Process for the carbonylation of dimethyl ether
    3.
    发明授权
    Process for the carbonylation of dimethyl ether 有权
    二甲醚羰基化方法

    公开(公告)号:US08283490B2

    公开(公告)日:2012-10-09

    申请号:US12450986

    申请日:2008-04-23

    IPC分类号: C07C67/36

    摘要: Process for the production of methyl acetate by carbonylating a dimethyl ether feed with carbon monoxide in the presence of hydrogen under substantially anhydrous conditions, at a temperature in the range of greater than 250° C. to 350° C. and in the presence of a zeolite catalyst effective for said carbonylation. The concentration of dimethyl ether is at least 1 mol % based on the total feed.

    摘要翻译: 在大气条件下,在氢气存在下,在大于250℃至350℃范围内的温度下,用一氧化碳羰基化二甲醚进料并在 对于所述羰基化有效的沸石催化剂。 基于总进料,二甲醚的浓度为至少1摩尔%。

    Process for the carbonylation of dimethyl ether
    9.
    发明授权
    Process for the carbonylation of dimethyl ether 有权
    二甲醚羰基化方法

    公开(公告)号:US08394983B2

    公开(公告)日:2013-03-12

    申请号:US12450988

    申请日:2008-04-23

    IPC分类号: C07C67/36

    摘要: Process for the production of methyl acetate by the carbonylation of a dimethyl ether feed with carbon monoxide under substantially anhydrous conditions, in the presence of a zeolite catalyst effective for the carbonylation. The carbonylation is carried out at a temperature in the range of greater than 250° C. to 350° C. and at a pressure in the range of greater than 10 barg to 100 barg.

    摘要翻译: 在有效用于羰基化的沸石催化剂的存在下,在基本无水条件下通过二氧化碳进料与一氧化碳羰基化生产乙酸甲酯的方法。 羰基化在大于250℃至350℃的范围内的温度下进行,在大于10巴至100巴的范围内进行。

    PROCESS FOR THE CARBONYLATION OF DIMETHYL ETHER
    10.
    发明申请
    PROCESS FOR THE CARBONYLATION OF DIMETHYL ETHER 有权
    二甲醚的羰基化方法

    公开(公告)号:US20100063315A1

    公开(公告)日:2010-03-11

    申请号:US12450986

    申请日:2008-04-23

    IPC分类号: C07C67/37

    摘要: Production of methyl acetate by carbonylating a dimethyl ether feed with carbon monoxide in the presence of hydrogen under substantially anhydrous conditions, in the presence of a zeolite catalyst at a temperature in the range of greater than 250° C. to 350° C. and a dimethyl ether concentration of at least 1 mol %.

    摘要翻译: 在大气条件下,在氢气存在下,在沸石催化剂存在下,在大于250℃至350℃的温度范围内,用一氧化碳羰基化二甲醚进料,生产乙酸甲酯, 二甲醚浓度至少为1摩尔%。