CN103480422B - There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method - Google Patents
There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method Download PDFInfo
- Publication number
- CN103480422B CN103480422B CN201210193753.XA CN201210193753A CN103480422B CN 103480422 B CN103480422 B CN 103480422B CN 201210193753 A CN201210193753 A CN 201210193753A CN 103480422 B CN103480422 B CN 103480422B
- Authority
- CN
- China
- Prior art keywords
- component
- catalyst
- carrier
- weight
- metallic element
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
Landscapes
- Catalysts (AREA)
Abstract
The invention provides a kind of Catalysts and its preparation method and the application with hydrogenation catalyst effect, this catalyst contains carrier and load at least one group VIII metallic element on the carrier and at least one group vib metallic element, wherein, described carrier is article shaped containing hydrated alumina or aluminium oxide article shaped, material forming containing at least one component A, at least one B component and at least one component C is obtained, described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether.Present invention also offers a kind of method for hydrotreating hydrocarbon oil, the method comprises under hydroprocessing conditions, by hydrocarbon ils and catalyst exposure provided by the invention.Catalyst of the present invention shows higher catalytic activity in the hydrotreatment of hydrocarbon ils.
Description
Technical field
The present invention relates to a kind of Catalysts and its preparation method and the application with hydrogenation catalyst effect, the invention still further relates to a kind of hydrotreating method.
Background technology
Hydrogen addition technology reduces one of impurity content, the major technique improving oil quality in oil product, and its core is hydrogenation catalyst.Conventional hydrogenation catalyst can by preparing the active component load with hydrogenation catalyst effect on porous support, and wherein, the most frequently used porous carrier is aluminium oxide article shaped.
The heavy-oil hydrogenation catalyst of RichardA.Kemp report adds in boehmite gel by the solution containing active metal component, then carry out extrusion molding, drying and roasting and prepare (RichardA.Kemp, CharlesT.Adam, AppliedCatalysisA:General, 134 (1996): 299-317).
The Hydrobon catalyst of D.Minoux report is by nickel nitrate and ammonium molybdate being mixed with boehmite, then carry out shaping, dry and roasting and prepare (D.Minoux, F.Diehl, P.Euzen, Jean-PierreJolivetb, EdmondPayen, StudiesinSurfaceScienceandCatalysis, 143 (2002): 767-775).
But along with environmental requirement increasingly stringent in world wide, various countries are day by day harsh to the quality requirement of vehicle fuel; Further, because petroleum resources reduce, oil property becomes and heavily becomes bad, and refinery has to process crude oil more inferior, therefore in the urgent need to having the hydrogenation catalyst of more high catalytic activity.
Summary of the invention
The object of the present invention is to provide a kind of there is hydrogenation catalyst effect Catalysts and its preparation method and application and hydrotreating method, catalyst according to the invention has the catalytic activity of raising.
A first aspect of the present invention provides a kind of catalyst with hydrogenation catalyst effect, this catalyst contains carrier and load at least one group VIII metallic element on the carrier and at least one group vib metallic element, wherein, described carrier is aluminium oxide article shaped or the article shaped containing hydrated alumina, material forming containing at least one component A, at least one B component and at least one component C is obtained, described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether.
A second aspect of the present invention provides a kind of method preparing the catalyst with hydrogenation catalyst effect, the method is included in supported on carriers at least one group VIII metallic element and at least one group vib metallic element, wherein, described carrier is aluminium oxide article shaped or the article shaped containing hydrated alumina, material forming containing at least one component A, at least one B component and at least one component C is obtained, described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether.
A third aspect of the present invention provides a kind of catalyst prepared by method of the present invention.
A fourth aspect of the present invention provides the application of catalyst of the present invention in hydrocarbon oil hydrogenation process.
A fifth aspect of the present invention provides a kind of hydrotreating method, and the method comprises under hydroprocessing conditions, and by hydrocarbon ils and catalyst exposure, wherein, described catalyst is catalyst provided by the invention.
Catalyst according to the invention demonstrates higher catalytic activity in the hydrotreatment of hydrocarbon ils.
Detailed description of the invention
A first aspect of the present invention provides a kind of catalyst with hydrogenation catalyst effect, and this catalyst contains carrier and load at least one group VIII metallic element on the carrier and at least one group vib metallic element.Term " at least one " refers to one or more.
Catalyst according to the invention, the content of described group VIII metallic element and group vib metallic element can carry out suitable selection according to the embody rule occasion of catalyst.Such as, when catalyst according to the invention is used for the hydrotreatment of hydrocarbon ils, with the total amount of described catalyst for benchmark, the content of described carrier can be 40-80 % by weight, is preferably 50-75 % by weight; With oxide basis, the content of described group VIII metallic element can be 2-15 % by weight, is preferably 4-10 % by weight; With oxide basis, the content of described group vib metallic element can be 15-45 % by weight, is preferably 20-40 % by weight.
Catalyst according to the invention, the various elements with hydrogenation catalyst effect that described group VIII metallic element and described group vib metallic element can be commonly used for this area.Preferably, described group VIII metallic element is cobalt and/or nickel, and described group vib metallic element is molybdenum and/or tungsten.
Catalyst according to the invention, described group VIII metallic element and group vib metallic element existence form are on the carrier not particularly limited, and can be that the routine of this area is selected.From the angle of catalytic activity improving further catalyst according to the invention, load is on the carrier in a salt form for described group VIII metallic element and described group vib metallic element basic (that is, mainly or in fact).That is, described group VIII metallic element preferably with the form load of the salt containing group VIII metallic element on the carrier, and described group vib metallic element preferably with the form load of the salt containing group vib metallic element on the carrier.Also namely, preferably basic (that is, mainly or in fact) with the form load of non-oxidized substance on the carrier for described group VIII metallic element and described group vib metallic element.
Catalyst according to the invention, the material forming containing at least one component A, at least one B component and at least one component C obtains by described carrier, and described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether.
According to the present invention, described raw material contains at least one component A, at least one B component and at least one component C, but not containing peptizing agent (such as: Alumina gel, nitric acid, citric acid, oxalic acid, acetic acid, formic acid, malonic acid, hydrochloric acid and trichloroacetic acid).Catalyst according to the invention, the composition of described raw material can carry out suitable selection according to the application scenario of catalyst, can meet instructions for use be as the criterion with the carrier prepared by this raw material.Usually, with the total amount of described raw material for benchmark, the content of described component C can be 0.5-12 % by weight, is preferably 1-10 % by weight, more preferably 3-8 % by weight; With Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter can be 88-99 % by weight, is preferably 90-98 % by weight, is more preferably 92-96 % by weight.In the present invention, when calculating the total amount of raw material, component A(namely, hydrated alumina) with Al
2o
3meter, the aluminium oxide leftover bits and pieces in B component is with Al
2o
3meter, and described raw material does not comprise the water will introduced in material forming process.
According to the present invention, the relative scale between described component A and described B component is not particularly limited, and can carry out suitable selection according to the embody rule occasion of catalyst.Usually, the weight ratio of described component A and described B component is 9-1:1, is preferably 9-2:1.
In the present invention, described component C is selected from cellulose ether, and described cellulose ether refers to the ether system derivative formed after the hydrogen atom at least part of hydroxyl in cellulosic molecule is replaced by one or more alkyl, wherein, multiple described alkyl can be identical, also can be different.Described alkyl is selected from the alkyl of replacement and unsubstituted alkyl.Described unsubstituted alkyl is preferably alkyl (such as: C
1-C
5alkyl).In the present invention, C
1-C
5the instantiation of alkyl comprise C
1-C
5straight chained alkyl and C
3-C
5branched alkyl, can for but be not limited to: methyl, ethyl, n-pro-pyl, isopropyl, normal-butyl, isobutyl group, the tert-butyl group, n-pentyl, isopentyl and tertiary pentyl.The alkyl of described replacement can be such as by the alkyl of hydroxyl or carboxyl substituted (such as: C
1-C
5the alkyl be optionally substituted by a hydroxyl group, C
1-C
5by the alkyl of carboxyl substituted), its instantiation can include but not limited to: methylol, ethoxy, hydroxypropyl, hydroxyl butyl, carboxymethyl, carboxyethyl and carboxylic propyl group.
The present invention is not particularly limited for the substituent quantity of the hydrogen atom in the kind of described cellulose ether and the hydroxyl in substituted cellulose molecule, can be common various cellulose ethers.Particularly, described cellulose ether (that is, described component C) can be selected from but be not limited to: methylcellulose, ethyl cellulose, hydroxyethylcellulose, HEMC, hydroxypropyl cellulose, hydroxypropyl methylcellulose, carboxymethyl cellulose, carboxyethyl cellulose and carboxymethyl hydroxyethyl cellulose.Preferably, described cellulose ether (that is, described component C) is selected from methylcellulose, HEMC and hydroxypropyl methylcellulose.
According to the present invention, described component A is selected from hydrated alumina.The present invention is not particularly limited for the kind of described hydrated alumina, can be that the routine of this area is selected.Preferably, described hydrated alumina (that is, described component A) is selected from boehmite, gibbsite, amorphous hydrated aluminium oxide and boehmite.More preferably, described hydrated alumina (that is, described component A) is boehmite.
In the present invention, described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces.
The present invention is for Al
2o
3kind be not particularly limited, can be the conventional various Al in this area
2o
3, such as: γ-Al
2o
3, δ-Al
2o
3, θ-Al
2o
3with α-Al
2o
3.Preferably, described Al
2o
3for γ-Al
2o
3.More preferably, described γ-Al
2o
3pore volume be 0.8-1.2mL/g, specific area is 200-400m
2/ g.Described pore volume and specific area adopt nitrogen adsorption/desorption method to measure.
In the present invention, described aluminium oxide leftover bits and pieces refers to that (comprise the aluminium oxide article shaped containing modifying element and the aluminium oxide article shaped containing molecular sieve, described modifying element such as can be selected from element silicon, P elements, titanium elements, zr element, elemental lithium, magnesium elements and boron element in the various aluminium oxide article shaped of preparation; Described molecular sieves is as being selected from Y molecular sieve and ZSM molecular sieve) process in the waste material that produces, such as: preparation as have hydrogenation catalyst effect catalyst carrier process in the leftover bits and pieces that produces.In the present invention, described aluminium oxide leftover bits and pieces is specifically as follows and can forms Al containing being selected under roasting condition
2o
3precursor and Al
2o
3in the mixture of at least one, adhesive, optional modifying element, optional molecular sieve and optional extrusion aid preparing the leftover bits and pieces produced in the process of aluminium oxide article shaped.The described precursor that can form aluminium oxide under roasting condition can be selected for the routine of this area, such as: various forms of hydrated alumina (hydrated alumina as previously described).Described aluminium oxide leftover bits and pieces can be the leftover bits and pieces through roasting, also can be unfired leftover bits and pieces.The particle diameter of described aluminium oxide leftover bits and pieces is not particularly limited, and is as the criterion can make the material forming for the preparation of the article shaped containing hydrated alumina of the present invention.Preferably, the average particulate diameter of described aluminium oxide leftover bits and pieces is 50-120 micron.Can by successively being carried out grinding and sieving by described aluminium oxide leftover bits and pieces before use, thus the average particulate diameter of described aluminium oxide leftover bits and pieces be within above-mentioned scope.In the present invention, the average particulate diameter of described aluminium oxide leftover bits and pieces adopts laser particle analyzer to measure.
According to the present invention, described raw material can also contain at least one extrusion aid.The content of described extrusion aid can be the routine selection of this area.Usually, with the total amount of described raw material for benchmark, the total content of described extrusion aid can be 0.1-8 % by weight, is preferably 0.5-5 % by weight.The present invention is not particularly limited for the kind of described extrusion aid, can be that the routine of this area is selected.Preferably, described extrusion aid is starch (that is, described raw material is also containing starch).The starch in the various sources that described starch can be commonly used for this area, such as: by vegetable seeds through pulverizing the powder obtained, as sesbania powder.
Catalyst according to the invention, the various methods that this area can be adopted conventional are by described material forming.Preferably, described article shaped prepares formed body by described raw material, and described formed body is carried out drying and optional roasting is made.
The various methods that this area can be adopted conventional, to prepare described formed body, are not particularly limited.Such as: at least one component A, at least one B component and at least one component C can be mixed with water, and by shaping for described mixture.Consumption for the preparation of the water of described mixture is not particularly limited, as long as the consumption of water can guarantee various component to mix.
Catalyst according to the invention, described shaping mode is not particularly limited, and can adopt the various molding modes that this area is conventional, such as: extrusion, round as a ball, spraying, compressing tablet or their combination.One of the present invention preferred embodiment in, come shaping by the mode of extrusion.
Catalyst according to the invention, described carrier can have various shape according to concrete instructions for use, such as: spherical, bar shaped, annular, cloverleaf pattern, honeycombed or butterfly.
The temperature of described formed body drying can be that the routine of this area is selected by catalyst according to the invention.Usually, the temperature of described drying can be more than 60 DEG C and lower than 350 DEG C, be preferably 80-300 DEG C, be more preferably 120-250 DEG C.The time of described drying can carry out suitable selection according to the temperature of drying, meets instructions for use be as the criterion can make volatile matter content in the article shaped that finally obtains.Usually, the time of described drying can be 1-48 hour, is preferably 2-24 hour, is more preferably 2-12 hour.According to the present invention, described drying can be carried out at ambient pressure, also can carry out at reduced pressure.
Catalyst according to the invention, the formed body prepared by described raw material can only drying and without roasting, directly be used as the carrier of catalyst of the present invention (namely, described carrier is the article shaped containing hydrated alumina), also the carrier (that is, described carrier is aluminium oxide article shaped) of catalyst of the present invention can be used as after successively drying and roasting.The present invention is not particularly limited for the condition of described roasting, can be that the routine of this area is selected.Particularly, the temperature of described roasting can be 450-950 DEG C, is preferably 500-900 DEG C; The time of described roasting can be 2-8 hour, is preferably 3-6 hour.From the further angle improving the catalytic activity of catalyst according to the invention, described carrier is preferably the article shaped containing hydrated alumina.
Catalyst according to the invention, described carrier has good intensity and absorbent properties.
Particularly, described carrier radial crushing strength loss late (that is, δ value) is after steeping less than 10%, can be even less than 5%, such as, can reach less than 3.5%.
In the present invention, δ value is used for the strength retention of evaluation carrier, is defined by following formula:
Wherein, Q
1for the radial crushing strength of the carrier without water soaking, in N/mm,
Q
2for through water soaking 30 minutes and in the radial crushing strength of the carrier of 120 DEG C of dryings after 4 hours, in N/mm.
Radial crushing strength (that is, the Q of described carrier
1) can be more than 12N/mm, be even more than 15N/mm, be generally 15-30N/mm(such as 15-25N/mm).
In the present invention, described radial crushing strength according to " Petrochemical Engineering Analysis method " (Science Press, nineteen ninety the first edition, the volumes such as Yang Cuiding) in the RIPP25-90 that records the method that specifies measure.
According to the present invention, the water absorption rate of described carrier is 0.4-1.5, is generally 0.6-1.
In the present invention, described water absorption rate refers to that the dry excessive deionized water of carrier soaks the ratio of the weight of the weight change value of 30 minutes front and back and the carrier of described drying.Concrete method of testing is: by carrier to be measured 120 DEG C of dryings 4 hours, then sieves with 40 object standard screens, takes 20g oversize and (be designated as w as testing sample
1), testing sample 50g deionized water is soaked 30 minutes, after filtration, solid phase is drained 5 minutes, the weight then weighing the solid phase drained (is designated as w
2), with following formulae discovery water absorption rate:
Catalyst according to the invention, described catalyst can also contain the various component can improving the catalytic performance of catalyst, such as: P elements.The present invention is not particularly limited for the described content that can improve the component of the catalytic performance of catalyst, can be that the routine of this area is selected.Usually, with the total amount of catalyst for benchmark, with oxide basis, the described content that can improve the component of the catalytic performance of catalyst can be 0.1-10 % by weight, is preferably 0.5-5 % by weight.
A second aspect of the present invention provides a kind of method preparing the catalyst with hydrogenation catalyst effect, the method is included in supported on carriers at least one group VIII metallic element and at least one group vib metallic element, wherein, described carrier is aluminium oxide article shaped or the article shaped containing hydrated alumina, material forming containing at least one component A, at least one B component and at least one component C is obtained, described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether.
According to method of the present invention, described containing group VIII metallic element and containing group vib metallic element load capacity on the carrier to make in the catalyst of final preparation, the content of group VIII metallic element and group vib metallic element can meet concrete instructions for use and be as the criterion.When prepared according to the methods of the invention catalyst is used for the hydrotreatment of hydrocarbon ils, describedly contain group vib metallic element and make the total amount of the catalyst finally prepared for benchmark containing the load capacity on the carrier of group VIII metallic element, the content of described carrier is 40-80 % by weight, is preferably 50-75 % by weight; With oxide basis, the content of described group VIII metallic element is 2-15 % by weight, is preferably 4-10 % by weight; With oxide basis, the content of described group vib metallic element is 15-45 % by weight, is preferably 20-40 % by weight.
According to method of the present invention, the various methods that this area can be adopted conventional by described group VIII metallic element and the load of group vib metallic element on the carrier, such as: dipping.Described dipping can be saturated dipping, also can be excessive dipping.
According to method of the present invention, can on the carrier by group VIII metallic element and the load of group vib metallic element simultaneously, also can gradation by described group VIII metallic element and the load of described group vib metallic element on the carrier.
In one embodiment of the invention, described group VIII metallic element and described group vib metallic element load mode are on the carrier comprised: with containing at least one containing the salt of group VIII metallic element and at least one containing the compound of group vib metallic element aqueous impregnation described in carrier, and carry out drying by flooding the carrier obtained.
In another embodiment of the invention, described group VIII metallic element and described group vib metallic element load mode are on the carrier comprised: with containing at least one containing group VIII metallic element salt aqueous impregnation described in carrier, and carry out drying by flooding the carrier obtained, there is the carrier of the described salt containing group VIII metallic element with the aqueous impregnation load of the compound containing group vib metallic element containing at least one, and carry out drying by flooding the carrier obtained.
In another embodiment of the present invention, described group VIII metallic element and described group vib metallic element load mode are on the carrier comprised: with containing at least one containing group vib metallic element compound aqueous impregnation described in carrier, and carry out drying by flooding the carrier obtained, there is the carrier of the described compound containing group vib metallic element with the aqueous impregnation load of the salt containing group VIII metallic element containing at least one, and carry out drying by flooding the carrier obtained.
According to method of the present invention, the present invention is not particularly limited for the concentration of the described aqueous solution, as long as can make in the catalyst of final preparation, the content of group VIII metallic element and group vib metallic element meets instructions for use (such as previously described requirement).
According to method of the present invention, under the condition can commonly used in this area, carry out drying by flooding the carrier obtained.Usually, the condition of described drying comprises: temperature can be 100-200 DEG C, is preferably 120-150 DEG C; Time can be 1-15 hour, is preferably 3-10 hour.
According to the present invention, the various water soluble salts containing group VIII metallic element that the described salt containing group VIII metallic element can be commonly used for this area, such as: the described salt containing group VIII metallic element can be selected from the water-soluble group VIII slaine of inorganic acid, the water-soluble group VIII slaine of organic acid and the water-insoluble salt containing group VIII metallic element and contact with sour (as phosphoric acid) and/or alkali (as ammoniacal liquor) water soluble salt formed in water.
Particularly, the described salt containing group VIII metallic element can be selected from but be not limited to: the water soluble salt that cobalt nitrate, cobalt acetate, basic cobaltous carbonate contact with acid (as phosphoric acid) and/or alkali (as ammoniacal liquor) and formed in water, cobalt chloride, aqueous cobalt complex compound, nickel nitrate, nickel acetate, basic nickel carbonate contact with acid (as phosphoric acid) and/or alkali (as ammoniacal liquor) water soluble salt, nickel chloride and the water-soluble nickel complex that are formed in water.Described aqueous cobalt complex compound can be such as Cobalt Edetate; Described water-soluble nickel complex can be such as citric acid nickel.Preferably, the described salt containing group VIII metallic element is selected from cobalt nitrate, basic cobaltous carbonate and in water, contact the water soluble salt, the basic nickel carbonate that are formed with acid (as phosphoric acid) and/or alkali (as ammoniacal liquor) contact with sour (as phosphoric acid) and/or alkali (as ammoniacal liquor) water soluble salt and nickel nitrate that are formed in water.
According to the present invention, the described kind containing the compound of group vib metallic element is not particularly limited, the various water soluble compounds containing group vib metallic element can commonly used for this area, such as can be selected from the water-soluble group vib slaine of inorganic acid, the water-soluble group vib slaine of organic acid, containing group vib metallic element heteropoly acid, in water, contact with acid (as phosphoric acid) or alkali the water soluble compound formed containing the heteropolyacid salt of group vib metallic element and the oxide of group vib metal.
Particularly, the described compound containing group vib metallic element can be selected from the water soluble salt of molybdic acid, the water soluble salt of para-molybdic acid, ammonium tungstate, ammonium metatungstate, ammonium paratungstate, ethyl ammonium metatungstate, phosphotungstic acid, phosphomolybdic acid, phosphotungstic acid nickel, phosphotungstic acid cobalt, silico-tungstic acid nickel, silico-tungstic acid cobalt, phosphomolybdic acid nickel, phosphomolybdic acid cobalt, P-Mo-Wo acid nickel, P-Mo-Wo acid cobalt, silicomolybdic acid nickel, silicomolybdic acid cobalt, silicon molybdenum nickel tungstate, silicon molybdenum cobaltous tungstate contact with molybdenum oxide the water soluble compound formed in water with phosphoric acid.In the present invention, the water soluble salt of described molybdic acid comprises water-soluble metal salt and the ammonium molybdate of molybdic acid; The water soluble salt of described para-molybdic acid comprises water-soluble metal salt and the ammonium paramolybdate of para-molybdic acid.Preferably, the described compound containing group vib metallic element is selected from ammonium molybdate, ammonium paramolybdate, ammonium metatungstate, ammonium tungstate and molybdenum oxide in water, contacts the water soluble compound formed with phosphoric acid.
According to method of the present invention, load has the carrier of described group VIII metallic element and group vib metallic element can carry out roasting (namely, in the catalyst of preparation, load is on the carrier in the form of the oxide for group VIII metallic element and group vib metal), also roasting can not be carried out (namely, in the catalyst of preparation, load is on the carrier substantially in a salt form for described group VIII metallic element and group vib metallic element; Also namely, in the catalyst of preparation, described group VIII metallic element and group vib metallic element are substantially with the form load of non-oxidized substance on the carrier).From the further angle improving the catalytic activity of prepared according to the methods of the invention catalyst, described group VIII metallic element and the preferred load substantially in a salt form of group vib metallic element are on the carrier.That is, according to method of the present invention, load has the carrier of described group VIII metallic element and group vib metallic element preferably not carry out roasting.
According to method of the present invention, the material forming containing at least one component A, at least one B component and at least one component C obtains by described carrier, and described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether.Described carrier can, for the article shaped containing hydrated alumina, also can be aluminium oxide article shaped; From the angle of the catalytic activity of the catalyst of raising preparation further, described carrier is preferably the article shaped containing hydrated alumina.The preparation method of described carrier is described above, is not described in detail in this.
According to method of the present invention, the radial crushing strength of described carrier can be more than 12N/mm, is even more than 15N/mm, is generally 15-30N/mm, such as 15-25N/mm.The δ value of described carrier is less than 10%, can be even less than 5%, such as, can be less than 3.5%.The water absorption rate of described carrier is 0.4-1.5, is generally 0.6-1.
According to method of the present invention, the component of the catalytic performance introducing the catalyst that can improve final preparation on described carrier can also be comprised, such as: P elements.By before group VIII metallic element described in load and group vib metallic element, described component can be introduced on described carrier; Also can while group VIII metallic element described in load and group vib metallic element, by described component load on the carrier.The described introduction volume can improving the component of the performance of catalyst can be selected for the routine of this area.Usually, with the total amount of catalyst for benchmark, with oxide basis, the described content that can improve the component of the catalytic performance of catalyst can be 0.1-10 % by weight, is preferably 0.5-5 % by weight.
The catalyst that prepared according to the methods of the invention has hydrogenation catalyst effect demonstrates higher catalytic activity in the hydrotreatment of hydrocarbon ils.
Thus, a third aspect of the present invention provides a kind of catalyst with hydrogenation catalyst effect prepared by method of the present invention.
The catalyst with hydrogenation catalyst effect provided by the invention is suitable for the hydroprocessing processes of all kinds of hydrocarbon oil crude material.
Thus, a fourth aspect of the present invention provides a kind of according to the application of catalyst in hydrocarbon oil hydrogenation process with hydrogenation catalyst effect of the present invention.
A fifth aspect of the present invention provides a kind of hydrotreating method, under the method is included in hydrocarbon oil hydrogenation treatment conditions, by hydrocarbon ils and catalyst exposure of the present invention.
Hydrotreating method according to the present invention is that the catalyst that the application of the invention provides obtains higher hydrogenation activity, is not particularly limited for the kind of hydrocarbon ils and hydroprocessing condition, can be that the routine of this area is selected.
Particularly, described hydrocarbon ils can be various heavy mineral oil, artificial oil or their mixed fraction oil, such as, described hydrocarbon ils can one or more for being selected from crude oil, distillate, solvent-refined oil, slack wax, sweat oil, Fischer-Tropsch synthesis oil, liquefied coal coil, frivolous coal tar and heavy deasphalted oil.Described hydroprocessing condition comprises: temperature can be 300-380 DEG C; In gauge pressure, pressure can be 4-8MPa; During the liquid of hydrocarbon ils, volume space velocity can be 1-3 hour
-1; Hydrogen to oil volume ratio can be 200-1000.
According to hydrotreating method of the present invention, described catalyst before the use, can carry out presulfurization under the normal condition of this area.The condition of presulfurization can be such as in presence of hydrogen, and at the temperature of 140-370 DEG C, carry out presulfurization with sulphur, hydrogen sulfide or sulfur-bearing raw material, described presulfurization can be carried out outside reactor, also can be In-situ sulphiding in reactor.
The present invention is described in detail below in conjunction with embodiment and comparative example.
In following examples and comparative example, the method specified in RIPP25-90 is adopted to measure the radial crushing strength of the carrier of preparation.
In following examples and comparative example, following methods is adopted to measure the δ value of the carrier of preparation: to adopt the method mensuration that specifies in RIPP25-90 (to be designated as Q without the radial crushing strength of the carrier of water soaking
1); The carrier of preparation is placed in 50g deionized water, soaks 30 minutes, then filter, by the solid that obtains at the temperature of 120 DEG C dry 4 hours, the radial crushing strength measuring dry solid according to the method specified in RIPP25-90 (was designated as Q
2), adopt following formulae discovery δ value,
In following examples and comparative example, following methods is adopted to measure the water absorption rate of the carrier of preparation: by carrier to be measured 120 DEG C of dryings 4 hours, then to sieve with 40 object standard screens, take 20g oversize and (be designated as w as testing sample
1), testing sample 50g deionized water is soaked 30 minutes, after filtration, solid phase is drained 5 minutes, the weight then weighing the solid phase drained (is designated as w
2), with following formulae discovery water absorption rate:
In following examples and comparative example, contents on dry basis is by measuring testing sample 600 DEG C of roastings 4 hours.
In following examples and comparative example, pore volume and specific area adopt nitrogen adsorption/desorption method to measure.
In following examples and comparative example, average particulate diameter adopts the laser particle analyzer that to be purchased from the model of Micromeritics company be SaturnDigiSizer5200 to measure.
Embodiment 1-9 is for illustration of Catalysts and its preparation method of the present invention.
Embodiment 1
(1) by 80.0g boehmite powder (purchased from Sinopec catalyst Chang Ling branch company, contents on dry basis is 69.5 % by weight), 20g γ-Al
2o
3(pore volume is 0.95mL/g, and specific area is 290m
2/ g), 4.0g methylcellulose (purchased from Zhejiang Hai Shen Chemical Co., Ltd.), 3.0g sesbania powder and 95mL deionized water mix.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar extruded is placed in baking oven, 150 DEG C of dryings 12 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) 5.88g basic nickel carbonate (NiO content is 51 % by weight), 15.0g molybdenum oxide and 2.79g phosphoric acid are dissolved in the water, are mixed with 60mL solution; The carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 77.0 % by weight) the solution impregnation 20.0g step (1) obtained prepared, dip time is 4 hours.After filtration, by the solid product that obtains in 120 DEG C of dryings 4 hours, obtain catalyst according to the invention B1.Adopt XRF to analyze catalyst, result illustrates in table 2.
Comparative example 1
(1) by 80.0g boehmite powder (with embodiment 1), 20.0g γ-Al
2o
3(with embodiment 1), 2.5mL red fuming nitric acid (RFNA), 4.0g sesbania powder and 95mL deionized water mix.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar extruded is placed in baking oven, 150 DEG C of dryings 12 hours, then 600 DEG C of roastings 4 hours, thus obtains carrier.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) 2.24g basic nickel carbonate (NiO content is 51 % by weight), 5.69g molybdenum oxide and 1.06g phosphoric acid are dissolved in the water, are mixed with 12.0mL nickel-molybdenum-phosphorus solution.The carrier (diameter is 1.1mm, and particle length is 2-5mm) the solution impregnation 14.3g step (1) obtained prepared, dip time is 1 hour.By the solid product that obtains in 120 DEG C of dryings 4 hours, then at 600 DEG C of roasting 3h, obtain catalyst A 1.Adopt XRF to analyze catalyst, result is listed in table 2.
Comparative example 2
(1) method identical with comparative example 1 is adopted to prepare carrier, unlike, do not carry out roasting at 600 DEG C, thus obtain carrier, its radial crushing strength, water absorption rate and δ value are listed in Table 1.
(2) the method Kaolinite Preparation of Catalyst identical with comparative example 1 is adopted, unlike, carrier is carrier prepared by comparative example 2 step (1), and in dipping process, the phenomenon of dissolving and structural breakdown appears in carrier, and result cannot obtain shaping catalyst.
Comparative example 3
(1) adopt the method identical with comparative example 1 to prepare carrier, its radial crushing strength, water absorption rate and δ value are listed in Table 1.
(2) the method Kaolinite Preparation of Catalyst identical with comparative example 1 is adopted, unlike, do not carry out roasting at 600 DEG C, thus obtain catalyst A 2.Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 2
(1) by 50.0g boehmite (purchased from Sinopec catalyst Chang Ling branch company, contents on dry basis is 69.5 % by weight), 20.0g gibbsite is (purchased from Pingguo Aluminium Industry Co., Guangxi, contents on dry basis is 64.5 % by weight), (this leftover bits and pieces is through roasting for 30.0g aluminium oxide leftover bits and pieces, the temperature of roasting is 600 DEG C, the time of roasting is 4 hours, average particulate diameter is 100 microns, this aluminium oxide leftover bits and pieces is the mixture by boehmite and nitric acid and sesbania powder, by the method extruded preparation as have hydrogenation catalyst effect catalyst carrier aluminium oxide article shaped process in produce), 2.0g methylcellulose (purchased from Zhejiang Hai Shen Chemical Co., Ltd.), 3.0g HEMC (purchased from Shanghai Hui Guang Fine Chemical Co., Ltd) and 95mL deionized water and stirring even.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar obtained is placed in baking oven, 220 DEG C of dryings 6 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) 6.00g basic cobaltous carbonate (CoO content is 70 % by weight), 21.00g molybdenum oxide and 3.91g phosphoric acid are dissolved in the water, are mixed with 60mL nickel-molybdenum-phosphorus solution.By the carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 79.2 % by weight) obtaining solution impregnation 20.0g step (1) and prepare, dip time is 4 hours.After filtration, by the solid that obtains in 120 DEG C of dryings 4 hours, obtain catalyst B 2 of the present invention.Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 3
(1) by 70.0g boehmite (purchased from Sinopec catalyst Chang Ling branch company, contents on dry basis is 69.5 % by weight), 30.0g γ-Al
2o
3(pore volume is 0.95mL/g, and specific area is 290m
2/ g), 1.0g methylcellulose (purchased from Zhejiang Hai Shen Chemical Co., Ltd.), 2.0g hydroxypropyl methylcellulose (purchased from Zhejiang Hai Shen Chemical Co., Ltd.), 3.0g sesbania powder and 95mL deionized water and stirring be even.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar obtained is placed in baking oven, 80 DEG C of dryings 12 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) by 7.10g nickel nitrate (Ni (NO
3)
26H
2o), 28.19g ammonium metatungstate ((NH
4)
6w
7o
244H
2o) be dissolved in the water, be mixed with 21.4mL nickel tungsten solution.The carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 78.2 % by weight) the solution impregnation 20.0g step (1) obtained prepared, dip time is 1 hour.By the carrier that obtains in 120 DEG C of dryings 4 hours, thus obtain catalyst according to the invention B3.Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 4
(1) in the retort of a 2L with and the mode of flowing adds the aluminum sulfate solution and sodium aluminate solution (Al that 2000mL concentration is 48g/L
2o
3content is 200g/L, and causticity coefficient is 1.58) carry out precipitation reaction, reaction temperature is 50 DEG C, and pH value is 6.0, and reaction time is 15 minutes; The slurries vacuum filter obtained is filtered, to be filtered complete after, on filter cake supplement add 20L deionized water (temperature is 40 ± 5 DEG C) flush cake about 60 minutes.Filter cake after washing is joined 1.5L deionized water for stirring and becomes slurries, slurries are carried out drying with being pumped in spray dryer, control the outlet temperature of spray dryer within the scope of 100-110 DEG C, the dry materials time is 2 minutes, obtain hydrated alumina, wherein, Al
2o
3content is 63 % by weight, is defined as amorphous state through XRD analysis.
(2) by 50.0g boehmite SB powder (purchased from Sasol company, contents on dry basis is 75.0 % by weight), 25.0g step (1) prepare amorphous hydrated aluminium oxide, (this leftover bits and pieces is without roasting for 25.0g aluminium oxide leftover bits and pieces, average particulate diameter is 80 microns, Al
2o
3content is 68.8 % by weight; Y zeolite content is 10 % by weight; this aluminium oxide leftover bits and pieces is the mixture by boehmite and Y zeolite and nitric acid and sesbania powder, by the method extruded preparation as have hydrogenation catalyst effect catalyst carrier aluminium oxide article shaped process in produce), 3.0g HEMC (purchased from Shanghai Hui Guang Fine Chemical Co., Ltd), 3.0g sesbania powder and 90mL deionized water and stirring be even.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar obtained is placed in baking oven, 150 DEG C of dryings 12 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(3) 5.00g basic nickel carbonate (NiO content is 51 % by weight), 13.25g molybdenum oxide and 1.32g phosphoric acid are dissolved in the water, are mixed with 60mL nickel-molybdenum-phosphorus solution.The carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 75.9 % by weight) the solution impregnation 20g step (1) obtained prepared, dip time is 4 hours.After filtration, by the solid product that obtains in 120 DEG C of dryings 4 hours, thus obtain catalyst according to the invention B4.Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 5
(1) by 85.0g boehmite SB powder (purchased from Sasol company, contents on dry basis is 75.0 % by weight), 15.0g aluminium oxide leftover bits and pieces, (without roasting, average particulate diameter is 120 microns to this leftover bits and pieces, Al
2o
3content is 79.7 % by weight; with oxide basis; the content of titanium elements is 10 % by weight; this aluminium oxide leftover bits and pieces is the mixture by boehmite and nitric acid and sesbania powder, by the method extruded preparation as have hydrogenation catalyst effect catalyst carrier aluminium oxide article shaped process in produce), 3.0g HEMC (purchased from Shanghai Hui Guang Fine Chemical Co., Ltd), 2.0g hydroxypropyl methylcellulose (purchased from Shanghai Hui Guang Fine Chemical Co., Ltd), 3.0g sesbania powder and 90mL deionized water mix.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar obtained is placed in baking oven, 250 DEG C of dryings 4 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) 3.50g basic nickel carbonate (NiO content is 51 % by weight), 9.10g molybdenum oxide and 0.90g phosphoric acid are dissolved in the water, are mixed with 60mL nickel-molybdenum-phosphorus solution.The carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 81.5 % by weight) the solution impregnation 20g step (1) obtained prepared, dip time is 4 hours.After filtration, by the solid that obtains in 150 DEG C of dryings 3 hours, obtain catalyst B 5 of the present invention.Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 6
(1) by 90.0g boehmite (purchased from Yantai, Shandong Heng Hui Chemical Co., Ltd., contents on dry basis is 71.0 % by weight), 10.0g γ-Al
2o
3(pore volume is 0.95mL/g, and specific area is 290m
2/ g), 5.0g hydroxypropyl methylcellulose (purchased from Shanghai Hui Guang Fine Chemical Co., Ltd), 3.0g sesbania powder and 90mL deionized water mix.The mixture obtained is sent in extruder and extrudes, obtain wet bar.The wet bar obtained is placed in baking oven, 120 DEG C of dryings 4 hours, obtains the carrier in catalyst of the present invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) 10.40g basic nickel carbonate (NiO content is 51 % by weight), 25.28g molybdenum oxide and 2.34g phosphoric acid are dissolved in the water, are mixed with 60mL nickel-molybdenum-phosphorus solution.The carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 74.2 % by weight) the solution impregnation 20g step (1) obtained obtained, dip time is 4 hours.After filtration, by the solid product that obtains in 120 DEG C of dryings 4 hours, thus obtain catalyst according to the invention B6.Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 7
(1) method identical with embodiment 6 is adopted to prepare hydrated alumina forming matter, unlike, the content of hydroxypropyl methylcellulose is 6.6g, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) the method Kaolinite Preparation of Catalyst B7 identical with embodiment 6 is adopted, unlike, carrier is carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 73.0 % by weight) prepared by embodiment 7 step (1).Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 8
(1) method identical with embodiment 3 is adopted to prepare article shaped, unlike, the wet bar obtained is placed in baking oven, 120 DEG C of dryings 12 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) the method Kaolinite Preparation of Catalyst B8 identical with embodiment 3 is adopted, unlike, carrier is carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 79.7 % by weight) prepared by embodiment 8 step (1).Adopt XRF to analyze catalyst, result is listed in table 2.
Embodiment 9
(1) method identical with embodiment 5 is adopted to prepare article shaped, unlike, the wet bar obtained is placed in baking oven, 300 DEG C of dryings 4 hours, thus obtains the carrier in catalyst according to the invention.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in Table 1.
(2) the method Kaolinite Preparation of Catalyst B9 identical with embodiment 5 is adopted, unlike, carrier is carrier (diameter is 1.1mm, and particle length is 2-5mm, and contents on dry basis is 82.3 % by weight) prepared by embodiment 9 step (1).Adopt XRF to analyze catalyst, result is listed in table 2.
Table 1
| Numbering | Crushing strength (N/mm) | Water absorption rate | δ value (%) |
| Embodiment 1 | 21.6 | 0.87 | 2.8 |
| Comparative example 1 | 21.9 | 0.96 | 2.2 |
| Comparative example 2 | 19.5 | 0.93 | 52.0 |
| Comparative example 3 | 21.9 | 0.96 | 2.2 |
| Embodiment 2 | 17.7 | 0.83 | 2.1 |
| Embodiment 3 | 15.4 | 0.94 | 3.2 |
| Embodiment 4 | 20.9 | 0.80 | 1.5 |
| Embodiment 5 | 18.9 | 0.73 | 2.0 |
| Embodiment 6 | 18.3 | 0.82 | 3.4 |
| Embodiment 7 | 20.5 | 0.80 | 2.9 |
| Embodiment 8 | 15.9 | 0.96 | 3.1 |
| Embodiment 9 | 19.3 | 0.69 | 2.2 |
The result display of table 1, the carrier in catalyst according to the invention has good strength retention, even if crushing strength still higher after soaking in water.
Table 2
Embodiment 10-18 is for illustration of catalyst of the present invention and application thereof and hydrotreating method.
Embodiment 10-18
With 4,6-dimethyl Dibenzothiophene (4,6-DMDBT) as model compound, the activity of catalyst prepared of Evaluation operation example 1-9 respectively on high-pressure hydrogenation micro-reactor, actual conditions is as follows.
The n-decane solution of reaction raw materials: 4,6-DMDBT, wherein, concentration is 0.45 % by weight;
The conditions of vulcanization of catalyst: temperature is 360 DEG C, pressure is 4.2MPa, H
2flow velocity is 400mL/min, and sulfurized oil adopts CS
2mass fraction is the cyclohexane solution of 5 % by weight, and sulfurized oil feed rate is 0.4mL/min, and sulfuration carries out 3 hours altogether.
Hydrodesulfurization reaction condition: reaction temperature is 280 DEG C, pressure is 4.2MPa, H
2flow velocity is 400mL/min, and the feed rate of reaction raw materials is 0.2mL/min, stable reaction after 3 hours sampling gas-chromatography analyze.
According to following formulae discovery desulfurization degree, thus the hydrodesulfurization activity of evaluate catalysts, result is listed in table 3,
Conversion ratio × (the S of desulfurization degree (%)=4,6-DMDBT
dMBCH+ S
dMCHB+ S
dMBP) × 100%
Wherein, S
dMBCH, S
dMCHBand S
dMBPin the product that obtains of 4,6-DMDBT hydrodesulfurization respectively, dimethyl connection cyclohexane, Dimethylcyclohexyl benzene and dimethyl diphenyl selective.
Comparative example 4-5
Adopt the method identical with embodiment 9-18 to evaluate the hydrodesulfurization activity of catalyst prepared by comparative example 1 and 3 respectively, result is listed in table 3.
Table 3
| Numbering | Catalyst is numbered | Desulfurization degree (%) |
| Embodiment 10 | B1 | 77.7 |
| Comparative example 4 | A1 | 55.1 |
| Comparative example 5 | A2 | 50.6 |
| Embodiment 11 | B2 | 73.8 |
| Embodiment 12 | B3 | 74.9 |
| Embodiment 13 | B4 | 76.8 |
| Embodiment 14 | B5 | 75.6 |
| Embodiment 15 | B6 | 82.5 |
| Embodiment 16 | B7 | 81.3 |
| Embodiment 17 | B8 | 76.2 |
| Embodiment 18 | B9 | 75.1 |
Embodiment 19-22 is for illustration of Catalysts and its preparation method of the present invention.
Embodiment 19
Adopt the method Kaolinite Preparation of Catalyst identical with embodiment 1, unlike, carry out roasting under the condition listed at table 4 by the carrier prepared according to embodiment 1 step (1), to obtain the carrier used in catalyst according to the invention, and then obtain catalyst according to the invention B10.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in table 4.Adopt XRF to analyze catalyst, result is listed in table 5.
Embodiment 20
Adopt the method Kaolinite Preparation of Catalyst identical with embodiment 2, unlike, carry out roasting under the condition listed at table 4 by the carrier prepared according to embodiment 2 step (1), to obtain the carrier used in catalyst according to the invention, and then obtain catalyst according to the invention B11.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in table 4.Adopt XRF to analyze catalyst, result is listed in table 5.
Embodiment 21
Adopt the method Kaolinite Preparation of Catalyst identical with embodiment 4, unlike, carry out roasting under the condition listed at table 4 by the carrier prepared according to embodiment 4 step (1), to obtain the carrier used in catalyst according to the invention, and then obtain catalyst according to the invention B12.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in table 4.Adopt XRF to analyze catalyst, result is listed in table 5.
Embodiment 22
Adopt the method Kaolinite Preparation of Catalyst identical with embodiment 5, unlike, carry out roasting under the condition listed at table 4 by the carrier prepared according to embodiment 5 step (1), to obtain the carrier used in catalyst according to the invention, and then obtain catalyst according to the invention B13.Measure the radial crushing strength of the carrier obtained, water absorption rate and δ value, result is listed in table 4.Adopt XRF to analyze catalyst, result is listed in table 5.
Table 4
Table 5
Embodiment 23-26 is for illustration of catalyst according to the invention and application thereof and hydrotreating method.
Embodiment 23-26
Adopt the hydrodesulfurization activity of catalyst that the method identical with embodiment 10-18 is prepared in Evaluation operation example 19-22 respectively, result is listed in table 6.
Table 6
| Numbering | Catalyst is numbered | Desulfurization degree (%) |
| Embodiment 23 | B10 | 69.7 |
| Embodiment 24 | B11 | 66.2 |
| Embodiment 25 | B12 | 68.6 |
| Embodiment 26 | B13 | 67.6 |
Shown by the result of table 3 and table 6, catalyst according to the invention demonstrates higher catalytic activity in the hydrotreatment of hydrocarbon ils.
Claims (39)
1. one kind has the catalyst of hydrogenation catalyst effect, this catalyst contains carrier and load at least one group VIII metallic element on the carrier and at least one group vib metallic element, it is characterized in that, described carrier is aluminium oxide article shaped or the article shaped containing hydrated alumina, a kind of material forming is obtained, described raw material by least one component A, at least one B component, at least one component C and containing or at least one extrusion aid that do not contain form, described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether;
With the total amount of described raw material for benchmark, the content of described component C is 0.5-12 % by weight, with Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter is 88-99 % by weight, and the weight ratio of described component A and described B component is 9-1:1.
2. catalyst according to claim 1, wherein, with the total amount of this catalyst for benchmark, with oxide basis, the content of described carrier is 40-80 % by weight, and the content of described group VIII metallic element is 2-15 % by weight, and the content of described group vib metallic element is 15-45 % by weight.
3. catalyst according to claim 1 and 2, wherein, described group VIII metallic element is cobalt and/or nickel, and described group vib metallic element is molybdenum and/or tungsten.
4. catalyst according to claim 1, wherein, with the total amount of described raw material for benchmark, the content of described component C is 1-10 % by weight, with Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter is 90-98 % by weight.
5. catalyst according to claim 4, wherein, with the total amount of described raw material for benchmark, the content of described component C is 3-8 % by weight, with Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter is 92-96 % by weight.
6. according to the catalyst in claim 1,4 and 5 described in any one, wherein, the weight ratio of described component A and described B component is 9-2:1.
7. according to the catalyst in claim 1,4 and 5 described in any one, wherein, described component C is selected from methylcellulose, HEMC and hydroxypropyl methylcellulose.
8. according to the catalyst in claim 1,4 and 5 described in any one, wherein, described component A is selected from boehmite, gibbsite, amorphous hydrated aluminium oxide and boehmite.
9. catalyst according to claim 1, wherein, described Al
2o
3for γ-Al
2o
3.
10. catalyst according to claim 1, wherein, the average particulate diameter of described aluminium oxide leftover bits and pieces is 50-120 micron.
11. catalyst according to claim 1 and 2, wherein, the water absorption rate of described carrier is 0.4-1.5, δ value is less than 10%, Q
1for more than 12N/mm,
Wherein,
Q
1for the radial crushing strength of the carrier without water soaking, in N/mm,
Q
2for through water soaking 30 minutes and in the radial crushing strength of the carrier of 120 DEG C of dryings after 4 hours, in N/mm.
12. catalyst according to claim 11, wherein, the water absorption rate of described carrier is 0.6-1, δ value is less than 5%, Q
1for 15-30N/mm.
13. catalyst according to claim 1, wherein, with the total amount of described raw material for benchmark, the content of described extrusion aid is 0.1-8 % by weight.
14. catalyst according to claim 13, wherein, with the total amount of described raw material for benchmark, the content of described extrusion aid is 0.5-5 % by weight.
15. according to the catalyst in claim 1,13 and 14 described in any one, and wherein, described extrusion aid is starch.
16. according to the catalyst in claim 1,13 and 14 described in any one, and wherein, described extrusion aid is sesbania powder.
17. 1 kinds of methods preparing the catalyst with hydrogenation catalyst effect, the method is included in supported on carriers at least one group VIII metallic element and at least one group vib metallic element, it is characterized in that, described carrier is aluminium oxide article shaped or the article shaped containing hydrated alumina, a kind of material forming is obtained, described raw material by least one component A, at least one B component, at least one component C and containing or at least one extrusion aid that do not contain form, described component A is selected from hydrated alumina, and described B component is selected from Al
2o
3with aluminium oxide leftover bits and pieces, described component C is selected from cellulose ether;
With the total amount of described raw material for benchmark, the content of described component C is 0.5-12 % by weight, with Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter is 88-99 % by weight, and the weight ratio of described component A and described B component is 9-1:1.
18. methods according to claim 17, wherein, by being immersed in supported on carriers at least one group VIII metallic element and at least one group vib metallic element.
19. methods according to claim 17 or 18, wherein, described group vib metallic element and the load capacity of group VIII metallic element on carrier make the total amount of the catalyst finally prepared for benchmark, the content of described carrier is 40-80 % by weight, with oxide basis, the content of described group VIII metallic element is 2-15 % by weight, and the content of described group vib metallic element is 15-45 % by weight.
20. methods according to claim 17 or 18, wherein, described group VIII metallic element is cobalt and/or nickel, and described group vib metal is molybdenum and/or tungsten.
21. methods according to claim 17, wherein, described carrier is aluminium oxide article shaped, and the method being prepared described carrier by described raw material comprises: by described material forming, and the formed body obtained successively is carried out drying and roasting; Or
Described carrier is the article shaped containing hydrated alumina, and the method being prepared described carrier by described raw material comprises: by described material forming, and the formed body obtained is carried out drying.
22. methods according to claim 21, wherein, the condition of described roasting comprises: temperature is 450-950 DEG C, and the time is 2-8 hour;
The temperature of described drying is more than 60 DEG C and lower than 350 DEG C.
23. methods according to claim 22, wherein, the temperature of described drying is 80-300 DEG C.
24. methods according to claim 17 or 21, wherein, with the total amount of described raw material for benchmark, the content of described component C is 1-10 % by weight, with Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter is 90-98 % by weight.
25. methods according to claim 24, wherein, with the total amount of described raw material for benchmark, the content of described component C is 3-8 % by weight, with Al
2o
3meter described component A and with Al
2o
3the total content of the described B component of meter is 92-96 % by weight.
26. methods according to claim 17 or 21, wherein, described component C is selected from methylcellulose, HEMC and hydroxypropyl methylcellulose.
27. methods according to claim 17 or 21, wherein, described component A is selected from boehmite, gibbsite, amorphous hydrated aluminium oxide and boehmite.
28. methods according to claim 17 or 21, wherein, described Al
2o
3for γ-Al
2o
3.
29. methods according to claim 17 or 21, wherein, the average particulate diameter of described aluminium oxide leftover bits and pieces is 50-120 micron.
30. according to the method in claim 17,18 and 21 described in any one, and wherein, the water absorption rate of described carrier is 0.4-1.5, δ value is less than 10%, Q
1for more than 12N/mm,
Wherein,
Q
1for the radial crushing strength of the carrier without water soaking, in N/mm,
Q
2for through water soaking 30 minutes and in the radial crushing strength of the carrier of 120 DEG C of dryings after 4 hours, in N/mm.
31. methods according to claim 30, wherein, the radial crushing strength of described carrier is 15-30N/mm, and water absorption rate is 0.6-1, δ value is less than 5%.
32. methods according to claim 17, wherein, with the total amount of described raw material for benchmark, the content of described extrusion aid is 0.1-8 % by weight.
33. methods according to claim 32, wherein, with the total amount of described raw material for benchmark, the content of described extrusion aid is 0.5-5 % by weight.
34. according to the method in claim 17,32 and 33 described in any one, and wherein, described extrusion aid is starch.
35. according to the method in claim 17,32 and 33 described in any one, and wherein, described extrusion aid is sesbania powder.
36. methods according to claim 17, wherein, the weight ratio of described component A and described B component is 9-2:1.
Catalyst prepared by the method in 37. claim 17-36 described in any one.
The application of catalyst in 38. claim 1-16 and 37 described in any one in hydrocarbon oil hydrogenation process.
39. 1 kinds of hydrotreating methods, the method comprises under hydroprocessing conditions, by hydrocarbon ils and catalyst exposure, it is characterized in that, described catalyst is the catalyst in claim 1-16 and 37 described in any one.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210193753.XA CN103480422B (en) | 2012-06-12 | 2012-06-12 | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201210193753.XA CN103480422B (en) | 2012-06-12 | 2012-06-12 | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103480422A CN103480422A (en) | 2014-01-01 |
| CN103480422B true CN103480422B (en) | 2016-01-13 |
Family
ID=49821209
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201210193753.XA Active CN103480422B (en) | 2012-06-12 | 2012-06-12 | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103480422B (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109569556B (en) * | 2017-09-29 | 2021-12-17 | 中国石油化工股份有限公司 | Catalyst with hydrogenation catalysis effect, preparation method and application thereof, and heavy oil hydrogenation asphaltene removal method |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5266188A (en) * | 1991-04-22 | 1993-11-30 | Amoco Corporation | Selective hydrotreating |
| US5358633A (en) * | 1993-05-28 | 1994-10-25 | Texaco Inc. | Hydrodesulfurization of cracked naphtha with low levels of olefin saturation |
| US5525211A (en) * | 1994-10-06 | 1996-06-11 | Texaco Inc. | Selective hydrodesulfurization of naphtha using selectively poisoned hydroprocessing catalyst |
| CN1289824A (en) * | 1999-09-29 | 2001-04-04 | 中国石油化工集团公司 | Hydrogenating catalyst for heavy oil and its preparing process |
| CN1352229A (en) * | 2000-11-08 | 2002-06-05 | 中国石油化工股份有限公司 | Heavy oil hydrogenating treatment catalyst and its preparing method |
| CN1458236A (en) * | 2002-05-15 | 2003-11-26 | 中国石油化工股份有限公司 | Process for preparing demetalizing and desulfurizing catalyst of heavy oil hydrogenation |
| CN1597117A (en) * | 2003-09-15 | 2005-03-23 | 中国石油化工股份有限公司 | Preparation method of aluminium oxide carrier |
| CN1597862A (en) * | 2003-09-15 | 2005-03-23 | 中国石油化工股份有限公司 | Preparation process for hydrogenating treatment catalyst |
-
2012
- 2012-06-12 CN CN201210193753.XA patent/CN103480422B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5266188A (en) * | 1991-04-22 | 1993-11-30 | Amoco Corporation | Selective hydrotreating |
| US5358633A (en) * | 1993-05-28 | 1994-10-25 | Texaco Inc. | Hydrodesulfurization of cracked naphtha with low levels of olefin saturation |
| US5525211A (en) * | 1994-10-06 | 1996-06-11 | Texaco Inc. | Selective hydrodesulfurization of naphtha using selectively poisoned hydroprocessing catalyst |
| CN1289824A (en) * | 1999-09-29 | 2001-04-04 | 中国石油化工集团公司 | Hydrogenating catalyst for heavy oil and its preparing process |
| CN1352229A (en) * | 2000-11-08 | 2002-06-05 | 中国石油化工股份有限公司 | Heavy oil hydrogenating treatment catalyst and its preparing method |
| CN1458236A (en) * | 2002-05-15 | 2003-11-26 | 中国石油化工股份有限公司 | Process for preparing demetalizing and desulfurizing catalyst of heavy oil hydrogenation |
| CN1597117A (en) * | 2003-09-15 | 2005-03-23 | 中国石油化工股份有限公司 | Preparation method of aluminium oxide carrier |
| CN1597862A (en) * | 2003-09-15 | 2005-03-23 | 中国石油化工股份有限公司 | Preparation process for hydrogenating treatment catalyst |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103480422A (en) | 2014-01-01 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103357445A (en) | Heavy-petroleum hydrogenating deasphaltenizing catalyst and preparation and application thereof | |
| CN104437518A (en) | Selective hydrodesulfurization catalyst, and preparation and application thereof | |
| CN104437517A (en) | Heavy-oil hydrotreatment catalyst, and preparation and application thereof | |
| CN110773209A (en) | Heavy oil hydrogenation deasphaltened catalyst and preparation and application thereof | |
| CN103480421B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method | |
| CN103480388B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method | |
| CN102861592A (en) | Reactive metal component inhomogeneously-distributed boron-contained hydrogenation catalyst and preparation thereof | |
| CN103374387B (en) | A kind of nickel and the high heavy oil hydrogenation treatment method of content of vanadium | |
| CN103480390B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and method for hydrotreating hydrocarbon oil | |
| CN103480422B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method | |
| CN103480338B (en) | Article shaped containing hydrated alumina and preparation method thereof and aluminium oxide article shaped and application | |
| CN103480409B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and method for hydrotreating hydrocarbon oil | |
| CN103480249B (en) | Hydrated alumina forming matter and preparation method and aluminium oxide article shaped and catalyst and preparation method and application and hydrotreating method | |
| CN102861601B (en) | A kind of fluorine-containing hydrogenation catalyst and preparation thereof | |
| CN103480423B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method | |
| CN104646008A (en) | Inferior heavy oil hydrodesulfurization demetalization catalyst and preparation method thereof | |
| CN103480337B (en) | Hydrated alumina forming matter and preparation method and aluminium oxide article shaped and application and catalyst and preparation method and hydrotreating method | |
| CN103923692B (en) | A kind of hydroprocessing process of heavy raw oil | |
| CN102861591B (en) | Hydrogenation catalyst containing boron and preparation method thereof | |
| CN103480386B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and method for hydrotreating hydrocarbon oil | |
| CN103480410B (en) | Catalyst with hydrogenation catalyst effect and its preparation method and application and hydrotreating method | |
| CN104293383B (en) | A kind of hydroprocessing process optimizing catalytically cracked material character | |
| CN102580769A (en) | Hydrogenation catalyst composition and preparation method | |
| CN103418397B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method | |
| CN103418398B (en) | There is the Catalysts and its preparation method of hydrogenation catalyst effect and application and hydrotreating method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |