Hydrocracking catalyst
    12.
    发明授权
    Hydrocracking catalyst 有权
    加氢裂化催化剂

    公开(公告)号:US09199228B2

    公开(公告)日:2015-12-01

    申请号:US13266713

    申请日:2010-04-15

    摘要: Process of preparing a hydrocracking catalyst carrier comprising amorphous binder and zeolite Y, which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C., hydrocracking catalyst carrier comprising amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which catalyst has a peak at 3690 cm−1, substantially reduced peaks at 3630 cm−1 and 3565 cm−1 and no peak at 3600 cm−1, hydrocracking catalyst carrier comprising an amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, which catalyst has an acidity as measured by exchange with perdeuterated benzene of at most 20 micro-mole/gram, hydrocracking catalyst derived from such carrier and hydrocracking process with the help of such catalyst.

    摘要翻译: 制备包含无定形粘合剂和沸石Y的加氢裂化催化剂载体的方法,该方法包括将二氧化硅与氧化铝摩尔比至少为10的沸石Y在700至1000℃的温度下煅烧,加氢裂化催化剂载体包含非晶态 粘结剂和二氧化硅与氧化铝摩尔比至少为10的沸石Y,其催化剂在3690cm -1处具有峰值的红外光谱,在3630cm-1和3565cm -1处基本上减少的峰,在3600cm处没有峰 -1,包含无定形粘合剂的加氢裂化催化剂载体和二氧化硅与氧化铝摩尔比至少为10的沸石Y,该催化剂具有通过与每氘代苯交换至多20微摩尔/克的加氢裂化催化剂得到的酸度 从这种载体和加氢裂化过程中借助于这种催化剂。

    HYDROCRACKING CATALYST
    20.
    发明申请
    HYDROCRACKING CATALYST 有权
    水解催化剂

    公开(公告)号:US20120055846A1

    公开(公告)日:2012-03-08

    申请号:US13266713

    申请日:2010-04-15

    摘要: Process of preparing a hydrocracking catalyst carrier comprising amorphous binder and zeolite Y, which process comprises subjecting zeolite Y having a silica to alumina molar ratio of at least 10 to calcination at a temperature of from 700 to 1000° C., hydrocracking catalyst carrier comprising amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, the infrared spectrum of which catalyst has a peak at 3690 cm−1, substantially reduced peaks at 3630 cm−1 and 3565 cm−1 and no peak at 3600 cm−1, hydrocracking catalyst carrier comprising an amorphous binder and zeolite Y having a silica to alumina molar ratio of at least 10, which catalyst has an acidity as measured by exchange with perdeuterated benzene of at most 20 micro-mole/gram, hydrocracking catalyst derived from such carrier and hydrocracking process with the help of such catalyst.

    摘要翻译: 制备包含无定形粘合剂和沸石Y的加氢裂化催化剂载体的方法,该方法包括将二氧化硅与氧化铝摩尔比至少为10的沸石Y在700至1000℃的温度下煅烧,加氢裂化催化剂载体包含非晶态 粘结剂和二氧化硅与氧化铝摩尔比至少为10的沸石Y,其催化剂在3690cm -1处具有峰值的红外光谱,在3630cm-1和3565cm -1处基本上减少的峰,在3600cm处没有峰 -1,包含无定形粘合剂的加氢裂化催化剂载体和二氧化硅与氧化铝摩尔比至少为10的沸石Y,该催化剂具有通过与每氘代苯交换至多20微摩尔/克的加氢裂化催化剂得到的酸度 从这种载体和加氢裂化过程中借助于这种催化剂。