CN103657700A - Catalytic cracking catalyst and preparation method thereof - Google Patents
Catalytic cracking catalyst and preparation method thereof Download PDFInfo
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Abstract
The invention relates to a catalytic cracking catalyst and a preparation method. The catalytic cracking catalyst contains a cracking activity component, clay and an adhesive, wherein the cracking activity component comprises a rare-earth Y-type molecular sieve; and the rare-earth content in the Y-type molecular sieve is 10-25 wt% on the basis of rare-earth oxides, the cell constant is 2.440-2.472nm, the crystallinity is 35-65%, the silicon/aluminum atomic ratio in the framework is 2.5-5.0, and the product of the ratio (I1/I2) of 2theta=11.8+/-0.1 degree peak intensity I1 to 2theta=12.3+/-0.1 degree peak intensity I2 in an X-ray diffraction pattern and the rare-earth weight percent in the molecular sieve on the basis of rare-earth oxides is greater than 50. The preparation method comprises the following steps: preparing a mixed slurry containing the cracking activity component, adhesive and clay, carrying out spray drying, washing and drying. Compared with the prior art, the rare-earth-containing Y-type molecular sieve has higher structural stability and activity stability; and the catalyst has higher thermal and hydrothermal stability, and can reduce the consumption of the molecular sieves in the catalyst, thereby lowering the catalyst production cost.
Description
Technical field
The present invention relates to a kind of catalytic cracking catalyst and preparation thereof containing rare earth modified Y zeolite.
Background technology
Catalytic cracking (FCC) is important crude oil secondary processing process, occupies very important status in petroleum refining industry.In catalytic cracking process, heavy end as vacuum distillate or more the residual oil of heavy constituent under catalyst exists, react, be converted into the high value added products such as liquefied gas, gasoline, diesel oil, in this process, conventionally need to use the catalysis material with high cracking activity.Micro-pore zeolite catalysis material, owing to having good shape selective catalysis performance and very high cracking reaction activity, is widely used in petroleum refining and processing industry.Wherein Y zeolite, since using first the sixties in last century, has been just the main active component of catalytic cracking catalyst always.Especially through rare earth modified Y zeolite, the improvement of acidic zeolite and structural stability is had to remarkable effect.
In recent years, because rare earth price rapidly goes up, greatly increase the production cost of rare-earth modified molecular-sieve, to manufacturing enterprise, caused no small pressure.In order effectively to utilize rare earth resources, reduce the molecular sieve production cost of molecular sieve production cost, particularly high rare-earth content, must improve the rare earth utilization rate in modifying process, reduce rare earth and run off, also will guarantee the cracking performance of molecular sieve simultaneously, improve the activity stability of molecular sieve as far as possible.
Rare earth Y type molecular sieve is used widely in catalytic cracking catalyst as active component at present, for example in olefine lowering catalyst, two roasting techniques are handed in general employing two, i.e. twice liquid phase rare earth ion exchanged and twice high-temperature roasting, molecular sieve Rare-Earth Content reaches the heavy % of 16-22, there is higher hydrogen transfer activity, fall alkene successful, but exist coke yield high, affect the problem of octane number and diesel yield ".
A kind of olefine lowering catalyst and preparation method thereof is disclosed in CN1317547A, it is that the heavy % of 12-20, degree of crystallinity are greater than 50% REY molecular sieve and content of rare earth is that the heavy % of 2-12, phosphorus content are phosphorus and the composite modified PREY molecular sieve of rare earth of heavy %, lattice constant 2.445-2.465nm of 0.2-3 that this catalyst mainly contains content of rare earth, compare with conventional catalyst, this catalyst falls alkene successful and can guarantee that product distributes and octane number.
A kind of hyperastable Y-type RE molecular sieve is disclosed in CN1506161A, the same two friendship two roasting techniques that adopt, after obtaining a friendship one roasting rare earth sodium Y, substep reacts with rare earth and phosphorus containg substances again, and carry out roasting for the second time, obtain the composite modified Y molecular sieve of content of rare earth 8-25 heavy %, phosphorus content 0.1-3.0 heavy %, degree of crystallinity 30-55%, lattice constant 2.455-2.477nm, this molecular sieve has the effect of significant reduction gasoline olefin, coke yield is moderate, diesel yield is high, and the utilization rate of modifying element is high.
Adopt two molecular sieves of handing over two roasting techniques to prepare also to there is some other feature, as disclosed molecular sieve that improves coking behavior and preparation method thereof in CN101537366A, still adopt two friendship two roasting techniques, this molecular sieve phosphorus content 0.05-5.0%, content of rare earth is few, be only 0.05-4.0%, lattice constant 2.430-2.440nm, degree of crystallinity 35-55%.
A kind of modcfied faujasite is disclosed in CN1436727A and containing the hydrocarbon cracking catalyzer of this zeolite, adopt one to hand over a roasting technique, be that NaY first carries out exchange reaction one time with phosphorus compound and ammonium compounds, add again subsequently earth solution to continue reaction, more after filtration, washing and hydrothermal calcine obtain, this preparation process flow process is short, catalyst activity good stability by this molecular sieve, gasoline yield is high, and coke yield is low, has stronger heavy oil cracking ability and preventing from heavy metal pollution ability.
A kind of high silicon rare earth Y type zeolite is disclosed in CN1382631A, by the gas-phase reaction of rare earth Y type zeolite and silicon tetrachloride, obtain the heavy % of a kind of intracrystalline content of rare earth 4-15, lattice constant 2.450-2.458nm, avalanche temperature 1000-1056 ℃, silica alumina ratio 8.3-8.8, sodium oxide content is less than the rare earth Y type zeolite of 1.0 heavy %, and this zeolite has good heavy oil cracking activity and selective, can improve yield of light oil, improve quality of gasoline, and there is good coke selectivity.
A kind of modified Y molecular sieve is disclosed in CN101823726A, adopt one to hand over a roasting technique, be that NaY first carries out exchange reaction one time with earth solution, add again subsequently phosphorus compound to continue reaction, more after filtration, washing and hydrothermal calcine obtain, the heavy % of the about 11-23 of its content of rare earth, rare earth major part is arranged in sodalite cage, molecular sieve stability improves, adjustable change acidic zeolite of while, and the catalyst that contains this molecular sieve has the advantages that heavy oil conversion performance is strong, coke selectivity is good.
In CN100344374C, disclose a kind of rare-earth Y molecular sieve and preparation method thereof, content of rare earth is counted the heavy % of 12-22 with rare earth oxide, and rare earth ion is all arranged in the little cage of molecular sieve, in its 27Al MAS NMR spectrogram, in chemical shift, is that 0ppm goes out not have peak to occur.Said preparation method adopts one to hand over a roasting technique, after a friendship, use alkaline solution regulator solution pH to 8-11, filter again, wash, be dried and roasting, or isolated molecule sieving cake after a friendship, collect filtrate, in filtrate, add alkaline solution regulator solution pH to 8-11, then the rare earth hydrate filter cake obtaining and molecular sieve filter cake are added to water making beating, filter, wash, be dried and roasting.This technique makes rare earth ion precipitation unnecessary in solution avoid rare earth run off and can guarantee that rare earth ion is all arranged in the little cage of molecular sieve.CN1322928C discloses a kind of catalyst that this molecular sieve is active component of take, and can significantly reduce catalytic cracking gasoline olefine content, has excellent heavy oil conversion performance simultaneously.
In prior art, no matter adopt two friendship two roasting techniques or rare-earth Y molecular sieves of handing over a roasting technique to obtain, content of rare earth in its product is always lower than the total rare earth (TRE) amount dropping into, as CN1053808A, CN1069553C, in CN1026225C, disclosed several rare-earth Y molecular sieves all have this feature, even if there is more rare earth ion to be positioned in little cage, but inevitably having part rare earth ion is still present in supercage, rare earth ion in supercage can be by under backwash in follow-up washing process, cause rare earth to run off, cause the reduction of rare earth utilization rate.
Summary of the invention
The technical problem to be solved in the present invention is to provide a kind of catalytic cracking catalyst and preparation method thereof, and this catalyst has higher activity and better heat and hydrothermal stability, can reduce molecular sieve consumption in catalyst.
Catalytic cracking catalyst provided by the invention contains cracking activity constituent element, clay and binding agent, and wherein, described cracking activity constituent element contains a kind of rare earth Y type molecular sieve, and the content of rare earth of this rare earth Y type molecular sieve is with rare earth oxide (RE
2o
3) count the heavy % of 10-25, lattice constant is 2.440-2.472nm, degree of crystallinity is 35-65%, framework silicon-aluminum atomic ratio is 2.5-5.0, and in this molecular sieve X-ray diffraction spectrogram, in the ratio (I1/I2) of the intensity I 1 at ° peak, 2 θ=11.8 ± 0.1 and the intensity I 2 at ° peak, 2 θ=12.3 ± 0.1 and molecular sieve, the product value in the rare earth weight percentage of rare earth oxide is greater than 50.
Preferably, the weight of catalyst of take is benchmark, and described catalytic cracking catalyst contains 10-60 % by weight cracking activity constituent element, 20-70 % by weight clay and 10-50 % by weight binding agent.
Described rare earth Y type molecular sieve is through two friendship two roastings, in conjunction with deposition of rare-earth process, obtains.More particularly, through following preparation process, obtain: NaY molecular sieve is contacted to processing with earth solution or earth solution with the mixed solution of ammonium salt, after filtration, washing, dry after, carry out calcination process for the first time, obtain rare earth sodium Y molecular sieve; Then by rare earth sodium Y molecular sieve making beating and contact with ammonium salt solution or acid solution processings, after filtration, mixes with earth solution, and to regulate the pH value of slurries be 6-10, filtration or do not filter, be dried, carries out calcination process for the second time, obtains described rare earth Y type molecular sieve again.
In above-mentioned rare earth Y type molecular sieve preparation process, the sial atomic ratio of raw material NaY molecular sieve be preferably greater than 2.5 and degree of crystallinity be greater than 80%.Saidly NaY molecular sieve and earth solution or rare earth are contacted in the process of processing with the mixed solution of ammonium salt, it is 0.06-0.14, preferred 0.08-0.12 that earth solution be take the part by weight of rare earth oxide and NaY molecular sieve butt, adjusting pH is 3.0-5.0, control water sieve weight ratio at 5-30, preferred 8-15, the process that said contact is processed is in room temperature-100 ℃, preferably carries out 0.3-3.0 hour, preferred 0.5-1.5 hour at 70-95 ℃.
In above-mentioned preparation process, said calcination process for the first time, is at 500-650 ℃, calcination process 0.5-4.0 hour, preferred 1.0-3.0 hour under 0-100% water vapor conditions.Wherein calcination process is preferred embodiment to carry out under 100% water vapor conditions for the first time.
In above-mentioned preparation process, said by rare earth sodium Y molecular sieve making beating and contact the process of processing with ammonium salt solution and be in room temperature-100 ℃, preferably process 0.3-3.0 hour, preferred 0.5-1.5 hour at 60-80 ℃, its middle rare earth sodium Y molecular sieve is by molecular sieve butt, with the part by weight of ammonium salt and water be 1:(0.05-0.5): (5-30), preferred 1:(0.1-0.4): (8-15).Said by rare earth sodium Y molecular sieve making beating and contact the process of processing with acid solution and be in room temperature-100 ℃, preferably process 0.3-2.0 hour, preferred 0.5-1.0 hour at 60-80 ℃, its middle rare earth sodium Y molecular sieve is by molecular sieve butt, with acid and H
2the part by weight of O is 1:(003-0.2): (5-30), preferred 1:(0.05-0.1): (8-15).Said ammonium salt is selected from any one or more the mixture in ammonium chloride, ammonium sulfate, ammonium nitrate, ammonium carbonate, carbonic hydroammonium.Said acid can be inorganic acid or organic acid, and inorganic acid can be selected from one or more the mixture in sulfuric acid, hydrochloric acid or nitric acid, and organic acid can be selected from one or more the mixture in oxalic acid, acetic acid, citric acid or tartaric acid.
In above-mentioned preparation process, by adding akaline liquid to regulate slurry pH value, be that 6-10, preferred pH value are 7-9, make rare earth ion all precipitate formation rare-earth hydroxide, i.e. the process of deposition of rare-earth.Said akaline liquid can be selected from one or more the mixture in ammoniacal liquor, waterglass, sodium metaaluminate or NaOH.
In above-mentioned preparation process, said calcination process for the second time, is under 500-650 ℃, 0-100% water vapor conditions, to process 0.5-4 hour, preferred 1-3 hour.Wherein calcination process is preferred embodiment to carry out under 100% water vapor conditions for the second time.
In above-mentioned preparation process, rare earths material is well known to those skilled in the art, can be selected from rare earth chloride or nitric acid rare earth, can be rare earth chloride or the nitric acid rare earth that Rare Earth Elements Determination forms, common lanthanum chloride, lanthanum nitrate, cerium chloride or cerous nitrate etc. of comprising wherein, also can be the mishmetal of different rare earth element ratios, as rich cerium type or rich lanthanum type mishmetal.
In above-mentioned preparation process, preferred embodiment be wherein said double roasting in processing, have at least be once 1-100%, more preferably 20-100%, most preferably under 100% water vapor conditions, carry out, steam treatment impels rare earth ion to move to little cage from molecular sieve supercage, therefore, the most preferred embodiment is that the said double roasting processing of preparation process is all to carry out under 100% water vapor conditions.
The present invention also provides a kind of preparation method of described catalytic cracking catalyst, and the method comprises mixes making beating by cracking activity constituent element, clay and binding agent, then spray be successively dried, washing, filtration and dry step.
The active component that catalytic cracking catalyst provided by the invention contains comprises a kind of rare earth Y type molecular sieve, it is by a liquid phase rare earth ion exchanged and a solid phase ion transition process, adopt the mode of deposition of rare-earth, through calcination process, rare earth ion is moved to little cage from supercage again, rare earth does not run off, molecular sieve structure good stability is (particularly through 800 ℃, 100% steam burin-in process is after 17 hours, crystallization of molecular sieves reservation degree is high), activity stability better (the micro-anti-MA value of light oil), this preparation process is modulation content of rare earth flexibly, accurately control, simple to operate, and rare earth utilization rate is high, can reach more than 98%, saved rare earth resources, reduced production cost.Catalytic cracking catalyst provided by the invention, has higher heat and hydrothermal stability.At content of rare earth quite or slightly low in the situation that, than prior art catalyst, there is higher cracking activity, the in the situation that molecular sieve content being lower in catalyst, still can obtain higher catalytic activity and product distribution preferably, therefore reduce the production cost of catalyst.
The specific embodiment
According to catalytic cracking catalyst provided by the invention, described cracking activity constituent element contains the first Y zeolite, described the first Y zeolite is rare earth Y type molecular sieve, its content of rare earth is counted the heavy % of 10-25 with rare earth oxide, lattice constant is 2.440-2.472nm, degree of crystallinity is 35-65%, framework silicon-aluminum atomic ratio is 2.5-5.0, and in this molecular sieve X-ray diffraction spectrogram, in the ratio (I1/I2) of the intensity I 1 at ° peak, 2 θ=11.8 ± 0.1 and the intensity I 2 at ° peak, 2 θ=12.3 ± 0.1 and molecular sieve, the product value in the rare earth weight percentage of rare earth oxide is greater than 50; In embodiments of the invention, this product value is further preferably greater than 55.
According to catalytic cracking catalyst provided by the invention, in described cracking activity constituent element except containing the first described Y zeolite, can also containing/or containing other Y zeolite.Described other Y zeolite is preferably the DASY molecular sieve (containing the hydro-thermal super-stable Y molecular sieves of rare earth, the present invention is called the second Y zeolite) containing rare earth, with RE
2o
3(rare earth oxide) meter, the described DASY molecular sieve Rare-Earth Content containing rare earth is 1.5-3.0 % by weight, the described DASY molecular sieve containing rare earth can be various commercially available prod, for example the DASY2.0 molecular sieve of China Petrochemical Industry's catalyst asphalt in Shenli Refinery.The butt weight of described active component of take is benchmark, the content of described the second Y zeolite of the butt of take as 0-50 % by weight can be for example 0-30 % by weight, 0-20 % by weight, the content of described the first Y zeolite is that 50-100 % by weight can be for example 70-100% weight or 80-100 % by weight.Preferably, when when other Y zeolite, the butt weight of catalyst of take is benchmark, and the content of the rare earth Y type molecular sieve described in described catalytic cracking catalyst (the first Y zeolite) is 10-60%, for example, can be 20-40 % by weight; The content of other Y zeolite is no more than 35 % by weight, and for example the content of other Y zeolite can be 0.5-30 % by weight, 0-10 % by weight or 0-5 % by weight.
In the present invention, described clay can be clay conventional in catalytic cracking catalyst, for example, can be one or more in kaolin, halloysite, imvite, diatomite, galapectite, saponite, rectorite, sepiolite, attapulgite, hydrotalcite and bentonite.
In the present invention, described binding agent can be the conventional various binding agents that use in catalytic cracking catalyst, for example, can, for being selected from one or more in Ludox, aluminium colloidal sol and boehmite, be preferably the double aluminium binder of aluminium colloidal sol and boehmite.
In preferred situation, catalytic cracking catalyst provided by the invention, the butt weight of described catalytic cracking catalyst of take is benchmark, it is 10-50 % by weight that described cracking activity constituent element be take the content of butt, it is 20-60 % by weight that described clay be take the content of butt, and it is 10-40 % by weight that described binding agent be take the content of butt.More preferably, the butt weight of described catalytic cracking catalyst of take is benchmark, it is 20-40 % by weight that described cracking activity constituent element be take the content of butt, it is 20-45 % by weight that described clay be take the content of butt, described binding agent take butt content as 20-40 % by weight can be for example 25-35 % by weight.
The preparation method of catalytic cracking catalyst provided by the invention, preferably includes following steps:
(1) NaY molecular sieve is contacted to processing with earth solution or earth solution with the mixed solution of ammonium salt, after filtration, washing, dry after, carry out calcination process for the first time, obtain rare earth sodium Y molecular sieve; Then rare earth sodium Y molecular sieve is pulled an oar and contacted processing with ammonium salt solution or acid solution, after filtration, mix with earth solution again, and the pH value that regulates slurries is 6-10, filter or do not filter, be dried, carry out calcination process for the second time, obtain rare earth Y type molecular sieve provided by the invention (the first Y zeolite);
(2) cracking activity constituent element, clay and binding agent are mixed to making beating, then spray successively and be dried, wash, filter and be dried, wherein, described cracking activity constituent element comprises the described Y zeolite (the first Y zeolite) containing rare earth, contains or do not contain other Y zeolites.
In above-mentioned preparation process, in step (1), the sial atomic ratio of raw material NaY molecular sieve be preferably greater than 2.5 and degree of crystallinity be greater than 80%.Saidly NaY molecular sieve and earth solution or earth solution are contacted in the process of processing with the mixed solution of ammonium salt, it is 0.06-0.14, preferred 0.08-0.12 that earth solution be take the part by weight of rare earth oxide and NaY molecular sieve butt, adjusting pH is 3.0-5.0, control water sieve weight ratio at 5-30, preferred 8-15, the process that said contact is processed is in room temperature-100 ℃, preferably carries out 0.3-3.0 hour, preferred 0.5-1.5 hour at 70-95 ℃.
In above-mentioned preparation process, the said calcination process for the first time of step (1), is at 500-650 ℃, calcination process 0.5-4.0 hour, preferred 1.0-3.0 hour under 0-100% water vapor conditions.Wherein calcination process is preferred embodiment to carry out under 100% water vapor conditions for the first time.
In above-mentioned preparation process, step (1) is said by rare earth sodium Y molecular sieve making beating and contact the process of processing with ammonium salt solution and be in room temperature-100 ℃, preferably process 0.3-3.0 hour, preferred 0.5-1.5 hour at 60-80 ℃, its middle rare earth sodium Y molecular sieve is by molecular sieve butt, with the part by weight of ammonium salt and water be 1:(0.05-0.5): (5-30), preferred 1:(0.1-0.4): (8-15).Said by rare earth sodium Y molecular sieve making beating and contact the process of processing with acid solution and be in room temperature-100 ℃, preferably process 0.3-2.0 hour, preferred 0.5-1.0 hour at 60-80 ℃, its middle rare earth sodium Y molecular sieve is by molecular sieve butt, with acid and H
2the part by weight of O is 1:(0.03-0.2): (5-30), preferred 1:(0.05-0.1): (8-15).Said ammonium salt is selected from any one or more the mixture in ammonium chloride, ammonium sulfate, ammonium nitrate, ammonium carbonate, carbonic hydroammonium.Said acid can be inorganic acid or organic acid, inorganic acid can be selected from one or more the mixture in sulfuric acid, hydrochloric acid (its proportioning is in HCl) or nitric acid, and organic acid can be selected from one or more the mixture in oxalic acid, acetic acid, citric acid or tartaric acid.
In above-mentioned preparation process, in step (1), by adding akaline liquid to regulate slurry pH value, be that 6-10, preferred pH value are 7-9, make rare earth ion all precipitate formation rare-earth hydroxide, i.e. the process of deposition of rare-earth.Said akaline liquid can be selected from one or more the mixture in ammoniacal liquor, waterglass, sodium metaaluminate or sodium hydroxide solution.
In above-mentioned preparation process, in step (1), said calcination process for the second time, is under 500-650 ℃, 0-100% water vapor conditions, to process 0.5-4 hour, preferred 1-3 hour.Wherein calcination process is preferred embodiment to carry out under 100% water vapor conditions for the second time.
In above-mentioned preparation process, rare earths material is well known to those skilled in the art, can be selected from rare earth chloride or nitric acid rare earth, can be rare earth chloride or the nitric acid rare earth that Rare Earth Elements Determination forms, common lanthanum chloride, lanthanum nitrate, cerium chloride or cerous nitrate etc. of comprising wherein, also can be the mishmetal of different rare earth element ratios, as rich cerium type or rich lanthanum type mishmetal.
In above-mentioned preparation process, preferred embodiment be wherein said double roasting in processing, have at least be once 1-100%, more preferably 20-100%, most preferably under 100% water vapor conditions, carry out, steam treatment impels rare earth ion to move to little cage from molecular sieve supercage, therefore, preferred embodiment is that the said double roasting processing of preparation process is all to carry out under 100% water vapor conditions.
According to the preparation method of catalytic cracking catalyst provided by the invention, described cracking activity constituent element, clay and binding agent are mixed to making beating, and follow-up spraying is dried, washs, filters and is dried, the implementation method of these operations all can adopt conventional method to implement, their specific implementation method for example has detailed description in patent application CN1916166A, CN1362472A, CN1727442A, CN1132898C, CN1727445A and CN1098130A, introduces in the lump here in the present invention with for referencial use.
The invention will be further described by the following examples.
In the following Examples and Comparative Examples, the second Y zeolite is DASY2.0 molecular sieve, rare earth oxide content 2 % by weight, and sial atomic molar, than 4.1, is produced by catalyst asphalt in Shenli Refinery of China Petrochemical Industry;
Aluminium colloidal sol is produced by catalyst asphalt in Shenli Refinery of China Petrochemical Industry, the Al of aluminium colloidal sol
2o
3content is 21.5 % by weight;
Kaolin is purchased from Suzhou China Kaolin Co., Ltd;
Boehmite is purchased from Shandong Aluminum Plant;
In each embodiment and comparative example, the chemical composition of molecular sieve is measured (referring to < < Petrochemical Engineering Analysis method (RIPP experimental technique) > > with x-ray fluorescence method, Yang Cui is the volume such as surely, Science Press, nineteen ninety publishes).The thing phase of molecular sieve and crystallinity data adopt X-ray diffraction method to measure, and the framework silicon-aluminum atomic ratio of molecular sieve adopts NMR method to measure.
Embodiment 1
(1) preparation of rare earth Y type molecular sieve
Get 2.6 kilograms of NaY molecular sieves (catalyst asphalt in Shenli Refinery of China Petrochemical Industry, the heavy % of igloss 22.5, silica alumina ratio 2.7, degree of crystallinity 88%, lower with) and 15 kilograms of deionized waters mix and pull an oar, add 1.0 liters of concentration 160gRE
2o
3the re chloride of/L and 0.24 kilogram of chloride solid, after stirring evenly, be warming up to 70 ℃ and regulate slurries pH to 4.0 with watery hydrochloric acid, continue exchange 1.5 hours, after filtering, wash, being dried, under 100% water vapor conditions in 550 ℃ of roastings 2 hours, obtain a friendship one roasting rare earth sodium Y molecular sieve Y-A1, the chemical composition of Y-A1 is the heavy % of sodium oxide molybdena 5.1, the heavy % of rare earth oxide 7.8.Then press molecular sieve: NH
4cl:H
2the ratio of O=1:0.2:10 is pulled an oar and in 70 ℃ of exchanges 1 hour, is filtered after washing, and reslurry also adds 0.27 liter of concentration 300gRE
2o
3the re chloride of/L, guarantee concentration of slurry 400-450g/L, after stirring evenly, add ammoniacal liquor to regulate slurries pH to 7.5 and continue and stir 10 minutes, dry after under 100% steam in 600 ℃ of roastings 2 hours, obtain rare earth Y type molecular sieve finished product of the present invention, be designated as Y-A.
The heavy % of sodium oxide molybdena 1.5 in Y-A, the heavy % of rare earth oxide 11.8, degree of crystallinity 50.3%, lattice constant 2.458nm, framework silicon-aluminum atomic ratio 3.5.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 89.7.
(2) preparation of catalytic cracking catalyst
The boehmite of 18 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 40 weight portion in butt, aluminium colloidal sol in 9 weight portions of butt, stir 20 minutes, add wherein more afterwards the rare earth Y type molecular sieve Y-A slurries in 33 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst C1.
Embodiment 2
The boehmite of 22 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 34 weight portion in butt, aluminium colloidal sol in 11 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve Y-A of 31 weight portions of butt with in the DASY2.0 molecular sieve mixed serum of 2 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst C2.
Embodiment 3
(1) preparation of rare earth Y type molecular sieve
Get 2.6 kilograms of NaY molecular sieves and 18 kilograms of deionized waters mixing making beating, add 1.25 liters of concentration 160gRE
2o
3the re chloride of/L and 0.12 kilogram of chloride solid, after stirring evenly, be warming up to 80 ℃ and regulate slurries pH to 3.8 with watery hydrochloric acid, continue exchange 1 hour, after filtering, wash, being dried, under 50% water vapor conditions in 570 ℃ of roastings 2 hours, obtain a friendship one roasting rare earth sodium Y molecular sieve Y-C1, the chemical composition of Y-C1 is the heavy % of sodium oxide molybdena 4.9, the heavy % of rare earth oxide 9.9.Then press molecular sieve: NH
4cl:H
2the ratio of O=1:0.15:12 is pulled an oar and in 75 ℃ of exchanges 1 hour, is filtered after washing, and reslurry also adds 0.27 liter of concentration 300gRE
2o
3the re chloride of/L, guarantee concentration of slurry 400-450g/L, after stirring evenly, add waterglass to regulate slurries pH to 8.0 and continue and stir 10 minutes, dry after under air atmosphere in 570 ℃ of roastings 2 hours, obtain rare earth Y type molecular sieve finished product of the present invention, be designated as Y-C.
The heavy % of sodium oxide molybdena 1.3 in Y-C, the heavy % of rare earth oxide 13.9, degree of crystallinity 48.8%, lattice constant 2.465nm, framework silicon-aluminum atomic ratio 3.1.The intensity I at its ° peak, 2 θ=11.8 ± 0.1
1intensity I with ° peak, 2 θ=12.3 ± 0.1
2ratio (I
1/ I
2) with molecular sieve in to take the product value of rare earth weight percentage of rare earth oxide be 55.6.
(2) preparation of catalytic cracking catalyst
The boehmite of 18 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 39 weight portion in butt, aluminium colloidal sol in 11 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve Y-C of 30 weight portions of butt with in the mixed serum of the DASY2.0 molecular sieve of 2 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst C3.
Embodiment 4
(1) preparation of rare earth Y type molecular sieve
Get 2.6 kilograms of NaY molecular sieves and 18 kilograms of deionized waters mixing making beating, add 1.25 liters of concentration 160gRE
2o
3the re chloride of/L and 0.12 kilogram of chloride solid, after stirring evenly, be warming up to 80 ℃ and regulate slurries pH to 3.8 with watery hydrochloric acid, continue exchange 1 hour, after filtering, wash, being dried, under air atmosphere in 600 ℃ of roastings 1.5 hours, obtain a friendship one roasting rare earth sodium Y molecular sieve Y-D1, the chemical composition of Y-D1 is the heavy % of sodium oxide molybdena 4.9, the heavy % of rare earth oxide 9.9; Then press molecular sieve: NH
4cl:H
2the ratio of O=1:0.15:12 is pulled an oar and in 75 ℃ of exchanges 1 hour, is filtered after washing, and reslurry also adds 0.4 liter of concentration 300gRE
2o
3the re chloride of/L, guarantee concentration of slurry 400-450g/L, after stirring evenly, add waterglass to regulate slurries pH to 8.0 and continue and stir 10 minutes, dry after under 100% steam in 570 ℃ of roastings 3 hours, obtain rare earth Y type molecular sieve finished product of the present invention, be designated as Y-D.
The heavy % of sodium oxide molybdena 1.3 in Y-D, the heavy % of rare earth oxide 15.9, degree of crystallinity 46.9%, lattice constant 2.466nm, framework silicon-aluminum atomic ratio 3.0.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 57.2.
(2) preparation of catalytic cracking catalyst
The boehmite of 22 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 37 weight portion in butt, aluminium colloidal sol in 10 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve Y-D of 28 weight portions of butt with in the mixed serum of the DASY2.0 molecular sieve of 3 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst C4.
Embodiment 5
(1) preparation of rare earth Y type molecular sieve
Get 2.6 kilograms of NaY molecular sieves and 20 kilograms of deionized waters mixing making beating, add 1.5 liters of concentration 160gRE
2o
3the re chloride of/L, after stirring evenly, be warming up to 75 ℃ and regulate slurries pH to 3.5 with watery hydrochloric acid, continue exchange 1 hour, after filtering, wash, being dried, under 100% water vapor conditions in 600 ℃ of roastings 2 hours, obtain a friendship one roasting rare earth sodium Y molecular sieve Y-E1, the chemical composition of Y-E1 is the heavy % of sodium oxide molybdena 4.8, the heavy % of rare earth oxide 11.9; Then press molecular sieve: NH
4cl:H
2the ratio of O=1:0.3:10 is pulled an oar and in 70 ℃ of exchanges 1 hour, is filtered after washing, and reslurry also adds 0.4 liter of concentration 300gRE
2o
3the re chloride of/L, guarantees concentration of slurry 400-450g/L, adds ammoniacal liquor to regulate slurries pH to 7.9 and continue and stir 10 minutes after stirring evenly, filter washing, after dry under 80% steam in 600 ℃ of roastings 2 hours, obtain rare earth Y type molecular sieve finished product of the present invention, be designated as Y-E.
The heavy % of sodium oxide molybdena 1.3 in Y-E, the heavy % of rare earth oxide 17.9, degree of crystallinity 45.2%, lattice constant 2.467nm, framework silicon-aluminum atomic ratio 3.2.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 62.6.
(2) preparation of catalytic cracking catalyst
The boehmite of 19 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 42 weight portion in butt, aluminium colloidal sol in 9 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve Y-E of 25 weight portions of butt with in the mixed serum of the DASY2.0 molecular sieve of 5 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst C5.
Embodiment 6
(1) preparation of rare earth Y type molecular sieve
Get 2.6 kilograms of NaY molecular sieves and 20 kilograms of deionized waters mixing making beating, add 1.5 liters of concentration 160gLa
2o
3the lanthanum chloride solution of/L, after stirring evenly, be warming up to 75 ℃ and regulate slurries pH to 3.5 with watery hydrochloric acid, continue exchange 1 hour, after filtering, wash, being dried, under air atmosphere in 620 ℃ of roastings 2 hours, obtain a friendship one roasting rare earth sodium Y molecular sieve Y-F1, the chemical composition of Y-F1 is the heavy % of sodium oxide molybdena 4.8, the heavy % of lanthana 11.9; Then press molecular sieve: oxalic acid: H
2the ratio of O=1:0.08:12 is pulled an oar and in 65 ℃ of exchanges 1 hour, is filtered after washing, and reslurry also adds 0.67 liter of concentration 300gLa
2o
3the lanthanum chloride solution of/L, guarantee concentration of slurry 400-450g/L, after stirring evenly, add ammoniacal liquor to regulate slurries pH to 8.2 and continue and stir 10 minutes, dry after under 100% steam in 620 ℃ of roastings 3 hours, obtain rare earth Y type molecular sieve finished product of the present invention, be designated as Y-F.
The heavy % of sodium oxide molybdena 1.5 in Y-F, the heavy % of lanthana 21.9, degree of crystallinity 41.7%, lattice constant 2.470nm, framework silicon-aluminum atomic ratio 3.1.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 70.1.
(2) preparation of catalytic cracking catalyst
The boehmite of 19 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 43 weight portion in butt, aluminium colloidal sol in 10 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve Y-F of 23 weight portions of butt with in the mixed serum of the DASY2.0 molecular sieve of 5 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst C6.
Comparative example 1
(1) preparation of rare earth Y type molecular sieve
This comparative example is the rare-earth Y molecular sieve of preparing according to method described in CN1053808A.
By NaY molecular sieve and re chloride (160gRE
2o
3/ L) and deionized water mix, regulate slurries pH to 3.5 and in 90 ℃ of exchanges 1 hour, filter, washing, filter cake is put into when pipe type calciner is warming up to 200 ℃ and is passed into steam, continue to be warming up to 550 ℃ of roastings 2 hours, by gained molecular sieve and (NH
4)
2sO
4and H
2o is in the ratio making beating of 1:0.2:40 and in 60 ℃ of exchanges 15 minutes, and filtration drying obtains comparative sample, is designated as DB-1.
The chemical composition of DB-1 is the heavy % of sodium oxide molybdena 1.3, the heavy % of rare earth oxide 12.1, degree of crystallinity 56.7%, lattice constant 2.468nm, framework si-al ratio 4.2.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 33.9.
(2) preparation of catalytic cracking catalyst
The boehmite of 18 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 40 weight portion in butt, aluminium colloidal sol in 9 weight portions of butt, stir 20 minutes, add wherein more afterwards the rare earth Y type molecular sieve DB-1 slurries in 33 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst DC-1.
Comparative example 2
(1) preparation of rare earth Y type molecular sieve
This comparative example hands over two roasting methods to prepare rare-earth Y molecular sieve according to conventional two.
By NaY molecular sieve and re chloride (160gRE
2o
3/ L) and deionized water mix by a certain percentage, exchange 1 hour at 90 ℃, filter, washing, dry after, under 520 ℃ of air atmospheres, roasting is 2 hours, by gained molecular sieve again with re chloride and H
2o pulls an oar in proportion and in 90 ℃ of exchanges 1 hour, filtration drying again carried out calcination process and obtains comparative sample, is designated as DB-2.
The chemical composition of DB-2 is the heavy % of sodium oxide molybdena 1.9, the heavy % of rare earth oxide 18.2, degree of crystallinity 43.6%, lattice constant 2.469nm, framework si-al ratio 2.7.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 16.4.
(2) preparation of catalytic cracking catalyst
The boehmite of 22 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 37 weight portion in butt, aluminium colloidal sol in 10 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve DB-2 of 28 weight portions of butt and the mixed serum of the DASY2.0 molecular sieve of 3 weight portions, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst DC-2.
Comparative example 3
(1) preparation of rare earth Y type molecular sieve
This comparative example is the rare-earth Y molecular sieve of preparing according to method described in CN100344374C.
NaY molecular sieve is mixed with deionized water and be warming up to 90 ℃, add ammonium sulfate and use salt acid for adjusting pH to 3.5-4.0, exchange after 1 hour, filter cake adds water making beating again and adds in proportion re chloride, salt acid for adjusting pH, to 3.5-5.5, stirs 1 hour under room temperature, then adds ammoniacal liquor to stir 5 minutes, after washing and drying, when weight space velocity 0.1
-1lower 540 ℃ of roastings of steam 1.5 hours; By 60 ℃ of ammonium chloride solutions washings for the molecular sieve after roasting 10 minutes, dryly obtain comparative sample, be designated as DB-3.
The chemical composition of DB-3 is the heavy % of sodium oxide molybdena 0.2, the heavy % of rare earth oxide 20.6, degree of crystallinity 50.7%, lattice constant 2.472nm, framework si-al ratio 3.7.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 26.8.
(2) preparation of catalytic cracking catalyst
The boehmite of 19 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 42 weight portion in butt, aluminium colloidal sol in 9 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve DB-3 of 25 weight portions of butt and the mixed serum of the DASY2.0 molecular sieve of 5 weight portions, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H2
oweight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst DC-3.
Comparative example 4
(1) preparation of rare earth Y type molecular sieve
This comparative example is the rare-earth Y molecular sieve of preparing according to method described in CN100344374C.
NaY molecular sieve is mixed to making beating with deionized water, then add the re chloride of metering, stir at 60 ℃ after 5 minutes with salt acid for adjusting pH between 3.5-5.5, continue to stir after 1 hour, add ammoniacal liquor to stir and filter for 5 minutes, after washing and drying, when weight space velocity 0.2
-1lower 600 ℃ of roastings of steam 1.5 hours; By 90 ℃ of ammonium chloride solutions washings for the molecular sieve after roasting 10 minutes, dryly obtain comparative sample, be designated as DB-4.
The chemical composition of DB-4 is the heavy % of sodium oxide molybdena 0.8, the heavy % of rare earth oxide 11.8, degree of crystallinity 56.5%, lattice constant 2.465nm, framework si-al ratio 3.3.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 40.1.
(2) preparation of catalytic cracking catalyst
The boehmite of 18 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 38 weight portion in butt, aluminium colloidal sol in 9 weight portions of butt, stir 20 minutes, add wherein more afterwards the rare earth Y type molecular sieve DB-4 slurries in 35 weight portions of butt, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO
4washing ((NH
4)
2sO
4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst DC-4.
Comparative example 5
(1) preparation of rare earth Y type molecular sieve
This comparative example is the rare-earth Y molecular sieve of preparing according to method described in CN100344374C.
NaY molecular sieve is mixed to making beating with deionized water, then add the re chloride of metering, stir at 60 ℃ after 5 minutes with salt acid for adjusting pH between 3.5-5.5, continue to stir after 1 hour, add ammoniacal liquor to stir and filter for 5 minutes, after washing and drying, 550 ℃ of roastings 1.5 hours; By 60 ℃ of ammonium chloride solutions washings for the molecular sieve after roasting 10 minutes, dryly obtain comparative sample, be designated as DB-5.
The chemical composition of DB-5 is the heavy % of sodium oxide molybdena 1.0, the heavy % of rare earth oxide 15.7, degree of crystallinity 52.9%, lattice constant 2.467nm, framework si-al ratio 3.6.The product value of rare earth weight percentage of rare earth oxide of take in the ratio (I1/I2) of the intensity I 2 at the intensity I 1 at its ° peak, 2 θ=11.8 ± 0.1 and ° peak, 2 θ=12.3 ± 0.1 and molecular sieve is 30.9.
(2) preparation of catalytic cracking catalyst
The boehmite of 22 weight portions in butt is mixed to making beating with deionized water, and be the hydrochloric acid peptization of 36 % by weight to adding concentration in the slurries that obtain, acid aluminum ratio (described 36 % by weight hydrochloric acid with take the weight ratio of boehmite of butt) is 0.20, be warming up to 65 ℃ of acidifyings 1 hour, add respectively the kaolinic slurries of 35 weight portion in butt, aluminium colloidal sol in 10 weight portions of butt, stir 20 minutes, add wherein more afterwards in the rare earth Y type molecular sieve DB-5 of 30 weight portions of butt and the mixed serum of the DASY molecular sieve of 3 weight portions, stir the slurries that obtain solid content 30 % by weight for 30 minutes, the dry microspherical catalyst of making of spraying.By the roasting 1 hour at 500 ℃ of this microspherical catalyst, then at 60 ℃ with (NH
4)
2sO4 washs ((NH
4)
2sO4: microspherical catalyst: H
2o weight ratio=0.05:1:10) to Na
2o content is less than 0.25 % by weight, finally uses deionized water drip washing, microspherical catalyst: H
2o weight ratio=1:10 is dried after filtration at 110 ℃, obtains catalytic cracking catalyst DC-5.
Embodiment 7
The present embodiment has been summed up the rare earth availability data of the rare earth Y type molecular sieve in embodiment 1-6 and comparative example 1-5.
The rare earth utilization rate of molecular sieve is listed in table 1
Table 1
| Sieve sample | Theoretical RE 2O 3Inventory/% | RE in product 2O 3Content/% | Rare earth utilization rate/% |
| Y-A | 12.0 | 11.8 | 98.3 |
| Y-B | 12.0 | 11.9 | 99.2 |
| Y-C | 14.0 | 13.9 | 99.3 |
| Y-D | 16.0 | 15.9 | 99.4 |
| Y-E | 18.0 | 17.9 | 99.4 |
| Y-F | 22.0 | 21.9 | 99.5 |
| DB-1 | 14.0 | 12.1 | 86.4 |
| DB-2 | 24.0 | 18.2 | 75.8 |
| DB-3 | 23.0 | 20.6 | 89.6 |
| DB-4 | 13.0 | 11.8 | 90.7 |
| DB-5 | 17.5 | 15.7 | 89.7 |
From table 1, the rare earth utilization rate of the molecular sieve that embodiment provides is all more than 98%, and comparative example middle rare earth utilization rate is lower, and the rare earth utilization rate of comparative example 2 is 75% left and right only, and the utilization rate of other comparative examples is slightly high, but substantially below 90%.Adopt of the present invention two to hand over the technique of two roastings and deposition of rare-earth effectively to improve rare earth utilization rate, reduced the waste of rare earth resources.
Embodiment 8
The present embodiment is in order to illustrate that rare earth Y type molecular sieve in embodiment 1-6 and comparative example 1-5 is in the materialization data of burin-in process after 17 hours under 800 ℃, 100% water vapor conditions.
By the molecular sieve in above-described embodiment and comparative example and ammonium chloride solution hybrid switching, by Na wherein
2o content is washed till below 0.3 heavy %, and after filtration drying, under 800 ℃, 100% water vapor conditions, burin-in process is 17 hours, carries out materialization sign and measures light oil microactivity MA.Light oil micro anti-evaluation condition: molecular sieve loading amount 2g, feedstock oil is huge port straight distillation light diesel oil, oil inlet quantity 1.56g, 460 ℃ of reaction temperatures.
The physico-chemical property characterization result of molecular sieve is in Table 2.
Table 2
| Sieve sample | RE 2O 3Content/% | Structure cell/nm | Crystallization reservation degree/% | MA |
| Y-A | 11.7 | 2.436 | 45.4 | 63 |
| Y-B | 11.8 | 2.436 | 45.9 | 63 |
| Y-C | 13.8 | 2.438 | 46.0 | 65 |
| Y-D | 15.9 | 2.439 | 46.3 | 67 |
| Y-E | 17.9 | 2.441 | 47.8 | 70 |
| Y-F | 21.8 | 2.445 | 46.0 | 72 |
| DB-1 | 11.8 | 2.433 | 27.1 | 56 |
| DB-2 | 17.1 | 2.438 | 35.0 | 65 |
| DB-3 | 19.5 | 2.441 | 39.6 | 68 |
| DB-4 | 11.8 | 2.433 | 34.9 | 56 |
| DB-5 | 14.9 | 2.436 | 38.4 | 63 |
From table 2, after sodium is washed in the friendship of molecular sieve through ammonium described in embodiment, content of rare earth does not have to change substantially, illustrate that rare earth ion is mainly positioned in the little cage of molecular sieve, can do not got off by anticommuting, rare earth ion in little cage has significant stabilization to molecular sieve structure, crystallization reservation degree surpasses more than 45%, and light oil activity is higher than the suitable contrast sample of content of rare earth.
Embodiment 9
The present embodiment is in order to illustrate the Catalytic Cracking Performance of the catalyst of embodiment 1-6 and comparative example 1-5.
Respectively by catalytic cracking catalyst C1-C6 and the DC1-DC5 of above-mentioned preparation, under 800 ℃, the condition of 100% water vapour aging 12 hours, be filled in afterwards in small fixed flowing bed ACE device (purchased from U.S. KTI company), amount of fill is 9g separately.Then, in reaction temperature, be that 510 ℃, weight (hourly) space velocity (WHSV) are under 12h-1, oil ratio (weight) condition that is 6, respectively the fcc raw material oil shown in table 3 injected to the fixed fluidized bed ACE device that is filled with described catalytic cracking catalyst C1-C6 and DC1-DC5 and carry out catalytic cracking reaction.The composition of analytical reactions product, and calculate conversion ratio according to following formula, the catalytic cracking reaction results of property of catalyst is as shown in table 4 below:
Table 3
| Density (20 ℃)/(kg/m 3) | 922.1 |
| Condensation point/℃ | 33 |
| Carbon residue/% by weight | 3.66 |
| Four component composition/% by weight | |
| Saturated hydrocarbons | 53.3 |
| Aromatic hydrocarbons | 31.5 |
| Colloid | 14.5 |
| Asphalitine | 0.7 |
| Element composition/% by weight | |
| C | 86.51 |
| H | 12.72 |
| S | 0.35 |
| N | 0.18 |
| Tenor/(μ g/g) | |
| Fe | 6.9 |
| Ni | 10.7 |
| V | 6.5 |
| Na | 0.1 |
| Ca | 1.7 |
Table 4
From table 4, in the situation that the content of rare earth of rare earth Y type molecular sieve used is suitable, catalytic cracking catalyst of the present invention shows higher activity in residual oil cracking process, and cracking reaction conversion ratio significantly improves (by embodiment 1 and comparative example 1 more visible); When content of rare earth in rare earth Y type molecular sieve used is lower, catalyst provided by the invention still can obtain higher conversion ratio (referring to embodiment 4 and comparative example 2, embodiment 5 and comparative example 3); Content of rare earth at rare earth Y type molecular sieve used is suitable, catalytic cracking catalyst provided by the invention is in the situation that the consumption of molecular sieve is less, still can obtain with existing catalyst quite or higher conversion ratio (referring to embodiment 1 and comparative example 4, embodiment 4 and comparative example 5), therefore not only the activity stability of catalyst is good in the present invention, and can reduce the production cost of catalyst.
Claims (9)
1. a catalytic cracking catalyst, contain cracking activity constituent element, clay and binding agent, wherein, described cracking activity constituent element contains rare earth Y type molecular sieve, it is characterized in that, the content of rare earth of described rare earth Y type molecular sieve is counted the heavy % of 10-25 with rare earth oxide, lattice constant is 2.440-2.472nm, degree of crystallinity is 35-65%, framework silicon-aluminum atomic ratio is 2.5-5.0, in this molecular sieve X-ray diffraction spectrogram, in the ratio (I1/I2) of the intensity I 1 at ° peak, 2 θ=11.8 ± 0.1 and the intensity I 2 at ° peak, 2 θ=12.3 ± 0.1 and molecular sieve, the product value in the rare earth weight percentage of rare earth oxide is greater than 50.
2. according to catalytic cracking catalyst claimed in claim 1, it is characterized in that, described catalytic cracking catalyst contains 10-60 % by weight cracking activity constituent element, 20-70 % by weight clay and 10-50 % by weight binding agent.
3. according to catalytic cracking catalyst claimed in claim 1, it is characterized in that, the content of rare earth of described rare earth Y type molecular sieve is counted the heavy % of 11-23 with rare earth oxide, and lattice constant is 2.450-2.470nm, and degree of crystallinity is 40-60%.
4. according to catalytic cracking catalyst claimed in claim 1, it is characterized in that, described rare earth Y type molecular sieve is being greater than 45% through 800 ℃, the crystallization reservation degree of 100% steam burin-in process after 17 hours.
5. according to the catalytic cracking catalyst of claim 1, it is characterized in that, described rare earth Y type molecular sieve is through two friendship two roastings and obtains in conjunction with deposition of rare-earth process.
6. according to catalytic cracking catalyst claimed in claim 5, it is characterized in that, said two hand over two roastings and are greater than 98% in conjunction with the rare earth utilization rate of deposition of rare-earth process.
7. according to catalytic cracking catalyst claimed in claim 1, it is characterized in that the intensity I at ° peak, 2 θ=11.8 ± 0.1 in said molecular sieve X-ray diffraction spectrogram
1intensity I with ° peak, 2 θ=12.3 ± 0.1
2ratio (I
1/ I
2) with molecular sieve in the product value of the rare earth weight percentage of rare earth oxide, be greater than 55.
8. the preparation method of the arbitrary described catalytic cracking catalyst of claim 1-7, the method comprises: the rare earth Y type molecular sieve that preparation is described; Preparation comprises the slurries of described rare earth Y type molecular sieve, binding agent and binding agent; Prepared slurries spraying is dry.
9. according to the preparation method of catalytic cracking catalyst claimed in claim 8, it is characterized in that, the preparation method of described rare earth Y type molecular sieve comprises: NaY molecular sieve is contacted to processing with earth solution or rare earth with the mixed solution of ammonium salt, after washing after filtration,, being dried, carry out calcination process for the first time, obtain rare earth sodium Y molecular sieve; Then by rare earth sodium Y molecular sieve making beating and contact with ammonium salt solution or acid solution processings, after filtration, mixes with earth solution, and to regulate the pH value of slurries be 6-10, filtration or do not filter, be dried, carries out calcination process for the second time, obtains described rare earth Y type molecular sieve again.
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| CN201210341407.1A CN103657700B (en) | 2012-09-14 | 2012-09-14 | A kind of catalytic cracking catalyst and preparation method thereof |
| SG11201501897RA SG11201501897RA (en) | 2012-09-14 | 2013-06-27 | A catalytic cracking catalyst having a rare earth-containing y zeolite and a preparation process thereof |
| JP2015531422A JP6301336B2 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst having rare earth-containing Y-type zeolite and method for producing the same |
| KR1020157009020A KR102109395B1 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst of rare earth-containing y-type molecular sieve and preparation method therefor |
| EP13837046.5A EP2896456B1 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst of rare earth-containing y-type molecular sieve and preparation method therefor |
| PCT/CN2013/000767 WO2014040365A1 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst of rare earth-containing y-type molecular sieve and preparation method therefor |
| AU2013314978A AU2013314978B2 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst of rare earth-containing Y-type molecular sieve and preparation method therefor |
| US13/929,078 US9656255B2 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst having a rare earth-containing Y zeolite and a preparation process thereof |
| RU2015113601A RU2628071C2 (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst containing ree-containing zeolite, and how to obtain it |
| TW102123169A TWI568495B (en) | 2012-09-14 | 2013-06-27 | Catalytic cracking catalyst with rare earth Y type molecular sieve and preparation method thereof |
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| CN106925335A (en) * | 2015-12-29 | 2017-07-07 | 中国石油天然气股份有限公司 | Heavy metal resistant catalytic cracking catalyst and preparation method thereof |
| CN108262056A (en) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | Catalytic cracking catalyst with adjustable pore volume and preparation method thereof |
| CN113318777A (en) * | 2020-02-28 | 2021-08-31 | 中国石油化工股份有限公司 | Catalytic cracking catalyst containing rare earth Y-type molecular sieve |
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| CN101250428A (en) * | 2008-04-07 | 2008-08-27 | 华东理工大学 | In-situ crystallization cracking catalyst and preparation method thereof |
| CN101767028A (en) * | 2008-12-31 | 2010-07-07 | 中国石油化工股份有限公司 | Preparation method of fluid catalytic cracking catalyst |
| CN102009985A (en) * | 2010-12-21 | 2011-04-13 | 南京工业大学 | MCM-22 zeolite molecular sieve with framework containing rare earth heteroatoms and preparation method thereof |
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| CN101250428A (en) * | 2008-04-07 | 2008-08-27 | 华东理工大学 | In-situ crystallization cracking catalyst and preparation method thereof |
| CN101767028A (en) * | 2008-12-31 | 2010-07-07 | 中国石油化工股份有限公司 | Preparation method of fluid catalytic cracking catalyst |
| CN102009985A (en) * | 2010-12-21 | 2011-04-13 | 南京工业大学 | MCM-22 zeolite molecular sieve with framework containing rare earth heteroatoms and preparation method thereof |
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| CN106925335A (en) * | 2015-12-29 | 2017-07-07 | 中国石油天然气股份有限公司 | Heavy metal resistant catalytic cracking catalyst and preparation method thereof |
| CN106925335B (en) * | 2015-12-29 | 2019-12-10 | 中国石油天然气股份有限公司 | Heavy metal resistant catalytic cracking catalyst and preparation method thereof |
| CN108262056A (en) * | 2016-12-30 | 2018-07-10 | 中国石油天然气股份有限公司 | Catalytic cracking catalyst with adjustable pore volume and preparation method thereof |
| CN113318777A (en) * | 2020-02-28 | 2021-08-31 | 中国石油化工股份有限公司 | Catalytic cracking catalyst containing rare earth Y-type molecular sieve |
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