Catalytic cracking gasoline prehydrogenation method

Patent metadata

Field	Value
Publication number	US-11674091-B2
Application number	US-202017133641-A
Country	US
Kind code	B2
Filing date	Dec 24, 2020
Priority date	Sep 11, 2018
Publication date	Jun 13, 2023
Grant date	Jun 13, 2023

Abstract

A catalytic cracking gasoline prehydrogenation method is provided. Thiol etherification and double bond isomerization reactions are carried out on catalytic cracking gasoline through a prehydrogenation reactor. The reaction conditions are as follows: the reaction temperature is between 80° C. and 160° C., the reaction pressure is between 1 MPa and 5 MPa, the liquid-volume hourly space velocity is from 1 to 10 h−1, and the hydrogen-oil volume ratio is (3-8):1; a prehydrogenation catalyst comprises a carrier and active ingredients, the carrier contains an aluminium oxide composite carrier with a macroporous structure and one or more of ZSM-5, ZSM-11, ZSM-12, ZSM-35, mordenite, amorphous form aluminum silicon, SAPO-11, MCM-22, a Y molecular sieve and a beta molecular sieve, the surface of the carrier is loaded with one or more of the active ingredients cobalt, molybdenum, nickel and tungsten; based on oxides, the content of the active ingredients is between 0.1% and 15.5%.

First claim

What is claimed is:

1. A catalytic cracking gasoline prehydrogenation method, comprising:
pumping catalytic cracking gasoline into a prehydrogenation reactor; and
carrying out thiol etherification and double bond isomerization reactions on the catalytic cracking gasoline with a prehydrogenation catalyst through the prehydrogenation reactor, wherein the reaction conditions are as follows: the reaction temperature is between 80° C. and 160° C., the reaction pressure is between 1 MPa and 5 MPa, the liquid-volume hourly space velocity is from 1 to 10 h −1 , and the hydrogen-oil volume ratio is (3-8):1; the prehydrogenation catalyst comprises a carrier and active ingredients, the carrier contains an aluminium oxide composite carrier with a macroporous structure and one or more of ZSM-5, ZSM-11, ZSM-12, ZSM-35, mordenite, amorphous form aluminum silicon, SAPO-11, MCM-22, a Y molecular sieve and a beta molecular sieve; the alumina composite carrier contains 0.1-12 wt % of tungsten-doped lanthanum ferrite, the mesopores of the alumina composite carrier account for 1-85 % of the total pores, and the macropores of the alumina composite carrier account for 1-70 % of the total pores; the surface of the carrier loads one or more of the active ingredients comprising cobalt, molybdenum, nickel, and tungsten, and based on oxides, the content of the active ingredients is between 0.1% and 15.5%; the tungsten-doped lanthanum ferrite is tungsten-doped lanthanum ferrite with micro-mesopores and the preparation method of the tungsten-doped lanthanum ferrite with micro-mesopores comprises: dissolving citric acid in water and stirring; next, adding lanthanum nitrate and ferric nitrate to the citric acid solution at stirring conditions; adding sodium polyacrylate or polyacrylic acid in an amount which is 0.1-9 wt % of the tungsten-doped lanthanum ferrite, and then adding a tungsten-containing compound, based on oxides, the tungsten content accounts for 0.1-8 wt % of the tungsten-doped lanthanum ferrite; stirring and reacting; and drying, calcining and grinding the resulting material, thus obtaining a finished product.

2. The catalytic cracking gasoline prehydrogenation method according to claim 1 , wherein the reaction conditions are as follows: the reaction temperature is between 90° C. and 145° C., the reaction pressure is between 1 MPa and 4 MPa, the liquid-volume hourly space velocity is from 1 to 8 −1 , and the hydrogen-oil volume ratio is (3-6):1.

3. The catalytic cracking gasoline prehydrogenation method according to claim 2 , wherein the aluminium oxide composite carrier contains 0.1-12 wt % of silicon oxide and 0.1-10 wt % of tungsten-doped lanthanum ferrite; mesopores account for 1-80% of the total pores, macropores account for 1-40% of the total pores, and the micropores, mesopores, and macropores in the carrier are unevenly distributed.

4. The catalytic cracking gasoline prehydrogenation method according to claim 2 , wherein the preparation method of the alumina composite carrier comprises: adding an aluminum source and sesbania powder to a kneader and mixing; adding an inorganic acid solution and an organic polymer and kneading; and then adding tungsten-doped lanthanum ferrite and kneading; and carrying out extruding, molding, drying and calcination, thus obtaining the alumina composite carrier.

5. The catalytic cracking gasoline prehydrogenation method according to claim 2 , wherein the preparation method of the prehydrogenation catalyst comprises: preparing an impregnation solution with active ingredient materials containing cobalt, molybdenum, nickel and tungsten, impregnating the carrier in the impregnation solution, drying at 120-180° C. for 4-8 h, and calcining at 450-800° C. for 3-9 h, thus obtaining a prehydrogenation catalyst.

6. The catalytic cracking gasoline prehydrogenation method according to claim 1 , wherein the tungsten-doped lanthanum ferrite in the alumina composite carrier accounts for 0.3-9 wt %, and in the tungsten-doped lanthanum ferrite, tungsten accounts for 0.1-8 wt %.

7. The catalytic cracking gasoline prehydrogenation method according to claim 6 , wherein the preparation method of the prehydrogenation catalyst comprises: preparing an impregnation solution with active ingredient materials containing cobalt, molybdenum, nickel and tungsten, impregnating the carrier in the impregnation solution, drying at 120-180° C. for 4-8 h, and calcining at 450-800° C. for 3-9 h, thus obtaining a prehydrogenation catalyst.

8. The catalytic cracking gasoline prehydrogenation method according to claim 1 , wherein in the aluminium oxide composite carrier with a macroporous structure, mesopores account for 5-70% of the total pores, and macropores account for 5-45% of the total pores.

9. The catalytic cracking gasoline prehydrogenation method according to claim 1 , wherein the aluminium oxide composite carrier contains 0.1-12 wt % of silicon oxide and 0.1-10 wt % of tungsten-doped lanthanum ferrite; mesopores account for 1-80% of the total pores, macropores account for 1-40% of the total pores, the micropores, mesopores, and macropores in the carrier are unevenly distributed.

10. The catalytic cracking gasoline prehydrogenation method according to claim 9 , wherein the preparation method of the alumina composite carrier comprises: adding an aluminum source and sesbania powder to a kneader and mixing; adding an inorganic acid or organic acid solution and an organic polymer and kneading; and then adding tungsten-doped lanthanum ferrite and mixing, thus obtaining an alumina precursor for later use; adding a silicon source to an acid solution of an organic polymer and mixing, and then mixing the resulting solution with the alumina precursor, wherein the unit content of the organic polymer in the alumina precursor is 1.5 times higher than the content of the organic polymer in the silicon source; and carrying out extruding, molding, drying and calcination, thus obtaining the alumina carrier.

11. The catalytic cracking gasoline prehydrogenation method according to claim 10 , wherein the silicon source is one or two of diatomite and opal, and the aluminum source is one or more of kaolin, rectorite, perlite, and montmorillonite.

12. The catalytic cracking gasoline prehydrogenation method according to claim 1 , wherein the preparation method of the alumina composite carrier comprises: adding an aluminum source and sesbania powder to a kneader and mixing; adding an inorganic acid solution and an organic polymer and kneading; and then adding tungsten-doped lanthanum ferrite and kneading; and carrying out extruding, molding, drying and calcination, thus obtaining the alumina composite carrier.

13. The catalytic cracking gasoline prehydrogenation method according to claim 12 , wherein the organic polymer is one or more of polyvinyl alcohol, sodium polyacrylate, polyethylene glycol, and polyacrylate.

14. The catalytic cracking gasoline prehydrogenation method according to claim 1 , wherein the preparation method of the prehydrogenation catalyst comprises: preparing an impregnation solution with active ingredient materials containing cobalt, molybdenum, nickel and tungsten, impregnating the carrier in the impregnation solution, drying at 120-180° C. for 4-8 h, and calcining at 450-800° C. for 3-9 h, thus obtaining a prehydrogenation catalyst.

Assignees

• Univ Fuzhou

Inventors

• Wang Tinghai
• Bao Xiaojun
• Yue Yuanyuan
• Wang Xueli
• Liu Jie
• Zhu Haibo
• Yuan Pei
• Bai Zhengshuai

Classifications

• C10G45/12 Primary

  containing crystalline alumino-silicates, e.g. molecular sieves · CPC title

• B01J23/8885

  containing also molybdenum · CPC title

• C10G2300/202

  Heteroatoms content, i.e. S, N, O, P · CPC title

• C10G45/04 Primary

  characterised by the catalyst used · CPC title

• C10G2300/4006

  Temperature · CPC title