture into a separation vessel, wherein it is allowed to settle into two phases, which form a hydrocarbon stream and a phenol-containing water stream, subsequently collecting the hydrocarbon stream, and conducting the phenol-containing water stream to the separation column for further separation.

    摘要翻译: 本申请涉及从水流中除去烃的方法,该方法可以包括将含苯酚的水流导入分离塔,使用热分离柱中的含苯酚的水以形成塔顶馏分和 底部部分,以及收集顶部部分以及底部部分。 此外,该方法可以包括向含水物流中加入洗脱液,从而形成水性混合物,随后将含水混合物导入分离容器中,其中将其沉降为两相,其形成烃流和含苯酚的 水流,随后收集烃流,并将含苯酚的水流导入分离塔进行进一步分离。

    Treatment of Phenol
    35.
    发明申请
    Treatment of Phenol 有权
    苯酚的处理

    公开(公告)号:US20100280285A1

    公开(公告)日:2010-11-04

    申请号:US12808369

    申请日:2008-12-22

    申请人: Veli-Matti Purola

    发明人: Veli-Matti Purola

    IPC分类号: C07C37/74 C07C37/68 B01J8/02

    摘要: A process for the removal of by-products from a phenolic mixture, which process may include the following steps: subjecting a phenolic mixture to extractive distillation to produce an initial phenolic mixture, contacting the initial phenolic mixture containing phenol and one or more by products with a catalyst to produce a first purified phenol product mixture, and distilling the first purified phenol product mixture to produce a second purified phenol product mixture; wherein the extractive distillation is carried out in two columns, a higher pressure column and a lower pressure column.

    摘要翻译: 一种从酚类混合物中除去副产物的方法,该方法可包括以下步骤:使酚类混合物进行萃取蒸馏以产生初始酚类混合物,使包含苯酚和一种或多种产物的初始酚类混合物与 产生第一纯化酚产物混合物的催化剂,并蒸馏第一纯化苯酚产物混合物以产生第二纯化苯酚产物混合物; 其中萃取蒸馏在高压塔和低压塔两列中进行。

    IMPACT-MODIFIED POLYPROPYLENE
    38.
    发明申请
    IMPACT-MODIFIED POLYPROPYLENE 有权
    IMPACT改性聚丙烯

    公开(公告)号:US20100256304A1

    公开(公告)日:2010-10-07

    申请号:US12734368

    申请日:2008-10-27

    IPC分类号: C08L23/12 C08L9/00

    摘要: The present invention relates to a polymer composition, comprising: (i) a polypropylene matrix; (ii) a first elastomeric phase dispersed within the matrix and having a glass transition temperature Tg1, measured with dynamical mechanical thermal analysis according to ISO 6721-2, wherein the first elastomeric phase comprises an ethylene copolymer having comonomer units derived from C3 to C8 olefins; (iii) a second elastomeric phase dispersed within the matrix, wherein the second elastomeric phase is crosslinked and has a glass transition temperature Tg2, measured with dynamical mechanical thermal analysis according to ISO 6721-2, within the range of −70° C. to −90° C., wherein the difference between Tg1 and Tg2 is at least 15° C. and Tg1 is higher than Tg2.

    摘要翻译: 本发明涉及聚合物组合物,其包含:(i)聚丙烯基质; (ii)分散在基体内并且具有根据ISO 6721-2的动态机械热分析测量的玻璃化转变温度Tg1的第一弹性体相,其中第一弹性体相包含具有衍生自C3至C8烯烃的共聚单体单元的乙烯共聚物 ; (iii)分散在基体内的第二弹性体相,其中第二弹性体相交联并且具有根据ISO 6721-2的动态机械热分析测量的玻璃化转变温度Tg2,其在-70℃至 -90℃,其中Tg1和Tg2之间的差为至少15℃,Tg1高于Tg2。