CN1084100A - The preparation of ZSM-5 zeolite/silica-gel composite catalyst material - Google Patents
The preparation of ZSM-5 zeolite/silica-gel composite catalyst material Download PDFInfo
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- CN1084100A CN1084100A CN 92110497 CN92110497A CN1084100A CN 1084100 A CN1084100 A CN 1084100A CN 92110497 CN92110497 CN 92110497 CN 92110497 A CN92110497 A CN 92110497A CN 1084100 A CN1084100 A CN 1084100A
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Abstract
A kind of preparation method with the synthetic ZSM-5 zeolite/silica-gel composite catalyst material of in-situ crystallization method is: solution or suspension that silica gel and aluminium source, sodium source, the agent of organic amine template, the water of any granular size are formed mix, stir, be heated to 130～190 ℃ of crystallizations 10 hours to 8 days, washing, filtration, drying.In this composite the content of ZSM-5 zeolite can be in the scope of 5～80 weight % modulation.This method makes zeolite be scattered in the blapharoplast surface securely, has improved the stability of little crystal grain zeolite on matrix, and has solved the difficulty of filtering in the common synthesizing small-grain zeolite process.
Description
The invention relates to the preparation method of the compound catalyze material that contains aluminosilicate zeolite, specifically, is about directly synthesizing the preparation method of the ZSM-5 zeolite compound catalyze material on silica gel.
ZSM-5 is the zeolite (USP3 with unique one dimension straight hole road that U.S. Mobile company succeeded in developing in sixties end, 702,886), the shape selective catalysis performance of its excellence makes the catalyst that contains the ZSM-5 zeolite can be widely used for various petroleum refinings and petrochemical process, as catalytic cracking, hydrocracking, hydrofinishing, face hydrogen dewaxing, hydroforming, xylene isomerization, synthesis gas system hydrocarbon or the like.
The general preparation method of zeolite catalyst is at present: the reaction mass gel mixture high temperature crystallization with certain proportioning makes zeolite earlier, then zeolite is combined with the carrier that contains or do not contain binding agent, makes the catalyst finished product through moulding again.The catalyst or the auxiliary agent that contain the ZSM-5 zeolite are no exception.Its active component zeolite of the catalyst that makes like this may reside in caltalyst each position in mutually, and can not high degree of dispersion give full play to its catalytic action in catalyst surface.On the other hand, the size of zeolite grain can influence activity of such catalysts: crystal grain is more little, and the utilization rate on zeolite activity surface is also high more, but has also brought the difficulty of filtering in the preparation process simultaneously; In addition, little zeolite grain is also unstable, destroyed because of being heated easily in catalyst.
U.S. Engelhardt moral mineral chemistry company has just begun the trial of synthetic zeolite on solid (being in-situ crystallization) as far back as the sixties, developed the method for synthetic A type, X type and y-type zeolite on kaolin, its purpose is to prepare zeolite (USP3 with the natural minerals clay as raw material, 391,994; USP3,657,154; USP3,746,659).In addition, USP4 once was reported in the method for synthetic ZSM-5 and X type zeolite on the asbestos in 511,667, and the granule of pointing out zeolite crystal is combined in and is the performance that a warty helps its shape selective catalysis effect on the asbestos fibre.Report the method for synthetic ZSM-5 zeolite on stratiform natural silicate-vermiculite among the CN1059673A, thereby made composited HZSM-5 zeolite/vermiculite catalyst.But do not see that so far having with common carrier in petroleum refining and the petrochemical process (as silica, aluminium oxide, amorphous aluminum silicide etc.) is the directly report of synthetic ZSM-5 zeolite of solid matrix.
The purpose of this invention is to provide and a kind of the ZSM-5 zeolite is directly synthesized in the lip-deep method of solid silicone, thereby make the ZSM-5 zeolite/silica-gel composite catalyst material.
Method provided by the invention is: the silica gel of any granular size is mixed with solution or the suspension be made up of aluminium source, sodium source, the agent of organic amine template, water, stir, stirring intensity should be controlled at and not make the silica gel particle fragmentation, be heated to 130～190 ℃ of crystallizations 10 hours to 8 days, washing, filter drying.Wherein said each raw material consumption following (mol ratio): Al
2O
3/ SiO
2=0.001～0.02, Na
2O/SiO
2=0.005～0.05, organic amine/SiO
2=0.01～0.2, H
2O/SiO
2=0.5～5.0.
Said silica gel can be any aperture in the inventive method, comprises the silica gel of gross porosity, mesopore, pore.Said aluminium source is a sodium aluminate.Said sodium source is the mixture of sodium aluminate or sodium aluminate and NaOH.The agent of said organic amine template is selected from the synthetic organic amine of tetraethyl ammonium hydroxide, triethylamine, tripropyl amine (TPA), ethamine and the various ZSM-5 of can be used for zeolite.
For quickening the nucleation and the crystallization of ZSM-5 zeolite, the crystal that can add the X type that is selected from, Y type, β, ZSM-5, ZSM-12 zeolite in the reaction system is as crystal seed, and the addition of crystal seed is 0.2～1.0% of a reaction system gross weight.
The ZSM-5 zeolite/silica-gel composite catalyst material that makes with said method has ZSM-5 zeolite and the superimposed x-ray diffraction spectra that forms of silica gel, and along with the increase of ZSM-5 zeolite content in the compound, the diffraction peak intensity of ZSM-5 zeolite also strengthens thereupon on the spectrogram.In this composite, the content of ZSM-5 zeolite can change in the scope of 5～80 heavy % by controlling charge ratio or crystallization condition.ZSM-5 zeolite grain high degree of dispersion in silica gel particle surface and with the latter organically strong bonded be one, demonstrate the characteristics of zeolite grain at the silica gel particle surface in-situ crystallization.The silica alumina ratio of zeolite depends on the amount of sodium aluminate and the amount that silica gel particle surface participates in the silica of crystallization.
Method provided by the invention has been improved the bonding state of zeolite and matrix when making zeolite only be scattered in the blapharoplast surface, improved the stability of little crystal grain zeolite on matrix.Because the crystallization process in this method is to carry out on molded blapharoplast, thereby has solved the problem of filtration difficulty in the common synthesizing small-grain zeolite process.
The compound catalyze material that makes with the method for the invention provides can be used alone as catalyst, also can with contain or do not contain binding agent, contain or do not contain other matrix and other zeolite and be mixed and made into composite catalyst and use.Can be Hydrogen through pickling transformation again through the roasting removed template method, also can after the ammonium salt solution exchange, use for Hydrogen transition through roasting again.Can alkali metal, alkaline-earth metal, rare earth, copper, iron, nickel, lead, zinc be introduced by the method for ion-exchange and wherein make it to become the catalyst that contains various different metals, also can pass through dipping or other method with various metallic compounds, make it to become the catalyst that contains various different metals through roasting reduction again after introducing wherein as the metallic compound of nickel, platinum, palladium, rubidium, cobalt, rhodium etc., can also be with various compound, as the compound that contains elements such as oxygen, sulphur, nitrogen, phosphorus, boron, gallium is introduced and is wherein made it to become the catalyst with specific use.This compound catalyze material can also make it to have higher silica alumina ratio with the part aluminium that methods such as pickling, chemical extracting are sloughed on the zeolitic frameworks.Above-mentioned compound catalyze material and various modified thereof can be used for multiple chemical industry, petrochemical industry or petroleum refining process catalyst.
Fig. 1 and Fig. 2 are with the X-ray diffraction pattern that the invention provides the compound catalyze material that method makes, and wherein the content of ZSM-5 zeolite is respectively 71.0 heavy % and 31.0 heavy %, and test is with CuK α radiation, Ni filtering.
Fig. 3 and Fig. 4 are that multiplication factor is respectively 2.6 thousand times and 8.7 thousand times with the stereoscan photograph that the invention provides the compound catalyze material that method makes.
Following example will give further instruction to preparation method provided by the invention.
Example 1～2
Prepare compound catalyze material provided by the invention with the tetraethyl ammonium hydroxide for the template agent.
Will (1) 0.2 gram sodium aluminate (Shanghai reagent two factory's products, Al
2O
3The heavy % of content 45, down with), 2.1 milliliters of tetraethyl ammonium hydroxide aqueous solution (Shanghai reagent one factory's product, 0.4344 grams per milliliter, down with) and after 21.0 ml waters mix; And after (2) 0.4 gram sodium aluminates, 4.2 milliliters of tetraethyl ammonium hydroxide aqueous solution and 21.0 ml waters mix, add 20 gram (butts respectively, 80～120 order silochroms (Qingdao silica gel factory product down together), stir down together), must not make the silica gel particle fragmentation during stirring, 150 ℃ of crystallizations are 8 days in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is respectively 28.4 heavy % and 71.0 heavy % in two samples that make thus, they all have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Example 3
Prepare compound catalyze material provided by the invention with the tripropyl amine (TPA) for the template agent.
With 0.1 gram sodium aluminate, 0.2 gram NaOH (Beijing Chemical Plant's product, analyze pure), 1.5 gram tripropyl amine (TPA) (Beijing Chemical Plant's products, chemical pure, 98 heavy %) and after 18.0 ml waters mix, add fully stirring in 15 grams, 40～60 order silochroms, must not make the silica gel particle fragmentation during stirring, 170 ℃ of crystallization are 16 hours in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is 48.9 heavy % in this sample, it have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Example 4
Prepare compound catalyze material provided by the invention with the triethylamine for the template agent.
With 0.1 gram sodium aluminate, 0.2 gram NaOH, 1.5 gram triethylamine (Beijing Chemical Plant's products, analyze pure, 99.0 heavy %) and after 18.0 ml waters mix, add in 15 grams, 40～60 order Kiselgel As (Qingdao silica gel factory product, down together) and fully stir, must not make the silica gel particle fragmentation during stirring, 170 ℃ of crystallization are 50 hours in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is 8.5 heavy % in this sample, it have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Example 5
Prepare compound catalyze material provided by the invention with ethamine for the template agent.
With 0.1 gram sodium aluminate, 0.35 gram NaOH, 2.0 gram ethylamine solution (Beijing Chemical Plant's products, chemical pure, 33.0 heavy %) and after 18.0 ml waters mix, add in 15 grams, 80～120 order silochroms and fully stir, must not make the silica gel particle fragmentation during stirring, 170 ℃ of crystallization are 4 days in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is 49.4 heavy % in this sample, it have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Example 6
With the y-type zeolite is that crystal seed prepares compound catalyze material provided by the invention.
With 0.1 gram sodium aluminate, 0.2 gram NaOH, 1.5 milliliters of tetraethyl ammonium hydroxides, 18.0 ml waters and through abundant porphyrize 0.2 restrain the y-type zeolite crystal seed and mix after, add in 15 grams, 80～120 order Kiselgel As and fully stir, must not make the silica gel particle fragmentation during stirring, 170 ℃ of crystallization are 64 hours in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is 31.0 heavy % in this sample, it have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Example 7
With the zeolite beta is that crystal seed prepares compound catalyze material provided by the invention.
With 0.1 gram sodium aluminate, 0.35 gram NaOH, 2.0 gram ethylamine solutions, 18.0 ml waters and through abundant porphyrize 0.2 restrain the zeolite beta crystal seed and mix after, add in 15 grams, 80～120 order silochroms and fully stir, must not make the silica gel particle fragmentation during stirring, 170 ℃ of crystallization are 2 days in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is 45.0 heavy % in this sample, it have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Example 8
With the ZSM-5 zeolite is that crystal seed prepares compound catalyze material provided by the invention.
With the tetraethyl ammonium hydroxide of 2.4 gram sodium aluminates, 25.2 milliliters of 2.807N, 20.0 ml waters and through abundant porphyrize 0.2 restrain ZSM-5 type zeolite seed crystal and mix after, add in 40 grams, 40～60 order Kiselgel As and fully stir, must not make the silica gel particle fragmentation during stirring, 190 ℃ of crystallization are 20 hours in stainless steel cauldron, cooled and filtered, washing is to neutral, and 110 ℃ of dryings promptly got the ZSM-5 zeolite/silica-gel composite catalyst material in 2 hours.
The content of ZSM-5 zeolite is 35.7 heavy % in this sample, it have as shown in the figure the X-ray diffraction pattern and the pattern shown in the stereoscan photograph.
Claims (7)
1, a kind of preparation method of ZSM-5 zeolite/silica-gel composite catalyst material, it is characterized in that: the silica gel of any granular size is mixed with solution or the suspension be made up of aluminium source, sodium source, the agent of organic amine template, water, stir, be heated to 130～190 ℃ of crystallizations 10 hours to 8 days, washing, filter drying;
Each raw material proportioning following (mol ratio): Al wherein
2O
3/ SiO
2=0.001～0.02, Na
2O/SiO
2=0.005～0.05, organic amine/SiO
2=0.01～0.2, H
2O/SiO
2=0.5～5.0.
2,, it is characterized in that said silica gel can be any aperture according to the described preparation method of claim 1.
3,, it is characterized in that said aluminium source is a sodium aluminate according to the described preparation method of claim 1.
4,, it is characterized in that said sodium source is the mixture of sodium aluminate or sodium aluminate and NaOH according to the described preparation method of claim 1.
5,, it is characterized in that said organic amine is selected from one of tetraethyl ammonium hydroxide, triethylamine, tripropyl amine (TPA) or ethamine according to the described preparation method of claim 1.
6,, it is characterized in that to add in the preparation process zeolite crystal of one of the X type that is selected from, Y type, β, ZSM-5, ZSM-12 as crystal seed according to the described preparation method of claim 1.
7, according to the said preparation method of claim 6, the addition that it is characterized in that said crystal seed is 0.2～1.0% of a reaction system gross weight.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92110497 CN1030286C (en) | 1992-09-09 | 1992-09-09 | Preparation of ZSM-5 zeolite/silica-gel composite catalyst material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN 92110497 CN1030286C (en) | 1992-09-09 | 1992-09-09 | Preparation of ZSM-5 zeolite/silica-gel composite catalyst material |
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| Publication Number | Publication Date |
|---|---|
| CN1084100A true CN1084100A (en) | 1994-03-23 |
| CN1030286C CN1030286C (en) | 1995-11-22 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN 92110497 Expired - Fee Related CN1030286C (en) | 1992-09-09 | 1992-09-09 | Preparation of ZSM-5 zeolite/silica-gel composite catalyst material |
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1058643C (en) * | 1996-07-22 | 2000-11-22 | 中国石油化工总公司 | Catalytic ZSM-5/metal or ceramic compounded material and its preparation |
| CN1069848C (en) * | 1996-06-05 | 2001-08-22 | 中国石油化工总公司 | Mordenite/metal or ceramic catalyzing composite material and preparation thereof |
| WO2008148684A1 (en) * | 2007-06-08 | 2008-12-11 | Albemarle Netherlands, B.V. | Basic cracking compositions substantially free of large pore zeolites |
| CN100455511C (en) * | 2006-11-10 | 2009-01-28 | 南京工业大学 | Method for synthesizing small-grain ZSM-5 zeolite molecular sieve |
| CN102502696A (en) * | 2011-11-16 | 2012-06-20 | 大连理工大学 | Synthetic method of ZSM-5 zeolites |
| CN102910644A (en) * | 2011-08-01 | 2013-02-06 | 中国石油化工股份有限公司 | Multistage pore ZSM-5 molecular sieve and preparation method thereof |
-
1992
- 1992-09-09 CN CN 92110497 patent/CN1030286C/en not_active Expired - Fee Related
Cited By (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1069848C (en) * | 1996-06-05 | 2001-08-22 | 中国石油化工总公司 | Mordenite/metal or ceramic catalyzing composite material and preparation thereof |
| CN1058643C (en) * | 1996-07-22 | 2000-11-22 | 中国石油化工总公司 | Catalytic ZSM-5/metal or ceramic compounded material and its preparation |
| CN100455511C (en) * | 2006-11-10 | 2009-01-28 | 南京工业大学 | Method for synthesizing small-grain ZSM-5 zeolite molecular sieve |
| WO2008148684A1 (en) * | 2007-06-08 | 2008-12-11 | Albemarle Netherlands, B.V. | Basic cracking compositions substantially free of large pore zeolites |
| CN102910644A (en) * | 2011-08-01 | 2013-02-06 | 中国石油化工股份有限公司 | Multistage pore ZSM-5 molecular sieve and preparation method thereof |
| CN102910644B (en) * | 2011-08-01 | 2014-07-23 | 中国石油化工股份有限公司 | Preparation method of multistage pore ZSM-5 molecular sieve |
| CN102502696A (en) * | 2011-11-16 | 2012-06-20 | 大连理工大学 | Synthetic method of ZSM-5 zeolites |
| CN102502696B (en) * | 2011-11-16 | 2014-04-23 | 大连理工大学 | Synthetic method of ZSM-5 zeolites |
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| Publication number | Publication date |
|---|---|
| CN1030286C (en) | 1995-11-22 |
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