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CN102515198B - Integral-type heteroatom replacing hierarchical porous molecular sieve and synthesis method thereof - Google Patents

Integral-type heteroatom replacing hierarchical porous molecular sieve and synthesis method thereof Download PDF

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CN102515198B
CN102515198B CN 201110370674 CN201110370674A CN102515198B CN 102515198 B CN102515198 B CN 102515198B CN 201110370674 CN201110370674 CN 201110370674 CN 201110370674 A CN201110370674 A CN 201110370674A CN 102515198 B CN102515198 B CN 102515198B
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molecular sieve
integral
hierarchical porous
porous molecular
heteroatom replacing
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CN102515198A (en
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程党国
Do·孟辉
陈丰秋
金炜阳
詹晓力
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Zhejiang University ZJU
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Zhejiang University ZJU
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  • Silicates, Zeolites, And Molecular Sieves (AREA)

Abstract

The invention discloses an integral-type heteroatom replacing hierarchical porous molecular sieve. The chemical formula of the integral-type heteroatom replacing hierarchical porous molecular sieve is (M<n+>)(x+y)/n[(MexAlySil-(x+y))O2].wH2O, wherein M<n+> is one or a mixture of several of cations: Na<+>, K<+>, H<+>, Ca<2+> and Mg<2+>; Me which enters a molecular sieve framework is one or a mixture of several of the following metal atoms: Cu, Mo, Fe, Co, Ti, Ni, Mn, W, V, Zn, Mg, Sn, Pt, Pd, Ce, La and Y; x, y and 1-(x+y) respectively represent mole fractions of Me, Al and Si; x ranges from 0.001 to 0.05, and y ranges from 0 to 0.6; w represents the number of water molecules in each mole of (MexAlySil-(x+y))O2; and w ranges from 1 to 80, and n is equal to 1 or 2. The preparation process is simple, and is low in cost.

Description

A kind of Integral-type heteroatom replacing hierarchical porous molecular sieve and synthetic method thereof
Technical field
The present invention relates to a kind of Integral-type heteroatom replacing hierarchical porous molecular sieve and one-step method for synthesizing thereof.
Background technology
But the catalytic performance of the well-regulated duct of zeolite molecular sieve tool, good shape selectivity, stability and modulation, fields such as being widely used in catalysis, ion-exchange, adsorbing and separating.Metal ion is introduced hydrothermal stability and the catalytic performance that molecular sieve can further improve molecular sieve.The investigator often is scattered in metallic element in molecular sieve surface or duct by methods such as ion-exchange, dipping and vapour depositions at present.But in these three kinds of preparation process, part is scattered in molecular sieve surface or duct because metallic element can not enter framework of molecular sieve fully, thereby is reduced to unavoidably metal and is run off under hydrogen atmosphere, causes catalyst stability to descend.Although isomorphous substitution method can overcome the shortcoming of aforesaid method, but metal ion very easily is hydrolyzed in the normally used alkaline medium of zeolite-water thermal synthesis and generates indissoluble oxyhydroxide or oxide precipitation, stop metallic element effectively to enter framework of molecular sieve, therefore must adopt new synthesis path just metallic element might be incorporated in framework of molecular sieve.Recently, Wu etc. proposes a kind of method that multistep is regulated the MCM-22 molecular sieve of the synthetic containing rare earth heteroatoms in skeleton of pH method.At first, with mixture heating hydrolysis in acidic medium of silicon source and rare earth compound, the pH value of controlling solution with HCl is 2, then adds the template of hexamethylene imine in the above-mentioned hydrolysate, and the pH value that obtains solution is 5-6.Add solution before last crystallization and mix that to contain the pH value that aluminium source and NaOH obtain solution be 11.6.(Y. Wu, J. Wang, P. Liu, W. Zhang, J. Gu, X. Wang. Framework-Substituted Lanthanide MCM-22 Zeolite:Synthesis and Characterization. J. AM. CHEM. SOC. 2010,132,17989 – 17991) although. the method is conducive to rare-earth heteroatoms and enters framework of molecular sieve, and preparation process is complicated, the difficult pH that controls.The heteroatomic molecular sieve of gained skeleton containing metal is generally powder.Although in industrial application, it is whole column or sheet shape that zeolite [molecular sieve adopts usually, also there is no any patent and the bibliographical information of Integral-type heteroatom replacing hierarchical porous molecular sieve at present.
Summary of the invention
The purpose of this invention is to provide a kind of Integral-type heteroatom replacing hierarchical porous molecular sieve and one-step method for synthesizing thereof.
Integral-type heteroatom replacing hierarchical porous molecular sieve of the present invention, its chemical constitution is expressed as (M n+ ) (x+y)/n [(Me x Al y Si 1 -( x+y) ) O 2]. wH 2O; Wherein, M n+ Be positively charged ion Na +, K +, H +, Ca 2+And Mg 2+In one or more mixing; Me is the atoms metal Cu that enters framework of molecular sieve, Mo, Fe, Co, Ti, Ni, Mn, W, V, Zn, Mg, Sn, Pt, Pd, Ce, one or more mixing in La and Y; x, y,1-( x+ y) represent respectively Me, the molar fraction of Al and Si, x=0.001 – 0.05, y=0 – 0.6; wRepresent every mole of (Me x Al y Si 1 -( x+y) ) O 2Middle water molecule number, w=1 – 80, n=1 or 2, its heteroatoms replaces the crystal of molecular sieve from unifying, and has the mesoporous of micropore less than 2nm, 2-50nm and greater than three grades of ducts of macropore of 50nm.
The method of Integral-type heteroatom replacing hierarchical porous molecular sieve of the present invention, employing be single stage method, its concrete steps are as follows:
Silicon source, aluminium source, water and template are mixed, 10 ~ 80 oC stirred 2 ~ 24 hours, added wherein alkali source, and then added metal-salt to get gel mixture, this gel mixture was moved in the stainless steel synthesis reactor seal, 80 ~ 200 oAfter C crystallization 6 ~ 72 hours, washing, drying, 550 ~ 650 oC roasting 4 ~ 12 hours gets Integral-type heteroatom replacing hierarchical porous molecular sieve;
The mol ratio of above-mentioned silicon source, aluminium source, water, template, metal-salt and alkali source is 1:0 ~ 0.1:5 ~ 80:0.1 ~ 0.8:0.002 ~ 0.05:0.08 ~ 0.4.
In the present invention, described alkali source is NaOH, KOH and NH 4The mixture of one or more in OH.Described silicon source is one or more mixing in silicon sol, water glass, silicon gel, tetraethyl orthosilicate and positive silicic acid propyl ester.Described aluminium source is one or more mixing in sodium aluminate, Tai-Ace S 150, aluminum isopropylate and tertiary butyl aluminium.Described template is organic amine (C nH 2n+1) 4One or more mixing in NX, wherein n=1 – 22; X=OH, Br or Cl.Described metal-salt is a kind of in the nitrate of Cu, Mo, Fe, Co, Ti, Ni, Mn, W, V, Zn, Mg, Sn, Ce, La and Y or several mixture arbitrarily.
Beneficial effect of the present invention:
The present invention adopts one-step synthesis, generates oxyhydroxide or water and oxide precipitation for fear of metal heteroatom because of hydrolysis in building-up process, and it is to promote gelating agent that the present invention adopts alkali source, then first gelation mother liquor adds metal-salt, atoms metal Me is existed with the form of Si-O-Me, need not add any unbodied carrier, need not mesoporous or macropore template, technique is simple, reduce water, crystallization time is short, and temperature is low, production cost is low, is suitable for the characteristics of suitability for industrialized production etc.The pure multistage pore canal heteroatoms of prepared monolithic devices replaces the crystal self join of molecular sieve.The hole is from the micropore to the macropore, and size distribution is wide, active, good hydrothermal stability, and physical strength is high.Can be used for petrochemical complex, the fields such as fine chemicals preparation and environmental catalysis.
Description of drawings
Fig. 1 is the XRD spectra of sintetics, and wherein a is the XRD spectra of embodiment 1, and b is the XRD spectra of embodiment 4;
Fig. 2 is the nitrogen absorption under low temperature-desorption isotherm figure of sintetics.In figure, 1 is adsorption curve, and 2 is the desorption curve.
Fig. 3 obtains pore volume and aperture graph of a relation adsorbing by BJH of sintetics.
Fig. 4 is the stereoscan photograph of sintetics, and wherein a is the stereoscan photograph of embodiment 1, and b is the stereoscan photograph of embodiment 4;
Fig. 5 is the UV-vis spectrogram of sintetics, and wherein a is the UV-vis spectrogram of embodiment 1, and b is the UV-vis spectrogram of embodiment 4.
Embodiment
Embodiment 1:
Colloidal sol (2.8 wt.% Al with 5.13g tetraethyl orthosilicate, 3g aluminum isopropylate 2O 3), 2g water and 4g TPAOH mix, 25 oC stirred after 3 hours, added wherein 3.5ml 6% NaOH solution, then added 0.06g Fe (NO 3) 3.9H 2O gets gel mixture, this gel mixture is moved in the stainless steel synthesis reactor seal, 155 oC crystallization 24 hours obtains the product of monolithic devices molecular sieve through washing, drying and 550 oAfter C roasting 6 hours, namely obtain the integral body that heteroatoms replaces multistage pore canal Fe-ZSM-5 molecular sieve.Its chemical formula is Na + 0..073[(Fe 0.006Al 0.067 Si 0.927) O 2]. 60H 2O。
Fig. 1 a is the XRD characterization result of product, can see that by Fig. 1 a product has typical MFI ZSM-5 molecular sieve structure, and sample has very high degree of crystallinity, shows that product has hydrothermal stability preferably.
Fig. 2 and Fig. 3 are respectively the nitrogen absorption under low temperature-desorption isotherm of product and obtain pore volume and aperture graph of a relation by BJH absorption.Can see that from spectrogram sample has mesoporous part (nitrogen adsorption isotherm line chart belongs to the H4 type).Mesoporous distribution of sizes is wide.
Fig. 4 a is the SEM photo of sample, can see from the SEM photo, and the Fe-ZSM-5 molecular sieve crystal is from being linked togather, and has simultaneously the integral body of micropore, mesoporous and macropore multistage pore canal, shows that product has higher physical strength.
Fig. 5 a is the UV-vis spectrogram, can see that from figure the Fe atom all is present in the ZSM-5 molecular sieve skeleton with the four-coordination form.
Embodiment 2:
Colloidal sol (2.8 wt.% Al with 5.13g tetraethyl orthosilicate, 3g aluminum isopropylate 2O 3), 2g water and 4g TPAOH mix, 25 oC stirred after 3 hours, added wherein 3.5ml 6% NaOH solution, then added 0.06g Fe (NO 3) 3.9H 2O gets gel mixture, this gel mixture is moved in the stainless steel synthesis reactor seal, 170 oThe C crystallization obtained the product of monolithic devices molecular sieve in 24 hours through washing, drying and 550 oAfter C roasting 6 hours, namely obtain heteroatoms and get multistage pore canal for the integral body of Fe-ZSM-5 molecular sieve.Its chemical formula is Na + 0..073[(Fe 0.006Al 0.067 Si 0.927) O 2]. 60H 2O。
Embodiment 3:
Colloidal sol (2.8 wt.% Al with 5.13g tetraethyl orthosilicate, 2g aluminum isopropylate 2O 3), 2g water and 4g TPAOH mix, 25 oC stirred after 3 hours, added wherein 3.5ml 6% NaOH solution, then added 0.12g Fe (NO 3) 3.9H 2O gets gel mixture, this gel mixture is moved in the stainless steel synthesis reactor seal, 170 oThe C crystallization obtained the product of monolithic devices molecular sieve in 24 hours through washing, drying and 550 oAfter C roasting 6 hours, namely obtain the integral body that heteroatoms replaces multistage pore canal Fe-ZSM-5 molecular sieve.Its chemical formula is Na + 0.067[(Fe 0.023Al 0.044 Si 0.933) O 2]. 60H 2O。
Embodiment 4:
Colloidal sol (2.8 wt.% Al with 5.13g tetraethyl orthosilicate, 3g aluminum isopropylate 2O 3), 2g water and 4g TPAOH mix, 25 oC stirred after 3 hours, added wherein 3.5ml 6% NaOH solution, then added 0.07g Ce (NO 3) 3.6H 2O gets gel mixture, this gel mixture is moved in the stainless steel synthesis reactor seal, 155 oThe C crystallization obtained the product of monolithic devices molecular sieve in 24 hours through washing, drying and 550 oAfter C roasting 6 hours, namely obtain the integral body that heteroatoms replaces multistage pore canal Ce-ZSM-5 molecular sieve.Its chemical formula is (Na + 0..073[(Ce 0.006Al 0.067 Si 0.927) O 2]. 60H 2O。
Fig. 1 b is the XRD characterization result of product, can see that by Fig. 1 b product has typical MFI ZSM-5 molecular sieve structure, and sample has very high degree of crystallinity, shows that product has hydrothermal stability preferably.
Fig. 4 a is the SEM photo of sample, can see from the SEM photo, and the Ce-ZSM-5 molecular sieve crystal shows that from being linked togather the integral body that forms the Ce-ZSM-5 molecular sieve that the duct varies in size product has higher physical strength.
Fig. 5 b is the UV-vis spectrogram of sample, can see that from figure the Ce atom is present in the four-coordination form all that the ZSM-5 molecular sieve skeleton, (250nm belongs to Ce 3+Four-coordination, 300nm belongs to Ce 4+Four-coordination).
Embodiment 5:
5.13g tetraethyl orthosilicate, 2g water and 4g TPAOH are mixed, 25 oC stirred after 3 hours, added wherein 3.5ml 6% NaOH solution, then added 0.07g Ce (NO 3) 3.6H 2O gets gel mixture, this gel mixture is moved in the stainless steel synthesis reactor seal, 170 oThe C crystallization obtained the product of monolithic devices molecular sieve in 24 hours through washing, drying and 550 oAfter C roasting 6 hours, namely obtain the integral body that heteroatoms replaces multistage pore canal Ce-Silicalite-1 molecular sieve.Its chemical formula is Na + 0..006[(Ce 0.006Si 0.994) O 2]. 60H 2O。
The above is only several case study on implementation of the present invention, is not that the present invention is done any pro forma restriction.Protection scope of the present invention is not limited to this.

Claims (6)

1. an Integral-type heteroatom replacing hierarchical porous molecular sieve, is characterized in that chemical constitution is expressed as (M n+ ) (x+y)/n [(Me x Al y Si 1 -( x+y) ) O 2] wH 2O; Wherein, M n+ Be positively charged ion Na +, K +, H +, Ca 2+And Mg 2+In one or more mixing; Me is the atoms metal Cu that enters framework of molecular sieve, Mo, Fe, Co, Ti, Ni, Mn, W, V, Zn, Mg, Sn, Pt, Pd, Ce, one or more mixing in La and Y; x, y,1-( x+ y) represent respectively Me, the molar fraction of Al and Si, x=0.001 – 0.05, y=0 – 0.6; wRepresent every mole of (Me x Al y Si 1 -( x+y) ) O 2Middle water molecule number, w=1 – 80, n=1 or 2, its heteroatoms replaces the crystal of molecular sieve from unifying, and has the mesoporous of micropore less than 2nm, 2-50nm and greater than three grades of ducts of macropore of 50nm.
2. synthesize the method for Integral-type heteroatom replacing hierarchical porous molecular sieve claimed in claim 1, it is characterized in that step is as follows:
Silicon source, aluminium source, water and template are mixed, 10 ~ 80 oC stirred 2 ~ 24 hours, added wherein alkali source, and then added metal-salt to get gel mixture, this gel mixture was moved in the stainless steel synthesis reactor seal, 80 ~ 200 oAfter C crystallization 6 ~ 72 hours, washing, drying, 550 ~ 650 oC roasting 4 ~ 12 hours gets Integral-type heteroatom replacing hierarchical porous molecular sieve;
The mol ratio of above-mentioned silicon source, aluminium source, water, template, metal-salt and alkali source is 1:0 ~ 0.1:5 ~ 80:0.1 ~ 0.8:0.002 ~ 0.05:0.08 ~ 0.4; Described template is TPAOH.
3. the method for described synthetic Integral-type heteroatom replacing hierarchical porous molecular sieve according to claim 2, is characterized in that described alkali source is NaOH, KOH and NH 4The mixture of one or more in OH.
4. the method for described synthetic Integral-type heteroatom replacing hierarchical porous molecular sieve according to claim 2 is characterized in that described silicon source is one or more mixing in silicon sol, water glass, silicon gel, tetraethyl orthosilicate and positive silicic acid propyl ester.
5. the method for described synthetic Integral-type heteroatom replacing hierarchical porous molecular sieve according to claim 2 is characterized in that described aluminium source is one or more mixing in sodium aluminate, Tai-Ace S 150, aluminum isopropylate and tertiary butyl aluminium.
6. the method for described synthetic Integral-type heteroatom replacing hierarchical porous molecular sieve according to claim 2 is characterized in that metal-salt used is a kind of in the nitrate of Cu, Mo, Fe, Co, Ti, Ni, Mn, W, V, Zn, Mg, Sn, Ce, La and Y or several mixture arbitrarily.
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CN107876084B (en) * 2017-10-23 2021-02-23 中海油天津化工研究设计院有限公司 Preparation method of integral nano heteroatom ZSM-22 molecular sieve catalyst
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CN111408402A (en) * 2020-04-10 2020-07-14 福建龙净环保股份有限公司 Titanium modified SSZ-13 type molecular sieve catalyst slurry, preparation method thereof, modified molecular sieve catalyst and catalytic ceramic filter tube
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Patent Citations (4)

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