Polyol-based polymers
    2.
    发明授权
    Polyol-based polymers 有权
    多元醇类聚合物

    公开(公告)号:US08912304B2

    公开(公告)日:2014-12-16

    申请号:US12600596

    申请日:2008-05-16

    摘要: The present invention provides inventive polyol-based polymers, materials, pharmaceutical compositions, and methods of making and using the inventive polymers and materials. In certain aspects of the invention, an inventive polymer corresponds to a polymer depicted below. Exemplary inventive polymers includes those prepared using polyol units (e.g., xylitol, mannitol, sorbitol, or maltitol) condensed with polycarboxylic acid units (e.g., citric acid, glutaric acid, or sebacic acid). The inventive polymers may be further derivatized or modified. For example, the polymer may be made photocrosslinkable by adding methacrylate moieties to the polymer.

    摘要翻译: 本发明提供本发明的多元醇基聚合物,材料,药物组合物以及制备和使用本发明的聚合物和材料的方法。 在本发明的某些方面,本发明的聚合物对应于下面描述的聚合物。 示例性的本发明聚合物包括使用与多元羧酸单元(例如柠檬酸,戊二酸或癸二酸)缩合的多元醇单元(例如木糖醇,甘露糖醇,山梨糖醇或麦芽糖醇)制备的那些聚合物。 本发明的聚合物可进一步衍生或修饰。 例如,可以通过向聚合物中加入甲基丙烯酸酯部分使聚合物可光交联。

    POLYOL-BASED POLYMERS
    8.
    发明申请
    POLYOL-BASED POLYMERS 有权
    基于聚合物的聚合物

    公开(公告)号:US20110008277A1

    公开(公告)日:2011-01-13

    申请号:US12600596

    申请日:2008-05-16

    IPC分类号: A61K31/765 C08G63/12

    摘要: The present invention provides inventive polyol-based polymers, materials, pharmaceutical compositions, and methods of making and using the inventive polymers and materials. In certain aspects of the invention, an inventive polymer corresponds to a polymer depicted below. Exemplary inventive polymers includes those prepared using polyol units (e.g., xylitol, mannitol, sorbitol, or maltitol) condensed with polycarboxylic acid units (e.g., citric acid, glutaric acid, or sebacic acid). The inventive polymers may be further derivatized or modified. For example, the polymer may be made photocrosslinkable by adding methacrylate moieties to the polymer.

    摘要翻译: 本发明提供本发明的多元醇基聚合物,材料,药物组合物以及制备和使用本发明的聚合物和材料的方法。 在本发明的某些方面,本发明的聚合物对应于下面描述的聚合物。 示例性的本发明聚合物包括使用与多元羧酸单元(例如柠檬酸,戊二酸或癸二酸)缩合的多元醇单元(例如木糖醇,甘露糖醇,山梨糖醇或麦芽糖醇)制备的那些聚合物。 本发明的聚合物可进一步衍生或修饰。 例如,可以通过向聚合物中加入甲基丙烯酸酯部分使聚合物可光交联。

    MULTI STAGE PROCESS FOR PRODUCING HYDROCARBONS FROM SYNGAS
    9.
    发明申请
    MULTI STAGE PROCESS FOR PRODUCING HYDROCARBONS FROM SYNGAS 审中-公开
    从SYNGAS生产石油烃的多阶段工艺

    公开(公告)号:US20100184873A1

    公开(公告)日:2010-07-22

    申请号:US12640298

    申请日:2009-12-17

    IPC分类号: C07C27/06

    CPC分类号: C10G2/30 C10K3/06

    摘要: The invention pertains to a multi-stage process for the production of hydrocarbons from syngas comprising hydrogen and carbon monoxide, which comprises the steps of: a) providing a fresh syngas feed to a first stage Fischer-Tropsch reactor and allowing CO and hydrogen to convert into hydrocarbon products at a temperature in the range from 125 to 400° C. and a pressure in the range from 5 to 150 bar absolute, and a gaseous hourly space velocity in the range from 500 to 10000 Nl/l/h; b) feeding the effluent from the first stage reactor to a separation unit; c) removing a gasous effluent stream comprising hydrogen and CO from the separation unit; d) removing one or more other streams comprising hydrocarbon and/or water from the separation unit; e) conveying a first portion of the gaseous effluent stream to a second stage Fischer-Tropsch reactor and allowing CO and hydrogen to convert into hydrocarbon products in the second stage Fischer-Tropsch reactor at a temperature in the range from 125 to 400° C. and a pressure in the range from 5 to 150 bar absolute, and a gaseous hourly space velocity in the range from 500 to 10000 Nl/l/h, whereby the first stage Fischer-Tropsch reactor and the second stage Fischer-Tropsch reactor are separate reactors; f) feeding the effluent from the second stage Fischer-Tropsch reactor to the separation unit; g) removing a second portion of the gaseous effluent stream as off-gas.

    摘要翻译: 本发明涉及用于从包含氢气和一氧化碳的合成气生产碳氢化合物的多级方法,其包括以下步骤:a)向新的第一阶段费 - 托反应器提供新的合成气进料并允许CO和氢转化 在125至400℃的温度和5至150巴绝对压力的范围内的气体产物,并且气时空速在500至10000Nl / l / h的范围内; b)将来自第一级反应器的流出物供给到分离单元; c)从分离单元中除去包含氢和CO的气体流出物流; d)从分离单元去除包含烃和/或水的一种或多种其它流; e)将第一部分气态流出物流输送到第二级费 - 托反应器,并允许CO和氢在第二级费 - 托反应器中在125-400℃的温度下转化成烃产物。 压力范围为5至150巴绝对压力,气时空速为500至10000Nl / l / h,其中第一级费 - 托反应器和第二级费 - 托反应器是分开的 反应堆 f)将来自第二级费 - 托反应器的流出物供给到分离单元; g)除去作为废气的气态流出物流的第二部分。