Hydrotreating catalyst, process for producing same, and process for hydrotreating hydrocarbon oil
A hydrotreating catalyst that exhibits excellent levels of both desulfurization activity and denitrification activity. The hydrotreating catalyst is prepared by supporting molybdenum, cobalt and nickel on a carrier comprising aluminum, silicon, phosphorus and boron, and then performing a presulfiding treatment, and has an average stacking number for molybdenum sulfide slab that is greater than 1.0 but not more than 1.9. Also, a process for producing a hydrotreating catalyst that enables a hydrotreating catalyst having excellent levels of both desulfurization activity and denitrification activity to be produced with comparative ease. The process includes a first step of mixing an acidic aluminum salt aqueous solution and a basic aluminum salt aqueous solution in the presence of phosphate ions and silicate ions to achieve a pH of 6.5 to 9.5, thereby obtaining a hydrate, a second step of adding boron to the hydrate to prepare a carrier-forming material, a third step of molding and calcining the carrier-forming material to obtain a carrier, a fourth step of supporting molybdenum, cobalt and nickel on the carrier to obtain a catalyst precursor, and a fifth step of performing a presulfiding treatment by bringing the catalyst precursor into contact with a mixed gas containing hydrogen and hydrogen sulfide under conditions including a pressure of not less than 2.0 MPa and a maximum temperature of 240 to 380° C.
1. A hydrotreating catalyst being a calcined product comprising:
a carrier comprising aluminum, silicon, phosphorus and boron; and
molybdenum, cobalt and nickel supported on the carrier; wherein, relative to 100% by mass of the carrier,
(a) an aluminum content in the carrier in terms of aluminum oxide (Al 2 O 3 ) is 75% or more,
(b) a silicon content in the carrier in terms of silicon oxide (SiO 2 ) is 0.2% or more and 10.0% or less,
(c) a phosphorus content in the carrier in terms of phosphorus oxide (P 2 O 5 ) is 1.0% or more and 5.0% or less, and
(d) a boron content in the carrier in terms of boron oxide (B 2 O 3 ) is 3.0% or more and 7.0% or less, wherein
the hydrotreating catalyst is calcined before a presulfiding treatment, and
an average stacking number for a molybdenum sulfide slab is greater than 1.0 but not more than 1.9.
2. The hydrotreating catalyst being a calcined product according to claim 1 , wherein, relative to 100% by mass of the carrier,
(e) a molybdenum content in terms of molybdenum oxide (MoO 3 ) is 10% or more and 23% or less,
(f) a cobalt content in terms of cobalt oxide (CoO) is 1.0% or more and 5.0% or less, and
(g) a nickel content in terms of nickel oxide (NiO) is 0.2% or more and 0.3% or less.
3. A process for producing the hydrotreating catalyst according to claim 1 , the process comprising subjecting a catalyst precursor, prepared by supporting molybdenum, cobalt and nickel on a carrier comprising aluminum, silicon, phosphorus and boron, to a presulfiding treatment such that an average stacking number for molybdenum sulfide slab following sulfidization is greater than 1.0 but not more than 1.9.
4. A process for hydrotreating a hydrocarbon oil, the process comprising bringing the hydrocarbon oil into contact with the hydrotreating catalyst according to claim 1 in the presence of hydrogen.
5. A process for producing the hydrotreating catalyst according to claim 1 , the process comprising:
a first step of mixing an acidic aluminum salt aqueous solution and a basic aluminum salt aqueous solution in presence of phosphate ions and silicate ions to achieve a pH of 6.5 to 9.5, thereby obtaining a hydrate,
a second step of adding boron to the hydrate to prepare a carrier-forming material,
a third step of molding and calcining the carrier-forming material to obtain a carrier,
a fourth step of supporting molybdenum, cobalt and nickel on the carrier to obtain a catalyst precursor, wherein calcination occurs after incorporation of the molybdenum, cobalt and nickel into the carrier, and
a fifth step of performing a presulfiding treatment by bringing the catalyst precursor into contact with a mixed gas comprising hydrogen and hydrogen sulfide under conditions including a pressure of not less than 2.0 MPa and a maximum temperature of 240 to 380° C.
6. The process for producing a hydrotreating catalyst according to claim 5 , wherein the supporting of molybdenum, cobalt and nickel on the carrier is performed in presence of phosphoric acid and a carboxylic acid compound.
7. A process for hydrotreating a hydrocarbon oil, the process comprising bringing the hydrocarbon oil into contact with the hydrotreating catalyst according to claim 2 in the presence of hydrogen.
8. A hydrotreating catalyst produced by a process for producing a hydrotreating catalyst, the process comprising:
a first step of mixing an acidic aluminum salt aqueous solution and a basic aluminum salt aqueous solution in the presence of phosphate ions and silicate ions to achieve a pH of 6.5 to 9.5, thereby obtaining a hydrate,
a second step of adding boron to the hydrate to prepare a carrier-forming material,
a third step of molding and calcining the carrier-forming material to obtain a carrier,
a fourth step of supporting molybdenum, cobalt and nickel on the carrier to obtain a catalyst precursor, wherein calcination occurs after incorporation of the molybdenum, cobalt and nickel into the carrier, and
a fifth step of performing a presulfiding treatment by bringing the catalyst precursor into contact with a mixed gas comprising hydrogen and hydrogen sulfide under conditions including a pressure of not less than 2.0 MPa and a maximum temperature of 240 to 380° C.,
wherein an average stacking number for a molybdenum sulfide slab is greater than 1.0 but not more than 1.9.
9. A process for hydrotreating a hydrocarbon oil, the process comprising bringing the hydrocarbon oil into contact with the hydrotreating catalyst according to claim 8 in the presence of hydrogen.