초록 ▼

This disclosure provides an adsorbing agent which, on the basis of the total weight of the adsorbing agent, comprises the following components: 1) a Si—Al molecular sieve having a BEA structure, in an amount of 1-20 wt %, 2) at least one binder selected from the group consisting of titanium dioxide,

This disclosure provides an adsorbing agent which, on the basis of the total weight of the adsorbing agent, comprises the following components: 1) a Si—Al molecular sieve having a BEA structure, in an amount of 1-20 wt %, 2) at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina, in an amount of 3-35 wt %, 3) a silica source, in an amount of 5-40 wt %, 4) zinc oxide, in an amount of 10-80 wt %, and 5) at least one promoter metal selected from the group consisting of cobalt, nickel, iron and manganese, based on the metal, in an amount of 5-30 wt %, wherein at least 10 wt % of the promoter metal is present in a reduced valence state. The adsorbing agent exhibits improved activity and stability, and at the same time, is capable of significantly improving the octane number of the product gasoline.

대표청구항 ▼

1. A process for producing a desulfurization adsorbing agent for hydrocarbon oil, comprising: (1) contacting at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina with a silica source, a Si—Al molecular sieve having a BEA structure and

1. A process for producing a desulfurization adsorbing agent for hydrocarbon oil, comprising: (1) contacting at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina with a silica source, a Si—Al molecular sieve having a BEA structure and zinc oxide, to obtain a carrier,(2) contacting the carrier with a promoter metal-containing compound, to obtain a precursor of the adsorbing agent, and(3) under a condition sufficient to present at least 10 wt % of the promoter metal in a reduced valence state, treating the precursor of the adsorbing agent, to obtain the desulfurization adsorbing agent for hydrocarbon oil,wherein the step (1) further comprises:(1a) mixing the binder or a binder precursor with an acid to form a slurry, and(1b) mixing the slurry, the silica source, the Si—Al molecular sieve having a BEA structure and zinc oxide to form a mixture and subject the mixture to molding, drying, and calcination to obtain the carrier,wherein the desulfurization adsorbing agent comprises:1) a Si—Al molecular sieve having a BEA structure:2) at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina;3) a silica source;4) zinc oxide; and5) at least one promoter metal selected from the group consisting of cobalt, nickel, iron and manganese, based on the metal, wherein at least 10 wt % of the promoter metal is present in a reduced valence state, andwherein the Si—Al molecular sieve is in an amount of 2-15 wt %, the binder is in an amount of 5-25 wt %, the silica source is in an amount of 10-30 wt %, zinc oxide is in an amount of 25-70 wt %, and the promoter metal is in an amount of 8-25 wt %, all based on a total weight of the desulfurization absorbing agent. 2. The process according to claim 1, wherein the binder precursor is at least one selected from the group consisting of halides, alkoxylates, carboxylic acid salts, hydrated oxides, hydroxides, hydrated hydroxides and oxyhalides, of titanium, tin, zirconium, and aluminum. 3. The process according to claim 1, wherein the acid is at least one selected from the group consisting of a water soluble inorganic acid and a water soluble organic acid, and the amount of the acid to be used is such that the pH value of the slurry reaches 0.5-6. 4. The process according to claim 1, wherein, in the desulfurization absorbing agent, the Si—Al molecular sieve having a BEA structure is in an amount of 2-10 wt %, the binder is in an amount of 8-15 wt %, the silica source is in an amount of 12-25 wt %, the zinc oxide is in an amount of 40-60 wt %, the promoter metal is in an amount of 12-20 wt %. 5. The process according to claim 1, wherein, in the desulfurization absorbing agent, the silica source is selected from the group consisting of silica or a natural mineral having a silica content of more than 45 wt %. 6. The process according to claim 1, wherein, in the desulfurization absorbing agent, the Si—Al molecular sieve having a BEA structure is a Beta-molecular sieve. 7. A process for producing a desulfurization adsorbing agent for hydrocarbon oil, comprising: (1) contacting at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina with a silica source, a Si—Al molecular sieve having a BEA structure and zinc oxide, to obtain a carrier;(2) contacting the carrier with a promoter metal-containing compound, to obtain a precursor of the adsorbing agent; and(3) under a condition sufficient to present at least 10 wt % of the promoter metal in a reduced valence state, treating the precursor of the adsorbing agent, to obtain the desulfurization adsorbing agent for hydrocarbon oil,wherein the step (1) further comprises: (1a′) mixing at least a part of the silica source and the binder or a binder precursor with an acid to form a slurry, and (1b′) mixing the slurry, the rest part of the silica source, the Si—Al molecular sieve having a BEA structure and zinc oxide to form a mixture and subject the mixture to molding, drying, and calcination to obtain the carrier, wherein the desulfurization adsorbing agent comprises:1) a Si—Al molecular sieve having a BEA structure:2) at least one binder selected from the group consisting of titanium dioxide, stannic oxide, zirconium oxide and alumina;3) a silica source;4) zinc oxide; and5) at least one promoter metal selected from the group consisting of cobalt, nickel, iron and manganese, based on the metal, wherein at least 10 wt % of the promoter metal is present in a reduced valence state, andwherein the Si—Al molecular sieve is in an amount of 2-15 wt %, the binder is in an amount of 5-25 wt %, the silica source is in an amount of 10-30 wt %, zinc oxide is in an amount of 25-70 wt %, and the promoter metal is in an amount of 8-25 wt %, all based on a total weight of the desulfurization absorbing agent. 8. The process according to claim 7, wherein the binder precursor is at least one selected from the group consisting of halides, alkoxylates, carboxylic acid salts, hydrated oxides, hydroxides, hydrated hydroxides and oxyhalides, of titanium, tin, zirconium, and aluminum. 9. The process according to claim 7, wherein the acid is at least one selected from the group consisting of a water soluble inorganic acid and a water soluble organic acid, and the amount of the acid to be used is such that the pH value of the slurry reaches 0.5-6. 10. The process according to claim 7, wherein, in the desulfurization absorbing agent, the Si—Al molecular sieve having a BEA structure is in an amount of 2-10 wt %, the binder is in an amount of 8-15 wt %, the silica source is in an amount of 12-25 wt %, the zinc oxide is in an amount of 40-60 wt %, the promoter metal is in an amount of 12-20 wt %. 11. The process according to claim 7, wherein, in the desulfurization absorbing agent, the silica source is selected from the group consisting of silica or a natural mineral having a silica content of more than 45 wt %. 12. The process according to claim 7, wherein, in the desulfurization absorbing agent, the Si—Al molecular sieve having a BEA structure is a Beta-molecular sieve.