CN104368352A - Hydrogenation activity protection catalyst, and its preparation method and application - Google Patents
Hydrogenation activity protection catalyst, and its preparation method and application Download PDFInfo
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Abstract
The invention relates to a hydrogenation activity protection catalyst, and its preparation method and application. The catalyst contains an alumina carrier having a bimodal porous structure and containing at least one of boron, silicon and fluorine assistants, and a result of characterization through a mercury intrusion technology shows that the pore volume of the carrier is 0.3-0.8ml/g, the specific surface area is 70-220m<2>/g, the pore volume of pores with the diameter of 6-10nm accounts for 8-25% of the total pore volume and the pore volume of pores with the diameter of 85-160nm accounts for 40-75% of the total pore volume. The hydrogenation activity protection catalyst provided by the invention has better metal protection performance than hydrogenation activity protection catalysts in the prior art.
Description
Technical field
The present invention relates to a kind of hydrogenation activity guard catalyst and preparation and application thereof.
Background technology
Along with crude quality is deteriorated, in crude oil, the impurity content such as colloid, asphalitine and organo-metallic compound increases, and the existence of these impurity is easy to the quick decline so that the inactivation that cause catalyst activity.The effective ways addressed this problem are the protective agents in the filling of hydrogenation catalyst bed top with hydrogenation activity.Have and hold metal and hold charcoal ability strong compared with the hydrogenation protecting catalyst of large pore volume and bore dia, the effect of protection downstream hydrogenation host can be played, extend the service life of host.
In prior art about the example of hydrogenation protecting catalyst and preparation thereof as:
CN200610113493.5 discloses a kind of hydrogenation protecting agent and preparation thereof; this protective agent contains the heat-resistant inorganic oxide of one or more porous; it is characterized in that; the total pore volume of described protective agent be 0.3-1.5 millimeter/gram; wherein containing grade macropore; grade macropore bore dia is 0.1 ~ 1.5 micron, and grade macropore pore volume is 0.05 ~ 0.7 ml/g.The preparation method of described hydrogenation protecting agent; comprise the precursor of the heat-resistant inorganic oxide of one or more porous and/or the heat-resistant inorganic oxide of porous is mixed with at least one organic matter, shaping, dry and roasting; wherein, described organic compound is fusing point between 30 ~ 200 DEG C, particle diameter 0.3 ~ 2.5 millimeter and water-fast solid particle.
CN201010220850.4 discloses the protectant preparation method of a kind of hydrotreatment.In the method, alumina support is prepared by the different boehmite dry glue powder kneading method of employing two kinds, then supported active metals; Wherein the first crystallization degree of pseudo-boehmite is relatively little, pore volume is large, the hole of bore dia 30nm ~ 100nm can be provided, the second crystallization degree of pseudo-boehmite is relatively high, can provide micron-sized hole, again because its acidity indexes is high, extremely hard bulk is presented after drying, after being pulverized, 100% by 50 orders, not only can increase the quantity of micrometer grade hole, also can improve the intensity of catalyst carrier.By adjustment mixed proportion between the two, the hydrotreatment protective agent that intensity is high, bulk density is large, pore volume is large and wear rate is low can be made.CN98111379.6 discloses hydrogenation protecting catalyst and preparation method thereof, and this catalyst carrier is ultra-large aperture, and aperture is the bimodal hole of 0.1-30 μm, and catalyst pore volume is 0.1-0.8ml/g, specific surface 0.1-20m
2/ g, containing group vib metallic element 6.65m%-20.0m and/or VIII race's metallic element 8.71% ,-26.13m%.Preparation method adopts particle to pile up legal system for alumina support, then adopts containing molybdenum solution and solution containing nickel equivalent impregnation, the catalyst after dipping at 100-120 DEG C of dry 2-5h, at 500-550 DEG C of roasting 2-5h.
CN00110019.X discloses a kind of Hydrogenation active protective agent and preparation method thereof, simultaneously containing γ mono-aluminium oxide and δ-aluminium oxide in protective agent used carrier; Containing group vib metal oxide 3-22m% and VIII family metal oxide 0.5-5m% in protective agent, containing IA family metal oxide 0-2m%, phosphorous 0-3m%, specific surface 100-250m
2/ g.Pore volume 0.4-0.8ml/g.
CN200910206230.2 discloses a kind of hydrotreating guard catalyst for residual oil and application thereof.This catalyst pore volume is large, and aperture is large, and porosity is high, reasonable pore distribution, and outer surface orifice is comparatively large, and duct penetrability is good, and more than 1000nm contains more than 36% in duct.In particular in residue fixed-bed hydrogenation method, the metal deviate from can be made to homogeneously precipitate in whole beds, impurity vanadium and calcium can be deposited in inside, duct, improve the utilization rate of hole, keep long-term operation.
CN1765509A discloses a kind of macropore alumina supporter, take aluminium oxide as main component, containing boron oxide, it is characterized in that boron oxide weight content is in the carrier 1.0% ~ 15.0%, average pore size 10 ~ 20nm, carrier>=350 DEG C of meleic acids are 0.05 ~ 0.3mmol/g, the pore volume of carrier is 0.5 ~ 1.0cm
3/ g, specific area is 150 ~ 270m
2/ g.This patent controls the temperature introducing boron in aluminium oxide precursor, and claim to adopt in this way while acquisition macropore alumina supporter, the acid amount in carrier increases.
Problem during above-mentioned prior art uses for hydrogenation protecting catalyst, gives various different solution.But when this kind of catalyst is used for processing of heavy oil, still there is the space of significant improvement in its performance.
Summary of the invention
The technical problem to be solved in the present invention be to provide a kind of newly, hold higher hydrogenation protecting catalyst of metal ability and its preparation method and application.
Usually, prepare hydrogenation protecting catalyst carrier and there is bimodal porous.The present inventor finds, the feature that the aluminium oxide article shaped of bimodal porous that what prior art provided have is general is, the aperture of the macroperforation in bimodal hole or (such as, more than 1000nm disclosed in CN200910206230.2) bigger than normal.By this kind of carrier for the preparation of hydrogenation protecting catalyst time, it holds metallicity and still there is the space of very large improvement.
The content that the present invention relates to comprises:
1, a hydrogenation protecting catalyst, containing the alumina support being selected from boron, silicon and fluorine auxiliary agent containing at least one with structure of double peak holes, characterize with mercury injection method, the pore volume of described carrier is 0.3-0.8 ml/g, and specific area is 70-220 rice
2/ gram, wherein, diameter is the 8-25% that the pore volume in 6-10nm hole accounts for total pore volume, and diameter is the 40-75% that the pore volume in 85-160nm hole accounts for total pore volume.
2, the hydrogenation protecting catalyst according to 1, is characterized in that, the pore volume of described carrier is 0.4-0.7 ml/g, and specific area is 80-210 rice
2/ gram, wherein, diameter is the 10-20% that the pore volume in 6-10nm hole accounts for total pore volume, and diameter is the 45-70% that the pore volume in 85-160nm hole accounts for total pore volume.
3. the catalyst according to 1, is characterized in that, with the content of the described auxiliary agent boron of oxide basis, silicon for 0.1-8 % by weight, in the Oil repellent of element for 0.1-8 % by weight.
4. the catalyst according to 3, is characterized in that, with the content of the described auxiliary agent boron of oxide basis, silicon for 1-6 % by weight, in the Oil repellent of element for 1-6 % by weight.
5. the catalyst according to 4, is characterized in that, with the content of the described auxiliary agent boron of oxide basis, silicon for 1-4 % by weight, in the Oil repellent of element for 1-4 % by weight.
6. the catalyst according to 1, it is characterized in that, hydrogenation active metals component in described catalyst is selected from least one metal component of group VIII and at least one metal component of group VIB, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is greater than 0 to being less than or equal to 4 % by weight, and the content of metal component of group VIB is greater than 0 to being less than or equal to 10 % by weight.
7. the catalyst according to 6, it is characterized in that, described metal component of group VIII is selected from cobalt and/or nickel, metal component of group VIB is selected from molybdenum and/or tungsten, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is 1-3 % by weight, and the content of metal component of group VIB is 3-6 % by weight.
8. the preparation method of the hydrogenation activity guard catalyst according to 1, what comprise that preparation has a structure of double peak holes is selected from boron containing at least one, the alumina support of silicon and fluorine auxiliary agent, the preparation method of described carrier comprises being mixed with a kind of Alpha-alumina by a kind of hydrated alumina and introducing in the mixture and contains at least one and be selected from boron, the compound of silicon and fluorine auxiliary agent, shaping, dry also roasting, sintering temperature is 750-1000 DEG C, roasting time is 1-10 hour, wherein, in the mixing ratio of the hydrated alumina of butt and Alpha-alumina for 15-70:30-85, the pore volume of described hydrated alumina is 0.3-1.1 ml/g, specific surface is 150-350 rice
2/ gram, most probable bore dia 5-20nm.
9, the method according to 8, it is characterized in that, described sintering temperature is 800-950 DEG C, roasting time is 2-8 hour, wherein, in the mixing ratio of the hydrated alumina of butt and Alpha-alumina for 30-70:30-70, the pore volume of described hydrated alumina is 0.35-1.0 ml/g, and specific surface is 150-300 rice
2/ gram, most probable bore dia 6-15nm.
10, the method according to 8 or 9, is characterized in that, described hydrated alumina is selected from boehmite.
11. methods according to 8, it is characterized in that, with described carrier for benchmark, make the content of boron, silicon in final carrier for 0.1-8 % by weight with the introduction volume of the described auxiliary agent boron of oxide basis, silicon, make the content of fluorine in final carrier for 0.1-8 % by weight in the introduction volume of the fluorine of element.
12. methods according to 11, is characterized in that, make the content of boron, silicon in final carrier for 1-6 % by weight with the introduction volume of the described auxiliary agent boron of oxide basis, silicon, make the content of fluorine in final carrier for 1-6 % by weight in the introduction volume of the fluorine of element.
13. methods according to 12, is characterized in that, make the content of boron, silicon in final carrier for 1-4 % by weight with the introduction volume of the described auxiliary agent boron of oxide basis, silicon, make the content of fluorine in final carrier for 1-4 % by weight in the introduction volume of the fluorine of element.
14. methods according to 8, it is characterized in that, described method is included in supported on carriers hydrogenation active metals component, the described method in supported on carriers hydrogenation active metals component is infusion process, comprise preparation contain the solution of the compound of hydrogenation active metals and use this solution impregnating carrier, carry out drying afterwards, roasting or not roasting, described hydrogenation active metals component is selected from the metal component of at least one group VIB and the metal component of at least one the VIIIth race, be benchmark with oxide basis and with catalyst, the consumption of the concentration of the described compound containing hydrogenation active metals in described solution and described solution makes the content of the metal component of the group VIB in final catalyst be greater than 0 to being less than or equal to 10 % by weight, the content of the metal component of described VIIIth race is greater than 0 to being less than or equal to 4 % by weight, described drying condition comprises: temperature is 100-250 DEG C, and the time is 1-10 hour, described roasting condition comprises: temperature is 360-500 DEG C, and the time is 1-10 hour.
15. methods according to 14, it is characterized in that, the metal component of described group VIB is selected from molybdenum and/or tungsten, the metal component of the VIIIth race is selected from cobalt and/or nickel, be benchmark with oxide basis and with catalyst, the described compound containing hydrogenation active metals makes the content of the metal component of the group vib in final catalyst be 3-6 % by weight in the concentration of described solution and the consumption of described solution, and the content of the metal component of the VIIIth race is 1-3 % by weight; Described drying condition comprises: temperature is 100-140 DEG C, and the time is 1-6 hour; Described roasting condition comprises: temperature is 360-450 DEG C, and the time is 2-6 hour.
The application of hydrogenation activity guard catalyst in hydrocarbon oil hydrogenation process in 16. claim 1-7 described in any one.
According to catalyst provided by the invention, wherein, characterize with mercury injection method, the pore volume of described shaping carrier is 0.3-0.8 ml/g, and specific area is 70-220 rice
2/ gram, wherein, diameter is the 8-25% that the pore volume in 6-10nm hole accounts for total pore volume, and diameter is the 40-75% that the pore volume in 85-160nm hole accounts for total pore volume; The pore volume of preferred described shaping carrier is 0.4-0.7 ml/g, and specific area is 80-210 rice
2/ gram, wherein, diameter is the 10-20% that the pore volume in 6-10nm hole accounts for total pore volume, and diameter is the 45-70% that the pore volume in 85-160nm hole accounts for total pore volume.
Take carrier as benchmark, in described carrier, the content of auxiliary agent is 0.1-8 % by weight, is preferably 1-6 % by weight, more preferably 1-4 % by weight.Wherein, boron and silicon are with oxide basis, and fluorine is in element.
In the present invention, the hydrogenation active metals component in described catalyst and content thereof are usually the conventional hydrogenation active metals component of hydrogenation protecting catalyst and content, such as, are selected from least one the VIIIth race's non-noble metal components and at least one group vib metal component.The metal component of preferred VIIIth race is nickel and/or cobalt, the metal component of preferred group vib is molybdenum and/or tungsten, with oxide basis and with described catalyst for benchmark, the content of described group VIII metal is for being greater than 0 to being less than or equal to 4 % by weight, be preferably 1 ~ 3 % by weight, the content of described group vib metal component, for being greater than 0 to being less than or equal to 10 % by weight, is preferably 3 ~ 6 % by weight.
According to catalyst provided by the invention, can also not affect containing any the adjuvant component that the performance that the invention provides catalyst maybe can improve catalyst performance provided by the invention.As contained the components such as phosphorus, be benchmark in element and with catalyst, the content of described auxiliary agent is no more than 10 % by weight, is preferably 0.5-5 % by weight.
According to the preparation method of hydrogenation protecting catalyst provided by the invention, the preparation method of wherein said carrier, comprise a kind of hydrated alumina being mixed with a kind of Alpha-alumina and introducing in the mixture and contain at least one and be selected from boron, the compound of silicon and fluorine auxiliary agent, shaping, dry also roasting, sintering temperature is 750-1000 DEG C, be preferably 800-950 DEG C, roasting time is 1-10 hour, be preferably 2-8 hour, wherein, in the mixing ratio of the hydrated alumina of butt and Alpha-alumina for 15-70:30-85(wherein, 15-70 refers to that the hydrated alumina (in butt) of every hundred parts is with the mixture of Alpha-alumina, the value of hydrated alumina number changes between 15-70, 30-85 refers to that the hydrated alumina (in butt) of every hundred parts is with the mixture of Alpha-alumina, the value of Alpha-alumina number changes between 30-85), be preferably 30-70:30-70.The pore volume of described hydrated alumina is 0.3-1.1 ml/g, and be preferably 0.35-1 ml/g, specific surface is 150-350 rice
2/ gram be preferably 150-300 rice
2/ gram, most probable bore dia is 5-20nm, is preferably 6-15nm.Be preferably the hydrated alumina containing boehmite.Here, the pore volume of described hydrated alumina, specific area and can and aperture, be that described hydrated alumina after 4 hours in 600 DEG C of roastings, is characterized by BET nitrogen absorption under low temperature and obtains.
In described hydrated alumina and Alpha-alumina mixture, introduce the method being selected from boron, silicon and fluorine auxiliary compound containing at least one is conventional method, such as, can be directly the compound containing described adjuvant component of aequum is mixed in aforesaid hydrated alumina and Alpha-alumina mixed process.
Concrete prepare in the embodiment of carrier at one, in described hydrated alumina and Alpha-alumina mixture, introduce the method being selected from boron, silicon and fluorine auxiliary compound containing at least one is be mixed with the aqueous solution by being selected from boron, silicon and fluorine auxiliary compound containing at least one, this aqueous solution is mixed into while described hydrated alumina mixes with Alpha-alumina or again this aqueous solution is mixed into after described hydrated alumina mixes with Alpha-alumina, aftershaping, dry and roasting.Compound containing described auxiliary agent is one or more in their water soluble compounds.Such as, containing one or more in the water-soluble inorganic salt of described auxiliary agent.
Wherein, described Alpha-alumina can be commercially available commodity (commodity alpha-alumina), also can be obtained through high-temperature roasting by hydrated alumina (alumina hydrate powder).Under being enough to that hydrated alumina roasting phase transformation is converted into the condition of Alpha-alumina, this process can adopt arbitrary existing method to realize, and does not limit this present invention.
Aluminium oxide shaping carrier in the present invention, can be made into the various shaping carrier being easy to operate depending on different requirement, such as spherical, cellular, nest like, tablet or bar shaped (clover, butterfly, cylindrical etc.).Shapingly can to carry out according to a conventional method.When shaping, such as extruded moulding, for ensureing described shapingly to carry out smoothly, can add in described mixture water, extrusion aid and/or adhesive, containing or not containing expanding agent, then extrusion molding, carry out drying also roasting afterwards.The kind of described extrusion aid, peptizing agent and consumption are conventionally known to one of skill in the art, such as common extrusion aid can be selected from one or more in sesbania powder, methylcellulose, starch, polyvinyl alcohol, PVOH, described peptizing agent can be inorganic acid and/or organic acid, and described expanding agent can be one or more in starch, synthetic cellulose, polymeric alcohol and surfactant.Synthetic cellulose is wherein preferably one or more in CMC, methylcellulose, ethyl cellulose, hydroxyl fiber fat alcohol polyethylene ether, polymeric alcohol is preferably one or more in polyethylene glycol, poly-propyl alcohol, polyvinyl alcohol, one or more in the propenyl copolymer that surfactant is preferably fat alcohol polyethylene ether, fatty alkanol amide and derivative thereof, molecular weight is 200-10000 and maleic acid copolymer.
In the present invention, described method that is shaping, dry and roasting is conventional method.Wherein, it is 750-1000 DEG C that the condition of roasting preferably includes sintering temperature, and roasting time is 1-10 hour, and it is 800-950 DEG C that the condition of preferably roasting further comprises sintering temperature, and roasting time is 2-8 hour.
According to the preparation method of hydrogenation protecting catalyst provided by the invention; comprise the step introducing hydrogenation active metals component on described carrier, hydrogenation active metals component is wherein selected from least one the VIIIth race's base metal and the combination being selected from least one group vib metal.The metal component of preferred group vib is molybdenum and/or tungsten, with oxide basis and with described catalyst for benchmark, the introduction volume of described group vib metal component makes the content of group vib metal component in final catalyst for being greater than 0 to being less than or equal to 10 % by weight, be preferably 3 ~ 6 % by weight, the introduction volume of described metal component of group VIII makes the content of metal component of group VIII in final catalyst for being greater than 0 to being less than or equal to 4 % by weight, is preferably 1 ~ 3 % by weight.
What on described carrier, introduce hydrogenation active metals component can be any means that those skilled in the art inform, such as, by carrier described in the solution impregnation with the compound containing described hydrogenation active metals component, the step of drying, roasting or not roasting can be carried out afterwards.
In the present invention, the described compound containing group vib metal be selected from they soluble compound in one or more.Such as, the compound containing molybdenum can be one or more in molybdenum oxide, molybdate, paramolybdate, preferably molybdenum oxide, ammonium molybdate, ammonium paramolybdate wherein; Tungstenic compound is selected from one or more in tungstates, metatungstate, ethyl metatungstate, preferably ammonium metatungstate, ethyl ammonium metatungstate wherein.
The described compound containing group VIII metal be selected from they soluble compound in one or more.Such as, the compound containing cobalt can be one or more in cobalt nitrate, cobalt acetate, basic cobaltous carbonate, cobalt chloride, is preferably cobalt nitrate, basic cobaltous carbonate; Nickel compound containing can be one or more in nickel nitrate, nickel acetate, basic nickel carbonate, nickel chloride, is preferably nickel nitrate, basic nickel carbonate.
According to the present invention, the solution of the compound containing described active component prepared by the various solvents that this area can be adopted to commonly use, as long as described compound can be dissolved in described solvent, forms the solution of stable homogeneous.Such as: described solvent can for water or carbon number be 1 ~ 5 alcohol (as: ethanol), be preferably water and/or ethanol, be more preferably water.
The method of described dipping can be the conventional various dipping methods in this area, such as, can be the saturated infusion process in hole.The present invention was not particularly limited for the time of described dipping and the number of times of dipping, as long as can guarantee that the amount with the active component of catalytic action on the catalyst that finally obtains meets concrete instructions for use.Usually, the time of described dipping can be 0.5 ~ 12 hour.
According to the present invention, the carrier for compound load being had described hydrogenation active metals component carries out dry method and condition is not particularly limited.Usually, the temperature of described drying can be 80 ~ 350 DEG C, is preferably 100 ~ 300 DEG C; The time of described drying can be 0.5 ~ 24 hour, is preferably 1 ~ 12 hour.
When catalyst after drying needs to carry out roasting, the present invention is not particularly limited described method of roasting and condition, can be conventional method and the condition of this area.Usually, the temperature of described roasting can be 350 ~ 650 DEG C, is preferably 400 ~ 500 DEG C; The time of described roasting can be 0.2 ~ 12 hour, is preferably 1 ~ 10 hour.Described roasting can be carried out in oxygen-containing atmosphere, also can carry out in an inert atmosphere.
According to preparation method provided by the invention, when in described catalyst also containing when being selected from the components such as phosphorus, also comprise the step introducing the components such as phosphorus, the introducing method of the components such as described phosphorus can pass through number of ways, such as, can be by directly mixing with the mixture of Alpha-alumina with hydrated alumina containing the compound of described auxiliary agent, shaping and roasting; Can be by the compound containing described auxiliary agent be mixed with containing the compound of hydrogenation active metals component after mixed solution with described carrier contact; Can also be by after independent for the compound containing auxiliary agent obtain solution with described carrier contact and roasting.When auxiliary agent and hydrogenation active metals introduce described carrier respectively, preferably first use containing auxiliary compound solution and described carrier contact and roasting, contact with the solution of the compound containing hydrogenation active metals component more afterwards, such as by the method for dipping, described sintering temperature is 250-600 DEG C, be preferably 350-500 DEG C, roasting time is 2-8 hour, is preferably 3-6 hour.
Protective agent provided by the invention is applicable to the protective agent carrying out adding man-hour as heavier hydrocarbon feeds; the heavy raw oil being particularly useful for doing high-sulfur height nitrogen height tenor inferior also comprises the protective agent of decompression residuum; this protective agent is loaded on hydrogenation catalyst top; effectively can solve the fouling of industrial hydrogenation plant bed, blocking, pressure drop excessive and be forced to the problem of stopping work, extend the service life of downstream hydrogenation catalyst.
Detailed description of the invention
The present invention is described further for example below.
Agents useful for same in example, except as expressly described, is chemically pure reagent.
Pressure mercury method (RIPP149-90) measures (Yang Cuiding etc., Petrochemical Engineering Analysis method, publishing house of the academy of sciences, the 1990, the 421-423 pages) such as the specific area of aluminium oxide shaping carrier, pore volume and pore size distributions.
BET nitrogen absorption under low temperature method (RIPP151-90) measures specific area, the pore volume and pore size distribution etc. (Yang Cuiding etc., Petrochemical Engineering Analysis method, publishing house of the academy of sciences, the 1990, the 424-426 page) of hydrated alumina.
Butt assay method, for getting appropriate amount of sample, in 600 DEG C of roasting temperature 3h, afterwards, calculates the mass percent of sample before sample and roasting after roasting, is the butt of this sample.
XRF method (RIPP132-90) is adopted to measure the content (Yang Cuiding etc., Petrochemical Engineering Analysis method, publishing house of the academy of sciences, 1990,371-375 page) of auxiliary agent and active metal component in catalyst.
Embodiment 1
(be available commercially from Yantai Heng Hui Chemical Co., Ltd., butt is 72 % by weight to take 200g hydrated alumina.Pore volume is 0.50 ml/g, and specific area is 290 meters
2/ gram, most probable bore dia is 7nm), 70 grams of alpha-aluminas (being formed for 6 hours by the hydrated alumina used in the present embodiment roasting at 1400 DEG C), after 9 grams of sesbania powder mixing and 15 grams of boraxs mix, by this mixture and concentration be at room temperature 4% ammonia spirit 220 milliliters mix, after mixing, kneading in double screw banded extruder is also extruded with the cylindrical orifice plate of φ 2.0mm, afterwards, wet bar through 120 DEG C of dryings after 4 hours in 850 DEG C of roastings 2 hours, obtain carrier T-1 of the present invention.Measure the specific surface of carrier T-1, can a few aperture, pore volume, pore size distribution, the results are shown in Table 1.
Embodiment 2
(be available commercially from the neat cyclopentadienyl catalyst factory in Zibo, butt is 68 % by weight to take 180g dry glue powder.Pore volume is 0.55 ml/g, and specific area is 278 meters
2/ gram, most probable bore dia is 8nm), 120 grams of alpha-aluminas (being available commercially from Beijing Shun Chuan Environmental Protection Technology Co., Ltd), 9 grams of sesbania powder mixing and 8 grams of boron oxides mix, add the aqueous solution 205 milliliters containing 10 grams of Boratexes afterwards, after mixing, in double screw banded extruder, kneading is also extruded with the cylindrical orifice plate of φ 2.0mm, afterwards, wet bar through 120 DEG C of dryings after 4 hours in 850 DEG C of roastings 2 hours, obtain carrier T-2 of the present invention.Measure the specific surface of carrier T-2, can a few aperture, pore volume, pore size distribution, the results are shown in Table 1.
Embodiment 3
(be available commercially from Yantai Heng Hui Chemical Co., Ltd., butt is 72 % by weight to take 150g dry glue powder.Pore volume is 0.50 ml/g, and specific area is 255 meters
2/ gram, most probable bore dia is 9nm), 150 grams of alpha-aluminas (with embodiment 2), 9 grams of sesbania powder, 9 grams of methylcellulose and 20 grams of boraxs mix, add the aqueous solution 205 milliliters mixing containing 35 grams of carbonic hydroammonium afterwards, shaping according to roller forming method after mixing, obtaining particle diameter is 5.5-6.5mm spheric granules.Wet bar through 120 DEG C of dryings after 4 hours in 800 DEG C of roastings 2 hours, obtain carrier T-3 of the present invention.Measure the specific surface of carrier T-3, can a few aperture, pore volume, pore size distribution, the results are shown in Table 1.
Embodiment 4
Take 260g dry glue powder (with embodiment 1), 140 grams of alpha-aluminas (with embodiment 1), 9 grams of sesbania powder, 9 grams of methylcellulose and 10 grams of antifungins mix, add afterwards containing 10 grams of boric acid 5% ammonia spirit 206 milliliters mixing, after mixing in double screw banded extruder kneading extruding with the cylindrical orifice plate of φ 2.0mm, wet bar through 120 DEG C of dryings after 4 hours in 800 DEG C of roastings 2 hours, obtain carrier T-4 of the present invention.Measure the specific surface of carrier T-4, can a few aperture, pore volume, the results are shown in Table 1.
Embodiment 5
Take 260g dry glue powder (with embodiment 2), 140 grams of alpha-aluminas (with embodiment 1), 9 grams of sesbania powder, 9 grams of methylcellulose mixing, add afterwards containing 7.5 grams, nitric acid, ammonium fluosilicate (is analyzed pure, Shanghai reagent three factory) aqueous solution 230 milliliters of 6 grams, mix rear extruded moulding, wet bar through 120 DEG C of dryings after 4 hours in 800 DEG C of roastings 2 hours, obtain carrier T-4 of the present invention.Measure the specific surface of carrier T-4, can a few aperture, pore volume, the results are shown in Table 1.
Comparative example 1
Take 300 grams of dry glue powders (with embodiment 3), 9 grams of sesbania powder, after mixing, add the solution 200 milliliters of mixed-formings containing 12 grams, nitric acid, wet bar through 120 DEG C of dryings after 4 hours in 850 DEG C of roastings 2 hours, obtain carrier D-1.Measure the specific surface of carrier D-1, can a few aperture, pore volume, the results are shown in Table 1.
Comparative example 2
(be available commercially from Chang Ling oil refining catalyst factory, butt is 65 % by weight to take 300 grams of dry glue powders.Pore volume is 0.8 ml/g, and specific area is 320 meters
2/ gram, most probable bore dia is 9nm), 9 grams of sesbania powder, add the solution 200 milliliters of mixed-formings containing 12 grams, nitric acid after mixing, wet bar through 120 DEG C of dryings after 4 hours in 850 DEG C of roastings 2 hours, obtain carrier D-2.Measure the specific surface of carrier D-2, can a few aperture, pore volume, the results are shown in Table 1.
Comparative example 3
((be available commercially from Chang Ling oil refining catalyst factory, butt is 65 % by weight to take dry glue powder.Pore volume is 0.8 ml/g, and specific area is 290 meters
2/ gram, most probable bore dia is 10nm)) 300 grams, add carbon black powder 24 grams, the mixing of 12 grams, sesbania powder, add containing concentration the aqueous solution 260 milliliters of the phosphoric acid 2.4 grams being 85 % by weight afterwards, kneading 15 minutes, double screw banded extruder is extruded into the butterfly bar of Φ 1.5mm, wet bar through 120 DEG C of dryings after 4 hours in 950 DEG C of roastings 2 hours, obtain carrier D-3.Measure the specific surface of carrier D-3, can a few aperture, pore volume, the results are shown in Table 1.
Comparative example 4
(be available commercially from Chang Ling oil refining catalyst factory, butt is 65 % by weight to take 300 grams of dry glue powders.Pore volume is 0.65 ml/g, and specific area is 288 meters
2/ gram, most probable bore dia is 9nm), 9 grams of sesbania powder and 20 grams of boraxs mix, and add the aqueous solution 360 milliliters of mixed-formings containing 35 grams of carbonic hydroammonium afterwards, wet bar through 120 DEG C of dryings after 4 hours in 950 DEG C of roastings 2 hours, obtain carrier D-4.Measure the specific surface of carrier D-4, can a few aperture, pore volume, the results are shown in Table 1.
Table 1
The result that table 1 provides shows, alumina support provided by the invention is except having larger most probable pore size, and pore size distribution mainly concentrates on bore dia is 6-10nm and 85-160nm, be namely 6-10nm and 85-160nm scope at bore dia is obvious bimodal distribution.
Embodiment 6
Get carrier 100 grams of rear drying and roastings of T1 dipping, in saturated leaching mode with containing 1.2g molybdenum oxide (containing MoO
399.9%) and the solution 82 milliliters dipping of 0.7g nickel nitrate (containing NiO25%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst TC-1 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Embodiment 7
Get carrier 100 grams of T2, in saturated leaching mode with containing 6.42g ammonium molybdate (containing MoO
382%) and the solution 80 milliliters dipping of 4.35g nickel nitrate (containing NiO51%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst TC-2 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Embodiment 8
Get carrier 20 grams of T3, in saturated leaching mode with containing 1.2g ammonium molybdate (containing MoO
382%) and the solution 15 milliliters dipping of 2.0g nickel nitrate (containing NiO25%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst TC-3 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Embodiment 9
Get carrier 20 grams of T4, in saturated leaching mode with containing 0.86g ammonium molybdate (containing MoO
382%) and the solution 16 milliliters dipping of 1.25g nickel nitrate (containing NiO25%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst TC-4 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Embodiment 10
Get carrier 20 grams of T5, in saturated leaching mode with containing 1.45g ammonium molybdate (containing MoO
382%) and the solution 13 milliliters dipping of 1.30g nickel nitrate (containing NiO25%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst TC-5 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Comparative example 5
Get carrier 20 grams of D4, in saturated leaching mode with containing 1.2g ammonium molybdate (containing MoO
382%) and the solution 12 milliliters dipping of 2.0g nickel nitrate (containing NiO25%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst DC-1 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Comparative example 6
Get carrier 20 grams of D1, in saturated leaching mode with containing 0.86g ammonium molybdate (containing MoO
382%) and the solution 11 milliliters dipping of 1.25g nickel nitrate (containing NiO25%), 120 DEG C of dryings 4 hours after dipping, 420 DEG C of roastings 3 hours guard catalyst DC-2 of the present invention.Wherein, the content of hydrogenation active metals component lists in table 2.
Table 2
Embodiment 11-12 illustrates the hydrogenation protecting agent performance that the invention provides carrier and prepare.
Embodiment 11
The medium-sized evaluating apparatus of 200ml evaluates protective agent TC-1, and raw materials used oil is for mixing slag faulty wax oil.Appreciation condition is reaction temperature 360 DEG C, hydrogen dividing potential drop 8.0MPa, volume space velocity 0.8h
-1, hydrogen to oil volume ratio 700:1.To evaluate after 2000h Fe deposition and coke content in sample analysis protective agent.The results are shown in table 3.
XRF method (XRF semi-quantitative analysis (B-U)) is adopted to measure element of Fe content in solid sample.
Infrared absorption method (RIPP106-90) is adopted to measure carbon deposit content in protective agent (Yang Cuiding etc., Petrochemical Engineering Analysis method, publishing house of the academy of sciences, the 1990,302nd page).
Embodiment 12
According to example 11 identical condition evaluating protective agent TC-2, to evaluate after 2000h Fe deposition and coke content in sample analysis protective agent.The results are shown in table 3.
Comparative example 7
According to the condition evaluating DC-1 identical with example 11.To evaluate after 2000h Fe deposition and coke content in sample analysis protective agent.The results are shown in table 3.
Comparative example 8
According to the condition evaluating DC-2 identical with example 11.To evaluate after 2000h Fe deposition and coke content in sample analysis protective agent.The results are shown in table 3.
Table 3
| Example number | Catalyst is numbered | Fe deposits total amount, w% | Carbon content, w% |
| Embodiment 11 | TC-1 | 1.85 | 11.0 |
| Embodiment 12 | TC-2 | 1.98 | 10.3 |
| Comparative example 7 | DC-1 | 0.37 | 17.87 |
| Comparative example 8 | DC-2 | 0.2 | 18.8 |
Above evaluation result shows, compared with the hydrogenation protecting agent provided with prior art, the protective agent prepared by carrier provided by the invention holds metal ability and anti-carbon deposition ability significantly improves.
Claims (16)
1. a hydrogenation protecting catalyst, containing the alumina support being selected from boron, silicon and fluorine auxiliary agent containing at least one with structure of double peak holes, characterize with mercury injection method, the pore volume of described carrier is 0.3-0.8 ml/g, and specific area is 70-220 rice
2/ gram, wherein, diameter is the 8-25% that the pore volume in 6-10nm hole accounts for total pore volume, and diameter is the 40-75% that the pore volume in 85-160nm hole accounts for total pore volume.
2. the catalyst according to 1, is characterized in that, the pore volume of described carrier is 0.4-0.7 ml/g, and specific area is 80-210 rice
2/ gram, wherein, diameter is the 10-20% that the pore volume in 6-10nm hole accounts for total pore volume, and diameter is the 45-70% that the pore volume in 85-160nm hole accounts for total pore volume.
3. the catalyst according to 1, is characterized in that, with the content of the described auxiliary agent boron of oxide basis, silicon for 0.1-8 % by weight, in the Oil repellent of element for 0.1-8 % by weight.
4. the catalyst according to 3, is characterized in that, with the content of the described auxiliary agent boron of oxide basis, silicon for 1-6 % by weight, in the Oil repellent of element for 1-6 % by weight.
5. the catalyst according to 4, is characterized in that, with the content of the described auxiliary agent boron of oxide basis, silicon for 1-4 % by weight, in the Oil repellent of element for 1-4 % by weight.
6. the catalyst according to 1, it is characterized in that, hydrogenation active metals component in described catalyst is selected from least one metal component of group VIII and at least one metal component of group VIB, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is greater than 0 to being less than or equal to 4 % by weight, and the content of metal component of group VIB is greater than 0 to being less than or equal to 10 % by weight.
7. the catalyst according to 6, it is characterized in that, described metal component of group VIII is selected from cobalt and/or nickel, metal component of group VIB is selected from molybdenum and/or tungsten, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is 1-3 % by weight, and the content of metal component of group VIB is 3-6 % by weight.
8. the preparation method of the hydrogenation activity guard catalyst according to 1, what comprise that preparation has a structure of double peak holes is selected from boron containing at least one, the alumina support of silicon and fluorine auxiliary agent, the preparation method of described carrier comprises being mixed with a kind of Alpha-alumina by a kind of hydrated alumina and introducing in the mixture and contains at least one and be selected from boron, the compound of silicon and fluorine auxiliary agent, shaping, dry also roasting, sintering temperature is 750-1000 DEG C, roasting time is 1-10 hour, wherein, in the mixing ratio of the hydrated alumina of butt and Alpha-alumina for 15-70:30-85, the pore volume of described hydrated alumina is 0.3-1.1 ml/g, specific surface is 150-350 rice
2/ gram, most probable bore dia 5-20nm.
9. the method according to 8, it is characterized in that, described sintering temperature is 800-950 DEG C, roasting time is 2-8 hour, wherein, in the mixing ratio of the hydrated alumina of butt and Alpha-alumina for 30-70:30-70, the pore volume of described hydrated alumina is 0.35-1.0 ml/g, and specific surface is 150-300 rice
2/ gram, most probable bore dia 6-15nm.
10. the method according to 8 or 9, is characterized in that, described hydrated alumina is selected from boehmite.
11. methods according to 8, it is characterized in that, with described carrier for benchmark, make the content of boron, silicon in final carrier for 0.1-8 % by weight with the introduction volume of the described auxiliary agent boron of oxide basis, silicon, make the content of fluorine in final carrier for 0.1-8 % by weight in the introduction volume of the fluorine of element.
12. methods according to 11, is characterized in that, make the content of boron, silicon in final carrier for 1-6 % by weight with the introduction volume of the described auxiliary agent boron of oxide basis, silicon, make the content of fluorine in final carrier for 1-6 % by weight in the introduction volume of the fluorine of element.
13. methods according to 12, is characterized in that, make the content of boron, silicon in final carrier for 1-4 % by weight with the introduction volume of the described auxiliary agent boron of oxide basis, silicon, make the content of fluorine in final carrier for 1-4 % by weight in the introduction volume of the fluorine of element.
14. methods according to 8, it is characterized in that, described method is included in supported on carriers hydrogenation active metals component, the described method in supported on carriers hydrogenation active metals component is infusion process, comprise preparation contain the solution of the compound of hydrogenation active metals and use this solution impregnating carrier, carry out drying afterwards, roasting or not roasting, described hydrogenation active metals component is selected from the metal component of at least one group VIB and the metal component of at least one the VIIIth race, be benchmark with oxide basis and with catalyst, the consumption of the concentration of the described compound containing hydrogenation active metals in described solution and described solution makes the content of the metal component of the group VIB in final catalyst be greater than 0 to being less than or equal to 10 % by weight, the content of the metal component of described VIIIth race is greater than 0 to being less than or equal to 4 % by weight, described drying condition comprises: temperature is 100-250 DEG C, and the time is 1-10 hour, described roasting condition comprises: temperature is 360-500 DEG C, and the time is 1-10 hour.
15. methods according to 14, it is characterized in that, the metal component of described group VIB is selected from molybdenum and/or tungsten, the metal component of the VIIIth race is selected from cobalt and/or nickel, be benchmark with oxide basis and with catalyst, the described compound containing hydrogenation active metals makes the content of the metal component of the group vib in final catalyst be 3-6 % by weight in the concentration of described solution and the consumption of described solution, and the content of the metal component of the VIIIth race is 1-3 % by weight; Described drying condition comprises: temperature is 100-140 DEG C, and the time is 1-6 hour; Described roasting condition comprises: temperature is 360-450 DEG C, and the time is 2-6 hour.
The application of hydrogenation activity guard catalyst in hydrocarbon oil hydrogenation process in 16. claim 1-7 described in any one.
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Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114433245A (en) * | 2020-10-30 | 2022-05-06 | 中国石油化工股份有限公司 | Catalyst carrier, hydrogenation catalyst and hydrogenation modification method of heavy distillate oil |
| CN114507546A (en) * | 2021-11-25 | 2022-05-17 | 宁波中金石化有限公司 | Inferior heavy oil processing method |
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| JPH03273092A (en) * | 1990-03-22 | 1991-12-04 | Nippon Oil Co Ltd | Catalyst for hydrogenation of residual oil |
| CN1289825A (en) * | 1999-09-29 | 2001-04-04 | 中国石油化工集团公司 | Carrier of hydrogenating catalyst for heavy oil and its preparing process |
| CN1488441A (en) * | 2002-10-10 | 2004-04-14 | 中国石油化工股份有限公司 | Method for preparing alumina supporter |
| CN1782031A (en) * | 2004-11-30 | 2006-06-07 | 中国石油化工股份有限公司 | Slag oil hydro-demetallization catalyst and its preparing method |
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2013
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| JPH03273092A (en) * | 1990-03-22 | 1991-12-04 | Nippon Oil Co Ltd | Catalyst for hydrogenation of residual oil |
| CN1289825A (en) * | 1999-09-29 | 2001-04-04 | 中国石油化工集团公司 | Carrier of hydrogenating catalyst for heavy oil and its preparing process |
| CN1488441A (en) * | 2002-10-10 | 2004-04-14 | 中国石油化工股份有限公司 | Method for preparing alumina supporter |
| CN1782031A (en) * | 2004-11-30 | 2006-06-07 | 中国石油化工股份有限公司 | Slag oil hydro-demetallization catalyst and its preparing method |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
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| CN114433245A (en) * | 2020-10-30 | 2022-05-06 | 中国石油化工股份有限公司 | Catalyst carrier, hydrogenation catalyst and hydrogenation modification method of heavy distillate oil |
| CN114433245B (en) * | 2020-10-30 | 2023-12-12 | 中国石油化工股份有限公司 | Catalyst carrier, hydrogenation catalyst and hydrogenation modification method of heavy distillate |
| CN114507546A (en) * | 2021-11-25 | 2022-05-17 | 宁波中金石化有限公司 | Inferior heavy oil processing method |
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| CN104368352B (en) | 2016-10-26 |
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