CN1448338A - Process for preparing fine-grain X zeolite - Google Patents
Process for preparing fine-grain X zeolite Download PDFInfo
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- CN1448338A CN1448338A CN 02116283 CN02116283A CN1448338A CN 1448338 A CN1448338 A CN 1448338A CN 02116283 CN02116283 CN 02116283 CN 02116283 A CN02116283 A CN 02116283A CN 1448338 A CN1448338 A CN 1448338A
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Abstract
The preparation of small crystal grain X zeolite includes the steps of: mixing siliceous compound, aluminum compound, sodium hydroxide and water and ageing at 0-10 deg.c to prepare guide agent in the composition of (11-18)Na2O:Al2O3:(10-17)SiO2:(100-350)H2O; mixing siliceous compound, aluminum compound, water and the guide agent to prepare the mixture of molar composition of (2.5-5)Na2O:Al2O3:(3-5)SiO2:(100-200)H2O; crystallization at 80-120 deg.c for 2-40 hr; water washing, filtering and drying. The X zeolite thus prepared has crystal grain of 0.5-1.0 micron and excellent thermal stability.
Description
Technical field
The present invention is a kind of fine-grain X type prepare zeolite method.Specifically, be the method for preparing fine-grain X zeolite with directing agent method.
Background technology
In adsorption process, adsorbent activity component commonly used is the X zeolite.As at fractionation by adsorption C
8During aromatic hydrocarbons, the active ingredient of sorbent material is BaX, KX or KBaX.The synthetic method of X zeolite has multiple, and wherein a kind of is as USP4, the synthetic method of 166, the 099 employing directed agents of being introduced.This method is a kind of Na of preparation earlier
2O-Al
2O
3-SiO
2Mixture, then this mixture was down made directed agents in aging at least 2 hours at 20～25 ℃, again this directed agents is mixed with the zeolite raw material, can obtain the X zeolite behind the hydrothermal crystallizing.But this method synthetic zeolite grain is bigger, is about about 3 microns.The sorbent material that is made by this zeolite is under the fractionation by adsorption operational condition, and the utilization ratio of zeolite is lower.
Use fine-grain X zeolite to be the adsorbent activity component, help improving the intragranular rate of diffusion, improve the zeolite utilization ratio.Fine-grain X zeolite can adopt and become the preparation of glue method of temperature in the disclosed reduction zeolite synthesis of GB1223592.Be about to sodium aluminate solution and be distributed in the sodium silicate solution, formation silicon oxide and alumina ration are 10～20: 1 solution, make silica content excessive greatly, stir into glue at 0～100 ℃ then, and hydrothermal crystallizing makes the X zeolite.This patent is pointed out, stirs into the glue mixture under the condition of 0～room temperature, is 0.01～0.05 micron zeolite with obtaining crystal grain.
Summary of the invention
The preparation method who the purpose of this invention is to provide the higher fine-grain X zeolite of a kind of stability.
We find, adopting directed agents to prepare in the method for X zeolite, that reduces the aging temperature of directed agents and zeolite precursor becomes the glue temperature, not only can obtain grain size and be 0.5～1.0 micron little crystal grain zeolite, and this zeolite has thermostability preferably, the less X zeolite of this crystal grain also can improve adsorbate in intragranular rate of diffusion, improves separation efficiency.
Description of drawings
Fig. 1 is the transmission electron microscope photo of the fine-grain X zeolite of the inventive method preparation.
Fig. 2 is the transmission electron microscope photo of X zeolite of preparation according to a conventional method.
Embodiment
The method for preparing fine-grain X zeolite provided by the invention comprises the steps:
(1) be (11～18) Na with silicon-containing compound, aluminum contained compound, sodium hydroxide and water according to mol ratio
2O: Al
2O
3: (10～17) SiO
2: (100～350) H
2The mixed of O is made directed agents after 0～10 ℃ of ageing,
(2) directed agents that silicon-containing compound, aluminum contained compound and water and (1) are made mixes at 0～10 ℃, makes to add the total mixture mole that makes after the directed agents and consist of (2.5～5) Na
2O: Al
2O
3: (3～5) SiO
2: (40～200) H
2O,
(3) total mixture that (2) are made is in 80～120 ℃ of crystallization 2～40 hours, washing, filters and dry.
Above-mentioned preparation method's step (1) is the preparation directed agents, the proportioning raw materials of this directed agents can adopt conventional method to prepare, as press USP4,166, method described in 099 is prepared the mixture of given mol ratio, but the mixture after the preparation of raw material needs ageing at low temperatures, preferred 5～20 hours of digestion time, and directed agents does not need crystallization.
Described step (2) is the precursor of preparation zeolite, and its synthetic method is that raw materials of synthetic zeolite is mixed, and then adds the directed agents of (1) step preparation, and the add-on of described raw material should make the mole of end reaction total mixture consist of (2.5～5) Na
2O: Al
2O
3: (3～5) SiO
2: (40～200) H
2O.The preparation of zeolite precursor also should be carried out at low temperatures, otherwise the zeolite particle diameter of preparation will be greater than 1.0 microns.
With directed agents with the preparation zeolite raw material mix after, can carry out step (3), described mixture is risen to comparatively high temps carries out crystallization.Preferred 90～110 ℃ of crystallization temperature, preferred 6～60 hours of time, more preferably 10～48 hours.
In the described method, during (2) step preparation zeolite precursor, can be earlier with raw materials of synthetic zeolite ageing 5～20 hours under 0～10 ℃ low temperature, the directed agents that makes with (1) step mixes at 0～10 ℃ again.Carry out crystallization then.
Material after the above-mentioned crystallization is washed according to a conventional method, filtered, promptly makes fine-grain X type zeolite after the drying.The ratio of the silicon oxide of this zeolite and aluminum oxide is less than 2.6, and degree of crystallinity reaches more than 80%.
In the described method, silicon-containing compound is selected from water glass or silicon sol, preferably water glass.Aluminum contained compound is selected from sodium aluminate, sodium metaaluminate or aluminum chloride.Sodium aluminate or sodium metaaluminate can be by aluminium hydroxide or aluminum chloride and sodium hydroxide prepared in reaction.The basicity of directed agents and synthesis material is provided by sodium hydroxide, with the Na in the mixing raw material
2O content is represented its height.
The add-on of described directed agents is counted 1～30 mole of % that reacts total mixture, preferred 5～20 moles of % with the butt aluminum oxide.
The crystal grain of the X type zeolite of the present invention's preparation is 0.5～1.0 micron.Zeolite grain is too small, and effective basket structure of absorption aromatic hydrocarbons will reduce in the zeolite, be unfavorable for improving adsorption efficiency; Zeolite grain is excessive, C
8Aromatic hydrocarbons is not high in the rate of diffusion of intracrystalline, and the zeolite utilization ratio reduces.
The fine-grain X zeolite that the inventive method provides is applicable to the adsorption separation process of forming similar compound, is specially adapted to from C
8Fractionation by adsorption p-Xylol in the aromatic hydrocarbons.
Further specify the present invention below by example, but the present invention is not limited to this.
In the example, synthesis material is Wenzhou Hua Hua group and produces.The zeolite mean grain size is measured with transmission electron microscopy (TEM), specific surface area is measured with CNS GB/T5816-1995 method, relative crystallinity (is seen " petrochemical complex analytical procedure " according to the RIPP146-90 standard method, Yang Cui waits volume surely, Science Press, nineteen ninety publishes) measure framework si-al ratio (SiO
2/ Al
2O
3Mol ratio) records the unit cell parameters a of NaX zeolite according to RIPP-145-90 standard method (the same)
0, calculate according to following formula then.
Example 1
Prepare fine-grain X zeolite by method of the present invention.
(1) preparation directed agents
At 264 ml water glass (Na
2The O1.384 mol, SiO
24.644 mol, proportion 1.278 kg/liter) 155 milliliters of high alkali deflection aluminium acid sodium solution (Na of middle adding
2The O5.226 mol, Al
2O
30.529 mol, proportion 1.310 kg/liter), 28 milliliters of NaOH solution (Na
2O5.306 mol, proportion 1.335 kg/liter) and 28 ml waters, after stirring with 350 rev/mins rotating speeds, 10 ℃ obtained directed agents in still aging 18 hours.
(2) preparation X zeolite
Under 5 ℃, in 172 ml water glass, add 374 milliliters of low alkali aluminium acid sodium solution (Na
2The O2.581 mol, Al
2O
30.9584 mol, proportion 1.264 kg/liter), add directed agents and 513 ml waters that 214 milliliters (1) step prepares again, stirred 0.5 hour with 350 rev/mins rotating speeds, be warming up to 100 ℃, static crystallization 10 hours.Product is through being washed to washings pH value less than 10, filter, 80 ℃ of dryings got NaX type zeolite in 12 hours, and its particle diameter records (magnification 5000) by the TEM photo of Fig. 1, performance data sees Table 1, and wherein silicon/al mole ratio is the mol ratio of silicon oxide and aluminum oxide in the zeolite framework.
Example 2
Method according to example 1 prepares the X zeolite, and the ageing temperature of directed agents that different is is 5 ℃, and the time is 6 hours, and under 10 ℃ low alkali aluminium acid sodium solution is added in the water glass.The zeolite properties data that make see Table 1.
Example 3
Under 10 ℃, in 224 ml water glass, add 374 milliliters of low alkali aluminium acid sodium solutions, 55 milliliters of NaOH solution, 448 ml waters, after stirring with 350 rev/mins rotating speeds, 5 ℃ of following ageings 8 hours, add 109 milliliters of directed agents again by the preparation of example 1 method, stir and be warming up to 98 ℃ after 1 hour, static crystallization 12 hours, product filters through being washed to washings pH value less than 10,70 ℃ of dryings 16 hours.The X type zeolite properties data that make see Table 1.
Example 4
Method by example 3 prepares the X zeolite, different is with water glass, sodium aluminate solution, NaOH solution and water mix after, 10 ℃ of following ageings 10 hours add directed agents again, the X type zeolite properties data that make see Table 1.
Example 5
Method according to example 1 prepares the X zeolite, adds 132 milliliters sodium aluminate (Na during preparation directed agents that different is
2The O4.828 mol, Al
2O
30.623 mol, proportion 1.406 kg/liter) and 60 milliliters of NaOH solution, the zeolite properties data that make see Table 1.
Comparative Examples 1
This example prepares the NaX zeolite with ordinary method.
In 131 ml water glass, add 47 milliliters of NaOH solution, 285 ml waters and 178 milliliters of low alkali aluminium acid sodium solutions, after stirring with 350 rev/mins rotating speeds, still aging 10 hours at 22 ℃, be warming up to 103 ℃ of static crystallization 13 hours, product is through being washed to washings pH value less than 10, filter 80 ℃ of dryings 12 hours.The X type zeolite properties data that make see Table 1, and its TEM photo is seen Fig. 2.
Comparative Examples 2
This Comparative Examples is pressed USP4, and 166,099 method prepares the X zeolite.
(1) preparation crystal seed
550 gram water glass and 112 gram NaOH (analytical pure) and 38 gram water are mixed and make solution A, get 29 and restrain sodium aluminate (Na
2O: Al
2O
3: 3H
2O) be dissolved in 300 grams and make solution in the water, 0 ℃, stir down and join in the above-mentioned solution A, and stirred 1 hour at 0 ℃ of rotating speed with 350 rev/mins, the gained mixture is 20 ℃ of static wearing out 16 hours, be warming up to 100 ℃ of static crystallization again 6 hours, product wash with water to washings pH value less than 10.85 ℃ of dryings 12 hours, the X zeolite seed crystal, its SiO
2/ Al
2O
3Mol ratio is 2.7, and grain size is 0.03～0.1 micron, and specific surface area is 700 meters
2/ gram.
(2) preparation X zeolite
36.6 milliliters of NaOH solution of adding and 224 ml waters mix in 102 ml water glass, under 350 rev/mins rotating speeds stir, add 165 milliliters of low alkali aluminium acid sodium solutions in 20 ℃, the gained mixture is static aging 16 hours at 20 ℃, add the crystal seed that 5 gram (1) steps made again, be warming up to 98 ℃ of static crystallization after stirring 4 hours, product is through being washed to washings pH value less than 10, filter 70 ℃ of dryings 16 hours.The NaX type zeolite properties data that make see Table 1.
Comparative Examples 3
In 315 ml water glass, add 82 milliliters of NaOH solution, 401 milliliters of low alkali aluminium acid sodium solutions and 338 ml waters, stirred the back 8 ℃ of ageings 9 hours, be warming up to 98 ℃ of static crystallization 10 hours, product is through being washed to washings pH value less than 10, filter 80 ℃ of dryings 12 hours.The X type zeolite properties data that make see Table 1.
Example 6
This example is estimated the thermostability of NaX type zeolite.
The NaX zeolite sample that makes in each example and the Comparative Examples 540 ℃ of roastings 4 hours, is recorded relative crystallinity before and after the zeolite roasting with X-ray diffraction method, the results are shown in Table 1.
As shown in Table 1, the X zeolite of the inventive method preparation not only crystal grain and still have higher relative crystallinity after 540 ℃ of roastings all less than 1 micron.Comparative Examples 1 adopts the X zeolite of ordinary method preparation, its crystal grain is bigger, and Comparative Examples 2 needs and will make crystal seed after the directed agents crystallization, prepares the X zeolite with this crystal seed and raw material reaction again, obviously, this method is than the inventive method complexity, and the zeolite grain of preparation is greater than 1.0 microns, and Comparative Examples adopts low temperature to become the glue legal system to be equipped with zeolite outward, though can make zeolite grain less than 1.0 microns, but the thermostability that makes zeolite is relatively poor, and relative crystallinity drops to 85% after the roasting.Table 1
| Instance number | The zeolite particle diameter, μ m | Silicon/al mole ratio | Relative crystallinity, % | Relative crystallinity after the roasting, % | Specific surface area, rice 2/ gram |
| ????1 | ????0.5 | ????2.43 | ????105 | ????100 | ????715 |
| ????2 | ????0.7 | ????2.45 | ????100 | ????98 | ????700 |
| ????3 | ????0.5 | ????2.40 | ????107 | ????101 | ????720 |
| ????4 | ????0.6 | ????2.50 | ????98 | ????96 | ????700 |
| ????5 | ????0.8 | ????2.46 | ????103 | ????98 | ????702 |
| Comparative Examples 1 | ????2.5 | ????2.52 | ????110 | ????100 | ????720 |
| Comparative Examples 2 | ????1.1 | ????2.56 | ????110 | ????107 | ????740 |
| Comparative Examples 3 | ????0.8 | ????2.42 | ????108 | ????85 | ????710 |
Claims (8)
1, a kind of method for preparing fine-grain X zeolite comprises the steps:
(1) be (1～18) Na with silicon-containing compound, aluminum contained compound, sodium hydroxide and water according to mol ratio
2O: Al
2O
3: (10～17) SiO
2: (100～350) H
2The mixed of O is made directed agents after 0～10 ℃ of ageing,
(2) directed agents that silicon-containing compound, aluminum contained compound and water and (1) are made mixes at 0～10 ℃, makes to add the total mixture mole that makes after the directed agents and consist of (2.5～5) Na
2O: Al
2O
3: (3～5) SiO
2: (40～200) H
2O,
(3) total mixture that (2) are made is in 80～120 ℃ of crystallization 2～40 hours, washing, filters and dry.
2, in accordance with the method for claim 1, it is characterized in that the digestion time described in (1) is 5～20 hours.
3, in accordance with the method for claim 1, it is characterized in that earlier silicon-containing compound, aluminum contained compound and water being mixed in (2) step, 0～10 ℃ of ageing 5～20 hours, the directed agents that makes with (1) step mixes at 0～10 ℃ again.
4,, it is characterized in that described silicon-containing compound is selected from water glass or silicon sol according to described any one method of claim 1～3.
5,, it is characterized in that described aluminum contained compound is selected from sodium aluminate, sodium metaaluminate or aluminum chloride according to described any one method of claim 1～3.
6,, it is characterized in that the add-on of described directed agents is counted 1～30 mole of % that reacts total mixture with the butt aluminum oxide according to described any one method of claim 1～3.
7, in accordance with the method for claim 6, the add-on that it is characterized in that directed agents is counted 5～20 moles of % that react total mixture with the butt aluminum oxide.
8,, it is characterized in that the crystal grain of the X zeolite for preparing is 0.5～1.0 micron according to described any one method of claim 1～3.
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Cited By (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1323944C (en) * | 2005-08-02 | 2007-07-04 | 洛阳市建龙化工有限公司 | Process method of improved 13X molecular screen |
| CN100358807C (en) * | 2004-07-12 | 2008-01-02 | 中国石油化工股份有限公司 | Selective preparation method for zeolite |
| CN101254928B (en) * | 2007-02-28 | 2010-06-23 | 中国石油化工股份有限公司 | Method for preparing fine-grain low silica/alumina ratio X zeolite |
| CN101863493A (en) * | 2010-06-23 | 2010-10-20 | 深圳市海川实业股份有限公司 | Method for preparing X-zeolite by taking quartz sand as raw material |
| CN102417190A (en) * | 2011-09-02 | 2012-04-18 | 吉林大学 | Method for preparing low-silicon NaX zeolite by applying activated silicon source |
| CN102107881B (en) * | 2009-12-23 | 2012-12-12 | 深圳市海川实业股份有限公司 | Method for preparing NaX zeolite |
| CN103508463A (en) * | 2012-06-15 | 2014-01-15 | 中国石油化工股份有限公司 | Preparation method of binderless spherical faujasite particles |
| CN103523796A (en) * | 2013-09-27 | 2014-01-22 | 上海绿强新材料有限公司 | Synthesis method and application of submicron X-type molecular sieve |
| US8791039B2 (en) | 2008-01-31 | 2014-07-29 | China Petroleum & Chemical Corporation | Agglomerated zeolite adsorbents and process for producing the same |
| CN110508241A (en) * | 2018-05-22 | 2019-11-29 | 中国石油化工股份有限公司 | A kind of coalescence type adsorbent and preparation method thereof |
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2002
- 2002-03-29 CN CNB021162832A patent/CN1191199C/en not_active Expired - Lifetime
Cited By (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN100358807C (en) * | 2004-07-12 | 2008-01-02 | 中国石油化工股份有限公司 | Selective preparation method for zeolite |
| CN1323944C (en) * | 2005-08-02 | 2007-07-04 | 洛阳市建龙化工有限公司 | Process method of improved 13X molecular screen |
| CN101254928B (en) * | 2007-02-28 | 2010-06-23 | 中国石油化工股份有限公司 | Method for preparing fine-grain low silica/alumina ratio X zeolite |
| US8791039B2 (en) | 2008-01-31 | 2014-07-29 | China Petroleum & Chemical Corporation | Agglomerated zeolite adsorbents and process for producing the same |
| CN102107881B (en) * | 2009-12-23 | 2012-12-12 | 深圳市海川实业股份有限公司 | Method for preparing NaX zeolite |
| CN101863493A (en) * | 2010-06-23 | 2010-10-20 | 深圳市海川实业股份有限公司 | Method for preparing X-zeolite by taking quartz sand as raw material |
| CN101863493B (en) * | 2010-06-23 | 2012-07-18 | 深圳市海川实业股份有限公司 | Method for preparing X-zeolite by taking quartz sand as raw material |
| CN102417190A (en) * | 2011-09-02 | 2012-04-18 | 吉林大学 | Method for preparing low-silicon NaX zeolite by applying activated silicon source |
| CN103508463A (en) * | 2012-06-15 | 2014-01-15 | 中国石油化工股份有限公司 | Preparation method of binderless spherical faujasite particles |
| CN103508463B (en) * | 2012-06-15 | 2015-07-01 | 中国石油化工股份有限公司 | Preparation method of binderless spherical faujasite particles |
| CN103523796A (en) * | 2013-09-27 | 2014-01-22 | 上海绿强新材料有限公司 | Synthesis method and application of submicron X-type molecular sieve |
| CN110508241A (en) * | 2018-05-22 | 2019-11-29 | 中国石油化工股份有限公司 | A kind of coalescence type adsorbent and preparation method thereof |
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