CN1214977C - Method for preparing zeolite molecular sieve with high activity and stability - Google Patents
Method for preparing zeolite molecular sieve with high activity and stability Download PDFInfo
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- CN1214977C CN1214977C CN 02155602 CN02155602A CN1214977C CN 1214977 C CN1214977 C CN 1214977C CN 02155602 CN02155602 CN 02155602 CN 02155602 A CN02155602 A CN 02155602A CN 1214977 C CN1214977 C CN 1214977C
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- 239000002808 molecular sieve Substances 0.000 title claims abstract description 99
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 99
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 68
- 239000010457 zeolite Substances 0.000 title claims abstract description 68
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 67
- 238000000034 method Methods 0.000 title claims abstract description 34
- 230000000694 effects Effects 0.000 title claims abstract description 30
- 239000012065 filter cake Substances 0.000 claims abstract description 29
- 150000003863 ammonium salts Chemical group 0.000 claims abstract description 18
- -1 filtering Substances 0.000 claims abstract description 18
- 238000005406 washing Methods 0.000 claims abstract description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 14
- 239000003513 alkali Substances 0.000 claims abstract description 13
- 239000002002 slurry Substances 0.000 claims abstract description 12
- 238000003756 stirring Methods 0.000 claims abstract description 9
- 238000010335 hydrothermal treatment Methods 0.000 claims abstract description 6
- 238000001914 filtration Methods 0.000 claims abstract 2
- 229910052761 rare earth metal Inorganic materials 0.000 claims description 24
- 238000002360 preparation method Methods 0.000 claims description 22
- NLXLAEXVIDQMFP-UHFFFAOYSA-N Ammonia chloride Chemical compound [NH4+].[Cl-] NLXLAEXVIDQMFP-UHFFFAOYSA-N 0.000 claims description 13
- 239000000243 solution Substances 0.000 claims description 12
- 239000007787 solid Substances 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 9
- 235000019270 ammonium chloride Nutrition 0.000 claims description 8
- 150000002910 rare earth metals Chemical class 0.000 claims description 8
- BFNBIHQBYMNNAN-UHFFFAOYSA-N ammonium sulfate Chemical group N.N.OS(O)(=O)=O BFNBIHQBYMNNAN-UHFFFAOYSA-N 0.000 claims description 7
- 229910052921 ammonium sulfate Inorganic materials 0.000 claims description 7
- 235000011130 ammonium sulphate Nutrition 0.000 claims description 7
- PAWQVTBBRAZDMG-UHFFFAOYSA-N 2-(3-bromo-2-fluorophenyl)acetic acid Chemical compound OC(=O)CC1=CC=CC(Br)=C1F PAWQVTBBRAZDMG-UHFFFAOYSA-N 0.000 claims description 6
- 229910002651 NO3 Inorganic materials 0.000 claims description 5
- 239000003637 basic solution Substances 0.000 claims description 5
- 238000007385 chemical modification Methods 0.000 claims description 4
- 239000004254 Ammonium phosphate Substances 0.000 claims description 3
- 229910000148 ammonium phosphate Inorganic materials 0.000 claims description 3
- 235000019289 ammonium phosphates Nutrition 0.000 claims description 3
- MNNHAPBLZZVQHP-UHFFFAOYSA-N diammonium hydrogen phosphate Chemical compound [NH4+].[NH4+].OP([O-])([O-])=O MNNHAPBLZZVQHP-UHFFFAOYSA-N 0.000 claims description 3
- 150000003839 salts Chemical class 0.000 claims description 3
- 235000002639 sodium chloride Nutrition 0.000 claims description 3
- ILRRQNADMUWWFW-UHFFFAOYSA-K aluminium phosphate Chemical compound O1[Al]2OP1(=O)O2 ILRRQNADMUWWFW-UHFFFAOYSA-K 0.000 claims description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 claims description 2
- 239000011707 mineral Substances 0.000 claims description 2
- 150000007530 organic bases Chemical class 0.000 claims description 2
- 230000014759 maintenance of location Effects 0.000 abstract description 6
- 230000003197 catalytic effect Effects 0.000 abstract description 2
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 230000000052 comparative effect Effects 0.000 description 14
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 8
- 150000002500 ions Chemical class 0.000 description 7
- 239000008367 deionised water Substances 0.000 description 6
- 229910021641 deionized water Inorganic materials 0.000 description 6
- 238000010438 heat treatment Methods 0.000 description 6
- 238000010792 warming Methods 0.000 description 6
- 239000003643 water by type Substances 0.000 description 6
- 150000001412 amines Chemical group 0.000 description 5
- 238000006243 chemical reaction Methods 0.000 description 5
- 229910021529 ammonia Inorganic materials 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 241000370738 Chlorion Species 0.000 description 3
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 3
- 239000007864 aqueous solution Substances 0.000 description 3
- 238000004523 catalytic cracking Methods 0.000 description 3
- 125000000129 anionic group Chemical group 0.000 description 2
- 238000001354 calcination Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 229910001723 mesolite Inorganic materials 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 229910001404 rare earth metal oxide Inorganic materials 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N sodium oxide Chemical compound [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 description 2
- 229910001948 sodium oxide Inorganic materials 0.000 description 2
- 230000006641 stabilisation Effects 0.000 description 2
- 238000011105 stabilization Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 description 1
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 1
- 238000002441 X-ray diffraction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 239000004411 aluminium Substances 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 235000011114 ammonium hydroxide Nutrition 0.000 description 1
- 229910021417 amorphous silicon Inorganic materials 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000000975 co-precipitation Methods 0.000 description 1
- 238000004737 colorimetric analysis Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 239000000796 flavoring agent Substances 0.000 description 1
- 235000019634 flavors Nutrition 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 230000003993 interaction Effects 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000003137 locomotive effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 239000011574 phosphorus Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 230000035484 reaction time Effects 0.000 description 1
- 239000012266 salt solution Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000000758 substrate Substances 0.000 description 1
- 230000003313 weakening effect Effects 0.000 description 1
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- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
A process for preparing zeolite molecular sieve with high activity and stability includes such steps as ammonium salt exchange of zeolite molecular sieve slurry, filtering, alkali washing of filter cake, adding RE solution to filter cake, stirring and hydrothermal treatment. Compared with the conventional water washing method, the modified molecular sieve prepared by the invention has the characteristics of high crystallinity retention rate, good catalytic activity stability, simple and convenient operation and low cost.
Description
Technical field
The invention relates to a kind of method for preparing the high-activity stable zeolite molecular sieve, exactly, is the method that a kind of preparation is applicable to the high-activity stable zeolite molecular sieve of catalytic cracking of hydrocarbon process.
Background technology
Be used to prepare FCC catalyst zeolite molecular sieve and mainly contain X type, y-type zeolite, ZSM-5, β zeolite, L zeolite, sour aluminium zeolite, omega zeolite, or the above-mentioned zeolite molecular sieve of process physics or chemical modification.These zeolite molecular sieves one or more and substrate material often mix, and make so-called FCC catalyzer through overmolding and are used for the catalytic cracking reaction process.
In order to improve the stability of catalytic activity of catalytic cracking process mesolite molecular sieve, people adopt various modification technologies to handle zeolite molecular sieve usually.Relatively typical method is: adopt various ammonium salt exchange NaY molecular sieves to make NH
4Y, calcination process under high-temperature vapor atmosphere again, obtain littler than its parent NaY molecular sieve lattice constant, framework si-al ratio is high, the super-stable Y molecular sieves of good hydrothermal stability.Handle through aforesaid method, the active centre number of zeolite descends to some extent.For improving the molecular sieve activity, can in zeolite, introduce element compounds such as rare earth, phosphorus, faujusite is through after the rare earth exchanged modification, the hydrothermal stability of the REY that obtains, REX, REHY, REHX zeolite can be improved (as USP4218307, USP3595611); CN86107598A discloses with coprecipitation mode and introduced rare earth oxide or rare earth hydrate in faujusite, also helps to improve the hydro-thermal activity stability of zeolite [molecular sieve.In addition, CN1024680A has reported in the super stabilizing process, introduces amorphous Si O in molecular sieve
2, can effectively improve the structural stability of molecular sieve.
In above-mentioned various method of modifying, all relate to and adopt ammonium salt exchange na-pretreated zeolite molecular sieve, usually the ammonium salt type that adopts has ammonium sulfate, ammonium nitrate, volatile salt, ammonium phosphate, ammonium chloride, and when carrying out permutoid reaction, the negatively charged ion of these ammonium salts is incorporated in the zeolite molecular sieve inevitably.When modified molecular screen exists sulfate ion, nitrate ion, chlorion, when the superheated vapor roasting, produce SO
x, NO
x, Cl
2Deng obnoxious flavour, both contaminate environment was corroded production unit again.Even more serious is, sulfate ion and chlorion can form corresponding acidic substance at the steam roasting process, the saboteur sieves degree of crystallinity, wherein there are interaction in sulfate ion and rare earth ion, hinder the locomotory movement of rare earth ion to y-type zeolite molecular sieve intracrystalline, reduced the static stabilization of rare earth ion to framework of molecular sieve, finally caused the degree of crystallinity of modified molecular screen to descend, activity stability is poor.Usually adopt the way of washing to remove these negatively charged ion at present in the industrial production, but this method need consume a large amount of washing water, especially when adopting the belt filter to carry out the molecular sieve exchange in the industrial production, because ammonium salt solution recycles, negatively charged ion such as sulfate radical can constantly be accumulated on molecular sieve, cause these anionic eliminating efficiencies to descend, in this case, negatively charged ion is particularly serious to the influence of molecular sieve crystallinity.
Summary of the invention
At the problems referred to above that exist in the present zeolite molecular sieve modifying process, the purpose of this invention is to provide the method that a kind of preparation has the high-activity stable zeolite molecular sieve, this method can remove the negatively charged ion of introducing in the molecular sieve exchange process effectively, thereby obviously improve the degree of crystallinity retention rate and the activity stability of modifying process mesolite molecular sieve, this method has characteristics easy and simple to handle, with low cost simultaneously.
Method provided by the invention is: after the zeolite molecular sieve slurries carry out the ammonium salt exchange, filter, filter cake is carried out alkali cleaning, and add earth solution in filter cake, carry out hydrothermal treatment consists after stirring.
Zeolite molecular sieve of the present invention is selected from y-type zeolite, L zeolite, ZSM-5 zeolite, β zeolite, aluminum phosphate zeolite, omega zeolite for one or more, preferred y-type zeolite, ZSM-5 zeolite, β zeolite, or the above-mentioned zeolite of conventional physics of process or chemical modification, comprise HY, USY, REY, REHY, REUSY, H-ZSM-5, H β.The zeolite molecular sieve slurry solid content is 50～450 grams per liters, preferably 150～400 grams per liters.
Ammonium salt of the present invention is selected from ammonium sulfate, ammonium nitrate, volatile salt, ammonium phosphate, ammonium chloride for one or more, preferably ammonium sulfate, ammonium chloride, ammonium nitrate.Described ammonium salt give-and-take conditions are ammonium salt/molecular sieve (weight)=0.05～1.0, and are best 0.1～0.8, water/molecular sieve (weight)=3～15, preferably 5～10, pH=2～5,50～100 ℃ of exchange temperature, 0.1～1.5 hour swap time.
The said alkali cleaning of the present invention refers to basic solution the molecular sieve filter cake be washed, wherein basic solution is the solution that contains mineral alkali such as ammoniacal liquor, organic bases such as quaternary amine, pH=10～14, alkali lye/molecular sieve (weight)=2～15, wash temperature is 10～100 ℃, preferably 30～80 ℃, washing time 0.02～1 hour, best 0.03～0.8 hour.
Earth solution of the present invention is rare earth chloride, rare earth nitrate, and the rare earth additional proportion is RE
2O
3/ molecular sieve (weight)=0.001～0.15, preferably RE
2O
3/ molecular sieve (weight)=0.01～0.10.
Hydrothermal treatment consists condition of the present invention be the molecular sieve filter cake at 400～700 ℃, roasting is 0.3～3.5 hour under 1～100% steam, best 0.5～2.5 hour.
Compare with conventional water washing method, the alkali cleaning method that the present invention adopts is by weakening the adsorption of ammonium salt negatively charged ion on the molecular sieve surface, improved anionic removal efficiency, thereby reduce the destruction of negatively charged ion to framework of molecular sieve, simultaneously because the filter cake after the alkali cleaning is an alkaline state, rare earth ion that helps introducing subsequently and hydroxide radical effect form oxyhydroxide, rare earth takes place to have improved the stabilization of framework of molecular sieve greatly from the transporting action of molecular sieve surface to super large cage and little cage easily in the hydrothermal treatment consists process like this.Therefore, adopt the modified molecular screen of the inventive method preparation to have high degree of crystallinity retention rate and activity stability.
Embodiment
Further set forth characteristics of the present invention below, but these examples can not limit the present invention with embodiment.
(1) main analytical procedure in the example
1. content of rare earth, chlorion: colorimetry.
2. sulfate radical: calcination weighting method.
3. relative crystallinity: X-ray diffraction method.
4. micro-activity: sample was handled 10 hours under 800 ℃, 100% water vapor conditions in advance.Reaction raw materials is the huge port solar oil, 460 ℃ of temperature of reaction, in 70 seconds reaction times, catalyzer loading amount 5.0 gram, agent weight of oil be than 3.2, with total conversion rate as micro-activity.
(2) raw materials used specification in the example
1.NaY molecular sieve, relative crystallinity 89%, unit cell parameters 2.472nm, industrial salable product; HY, USY, REUSY, REHY, ZSM-5, β zeolite are the qualified middle product of industry.
2. rare earth nitrate: RE
2O
3218 grams per liters; Rare earth chloride; RE
2O
3223 grams per liters are industrial goods.
3. industrial ammonia: concentration 15%; The solid quaternary amine, salable product.
4. ammonium salt: ammonium sulfate, ammonium chloride, ammonium nitrate are industrial salable product.
Embodiment 1
In having the reactor of heating, add 100 gram NaY molecular sieve and a certain amount of deionized waters, making solid content is 250 grams per liter slurries, add 50 gram ammonium sulfate again, stir, regulator solution pH is 3.2, be warming up to 95 ℃, reacted 1.5 hours, filter then, molecular sieve filter cake pH is 13, temperature is that 85 ℃ ammonia soln washs, and then filter cake and 23ml rare earth nitrate is mixed, 50% steam and 600 ℃ of following roastings 2.5 hours, make the modified molecular screen sample A of the present invention's preparation.
Comparative Examples 1
The deionized water that molecular sieve filter cake washing among the embodiment 1 is changed into 85 ℃ washs, and other modified condition and add-on are constant, makes contrast modified molecular screen sample A1.
Embodiment 2
In having the reactor of heating, add 100 gram HY molecular sieve and a certain amount of deionized waters, making solid content is 350 grams per liter slurries, add 70 gram ammonium nitrate again, stir, regulator solution pH is 2.8, be warming up to 85 ℃, reacted 1 hour, filter then, molecular sieve filter cake pH is 12.5, temperature is that 75 ℃ the quaternary amine aqueous solution washs, and then filter cake and 35ml rare earth chloride is mixed, 30% steam and 550 ℃ of following roastings 2.0 hours, make the molecular sieve modified sample B of the present invention's preparation.
Comparative Examples 2
The deionized water that molecular sieve filter cake washing among the embodiment 2 is changed into 75 ℃ washs, and other modified condition and add-on are constant, makes contrast modified molecular screen sample B1.
Embodiment 3
In having the reactor of heating, add 100 gram REHY molecular sieve and a certain amount of deionized waters, making solid content is 150 grams per liter slurries, add 50 gram ammonium chlorides again, stir, regulator solution pH is 3.8, be warming up to 75 ℃, reacted 0.5 hour, filter then, molecular sieve filter cake pH is 12.0, temperature is that 70 ℃ the quaternary amine aqueous solution washs, and then filter cake and 11.5ml rare earth chloride is mixed, 70% steam and 500 ℃ of following roastings 1.5 hours, make the molecular sieve modified sample C of the present invention's preparation.
Comparative Examples 3
The deionized water that molecular sieve filter cake washing in the example 3 is changed into 70 ℃ washs, and other modified condition and add-on are constant, makes contrast modified molecular screen sample C1.
Embodiment 4
In having the reactor of heating, add 100 gram USY molecular sieve and a certain amount of deionized waters, making solid content is 200 grams per liter slurries, add 30 gram ammonium chlorides again, stir, regulator solution pH is 3.8, be warming up to 90 ℃, reacted 0.5 hour, filter then, molecular sieve filter cake pH is 12.8, temperature is that 65 ℃ ammonia soln washs, and then filter cake and 10ml rare earth chloride is mixed, 70% steam and 500 ℃ of following roastings 1.0 hours, make the molecular sieve modified sample D of the present invention's preparation.
Comparative Examples 4
The deionized water that molecular sieve filter cake washing in the example 4 is changed into 65 ℃ washs, and other modified condition and add-on are constant, makes contrast modified molecular screen sample D1.
Embodiment 5
In having the reactor of heating, add 100 gram ZSM-5 molecular sieve and a certain amount of deionized waters, making solid content is 280 grams per liter slurries, add 20 gram ammonium sulfate again, stir, regulator solution pH is 3.7, be warming up to 82 ℃, reacted 0.7 hour, filter then, molecular sieve filter cake pH is 11.5, temperature is that 60 ℃ ammonia soln washs, and then filter cake and 8ml rare earth nitrate is mixed, 75% steam and 550 ℃ of following roastings 0.8 hour, make the molecular sieve modified sample E of the present invention's preparation.
Comparative Examples 5
The deionized water that molecular sieve filter cake washing in the example 5 is changed into 60 ℃ washs, and other modified condition and add-on are constant, makes contrast modified molecular screen sample E1.
Embodiment 6
In having the reactor of heating, add 100 gram beta-molecular sieve and a certain amount of deionized waters, making solid content is 200 grams per liter slurries, add 30 gram ammonium chlorides again, stir, regulator solution pH is 3.8, be warming up to 70 ℃, reacted 0.8 hour, filter then, molecular sieve filter cake pH is 12.8, temperature is that 65 ℃ the quaternary amine aqueous solution washs, and then filter cake and 6.5ml rare earth chloride is mixed, 70% steam and 500 ℃ of following roastings 0.6 hour, make the molecular sieve modified sample F of the present invention's preparation.
Comparative Examples 6
The deionized water that molecular sieve filter cake washing in the example 6 is changed into 65 ℃ washs, and other modified condition and add-on are constant, makes contrast modified molecular screen sample F 1.
The experimental result of embodiment 1～6 and Comparative Examples 1～6 is listed in the table 1, by table 1 data as can be known, compare with conventional water washing method, adopt the degree of crystallinity retention rate of Y type modified molecular screen of alkali cleaning method of the present invention preparation and reactive behavior all high 5 more than the unit, the degree of crystallinity retention rate of the modified molecular screen of embodiment 2 is than the result of Comparative Examples 2 even high 13 units; For ZSM-5 or beta-zeolite molecular sieve, because the structural stability of molecular sieve itself is higher, the stable increase rate of modified molecular screen decreases, and also can improve 2 substantially more than the unit.Above result shows that modified molecular screen provided by the invention has obviously improved the molecular sieve activity stability.
The character of table 1 modified molecular screen
| Molecular sieve | Experiment numbers | Sodium oxide m% | Rare earth oxide m% | Relative crystallinity, m% | The degree of crystallinity retention rate, % | The molecular sieve activity, m% | |
| Unaged | Aging (800 * 2h) | ||||||
| A | Embodiment 1 | 4.1 | 4.8 | 75 | 45 | 60 | / * |
| A1 | Comparative Examples 1 | 4.2 | 4.7 | 65 | 35 | 54 | / * |
| B | Embodiment 2 | 0.4 | 7.5 | 60 | 45 | 75 | 65 |
| B1 | Comparative Examples 2 | 0.5 | 7.6 | 52 | 32 | 62 | 60 |
| C | Embodiment 3 | 0.6 | 9.5 | 50 | 32 | 64 | 66 |
| C1 | Comparative Examples 3 | 0.5 | 9.3 | 43 | 25 | 58 | 57 |
| D | Embodiment 4 | 0.5 | 2.1 | 62 | 50 | 81 | 59 |
| D1 | Comparative Examples 4 | 0.7 | 2.0 | 57 | 43 | 75 | 50 |
| E | Embodiment 5 | 0.3 | 1.7 | 85 | 65 | 76 | 34 |
| E1 | Comparative Examples 5 | 0.2 | 1.6 | 83 | 60 | 72 | 32 |
| F | Embodiment 6 | 0.4 | 1.4 | 78 | 64 | 82 | 45 |
| F1 | Comparative Examples 6 | 0.4 | 1.3 | 75 | 60 | 80 | 42 |
*The sodium oxide of molecular sieve-4 A and A1 is too high, and micro-activity is difficult to accurate mensuration.
Claims (13)
1. a method for preparing the high-activity stable zeolite molecular sieve is characterized in that filtering after the zeolite molecular sieve slurries carry out the ammonium salt exchange, filter cake is carried out alkali cleaning, and add earth solution in filter cake, carries out hydrothermal treatment consists after stirring; Wherein alkali cleaning refers to basic solution the molecular sieve filter cake be washed, wherein basic solution is the solution that contains mineral alkali, organic bases, and pH is 10～14, and the weight ratio of basic solution/molecular sieve is 2～15, the wash temperature of alkali cleaning is 10～100 ℃, and washing time is 0.02～1 hour.
2. the preparation method of high-activity stable zeolite molecular sieve according to claim 1, it is characterized in that described zeolite molecular sieve is selected from y-type zeolite, L zeolite, ZSM-5 zeolite, β zeolite, aluminum phosphate zeolite, omega zeolite for one or more, or the above-mentioned zeolite of conventional physics of process or chemical modification.
3. the preparation method of high-activity stable zeolite molecular sieve according to claim 1, it is characterized in that described zeolite molecular sieve is selected from y-type zeolite, ZSM-5 zeolite, β zeolite for one or more, or the above-mentioned zeolite of conventional physics of process or chemical modification.
4. the preparation method of high-activity stable zeolite molecular sieve according to claim 1 is characterized in that described zeolite molecular sieve slurry solid content is 50～450 grams per liters.
5. the preparation method of high-activity stable zeolite molecular sieve according to claim 1 is characterized in that described zeolite molecular sieve slurry solid content is 150～400 grams per liters.
6. the preparation method of high-activity stable zeolite molecular sieve according to claim 1 is characterized in that described ammonium salt is selected from ammonium sulfate, ammonium nitrate, volatile salt, ammonium phosphate, ammonium chloride for one or more.
7. the preparation method of high-activity stable zeolite molecular sieve according to claim 1, it is characterized in that described ammonium salt give-and-take conditions are that ammonium salt/molecular sieve weight ratio is 0.05～1.0, the weight ratio of water/molecular sieve is 3～15, pH is 2～5,50～100 ℃ of exchange temperature, 0.1～1.5 hour swap time.
8. the preparation method of high-activity stable zeolite molecular sieve according to claim 1, it is characterized in that described ammonium salt give-and-take conditions are that ammonium salt/molecular sieve weight ratio is 0.1～0.8, water/molecular sieve weight ratio is 5～10, pH is 2～5,50～100 ℃ of exchange temperature, 0.1～1.5 hour swap time.
9. the preparation method of high-activity stable zeolite molecular sieve according to claim 1, the wash temperature that it is characterized in that described alkali cleaning is 30～80 ℃, washing time is 0.03～0.8 hour.
10. the preparation method of high-activity stable zeolite molecular sieve according to claim 1 is characterized in that described earth solution is rare earth chloride, rare earth nitrate.
11. the preparation method of high-activity stable zeolite molecular sieve according to claim 1 is characterized in that the rare earth additional proportion is RE
2O
3The weight ratio of/molecular sieve is 0.001～0.15.
12. the preparation method of high-activity stable zeolite molecular sieve according to claim 1 is characterized in that the rare earth additional proportion is RE
2O
3The weight ratio of/molecular sieve is 0.01～0.10.
13. the preparation method of high-activity stable zeolite molecular sieve according to claim 1, it is characterized in that described hydrothermal treatment consists condition be the molecular sieve filter cake at 400～700 ℃, roasting is 0.3～3.5 hour under 1～100% steam.
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| CN103962177B (en) * | 2013-01-31 | 2016-08-24 | 中国石油化工股份有限公司 | A kind of preparation method of the catalyst containing molecular sieve |
| CN104108728B (en) * | 2013-04-18 | 2016-04-27 | 中国石油化工股份有限公司 | A kind of SAPO-11 molecular sieve |
| CN106927482B (en) * | 2015-12-29 | 2019-09-03 | 中国石油天然气股份有限公司 | Preparation method of ultrastable Y-type molecular sieve |
| CN106927483B (en) * | 2015-12-29 | 2019-09-03 | 中国石油天然气股份有限公司 | Preparation method of modified Y-type molecular sieve |
| CN107473238B (en) * | 2016-06-08 | 2019-11-01 | 中国石油化工股份有限公司 | A kind of KL molecular sieve and its preparation method and application |
| CN108976848A (en) * | 2018-05-24 | 2018-12-11 | 胡春宇 | Nano rare earth zeolite coating |
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