초록 ▼

The invention discloses a multi-metallic bulk catalyst with layered structure, wherein the metals in the multi-metallic bulk catalyst is consisted of a Group VIII metal MI, at least one metal MII with the valence of +3 and at least two Group VIB metals MIII+MIV, wherein (the mole number of MI+the mo

The invention discloses a multi-metallic bulk catalyst with layered structure, wherein the metals in the multi-metallic bulk catalyst is consisted of a Group VIII metal MI, at least one metal MII with the valence of +3 and at least two Group VIB metals MIII+MIV, wherein (the mole number of MI+the mole number of MII):(the mole number of MIII+the mole number of MIV) is from 1:9 to 9:1; the mole number of MI:the mole number of MII is from 1:5 to 5:1; and the mole number of MIII:the mole number of MIV is from 1:5 to 5:1. The invention also discloses the preparation method and use of the above catalyst. The invention is use for the hydrodesulfurization of diesel distillate including 4,6-dimethyldibenzothiophene, wherein the catalyst exhibits a extreme high hydrodesulfurization activity. Thus, the ultra-deep hydrodesulfurization is achieved and the cost of the bulk catalyst is reduced.

대표청구항 ▼

1. A multi-metallic bulk catalyst with layered structure, wherein the metals in the multi-metallic bulk catalyst is consisted of Ni, Al, Mo, and W, wherein: (the mole number of Ni+the mole number of Al):(the mole number of Mo+the mole number of W) is from 1:9 to 9:1;the mole number of Ni:the mole nu

1. A multi-metallic bulk catalyst with layered structure, wherein the metals in the multi-metallic bulk catalyst is consisted of Ni, Al, Mo, and W, wherein: (the mole number of Ni+the mole number of Al):(the mole number of Mo+the mole number of W) is from 1:9 to 9:1;the mole number of Ni:the mole number of Al is from 1:5 to 5:1;the mole number of Mo:the mole number of W is from 1:5 to 5:1; andthe multi-metallic bulk catalyst exists in a form of oxide. 2. The multi-metallic bulk catalyst according to claim 1 wherein (the mole number of Ni+the mole number of Al):(the mole number of Mo+the mole number of W) is from 1:3 to 3:1; the mole number of Ni:the mole number of Al is from 1:2 to 2:1; the mole number of Mo:the mole number of W is from 1:2 to 2:1. 3. A process for preparing the multi-metallic bulk catalyst according to claim 1, comprising the steps of: 1) heating a solution of soluble salts containing anion groups of the at least two Group VIB metals of molybdenum and tungsten, a mixed solvent of water and an organic solvent, and a surfactant to 50-150° C. under stirring, wherein the concentrations of the anions of the at least two Group VIB metals in the solution is 0.02-0.2 mol/L, respectively, and the concentration of the surfactant in the solution is 1-5 wt %; and2) adding a slurry of a catalyst precursor with layered structure into the solution of the step 1) to obtain a solid product, wherein in the slurry of a catalyst precursor with layered structure, the catalyst precursor with layered structure has a concentration of 0.1-0.9 mol/L, which is prepared by mixing an aqueous solution of a soluble salt of the Group VIII metal nickel and an aqueous solution of a soluble salt of the metal with the valence of +3 of aluminum, and heating to 50-150° C. to form the catalyst precursor with layered structure, wherein in the aqueous solution of the soluble salt of the Group VIII metal, the soluble salt of the Group VIII metal has a concentration of 0.01-0.1 mol/L, and in the aqueous solution of the soluble salt of the metal with the valence of +3, the soluble salt of the metal with the valence of +3 has a concentration of 0.01-0.1 mol/L. 4. The process according to claim 3 wherein the soluble salt of the Group VIII metal comprises one selected from the group consisting of nickel nitrate, nickel acetate, nickel sulfate and nickel chloride; the soluble salt of the metal with the valence of +3 comprises one selected from the group consisting of aluminium nitrate, aluminium chloride, and aluminium acetate;the soluble salts containing anion groups of the at least two Group VIB metals comprise one selected from the group consisting of ammonium molybdate and sodium molybdate, and one selected from the group consisting of ammonium tungstate, ammonium metatungstate and sodium tungstate. 5. The process according to claim 3 wherein the surfactant is hexadecyltrimethylammonium bromide, hexadecyltrimethylammonium chloride, octadecyltrimethylammonium bromide, or octadecyltrimethylammonium chloride. 6. A process of using the multi-metallic bulk catalyst according to claim 1 comprising contacting the catalyst of claim 1 with hydrogen and fuels having organic sulfur-containing compounds thus hydrodesulfurizing said fuels under a condition for hydrodesulfurization reaction. 7. The process according to claim 6 wherein the conditions for the hydrodesulfurization reaction are: a temperature of from 280 to 400° C., a pressure of hydrogen of from 1 to 20 MPa, a ratio by volume of hydrogen to the fuels having organic sulfur-containing compounds of from 50 to 1000, and a weight hourly space velocity of the raw materials of from 0.1 to 10 h−1. 8. The process according to claim 6 wherein, the catalyst, prior to the hydrodesulfurization reaction, is pre-treated by: a) pulverizing, kneading and molding; andb) pre-sulfurizing in situ in a hydrodesulfurization fixed-bed reactor at 300 to 450° C. with a mixed gas of a sulfur-containing compound and hydrogen. 9. The process according to claim 6 wherein the sulfur-containing compound is hydrogen sulfide, carbon disulfide or dimethyl disulfide.