-
1.发明公开CATALYSEUR MESOPOREUX ET MACROPOREUX A BASE DE NICKEL OBTENU PAR COMALAXAGE ET AYANT UN DIAMETRE MEDIAN MACROPOREUX SUPERIEUR A 300 NM ET SON UTILISATION EN HYDROGENATION D'HYDROCARBURES 审中-公开介孔和大孔的催化剂FROM通过联合磨削生产的镍和与宏多孔介质直径大于300纳米及其用途中的烃的氢化
公开(公告)号：EP3154686A1
公开(公告)日：2017-04-19
申请号：EP15730988.1
申请日：2015-06-09
IPC分类号： B01J23/755 , B01J21/04 , B01J35/10 , B01J37/03 , B01J37/04 , B01J37/08 , B01J37/16 , B01J37/20 , B01J33/00 , C10G45/36 , C10G45/48 , C07C5/03 , C07C5/10 , B01J27/185 , C01F7/02 , C01F7/34
CPC分类号： B01J23/755 , B01J21/04 , B01J33/00 , B01J35/006 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1057 , B01J35/1061 , B01J35/1066 , B01J35/1071 , B01J35/108 , B01J37/009 , B01J37/0236 , B01J37/03 , B01J37/036 , B01J37/04 , B01J37/08 , B01J37/16 , B01J37/20 , C07C5/03 , C07C5/05 , C07C5/10 , C07C2521/04 , C07C2523/755 , C07C2601/14 , C10G45/36 , C10G45/40 , C10G45/48 , C10G45/52 , C10G2300/1096 , C10G2300/705 , C07C13/18 , C07C15/073 , C07C11/10 , C07C9/18
摘要： The invention concerns a catalyst comprising a predominantly calcined aluminium oxide matrix and an active phase comprising nickel, said active phase being at least partially comulled in said predominantly calcined aluminium oxide matrix, the nickel content being between 5 and 65% by weight of said element relative to the total mass of the catalyst, said active phase not comprising group VIB metal, the nickel particles having a diameter less than 15 nm, said catalyst having a mesoporous median diameter of between 8 nm and 25 nm, a macroporous median diameter greater than 300 nm, a mesoporous volume measured by mercury porosimetry greater than or equal to 0.30 mL/g and a total porous volume measured by mercury porosimetry greater than or equal to 0.34 mL/g. The invention also concerns the method of preparing said catalyst and the use of same in a hydrogenation method.
摘要翻译： 本发明涉及一种催化剂，其包含煅烧的氧化物基体的所有主要是氧化铝和在活性相包含镍，所述活性相是至少部分共混合所述煅烧氧化物基质内的所有这主要是氧化铝，镍含量范围为5％为 至65％重量的所述元件相对于催化剂的总质量，所述活性相不包含选自第VIB族的金属，其具有直径小于15纳米的镍颗粒，所述催化剂具有在范围为8的中值孔直径 纳米至25纳米，超过300纳米，介孔体积的中值大孔直径，由压汞法测定的12:30毫升/ g以上，总孔体积，通过压汞法测定的12点34毫升/克或更多，。 因此，本发明涉及所述方法为催化剂。所述的制备，和它在氢化过程中使用。
-
2.发明公开CATALYSEUR A BASE DE NICKEL MESOPOREUX ET MACROPOREUX AYANT UN DIAMETRE MEDIAN MACROPOREUX SUPERIEUR A 200 NM ET SON UTILISATION EN HYDROGENATION D'HYDROCARBURES 审中-公开拥有超过200nm的大孔中直径及其用途在KOHLENWASSERSTOFFHYDRIERUNG介孔孔镍制得的催化剂
公开(公告)号：EP3154684A1
公开(公告)日：2017-04-19
申请号：EP15726214.8
申请日：2015-06-09
IPC分类号： B01J23/755 , B01J21/04 , B01J23/74 , B01J37/03 , B01J37/08 , B01J37/16 , B01J37/20 , B01J23/78 , B01J23/835 , B01J23/89 , B01J27/185 , B01J33/00 , B01J35/10 , B01J37/02 , C07C5/03 , C07C5/10 , C10G45/36 , C10G45/48 , C01F7/02 , C01F7/34
摘要： The invention concerns a supported catalyst comprising a predominantly calcined aluminium oxide support and an active phase comprising nickel, the nickel content being between 5 and 65% by weight of said element relative to the total mass of the catalyst, said active phase not comprising group VIB metal, the nickel particles having a diameter less than or equal to 20 nm, said catalyst having a mesoporous median diameter of between 8 nm and 25 nm, a macroporous median diameter greater than 200 nm, a mesoporous volume measured by mercury porosimetry greater than or equal to 0.30 mL/g and a total porous volume measured by mercury porosimetry greater than or equal to 0.34 mL/g. The invention also concerns the method of preparing said catalyst and the use of same in a hydrogenation method.
摘要翻译： 本发明涉及的担载催化剂并氧化物基板包括所做的是在大多数情况下煅烧铝，并在活跃期做包括镍，与镍含量为5和65％之间（重量）所述元件相对于总质量 催化剂，用所述活性相不包含第VIB族的金属，具有直径镍颗粒确实是小于或等于20nm，所述催化剂具有8nm和，中值大孔直径之间25nm的中值孔直径 大于200nm时，中孔量并通过压汞法测定所做的是大于或等于0:30毫升/克，和总孔体积也通过压汞法测定所做的是大于或等于0:34毫升/克。 因此本发明涉及一种用于制备所述催化剂和其使用在氢化方法中的方法。
-
3.发明公开CATALYSEUR MESOPOREUX ET MACROPOREUX A BASE DE NICKEL AYANT UN DIAMETRE MEDIAN MACROPOREUX COMPRIS ENTRE 50 NM ET 200 NM ET SON UTILISATION EN HYDROGENATION D'HYDROCARBURES 审中-公开与宏多孔介质直径之间50和200nm及其用途中的烃的氢化中孔和大孔的催化剂中金属镍
公开(公告)号：EP3154685A1
公开(公告)日：2017-04-19
申请号：EP15726639.6
申请日：2015-06-09
IPC分类号： B01J23/755 , B01J23/78 , B01J23/835 , B01J23/89 , B01J37/03 , B01J35/10 , B01J37/08 , B01J37/16 , B01J37/20 , B01J27/185 , B01J37/02 , B01J33/00 , C07C5/03 , C07C5/10 , C10G45/36 , C10G45/48 , C01F7/02 , C01F7/34
摘要： The invention concerns a supported catalyst comprising a predominantly calcined aluminium oxide support and an active phase comprising nickel, the nickel content being between 5 and 65% by weight of said element relative to the total mass of the catalyst, said active phase not comprising group VIB metal, the nickel particles having a diameter less than or equal to 20 nm, said catalyst having a mesoporous median diameter of between 14 nm and 30 nm, a macroporous median diameter of between 50 and 200 nm, a mesoporous volume measured by mercury porosimetry greater than or equal to 0.40 mL/g and a total porous volume measured by mercury porosimetry greater than or equal to 0.42 mL/g. The invention also concerns the method of preparing said catalyst and the use of same in a hydrogenation method.
摘要翻译： 本发明涉及一种负载型催化剂，其包括主要的煅烧氧化铝载体和活性相包含镍，镍含量5至65％之间（重量）元素相对于催化剂的总质量。所述的，所述活性相不包含VIB族 金属，具有直径小于或等于20nm的镍颗粒，其具有14纳米和30纳米，50至200纳米之间的大孔的中值粒径之间的中孔的中值粒径，所述催化剂，中孔容积通过水银孔隙率更大的测量 大于或等于0:40毫升/克和通过水银孔隙率大于或等于0:42毫升/克测量的总孔体积。 本发明因此涉及制备所述催化剂，并在氢化方法中的用途的相同的方法。
-
4.发明公开CATALYSEUR MESOPOREUX A BASE DE NICKEL ET SON UTILISATION EN HYDROGENATION D'HYDROCARBURES 审中-公开CATALYSEUR MESOPOREUX A底部和底部的催化剂用于加氢和烃加氢
公开(公告)号：EP3191221A1
公开(公告)日：2017-07-19
申请号：EP15759689.1
申请日：2015-08-21
IPC分类号： B01J21/04 , B01J23/755 , B01J23/78 , B01J23/835 , B01J23/89 , B01J27/185 , B01J33/00 , B01J37/03 , B01J37/08 , B01J37/16 , B01J37/20 , B01J35/10 , B01J37/02 , C07C5/03 , C07C5/10 , C10G45/36 , C10G45/48 , C01F7/02 , C01F7/34
摘要： The invention relates to a supported catalyst comprising a predominantly calcined aluminium oxide support and an active phase comprising nickel, the nickel content being between 5 and 65% by weight of said element relative to the total mass of the catalyst, said active phase not comprising group VIB metals, the nickel particles having a diameter less than or equal to 20 nm, said catalyst having a mesoporous median diameter greater than or equal to 14 nm, a mesoporous volume measured by mercury porosimetry of greater than or equal to 0.45 ml/g, a total porous volume measured by mercury porosimetry greater than or equal to 0.45 ml/g, a macroporous volume less than 5% of the total porous volume, said catalyst being in the form of grains having a mean diameter of between 0.5 et 0 mm. The invention also relates to the method for preparation of said catalyst and the use of same in a hydrogenation method.
摘要翻译： 本发明涉及负载型催化剂，其包含主要煅烧的氧化铝载体和包含镍的活性相，镍含量相对于催化剂的总质量为5-65重量％，所述活性相不包含基团 VIB金属，直径小于或等于20nm的镍颗粒，所述催化剂具有大于或等于14nm的中孔直径，通过水银孔隙率测量法测量的介孔体积大于或等于0.45ml / g， 通过水银孔隙率测量法测量的总多孔体积大于或等于0.45ml / g，大孔体积小于总多孔体积的5％，所述催化剂呈平均直径在0.5和0mm之间的颗粒形式。 本发明还涉及制备所述催化剂的方法及其在氢化方法中的用途。
-
5.发明公开CATALYSEUR MESOPOREUX ET MACROPOREUX A PHASE ACTIVE DE NICKEL OBTENU PAR COMALAXAGE ET AYANT UN DIAMETRE MEDIAN MACROPOREUX COMPRIS ENTRE 50 ET 300 NM ET SON UTILISATION EN HYDROGENATION D'HYDROCARBURES 审中-公开具有由CO-搅拌孔和大孔的催化剂制造了具有在烃的氢化的50至300纳米，它的使用之间的大孔平均直径的镍活性相
公开(公告)号：EP3154676A1
公开(公告)日：2017-04-19
申请号：EP15726215.5
申请日：2015-06-09
IPC分类号： B01J21/04 , B01J23/78 , B01J23/835 , B01J23/89 , B01J27/185 , B01J33/00 , B01J35/10 , B01J37/03 , B01J37/04 , B01J37/08 , B01J37/16 , B01J37/20 , C07C5/03 , C07C5/10 , C10G45/36 , C10G45/48 , C01F7/02 , C01F7/34 , B01J23/755
CPC分类号： B01J23/755 , B01J21/04 , B01J23/835 , B01J23/892 , B01J27/1853 , B01J33/00 , B01J35/006 , B01J35/023 , B01J35/026 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J35/1047 , B01J35/1061 , B01J35/1066 , B01J35/109 , B01J35/1095 , B01J37/0009 , B01J37/0045 , B01J37/009 , B01J37/0236 , B01J37/03 , B01J37/036 , B01J37/038 , B01J37/04 , B01J37/08 , B01J37/20 , B01J2523/00 , C07C5/03 , C07C5/05 , C07C5/10 , C07C2521/04 , C07C2523/755 , C07C2601/14 , C10G45/36 , C10G45/48 , C07C9/18 , C07C15/073 , C07C11/10 , C07C13/18 , B01J2523/31 , B01J2523/847
摘要： The invention concerns a catalyst comprising a predominantly calcined aluminium oxide matrix and an active phase comprising nickel, said active phase being at least partially comulled in said predominantly calcined aluminium oxide matrix, the nickel content being between 5 and 65% by weight of said element relative to the total mass of the catalyst, said active phase not comprising group VIB metal, the nickel particles having a diameter less than 15 nm, said catalyst having a mesoporous median diameter of between 12 nm and 25 nm, a macroporous median diameter of between 50 and 300 nm, a mesoporous volume measured by mercury porosimetry greater than or equal to 0.40 mL/g and a total porous volume measured by mercury porosimetry greater than or equal to 0.45 mL/g. The invention also concerns the method of preparing said catalyst and the use of same in a hydrogenation method.
摘要翻译： 本发明涉及一种催化剂，其包含主要煅烧氧化铝基质和活性相包含镍，所述活性相是至少部分comulled在说主要煅烧氧化铝基质，镍含量5至65％之间重量的所述元件相对于 对于催化剂的总质量，所述活性相不包含VIB族金属，直径小于15nm的镍颗粒，所述催化剂具有12纳米之间和25nm的中孔的中值粒径，50之间的大孔的中值粒径 和300nm的中孔容积通过水银孔隙率大于或等于测量到00:40毫升/克和通过水银孔隙率大于或等于12:45毫升/克测量的总孔体积。 本发明因此涉及制备所述催化剂，并在氢化方法中的用途的相同的方法。
-
-
-
-
搜索结果
5 条记录 (耗时 0.012 秒)
