CN100358805C - Nitrogen-containing aluminium phosphate mesoporous molecular sieve and its prepn - Google Patents
Nitrogen-containing aluminium phosphate mesoporous molecular sieve and its prepn Download PDFInfo
- Publication number
- CN100358805C CN100358805C CNB2006100293629A CN200610029362A CN100358805C CN 100358805 C CN100358805 C CN 100358805C CN B2006100293629 A CNB2006100293629 A CN B2006100293629A CN 200610029362 A CN200610029362 A CN 200610029362A CN 100358805 C CN100358805 C CN 100358805C
- Authority
- CN
- China
- Prior art keywords
- molecular sieve
- mesoporous
- aluminium phosphate
- aluminum phosphate
- mesoporous molecular
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
Images
Abstract
The present invention relates to nitrogen-containing aluminum phosphate mesoporous molecular sieve and its preparation process. The prepared mesoporous molecular sieve has pore size distribution of 4-7.0 nm, specific surface area of 150-400 sq m/g and nitrogen content up to 16.1 wt%. The preparation process includes the following two steps: 1. the first synthesis of ordered mesoporous aluminum phosphate base material; and 2. the subsequent gas-solid reaction of the mesoporous aluminum phosphate base material with introduced dry ammonia gas at high temperature inside a tubular furnace to prepare nitrogen-containing aluminum phosphate mesoporous molecular sieve. The gas-solid reaction has ammonia gas flow rate of 50-1000 ml/min, nitriding temperature of 700-800 deg.c and nitriding time within 14 hr. The prepared nitrogen-containing aluminum phosphate mesoporous molecular sieve has great specific surface area, great pore volume, controllable nitrogen content, great latent application, etc.
Description
Technical field
The present invention relates to a kind of nitrogenous aluminium phosphate mesoporous molecular sieve and synthetic method thereof.In aluminium phosphate mesoporous base-material, introduce nitrogen-atoms specifically, thereby the Sauerstoffatom that nitrogen-atoms is partly replaced in the aluminum phosphate obtains a kind of nitrogenous, high-specific surface area, orderly aluminium phosphate mesoporous molecular sieve of hole arrangement.This preparation method also can expand to preparation different metal aluminium phosphate mesoporous molecular sieve ion doping, nitrogenous.
Background technology
Since Mobil Oil Corp. successfully synthesized the M41S mesoporous material, mesoporous material was because it has the adjustable (advantages such as 2～10nm) and be subjected to paying close attention to widely in Application Areass such as heterogeneous catalyst, absorption in high specific surface area, narrow pore size distribution and aperture.
Recent years, base catalyzed reactions has been brought into play more and more important effect in modern fine chemistry industry industry, but comparatively speaking, the solid base catalyst kind that can select to use is more than solid acid catalyst kind much less, and the research and development process of accelerating solid base catalyst is very urgent.At present, the research and development emphasis about solid base catalyst mainly concentrates on metal oxide and the alkali metals modified zeolite.In recent years, some new particularly nitrogenous materials of catalyzed by solid base material just attract much attention.Unformed nitrogenous aluminum phosphate be wherein a kind of novel nitrogen-containing base catalysis material (Journal of Catalysis, 1996,163,392-398).This kind new catalyst obtains with ammonia gas react under 800 ℃ of high temperature by unformed aluminum phosphate, wherein the Sauerstoffatom that can partly replace in the aluminum phosphate under the effect of temperature of the nitrogen-atoms in the ammonia enters the aluminum phosphate skeleton, generate nitrogenize aluminum phosphate base catalysis material, and the nitrogen content of material can be regulated by nitriding temperature and nitridation time.But in this unformed nitrogenize aluminum phosphate material structure, there is not orderly mesopore orbit, thereby do not have the advantage of ordered mesoporous material yet, limited its application to a certain extent, such as selectivity catalysis etc.Therefore, explore the technology focus that the method for preparing the nitrogenize aluminum phosphate new catalytic material with ordered mesoporous pore canals structure becomes this field.
Summary of the invention
The object of the present invention is to provide a kind of nitrogenous aluminium phosphate mesoporous molecular sieve and preparation method thereof.The feature molecular formula of such nitrogenous aluminium phosphate mesoporous molecular sieve is AlPO
xN
y, wherein " x ", " y " are respectively O, the molar fraction of N, and 0＜y≤1.26,2x+3y=8.Such nitrogenous aluminium phosphate mesoporous molecular sieve is to prepare by the direct aluminum phosphate base-material that has an ordered mesoporous pore canals structure with the ammonia high-temperature ammonolysis.At first prepare aluminum phosphate base-material, then it is put into alumina tube furnace and feed ammonia nitrogenize at high temperature, control the nitrogen content of the finished product by control nitriding temperature and nitridation time with ordered mesoporous pore canals structure.Do not cave in for the meso-hole structure that guarantees product simultaneously, strict control nitriding temperature can not be too high, and nitridation time can not be long.Adopt the nitrogenous aluminium phosphate mesoporous molecular sieve of the present invention's preparation not only to have adjustable nitrogen content (being no more than 16.1wt%), but also have the ordered mesoporous pore canals of aperture at 4-7.0nm, its specific surface area is 150-400m
2/ g, pore volume are 0.40-0.50ml/g.From Fig. 1, can clearly see in the prepared nitrogenous aluminum phosphate material and have orderly mesopore orbit.
The nitrogenous aluminium phosphate mesoporous material preparation that the present invention relates to is divided into two steps: (1) ordered mesoporous aluminum phosphate (AlPO
4) the base-material preparation.With aluminium source (aluminum trichloride (anhydrous)), phosphorus source (phosphoric acid), organic formwork agent and dehydrated alcohol are raw material, be mixed with aluminium, phosphorus, ethanolic soln that the organic formwork agent three is stable earlier, behind the mixing solutions stirring certain hour that obtains, put into container, at a certain temperature solvent flashing, pour ceramic boat into obtaining xerogel then, put into calcining furnace and remove organic formwork agent.(2) grind the flaky aluminium phosphate mesoporous material that obtains again afterwards, and put into the logical ammonia gas-solid reaction of tube furnace and implement high-temperature ammonolysis (700～800 ℃), obtain nitrogenous ordered mesoporous aluminum phosphate molecular sieve-4 A lPO behind the certain hour
xN
y
The concrete step of preparation process of nitrogenous ordered mesoporous aluminum phosphate molecular sieve is: the 1) synthesizing ordered mesoporous aluminum phosphate (AlPO of elder generation
4) mesoporous base-material: (R is polyethylene-polypropylene-poly triblock copolymer EO with template R
aPO
bEO
cOr cetyl trimethylammonium bromide CTAB) is dissolved in a certain amount of alcohol solvent, adds phosphoric acid (concentration is 85% phosphoric acid) and aluminium source (aluminum trichloride (anhydrous)) then, continue stirring and obtained colloidal sol in 5～12 hours; 2) resulting colloidal sol is poured in the container, put into baking oven, low temperature 30-40 ℃ was dried by the fire 6-12 hour, high temperature 60-90 ℃ of baking 1-4 hour, obtained xerogel then.Pour resulting xerogel into ceramic boat from container, and in the calcining furnace of packing into, remove organic formwork agent, obtain aluminium phosphate mesoporous base-material at 350-600 ℃ of temperature lower calcination.3) the aluminium phosphate mesoporous base-material that will obtain is put into atmosphere furnace, feeds the NH of clean dry
3, realize high-temperature ammonolysis, nitriding temperature is 700-800 ℃; Nitridation time is 2～14 hours; Ammonia flow is 50-1000ml/min.Obtain nitrogenous aluminium phosphate mesoporous molecular sieve AlPO
xN
y, its nitrogen content is no more than 16.1wt%.
Described polyethylene-polypropylene-poly triblock copolymer EO
aPO
bEO
cMiddle a, b and c are the polymerization degree, and in the 10-100 scope, the molecular weight of this polymkeric substance is between 3000-8000 respectively.
The mole proportioning of each material is in the described sol solution: (0.0003～0.0009) R: 1.0P
2O
5: 1.0 Al
2O
3: (0.1～0.5) ethanol, the consumption in phosphorus source and aluminium source all is converted into P
2O
5And Al
2O
3Calculate.
For high-temperature ammonolysis ordered mesoporous aluminum phosphate base-material, most important process control parameter is exactly nitriding temperature and nitridation time.Nitriding temperature can not be low excessively, and when nitriding temperature was lower than 700 ℃, aluminum phosphate and ammonia gas react were very slow, and the corresponding time that obtains the ordered mesoporous aluminum phosphate molecular sieve of high nitrogen-containing will prolong.Simultaneously, nitriding temperature can not be too high, when nitriding temperature is higher than 800 ℃, and the phosphorus meeting heavy losses in the ordered mesoporous aluminum phosphate, the final completely destroy that also causes meso-hole structure.Working as nitriding temperature in addition is 800 ℃, and the time of nitrogenize ordered mesoporous aluminum phosphate base-material can not be long, and general nitridation time is no more than 14 hours.Along with the prolongation of nitridation time, mesoporous framework can be shunk to some extent because temperature effective and nitrogen replace the double influence of oxygen gradually, and general performance is the contraction in aperture.In case nitridation time is long, Sauerstoffatoms a large amount of in the mesoporous aluminum phosphate are replaced by the nitrogen-atoms in the ammonia, and aluminum phosphate microstructure meeting considerable damage finally causes collapsing of meso-hole structure.
Characteristics of the present invention are: combine with high-temperature ammonolysis technology ordered mesoporous aluminum phosphate is synthetic, prepared a kind of nitrogenous aluminium phosphate mesoporous molecular sieve.The pore size distribution of prepared mesopore molecular sieve is in the 4-7.0nm scope, and specific surface area is 150-400m
2/ g, high nitrogen-containing is 16.1wt%.This material has sizable potential using value in fields such as fractionation by adsorption, acid-base catalysis, micro sensors.
The invention provides a kind of effective preparation method of nitrogenous aluminium phosphate mesoporous molecular sieve, with the ordered mesoporous aluminum phosphate base-material is presoma, obtain a kind of mesopore molecular sieve of nitrogenous aluminum phosphate by high-temperature ammonolysis in ammonia, control nitriding temperature and nitridation time can be controlled the nitrogen content of final material, the integrity that simultaneously suitable nitriding temperature and nitridation time have also guaranteed meso-hole structure.
Description of drawings
Fig. 1: nitrogenous aluminium phosphate mesoporous material inner duct ordered arrangement (HRTEM photo, scale length 50nm).
Embodiment
With 0.8-1.2g (PEO)
20(PPO)
70(PEO)
20Perhaps 0.5-0.7g CTAB (cetyl trimethylammonium bromide CTAB) template is dissolved in the 20-30g ethanol and stirs 0.5h, and then adds 0.005mol aluminum trichloride (anhydrous) (AlCl
3) and 0.005mol phosphoric acid (H
3PO
4, concentration 85%) after, continue to stir 5-12 hour, then mixture is poured in the container, put into 30-40 ℃ of baking of baking oven low temperature 6-12 hour, dried by the fire again 1-4 hour at high temperature 60-90 ℃ then, obtain xerogel.With the xerogel calcining furnace of packing into, template is removed in calcining in air, obtains ordered mesoporous aluminum phosphate (AlPO
4) base-material.Then the mesoporous aluminum phosphate material that obtains is put into the tubular type road and fed ammonia nitrogenize, nitriding temperature 700-800 ℃, nitridation time 2-14h.Final product is to have orderly aluminium phosphate molecular sieve (the AlPO mesopore orbit structure, nitrogenous
xN
y), nitrogen content is no more than 16.1wt%.The specific embodiment characteristic of the nitrogenous mesoporous aluminum phosphate molecular sieve of preparation is listed in table 1 under the different condition.
The technology of the nitrogenous aluminium phosphate mesoporous molecular sieve for preparing under table 1, the different condition and performance perameter contrast.
| Embodiment | Nitriding temperature/℃ | Nitridation time/h | Nitrogen content/wt% | Molecular formula | Mesoporous aperture/nm | Pore volume/cm 3g -1 | Specific surface area/m 2g -1 |
| 1 | 700 | 8 | 6.4 | AlPO 3.20N 0.53 | 5.4 | 0.45 | 270 |
| 2 | 750 | 8 | 8.9 | AlPO 2.91N 0.73 | 5.2 | 0.43 | 245 |
| 3 | 800 | 2 | 5.8 | AlPO 3.27N 0.49 | 5.5 | 0.47 | 256 |
| 4 | 800 | 4 | 8.7 | AlPO 2.93N 0.71 | 5.3 | 0.46 | 250 |
| 5 | 800 | 8 | 12.5 | AlPO 2.50N 1.00 | 5.3 | 0.43 | 237 |
| 6 | 800 | 12 | 14.9 | AlPO 2.24N 1.17 | 5.1 | 0.43 | 221 |
| 7 | 800 | 14 | 16.1 | AlPO 2.11N 1.26 | 4.9 | 0.40 | 195 |
Claims (8)
1, a kind of nitrogenous aluminium phosphate mesoporous molecular sieve, its feature molecular formula is AlPO
xN
y, wherein x and y are respectively the mole number of O and N, 0＜y≤1.26, and 2x+3y=8, and have the order mesoporous passage of aperture at 4-7.0nm.
2, by the described nitrogenous aluminium phosphate mesoporous molecular sieve of claim 1, its constitutional features is that the specific surface area of described mesopore molecular sieve is: 150-400m
2/ g; Pore volume 0.40-0.50ml/g.
3,, it is characterized in that high nitrogen-containing is 16.1wt% by the described nitrogenous aluminium phosphate mesoporous molecular sieve of claim 1.
4, preparation is characterized in that may further comprise the steps as the method for claim 1,2 or 3 described mesopore molecular sieves:
(a) the synthesizing ordered mesoporous aluminum phosphate base-material of elder generation, template R is dissolved in a certain amount of alcohol solvent, add phosphoric acid and aluminium source then, continue stirring and obtained colloidal sol in 5～12 hours, described template R is 1) polyethylene-polypropylene-poly triblock copolymer EO
aPO
bEO
c, a wherein, b, c are the polymerization degree, and a, b, c be respectively in the 10-100 scope, or 2) cetyl trimethylammonium bromide; The mole proportioning of each material is: (0.0003～0.0009) R: 1.0 P
2O
5: 1.0 Al
2O
3: (0.1～0.5) ethanol, the consumption in phosphorus source and aluminium source all is converted into P
2O
5And Al
2O
3Calculate;
(b) colloidal sol that step (a) is obtained is poured in the container, puts into baking oven, and baking is 6-12 hour under 30-40 ℃ of temperature, dries by the fire 1-4 hour under 60-90 ℃ of temperature then, obtains xerogel;
(c) xerogel that step (b) is obtained is poured ceramic boat from container into, and in the calcining furnace of packing into, removes organic formwork agent at 350-600 ℃ of temperature lower calcination, obtains orderly aluminium phosphate mesoporous base-material;
(d) the aluminium phosphate mesoporous base-material that step (c) is obtained is put into atmosphere furnace, feeds the NH of clean dry
3, high-temperature ammonolysis obtains nitrogenous aluminium phosphate mesoporous molecular sieve; Nitriding temperature is 700-800 ℃, and nitridation time is 2-14 hour.
5, according to the described preparation method of claim 4, the molecular weight that it is characterized in that described polyethylene-polypropylene-poly triblock copolymer is between the 3000-8000.
6,, it is characterized in that described aluminium source is an aluminum trichloride (anhydrous) according to the described preparation method of claim 4; Described concentration of phosphoric acid is 85%.
7,, it is characterized in that described ammonia flow is 50-1000ml/min according to the described preparation method of claim 4.
8, a kind of application by claim 1,2 or 3 described nitrogenous aluminium phosphate mesoporous molecular sieves is characterized in that being used for fractionation by adsorption, acid-base catalysis or micro sensor.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100293629A CN100358805C (en) | 2006-07-26 | 2006-07-26 | Nitrogen-containing aluminium phosphate mesoporous molecular sieve and its prepn |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CNB2006100293629A CN100358805C (en) | 2006-07-26 | 2006-07-26 | Nitrogen-containing aluminium phosphate mesoporous molecular sieve and its prepn |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN1887706A CN1887706A (en) | 2007-01-03 |
| CN100358805C true CN100358805C (en) | 2008-01-02 |
Family
ID=37576986
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNB2006100293629A Expired - Fee Related CN100358805C (en) | 2006-07-26 | 2006-07-26 | Nitrogen-containing aluminium phosphate mesoporous molecular sieve and its prepn |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN100358805C (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9802182B2 (en) | 2013-03-13 | 2017-10-31 | Basf Corporation | Stabilized metal-exchanged SAPO material |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102616809B (en) * | 2012-03-29 | 2014-11-05 | 昆明理工大学 | Preparation method for NZP family mesoporous phosphate molecular sieve CaZr4P6O24 |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4310440A (en) * | 1980-07-07 | 1982-01-12 | Union Carbide Corporation | Crystalline metallophosphate compositions |
| CN1346797A (en) * | 2001-09-26 | 2002-05-01 | 复旦大学 | Molecular sieve of aluminium phosphate and its preparing process |
| JP2005060173A (en) * | 2003-08-13 | 2005-03-10 | Mitsubishi Chemicals Corp | Method of producing aluminophosphates |
| CN1749165A (en) * | 2005-08-26 | 2006-03-22 | 吉林大学 | High heat stability ordered mesoporous aluminum phosphate material and its preparing method |
-
2006
- 2006-07-26 CN CNB2006100293629A patent/CN100358805C/en not_active Expired - Fee Related
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4310440A (en) * | 1980-07-07 | 1982-01-12 | Union Carbide Corporation | Crystalline metallophosphate compositions |
| CN1346797A (en) * | 2001-09-26 | 2002-05-01 | 复旦大学 | Molecular sieve of aluminium phosphate and its preparing process |
| JP2005060173A (en) * | 2003-08-13 | 2005-03-10 | Mitsubishi Chemicals Corp | Method of producing aluminophosphates |
| CN1749165A (en) * | 2005-08-26 | 2006-03-22 | 吉林大学 | High heat stability ordered mesoporous aluminum phosphate material and its preparing method |
Non-Patent Citations (1)
| Title |
|---|
| 在非水体系中介孔磷酸铝分子筛的合成与表征. 吕彤等.精细石油化工，第1期. 2005 * |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US9802182B2 (en) | 2013-03-13 | 2017-10-31 | Basf Corporation | Stabilized metal-exchanged SAPO material |
| US9931620B2 (en) | 2013-03-13 | 2018-04-03 | Basf Corporation | Stabilized metal-exchanged SAPO material |
Also Published As
| Publication number | Publication date |
|---|---|
| CN1887706A (en) | 2007-01-03 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN101643219B (en) | Preparation method of nano-ZSM-5 molecular sieve | |
| CN104248990B (en) | The preparation method of the composite mesoporous carrier of spherical attapulgite and loaded catalyst and its preparation method and application and ethyl acetate | |
| CN101391786B (en) | Method for preparing high specific surface area nano alumina material | |
| CN101804324B (en) | Modified molecular sieve with high selectivity to ammonia nitrogen in waste water and preparation method thereof | |
| CN106964396B (en) | RTH type topological structure molecular sieve catalyst and its preparation method and application for dimethyl ether carbonylation reaction | |
| CN102795635A (en) | Multi-orifice zeolite material as well as preparation method and application thereof | |
| CN104043477B (en) | ZSM-5/MCM-48 composite molecular sieve, preparation method and application thereof | |
| CN106830007A (en) | With the molecular sieve catalysts of multi-stage porous SSZ 13 and its synthetic method and application | |
| CN101172240B (en) | Method for preparing propylene by butylene disproportionation | |
| CN106044793A (en) | Method for synthesis of nanometer ZSM-5 molecular sieve from mother liquor flocculate | |
| CN100522349C (en) | Novel gamma aluminium oxide catalyst and producing technology | |
| CN106268926A (en) | A kind of MCM-22 molecular sieve with multistage pore canal and its preparation method and application | |
| CN100358805C (en) | Nitrogen-containing aluminium phosphate mesoporous molecular sieve and its prepn | |
| CN108821304A (en) | High activity multi-stage porous Titanium Sieve Molecular Sieve and its preparation method and application | |
| CN102451745A (en) | Hydrocracking catalyst containing Y-shaped molecular sieve/amorphous silicon-aluminum, and preparation method thereof | |
| CN110860307A (en) | Beta molecular sieve catalyst, preparation method and application thereof in preparation of aromatic ketone by acylation method | |
| AU610647B2 (en) | Silica extrudates | |
| CN101445228A (en) | Spherical nano-aluminum phosphate powder and preparation method | |
| JP4524427B2 (en) | Composition comprising heteropolyacid salt and inorganic oxide and method for producing the same | |
| CN103803616B (en) | Preparation method for alumina dry gel | |
| CN1121979C (en) | Process for preparing ZSM-5 molecular sieve | |
| CN106586996A (en) | Preparation method of anhydrous iron phosphate | |
| CN1380250A (en) | Double mesopore molecular sieve and its preparation method | |
| CN104944440B (en) | A kind of HTS poromerics and its synthetic method | |
| CN112569922A (en) | Amorphous silicon-aluminum oxide catalyst and preparation method and application thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20080102 Termination date: 20140726 |
|
| EXPY | Termination of patent right or utility model |