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    Process For Manufacturing Ethanol Using A Metallic Catalyst Supported on Titania
    41.
    发明申请
    Process For Manufacturing Ethanol Using A Metallic Catalyst Supported on Titania 审中-公开
    使用二氧化钛负载的金属催化剂制造乙醇的方法

    公开(公告)号：US20130197278A1

    公开(公告)日：2013-08-01

    申请号：US13360067

    申请日：2012-01-27

    申请人： Zhenhua Zhou ,  Radmila Jevtic ,  Victor J. Johnston ,  Heiko Weiner

    发明人： Zhenhua Zhou ,  Radmila Jevtic ,  Victor J. Johnston ,  Heiko Weiner

    IPC分类号： C07C29/149

    CPC分类号： C07C29/149 ,  C07C31/08

    摘要： The present invention relates to a process for producing ethanol by contacting a feedstock comprising acetic acid and hydrogen in a reaction zone at hydrogenation conditions including a temperature from 125° C. to 350° C. with a catalyst composition, wherein the catalyst composition comprises from 1.5 wt. % to 3 wt. % active metals on a titania support, said active metals comprising at least one Group VIII metal and an excess molar amount of tin, relative to the at least one Group VIII metal.

    摘要翻译： 本发明涉及一种生产乙醇的方法，该方法通过在催化剂组合物的氢化条件（包括125℃至350℃的温度）下在反应区中使包含乙酸和氢的原料接触，其中催化剂组合物包含 1.5重量％ ％〜3重量％ 相对于至少一种第Ⅷ族金属，所述活性金属包含至少一种第Ⅷ族金属和过量摩尔量的锡。

    Chemisorption of ethyl acetate during hydrogenation of acetic acid to ethanol
    46.
    发明授权
    Chemisorption of ethyl acetate during hydrogenation of acetic acid to ethanol 有权
    在乙酸氢化成乙醇期间乙酸乙酯的化学吸附

    公开(公告)号：US09050585B2

    公开(公告)日：2015-06-09

    申请号：US13371064

    申请日：2012-02-10

    申请人： Zhenhua Zhou ,  Heiko Weiner ,  Dheeraj Kumar ,  Xiaoyan Tu ,  Victor J. Johnston ,  Radmila Jevtic

    发明人： Zhenhua Zhou ,  Heiko Weiner ,  Dheeraj Kumar ,  Xiaoyan Tu ,  Victor J. Johnston ,  Radmila Jevtic

    IPC分类号： C07C27/04 ,  B01J23/89 ,  C07C29/149 ,  C07C67/56 ,  C07C31/08 ,  B01J37/02 ,  B01J37/00

    CPC分类号： B01J23/8993 ,  B01J23/8966 ,  B01J23/898 ,  B01J37/0018 ,  B01J37/0201 ,  B01J37/0205 ,  C07C29/149 ,  C07C31/08 ,  C07C67/56 ,  C07C69/14

    摘要： A hydrogenation catalyst and process using the catalyst for converting a mixture comprising acetic acid and ethyl acetate to ethanol at a first temperature, and the catalyst desorbs ethyl acetate, in the absence of hydrogen, at a second temperature that is greater than the first temperature. The catalyst has a suitable chemisorption of ethyl acetate at the first temperature in the absence of hydrogen. In one embodiment, the first temperature ranges from 125° C. to 350° C. and the second temperature ranges from 300° C. to 600° C. The catalyst comprises one or more active metals or oxide thereof on a support that comprises tungsten or an oxide thereof. The one or more active metals are selected from the group consisting of cobalt, copper, gold, iron, nickel, palladium, platinum, iridium, osmium, rhenium, rhodium, ruthenium, tin, zinc, lanthanum, cerium, manganese, chromium, vanadium, and molybdenum.

    摘要翻译： 一种氢化催化剂和在第一温度下将包含乙酸和乙酸乙酯的混合物转化成乙醇的催化剂的方法，催化剂在不存在氢气的情况下在大于第一温度的第二温度下解吸乙酸乙酯。 在不存在氢气的情况下，催化剂在第一温度下具有适当的乙酸乙酯化学吸附。 在一个实施方案中，第一温度范围为125℃至350℃，第二温度范围为300℃至600℃。催化剂在包含钨的载体上包含一种或多种活性金属或其氧化物 或其氧化物。 一种或多种活性金属选自钴，铜，金，铁，镍，钯，铂，铱，锇，铼，铑，钌，锡，锌，镧，铈，锰，铬，钒 ，和钼。