CN104368395A - Hydrogenation asphaltene removal catalyst and preparation and use thereof - Google Patents
Hydrogenation asphaltene removal catalyst and preparation and use thereof Download PDFInfo
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- CN104368395A CN104368395A CN201310353863.2A CN201310353863A CN104368395A CN 104368395 A CN104368395 A CN 104368395A CN 201310353863 A CN201310353863 A CN 201310353863A CN 104368395 A CN104368395 A CN 104368395A
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Abstract
The invention discloses a hydrogenation asphaltene removal catalyst and preparation and use thereof, the hydrogenation asphaltene removal catalyst comprises a halogen-containing dual-peak pore alumina carrier which is characterized by the mercury injection method, the carrier pore volume is 0.6-1.4 ml / g, the specific surface area is 80-400 m <2> / g, the volume of the pore with the diameter of 5-20nm accounts for 30-55% of the total pore volume, and the volume of the pore with the diameter of 100-300nm accounts for 15-45% of the total pore volume. Compared with the prior art, the catalyst has better hydrogenation asphaltene and metal removal performances when used in residual oil hydrogenation treatment.
Description
Technical field
The present invention relates to a kind of hydrogenation diasphaltene catalyst and preparation and application thereof.
Background technology
Carry out deep processing to the mink cell focus comprising residual oil to be not only conducive to improving the utilization rate of crude oil, alleviate the nervous trend of energy supply, can also environmental pollution be reduced simultaneously, reach the clean utilization of the energy.Compared with distillate, containing a large amount of macromolecular reaction things such as asphalitine, colloid in mink cell focus, and the heteroatomic compound such as sulphur, nitrogen, oxygen in mink cell focus and the heavy metal such as nickel and vanadium and condensed-nuclei aromatics major part concentrate in asphalitine, these impurity and heavy metal can pollute corresponding catalyst in follow-up process, and thus bitum hydro-conversion is a critical step in residual hydrogenation process.And in bitum conversion and subtractive process, need according to bitum characteristic, select activity high and the catalyst of the function admirable of good stability.
For the hydrogenation catalyst of diasphaltene, its pore-size distribution is of great significance catalyst performance tool.Bitum molecular size is about tens of to hundreds of nanometer, if the spacing of catalyst active center is less than asphaltene molecules, then asphaltene molecules is difficult to be contacted with the activated centre of catalyst by diffusion, and be mainly adsorbed on outer surface or the aperture of catalyst, along with the carrying out of reaction can only form coke because of thermal condensation, cause catalysqt deactivation.Macroporous catalyst is conducive to bitum removing, but the aperture of catalyst and specific surface negative correlation each other, the catalyst that namely average pore size is large, its specific area is just little.Therefore in order to take into account this character, catalyst needs rational pore size distribution.
The weak point of existing Heavy oil hydrogenation catalyst is its S, N removal efficiency, can not reaches good coupling between heavy metal removing rate and asphaltene removal, such as, often S, N removal efficiency and asphaltene removal are not high to remove the high catalyst of metal active.The reason producing problems is very complicated.First be raw material, in residual oil, the feature of each component is that molecular weight is large, and complex structure, saturation degree low (armaticity is high), S, N content are high.And beyond sulphur removal, the overwhelming majority of impurity again more to be present in asphalitine, therefore for removing this type of S, N, the conversion (comprising saturated, open loop and hydrogenolysis etc.) of appropriateness must be carried out to asphaltene molecules.Next is catalyst.In prior art, having the catalyst being suitable for carrying out this type of reaction aperture is guard catalyst and catalyst for demetalation, such as:
A kind of disclosed in CN1267537C have Hydrodemetalation catalyst of lower carbon deposition quantity and greater activity and preparation method thereof.
A kind of residuum hydrogenating and metal-eliminating catalyst disclosed in CN1796500A, the carrier that this catalyst has a double-hole by a kind of and load molybdenum on this carrier and/or tungsten and cobalt and/or nickel metal component form.The preparation method of carrier that catalyst uses comprise a kind of precursor of aluminium oxide is mixed with the nitrogen-containing compound beyond a kind of deacidification, shaping and roasting.
Catalyst for heavy oil fixed bed hydrogenating treatment and preparation method etc. disclosed in CN1233795C.
But the asphaltene removal of these catalyst is general lower.
Summary of the invention
The technical problem to be solved in the present invention be to provide a kind of newly, there is the better catalyst of hydrogenation diasphaltene performance, the preparation method of this catalyst and application.
The present invention relates to following content:
1. a hydrogenation diasphaltene catalyst, containing the halogen-containing alumina support with structure of double peak holes, characterize with mercury injection method, the pore volume of described carrier is 0.6-1.4 ml/g, and specific area is 80-400 rice
2/ gram, diameter is the 30-55% that the pore volume in 5-20nm hole accounts for total pore volume, and diameter is the 15-45% that the pore volume in 100-300nm hole accounts for total pore volume.
2. the catalyst according to 1, is characterized in that, the pore volume of described carrier is 0.7-1.3 ml/g, and specific area is 100-300 rice
2/ gram, diameter is the 35-50% that the pore volume in 5-20nm hole accounts for total pore volume, and diameter is the 20-40% that the pore volume in 100-300nm hole accounts for total pore volume.
3. the catalyst according to 1, is characterized in that, described halogen is selected from fluorine and chlorine, is benchmark in element and with carrier, and the content of described halogen is 0.1-6 % by weight.
4. the catalyst according to 3, is characterized in that, described halogen is fluorine, is benchmark in element and with carrier, and the content of described halogen is 0.3-4 % by weight.
5. the catalyst according to 4, is characterized in that, is benchmark in element and with carrier, and the content of described halogen is 0.5-2.5 % 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 group vib metal component, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is greater than 0.8 to being less than or equal to 3 % by weight, and the content of metal component of group VIB is greater than 3 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, group vib metal component 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 1-2 % by weight, and the content of metal component of group VIB is 4-8 % by weight.
8. the preparation method of catalyst according to 1, comprise the halogen-containing alumina support that preparation has structure of double peak holes, the preparation method of described carrier comprises and mix with a kind of modifier PC of the hydrated alumina containing boehmite by hydrated alumina PA and PB containing boehmite and to introduce halogen-containing compound, shaping, dry also roasting in the mixture, wherein, the Mixing ratio by weight of described PA, PB and PC is 20-60:20-50:5-50, the κ value of PC is 0 to being less than or equal to 0.9, described κ=DI
2/ DI
1, DI
1for the sour peptization index of PC hydrated alumina before modified, DI
2for the sour peptization index of described PC.
9. the method according to 8, is characterized in that, the Mixing ratio by weight of described PA, PB and PC is 30-50:35-50:10-30; The k value of described PC is 0 to being less than or equal to 0.6; The pore volume of the described hydrated alumina PA containing boehmite is 0.75-1 ml/g, and specific surface is 200-450 rice
2/ gram, can and bore dia 3-10nm; The pore volume of the described hydrated alumina PB containing boehmite is 0.9-1.4 ml/g, and specific surface is 100-350 rice
2/ gram, can and bore dia be greater than 10 to being less than or equal to 30nm; Described halogen is selected from fluorine and chlorine, is benchmark in element and with carrier, and the introduction volume of described halogen-containing compound makes the content of halogen in final carrier be 0.1-6 % by weight.
10. the method according to 9, is characterized in that, the pore volume of the described hydrated alumina PA containing boehmite is 0.80-0.95 ml/g, and specific surface is 200-400 rice
2/ gram, can and bore dia 5-10nm; The pore volume of the described hydrated alumina PB containing boehmite is 0.95-1.3 ml/g, and specific surface is 120-300 rice
2/ gram, can and bore dia be greater than 10 to being less than or equal to 25nm; Described halogen is fluorine, is benchmark in element and with carrier, and the introduction volume of described halogen-containing compound makes the content of halogen in final carrier be 0.3-4 % by weight.
11. catalyst according to 10, it is characterized in that, be benchmark in element and with carrier, and the introduction volume of described halogen-containing compound makes the content of halogen in final carrier be 0.5-2.5 % by weight.
12. methods according to 8 or 9, it is characterized in that, described PC is 80-300 object particle.
13. methods according to 12, it is characterized in that, described PC is 100-200 object particle.
14. methods according to 8, it is characterized in that, the condition of described drying comprises: temperature is 40-350 DEG C, and the time is 1-24 hour, and the condition of described roasting comprises: temperature is for being greater than 500 to being less than or equal to 1200 DEG C, and the time is 1-8 hour.
15. methods according to 14, it is characterized in that, the condition of described drying comprises: temperature is 100-200 DEG C, and the time is 2-12 hour, and the condition of described roasting comprises: temperature is for being greater than 800 to being less than or equal to 1000 DEG C, and roasting time is 2-6 hour.
16. methods according to 8, it is characterized in that, by shaping, dry for the described hydrated alumina containing boehmite by one of hydrated alumina method being modified as PC containing boehmite, afterwards its all or part of carrying out is ground, sieves, the condition of described drying comprises: temperature is 40-350 DEG C, and the time is 1-24 hour; Two of method is article shaped roastings method one obtained, and sintering temperature is for being greater than 350 to being less than or equal to 1400 DEG C, and roasting time is 1-8 hour, afterwards its all or part of carrying out is ground, is sieved; Three of method is dodged by the hydrated alumina containing boehmite to do, and dodge dry temperature for being greater than 150 to being less than or equal to 1400 DEG C, flash-off time is 0.05-1 hour; Four of method is mixed to get one or more in two and the modifier that obtains with three of method of one of method, method.
17. methods according to 16, it is characterized in that, the condition of the drying in described method one comprises: temperature is 100-200 DEG C, and the time is 2-12 hour; Method two in sintering temperature be 500-1200 DEG C, roasting time is 0.1-6 hour; Method three in sudden strain of a muscle to do temperature be 200-1000 DEG C, flash-off time is 0.1-0.5 hour.
18. methods according to 16, is characterized in that, described PC is 80-300 object particle in the modifier of hydrated alumina containing boehmite.
19. methods according to 18, is characterized in that, described PC is 100-200 object particle in the modifier of hydrated alumina containing boehmite.
20. methods according to 8, it is characterized in that, be included in described 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 described compound containing hydrogenation active metals makes the content of the metal component of the group VIB in final catalyst be greater than 3 to being less than or equal to 10 % by weight in the concentration of described solution and the consumption of described solution, the content of the metal component of described VIIIth race is greater than 0.8 to being less than or equal to 3 % 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.
21. methods according to 20, 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 4-8 % 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 1-2 % 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 catalyst in 22. claim 1-7 described in any one in hydrocarbon oil hydrogenation process.
According to catalyst provided by the invention, require that carrier wherein can be made into the various article shaped being easy to operate depending on different, such as spherical, cellular, nest like, tablet or bar shaped (clover, butterfly, cylindrical etc.).Wherein, be conventional method by the method for described PA, PB and PC mixing, such as, PA, PB and PC of powder dropped in stirring-type batch mixer according to ingredient proportion and mixes.The method introducing halogen-containing compound in described PA, PB and PC mixture is conventional method, such as, can be directly be mixed in aforesaid PA, PB and PC mixed process by the halogen-containing compound of aequum.
Concrete prepare in the embodiment of carrier at one, the method introducing halogen-containing compound in the mixture of described PA, PB and PC is that halogen-containing compound is mixed with the aqueous solution, this aqueous solution is mixed into while described PA, PB and PC mixing or again this aqueous solution is mixed into after described PA, PB and PC mixing, aftershaping, dry and roasting.Described halogen-containing compound can be one or more in arbitrary halogen-containing water soluble compound.Such as fluorochemical can be selected from hydrofluoric acid, one in ammonium fluoride and composition thereof.
In the present invention, describedly shapingly can to carry out according to a conventional method, such as, a kind of method in spin, compressing tablet and extruded moulding or the combination of several 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.
After sour peptization index D I in the preparation of described carrier refers to that the hydrated alumina containing boehmite adds nitric acid by certain sour aluminum ratio, within certain reaction time by the hydrated alumina containing boehmite of peptization with Al
2o
3the percentage of meter, DI=(1-W
2/ W
1) × 100%, W
1and W
2be respectively intend thin water aluminium and acid reaction front and with acid reaction after with Al
2o
3the weight of meter.
The mensuration of DI comprises: (calcination base content refers to quantitative boehmite in 600 DEG C of roastings 4 hours calcination base (also referred to as the butt) content of hydrated alumina (1) measuring containing boehmite, its ratio burning rear weight and burn front weight, be expressed as a percentage), count a; (2) take the hydrated alumina W containing boehmite with assay balance
0gram, W
0amount meet with Al
2o
3the W of meter
1be 6 grams of (W
1/ a=W
0), take deionized water W gram, W=40.0-W
0, under stirring, the hydrated alumina containing boehmite taken and deionized water are added in beaker and mix; With 20mL pipette pipette 20mL, concentration is the dilute nitric acid solution of 0.74N, is joined by this acid solution in the beaker of step (2), stirs lower reaction 8 minutes; (4) step (3) reacted slurries are carried out centrifugation in centrifuges, inserted by sediment in the crucible of having weighed, afterwards, by it in 125 DEG C of dryings 4 hours, in Muffle furnace, 850 DEG C of roastings 3 hours, weigh and obtain calcination sample size W
2gram; (5) according to formula DI=(1-W
2/ W
1) × 100% calculates.
Under being enough to make final carrier meet the prerequisite of application claims, the present invention does not specially require described hydrated alumina PA and PB containing boehmite, it can be boehmite prepared by any prior art, also can be the mixture of boehmite and other hydrated alumina, other hydrated alumina described be selected from one or more in a Water oxidize aluminium, gibbsite and amorphous hydrated aluminium oxide.
In a detailed description of the invention, the described preferred pore volume of hydrated alumina PA containing boehmite is 0.75-1 ml/g, and specific surface is 200-450 rice
2/ gram, can and bore dia 3-10nm, preferably pore volume is 0.80-0.95 ml/g further, and specific surface is 200-400 rice
2/ gram, can and bore dia 5-10nm; The described preferred pore volume of hydrated alumina PB containing boehmite is 0.9-1.4 ml/g, and specific surface is 100-350 rice
2/ gram, can and bore dia be greater than 10 to being less than or equal to 30nm, preferably pore volume is 0.95-1.3 ml/g further, and specific surface is 120-300 rice
2/ gram, can and bore dia be greater than 10 to being less than or equal to 25nm.
In the present invention, the pore volume of the hydrated alumina containing boehmite, specific area and can and aperture, be that the described hydrated alumina containing boehmite after 4 hours in 600 DEG C of roastings, is characterized by BET N2 adsorption and obtains.
In further preferred embodiment, characterize with X diffraction, the boehmite content in described hydrated alumina PA and PB containing boehmite is not less than 50%, is more preferably not less than 60%.
The present inventor is surprised to find, hydrated alumina containing boehmite is heat-treated and obtains modifier PC, relative to the original hydrated alumina containing boehmite, the peptization index of modifier PC changes, by this modifier and PA and PB mixed-forming, dry and after roasting, the carrier obtained has obvious bimodal pore distribution.Particularly by 80-300 object particle wherein, preferred 100-200 object particle and PA and PB mixed-forming, dry and after roasting, the carrier obtained bimodal in each unimodal pore size distribution concentrated especially.Here, described 80-300 object particle, preferred 100-200 object particle refers to that described modifier is through sieve (step comprising fragmentation or grinding if desired), its screening thing (screenings) meets 80-300 object particle, the percentage (by weight) that preferred 100-200 object particle accounts for total amount is not less than 60%, is preferably not less than 70% further.Here the hydrated alumina containing boehmite can be boehmite prepared by any prior art, also can be the mixture of boehmite and other hydrated alumina, other hydrated alumina described be selected from one or more in a Water oxidize aluminium, gibbsite and amorphous hydrated aluminium oxide.In a preferred embodiment, described PC is the modifier of PA and/or PB.
In the present invention, the Mixing ratio by weight of described PA, PB and PC refers to the ratio of the shared parts by weight of PA, PB and PC difference in the mixture of every hundred parts of described PA, PB and PC.Wherein, PA:PB:PC is preferably 20-60:20-50:5-50, more preferably 30-50:35-50:10-30.
In the present invention, described PC conveniently can be obtained by following method:
Below, the method for PC is obtained with described PA and PB for initiation material illustrates.
(1) obtain PC based on drying, comprise and prepare in regular oxidation alumina supporter process by hydrated alumina PA and/or PB containing boehmite is shaping according to a conventional method, the tailing of drying by-product, such as: in extruded moulding, bar shaped article shaped is at tailing (being called dry waste material traditionally) that is dry, integer process by-product, this tailing is milled, sieves and obtain PC.
(2) obtain based on roasting, comprise and prepare in regular oxidation alumina supporter process by hydrated alumina PA and/or PB containing boehmite is shaping according to a conventional method, through the tailing (being called roasting waste material traditionally) of roasting by-product, such as, in roller forming, the tailing of spheric granules by-product in roasting process, mills this tailing, sieves and obtain PC; Or directly PA and/or PB is dodged dry obtaining, when directly dodging dry by PA and/or PB, flash-off time is preferably 0.05-1 hour, more preferably 0.1-0.5 hour.
(3) two or more be mixed to get in the modifier PC obtained based on preceding method.When adopting mixed method to obtain C, the mixed proportion of the modifier PC that aforementioned several method obtains respectively is not limited.
According to catalyst provided by the invention, hydrogenation active metals component is wherein selected from least one metal component of group VIII and at least one group vib metal component, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is greater than 0.8 to being less than or equal to 3 % by weight, be preferably 1-2 % by weight, the content of metal component of group VIB is greater than 3 to being less than or equal to 10 % by weight, is preferably 4-8 % by weight.
Be enough under the prerequisite that described hydrogenation active metals component is carried on described carrier, the present invention is not particularly limited described carrying method, preferred method is infusion process, comprises the dipping solution of preparation containing the compound of described metal, afterwards with the carrier described in this solution impregnation.Described dipping method is conventional method, such as, can be excessive immersion stain, hole saturation infusion process.One or more in the described soluble compound be selected from containing the metal component compound being selected from VI B race in them, as one or more in molybdenum oxide, molybdate, paramolybdate, preferably molybdenum oxide, ammonium molybdate, ammonium paramolybdate wherein; One or more in tungstates, metatungstate, ethyl metatungstate, preferably ammonium metatungstate, ethyl ammonium metatungstate wherein.Described containing the compound being selected from VIII race's metal component be selected from their soluble compound one or more, as one or more in the soluble complexes of cobalt nitrate, cobalt acetate, basic cobaltous carbonate, cobalt chloride and cobalt, be preferably cobalt nitrate, basic cobaltous carbonate; One or more in the soluble complexes of nickel nitrate, nickel acetate, basic nickel carbonate, nickel chloride and nickel, are preferably nickel nitrate, basic nickel carbonate.
According to catalyst provided by the invention, can also the invention provides containing any impact the addO-on therapy that catalyst performance maybe can improve the catalytic performance of catalyst provided by the invention.As contained the addO-on therapy such as phosphorus, be benchmark with oxide basis and with catalyst, the content of described addO-on therapy is no more than 10 % by weight, is preferably 0.1-4 % by weight.
When in described catalyst also containing the addO-on therapy such as phosphorus time, the introducing method of described addO-on therapy can be arbitrary method, as can be by containing as described in the component such as phosphorus compound directly with as described in boehmite mix, shaping and roasting; Can be flood described carrier after the compound containing components such as described phosphorus and the compound containing hydrogenation active metals component are mixed with mixed solution; Can also be flood described carrier and roasting by after independent for the compound containing components such as phosphorus obtain solution.When the addO-on therapy such as phosphorus and hydrogenation active metals introduce described carrier respectively, preferably first use carrier described in the solution impregnation containing described addO-on therapy compound and roasting, afterwards again by the solution impregnation containing hydrogenation active metals component composition.Wherein, described sintering temperature is 400-600 DEG C, and be preferably 420-500 DEG C, roasting time is 2-6 hour, is preferably 3-6 hour.
According to hydrocarbon ils provided by the present invention (comprising residual oil) hydrotreating method, the reaction condition of the hydrotreatment of described hydrocarbon ils is not particularly limited, in a preferred embodiment, described hydrotreatment reaction condition is: reaction temperature 300-550 DEG C, preferred 330-480 DEG C further, hydrogen dividing potential drop 4-20 MPa, further preferred 6-18 MPa, volume space velocity 0.1-3.0 hour
-1, preferred 0.15-2 hour further
-1, hydrogen to oil volume ratio 200-2500, further preferred 300-2000.
The device of described hydrogenation reaction can carry out in the reactor that described feedstock oil is reacted with described catalyst exposure at hydrotreating reaction conditions in any being enough to, and such as, at described fixed bed reactors, carries out in moving-burden bed reactor or fluidized bed reactor.
According to the conventional method in this area, described hydrotreating catalyst before the use, usually can be in presence of hydrogen, presulfurization is carried out with sulphur, hydrogen sulfide or sulfur-bearing raw material at the temperature of 140-370 DEG C, this presulfurization can be carried out outside device also can be In-situ sulphiding in device, and the active metal component of its load is converted into metal sulfide component.
Catalyst provided by the invention can be used alone, and also can use with other catalyst combination, this catalyst be particularly suitable for heavy oil particularly poor residuum carry out hydrotreatment, to provide qualified feedstock oil for subsequent technique (as catalytic cracking process).Compared with prior art, catalyst provided by the invention is for having better hydrogenation diasphaltene and demetalization performance during residual hydrocracking.
Detailed description of the invention
The present invention will be further described for the following examples, but therefore should not be interpreted as limitation of the invention.
Agents useful for same in example, except as expressly described, is chemically pure reagent.
The boehmite used below in an example comprises:
PA-1: (pore volume is 0.9 ml/g to the dry glue powder that Chang Ling catalyst branch company produces, and specific surface is 280 meters
2/ gram, can and bore dia 8.5nm.Butt is 73%, and wherein boehmite content is 68%, and gibbsite content is 5 % by weight, and surplus is amorphous alumina, DI value 34.6).
PA-2: (pore volume is 0.9 ml/g to the dry glue powder of the limited production of the neat cyclopentadienyl catalyst in Zibo, and specific surface is 290 meters
2/ gram, can and bore dia 8.3nm.Butt is 73%, and wherein boehmite content is 68%, and gibbsite content is 5 % by weight, and surplus is amorphous alumina, DI value 33.2).
PB-1: (pore volume is 1.2 mls/g to the dry glue powder that Chang Ling catalyst branch company produces, and specific surface is 280 meters
2/ gram, can and bore dia 15.8nm.Butt is 73%, and wherein boehmite content is 68%, and gibbsite content is 5 % by weight, and surplus is amorphous alumina, DI value 15.8).
PB-2: (pore volume is 1.1 mls/g to the dry glue powder that Yantai Heng Hui Chemical Co., Ltd. produces, and specific surface is 260 meters
2/ gram, can and bore dia 12nm.Butt is 71%, and wherein boehmite content is 67%, and gibbsite content is 5 % by weight, and surplus is amorphous alumina, DI value 17.2).
Embodiment 1-10 illustrates PC of the present invention and preparation method thereof.
Embodiment 1
Take 1000 grams of PA-1, add the aqueous solution 1000 milliliters containing 10 milliliters, nitric acid (Tianjin chemical reagent three factory product) afterwards, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar was in 120 DEG C of dryings 4 hours, and obtain dried strip, by dried strip shaping, sieve, the dried strip material (being commonly referred to as industrially drying bar waste material) length being less than 2mm is milled, and sieves, gets wherein 100 ~ 200 mesh sieves and divide, obtain the modifier PC-A1 of PA-1.The k value of PC-A1 is in table 1.
Embodiment 2
Take 1000 grams of PA-1, add the aqueous solution 1000 milliliters containing 10 milliliters, nitric acid (Tianjin chemical reagent three factory product) afterwards, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar was in 120 DEG C of dryings 4 hours, and 800 DEG C of roastings 4 hours, obtain carrier, by carrier strip shaping, sieve, the carrier strip material (being commonly referred to as industrial carrier waste material) length being less than 2mm is milled, sieve, get wherein 100 ~ 200 mesh sieves and divide, obtain the modifier PC-A2 of PA-1.The k value of PC-A2 is in table 1.
Embodiment 3
Take 1000 grams of PA-2, dodge dry 6 minutes in 400 DEG C, obtain the modifier PC-A3 of PA-2.The k value of PC-A3 is in table 1.
Embodiment 4
The each 200 grams of mixing of the PC-A3 that the PC-A1 obtain embodiment 1 and embodiment 3 obtain, obtain the modifier PC-A4 of PA-1 and PA-2.The k value of PC-A4 is in table 1.
Embodiment 5
Take 1000 grams of PB-1, add the aqueous solution 1440 milliliters containing 10 milliliters, nitric acid (Tianjin chemical reagent three factory product) afterwards, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar was in 120 DEG C of dryings 4 hours, and 1200 DEG C of roastings 4 hours, obtain carrier, by carrier strip shaping, sieve, the carrier strip material (being commonly referred to as industrial carrier waste material) length being less than 2mm is milled, sieve, get wherein 100 ~ 200 mesh sieves and divide, obtain the modifier PC-B1 of PB-1.The k value of PC-B1 is in table 1.
Embodiment 6
Take 1000 grams of PB-2, dodge dry 10 minutes in 650 DEG C, obtain the modifier PC-B2 of PB-2.The k value of PC-B2 is in table 1.
Embodiment 7
Take 1000 grams of PB-2, add the aqueous solution 1440 milliliters containing 10 milliliters, nitric acid (Tianjin chemical reagent three factory product) afterwards, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar was in 120 DEG C of dryings 4 hours, and obtain dried strip, by dried strip shaping, sieve, the dried strip material (being commonly referred to as industrially drying bar waste material) length being less than 2mm is milled, and sieves, gets wherein 100 ~ 200 mesh sieves and divide, obtain the modifier PC-B3 of PB-2.The k value of PC-B3 is in table 1.
Embodiment 8
The each 200 grams of mixing of the PC-B2 that the PC-B1 obtain embodiment 5 and embodiment 6 obtain, obtain the modifier PC-B4 of PB-1 and PB-2.The k value of PC-B4 is in table 1.
Embodiment 9
150 grams of PC-B3 mixing that 100 grams of PC-A1 embodiment 1 obtained and embodiment 7 obtain, obtain the modifier PC-B5 of PA-1 and PB-2.The k value of PC-B5 is in table 1.
Embodiment 10
The each 150 grams of mixing of the PC-B1 that the PC-A3 obtain embodiment 3 and embodiment 5 obtain, obtain the modifier PC-B6 of PA-2 and PB-1.The k value of PC-B6 is in table 1.
Table 1
| Embodiment | Raw material | DI | k |
| 1 | PC-A1 | 10.0 | 0.29 |
| 2 | PC-A2 | 0.9 | 0.02 |
| 3 | PC-A3 | 3.6 | 0.11 |
| 4 | PC-A4 | 6.7 | 0.20 |
| 5 | PC-B1 | 0 | 0 |
| 6 | PC-B2 | 2.1 | 0.12 |
| 7 | PC-B3 | 5.3 | 0.31 |
| 8 | PC-B4 | 1.0 | 0.06 |
| 9 | PC-B5 | 7.0 | 0.29 |
| 10 | PC-B6 | 1.6 | 0.07 |
Embodiment 11-18 illustrates the preparation method of halogen-containing bimodal hole provided by the invention carrier.Comparative example 1-5 illustrates the preparation method of conventional catalyst carrier.
Embodiment 11
Take each 400 grams of PA-1 and PB-1, after 200 grams of raw material PC-A2 obtained with embodiment 2 mix, add the aqueous solution 1300 milliliters containing 10 milliliters, nitric acid (Tianjin chemical reagent three factory product), fluorinated ammonia 9.8g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 900 DEG C of roastings 3 hours, obtains carrier Z1.The character of carrier Z1 lists in table 2.
Embodiment 12
Take 300 grams of PA-2,200 grams of PB-2, after 500 grams of raw material PC-B2 obtained with embodiment 6 mix, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1300 milliliters of chloride containing ammonia 7.6g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 900 DEG C of roastings 3 hours, obtains carrier Z2.The character of carrier Z2 lists in table 2.
Embodiment 13
Take 500 grams of PA-2,300 grams of PB-2, after 200 grams of raw material PC-B4 obtained with embodiment 8 mix, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1300 milliliters of fluorinated ammonia 9.8g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 950 DEG C of roastings 3 hours, obtains carrier Z3.The character of carrier Z3 lists in table 2.
Comparative example 1
Take 500 grams of PA-2,500 grams of PB-2, add after mixing containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1300 milliliters of fluorinated ammonia 9.8g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 900 DEG C of roastings 3 hours, obtains carrier DZ1.The character of carrier DZ1 lists in table 2.
Comparative example 2
Take 400 grams of PA-1,600 grams of PB-1, add after mixing containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1300 milliliters of fluorinated ammonia 9.8g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 950 DEG C of roastings 3 hours, obtains carrier DZ2.The character of carrier DZ2 lists in table 2.
Embodiment 14
Take 250 grams of PA-1,500 grams of PB-1, after 250 grams of raw material PC-B5 obtained with embodiment 9 mix, add the aqueous solution 1300 milliliters containing 10 milliliters, nitric acid (Tianjin chemical reagent three factory product), fluorinated ammonia 19.6g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 1000 DEG C of roastings 3 hours, obtains carrier Z4.The character of carrier Z4 lists in table 2.
Embodiment 15
Take 350 grams of PA-2,350 grams of PB-2, after 300 grams of raw materials obtained with embodiment 10 mix, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1440 milliliters of fluorinated ammonia 19.6g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 1000 DEG C of roastings 3 hours, obtains carrier Z5.The character of carrier Z5 lists in table 2.
Embodiment 16
Take 200 grams of PA-1,600 grams of PB-1, after 200 grams of raw material PC-B1 obtained with embodiment 5 mix, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1440 milliliters of chloride containing ammonia 15.2g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 850 DEG C of roastings 3 hours, obtains carrier Z6.The character of carrier Z6 lists in table 2.
Embodiment 17
Take 200 grams of PA-1,600 grams of PB-1, after 200 grams of raw material PC-A4 obtained with embodiment 4 mix, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1440 milliliters of fluorinated ammonia 39.2g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 850 DEG C of roastings 3 hours, obtains carrier Z7.The character of carrier Z76 lists in table 2.
Embodiment 18
Take 200 grams of PA-1,600 grams of PB-1, after 200 grams of raw material PC-A2 obtained with embodiment 2 mix, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1440 milliliters of fluorinated ammonia 39.2g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 850 DEG C of roastings 3 hours, obtains carrier Z8.The character of carrier Z8 lists in table 2.
Comparative example 3
According to the method that patent CN1782031A embodiment 7 provides, plunger type bar extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 900 DEG C of roastings 3 hours, obtains carrier DZ3.The character of carrier DZ3 lists in table 2.
Comparative example 4
According to the method that patent CN1120971A embodiment 1 provides, plunger type bar extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 1000 DEG C of roastings 3 hours, obtains carrier DZ3.The character of carrier DZ3 lists in table 2.
Comparative example 5
Take 200 grams of PA-1,800 grams of PB-2, add containing nitric acid Tianjin chemical reagent three factory product) 10 milliliters, the aqueous solution 1300 milliliters of fluorinated ammonia 39.2g, double screw banded extruder is extruded into the butterfly bar of external diameter φ 1.4mm.Wet bar, in 120 DEG C of dryings 4 hours, obtains article shaped, by this article shaped 1000 DEG C of roastings 3 hours, obtains carrier DZ5.The character of carrier DZ5 lists in table 2.
Table 2
Can be seen by the result of table 2, compared with conventional method, the alumina support prepared by the method for the invention provides has obvious structure of double peak holes.
Embodiment 19-23 illustrates Catalysts and its preparation method provided by the invention.
Wherein, in catalyst, the content of active metal component adopts Xray fluorescence spectrometer to measure (all appts is Rigaku electric machine industry Co., Ltd. 3271 type Xray fluorescence spectrometer, and concrete grammar is shown in Petrochemical Engineering Analysis method RIPP133-90).
Embodiment 19
Get 200 grams of carrier Z1, with 210 milliliters containing MoO
367.9 grams per liters, molybdenum oxide and the basic cobaltous carbonate mixed solution of CoO 11.3 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst C1.Molybdenum oxide in catalyst C1 and the content of cobalt oxide list in table 3.
Comparative example 6
Get 200 grams of carrier DZ1, with 180 milliliters containing MoO
379.2 grams per liters, molybdenum oxide and the basic cobaltous carbonate mixed solution of CoO 13.2 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst DC1.Molybdenum oxide in catalyst DC1 and the content of cobalt oxide list in table 3.
Embodiment 20
Get 200 carrier Z2, with 200 milliliters containing MoO
353.1 grams per liters, molybdenum oxide and the basic nickel carbonate mixed solution of NiO 10.6 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst C2.Molybdenum oxide in catalyst C2 and the content of nickel oxide list in table 3.
Comparative example 7
Get 200 carrier DZ3, with 180 milliliters containing MoO
359.0 grams per liters, molybdenum oxide and the basic nickel carbonate mixed solution of NiO 11.8 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst DC2.Molybdenum oxide in catalyst DC2 and the content of nickel oxide list in table 3.
Embodiment 21
Get 200 grams of carrier Z3, with 205 milliliters containing MoO
378.5 grams per liters, ammonium molybdate and the nickel nitrate mixed solution of NiO 15.7 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst C3.Molybdenum oxide in catalyst C3 and the content of nickel oxide list in table 3.
Comparative example 8
Get 200 grams of carrier DZ4, with 180 milliliters containing MoO
387.2 grams per liters, molybdenum oxide and the basic nickel carbonate mixed solution of NiO 17.4 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst DC3.Molybdenum oxide in catalyst DC3 and the content of nickel oxide list in table 3.
Embodiment 22
Get 200 grams of carrier Z6, with 210 milliliters containing MoO
367.9 grams per liters, molybdenum oxide and the basic nickel carbonate mixed solution of NiO 11.3 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst C4.Molybdenum oxide in catalyst C4 and the content of nickel oxide list in table 3.
Embodiment 23
Get 200 grams of carrier Z8, with 200 milliliters containing MoO
382.8 grams per liters, molybdenum oxide and the basic cobaltous carbonate mixed solution of CoO 19.1 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst C5.Molybdenum oxide in catalyst C5 and the content of cobalt oxide list in table 3.
Comparative example 9
Get 200 grams of carrier DZ5, with 200 milliliters containing MoO
382.8 grams per liters, molybdenum oxide and the basic cobaltous carbonate mixed solution of CoO 19.1 grams per liter flood 1 hour, dry 2 hours in 120 DEG C, and 420 DEG C of roastings 3 hours, obtain catalyst DC4.Molybdenum oxide in catalyst DC4 and the content of cobalt oxide list in table 3.
Table 3
Embodiment 24-28
Embodiment 24-28 illustrates the residuum hydrogenating and metal-eliminating performance of catalyst provided by the invention.
The particle respectively catalyst C1, C2, C3, C4 and C5 being broken into diameter 2-3 millimeter loads reactor.Reaction condition is: reaction temperature 380 DEG C, hydrogen dividing potential drop 14 MPa, inductive coupling plasma emission spectrograph (ICP-AES) is adopted to measure the content (instrument is U.S. PE company PE-5300 type plasma quantometer, and concrete grammar is shown in Petrochemical Engineering Analysis method RIPP124-90) of nickel and vanadium in oil before and after hydrotreatment.Asphalt compound mensuration method is adopted to analyze oily studies on asphaltene mass fraction (concrete grammar is see SH/T0509-92) before and after hydrotreatment.Calculate asphalitine and metal removal rate according to the following formula:
The normal slag of Kuwait that feedstock oil is nickel content is 29.3ppm, content of vanadium is 83ppm, sulfur content is 4.7%, nitrogen content is 0.3%, carbon residue is 15.1%.
The activity data of each catalyst is in table 4.
Comparative example 10-13
According to demetallization per and the diasphaltene rate of method evaluation catalyst DC1, DC2, DC3 and DC4 of embodiment 24-28, the results are shown in Table 4.
Table 4
| Embodiment | Catalyst is numbered | Diasphaltene rate/% | Demetallization per/% |
| 24 | C1 | 85 | 77 |
| Comparative example 10 | DC1 | 64 | 70 |
| 25 | C2 | 89 | 71 |
| Comparative example 11 | DC2 | 62 | 63 |
| 26 | C3 | 90 | 75 |
| Comparative example 12 | DC3 | 75 | 70 |
| 27 | C4 | 91 | 76 |
| 28 | C5 | 92 | 81 |
| Comparative example 13 | DC4 | 80 | 76 |
Can be seen by table 4 result, in poor residuum hydroprocessing processes, will obviously be better than existing catalyst by the diasphaltene and metal removal activity that the invention provides catalyst, illustrate that this technological invention catalyst is more suitable for the processing process of poor residuum.
Claims (22)
1. a hydrogenation diasphaltene catalyst, containing the halogen-containing alumina support with structure of double peak holes, characterize with mercury injection method, the pore volume of described carrier is 0.6-1.4 ml/g, and specific area is 80-400 rice
2/ gram, diameter is the 30-55% that the pore volume in 5-20nm hole accounts for total pore volume, and diameter is the 15-45% that the pore volume in 100-300nm hole accounts for total pore volume.
2. the catalyst according to 1, is characterized in that, the pore volume of described carrier is 0.7-1.3 ml/g, and specific area is 100-300 rice
2/ gram, diameter is the 35-50% that the pore volume in 5-20nm hole accounts for total pore volume, and diameter is the 20-40% that the pore volume in 100-300nm hole accounts for total pore volume.
3. the catalyst according to 1, is characterized in that, described halogen is selected from fluorine and chlorine, is benchmark in element and with carrier, and the content of described halogen is 0.1-6 % by weight.
4. the catalyst according to 3, is characterized in that, described halogen is fluorine, is benchmark in element and with carrier, and the content of described halogen is 0.3-4 % by weight.
5. the catalyst according to 4, is characterized in that, is benchmark in element and with carrier, and the content of described halogen is 0.5-2.5 % 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 group vib metal component, be benchmark with oxide basis and with catalyst, the content of described VIII race's metal component is greater than 0.8 to being less than or equal to 3 % by weight, and the content of metal component of group VIB is greater than 3 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, group vib metal component 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 1-2 % by weight, and the content of metal component of group VIB is 4-8 % by weight.
8. the preparation method of catalyst according to 1, comprise the halogen-containing alumina support that preparation has structure of double peak holes, the preparation method of described carrier comprises and mix with a kind of modifier PC of the hydrated alumina containing boehmite by hydrated alumina PA and PB containing boehmite and to introduce halogen-containing compound, shaping, dry also roasting in the mixture, wherein, the Mixing ratio by weight of described PA, PB and PC is 20-60:20-50:5-50, the κ value of PC is 0 to being less than or equal to 0.9, described κ=DI
2/ DI
1, DI
1for the sour peptization index of PC hydrated alumina before modified, DI
2for the sour peptization index of described PC.
9. the method according to 8, is characterized in that, the Mixing ratio by weight of described PA, PB and PC is 30-50:35-50:10-30; The k value of described PC is 0 to being less than or equal to 0.6; The pore volume of the described hydrated alumina PA containing boehmite is 0.75-1 ml/g, and specific surface is 200-450 rice
2/ gram, can and bore dia 3-10nm; The pore volume of the described hydrated alumina PB containing boehmite is 0.9-1.4 ml/g, and specific surface is 100-350 rice
2/ gram, can and bore dia be greater than 10 to being less than or equal to 30nm; Described halogen is selected from fluorine and chlorine, is benchmark in element and with carrier, and the introduction volume of described halogen-containing compound makes the content of halogen in final carrier be 0.1-6 % by weight.
10. the method according to 9, is characterized in that, the pore volume of the described hydrated alumina PA containing boehmite is 0.80-0.95 ml/g, and specific surface is 200-400 rice
2/ gram, can and bore dia 5-10nm; The pore volume of the described hydrated alumina PB containing boehmite is 0.95-1.3 ml/g, and specific surface is 120-300 rice
2/ gram, can and bore dia be greater than 10 to being less than or equal to 25nm; Described halogen is fluorine, is benchmark in element and with carrier, and the introduction volume of described halogen-containing compound makes the content of halogen in final carrier be 0.3-4 % by weight.
11. catalyst according to 10, it is characterized in that, be benchmark in element and with carrier, and the introduction volume of described halogen-containing compound makes the content of halogen in final carrier be 0.5-2.5 % by weight.
12. methods according to 8 or 9, it is characterized in that, described PC is 80-300 object particle.
13. methods according to 12, it is characterized in that, described PC is 100-200 object particle.
14. methods according to 8, it is characterized in that, the condition of described drying comprises: temperature is 40-350 DEG C, and the time is 1-24 hour, and the condition of described roasting comprises: temperature is for being greater than 500 to being less than or equal to 1200 DEG C, and the time is 1-8 hour.
15. methods according to 14, it is characterized in that, the condition of described drying comprises: temperature is 100-200 DEG C, and the time is 2-12 hour, and the condition of described roasting comprises: temperature is for being greater than 800 to being less than or equal to 1000 DEG C, and roasting time is 2-6 hour.
16. methods according to 8, it is characterized in that, by shaping, dry for the described hydrated alumina containing boehmite by one of hydrated alumina method being modified as PC containing boehmite, afterwards its all or part of carrying out is ground, sieves, the condition of described drying comprises: temperature is 40-350 DEG C, and the time is 1-24 hour; Two of method is article shaped roastings method one obtained, and sintering temperature is for being greater than 350 to being less than or equal to 1400 DEG C, and roasting time is 1-8 hour, afterwards its all or part of carrying out is ground, is sieved; Three of method is dodged by the hydrated alumina containing boehmite to do, and dodge dry temperature for being greater than 150 to being less than or equal to 1400 DEG C, flash-off time is 0.05-1 hour; Four of method is mixed to get one or more in two and the modifier that obtains with three of method of one of method, method.
17. methods according to 16, it is characterized in that, the condition of the drying in described method one comprises: temperature is 100-200 DEG C, and the time is 2-12 hour; Method two in sintering temperature be 500-1200 DEG C, roasting time is 0.1-6 hour; Method three in sudden strain of a muscle to do temperature be 200-1000 DEG C, flash-off time is 0.1-0.5 hour.
18. methods according to 8 or 16, is characterized in that, described PC is 80-300 object particle in the modifier of hydrated alumina containing boehmite.
19. methods according to 18, is characterized in that, described PC is 100-200 object particle in the modifier of hydrated alumina containing boehmite.
20. methods according to 8, it is characterized in that, be included in described 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 described compound containing hydrogenation active metals makes the content of the metal component of the group VIB in final catalyst be greater than 3 to being less than or equal to 10 % by weight in the concentration of described solution and the consumption of described solution, the content of the metal component of described VIIIth race is greater than 0.8 to being less than or equal to 3 % 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.
21. methods according to 20, 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 4-8 % 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 1-2 % 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 catalyst in 22. claim 1-7 described in any one in hydrocarbon oil hydrogenation process.
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| JPH0295443A (en) * | 1988-09-30 | 1990-04-06 | Nippon Oil Co Ltd | Catalyst for hydrogenation treatment of residual oil |
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| 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 |
| CN1626625A (en) * | 2003-12-10 | 2005-06-15 | 中国石油化工股份有限公司 | Demetallization catalyst of addig hydrogen to residual oil and preparation method |
| CN101066530A (en) * | 2006-05-22 | 2007-11-07 | 林方 | Hydrodemetalizing catalyst and its prepn |
| CN101468322A (en) * | 2007-12-27 | 2009-07-01 | 中国石油化工股份有限公司 | Alumina supporter and preparation method thereof |
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2013
- 2013-08-14 CN CN201310353863.2A patent/CN104368395B/en active Active
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0295443A (en) * | 1988-09-30 | 1990-04-06 | Nippon Oil Co Ltd | Catalyst for hydrogenation treatment of residual oil |
| CN1120971A (en) * | 1994-10-19 | 1996-04-24 | 中国石油化工总公司抚顺石油化工研究院 | Prepn of alumina supporter |
| 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 |
| CN1626625A (en) * | 2003-12-10 | 2005-06-15 | 中国石油化工股份有限公司 | Demetallization catalyst of addig hydrogen to residual oil and preparation method |
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| CN101468322A (en) * | 2007-12-27 | 2009-07-01 | 中国石油化工股份有限公司 | Alumina supporter and preparation method thereof |
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