CN1301593A - MeAPSO-17 molecular sieve and its synthesizing method - Google Patents
MeAPSO-17 molecular sieve and its synthesizing method Download PDFInfo
- Publication number
- CN1301593A CN1301593A CN 99127142 CN99127142A CN1301593A CN 1301593 A CN1301593 A CN 1301593A CN 99127142 CN99127142 CN 99127142 CN 99127142 A CN99127142 A CN 99127142A CN 1301593 A CN1301593 A CN 1301593A
- Authority
- CN
- China
- Prior art keywords
- molecular sieve
- meapso
- described synthetic
- template agent
- mixture
- 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.)
- Granted
Links
Landscapes
- Silicates, Zeolites, And Molecular Sieves (AREA)
- Catalysts (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
A new-water-base chemical composition of the molecular sieve MeAPSO-17 is expressed by mR.nMe(SixAlyPz)O2, where R is one template agent existing in pores of molecular sieve, m as the molar number of R in each mole of (SixAlyPz)O2 is 0.03-2.00; x,y and z are mole fractions of Si, Al and P atoms separately, and x+y+z=1 and x=0.001-0.60, y=0.01-0.06 and z=0.01-0.06; Me is metal atom entering the molecular sieve, n as the molar number of Me in each mole of (SixAlyPz)O2 is 0.01-0.60. By altering the amount of added metal compound, the surface acidity of the said molecular sieve may be regulated so that its catalytic performance may be raised greatly.
Description
The invention provides a kind of MeAPSO-17 molecular sieve and synthetic method thereof.
U.S. Pat P 4,440,871 once disclosed the synthetic method of several silicoaluminophosphamolecular molecular sieves, its technical characterstic is to adopt silicon source, aluminium source, phosphorus source and different template agent to synthesize a class SAPO molecular sieve, the molecular sieve of some of them small structure such as SAPO-34 etc. have been successfully applied to MTO (preparing low carbon olefinic hydrocarbon with methanol) or SDTO processes such as (synthesis gas are produced low-carbon alkene via dimethyl ether), but the application of SAPO-17 molecular sieve report is less.The SAPO-17 molecular sieve has been formed the ERI structure by phosphorus, silicon, aluminium and oxygen, and its construction unit is by PO
2 +, AlO
2 -And SiO
2Tetrahedron is formed.Anhydrous chemical constitution formula can be expressed as: mR:(Si
xAl
yP
z) O
2, wherein R is the template agent that is present in the microporous molecular sieve, m is every mole of (Si
xAl
yP
z) O
2The molal quantity of middle R, x, y, z are respectively the molar fraction of Si, Al, P, and satisfy x+y+z=1.
The object of the present invention is to provide a kind of MeAPSO-17 molecular sieve, this molecular sieve analog can pass through its surface acidity of amount modulation of the metallic compound of adding, thereby can improve its catalytic perfomance greatly.
MeAPSO-17 molecular sieve provided by the invention is characterized in that the moisture-free basis chemical composition of institute's synthesis of molecular sieve can be expressed as: mRnMe:(Si
xAl
yP
z) O
2, wherein R is a kind of template agent that is present in the microporous molecular sieve, m is every mole of (Si
xAl
yP
z) O
2The molal quantity of middle R, and m=0.03~2.00; X, y, z are respectively the molar fraction of Si, Al, P, and satisfy x+y+z=1, simultaneously, and x=0.001~0.60, y=0.01~0.60, z=0.01~0.60; Me is the metallic atom that enters in the molecular sieve, and n is every mole of (SixAlyPz) O
2The molal quantity of middle Me, n=0.01~0.60..
In the molecular sieve of the invention described above, metallic atom can MeO
2 qTetrahedroid becomes framework of molecular sieve or otherwise is present in the molecular sieve.In addition, the metallic atom Me that is present in the molecular sieve is a kind of or several arbitrarily in the metals such as titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, magnesium, calcium, strontium, barium and lanthanum.
Synthetic MeAPSO-17 molecular sieve method provided by the invention is characterized in that preparation process is as follows:
(1) in proportion silicon source material, aluminium source material, phosphorus source material, metallic compound, template agent and water are under agitation mixed, get initial gel mixture;
(2) will seal in the initial gel mixture material immigration stainless steel synthesis reactor, constant temperature is 2-10 hour in 100~130 ℃ of baking ovens.Be warmed up to 185~205 ℃ again, constant temperature 20-160 hour, complete until crystallization;
(3) solid crystallized product is separated with mother liquor, wash to neutrality, behind 80-130 ℃ of air drying, obtain the MeAPSO-17 molecular screen primary powder with deionized water.
(4) molecular screen primary powder is no less than 3 hours 300-700 ℃ of following bubbling air roasting, promptly obtains adsorbent and the catalyst of molecular sieve MeAPSO-17.
Used silicon source is a kind of or any several mixture in Ludox, waterglass, active silica or the positive esters of silicon acis; The aluminium source is a kind of or any several mixture in aluminium salt, aluminate, activated alumina, aluminum alkoxide, false boehmite or the boehmite; The phosphorus source is a kind of or any several mixture in orthophosphoric acid, phosphate, organic phosphorus compound or the phosphorous oxides; Metallic compound is a kind of in the oxide, oxychlorination thing of metals such as titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, magnesium, calcium, strontium, barium and lanthanum or inorganic, the organic metal hydrochlorate or several mixture arbitrarily.The template agent is a kind of or any several mixture in cyclohexylamine, triethylamine, diethylamine, n-propylamine, isopropylamine, di-n-propylamine, diisopropylamine, tripropyl amine (TPA), n-butylamine, isobutyl amine, monoethanolamine, diethanol amine, triethanolamine, tetramethyl oxyammonia, tetraethyl oxyammonia, tetrapropyl oxyammonia or tetrabutylammonium hydroxide amine and the alcohols.
Proportioning between each raw material (by the oxide molecule ratio) is:
MeO
x/Al
2O
3=0.01~1.0;
SiO
2/Al
2O
3=0.001~10;
P
2O
5/Al
2O
3=0.5~15;
H
2O/Al
2O
3=10~100;
R/Al
2O
3=1~10; R is the mixture of one or more template agent.
In addition, in above-mentioned reaction, crystallization pressure is its self-generated pressure or nitrogen, air or the inert gas etc. that charge into 0.01~1MPa.
Below by embodiment in detail the present invention is described in detail.
Embodiment 1 TiAPSO-17
The 6.88g boehmite (is contained Al
2O
374.2%) powder is put into 100ml stainless steel synthesis reactor, and [11.53g phosphoric acid (contains H in adding
3PO
485%)+and the 14ml deionized water], after waiting to stir, add the 1.2g Ludox and (contain SiO
225%), continue to stir 10 minutes, under agitation add 1.7ml tetrabutyl titanate ester and deionized water 17ml, add cyclohexylamine 7.5ml then, stir 15 minutes until mixing, its gel consists of: 1.5C
6H
11NH
2: 0.1SiO
2: Al
2O
3: P
2O
5: 0.05TiO
2: 39H
2O.
With synthesis reactor sealing, in 120 ℃ of baking ovens aging 5 hours, crystallization 24 hours under 200 ℃ of conditions again.Take out synthesis reactor, put into cold water and be cooled to room temperature, solid is separated with mother liquor, spend deionised water to neutral, 100 ℃ dry down, be TiAPSO-17 through XRD diffraction analysis product, 25 ℃ down its saturated water adsorptive value be 26.8%wt.
By analysis of chemical elements as can be known, its solid product consists of: 2.8wt.%C, 0.5wt.%N, 3.5wt.%SiO
2, 41.2wt.%Al
2O
3, 47.3wt.%P
2O
5, 2.6wt.%TiO
2, 2.1wt.%H
2O.
Comparative Examples 1
In embodiment 1, only change the 1.2g Ludox into 1.8g, all the other components and crystallization condition are constant, and product is the mixed crystal of TiAPSO-17 and TiAPSO-44 molecular sieve.
Comparative Examples 2
In embodiment 1, only change the 1.2g Ludox into 3.6g, all the other components and crystallization condition are constant, and product is the TiAPSO-44 molecular sieve.
Embodiment 2 VAPSO-17
The false boehmite of 7.06g (is contained Al
2O
372.2%) powder is put into 100ml stainless steel synthesis reactor, and [11.53g phosphoric acid (contains H in adding
3PO
485%)+and the 14ml deionized water], after waiting to stir, add the 1.2g Ludox and (contain SiO
225%), continues to stir 10 minutes, under agitation add 0.59gNH
4VO
3With the 17ml deionized water, add cyclohexylamine 7.5ml then, stir 15 minutes until mixing, its gel consists of: 1.5C
6H
11NH
2: 0.1SiO
2: Al
2O
3: P
2O
5: 0.05V
2O
5: 39H
2O.
Seal after synthesis reactor being charged into the nitrogen of 0.4Mpa, in 120 ℃ of baking ovens aging 5 hours, crystallization 24 hours under 200 ℃ of conditions again.Take out synthesis reactor, put into cold water and be cooled to room temperature, solid is separated with mother liquor, spend deionised water to neutral, 100 ℃ dry down, be VAPSO-17 through XRD diffraction analysis product, 25 ℃ down its saturated water adsorptive value be 24.5%wt.
Embodiment 3 CrAPSO-17
In embodiment 2, with 0.59g NH
4VO
3Change 2.00g Cr (NO into
3)
39H
2O, all the other components and crystallization condition are constant, and product is the CrAPSO-17 molecular sieve through XRD analysis, and 25 ℃ of following its saturated water adsorptive values are 25.8wt%.
Embodiment 4 ZrAPSO-17
The 6.88g boehmite (is contained Al
2O
374.2%) powder is put into 100ml stainless steel synthesis reactor, and [11.53g phosphoric acid (contains H in adding
3PO
485%)+and the 14ml deionized water], after waiting to stir, add the 1.2g Ludox and (contain SiO
225%), continues to stir 10 minutes, under agitation add (1.07g zirconium nitrate [Zr (NO
3)
45H
2O] and the 17ml deionized water), add cyclohexylamine 7.5ml then, stir 15 minutes until mixing, its gel consists of: 1.5C
6H
11NH
2: 0.1SiO
2: Al
2O
3: P
2O
5: 0.05ZrO
2: 39H
2O.
With synthesis reactor sealing, in 120 ℃ of baking ovens aging 5 hours, crystallization 24 hours under 200 ℃ of conditions again.Take out synthesis reactor, put into cold water and be cooled to room temperature, solid is separated with mother liquor, spend deionised water to neutral, 100 ℃ dry down, be ZrAPSO-17 through XRD diffraction analysis product, 25 ℃ down its saturated water adsorptive value be 24.1%wt.
Embodiment 5 MgAPSO-17
In embodiment 4, with 1.07gZr (NO
3)
45H
2O changes 1.08gMg (CH into
3COO)
24H
2O, and with 8.1ml triethylamine replacement cyclohexylamine, all the other components and crystallization condition are constant, product is the MgAPSO-17 molecular sieve through XRD analysis, 25 ℃ of following its saturated water adsorptive values are 23.1wt%.
Embodiment 6 CaAPSO-17
In embodiment 4, with 1.07gZr (NO
3)
45H
2O changes 1.19g Ca (NO into
3)
24H
2O, and with 6.9ml diethylamine replacement cyclohexylamine, all the other components and crystallization condition are constant, product is the CaAPSO-17 molecular sieve through XRD analysis, 25 ℃ of following its saturated water adsorptive values are 20.5wt%.
Embodiment 7 SrAPSO-17
In embodiment 4, with 1.07gZr (NO
3)
45H
2O changes 1.06g Sr (NO into
3)
2, and with 6.1ml isopropylamine replacement cyclohexylamine, all the other components and crystallization condition are constant, and product is the SrAPSO-17 molecular sieve through XRD analysis, 25 ℃ of following its saturated water adsorptive values are 25.1wt%.
Embodiment 8 BaAPSO-17
In embodiment 4, with 1.07gZr (NO
3)
45H
2O changes 1.31g Ba (NO into
3)
2, and with 8.7ml tripropyl amine (TPA) replacement cyclohexylamine, all the other components and crystallization condition are constant, and product is the BaAPSO-17 molecular sieve through XRD analysis, 25 ℃ of following its saturated water adsorptive values are 24.3wt%.
Embodiment 9 FAPSO-17
In embodiment 4, with 1.07gZr (NO
3)
45H
2O changes 1.02g Fe (NO into
3)
29H
2O, and with 8.2ml di-n-propylamine replacement cyclohexylamine, all the other components and crystallization condition are constant, product is the FAPSO-17 molecular sieve through XRD analysis, 25 ℃ of following its saturated water adsorptive values are 25.8wt%.
Embodiment 10 CoAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 1.25gCo (CH into
3COO)
44H
2O, and with 7.4ml tetramethyl oxyammonia replacement cyclohexylamine, all the other components and operating condition are constant, products therefrom is the CoAPSO-17 molecular sieve through the XRD diffraction analysis, its saturated water adsorptive value is 24.5%wt.
Embodiment 11 NiAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 1.48g Ni (NO into
3)
26H
2O, and do the template agent with 4.2ml cyclohexylamine and 2.6ml diethylamine, all the other components and operating condition are constant, and products therefrom is the NiAPSO-17 molecular sieve through the XRD diffraction analysis, and its saturated water adsorptive value is 26.8%wt.
Embodiment 12 CuAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 1.21g Cu (NO into
3)
23H
2O, and do the template agent with 3.7ml triethylamine and 3.4ml diethylamine, all the other components and operating condition are constant, and products therefrom is the CuAPSO-17 molecular sieve through the XRD diffraction analysis, and its saturated water adsorptive value is 22.5%wt.
Embodiment 13 ZnAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 1.11gZn (CH into
3COO)
22H
2O, and do the template agent with 3.1ml triethylamine and 3.5ml n-propylamine, all the other components and operating condition are constant, and products therefrom is the ZnAPSO-17 molecular sieve through the XRD diffraction analysis, and its saturated water adsorptive value is 25.3%wt.
Embodiment 14 MnAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 1.25gMn (CH into
3COO)
44H
2O charges into 0.1MPa nitrogen after raw material added synthesis reactor sealing, and all the other components and operating condition are constant, and products therefrom is the MnAPSO-17 molecular sieve through the XRD diffraction analysis, 25 ℃ down its saturated water adsorptive values be 23.1%wt
Embodiment 15 MoAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 0.89g (NH into
4)
6Mo
7O
244H
2O charges into the 0.1Mpa air after raw material added synthesis reactor sealing, and all the other components and operating condition are constant, and products therefrom is the MoAPSO-17 molecular sieve through the XRD diffraction analysis, 25 ℃ down its saturated water adsorptive values be 21.1%
Embodiment 16 LaAPSO-17
In embodiment 4, only with 1.07gZr (NO
3)
45H
2O changes 1.85g La (NO into
3)
3NH
2O (contains La
2O
345%), charge into the 0.8Mpa air after raw material added synthesis reactor sealing, all the other components and operating condition are constant, and products therefrom is the LaAPSO-17 molecular sieve through the XRD diffraction analysis, 25 ℃ down its saturated water adsorptive values be 25.6%wt
Embodiment 17 catalytic reactions
The roasting in 550 ℃ of air of MeAPSO-17 molecular screen primary powder among the embodiment 1~16 was obtained the MeAPSO-17 molecular sieve catalyst in 5 hours, and at 450 ℃, the methyl alcohol weight space velocity is 2h
-1The time, its MTO reaction result is methanol conversion 100%, C
2 =~C
3 =Selectivity is as shown in table 1.
Table 1 sample C
2 =~C
3 =(wt%) TiAPSO-17 56.84VAPSO-17 56.28CrAPSO-17 53.44ZrrAPSO-17 53.32MgAPSO-17 52.55CaAPSO-17 52.10SrAPSO-17 48.55BaAPSO-17 48.47FeAPSO-17 46.78CoAPSO-17 48.65NiAPSO-17 55.62CuAPSO-17 47.87ZnAPSO-17 57.84MnAPSO-17 49.81MoAPSO-17 46.24LaAPSO-7 51.22
Embodiment 18 TiAPO-17
The 6.88g boehmite (is contained Al
2O
374.2%) powder is put into 100ml stainless steel synthesis reactor, and [11.53g phosphoric acid (contains H in adding
3PO
485%)+the 14ml deionized water], after waiting to stir, add tetrabutyl titanate ester 3.4ml, continue to stir 10 minutes, under agitation add deionized water 17ml, add cyclohexylamine 7.5ml then, stir 15 minutes until mixing, its gel consists of: 1.5C
6H
11NH
2: Al
2O
3: P
2O
5: 0.1TiO
2: 39H
2O.
With synthesis reactor sealing, in 120 ℃ of baking ovens aging 5 hours, crystallization 24 hours under 200 ℃ of conditions again.Take out synthesis reactor, put into cold water and be cooled to room temperature, solid is separated with mother liquor, spend deionised water to neutral, 100 ℃ dry down, be TiAPO-17 through XRD diffraction analysis product, 25 ℃ down its saturated water adsorptive value be 24.0%wt.
By analysis of chemical elements as can be known, its solid product consists of: 2.6wt.%C, 0.5wt.%N, 42.9wt.%Al
2O
3, 48.0wt.%P
2O
5, 3.1wt.%TiO
2, 2.9wt.%H
2O).
Embodiment 19 ZrAPO-17
The false boehmite of 7.06g (is contained Al
2O
372.2%) powder is put into 100ml stainless steel synthesis reactor, and [11.53g phosphoric acid (contains H in adding
3PO
485%)+and the 14ml deionized water], after waiting to stir, under agitation add (2.15g zirconium nitrate [Zr (NO
3)
45H
2O] and the 17ml deionized water), add cyclohexylamine 7.5ml then, stir 15 minutes until mixing, its gel consists of: 1.5C
6H
11NH
2: Al
2O
3: P
2O
5: 0.1ZrO
2: 39H
2O.
With the synthesis reactor sealing, crystallization is 24 hours in 200 ℃ of baking ovens.Take out synthesis reactor, put into cold water and be cooled to room temperature, solid is separated with mother liquor, spend deionised water to neutral, 100 ℃ dry down, be ZrAPSO-17 through XRD diffraction analysis product, 25 ℃ down its saturated water adsorptive value be 23.5%wt.
Embodiment 20 CoAPO-17
In embodiment 19, only with (2.15g zirconium nitrate [Zr (NO
3)
45H
2O] and the 17ml deionized water) change (2.50g cobalt acetate [Co (CH into
3COO)
44H
2O]+the 17ml deionized water), all the other components and operating condition are constant, and products therefrom is the CoAPO-17 molecular sieve through the XRD diffraction analysis, and 25 ℃ of following its saturated water adsorptive values are 23.1%wt.
Embodiment 21 MnAPO-17
In embodiment 19, only with (2.15g zirconium nitrate [Zr (NO
3)
45H
2O] and the 17ml deionized water) change (2.50g manganese acetate [Mn (CH into
3COO)
44H
2O]+the 17ml deionized water), all the other components and operating condition are constant, and products therefrom is the MnAPO-17 molecular sieve through the XRD diffraction analysis, and 25 ℃ of following its saturated water adsorptive values are 22.4%wt.
Can see by the foregoing description, utilize synthetic method of the present invention, by selecting the template agent and adding the different metal compound and can synthesize the MeAPSO-17 molecular sieve.This molecule case has adsorptivity preferably, and is that low-carbon alkene reaction has higher activity and product selectivity to methanol conversion.
Claims (13)
1. a MeAPSO-17 molecular sieve is characterized in that the moisture-free basis chemical composition can be expressed as: mRnMe (Si
xAl
yP
z) O
2, wherein R is a kind of template agent that is present in the microporous molecular sieve, m is every mole of (Si
xAl
yP
z) O
2The molal quantity of middle R, and m=0.03~2.00; X, y, z are respectively the molar fraction of Si, Al, P atom, and satisfy x+y+z=1, simultaneously, and x=0.001~0.60, y=0.01~0.60, z=0.01~0.60; Me is the metal heteroatom that is present in the molecular sieve, and n is every mole of (Si
xAl
yP
z) O
2The molal quantity of middle Me, n=0.01~0.60.
2. according to the described MeAPSO-17 molecular sieve of claim 1, it is characterized in that metallic atom to small part with MeO
2 qTetrahedroid becomes framework of molecular sieve to be present in the molecular sieve.
3. according to the described MeAPSO-17 molecular sieve of claim 1, the metallic atom that it is characterized in that being present in the molecular sieve is a kind of or several arbitrarily in titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, magnesium, calcium, strontium, barium and the lanthanum.
4. the method for a synthetic MeAPSO-17 molecular sieve is characterized in that being undertaken by following process:
(1) in proportion silicon source material, aluminium source material, phosphorus source material, metallic compound, template agent and water are under agitation mixed, get initial gel mixture;
(2) with sealing in the initial gel mixture material immigration stainless steel synthesis reactor, be 2-10 hour, be warmed up to 185~205 ℃ again at 100~130 ℃ of constant temperature, constant temperature 20-160 hour, complete until crystallization;
(3) solid crystallized product is separated with mother liquor, wash to neutrality, behind 80-100 ℃ of air drying, obtain the MeAPSO-17 molecular screen primary powder with deionized water;
(4) molecular screen primary powder is no less than 3 hours 300-700 ℃ of following bubbling air roasting, promptly obtains adsorbent and the catalyst of molecular sieve MeAPSO-17.
5. according to the method for the described MeAPSO-17 molecular sieve of claim 4, it is characterized in that employed each raw material proportioning (by the oxide molecule ratio) is:
MeO
x/Al
2O
3=0.01~1.0;
SiO
2/Al
2O
3=0.001~10;
P
2O
5/Al
2O
3=0.5~15;
H
2O/Al
2O
3=10~100;
R/Al
2O
3=1~10; R is the mixture of one or more template agent.
6. according to the method for the described synthetic MeAPSO-17 molecular sieve of claim 4, it is characterized in that employed metallic compound is a kind of in the oxide, oxychlorination thing of titanium, vanadium, chromium, manganese, iron, cobalt, nickel, copper, zinc, zirconium, molybdenum, magnesium, calcium, strontium, barium and lanthanum or inorganic, the acylate or several mixture arbitrarily.
7. according to the method for the described synthetic MeAPSO-17 molecular sieve of claim 4, it is characterized in that used silicon source is a kind of or any several mixture in Ludox, waterglass, active silica or the positive esters of silicon acis;
8. according to the method for the described synthetic MeAPSO-17 molecular sieve of claim 4, it is characterized in that used aluminium source is a kind of or any several mixture in aluminium salt, aluminate, activated alumina, aluminum alkoxide, false boehmite or the boehmite;
9. according to the method for the described synthetic MeAPSO-17 molecular sieve of claim 4, it is characterized in that used phosphorus source is a kind of or any several mixture in orthophosphoric acid, phosphate, organic phosphorus compound or the phosphorous oxides;
10. according to the method for the described synthetic MeAPSO-17 molecular sieve of claim 4, it is characterized in that employed template agent is a kind of of cyclohexylamine, triethylamine, diethylamine, n-propylamine, isopropylamine, di-n-propylamine, diisopropylamine, tripropyl amine (TPA), n-butylamine, isobutyl amine, monoethanolamine, diethanol amine, triethanolamine, tetramethyl oxyammonia, tetraethyl oxyammonia, tetrapropyl oxyammonia or tetrabutylammonium hydroxide amine and alcohols or any several mixture.
11., it is characterized in that crystallization pressure is its self-generated pressure or nitrogen, air or the inert gas etc. that charge into 0.01~MPa according to the method for the described synthetic MeAPSO-17 molecular sieve of claim 4.
12. one kind according to the described synthetic MeAPSO-17 molecular sieve of claim 1, as adsorbent.
13. one kind according to the described MeAPSO-17 molecular sieve of claim 1, as catalytic cracking, polymerization, reformation, alkylation, dealkylation, oxidation, transalkylation, isomerization, hydrogenation cyclisation, dehydrogenation and hydrogenation etc.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN99127142A CN1108867C (en) | 1999-12-29 | 1999-12-29 | MeAPSO-17 molecular sieve and its synthesizing method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN99127142A CN1108867C (en) | 1999-12-29 | 1999-12-29 | MeAPSO-17 molecular sieve and its synthesizing method |
Publications (2)
Publication Number | Publication Date |
---|---|
CN1301593A true CN1301593A (en) | 2001-07-04 |
CN1108867C CN1108867C (en) | 2003-05-21 |
Family
ID=5284741
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN99127142A Expired - Lifetime CN1108867C (en) | 1999-12-29 | 1999-12-29 | MeAPSO-17 molecular sieve and its synthesizing method |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN1108867C (en) |
Cited By (10)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102153106A (en) * | 2010-07-29 | 2011-08-17 | 兰州理工大学 | Quick reparation method for heteroatom phosphorus aluminum molecular sieve in eutectoid |
WO2013181833A1 (en) * | 2012-06-08 | 2013-12-12 | 中国科学院大连化学物理研究所 | Metal silicoaluminophosphate molecular sieve having rho skeleton structure and preparation process therefor |
CN104682938A (en) * | 2015-03-30 | 2015-06-03 | 威海远晨光电有限公司 | Light-controlled contactor |
CN107262146A (en) * | 2016-12-04 | 2017-10-20 | 中国科学院大连化学物理研究所 | One kind prepares 2,6 dimethylnaphthalene catalyst and its preparation and application |
CN107986295A (en) * | 2018-01-28 | 2018-05-04 | 江西和德瑞新材料有限公司 | A kind of siliceous molecular sieve and preparation method thereof |
CN108083974A (en) * | 2018-01-28 | 2018-05-29 | 江西和德瑞新材料有限公司 | The method of cyclohexyl hydroperoxide catalytic decomposition |
CN108117087A (en) * | 2018-01-28 | 2018-06-05 | 江西和德瑞新材料有限公司 | Siliceous molecular sieve and preparation method thereof |
CN108283934A (en) * | 2018-01-28 | 2018-07-17 | 江西和德瑞新材料有限公司 | The method of cyclohexane oxide solution processing |
CN108329191A (en) * | 2018-01-28 | 2018-07-27 | 江西和德瑞新材料有限公司 | A kind of method of cyclohexane oxide solution processing |
CN108329190A (en) * | 2018-01-28 | 2018-07-27 | 江西和德瑞新材料有限公司 | A kind of method of cyclohexyl hydroperoxide catalytic decomposition |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4440871A (en) * | 1982-07-26 | 1984-04-03 | Union Carbide Corporation | Crystalline silicoaluminophosphates |
US5962762A (en) * | 1995-12-13 | 1999-10-05 | Sun; Hsian-Ning | Use of transition metal containing small pore molecular sieve catalysts in oxygenate conversion |
CN1076219C (en) * | 1996-08-02 | 2001-12-19 | 中国科学院大连化学物理研究所 | Silicon phosphorus aluminium molecular sieve containing alkaline earth metal and its synthesis |
-
1999
- 1999-12-29 CN CN99127142A patent/CN1108867C/en not_active Expired - Lifetime
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102153106A (en) * | 2010-07-29 | 2011-08-17 | 兰州理工大学 | Quick reparation method for heteroatom phosphorus aluminum molecular sieve in eutectoid |
CN102153106B (en) * | 2010-07-29 | 2012-12-12 | 兰州理工大学 | Quick reparation method for heteroatom phosphorus aluminum molecular sieve in eutectoid |
WO2013181833A1 (en) * | 2012-06-08 | 2013-12-12 | 中国科学院大连化学物理研究所 | Metal silicoaluminophosphate molecular sieve having rho skeleton structure and preparation process therefor |
US9499409B2 (en) | 2012-06-08 | 2016-11-22 | Dalian Institute Of Chemical Physics, Chinese Academy Of Sciences | Metal silicoaluminophosphate molecular sieve with RHO framework structure, and method for preparing the same |
EA028185B1 (en) * | 2012-06-08 | 2017-10-31 | Чайниз Академи Оф Сайэнсиз | Metal silicoaluminophosphate molecular sieve with rho framework structure and method for preparing the same |
CN104682938A (en) * | 2015-03-30 | 2015-06-03 | 威海远晨光电有限公司 | Light-controlled contactor |
CN107262146A (en) * | 2016-12-04 | 2017-10-20 | 中国科学院大连化学物理研究所 | One kind prepares 2,6 dimethylnaphthalene catalyst and its preparation and application |
CN108083974A (en) * | 2018-01-28 | 2018-05-29 | 江西和德瑞新材料有限公司 | The method of cyclohexyl hydroperoxide catalytic decomposition |
CN107986295A (en) * | 2018-01-28 | 2018-05-04 | 江西和德瑞新材料有限公司 | A kind of siliceous molecular sieve and preparation method thereof |
CN108117087A (en) * | 2018-01-28 | 2018-06-05 | 江西和德瑞新材料有限公司 | Siliceous molecular sieve and preparation method thereof |
CN108283934A (en) * | 2018-01-28 | 2018-07-17 | 江西和德瑞新材料有限公司 | The method of cyclohexane oxide solution processing |
CN108329191A (en) * | 2018-01-28 | 2018-07-27 | 江西和德瑞新材料有限公司 | A kind of method of cyclohexane oxide solution processing |
CN108329190A (en) * | 2018-01-28 | 2018-07-27 | 江西和德瑞新材料有限公司 | A kind of method of cyclohexyl hydroperoxide catalytic decomposition |
CN108083974B (en) * | 2018-01-28 | 2020-03-27 | 江西科因润滑材料有限公司 | Method for catalytic decomposition of cyclohexyl hydroperoxide |
CN108283934B (en) * | 2018-01-28 | 2020-03-27 | 江西科因润滑材料有限公司 | Method for processing cyclohexane oxidation liquid |
CN107986295B (en) * | 2018-01-28 | 2020-03-27 | 江西科因润滑材料有限公司 | Silicon-containing molecular sieve and preparation method thereof |
CN108117087B (en) * | 2018-01-28 | 2020-03-27 | 江西科因润滑材料有限公司 | Silicon-containing molecular sieve and preparation method thereof |
Also Published As
Publication number | Publication date |
---|---|
CN1108867C (en) | 2003-05-21 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN88101443A (en) | The preparation method of aromatic hydrocarbon | |
EP0903178B1 (en) | A pentasil-type molecular sieve containing composition, its preparation method and use | |
CN1037334C (en) | Synthesis silicon phosphorus aluminium molecular sieve and equipment using triethylamine as mould agent | |
CN1950321A (en) | Process for preparing carboxylic acids and derivatives thereof | |
CN1108867C (en) | MeAPSO-17 molecular sieve and its synthesizing method | |
CN101367530B (en) | Metal silicon-aluminum phosphate molecular sieve with AFO structure and synthesis method thereof | |
US9480975B2 (en) | Catalyst for catalytic cracking in a fluidized bed | |
CN1048429C (en) | Method of synthesizing aluminosilico-phosphate molecular sieve using double template agent | |
CN100448537C (en) | Catalyst for chloromethane conversion to produce low carbon olefin and its uses | |
CN104437613A (en) | Binderless ZSM-5/beta symbiotic molecular sieve catalyst and preparation method thereof | |
CN1901993A (en) | Catalyst, process for preparing the catalyst and process for producing lower hydrocarbon with the catalyst | |
CN1724366A (en) | Method for manufacturing zeolite and method for manufacturing epsilon-caprolatam | |
CN1132698C (en) | MeAPSO-44 molecular sieve and its synthesizing method | |
CN1195679C (en) | Silicon-aluminium phosphate molecular sieve and its preparing process | |
CN1182034C (en) | Method for preparing aluminium silicophosphate molecular sieve | |
CN1087292A (en) | A kind of is the synthesized silicon phosphor aluminum molecular sieve and the preparation thereof of template with the triethylamine | |
JP6798282B2 (en) | Manufacturing method of AEI type zeolite | |
CN1108869C (en) | MeAPSO-35 molecular sieve and its synthesizing method | |
CN102627286A (en) | Method for manufacturing zeolite and method for manufacturing epsilon-caprolatam | |
CN114572997B (en) | Mordenite molecular sieve, preparation method and application | |
CA2075166A1 (en) | Zeolite-type material | |
CN1108868C (en) | MeAPSO-18 molecular sieve and its synthesizing method | |
CN1111091C (en) | ZrAPSO-34 molecular sieve and its synthsizing method | |
CN104437612A (en) | Binderless ZSM-5/beta co-crystallized molecular sieve catalyst and preparation method thereof | |
CN1076219C (en) | Silicon phosphorus aluminium molecular sieve containing alkaline earth metal and its synthesis |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C06 | Publication | ||
PB01 | Publication | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20030521 |