发明名称 |
Selective nickel based hydrogenation catalyst and the preparation thereof |
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. |
申请公布号 |
US9597668(B2) |
申请公布日期 |
2017.03.21 |
申请号 |
US201414456858 |
申请日期 |
2014.08.11 |
申请人 |
PETROCHINA COMPANY LIMITED |
发明人 |
Liang Shunqin;Qian Ying;Lv Longgang;Sun Limin;Zheng Yundi;Wang Tinghai;Wu Jie;Cao Fengxia |
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 |
主分类号 |
B01J23/888 |
代理机构 |
Knobbe, Martens, Olson & Bear, LLP |
代理人 |
Knobbe, Martens, Olson & Bear, LLP |
主权项 |
1. A method for preparing a selective nickel-based hydrogenation catalyst, the method comprising:
adding silica or its precursor and alkaline earth metal oxide or its precursor into an alumina carrier so as to form a first mixture; calcinating the first mixture at the temperature of 800-1100° C. for 3-6 hours to form a modified alumina carrier; adding soluble salts of nickel, rare earth element and VIB group element into water so as to form a solution; adjusting the pH of the solution to 4-5 following full dissolution of the soluble salts to form an impregnating solution; impregnating the modified alumina carrier with the impregnating solution to form a second mixture; after impregnating, drying the second mixture at the temperature of 40-120° C.; and after drying, calcinating the second mixture at the temperature of 350-450° C. for 3-6 hours, thereby obtaining the resultant catalyst, wherein the modified alumina carrier is prepared by: adding silica sol, nitric acid and water into alumina hydrate so as to form a third mixture; after kneading and extruding the third mixture, drying the third mixture at the temperature of 40-120° C.; after drying, calcinating the third mixture at the temperature of 300-600° C. for 4-6 hours so as to form a carrier; impregnating the carrier with an impregnating solution formed by adding alkaline earth metal oxide into water; after impregnating, drying the carrier at the temperature of 40-120° C.; and after drying, calcinating the carrier at the temperature of 800-1100° C. for 4-6 hours, thereby forming the modified alumina carrier. |
地址 |
Beijing CN |