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公开(公告)号:US20140349844A1
公开(公告)日:2014-11-27
申请号:US14456858
申请日:2014-08-11
发明人: Shunqin Liang , Ying Qian , Longgang Lv , Limin Sun , Yundi Zheng , Tinghai Wang , Jie Wu , Fengxia Cao
IPC分类号: B01J23/888 , B01J23/86 , B01J23/887
CPC分类号: B01J23/888 , B01J21/04 , B01J21/12 , B01J23/78 , B01J23/83 , B01J23/85 , B01J23/866 , B01J23/8871 , B01J23/8872 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J37/0009 , B01J37/0207 , B01J37/024 , C10G2400/02
摘要: A selective nickel-based hydrogenation catalyst and the preparation thereof, characterized in that: provided that the catalyst is weighed 100%, it comprises nickel oxide 14-20% as active component, lanthanum oxide and/or cerium oxide 2-8%, and VIB element oxide 1-8% as aids, 2-8% silica, 1-8% alkaline earth metal oxides, and alumina as the balance. The catalyst specific surface area is 60-150 m2/g, and the pore volume is 0.4-0.6 ml/g. The catalyst has good hydrogenation performance, especially impurity and colloid resistance and hydrogenation stability. The catalyst can be applied to the diolefin selective hydrogenation of medium or low-distillate oil, especially of the full-distillates pyrolysis gasoline.
摘要翻译: 一种选择性镍基氢化催化剂及其制备方法,其特征在于:如果催化剂称重为100%,则其包含氧化镍14-20%作为活性组分,氧化镧和/或氧化铈2-8%,以及 VIB元素氧化物1-8%作为助剂,2-8%二氧化硅,1-8%碱土金属氧化物和氧化铝作为余量。 催化剂比表面积为60-150m2 / g,孔体积为0.4-0.6ml / g。 该催化剂具有良好的氢化性能,特别是杂质和胶体阻力以及氢化稳定性。 催化剂可用于中等或低馏分油,特别是全馏分裂解汽油的二烯烃选择性氢化。
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公开(公告)号:US09597668B2
公开(公告)日:2017-03-21
申请号:US14456858
申请日:2014-08-11
发明人: Shunqin Liang , Ying Qian , Longgang Lv , Limin Sun , Yundi Zheng , Tinghai Wang , Jie Wu , Fengxia Cao
IPC分类号: B01J23/888 , B01J21/12 , B01J23/83 , B01J23/85 , B01J23/86 , B01J23/887 , B01J35/10 , B01J37/02 , B01J21/04 , B01J23/78 , B01J37/00
CPC分类号: B01J23/888 , B01J21/04 , B01J21/12 , B01J23/78 , B01J23/83 , B01J23/85 , B01J23/866 , B01J23/8871 , B01J23/8872 , B01J35/1014 , B01J35/1019 , B01J35/1038 , B01J35/1042 , B01J37/0009 , B01J37/0207 , B01J37/024 , C10G2400/02
摘要: A selective nickel-based hydrogenation catalyst and the preparation thereof, characterized in that: provided that the catalyst is weighed 100%, it comprises nickel oxide 14-20% as active component, lanthanum oxide and/or cerium oxide 2-8%, and VIB element oxide 1-8% as aids, 2-8% silica, 1-8% alkaline earth metal oxides, and alumina as the balance. The catalyst specific surface area is 60-150 m2/g, and the pore volume is 0.4-0.6 ml/g. The catalyst has good hydrogenation performance, especially impurity and colloid resistance and hydrogenation stability. The catalyst can be applied to the diolefin selective hydrogenation of medium or low-distillate oil, especially of the full-distillates pyrolysis gasoline.
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