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    Method for the production of defined mixtures of THF, BDO and GBL by gas phase hydrogenation
    7.
    发明授权
    Method for the production of defined mixtures of THF, BDO and GBL by gas phase hydrogenation 失效
    通过气相氢化制备THF，BDO和GBL的限定混合物的方法

    公开(公告)号：US07442810B2

    公开(公告)日：2008-10-28

    申请号：US10581074

    申请日：2004-12-04

    申请人： Markus Roesch ,  Rolf Pinkos ,  Michael Hesse ,  Stephan Schlitter ,  Henrik Junicke ,  Olga Schubert ,  Alexander Weck ,  Gunther Windecker

    发明人： Markus Roesch ,  Rolf Pinkos ,  Michael Hesse ,  Stephan Schlitter ,  Henrik Junicke ,  Olga Schubert ,  Alexander Weck ,  Gunther Windecker

    IPC分类号： C07D307/00 ,  C07D307/02

    CPC分类号： C07D307/33 ,  C07D307/08

    摘要： A process for variably preparing mixtures of optionally alkyl-substituted BDO, GBL and THF by two-stage hydrogenation in the gas phase of C4 dicarboxylic acids and/or derivatives thereof, which comprises a) hydrogenating in a gas phase a gas stream of C4 dicarboxylic acids and/or derivatives thereof over a particular catalyst at a particular pressure and temperature to give a stream mainly containing of optionally alkyl-substituted GBL and THF, b) removing any succinct anhydride, c) converting the products remaining predominantly in the gas phase in the partial condensation, THF, water and GBL to give a stream comprising a mixture of BDO, GBL and THF, d) removing the hydrogen from the products and recycling it into the hydrogenation, e) distillatively separating the products, THF, BDO, GBL and water, if appropriate recycling a GBL-rich stream or if appropriate discharging it, and working up BDO, THF and GBL distillatively, and setting the ratio of the products, THF, GBL and BDO, relative to one another within the range from 10 to 100% by weight of THF, from 0 to 90% by weight of GBL and from 0 to 90% by weight of BDO only by varying the temperatures in the two hydrogenation zones and also if appropriate the GBL recycle stream.

    摘要翻译： 一种在可能地制备任选烷基取代的BDO，GBL和THF的混合物的方法，其通过在C 4 C 4羧酸和/或其衍生物的气相中进行两步氢化，其包括a）在 在特定的压力和温度下，将特定催化剂上的C 4 O 2羧酸和/或其衍生物的气流气相，得到主要含有烷基取代的GBL和THF的物流，b）除去 任何简单的酸酐，c）将部分冷凝，THF，水和GBL中主要保留在气相中的产物进行转化，得到包含BDO，GBL和THF的混合物的流，d）从产物中除去氢并将其再循环 进入氢化，e）蒸馏分离产物，THF，BDO，GBL和水，如果适当回收富含GBL的物流或适当排放，并蒸馏处理BDO，THF和GBL，并设定产物的比例 ，TH F，GBL和BDO相对于10重量％至100重量％的THF，0至90重量％的GBL​​和0至90重量％的BDO，仅通过改变两者中的温度 加氢区，如果合适的话也可以使用GBL再循环流。

    Catalyst and method for the production of polytetrahydrofuran
    8.
    发明授权
    Catalyst and method for the production of polytetrahydrofuran 有权
    用于生产聚四氢呋喃的催化剂和方法

    公开(公告)号：US07041752B2

    公开(公告)日：2006-05-09

    申请号：US10481564

    申请日：2002-06-24

    申请人： Stephan Schlitter ,  Christoph Sigwart ,  Walter Dörflinger ,  Michael Hesse ,  Rolf-Hartmuth Fischer

    发明人： Stephan Schlitter ,  Christoph Sigwart ,  Walter Dörflinger ,  Michael Hesse ,  Rolf-Hartmuth Fischer

    IPC分类号： B01J29/06

    CPC分类号： B01J21/16 ,  B01J35/10 ,  B01J35/1061 ,  B01J35/1066 ,  C08G65/20 ,  C08G65/2657

    摘要： Polytetrahydrofuran, polytetrahydrofuran copolymers, diesters or monoesters of these polymers are prepared by polymerization of tetrahydrofuran in the presence of at least one telogen and/or comonomer, which is in the form of shaped catalyst bodies or catalyst particles having a volume of the individual shape of the body or particle of at least 0.05 mm3, preferably at least 0.2 mm3, in particular 1 mm3, and has at least one of the features a) and b): a) a pore radius distribution having at least one maximum in the pore radius range from 100 to 5000 Å, b) a pore volume of catalyst pores having radii of 200–3000 Å of greater than 0.05 cm3/g and/or a pore volume of pores having radii of 200–5000 Å of greater than 0.075 cm3/g and/or a pore volume of pores having radii of >200 Å of greater than 0.1 cm3/g.

    摘要翻译： 这些聚合物的聚四氢呋喃，聚四氢呋喃共聚物，二酯或单酯通过四氢呋喃在至少一种具有各种形状的成型催化剂体或催化剂颗粒的形式的存在下， 至少0.05mm 3的体或颗粒，优选至少0.2mm 3，特别是1mm 3，并且具有至少一个 的特征a）和b）：a）孔半径分布在孔半径范围内具有至少一个最大值为100至5000，b）具有大于0.05的半径的催化剂孔的孔体积为200-3000 cm 3 / g和/或具有大于0.075cm 3 / g的半径为200-5000的孔的孔体积和/或具有 > 200的半径大于0.1cm 3 / g。