CN101514005B - Magadiite-beta zeolite coexisting material and method for synthesizing same - Google Patents
Magadiite-beta zeolite coexisting material and method for synthesizing same Download PDFInfo
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- CN101514005B CN101514005B CN2008100431115A CN200810043111A CN101514005B CN 101514005 B CN101514005 B CN 101514005B CN 2008100431115 A CN2008100431115 A CN 2008100431115A CN 200810043111 A CN200810043111 A CN 200810043111A CN 101514005 B CN101514005 B CN 101514005B
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- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
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- Y02P30/20—Technologies relating to oil refining and petrochemical industry using bio-feedstock
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P30/00—Technologies relating to oil refining and petrochemical industry
- Y02P30/40—Ethylene production
Abstract
The invention relates to a magadiite-beta zeolite coexisting material and a method for synthesizing the same, and mainly solves the problems that a porous material synthesized by the prior art is single and nonadjustable in pore-size distribution. The method prepares a magadiite-beta zeolite coexisting material by well controlling the nucleating and growing process of a molecular sieve during a synthesis process of beta zeolite molecular sieve material. The coexistence phase ratio of the magadiite-beta zeolite coexisting material is adjustable, and a mole relation of the components of the synthesized magadiite-beta zeolite coexisting material is nSiO2 :Al2O3, wherein n is between 20 and 2,000; the magadiite-beta zeolite coexisting material has two coexistence phases, the XRD diffraction pattern of the magadiite-beta zeolite coexisting material comprises a technical proposal that a maximum value of a distance d is at positions between 15.73-0.1 and 15.73+0.1 A, 11.14-0.1 and 11.14+0.1 A, 9.97-0.1 and 9.97+0.1 A, 7.74-0.1 and 7.74+0.1 A, 5.14-0.1 and 5.14+0.1 A, 3.86-0.05 and 3.86+0.05 A, 3.66-0.05 and 3.66+0.05 A, 3.45-0.05 and 3.45+0.05 A, 3.30-0.05 and 3.30+0.05 A, and 3.14-0.1 and 3.14+0.1 A; therefore, the problems are solved well. The magadiite-beta zeolite coexisting material can be used in the industrial production of ethylene and propylene through the dehydration of methanol.
Description
Technical field
The present invention relates to a kind of Magadiite/ beta zeolite coexisting material and synthetic method thereof.
Background technology
β zeolite porous material is applied in field of petrochemical industry widely owing to have good shape selective catalysis performance and thermostability preferably.But, can not handle complicated component because β zeolitic material aperture is evenly single, bore dia is difficult for regulated at will.Magadiite is the two-dimensional layered structure material, its laminate is made up of electronegative Si-0 tetrahedron, thereby has a thermostability preferably, Magadiite has some typical propertieies of charged layer structure material, for example to the absorption of water and some small molecules polarity organic molecules, interlayer has the hydration sodium ion that can be exchanged, has swelling property preferably between the laminate, the little proton that arrives be can hold and polymer equimolecular or group arrived greatly, Na-magadiite can be converted into the H-magadiite solid peracid of crystalline state, and these character have promoted Magadiite in the application aspect cationite and catalyzer.The regularity of Magadiit layer structure and interlamellar spacing controllability make it become the catalytic material that broad prospect of application is arranged in the catalytic field.Contain the Magadiite/ beta zeolite coexisting material of two kinds of components, contain multi-stage artery structure, the aperture is adjustable, can handle molecular diameter complex component not of uniform size, and can bring into play their concerted catalysis effect.
Document CN1565967A, CN1565970A report adopts ZSM-5 molecular sieve or mordenite as crystal seed, adds respectively in the resulting solution of mordenite or ZSM-5 molecular sieve, has synthesized the mixed crystal material of ZSM-5 and mordenite.Its catalytic effect is better than the effect of two kinds of molecular sieve mechanically mixing, but needs to add different crystal seeds in the building-up process as inductor, also needs to add fluorochemical in addition, and building-up process is comparatively complicated.
Document CN1393403 report adopts the method for segmentation crystallization to synthesize middle mesoporous-microporous composite molecular sieve composition, is used for heavy oil upgrading.Synthetic method is to prepare the reaction mixture gel of synthetic microporous molecular sieve earlier, under 30～300 ℃ of conditions, carry out the crystallization of fs then, after the crystallization 3～300 hours, the pH value of adjusting reaction mixture is 9.5～12, and the synthetic used template of mesoporous molecular sieve of adding, and then at 30～170 ℃ from depressing the hydrothermal crystallizing that carries out subordinate phase, crystallization time is 15～480 hours, mesoporous-microporous composite molecular sieve composition in obtaining, but the building-up process of molecular sieve needs the segmentation crystallization, and the pH value also will be regulated in the centre, and synthetic method is also comparatively complicated.
Document CN03133557.8 has reported and has synthesized the composite structure molecular sieve with TON and two kinds of structures of MFI under the static conditions, this molecular sieve has added a spot of crystal seed and salt in the preparation gelation process, control suitable crystallization parameter, can obtain the molecular sieve of two kinds of crystal formation different ratioss, silica alumina ratio obtains the reaction process that composite molecular screen of the present invention can be used for mixture such as petroleum fractions greater than 50 on the lattice of molecular sieve.Building-up process of the present invention also needs to add crystal seed and salt.
Document CN1583562 has reported a kind of double-micropore zeolites molecular sieve and preparation method, it is characterized in that adopting orderly synthesis method, tentatively synthesizes y-type zeolite by certain material proportion earlier; After it is mixed with the tetraethyl-amine bromide solution that is dissolved with ammoniacal liquor, adding a certain amount of silicon sol at last more fully stirs and makes it even, in 130 ℃～140 ℃ following crystallization 4～7 days, obtain having the composite zeolite molecular sieve of the two microvoid structures of Y/ β, this method is also similar with the segmentation crystallization.
Document CN1632115 report utilizes the self-assembling method of biological enzyme at Magadiite stratified material interlayer, prepared a kind of layered silicate interlayer fixed biological enzyme nano composite material, this nano composite material is similar to the structure of sandwich, the phyllosilicate nano particle keeps original structure constant as enzyme immobilization carrier, and myohaemoglobin and oxyphorase are fixed between the silicate laminate.This material catalytic activity in organic solvent is higher than biological enzyme freely.The document does not relate to the symbiosis problem of Magadiite material and in the application of other catalytic fields.
Summary of the invention
Technical problem to be solved by this invention one of be that prior art synthetic aperture of porous material is single, problem that bore dia can not regulated at will.A kind of new Magadiite/ beta zeolite coexisting material is provided, and this Magadiite/ beta zeolite coexisting material has multi-stage artery structure, the characteristics that the aperture can be regulated; Two of technical problem to be solved by this invention is the problems that do not relate to above-mentioned Magadiite/ beta zeolite coexisting material preparation method in the prior art, and a kind of preparation method of new Magadiite/ beta zeolite coexisting material is provided.
For one of solving the problems of the technologies described above, the technical solution used in the present invention is as follows: a kind of Magadiite/ beta zeolite coexisting material, the composition with following molar relationship: nSiO
2: Al
2O
3, n=20 in the formula～2000, wherein said Magadiite/ beta zeolite coexisting material has two kinds of Symbiont phases, its XRD diffracting spectrum is included in 15.73 ± 0.1, and 11.32 ± 0.05,11.14 ± 0.05,9.97 ± 0.1,7.74 ± 0.1,5.14 ± 0.1,4.15 ± 0.04,3.96 ± 0.04,3.85 ± 0.05,3.65 ± 0.05,3.45 ± 0.08,3.30 ± 0.05,3.14 there is d-spacing maximum value at ± 0.05,3.02 ± 0.05 dust places.
In the technique scheme, nSiO
2: Al
2O
3The preferable range of n is n=40～1000 in the formula, contains two kinds of Symbionts of ZSM-5 molecular sieve and Magadiite in the Magadiite/ beta zeolite coexisting material at least mutually, and Symbiont phase adjustable ratio.
For solve the problems of the technologies described above two, the technical solution used in the present invention is as follows: a kind of synthetic method of Magadiite/ beta zeolite coexisting material may further comprise the steps:
(1) silicon source, aluminium source, alkali source, template M and water are mixed;
(2) SiO to contain in the silicon source
2Weight is benchmark, adds an amount of crystal seed in above-mentioned mixing solutions, and amount of seed is SiO
20.01～20% of weight, crystal seed are SiO
2/ Al
2O
3Mol ratio is 10～200 the crystal grain that the contains β zeolite precursor body amorphous substance in 1～500 nanometer;
(3) reaction mixture with molar ratio computing is: SiO
2/ Al
2O
3=20～2000, Na
2O/SiO
2=0.02～8, M/SiO
2=0.05～3.0, H
2O/SiO
2=10～500, the pH value of regulator solution is between 8～14;
(4) the above-mentioned reaction mixture that will mix is put into closed pressure vessel under autogenous pressure, and 80～220 ℃, crystallization 8～200 hours;
(5) crystallization is good product takes out, and washing is filtered, and after the drying, makes the Magadiite/ beta zeolite coexisting material; Wherein used silicon source is to be selected from least a in organosilicon, soft silica, silicon sol, solid oxidation silicon, silica gel, diatomite or the water glass; Used aluminium source is at least a in the oxide compound of the oxyhydroxide that is selected from aluminate, meta-aluminate, aluminium salt, aluminium, aluminium or the aluminiferous mineral; Used alkali source is to be selected from least a in the alkali-metal oxyhydroxide; Template used dose of M is selected from least a in organic amine or the inorganic ammonium.
In the technique scheme, reaction mixture is with molar ratio computing, and preferable range is: SiO
2/ Al
2O
3=40～1000, Na
2O/SiO
2=0.1～4, M/SiO
2=0.1～3.0, H
2O/SiO
2=20～300, crystal seed is SiO
2/ Al
2O
3The mol ratio preferable range is 20～100 the crystal grain preferable range that the contains β zeolite precursor body amorphous substance in 10～400 nanometers, and the amount of seed preferable range is SiO
20.1～10% of weight; Used organic amine preferred version is to be selected from least a in 4-propyl bromide, TPAOH, tetraethylammonium bromide, tetraethyl ammonium hydroxide, Tetrabutyl amonium bromide, TBAH, triethylamine, n-Butyl Amine 99, quadrol or the ethamine, when selecting mixed templates for use, mol ratio is 1: 1 or 1: 1: 1 (selecting three kinds of template for use); Inorganic ammonium preferred version is to be selected from least a in ammoniacal liquor, the ammonium salt; The pH value is regulated with dilute acid soln, and the preferred version of used dilute acid soln is at least a in dilute hydrochloric acid, dilute sulphuric acid, rare nitric acid, dilute phosphoric acid, oxalic acid or the acetate, and the preferable range of regulating the pH value is between 8～14, and more preferably scope is between 9～14; The crystallization temperature preferable range is 100～200 ℃, and the crystallization time preferable range is 10～60 hours.
The synthetic method concrete operations of Magadiite/ beta zeolite coexisting material are, get silicon source, alkali source template M and the aluminium source of aequum by material proportion, make solution with dissolved in distilled water respectively, then two kinds of solution are mixed, the powerful stirring, stir after 30 minutes and regulate the pH value in 8～14 scopes, supply distilled water again with dilute acid soln.Colloidal sol is put into autoclave, control required temperature, crystallization was taken out 4 hours, 550 ℃ roastings of 2 times, 120 ℃ oven dry of washing 3 hours after 10～100 hours, can obtain described Magadiite/ beta zeolite coexisting material.
The present invention is because the template that has adopted suitable two or more things of while to grow mutually, regulate and be fit to the pH value scope that related thing is grown mutually, control is fit to the silica alumina ratio and the crystallization temperature of growth, under hydrothermal condition, can in mixed sols, induce the crystal seed of two kinds of thing phases simultaneously, in the environment that is fit to their growths, generated this Magadiite/ beta zeolite coexisting material then, and Magadiite is a layer columnar structure, can be by introducing big positively charged ion at interlayer, promptly by the poroid material of the constitutionally stable two dimension of pillared formation, with suitable column-supporting agent pillared after, specific surface area increases, the duct size adjustable, and a large amount of available β ronsted and Lewis catalytic sites are provided.Not only made things convenient for reactant near catalytic active site, and layer and duct size have also improved the selectivity of catalyzed reaction.Because the surface of Magadiite/ beta zeolite coexisting material has than big difference with interface, acidity and specific surface and the simple mutually mechanical blended of thing, contain multistage pore canal, so catalytic performance is preferably arranged, can handle the different mixture material of molecular diameter, can be used for having obtained better technical effect in the industrial production of methanol dehydration preparing ethylene and propylene.
Description of drawings
Fig. 1 is the XRD diffracting spectrum of synthetic Magadiite/ beta zeolite coexisting material.
The present invention is further elaborated below by embodiment.
Embodiment
[embodiment 1]
Getting 569 gram Starsos is dissolved in the 900 gram deionized waters.In addition 33.4 gram Tai-Ace S 150 are dissolved in the 150 gram deionized waters, add in the sodium silicate solution under stirring.The mixed evenly back of solution is stirred and is added 59 gram tetraethyl ammonium hydroxides down, and it is 11 that the pH value is regulated with 30% sulphuric acid soln in the back that stirs, and continues then to be stirred to evenly, carries out conventional hydrothermal crystallizing 10 hours under 150 ℃.Product after washing 130 ℃ dry 4 hours down, 550 ℃ of following roastings 3 hours promptly get crystal seed required for the present invention, remember and make M1.
[embodiment 2]
Method and content according to embodiment 1 is provided change the Tai-Ace S 150 add-on into 17.7 grams, make crystal seed required for the present invention, are designated as M2.
[embodiment 3]
Get 33.3 gram Starsos, become solution A with 100 gram dissolved in distilled water, get the silicon sol of 57.4 grams 40%, make solution β with 100 gram distilled water, get 0.48 gram Tai-Ace S 150, make solution C with 20 ml distilled waters, respectively A and C solution are slowly poured in the β solution, the powerful stirring, add 2.6 gram sodium hydroxide and 29.4 gram tetraethyl ammonium hydroxides, and then add 1.2 gram β zeolite seed crystal M1, after stirring for some time, regulate the pH value 11 with dilute sulphuric acid, the mole proportioning of control colloidal sol is: Si: Al: Na: M: H
2O=1: 0.005: 0.6: 0.4: 40, mixing solutions is put into autoclave, 160 ℃ of insulations 40 hours, take out 4 hours, 550 ℃ roastings of 2 times, 120 ℃ oven dry of washing 3 hours then, make the Magadiite/ beta zeolite coexisting material, the XRD diffracting spectrum as shown in Figure 1,15.73,11.32,11.14,9.97,7.74,5.14,4.15,3.96,3.85,3.65,3.45,3.30 there is d-spacing maximum value at 3.14,3.02 dust places.With the XRD diffraction quantitatively as can be known in the coexisting material β zeolite quality percentage composition be 55.4%, Magadiite content is 44.6%.
[embodiment 4～7]
According to the method for embodiment 3, use M2 to be crystal seed, raw materials used as shown in table 4, the pH difference of control solution sees Table 1, synthesizes the Magadiite/ beta zeolite coexisting material respectively.The XRD diffracting spectrum is identical with embodiment 3, and the ratio of Magadiite and β zeolite sees Table 3 in the coexisting material.
Table 1
| Embodiment | The pH value of solution value | Sample number into spectrum |
| Embodiment 4 | 8 | FH-4 |
| Embodiment 5 | 9 | FH-5 |
| Embodiment 6 | 13 | FH-6 |
| Embodiment 7 | 14 | FH-7 |
[embodiment 8～14]
According to the method for embodiment 3, raw materials used as shown in table 4, the different mole proportionings of control solution, synthetic Magadiite/ beta zeolite coexisting material sees Table 2 respectively.The XRD diffracting spectrum is identical with embodiment 3, and the ratio of Magadiite and β zeolite sees Table 3 in the coexisting material.
Table 2
| Embodiment | Solution mole proportioning | Sample number into spectrum |
| Embodiment 8 | Si∶Al∶Na∶M∶H 2O＝1∶0.002∶0.01∶0.2∶40 | FH-8 |
| Embodiment 9 | Si∶Al∶Na∶M∶H 2O＝1∶0.01∶0.8∶0.1∶100 | FH-9 |
| |
Si∶Al∶Na∶M∶H 2O＝1∶0.2∶1∶0.05∶500 | FH-10 |
| Embodiment 11 | Si∶Al∶Na∶M∶H 2O＝1∶0.005∶0.4∶1∶10 | FH-11 |
| Embodiment 12 | Si∶Al∶Na∶M∶H 2O＝1∶0.1∶4∶0.4∶40 | FH-12 |
| Embodiment 13 | Si∶Al∶Na∶M∶H 2O＝1∶0.005∶2∶2∶200 | FH-13 |
| Embodiment 14 | Si∶Al∶Na∶M∶H 2O＝1∶0.05∶3∶3∶20 | FH-14 |
[embodiment 15～17]
According to the method for embodiment 3, raw materials used as shown in table 4, the mole proportioning of control solution is identical, and crystallization temperature is set to 80 ℃ respectively; 130 ℃ and 220 ℃, synthesized the Magadiite/ beta zeolite coexisting material respectively, be designated as FH-15, FH-16 and FH-17.The XRD diffracting spectrum is identical with embodiment 3, and the ratio of Magadiite and β zeolite sees Table 3 in the coexisting material.
[embodiment 18～21]
According to the method for embodiment 3, raw materials used as shown in table 4, the mole proportioning of control solution is identical, and crystallization time is controlled to be 8 hours respectively; 20 hours; 100 hours and 200 hours, synthesized the Magadiite/ beta zeolite coexisting material respectively, be designated as FH-18, FH-19, FH-20 and FH-21.The XRD diffracting spectrum is identical with embodiment 3, and the ratio of Magadiite and β zeolite sees Table 3 in the coexisting material.
[embodiment 22～25]
According to the method for embodiment 3, raw materials used as shown in table 4, the mole proportioning of control solution is identical, adds M1 crystal seed amount and is respectively SiO in the raw material
20.01% of weight; 0.1%; 10% and 20%, synthesized the Magadiite/ZSM-5 coexisting material respectively, be designated as FH-22, FH-23, FH-24 and FH-25, the XRD diffracting spectrum is identical with embodiment 3, and the ratio of Magadiite and β zeolite sees Table 3 in the coexisting material.
Table 3
| Sample number into spectrum | Magadiite content (weight %) | β zeolite content (weight %) |
| FH-4 | 25.5 | 74.5 |
| FH-5 | 30.6 | 69.4 |
| FH-6 | 67.9 | 32.1 |
| FH-7 | 85.1 | 14.9 |
| FH-8 | 91.2 | 8.8 |
| FH-9 | 25.4 | 74.6 |
| FH-10 | 3.9 | 96.1 |
| FH-11 | 86.3 | 13.7 |
| FH-12 | 88.2 | 11.8 |
| FH-13 | 90.6 | 9.4 |
| FH-14 | 15.8 | 84.2 |
| FH-15 | 47.3 | 52.7 |
| FH-16 | 37.6 | 62.4 |
| FH-17 | 88.4 | Youngster .6 |
| FH-18 | 73.0 | 27.0 |
| FH-19 | 66.4 | 33.6 |
| FH-20 | 71.9 | 28.1 |
| FH-21 | 79.3 | 20.7 |
| FH-22 | 94.7 | 5.3 |
| FH-23 | 89.8 | 10.2 |
| FH-24 | 34.5 | 65.5 |
| FH-25 | 11.2 | 88.8 |
Table 4
| Sample number into spectrum | The silicon source | The aluminium source | Template | Alkali source | Acid |
| FH-4 | Starso | Tai-Ace S 150 | Quadrol, tetraethyl ammonium hydroxide | Sodium hydroxide | Dilute sulphuric acid |
| FH-5 | Silicon sol | Sodium metaaluminate | N-Butyl Amine 99 | Sodium hydroxide | Dilute hydrochloric acid |
| FH-6 | Silica gel | Bauxite | Tetraethyl ammonium hydroxide | Sodium hydroxide | Oxalic acid |
| FH-7 | Diatomite | Aluminium hydroxide, colloidal sol | N-Butyl Amine 99 | Sodium hydroxide | Acetate |
| FH-8 | Water glass | Pseudo-boehmite | Quadrol | Sodium hydroxide | Dilute hydrochloric acid |
| FH-9 | Silicon sol | Sodium aluminate | Tetraethyl ammonium hydroxide | Sodium hydroxide | Dilute sulphuric acid |
| FH-10 | Tetraethoxy | Tai-Ace S 150 | Quadrol | Sodium hydroxide | Dilute hydrochloric acid |
| FH-11 | Silicon sol | Aluminum nitrate | Ethamine | Sodium hydroxide | Dilute hydrochloric acid |
| FH-12? | Soft silica | Aluminum chloride | Tetraethyl ammonium hydroxide | Sodium hydroxide | Dilute sulphuric acid |
| FH-13 | Silicon sol | Sodium aluminate | Ethamine | Sodium hydroxide | Dilute sulphuric acid |
| FH-14 | Starso, silicon sol | Tai-Ace S 150 | Ethamine, tetraethyl ammonium hydroxide | Sodium hydroxide | Dilute sulphuric acid, dilute hydrochloric acid |
| FH-15? | Tetraethoxy, silicon sol | Tai-Ace S 150 | Ethamine | Sodium hydroxide, potassium hydroxide | Dilute sulphuric acid |
| FH-16 | Tetraethoxy | Sodium metaaluminate, Tai-Ace S 150 | TPAOH | Potassium hydroxide, sodium hydroxide | Dilute sulphuric acid, dilute hydrochloric acid |
| FH-17 | Tetraethoxy | Sodium metaaluminate | 4-propyl bromide | Potassium hydroxide | Rare nitric acid |
| FH-18 | Water glass | Tai-Ace S 150 | Tetraethyl ammonium hydroxide | Sodium hydroxide | Rare nitric acid |
| FH-19 | Tetraethoxy | Sodium metaaluminate, Tai-Ace S 150 | Tetraethylammonium bromide | Sodium hydroxide | Rare nitric acid |
| FH-20 | Water glass | Sodium aluminate | N-Butyl Amine 99, tetraethyl ammonium hydroxide | Potassium hydroxide, sodium hydroxide | Rare nitric acid |
| FH-21 | Silica gel | Sodium aluminate | Ethamine, quadrol | Sodium hydroxide | Rare nitric acid |
| FH-22 | Soft silica | Sodium aluminate | Ammoniacal liquor, tetraethyl ammonium hydroxide | Sodium hydroxide | Rare nitric acid |
| FH-23 | Silica gel | Sodium aluminate | TPAOH, n-Butyl Amine 99 | Sodium hydroxide | Rare nitric acid |
| FH-24 | Silica gel | Sodium aluminate | Tetraethyl ammonium hydroxide | Sodium hydroxide | Dilute sulphuric acid |
| FH-25 | Silicon sol | Sodium aluminate | Triethylamine | Sodium hydroxide | Dilute sulphuric acid |
[embodiment 26]
Getting embodiment 3 synthetic coexisting materials, is that the 5wt% ammonium nitrate solution carries out ammonium exchange 3 hours at 90 ℃ with weight percentage.Product after filtration, washing, 130 ℃ down after dry 3 hours, repeat an ammonium exchange again, after filtration, washing, 130 ℃ be down after dry 3 hours, 550 ℃ of following roastings 3 hours, make the Hydrogen coexisting material, then compressing tablet, break into pieces, sieve, it is standby to get 20～40 purpose particles.With methyl alcohol was raw material, is 12 millimeters fixed-bed reactor with diameter, 480 ℃, weight space velocity 1 hour
-1, water/methyl alcohol weight ratio 3: 1, pressure is to check and rate under the condition of 0.02MPa, the ethene molar yield reaches 23.5%, the propylene molar yield reaches 34.7%, ethene and propylene diene mole total recovery are 59.2%, have obtained better technical effect.
[embodiment 27]
Get embodiment 3 synthetic coexisting materials, the method for pressing embodiment 26 makes the Hydrogen coexisting material.Get wherein 10 gram Hydrogen coexisting materials, put into the TBAH solution of 200 milliliter of 0.05 mol, use ultra-sonic oscillation 30 minutes, suction filtration is put into 110 ℃ of bakings of baking oven 3 hours then.Make the coexisting material behind the intercalation, measure its specific surface, bore dia and pore volume, measurement result such as table 5 with nitrogen temperature programmed desorption(TPD) device.
[embodiment 28]
Method by embodiment 26 prepares Hydrogen Magadiite/ beta zeolite coexisting material, measures its specific surface, bore dia and pore volume by the method for embodiment 27, and the result is as shown in table 5.
Table 5
| Embodiment | Sample type | Specific surface area (m 2/g) | Pore volume (m 3/g) | Mean pore size (nm) |
| Embodiment 27 | Magadiite/ β zeolite behind the intercalation | 298.7 | 0.28 | 3.1 |
| Embodiment 28 | Hydrogen Magadiite/ β zeolite | 255.4 | 0.24 | 2.4 |
Claims (2)
1. Magadiite/ beta zeolite coexisting material, the composition with following molar relationship: nSiO
2: Al
2O
3, n=20 in the formula～2000 is characterized in that described material has two kinds of Symbiont phases, its XRD diffracting spectrum is included in 15.73 ± 0.1, and 11.32 ± 0.05,11.14 ± 0.05,9.97 ± 0.1,7.74 ± 0.1,5.14 ± 0.1,4.15 ± 0.04,3.96 ± 0.04,3.85 ± 0.05,3.65 ± 0.05,3.45 ± 0.08,3.30 ± 0.05,3.14 there is d-spacing maximum value at ± 0.05,3.02 ± 0.05 dust places.
2. Magadiite/ beta zeolite coexisting material according to claim 1 is characterized in that n=40～1000.
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