CN111085206A

CN111085206A - Regular carrier catalyst with desulfurization effect and preparation and application thereof

Info

Publication number: CN111085206A
Application number: CN201811238869.4A
Authority: CN
Inventors: 王鹏; 孙言; 严加松; 宋海涛; 姜秋桥; 田辉平; 林伟; 龙军
Original assignee: Sinopec Research Institute of Petroleum Processing; China Petroleum and Chemical Corp
Current assignee: Sinopec Research Institute of Petroleum Processing; China Petroleum and Chemical Corp
Priority date: 2018-10-23
Filing date: 2018-10-23
Publication date: 2020-05-01

Abstract

A regular carrier catalyst with desulfurization function and preparation and application thereof are provided, wherein the regular carrier catalyst comprises a regular carrier and an active coating attached to the surface of the regular carrier, the active coating comprises a heat-resistant inorganic oxide matrix and a modified metal film, the modified metal film comprises modified metal, and the modified metal is one or more of Fe, Co, Ni, Mn, Ti, Zr, V, Ge, Pb, Sn, Sb and Bi. The preparation method comprises the following steps: forming a mixture of metal powder, a hydroxyl-containing solvent and a surfactant, and then treating under ultrasonic waves to obtain an ultrasonic mixed solution; separating the mixed solution after ultrasonic treatment to obtain a suspension; and (3) contacting the suspension with the matrix particles, freezing and drying to obtain the matrix particles containing the modified metal membrane, and then coating the matrix particles containing the modified metal membrane on a regular carrier to obtain the regular carrier catalyst. The catalyst has high desulfurization activity, good stability and high product yield, is used for gasoline desulfurization, and has small octane value loss.

Description

Regular carrier catalyst with desulfurization effect and preparation and application thereof

Technical Field

The invention relates to a modified molecular sieve for hydrodesulphurization and a preparation method and an application method thereof.

Background

Sulfur in the fuel is combusted to generate sulfur oxide, the sulfur oxide can inhibit the activity of a noble metal catalyst in an automobile exhaust converter and can irreversibly poison the noble metal catalyst, the effect of catalyzing and converting toxic gases in the automobile exhaust cannot be realized, so that the discharged automobile exhaust contains unburned oxides of non-methane hydrocarbon and nitrogen and carbon monoxide, the toxic gases are catalyzed by sunlight to easily form photochemical smog to cause acid rain, and the sulfur oxide is also one of main reasons for forming the acid rain.

Reducing the sulfur content in fuels such as gasoline and diesel is considered to be one of the most important measures to improve air quality. With the increasing attention of people on environmental protection, environmental regulations are becoming stricter, and the sulfur content of the European V gasoline standard implemented in 2010 of the European Union is less than 10 mug/g by taking gasoline as an example. The current gasoline product standard GB 17930-2013 'automotive gasoline' in China requires that the sulfur content in gasoline must be reduced to 10 mu g/g. But also the future gasoline quality standards will be more stringent.

Currently, the main methods for desulfurizing hydrocarbon fuels are hydrodesulfurization and adsorption desulfurization. Hydrodesulfurization reacts sulfur-containing hydrocarbons, such as gasoline, in contact with hydrogen in the presence of a hydrogenation catalyst, which, with increasing fuel oil standards, requires more severe hydrogenation conditions, such as higher reaction pressure or temperature, to lower the sulfur content, but due to the high amount of olefins in the gasoline, increasing the hydrogenation severity results in higher octane number loss. The adsorption desulfurization is usually carried out by contacting an adsorbent with sulfur-containing hydrocarbon under the hydrogen condition, wherein the sulfur-containing hydrocarbon in the oil product is captured on the adsorbent, and hydrogen sulfide is generated by hydrogenation and then is combined with zinc oxide to generate a zinc sulfide compound, which can also cause the octane number of the gasoline product to be reduced; in addition, when the sulfur combined on the zinc oxide is saturated, the desulfurization activity is reduced, the sulfur must be removed through oxidation regeneration, and in the frequent oxidation regeneration-reduction process, the deactivation rate of the adsorbent is high, which affects the implementation effect of sulfur-containing hydrocarbon desulfurization.

The existing adsorption desulfurization and hydrodesulfurization are all desulfurized in the presence of hydrogen, and in order to achieve the purpose of deep desulfurization, the operation needs to be carried out under more severe conditions.

Disclosure of Invention

The technical problem to be solved by the invention is to provide a regular carrier catalyst for hydrodesulphurization, which has higher desulphurization activity and stability. The invention aims to solve the other technical problem of providing a preparation and application method of the catalyst.

Therefore, the invention provides the following technical scheme:

technical scheme 1. a structured carrier catalyst with desulfurization function, wherein the structured carrier catalyst comprises a structured carrier and an active coating (also called an active component coating) attached to the surface of the structured carrier, the active coating comprises a heat-resistant inorganic oxide matrix and a modified metal film, the modified metal film comprises modified metal, and the modified metal is one or more of Fe, Co, Ni, Mn, Ti, Zr, V, Ge, Pb, Sn, Sb and Bi.

Technical scheme 2. the structured carrier catalyst according to the technical scheme 1, wherein the modified metal film is positioned on the outer surface of the matrix particles, and the thickness of the modified metal film is 5-30 nm, preferably 5-20 nm.

Technical solution 3. the structured carrier catalyst according to the technical solution 1 or 2, wherein the active coating layer is contained in an amount of 5 to 50 wt%, for example, 10 to 30 wt%, or 15 to 25 wt%, or 20 to 30 wt%, and the structured carrier is contained in an amount of 50 to 95%, for example, 70 to 90 wt%, or 75 to 85 wt%, or 70 to 80 wt%, based on the total weight of the structured carrier, on a dry basis.

The technical scheme 4. the structured carrier catalyst according to any one of the technical schemes 1 to 3, wherein the active component coating contains 8 to 25 weight percent of modified metal film and 75 to 92 weight percent of matrix in terms of dry basis based on the total weight of the active component coating; preferably, the modified metal film comprises 10-20 wt% of modified metal film and 80-90 wt% of matrix;

a refractory inorganic oxide matrix, such as one or more of an alumina matrix, a silica matrix, a zirconia matrix, a titania matrix, and a silica-alumina matrix, such as kaolin and/or silica-alumina gel; the preferred refractory inorganic oxide matrix is alumina.

Technical solution 5. the structured carrier catalyst according to any one of technical solutions 1 to 4, wherein the structured carrier is an integral carrier (honeycomb carrier) having a parallel pore structure with openings at both ends; preferably, the pore density of the cross section of the structured carrier is 40 to 800 pores per square inch, for example 100 to 400 pores per square inch, and typically, the cross sectional area of each pore in the structured carrier is 400 μm²～1.8×10⁵μm². The regular structure carrier can be at least one of a cordierite honeycomb carrier, a mullite honeycomb carrier, a diamond honeycomb carrier, a corundum honeycomb carrier, a zirconia corundum honeycomb carrier, a quartz honeycomb carrier, a nepheline honeycomb carrier, a feldspar honeycomb carrier, an alumina honeycomb carrier or a metal alloy honeycomb carrier.

The structured carrier catalyst according to any of the claims 1 to 5, wherein the modified metal comprises one or more first metals selected from Fe, Co, Ni, Mn, Ti, Zr, Pb, Ge, Sn and optionally one or more second metals selected from V, Sb, Bi, preferably the weight ratio of the second metal to the first metal is 0 to 1:1 or 0 to 0.8:1 or 0 to 0.5:1 or 0 to 0.3: 1; in a first embodiment, the first metal is one or more of Fe, Co, Ni and Mn, optionally contains one or more of Ti, Zr, Pb, Ge and Sn, and the ratio of one or more of Fe, Co, Ni and Mn to one or more of Pb, Ge and Sn is 0.5-2: 0-1; in a second embodiment, the modified metal comprises a first metal and optionally a second metal, wherein the first metal is one or more of Pb, Ge and Sn, and the second metal is one or more of Sb and Bi, preferably, the weight ratio of the second metal to the first metal is 0.2-1: 1, such as 0.4-0.8: 1; in a third embodiment, the first metal is Ti and/or Zr and the optional second metal is preferably V, preferably Ti: Zr: the weight ratio of V is (0.8-1.2): 0.4-0.6); in a fourth embodiment, the modified metal film comprises a third element selected from one or more of Cr, Mo, W, Cu, Ag, Au, Al, Ga, Mg, B; preferably, the weight ratio of the second metal to the first metal is 0-1: 1 or 0-0.5: 1 or 0 to 0.3:1, preferably, the weight ratio of the third element to the first metal is 0-1: 1 or 0-0.5: 1 or 0 to 0.3: 1; in the fourth embodiment, it is preferable that the active coating layer of the structured carrier catalyst contains 5 to 20 wt% of the first metal, such as 8 to 17 wt% or 10 to 15 wt%, 0 to 10 wt% of the second metal, such as 0 to 5 or 0 to 3 wt%, and 0 to 10 wt% of the third element, such as 0 to 5 or 0 to 3 wt%, based on the weight of the active coating layer.

Technical scheme 7. a method for preparing a regular carrier catalyst comprises the following steps: forming a mixture of metal powder, a hydroxyl-containing solvent and a surfactant, and then treating under ultrasonic waves to obtain an ultrasonic mixed solution; separating the mixed solution after ultrasonic treatment to obtain a suspension; contacting the suspension with matrix particles, freeze-drying to obtain matrix particles containing modified metal membranes, and coating the matrix particles containing modified metal membranes on a structured carrier to obtain the structured carrier catalyst, wherein preferably the matrix particlesParticle diameter d₉₀Not more than 10 microns, for example 1 to 8 microns or 2 to 5 microns.

Technical scheme 8. the preparation method of the structured carrier catalyst according to the technical scheme 7, wherein the concentration of the modified metal in the suspension is 5-45 g/Kg, for example, 8-40 g/Kg or 10-35 mass per thousand, preferably 10-25 g/Kg.

Technical solution 9. the method for preparing a modified structured carrier catalyst according to technical solution 7 or 8, wherein the particle size D of the particles in the suspension is₉₀Is 20nm or less, for example, 3 to 20nm or 4 to 10nm or 4 to 8nm, preferably 10nm or less, more preferably 5nm or less.

Technical scheme 10. the preparation method of the structured carrier catalyst according to any one of technical schemes 7 to 9, wherein the weight ratio of the hydroxyl-containing solvent to the metal powder is 2-15: 1, the weight ratio of the hydroxyl-containing solvent to the metal powder is preferably 5-10: 1.

technical scheme 11. the preparation method of the structured carrier catalyst according to any one of technical schemes 7 to 10, wherein the ratio of the surfactant to the hydroxyl-containing solvent is 0.001 to 100mg/mL, preferably 0.002 to 10mg/mL, or 0.05 to 5mg/mL, or 0.01 to 2mg/mL, or 0.02 to 2.5mg of the surfactant per mL of the hydroxyl-containing solvent, or 0.2 to 1.5 mg/mL.

Technical solution 12. the preparation method of the structured carrier catalyst according to any one of the technical solutions 7 to 11, wherein the ultrasonic wave is processed under the ultrasonic wave, and the power of the ultrasonic wave is 10 to 500W, such as 30 to 450W, 60 to 300W, or 160 to 400W, relative to 100ml of the solvent, and the frequency of the ultrasonic wave is 20 to 100KHz, such as 20 to 50 KHz; the ultrasonic treatment time is 3 to 15 hours, for example, 4 to 12 hours or 5 to 8 hours.

Technical scheme 13. the preparation method of the structured carrier catalyst according to any one of the technical schemes 7 to 12, wherein the average diameter of the metal powder is less than 20 μm, for example, 1 to 18 micrometers, or 2 to 17 micrometers, or 4 to 16 micrometers.

Technical scheme 14. the preparation method of the structured carrier catalyst according to any one of the technical schemes 7 to 13, wherein the metal powder can be one or more of pure metal powder or metal alloy powder; in the metal powder, the weight ratio of the third element to the modified metal is 0-1: 1, such as 0-0.8: 1 or 0-0.5: 1 or 0.05-0.5: 1 or 0.1-0.3: 1; the metal powder is metal alloy powder, pure metal powder or a mixture of a plurality of the metal alloy powder and the pure metal powder; the pure metal powder is one or more of Fe powder, Co powder, Ni powder, Mn powder, Ti powder, Zr powder, V powder, Sn powder, Sb powder and Bi powder; the alloy powder is an alloy formed by a plurality of Fe, Co, Ni, Mn, Ti, Zr, V, Sn, Sb and Bi, or an alloy formed by one or more of Fe, Co, Ni, Mn, Ti, Zr, V, Sn, Sb and Bi and one or more of third elements, such as iron-cobalt alloy powder, iron-nickel alloy powder, iron-manganese alloy powder, cobalt-nickel alloy powder, cobalt-manganese alloy powder, nickel-manganese alloy powder, iron-chromium alloy powder, iron-molybdenum alloy powder, iron-tungsten alloy powder, iron-vanadium alloy powder, iron-copper alloy powder, iron-silver alloy powder, iron-gold alloy powder, iron-tin alloy powder, iron-antimony alloy powder, iron-bismuth alloy powder, iron-magnesium alloy powder, nickel-tungsten alloy powder, nickel-aluminum alloy powder, cobalt-molybdenum alloy powder, cobalt-titanium alloy powder, cobalt-gallium alloy powder, tin-antimony alloy powder, cobalt-molybdenum alloy powder, cobalt-titanium alloy powder, tin-antimony alloy powder, nickel-, One or more of tin-bismuth alloy powder, antimony-bismuth alloy powder, tin-antimony-bismuth alloy powder and titanium-zirconium-vanadium alloy powder; preferably, the content of the first metal in the alloy powder is higher than the content of the second metal. In the alloy powder, the ratio of the second metal: a third element: the weight ratio of the first metal is 0-1: 1, for example, 0-0.8: 1 or 0-0.5: 1, preferably 0-0.3: 1.

Technical scheme 15. the preparation method of the structured carrier catalyst according to any one of the technical schemes 7 to 14, wherein the surfactant is an anionic surfactant, a cationic surfactant or an amphoteric surfactant; for example, one of sodium glycocholate, sodium dioctyl sulfosuccinate, sodium dodecyl benzene sulfonate, sodium dodecyl sulfate, sodium lauryl sulfate, stearic acid, oleic acid, lauric acid, fatty acid amine, cetyl trimethyl ammonium bromide, sodium dodecyl sulfate, cetyl trimethyl ammonium bromide, fatty acid methyl ester, and polyoxyethylene ether; the fatty acid amine carbon chain length is preferably between C8-C10 (carbon chain is C8, C9 or C10); the fatty acid methyl ester carbon chain length is preferably between C8-C10.

Technical solution 16. the method for preparing a structured carrier catalyst according to any one of technical solutions 7 to 15, wherein the hydroxyl group-containing solvent is water and/or a hydroxyl group-containing organic solvent, for example, an organic solvent having one or more hydroxyl groups in a molecule, the hydroxyl group-containing organic solvent is, for example, a monohydric alcohol, a dihydric alcohol, a trihydric alcohol or a derivative thereof, and usually, the number of carbon atoms in the molecule of the hydroxyl group-containing solvent is not more than 6, for example, 1,2, 3 or 4; the monohydric alcohol is one or more of methanol and ethanol, and the dihydric alcohol is, for example: ethylene glycol, said glycol derivatives such as: ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether, glycol ethers, trihydric alcohols such as glycerol, trihydric alcohol derivatives such as triethanolamine.

Technical solution 17. the preparation method of the structured carrier catalyst according to any one of the technical solutions 7 to 16, wherein the separation is performed by slow centrifugal separation, in one embodiment, the rotation speed of the slow centrifugal separation is 1200r/min to 3000r/min or 1500 to 2500r/min, and the time of the centrifugal separation can be 10 to 30 minutes, for example, 15 to 20 minutes; the container used for centrifugal separation may be cylindrical or prismatic, and the ratio of the diameter to the height thereof is, for example, 0.1 to 1:1 or 0.25 to 1: 1.

technical scheme 18. the preparation method of the structured carrier catalyst according to any one of technical schemes 7 to 17, wherein the freeze drying method is sublimation drying at low temperature and under high vacuum, the drying temperature is lower than the freezing point temperature of the hydroxyl-containing solvent, the drying time has no special requirement, as long as the hydroxyl-containing solvent can volatilize, and the particles containing the hydroxyl-containing solvent are dried; for example, the freeze-drying time can be 24-48 h. Generally, a mixture formed by the molecular sieve and the suspension is cooled and solidified, and then the mixture is freeze-dried under the freezing point temperature (or the freezing point temperature) of the solvent and the vacuum condition, preferably, the freeze-drying temperature is-30 to 5 ℃, and the pressure (absolute pressure) is not more than 0.05MPa, such as 50000Pa to 1Pa or 2 to 20000Pa, preferably 5 to 1000Pa, such as 5 to 100Pa or 10 to 50Pa or 15 to 60 Pa.

Technical scheme 19. the preparation method of the structured carrier catalyst according to any one of the technical schemes 7 to 18, wherein the thickness of the active coating of the structured carrier catalyst is, for example, 0.5 to 500 micrometers, such as 1 to 400 micrometers, or 5 to 300 micrometers, or 8 to 200 micrometers, or 10 to 100 micrometers.

Technical solution 20. the method for preparing a structured carrier catalyst according to any one of technical solutions 7 to 19, wherein,

the structured carrier catalyst comprises 10-50 wt%, preferably 10-30 wt%, or 15-25 wt%, or 20-30 wt%, or 15-30 wt%, of an active coating layer and 50-90 wt%, preferably 70-90 wt%, or 75-85 wt%, or 70-80 wt%, or 70-85 wt%, of a structured carrier, based on the total weight of the structured carrier catalyst, calculated on a dry basis;

the active coating comprises a substrate and a modified metal film, the metal film comprises a modified metal and a third element, and the content of the substrate is 75-92 wt% and the total content of the modified metal and the third element is 8-25 wt% on a dry basis based on the total weight of the active coating; preferably, the matrix is contained in an amount of 80 to 90 wt%, for example, 83 to 92 wt%, and the total content of the modified metal and the third element is 10 to 20 wt%, for example, 8 to 17 wt%.

Technical scheme 21. the method for preparing a structured carrier catalyst according to any one of technical schemes 7 to 20, wherein the step of coating the structured carrier with the matrix particles containing the modified metal film comprises the steps of coating the structured carrier with the matrix slurry containing the modified metal film, drying and roasting, wherein the drying temperature is between room temperature and 150 ℃, for example, 80 to 120 ℃, and the drying time can be more than 1 hour, for example, 2 to 8 hours; the roasting temperature is 200-600 ℃, for example 200-450 ℃, and the roasting time is more than 1h, for example 2-4 h.

The method for preparing a structured carrier catalyst according to any one of claims 7 to 21, wherein the matrix particles are one or more of alumina particles, silica-alumina particles, zirconia particles, titania particles, or particles selected from one or more of alumina, silica and alumina, zirconia and titania, preferably the matrix is alumina, such as one or more of γ -alumina, β -alumina, α -alumina, η -alumina, and κ -alumina, the alumina matrix particles are commercially available or obtained by molding or grinding a material that can be converted into alumina under calcination conditions, such as hydrated alumina and/or alumina sol, the hydrated alumina is one or more of boehmite, pseudo-boehmite, alumina trihydrate and amorphous aluminum hydroxide, the silica-alumina source is one or more of clay, silica gel, bentonite, montmorillonite, bentonite, montmorillonite, or montmorillonite.

The technical scheme 23 is a sulfur-containing hydrocarbon desulfurization method, which comprises the step of carrying out contact reaction on a hydrocarbon material containing a sulfur compound, a hydrogen donor and the structured carrier catalyst according to any one of the technical schemes 1 to 6, wherein the reaction temperature is 150 to 350 ℃, the reaction pressure is 0.5 to 5MPa, and the sulfur-containing hydrocarbon feeding weight hourly space velocity is 0.1 to 100h^-1The volume ratio of the hydrogen donor to the sulfur-containing hydrocarbon is 0.01 to 1000. Preferably, the reaction temperature is 200-300 ℃, the reaction pressure is 1-3.5 MPa, and the weight hourly space velocity of the sulfur-containing hydrocarbon feeding material is 1-10 h^-1The volume ratio of the hydrogen donor to the sulfur-containing hydrocarbon is 0.05 to 500.

Technical solution 24 the desulfurization method according to the technical solution 23, wherein the hydrogen donor may be one or more of hydrogen gas, hydrogen-containing gas, and hydrogen donor; the hydrogen gas can be supplied using a hydrogen-containing gas raw material of various purities, and the hydrogen gas content in the hydrogen-containing gas raw material is usually 30 vol% or more; hydrogen-containing gas such as one or more of catalytic cracking (FCC) dry gas, coking dry gas and thermal cracking dry gas, wherein the hydrogen donor is at least one of tetrahydronaphthalene, decahydronaphthalene and indane; the hydrocarbon material is selected from one or more of natural gas, dry gas, liquefied gas, gasoline, kerosene, diesel oil and gas oil, and is preferably gasoline and/or diesel oil; the above gasoline, kerosene, diesel oil and gas oil fractions are full fractions thereof and/or partially narrow fractions thereof.

Technical scheme 25. according to the desulfurization method of the technical scheme 23 or 24, the sulfur content of the hydrocarbon material containing sulfur compounds is 10-1000 mg/Kg, for example, the sulfur-containing compound material is catalytically cracked gasoline or catalytically cracked diesel oil. Typically, the catalytically cracked gasoline has an olefin content of 15 to 50 wt.%.

The structured carrier catalyst provided by the invention has one or more of the following advantages, at least one of the following effects can be realized, and preferably, a plurality of effects can be realized:

(1) may have a higher activity. Under the condition of the same active metal, the catalyst has higher desulfurization activity than the prior hydrodesulfurization catalyst and hydrodesulfurization adsorbent. For example, desulfurization at a lower reaction temperature and a lower hydrogen pressure can result in a higher desulfurization rate than existing desulfurization catalysts, thereby allowing the reaction temperature to be lowered.

(2) The metal is not easy to lose or gather, the stability of the desulfurization activity is better, frequent regeneration is not needed, the regeneration period can be prolonged, the long-period operation of a desulfurization device is facilitated, and the stability of the hydrodesulfurization is better than that of the conventional hydroabsorption desulfurization.

(3) The catalyst is used for hydrodesulfurizing gasoline containing olefin and has low hydrogen consumption.

(4) The catalyst is used for hydrodesulfurizing gasoline containing olefin, such as catalytically cracked gasoline, and has obviously lowered olefin content.

(5) The method is used for hydrodesulfurizing the gasoline containing olefin, and has small octane number loss compared with the existing desulfurization method.

(6) The catalyst is used for hydrodesulfurizing gasoline containing olefin, and compared with the existing desulfurizing technology, the content of aromatic hydrocarbon is not increased or is slightly lower.

(7) The catalyst is used for desulfurizing the gasoline containing olefin, so that the content of isomeric hydrocarbon in the desulfurized gasoline is obviously improved, and the normal paraffin is obviously reduced.

(8) The catalyst is used for desulfurizing the gasoline containing olefin and has higher gasoline yield.

The regular carrier catalyst provided by the invention can be obtained by the preparation method of the regular carrier catalyst provided by the invention.

The desulfurization method provided by the invention can have higher desulfurization rate and higher yield of desulfurization products under the same reaction temperature, can be operated for a long period and has small octane number loss of gasoline.

Detailed Description

In the present invention, the term "regular carrier catalyst" is used to refer to a catalyst comprising a regular structure carrier and an active component coating layer distributed on the inner surface and/or the outer surface of the carrier, also called regular structure catalyst; "regular structure carrier" is also called regular carrier, is a carrier with regular structure; the regular structure reactor is a fixed bed reactor filled with a regular structure catalyst as a catalyst bed layer.

The dry basis weight (dry weight for short) is the weight of the solid product obtained after the material has been calcined at 800 ℃ for one hour.

The sulfur-containing hydrocarbon feed weight hourly space velocity refers to the weight of sulfur-containing hydrocarbon feed per hour of the reactor relative to the weight of the active coating of the structured supported catalyst. The volume ratio of the hydrogen donor to the sulfur-containing hydrocarbon (abbreviated as hydrogen-oil ratio) is the ratio of the volume of the hydrogen donor introduced into the reactor in a standard state to the volume of the hydrocarbon feed at 20 ℃ under one standard atmosphere.

The regular carrier catalyst with the desulfurization function comprises a regular carrier and an active coating, wherein the active coating comprises a matrix and a modified metal film (metal film for short), and the metal film is positioned on the outer surface of matrix particles. The metal film is attached to the outer surface of the matrix particle, and may cover part or all of the outer surface of the matrix particle, for example, the metal film may be a whole block or may be dispersed into multiple blocks on the outer surface of the matrix, and the blocks are continuous or spaced. The thickness of the metal film on the substrate particles is 5-30 nm, preferably 5-20 nm. The metal film may be measured by transmission electron microscopy. Preferably, the structured carrier catalyst comprises 65-85 wt% of structured carrier and 15-35 wt% of active coating or comprises 70-85 wt% of structured carrier, preferably 70-80 wt% of active coating, and 15-30 wt% of active coating, preferably 20-30 wt%. Preferably, the active coating comprises 8-25 wt% of the modified metal and 75-92 wt% of the substrate, for example 10-20 wt% of the modified metal and 80-90 wt% of the substrate.

The regular carrier catalyst (also called regular structure catalyst) with the desulfurization function comprises a regular carrier (regular structure carrier), and can be used for providing a catalyst bed layer in a fixed bed reactor. The regular structure carrier can be a whole carrier block, a hollow pore channel structure is formed inside the regular structure carrier, a catalyst coating can be distributed on the inner wall of a pore channel, and the pore channel space can be used as a flowing space of fluid. Preferably, the regular structure carrier is selected from monolithic carriers having a parallel channel structure with two open ends, for example, the regular structure carrier may be a honeycomb type regular carrier (referred to as a honeycomb carrier) with a honeycomb-shaped opening in the cross section. The structured carrier can be at least one of cordierite honeycomb carrier, mullite honeycomb carrier, diamond honeycomb carrier, corundum honeycomb carrier, zirconia corundum honeycomb carrier, quartz honeycomb carrier, nepheline honeycomb carrier, feldspar honeycomb carrier, alumina honeycomb carrier and metal alloy honeycomb carrier.

According to the regular carrier catalyst provided by the invention, preferably, the regular carrier is a honeycomb carrier, and the pore density of the cross section of the honeycomb carrier is 40-800 pores per square inch, preferably 100-400 pores per square inch; the cross-sectional area of each hole in the honeycomb structured carrier is preferably 400-1.8 multiplied by 10⁵μm²More preferably 1500 to 22500 μm²The aperture ratio of the carrier surface of the honeycomb structured carrier is 20-80%, preferably 50-80%. The shape of the hole can be one of a square, a wing square (namely, the wing with inward vertical edges is arranged at the center of four sides in the square hole, and the length of the wing is 1/5-2/5 of the side length of the square), a regular triangle, a regular hexagon, a circle and a ripple shape.

The preparation method of the regular carrier catalyst provided by the invention comprises the step of preparing the suspension. The suspension preparation method comprises the following steps: forming a mixture of metal powder, a hydroxyl-containing solvent and a surfactant, and treating under ultrasonic waves to obtain an ultrasonic mixed solution; wherein, in the ultrasonic treatment process, fine metal particles stripped from metal powder are suspended in a solvent (solvent for short) containing hydroxyl; separating larger particles from the mixed liquid after ultrasonic treatment to obtain a suspension, wherein the suspension is suspended with fine particles containing the modified metal. The metal powder (also referred to as metal powder) may be a pure metal powder (in the case where the metal film contains only the modifying metal and the modifying metal is one kind), an alloy powder containing the modifying metal and boron, or an alloy powder containing a plurality of modifying metals. The metal powder (the relative content of the hydroxyl-containing solvent) is not particularly required, and the hydroxyl-containing solvent can contain the modified metal element with the required content after ultrasonic treatment, so the use amount of the metal powder can be excessive (exceeding the metal content in the suspension), preferably, the weight ratio of the hydroxyl-containing solvent to the metal powder is 2-15: 1, for example, 3-12: 1 or 5-10:1, and the content of the modified metal element with the required concentration in the hydroxyl-containing solvent can be ensured by controlling the time and the power of ultrasonic treatment.

The preparation method of the regular carrier catalyst provided by the invention leads metal powder to generate metal stripping in the presence of a surfactant through ultrasonic treatment to form fine particles suspended in a hydroxyl-containing solvent. Generally, there is no special requirement for the power and frequency of the ultrasonic wave, the power of the ultrasonic wave is small, and a long treatment time is required to achieve a certain concentration of the modified metal in the hydroxyl group-containing solvent. Preferably, the power of the ultrasonic wave in the ultrasonic wave treatment is 10 to 500W, such as 30 to 450W, 160 to 400W, 40 to 200W, or 30 to 300W, relative to 100ml of the solvent, the frequency of the ultrasonic wave is 20 to 100KHz, such as 20 to 50KHz, and the time of the ultrasonic wave treatment is 3 to 15 hours, such as 5 to 8 hours. (the power of the ultrasonic waves applied to the solvent per unit volume is a specific ultrasonic power, for example, when the power applied to 100mL of solvent is 30 to 500W, the specific ultrasonic power is 0.3 to 5W/mL or 30 to 500W/100 mL).

The invention has no special requirement on the particle size of the metal powder, the particles are usually larger, and longer ultrasonic treatment time is needed to obtain a suspension with a certain metal concentration, and the average diameter of the metal powder is preferably less than 20 microns, such as 1-15 microns, or 1-18 microns, or 4-16 microns.

In the present invention, the average diameter of the metal powder, the particle size distribution of the matrix particles and D₉₀Particle size distribution of solid particles and D₉₀The measurement is carried out by a laser particle size instrument, and the measurement method can be seen in national standard GB/T19077-2016, particle size distribution laser diffraction method. (D)₉₀Also written as d₉₀D90 or D90, is the particle diameter at which the particle size distribution cumulatively reaches 90% by volume

The preparation method of the regular carrier catalyst provided by the invention is characterized in that ultrasonic treatment is carried out in the presence of a surfactant. The surfactant is introduced for the purpose of peeling off the metal, forming a stable suspension, and contributing to the formation and stabilization of the metal film and the improvement of the catalyst performance, forming a metal film having higher activity. The weight ratio of the surfactant to the hydroxyl group-containing solvent is 0.001 to 100mg/g, for example, 0.01 to 10mg/g, 0.05 to 5mg/g, 0.002 to 2mg/g, 0.005 to 1mg/g, or 0.2 to 1.5 mg/g.

According to the preparation method of the regular carrier catalyst, undissolved particles after ultrasonic treatment are separated through separation, so that a suspension is obtained. The suspension contains fine particles including the modifying metal. The separation method of the invention is preferably a centrifugal separation method, larger particles are settled at the bottom of the container through centrifugal separation, smaller particles which are not separated exist in the solvent, namely in the suspension, the suspension at the upper layer is led out from the separation container, and the settled metal particles can be recycled. In one embodiment, the separation is performed by slow centrifugal separation, the rotation speed of the slow centrifugal separation is 1200-3000 r/min, preferably 1500-2500 r/min, and the time of the centrifugal separation is 15-20 min. In one embodiment, the container for centrifugal separation is cylindrical, and the ratio of the diameter to the height of the container is 0.1-1: 1, for example, 0.1 to 0.5: 1.

preferably, the particle size D of the particles in the suspension obtained after centrifugation₉₀Is 20nm or less, preferably 10nm or less, more preferably 5nm or less, for example, 3 to 20nm, 3 to 10nm, or 3 to 5 nm.

Particle size distribution of the suspension and D₉₀Analysis can be performed using a nanoparticle analyzer, such as the Zetasizer NanoZSP nanoparticle analyzer from Malvern.

According to the preparation method of the regular carrier catalyst provided by the invention, the suspension and the matrix are uniformly mixed, and then are frozen and dried, usually, the mixture is frozen and then is dried under vacuum and freezing conditions. In one embodiment, the temperature of the mixture is lower than the solidification temperature of the solvent, so that the mixture is solidified into a solid, and then the solvent is sublimated and volatilized under the vacuum condition of the temperature lower than the solidification point or the freezing point of the solvent to obtain the matrix and/or the molecular sieve particles wrapping the modified metal film.

According to the process for preparing the structured support catalyst of the present invention, the suspension may be contacted with the matrix particles by any method suitable for contacting solids with liquids. Such as mixing, spraying, soaking.

For the convenience of freezing and drying, the hydroxyl-containing solvent (solvent for short) with a high freezing point (freezing point) is preferably selected in the invention, preferably, the temperature of the solvent is not lower than-25 ℃, more preferably, the freeze drying is carried out at the temperature of-20-5 ℃, and therefore, the solvent with the freezing point temperature of-20-5 ℃ is preferably used. Preferably, the drying is carried out under vacuum at a pressure of 10 to 10000Pa (absolute), for example 5 to 1000Pa, 10 to 100Pa, 10 to 50Pa, or 15 to 35 Pa.

The hydroxyl-containing solvent is preferably one or more of water, ethylene glycol, glycerol and methanol. In one embodiment, the mixture comprises water and a hydroxyl group-containing organic solvent at a weight ratio of water to hydroxyl group-containing organic solvent of 0.2 to 4:1, such as 0.4 to 3.6:1 or 0.3 to 2:1 or 0.025 to 0.4:1 or 0.03 to 0.3: 1.

the preparation method of the regular carrier catalyst provided by the invention comprises the following steps: uniformly mixing metal powder and a hydroxyl-containing solvent, then carrying out ultrasonic treatment for 5-8 h at the specific ultrasonic power of 50-250W/(100 g of hydroxyl-containing solvent) and preferably 100-150W/(100 g of hydroxyl-containing solvent), then carrying out centrifugal separation on the mixed liquid after ultrasonic treatment at the rotation speed of 1200-3000 r/min and preferably 1500-2500 r/min, and obtaining a suspension after separation; then mixing the substrate and/or the molecular sieve and/or the particles containing the substrate and the molecular sieve with the suspension, after uniform dispersion, freeze-drying, and coating the regular carrier to obtain the regular carrier catalyst. The average particle size of the metal powder is less than 20 micrometers, preferably 1-15 micrometers or 3-18 micrometers; the metal powder: a hydroxyl group-containing solvent in a weight ratio of 1:2 to 15, preferably 1:5 to 10; the surfactant: 1mL of a solvent (0.001-100 mg). The metal powder is one or more of metal simple substance powder and alloy powder, the freeze drying temperature is preferably-20-5 ℃, the freeze drying is carried out in vacuum, and the freeze drying pressure is 5-1000 Pa. The freeze-drying time is, for example, 24 to 48 hours.

The first embodiment of the preparation method of the regular carrier catalyst provided by the invention comprises the following steps:

s1, mixing the particle diameter D₉₀Mixing the substrate particles with the particle size of 1-10 microns, such as 2-8 microns, preferably 2-5 microns, with the suspension, and freeze-drying to obtain a substrate containing the modified metal film;

s2, preparing a slurry (called coating slurry) from the matrix containing the modified metal film, coating the slurry on a regular structure carrier (also called a regular carrier), drying and roasting.

According to the preparation method of the regular carrier catalyst, the coating is carried out, so that the content of the active coating in the product obtained by coating is 10-50 wt%, preferably 15-30 wt%, and more preferably 20-30 wt% on a dry basis. The coating is carried out one or more times, preferably, each time after coating, drying and optionally roasting, and the roasting is carried out after the last coating, so that the content of the active coating in the obtained product meets the requirement.

According to the process for the preparation of the structured carrier catalysts of the present invention, the matrix particles can be purchased commercially or manufactured in house. The matrix particles are preferably alumina particles; a method for preparing alumina particles includes the following steps:

pulping, spray drying, forming and roasting an alumina source, wherein the alumina source is preferably hydrated alumina and/or alumina sol; the hydrated alumina is at least one of boehmite (also called boehmite, boehmite), pseudoboehmite (also called pseudoboehmite), alumina trihydrate and amorphous aluminum hydroxide. Preferably, the method further comprises a step of pretreating the alumina source, wherein the step of pretreating the alumina source comprises the steps of adding water to the alumina source, mixing and pulping, adding an acid solution to the obtained slurry to make the slurry in a gel state, and then aging the slurry in the gel state. Pretreating an alumina source, preferably selecting the added acid solution from one or more of hydrochloric acid, dilute nitric acid, oxalic acid, acetic acid and dilute sulfuric acid, wherein the concentration of the acid solution is preferably 15-37 wt%; in the step of adding the acid solution to the obtained slurry, the pH value of the slurry after the acid is added is preferably 1-5, preferably 2-4, and the control of the pH value of the slurry is beneficial to simply and conveniently mastering the gel state of the slurry. Preferably, in the step of aging the slurry in the gel state, the temperature of the aging treatment is 50-80 ℃ and the time is 0.5-2 h. The roasting temperature is 400-800 ℃, for example 500-700 ℃; the roasting time is at least 0.5 hour, for example, 1 to 10 hours.

According to the preparation method of the regular supported catalyst, the first embodiment has no special requirement on the solid content of the prepared coating slurry, however, the difficulty of coating the slurry can be increased due to the fact that the solid content of the slurry is too high, and the adhesion amount of each coating can be reduced due to the fact that the solid content of the slurry is too low, so that the coating times are increased. Preferably, the solid content of the coating slurry is 10 to 45 wt%, preferably 20 to 40 wt%.

According to a first embodiment of the process for preparing a structured carrier catalyst of the present invention, the coating slurry may be distributed on the inner and/or outer surface of the structured carrier by various coating methods. The coating method may be a water coating method, a dipping method or a spraying method. The specific operation of coating can be carried out with reference to the method described in CN 1199733C. Preferably, the coating is carried out by a water coating method, namely, a carrier is coated by a dispersion liquid obtained by beating the coating material and water, one end of the carrier is immersed in the slurry liquid in the coating process, and the other end of the carrier is vacuumized so that the slurry liquid continuously passes through the pore channels of the carrier. The volume of the slurry passing through the carrier pore channel is 2-20 times of the volume of the carrier, the applied vacuum pressure is-0.1 MPa to-0.01 MPa, the coating temperature is 10-70 ℃, and the coating time is 0.1-100 seconds.

The method and conditions for drying and calcining the structured carrier coated with the coating slurry according to the first embodiment of the method for preparing a structured carrier catalyst of the present invention are well known to those skilled in the art. For example, the drying method may be air drying, oven drying, forced air drying; the method of calcination may also be a method known in the art. Preferably, the drying temperature is between room temperature and 150 ℃, preferably between 80 and 120 ℃, and the drying time is more than 1 hour, preferably between 2 and 8 hours; the roasting temperature is 200-600 ℃, preferably 200-350 ℃ or 250-450 ℃, and the roasting time is more than 1 hour, preferably 2-4 hours.

The desulfurization method provided by the invention can be carried out at a lower reaction temperature and has a better desulfurization effect. For example, in one embodiment, the reaction temperature is 250-300 ℃, the reaction pressure is 1-3.5 MPa, the hydrogen partial pressure is preferably 0.5-2 MPa, and the weight hourly space velocity of the sulfur-containing hydrocarbon feed is 1-10 h^-1The volume ratio of the hydrogen donor to the sulfur-containing hydrocarbon is 0.05 to 500.

In the present invention, all pressures are expressed in absolute pressure unless otherwise specified.

The method for desulfurizing the sulfur-containing hydrocarbon can regenerate the sulfur-containing hydrocarbon at intervals after the desulfurization effect of the sulfur-containing hydrocarbon does not meet the requirement; and the active metal is not easy to gather without repeated oxidation regeneration-reduction, which is beneficial to improving the desulfurization activity of the catalyst and the stability of the desulfurization process of the sulfur-containing hydrocarbon. The regeneration method can refer to the existing method, for example, an oxidation method can be adopted, the invention has no special requirement, and the invention is not described again.

In the following examples and comparative examples,

XRD analysis was carried out by measuring cell constants and relative crystallinity by means of XRD analysis on a Japanese D/Max-IIIA X-ray diffractometer (Cu-K α target) by the RIPP146-90 method (see "analytical methods in Petroleum and chemical industries (RIPP laboratory methods), eds of Yankee and the like, published by scientific publishers, 1990).

The regular carrier and the metal content in the regular carrier catalyst are calculated according to the charge ratio.

Analysis of the thickness of the metal film: the transmission electron microscope method is adopted, and the specific analysis method is as follows: randomly selecting 30 particles from a sample, measuring the thickness of the metal film at any position of each particle, and then taking the average value of all the thicknesses to obtain the thickness of the metal film of the sample;

the product composition is calculated according to the feed ratio.

Laser particle size analysis: a Malvern Mastersizer 2000 laser particle size analyzer is adopted;

and (3) nano-particle size analysis: zetasizer NanoZSP Analyzer from Malvern;

motor Octane Number (MON) and Research Octane Number (RON) of gasoline: measured by GB/T503-1995 and GB/T5487-1995;

and (3) measuring the sulfur content: measuring by an off-line chromatographic analysis method, and measuring by adopting a GC6890-SCD instrument of the agilent company;

a centrifugal separator: model DT5-4B, Beijing times Beili centrifuge, Inc., container diameter and height ratio 1: 1;

an ultrasonic cleaner: model KQ-400DB, frequency 40 KHZ;

solvents, surfactants, not specified, used in the examples were purchased from national pharmaceutical group chemical agents, ltd, grades: and AR.

In the following examples and comparative examples, the method for coating the substrate slurry on the regular structure carrier is a water coating method, and the specific process method comprises the following steps: in each coating process, one end of the regular structure carrier is immersed in the matrix coating slurry, and the other end of the regular structure carrier is vacuumized to enable the slurry to continuously pass through the pore channel of the carrier; wherein the volume of the slurry passing through the carrier pore channel is 2.5 times of the volume of the carrier, the applied vacuum pressure is-0.03 MPa (the vacuum degree is 0.03MPa), the coating temperature is 35 ℃, and the coating time is 60-300 seconds.

The used structured vector, noted ZT 1: is a cellular cordierite regular carrier, produced by Jiangsu Yixing non-metal chemical mechanical plant Limited company and has the size of

The open porosity was 70%, the cell density of the cross section was 200 cells/square inch, and the cross sectional area of the cells was 5625 μm²And cutting the required size for coating when in use.

Preparation of alumina matrix particles:

3.1kg of pseudoboehmite (produced by Shandong aluminum Co., Ltd., solid content 65% by weight, alumina 2kg, particle diameter d)₉₀35nm, same below) was mixed with 7kg of deionized water (pH 7, same below) and slurried uniformly, 1000mL of hydrochloric acid having a concentration of 18% by weight was added, the pH of the slurry was adjusted to 1.8 to make the slurry in a gel state, aged at 60 ℃ for 1h to obtain a pretreated pseudoboehmite, spray-dried, and calcined at 450 ℃ for 2 hours to obtain alumina matrix particles having an average particle size of 60 μm, which was designated JZ 1.

Example 1

(1) Preparation of a substrate containing a metal film:

firstly, 10g of nickel powder (average particle size of the nickel powder is 10 microns, source: national drug group) and 100ml of ethylene glycol (national drug group, purity AR) are added into a 200ml wide-mouth bottle, mixed uniformly, and then 60mg of surfactant sodium glycocholate (purity AR, source: Nanjing Paels Biotech limited) is added; then, the reaction vessel (jar) was placed in an ultrasonic cleaner and sonicated at 160W power for 6h (frequency 40 KHz); centrifuging the liquid after ultrasonic treatment in a centrifugal separator at 1500r/min for 20min, taking out supernatant (suspension) with a pipette, wherein the concentration of metallic nickel in the suspension is 15g/Kg, and D₉₀Is 5 nm;

13.5g of the above-mentioned alumina matrix particles JZ1 and 10g of deionized water were mixed and ground to give D₉₀5 micron slurry, added to 100 grams of the above suspension; stirring for 10min to obtain a mixture, denoted as JY-1, pre-freezing the JY-1 at-40 ℃, and then drying for 24h under the vacuum condition of-30 ℃ and 50Pa to obtain a matrix containing a metal film, denoted as ZA1, wherein the thickness of the metal film ZA1 is 5nm, and the nickel content is 10 wt%.

(2) Preparation of regular Supported catalysts

Mixing ZA1 with water and pulping to prepare slurry with solid content of 35 wt%; taking a diameter of 30mm and a length of 50mm (expressed as

) And coating ZT1 with the slurry, drying at 120 ℃ for 2 hours, roasting at 450 ℃ for 2 hours, repeatedly coating for 3 times, wherein the dry basis weight of the active coating accounts for 30 wt%, and the final product is the regular carrier catalyst, and is marked as A1.

The structured carrier catalyst A1 contained 70 wt.% cordierite, 27 wt.% alumina, and 3 wt.% metallic nickel based on its dry weight.

Comparative example 1

An alumina substrate JZ1 (ground to D90 ═ 5 μm as in example 1) was mixed with an aqueous nickel nitrate solution, impregnated, slurried, and coated with a structured carrier ZT1 to obtain a structured carrier catalyst product DB 1. The active coating and nickel content were the same as in example 1.

Comparative example 2

10g of nickel nitrate (calculated as nickel) is dissolved in 100ml of ethylene glycol, then the reaction vessel is placed in an ultrasonic cleaning machine, ultrasonic treatment is carried out for 6h at the power of 160W, mixed and impregnated with JZ1 described in example 1, and then drying is carried out at 120 ℃, roasting is carried out at 450 ℃ for 2 hours, the structured carrier catalyst is coated, drying is carried out at 120 ℃ for 2 hours, and roasting is carried out at 450 ℃ for 2 hours, so that the product DB2 is obtained. Based on its dry weight, it contained cordierite 70 wt%, alumina 27 wt%, and nickel 3 wt%.

Comparative example 3

In the existing S-ZORB adsorbent, nickel is a hydrogenation active component, the composition of the S-ZORB adsorbent is that the content of zinc oxide is 44.3 wt%, the content of expanded perlite is 24.0 wt%, the content of alumina is 13.6 wt%, and the content of nickel is 18.1 wt%, and a structured carrier ZT1 is coated with the adsorbent slurry to obtain a structured carrier catalyst which is recorded as DB 3.

Comparative example 1

A structured supported catalyst was prepared as in example 1 except that the metal-containing membrane substrate was dried by a drying process at 120 ℃ without freeze-drying as described to provide a structured supported catalyst designated BJ 1.

Example 2

This example serves to illustrate the structured support catalyst of the invention and its preparation.

(1) Preparation of substrates containing Metal films

50g of iron powder (average particle size 15 μm, purity AR, manufacturing company: Shanghai Kefeng industries Co., Ltd.) and 400ml of ethylene glycol (analytical grade) were added to a 500ml jar, mixed uniformly, and 120mg of sodium lauryl sulfate (analytical grade, national drug group) as a surfactant was added; then, placing the reaction container in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 4h at 200W; centrifuging the liquid after ultrasonic treatment at 2000r/min for 10min, taking out suspension with iron concentration of 25g/Kg and iron particle size D₉₀Is 10 nm;

40g of α -Al₂O₃(product of Shandong aluminum industries, D)₉₀6 microns) and 40g of deionized water are added into 400g of the suspension, the mixture is stirred for 10min, the slurry is pre-frozen at the temperature of minus 40 ℃, and then is dried for 24h at the temperature of minus 30 ℃ and the pressure of 20Pa, and the final product is α -Al coated with the iron metal film₂O₃Designated ZA2, having a metal film thickness of 15nm and an iron content of 20% by weight, calculated on a dry basis, of ZA 2.

(2) Preparation of regular Supported catalysts

Intercepting a structured carrier ZT1 with the diameter of 30mm and the length of 50mm, preparing slurry with the solid content of 30 weight percent by ZA2 and water, coating ZT1 with the slurry of ZA2, drying at 120 ℃ for 2 hours, roasting at 450 ℃ for 2 hours, and repeatedly coating to ensure that the content of an active coating in the obtained structured carrier catalyst accounts for 20 weight percent to obtain the structured carrier catalyst, which is marked as A2. Composition of the structured catalyst a 2: based on the dry weight of A2, the catalyst contained 80 wt% cordierite and 16 wt% alumina, and 4 wt% metallic iron.

Example 3

(1) Preparation of a substrate containing a metal film: 60g of cobalt powder (average particle size 5 μm, purity 99%, pharmaceutical group) and 300ml of ethylene glycol (same as used in example 1) were added to a 500ml jar, mixed well, and 400mg of stearic acid (purchased from pharmaceutical group, purity AR) as a surfactant was added; then, putting the mixture into an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 10 hours at the power of 500W; then centrifuging at 1500r/min for 30min, and taking out the suspension; co concentration in the suspension 10g/Kg, particle size D of Co₉₀Is 4 nm;

17 g of β -Al₂O₃Powder (D90 ═ 20 microns, technical grade, product of the well petrochemical catalyst, Qilu division), mixed with 30 grams of deionized water, wet ball milled into a slurry with a particle diameter D₉₀5 microns; then 300g of the above suspension was added thereto; stirring for 10 min; the slurry was pre-frozen at-40 ℃ and then dried at-30 ℃ under 50Pa pressure (absolute) for 48h to give the final product, the matrix surrounding the metal film, designated ZA 3. The thickness of the metal film was 10nm, and the modified metal content was 15 wt%. D₉₀Is 5 microns.

(2) Preparation of regular Supported catalysts

Will be provided with

ZT1 of (1) was coated with a slurry of ZA3 and water (35% by weight solids), dried at 120 ℃ for 2 hours, calcined at 400 ℃ for 3 hours, and coated twice to give a structured supported catalyst, designated A3.

Composition of a 3: on a dry basis, this contained 75 wt.% cordierite, 21.25 wt.% alumina, and 3.75 wt.% metallic cobalt.

Example 4

(1) Preparation of a substrate containing a metal film: adding 450g of nickel-tungsten alloy fine powder (sourced from Tianjin Hainan alloy Co., Ltd., weight ratio of nickel to tungsten is 3: 2) and 500ml of water into a 1000ml wide-mouth bottle, uniformly mixing, and adding 2.8g of surfactant sodium glycocholate (sourced from Nanjing Paersi Biotech Co., Ltd., purity AR); then, placing the wide-mouth bottle in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 6h at the power of 150W; centrifuging the liquid after ultrasonic treatment at 1500r/min for 20min, and taking out the suspension; the weight ratio of nickel to tungsten in the suspension is 3: 2;

14.5 g of JZ1 powder was mixed with 10g of deionized water and wet ball milled to a slurry with a particle diameter D₉₀5 microns; 100g of the above suspension was added thereto; stirring for 10 min; pre-freezing at-10 deg.C, drying at-5 deg.C under 50Pa (absolute pressure) for 24 hr to obtain final product, namely matrix coated with nickel-tungsten bimetallic membrane, and marking as ZA 4; the thickness of the metal film is 10nm, and the total content of modified metal Ni and W is 20 wt%;

(2) preparation of regular Supported catalysts

Get

ZT1, coating the support with a slurry of ZA4 and water (35 wt% solids), drying at 120 ℃ for 2 hours, calcining at 350 ℃ for 3 hours, repeating the above process twice, and the final product is a structured supported catalyst, designated as a 4.

Composition of a4 dry basis: the catalyst contained 70 wt% of cordierite, 24 wt% of alumina, 3.6 wt% of metallic nickel and 2.4 wt% of metallic tungsten.

Example 5

Adding 50g of nickel-titanium alloy fine powder (purity 98%, nickel-titanium weight ratio 3:1, Luoyang Tongzhong information technology Co., Ltd.) and 300ml of water into a 500ml wide-mouth bottle, mixing uniformly, and adding 120mg of surfactant lauryl sodium sulfate (purity AR); then, the mixture is placed in an ultrasonic cleaning machine and is subjected to ultrasonic treatment for 4 hours at the power of 240W; centrifuging the liquid after ultrasonic treatment in a centrifuge at 3000r/min for 10min, and taking out the suspension; the concentration of metallic nickel and titanium in the suspension was 25g/Kg, D₉₀Is 4 nm;

42.5 grams of JZ1 powder was mixed with 35 grams of deionized water and wet ball milled to a slurry (with particle diameter D)₉₀5 microns); the slurry was added in its entirety to the above 300g of suspension; stirring for 10 min;

freezing the obtained slurry at-20 deg.C, and drying at-10 deg.C under 30Pa for 24 hr to obtain a coated nickel-titanium metal filmMatrix, designated ZA 5. ZA5 having a metal film thickness of 9nm, a total modified metal content of 15 wt.%, a Ni/Ti weight ratio of 3:1, D₉₀Is 5 microns.

Get

The structured carrier ZT1 was coated with a slurry (solid content 30 wt%) of ZA5 and water, dried at 120 ℃ for 2 hours, calcined at 400 ℃ for 2 hours, and the coating process was repeated 2 times to give a product with an active coating content of 20 wt%, and a structured carrier catalyst was obtained, designated A5.

On a dry basis, a5 contained 80 wt% cordierite, 17 wt% alumina, 2.25 wt% metallic nickel, and 0.75 wt% metallic titanium.

Example 6

Adding 30g of nickel-aluminum alloy fine powder (nickel-aluminum weight ratio is 4:1, average particle size is 20 μm, sourced from Nanjing chemical reagent Co., Ltd.) and 150ml of water into a 250ml wide-mouth bottle, uniformly mixing, and adding 200mg of surfactant stearic acid (carbon chain length is 18, sourced from Aladdin chemical reagent Co., Ltd., purity is 99.5%); then, carrying out ultrasonic treatment for 10h in an ultrasonic cleaning machine at the power of 210W; centrifuging the liquid subjected to ultrasonic treatment at 1500r/min for 30min, and taking out the suspension; the total concentration of metallic nickel and aluminium in the suspension was 20g/Kg, D₉₀Is 6 nm.

17 grams of JZ1 powder was mixed with 30 grams of deionized water and wet ball milled to a slurry with a particle diameter D₉₀5 microns; then 150g of the above suspension was added thereto; stirring for 10 min; the slurry was frozen at-65 ℃ and dried at-60 ℃ under 20pa for 36h, and the resulting product, a metal film-containing matrix, designated ZA 6. ZA6 has a metal film thickness of 10nm, a total content of nickel and aluminum modified metal of 15 wt%, a weight ratio of nickel to aluminum in the modified metal of 4:1, D₉₀Is 5 microns.

Will be provided with

The structured carrier ZT1 was coated with a slurry of ZA6 and water (35% by weight solids content), dried at 120 ℃ for 2 hours, calcined at 450 ℃ for 2 hours and repeatedThe coating was carried out twice to give an active coating content of 25% by weight in the final product, i.e. the structured supported catalyst, designated A6.

The desulfurization catalyst A6 had a cordierite content of 75 wt% alumina, and a total content of metallic nickel and aluminum of 3.75 wt% based on the dry weight of the catalyst, wherein the weight ratio of nickel to aluminum was 4: 1.

Example 7

Adding 10g of iron-nickel alloy fine powder (iron-nickel weight ratio 2:1, average particle size 15 μm, purity 98 wt% from south-palace Ruiteng alloy materials Co., Ltd.) and 100ml of glycerol (analytical grade) into a 200ml wide-mouth bottle, mixing uniformly, and adding 60mg of surfactant sodium glycocholate (purity AR from Nanjing Parls Biotech Co., Ltd.); then, putting the wide-mouth bottle into an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 6h at 160W power; centrifuging the liquid subjected to ultrasonic treatment at 1500r/min for 20min, and taking out the suspension; the total concentration of metallic iron and nickel in the suspension is 25g/Kg, the weight ratio of iron to nickel is 2:1, D₉₀Is 5 nm;

mixing 11.3 g of JZ1 with 10g of deionized water, and wet ball-milling into slurry, wherein the particle diameter d90 is 5 microns; then adding the whole into 100g of the suspension; stirring for 10 min; obtaining slurry JY-7;

and freezing the slurry JY-7 at-20 ℃, and drying at-15 ℃ and 30Pa (absolute pressure) for 24h to obtain a final product, namely the matrix wrapping the iron-nickel bimetallic membrane, which is recorded as ZA 7. The ZA7 metal film had a thickness of 12nm, a total iron and nickel modified metal content of 18 wt%, and a weight ratio of iron to nickel in the modified metal of 2: 1. ZA 7D₉₀Is 5 microns.

Will be provided with

Coating ZT1 with slurry (solid content 35 wt%) formed by ZA7 and water, drying at 120 deg.C for 2 hr, calcining at 450 deg.C for 2 hr, and repeatedly coating for 2 times, wherein the active coating layer in the product accounts for 30 wt% to obtain a structured carrier catalyst, which is marked as A7.

A7 contained cordierite 70 wt% alumina 24.6 wt%, metallic iron 3.6 wt%, metallic nickel 1..8 wt% on a dry basis.

Example 8

Adding 50g of iron-cobalt alloy fine powder (iron-cobalt weight ratio of 3:1, average particle size of 12 microns, purity of 99% from Kaixin alloy materials Co., Ltd., Danyang) and 300ml of glycerol (analytically pure) into a 500ml wide-mouth bottle, uniformly mixing, and adding 120mg of surfactant sodium dodecyl sulfate (analytically pure); then, placing the reaction container in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 4h at the power of 180W; centrifuging the liquid subjected to ultrasonic treatment at 2000r/min for 10min, and taking out the suspension; the total concentration of metallic iron and cobalt in the suspension was 20g/Kg, the weight ratio of iron to cobalt was 3:1, D₉₀Is 4 nm;

24 grams of JZ1 powder (dry basis) was mixed with 10 grams of deionized water and wet ball milled to a slurry with a particle diameter D₉₀5 microns; then 300g of the suspension is added into the solution and stirred for 10 min;

freezing the slurry at-20 ℃, drying the slurry at-15 ℃ under 20Pa for 30h, and obtaining a final product, namely a matrix coated with the iron-cobalt metal film, which is recorded as ZA8, wherein the total content of iron and cobalt modified metals is 20 wt%, and the weight ratio of iron to cobalt in the modified metals is 2:1, ZA 8D₉₀Is 5 microns.

ZT1(

I.e. 30mm diameter and 50mm height) was coated with a slurry of ZA8 and water (35% by weight solids), dried at 120 c for 2 hours, calcined at 450 c for 2 hours, and coated repeatedly 2 times to give 20% by weight active coating, the final product being a structured support catalyst, designated a 8.

A8 contained cordierite 80 wt%, alumina 16 wt%, metallic iron 3 wt%, and metallic cobalt 1 wt% on a dry basis. .

Example 9

Adding 30g of iron-magnesium alloy fine powder (iron-magnesium weight ratio is 4:1, average particle size is 16 microns, source Anyang, Jinding iron alloy Co., Ltd., purity is 99.5%) and 150ml of glycerol into a 250ml wide-mouth bottle, uniformly mixing, and adding 200mg of surfactant stearic acid; then, the reaction vessel is placedPlacing the mixture in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 10 hours at the power of 280W; centrifuging the liquid subjected to ultrasonic treatment at 1500r/min for 30min, and taking out the suspension; the total concentration of metallic iron and cobalt in the suspension was 18g/Kg, the weight ratio of iron to magnesium was 4:1, D₉₀Is 5 nm;

22.3 grams of JZ1 powder (dry basis) was mixed with 10 grams of deionized water and wet ball milled to a slurry with a particle diameter D₉₀5 microns; then 150g of the suspension is added into the mixture and stirred for 10 min;

freeze-drying the above slurry for 24h at-25 deg.C under 50Pa (i.e. drying under-25 deg.C and 50Pa for 24 hr); the final product, i.e. the substrate coated with the film of iron-magnesium alloy, is designated ZA9, wherein the total content of iron and magnesium modified metal is 10.8% by weight, the weight ratio of iron to magnesium in the modified metal is 4:1, D₉₀Is 5 microns.

Get

ZT1 (g), coated with a slurry of ZA9 and water (30 wt% solids), dried at 120 ℃ for 2 hours, calcined at 450 ℃ for 2 hours, and coated repeatedly 2 times, the coating being such that the weight of the active coating in the coated product is 15 wt% on a dry basis, giving a structured support catalyst, designated a9, containing 75 wt% cordierite, 22.3 wt% alumina, 2.16 wt% metallic iron, and 0.54 wt% metallic magnesium, on a dry basis.

Example 10

Adding 10g of cobalt-molybdenum alloy fine powder (weight ratio of cobalt to molybdenum 3:1, average particle size 10 μm, purity 99% from Tianjin kenna Metal materials Co., Ltd.) and 100ml of a mixture of methanol and water (methanol content 50 vol%) into a 200ml jar, mixing uniformly, and adding 60mg of surfactant sodium glycocholate; then, placing the reaction container in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 6h at the power of 320W; centrifuging the liquid after ultrasonic treatment at 1500r/min for 20min, and taking out the suspension; the total concentration of metallic cobalt and molybdenum in the suspension was 45g/Kg, the weight ratio of cobalt to molybdenum was 3: 2, D₉₀Is 6 nm;

18 grams of JZ1 powder (dry basis) was mixed with 20 grams of deionized water, wetBall-milling into a slurry having a particle diameter D₉₀5 microns; then 100g of the above suspension was added thereto; stirring for 10 min; finally, freeze-drying the slurry for 24h, wherein the freeze-drying temperature is-30 ℃, and the absolute pressure is 50 Pa; the final product, the matrix surrounding the metal film, is designated ZA 10. ZA10 having a total cobalt and molybdenum modified metal content of 20 wt%, the weight ratio of cobalt to molybdenum in the modified metal being 3:1, D₉₀Is 5 microns.

Intercepting

ZT1 (g) was coated with a slurry of ZA10 and water (35 wt% solids), dried at 120 ℃ for 2 hours, calcined at 450 ℃ for 2 hours, and coated 2 times to make the weight of the active coating 30 wt%, and the final product, the structured supported catalyst, was designated a, 10. A10 contained, on a dry basis, 70 wt.% cordierite, 24 wt.% alumina, and 6 wt.% total metallic cobalt and molybdenum, with a cobalt to molybdenum weight ratio of 3: 1.

Example 11

A regular supported catalyst was prepared by the method of reference example 1 except that a suspension was prepared using cobalt titanium alloy powder (cobalt titanium weight ratio 1:1, average particle diameter 15 μm, available from Tianjin kenna metallic materials Co., Ltd., purity 99.5%).

Adding 50g of cobalt-titanium alloy fine powder and 300ml of a mixture of methanol and water (the methanol content is 50 vol%) into a 500ml wide-mouth bottle, uniformly mixing, and adding 120mg of surfactant sodium dodecyl sulfate; then, placing the reaction container in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 4h at the power of 450W; centrifuging the liquid subjected to ultrasonic treatment for 10min at 2000r/min, and taking out the suspension; the total concentration of metallic cobalt and titanium in the suspension was 30g/Kg, the weight ratio of cobalt to titanium was 1:1, D₉₀Is 5 nm;

36 grams of JZ1 powder (dry basis) was mixed with 30 grams of deionized water and wet ball milled to a slurry with a particle diameter D₉₀5 microns; then 300g of the above suspension was added thereto; stirring for 10 min;

freeze-drying the slurry for 30h at-30 deg.C under 20 Pa; the final product being a metal-containing filmMatrix, designated ZA11, in which the total content of cobalt and titanium modified metals is 20% by weight, the weight ratio of cobalt to titanium in the modified metals being 1:1, D₉₀Is 5 microns.

Intercepting

ZT1 (g), coated with a slurry of ZA11 and water (30 wt% solids), dried at 110 ℃ for 2 hours, calcined at 350 ℃ for 2 hours, and coated 2 times to give a structured supported catalyst, designated a 11. On a dry basis, a11 contains 80 wt% of cordierite, 16 wt% of alumina, 2 wt% of metallic cobalt, and 2 wt% of metallic titanium.

Example 12

A structured supported catalyst was prepared by the method of reference example 1, except that cobalt-gallium alloy powder (cobalt-gallium weight ratio 4:1, average particle diameter 10 μm, available from Tianjin kenna metals Co., Ltd., purity 99%) was used, and the preparation process parameters are shown in Table 2, which is not described in reference example 1.

30g of cobalt-gallium alloy fine powder and 150ml of a mixture of methanol and water (methanol content: 50 vol%) were added to a 250ml jar, mixed uniformly, and 200mg of stearic acid as a surfactant was added; then, placing the reaction container in an ultrasonic cleaning machine, and carrying out ultrasonic treatment for 10 hours at the power of 240W; centrifuging the liquid subjected to ultrasonic treatment at 1500r/min for 30min, and taking out the suspension; the total concentration of metallic cobalt and gallium in the suspension was 35g/Kg, the weight ratio of cobalt to gallium was 4:1, D₉₀Is 5 nm;

29.75 grams of JZ1 (dry basis) was mixed with 30 grams of deionized water and wet ball milled to a slurry with a particle diameter D₉₀5 microns; then 150g of the above suspension was added thereto; stirring for 10 min; freeze-drying for 24h at-35 deg.C under 30Pa (absolute pressure); obtaining a matrix containing a metal film, denoted ZA12, wherein the total content of cobalt and gallium modified metals is 15% by weight, the weight ratio of cobalt to gallium in the modified metals is 4:1, particle diameter D₉₀Is 5 microns.

Intercepting

Z of (A)T1, coating with slurry (solid content is 35 wt%) formed by ZA12 and water, drying at 120 ℃ for 2 hours, roasting at 450 ℃ for 2 hours, and repeatedly coating for 2 times (the repeated coating means that the coating, drying and roasting processes are carried out again), so as to obtain the regular carrier catalyst, which is marked as A1, 2; the composition contained 75 wt% of cordierite, 21.25 wt% of alumina, 3 wt% of metallic cobalt and 0.75 wt% of metallic gallium.

Example 13

A structured carrier catalyst was prepared as in example 1, except that a Sn-Sb alloy powder was used, wherein Sn: sb 2:1 weight ratio. The resulting catalyst was designated A13.

Example 14

A structured supported catalyst was prepared as in example 1, except that an alloy powder having a Ti-Zr-V ratio of 1:1:0.5 was used. The regular carrier catalyst A14 was obtained.

Example 15

A structured carrier catalyst was prepared as in example 1, except that a Sb-Bi-Cu alloy powder was used in a Sb-Bi-Cu weight ratio of 5:4: 1. The regular carrier catalyst A15 was obtained.

Application example

The modified sub-sieves A1-A14, DB1 and BJ1 prepared in examples 1-15, comparative examples 1-3 and comparative example 1 of the invention are subjected to desulfurization evaluation experiments by using a fixed bed micro-reaction experimental device, and the specific method comprises the following steps: a regular carrier catalyst (may also be referred to as a desulfurization catalyst) was packed in a fixed bed reactor having an inner diameter of 30mm and a length of 1 m. Hydrogen is used as hydrogen supplying medium, the reaction temperature is 300 ℃, the reaction pressure is 1.38Mpa, the hydrogen-oil ratio is 100, and the weight space velocity of the raw material hydrocarbon oil is 4h^-1Under the reaction conditions of (1), a desulfurization reaction of the sulfur-containing hydrocarbon oil is carried out. The raw material hydrocarbon oil is gasoline, the composition is shown in table 1, and the reaction result is shown in tables 2-4.

TABLE 1

Item	Analyzing data	Item	Analyzing data
				Density (20 ℃ C.) (kg.m)^-3)	727.3	Induction phase (min)	922
Actual gum (mg/mL)	0.34	Distillation range (. degree.C.)
				Refractive index (20 ℃ C.)	1.4143	Initial boiling point	38.5
Sulfur content (ng./. mu.L)	960.48	5％	49.0
				Mercaptan sulfur content (ng/. mu.L)	10.2	10％	55.5
Hydrogen sulfide content (ng/. mu.L)	0	30％	74.7
				Octane number (RON/MON)	93.7/83.6	50％	97.2
Group composition volume (%)		70％	124.2
				Saturated hydrocarbons	44.0	90％	155.2
Olefins	41.2	95％	165.2
				Aromatic hydrocarbons	14.8	End point of distillation	185.0

TABLE 2

TABLE 3

TABLE 4

Note: in tables 2 to 4:

1. the feed gasoline had a sulfur content of 960ppm, a RON of 93.7 and a MON of 83.6.

2.Δ MON represents the increase in product MON;

3.Δ RON represents the increase in product RON;

4. delta (RON + MON)/2 is the difference between the antiknock index of the product and the antiknock index of the raw material.

5. The sulfur content of the samples at each time point is the sulfur content of the samples collected within one hour before the sampling time point, and the gasoline composition and octane number are the average values of the analysis results of each sample.

From the results data of tables 2 to 4, it can be seen that:

after the regular carrier catalysts A1-A15 prepared in examples 1-15 are used as catalysts for gasoline desulfurization treatment, the sulfur content in a gasoline product is lower than 0.5ppm (chromatographic detection limit) in the initial reaction stage, and gradually increases with the reaction time, but after the reaction for 240-960 h, the sulfur content in the gasoline product can still be lower than 10ppm, the octane number loss of gasoline is small, and in some cases, the octane number of gasoline is even increased.

Claims

1. A regular carrier catalyst with desulfurization function is characterized by comprising a regular carrier and an active coating attached to the surface of the regular carrier, wherein the active coating comprises a heat-resistant inorganic oxide matrix and a modified metal film, the modified metal film comprises modified metal, and the modified metal is one or more of Fe, Co, Ni, Mn, Ti, Zr, V, Ge, Pb, Sn, Sb and Bi.

2. The structured carrier catalyst as recited in claim 1, wherein the modified metal film is on the outer surface of the matrix particles, and the modified metal film has a thickness of 5 to 30 nm.

3. The structured catalyst according to claim 1, wherein the active coating comprises 5 to 50 wt% and the structured carrier comprises 50 to 95 wt% on a dry basis, based on the total weight of the structured catalyst;

the active component coating comprises 8-25 wt% of modified metal film and 75-92 wt% of matrix on a dry basis based on the total weight of the active component coating;

the heat-resistant inorganic oxide matrix, such as one or more of an alumina matrix, a silica matrix, a zirconia matrix, a titania matrix, and a silica-alumina matrix;

the regular structure carrier is an integral carrier with a parallel pore channel structure with openings at two ends.

4. A structured support catalyst according to any of claims 1 to 3, wherein the modified metal film comprises a third element selected from one or more of Cr, Mo, W, Cu, Ag, Au, Al, Ga, Mg, B.

5. A method for preparing a structured carrier catalyst comprises the following steps: forming a mixture of metal powder, a hydroxyl-containing solvent and a surfactant, and then treating under ultrasonic waves to obtain an ultrasonic mixed solution; separating the mixed solution after ultrasonic treatment to obtain a suspension; and (3) contacting the suspension with the matrix particles, freezing and drying to obtain the matrix particles containing the modified metal membrane, and then coating the matrix particles containing the modified metal membrane on a regular carrier to obtain the regular carrier catalyst.

6. A process for preparing a structured carrier catalyst as claimed in claim 5, wherein the concentration of the modifying metal in the suspension is 5 to 45 g/Kg.

7. Process for the preparation of a modified structured support catalyst according to claim 5 or 6, wherein the particles in the suspension have a size D₉₀Is 20nm or less.

8. A process for preparing a structured carrier catalyst as claimed in claim 5, wherein the weight ratio of the hydroxyl-containing solvent to the metal powder is from 2 to 15: 1, the ratio of the surfactant to the hydroxyl group-containing solvent is 0.001 to 100 mg/mL.

9. The method for preparing a structured carrier catalyst according to claim 5, wherein the ultrasonic treatment is carried out at a power of 10 to 500W per 100ml of solvent, and the average diameter of the metal powder is less than 20 μm.

10. A process for preparing a structured support catalyst as defined in claim 5 wherein the metal powder is one or more of a pure metal powder or a metal alloy powder; the pure metal powder is one or more of Fe powder, Co powder, Ni powder, Mn powder, Ti powder, Zr powder, V powder, Sn powder, Sb powder and Bi powder; the alloy powder is an alloy formed by a plurality of Fe, Co, Ni, Mn, Ti, Zr, V, Sn, Sb and Bi, or an alloy formed by one or more modified metals of one or more of Fe, Co, Ni, Mn, Ti, Zr, V, Sn, Sb and Bi and one or more of third elements; in the metal powder, the weight ratio of the third element to the modified metal is 0-1: 1, such as 0-0.8: 1 or 0-0.5: 1 or 0.1-0.3: 1.

11. a method for preparing a structured carrier catalyst as defined in claim 5 wherein the surfactant is one of sodium glycocholate, sodium dioctyl sulfosuccinate, sodium dodecylbenzenesulfonate, sodium dodecyl sulfate, sodium lauryl sulfate, stearic acid, oleic acid, lauric acid, fatty acid amine, cetyl trimethylammonium bromide, sodium dodecyl sulfate, cetyl trimethylammonium bromide, fatty acid methyl ester, and polyoxyethylene ether.

12. A method for preparing a structured carrier catalyst according to claim 5 or 11 wherein the hydroxyl containing solvent is water and/or a hydroxyl containing organic solvent, the hydroxyl containing organic solvent is preferably a mono-, di-, tri-or derivative thereof, the mono-alcohol is one or more of methanol and ethanol, the di-alcohol is ethylene glycol, the di-alcohol derivative is one or more of ethylene glycol monomethyl ether, ethylene glycol monoethyl ether, ethylene glycol monobutyl ether and ethylene glycol ether, the tri-alcohol is glycerol, and the tri-alcohol derivative is triethanolamine.

13. A process for preparing a structured carrier catalyst according to claim 5, wherein the separation is carried out by centrifugation at a rotational speed of 1200 to 3000 r/min.

14. A process for preparing a structured support catalyst according to claim 5, wherein the freeze-drying is a sublimation drying at low temperature and high vacuum.

15. A process for preparing a structured support catalyst according to claim 5,

on the basis of the total weight of the structured carrier catalyst, the structured carrier catalyst comprises 10-50 wt% of an active coating and 50-90 wt% of a structured carrier on a dry basis;

the active coating comprises a substrate and a modified metal film, wherein the modified metal film comprises a modified metal and a third element, and the content of the substrate in the active coating is 75-92 wt% and the total content of the modified metal and the third element is 8-25 wt% in terms of dry basis based on the total weight of the active coating.

16. The method for preparing a structured carrier catalyst according to claim 5, wherein the step of coating the structured carrier with the matrix particles containing the modified metal film comprises the steps of coating the structured carrier with a matrix slurry containing the modified metal film, drying, and calcining at a temperature of 200 to 600 ℃ for a time of 1 hour or more.

17. A method for preparing a structured support catalyst as claimed in claim 5 wherein the matrix particles are one or more of alumina particles, silica-alumina particles, zirconia particles, titania particles or particles selected from the group consisting of alumina, silica and alumina, zirconia and titania.

18. A desulfurization method of sulfur-containing hydrocarbon comprises the step of carrying out contact reaction on a hydrocarbon material containing sulfur compounds, a hydrogen donor and the structured carrier catalyst of any one of claims 1 to 4, wherein the reaction temperature is 150-350 ℃, the reaction pressure is 0.5-5 MPa, and the weight hourly space velocity of the sulfur-containing hydrocarbon is 0.1-100 h^-1The volume ratio of the hydrogen donor to the sulfur-containing hydrocarbon is 0.01-1000; the hydrogen donor is one or more of hydrogen, hydrogen-containing gas and hydrogen donor; the hydrocarbon material is one or more of natural gas, dry gas, liquefied gas, gasoline, kerosene, diesel oil and gas oil.