Method for synthesizing nano SAPO-34 molecular sieve, and SAPO-34 molecular sieve catalyst and application thereof
10822244 ยท 2020-11-03
Assignee
Inventors
- Pengfei Wu (Dalian, CN)
- Miao Yang (Dalian, CN)
- Peng Tian (Dalian, CN)
- Zhongmin Liu (Dalian, CN)
- Linying Wang (Dalian, CN)
- Lin Liu (Dalian, CN)
Cpc classification
B01J29/85
PERFORMING OPERATIONS; TRANSPORTING
B01J37/0018
PERFORMING OPERATIONS; TRANSPORTING
C01B37/08
CHEMISTRY; METALLURGY
International classification
B01J29/85
PERFORMING OPERATIONS; TRANSPORTING
B01J37/00
PERFORMING OPERATIONS; TRANSPORTING
Abstract
A method for synthesizing a nano SAPO-34 molecular sieve, and an SAPO-34 molecular sieve catalyst and application thereof. A nano SAPO-34 molecular sieve is synthesized by adding a microporous templating agent and a templating agent having a functionalized organic silane to hydrothermal synthesis. The nano SAPO-34 molecular sieve is calcined to obtain a nano SAPO-34 molecular sieve catalyst. The catalyst can be used in a reaction for preparing low-carbon olefin from an oxygen-containing compound. The nano SAPO-34 molecular sieve obtained by this method has a pure CHA crystal phase. Moreover, the nano SAPO-34 molecular sieve catalyst obtained by this method has good catalytic performance in a MTO reaction, the service life of the catalyst is significantly prolonged, and the selectivity of the low-carbon olefin is improved.
Claims
1. A method for synthesizing nano SAPO-34 molecular sieve, the method comprising: synthesizing the nano SAPO-34 molecular sieve by hydrothermal method in the presence of a functionalized organosilane, the functionalized organosilane having the structure shown in Formula I: ##STR00003## wherein n is an integer ranging from 1 to 16; R.sup.1 is selected from C.sub.110 alkyl group; R.sup.2 is selected from C.sub.16 alkyl group; R.sup.3 is selected from diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl group; x is an integer ranging from 0 to 2, y is an integer ranging from 1 to 3, and x+y=3.
2. A method for preparing a SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 1 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
3. The method according to claim 1, wherein in the Formula I, n is an integer ranging from 3 to 8; R.sup.1 and R.sup.2 are each independently selected from C.sub.14 alkyl group; R.sup.3 is selected from piperazinyl, pyridyl or morpholinyl group.
4. A method for preparing a SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 3 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
5. The method according to claim 1, wherein the method comprises the following steps: a) dissolving the functionalized organosilane in water, and then adding sequentially an aluminum source, a phosphorus source, an organic amine and an additional silicon source to obtain a mixture with the following molar ratio: SiO.sub.2:P.sub.2O.sub.5:Al.sub.2O.sub.3:organic amine:H.sub.2O=0.21.2:0.51.5:0.61.4:1.55.5:50200; b) crystallizing the mixture obtained from step a) for a crystallization time in a range from 0.4 to 10 days at a crystallization temperature in a range from 150 to 220 C.; c) after the crystallization of step b), separating the solid product, and washing and drying it to obtain the nano SAPO-34 molecular sieve.
6. The method according to claim 5, wherein the molar ratio of the functionalized organosilane to the additional silicon source in the mixture obtained from step a) is 155:10, based on the molar number of SiO.sub.2.
7. A method for preparing SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 6 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
8. The method according to claim 5, wherein in step a), the phosphorus source is one or more selected from orthophosphoric acid, metaphosphoric acid, phosphate and phosphite; the aluminum source is one or more selected from aluminum salt, active alumina, alkoxy aluminum and metakaolin; the additional silicon source is one or more selected from silica sol, active silica, orthosilicate and metakaolin.
9. A method for preparing SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 8 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
10. The method according to claim 5, wherein in step a), the organic amine is one or more selected from triethylamine, tetraethylammonium hydroxide, morpholine, diethylamine, di-n-propylamine and diisopropylamine.
11. A method for preparing SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 10 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
12. The method according to claim 5, wherein in step a), the organic amine is triethylamine.
13. A method for preparing SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 12 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
14. The method according to claim 5, wherein in step b), the crystallization time is in a range from 1 to 7 days.
15. A method for preparing SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 14 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
16. A method for preparing a SAPO-34 molecular sieve catalyst, comprising calcining the nano SAPO-34 molecular sieve synthesized by the method according to claim 5 in air at a temperature in a range from 400 to 700 C. to obtain the SAPO-34 molecular sieve catalyst.
Description
BRIEF DESCRIPTION OF THE FIGURES
(1)
(2)
(3)
DETAILED DESCRIPTION
(4) According to one aspect, the present application provides a method for synthesizing nano SAPO-34 molecular sieve by hydrothermal method with assistance of a functionalized organosilane. The functions of the functionalized organosilane in the synthesis are at least in the following three aspects: 1) as a crystal growth inhibitor to reduce crystal size; 2) as an organic silicon source; 3) the functional groups of the functionalized organosilane have partly a structure-directing effect to inhibit the SAPO-18 eutectic crystal produced by using such as triethylamine as a microporous template, and thus the nano SAPO-34 molecular sieve with a pure CHA crystal phase is successfully synthesized.
(5) In the present invention, the obtained nano SAPO-34 molecular sieves are usually an aggregate of nanoparticles.
(6) In the present invention, the functionalized organosilane is selected from at least one of the alkoxy organosilane compounds containing diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl groups. Among them, the alkoxy organosilane may generally be regarded as an organosilicon compound composed of silicon atoms directly connected with 14 alkoxy groups. The diethylamino group is a group obtained by losing hydrogen atom on the nitrogen atom in diethylamine molecule. The triethylamino group is a group obtained by losing hydrogen atom on the nitrogen atom in triethylamine molecule. The piperazinyl group is a group obtained by losing hydrogen atom on a nitrogen atom in the six-membered cyclic piperazine molecule. The pyridyl group is a group obtained by losing hydrogen atom on the nitrogen atom or any carbon atom in the six-membered cyclic piperazine molecule. The morpholinyl group is a group obtained by losing hydrogen atom on the nitrogen atom or any carbon atom in the six-membered cyclic morpholine molecule.
(7) Preferably, the functionalized organosilane has the structure shown in Formula I:
(8) ##STR00002##
(9) wherein n is an integer of 116; R.sup.1 is a C.sub.110 alkyl group; R.sup.2 is a C.sub.16 alkyl group; R.sup.3 is a diethylamino, triethylamino, piperazinyl, pyridyl or morpholinyl group; x is an integer of 02, y is an integer of 13, and x+y=3. More preferably, n is an integer of 38; R.sup.1 and R.sup.2 are each independently a C.sub.14 alkyl group; R.sup.3 is a piperazinyl, pyridyl or morpholinyl group.
(10) In the present invention, the alkyl group is a group formed by losing any hydrogen atom in any linear or branched saturated alkane molecule.
(11) In the present invention, preferably, the method for synthesizing nano SAPO-34 molecular sieve comprises the following synthetic steps:
(12) a) dissolving the functionalized organosilane in water, and then adding sequentially an aluminum source, a phosphorus source, an organic amine and an additional silicon source (i.e. organic silicon source or inorganic silicon source) to obtain a mixture with the following molar ratio (the addition amount of the functionalized organosilane and the additional silicon source is based on the molar number of SiO.sub.2, the addition amount of the phosphorus source is based on the molar number of P.sub.2O.sub.5, and the addition amount of the aluminum source is based on the molar number of Al.sub.2O.sub.3):
(13) SiO.sub.2:P.sub.2O.sub.5:Al.sub.2O.sub.3:organic amine:H.sub.2O=0.21.2:0.51.5:0.61.4:1.55.5:50200;
(14) b) crystallizing the mixture obtained from step a) for 0.410 days at 150220 C.;
(15) c) after the crystallization of step b) is completed, separating the solid product, and washing and drying it to obtain the nano SAPO-34 molecular sieve.
(16) The above-described method may be carried out in a conventional reactor for hydrothermally synthesizing molecular sieves, such as a crystallization reactor.
(17) Preferably, in the mixture obtained from step a), the molar ratio of the functionalized organosilane to the additional silicon source (functionalized organosilane: additional silicon source) is 155:10, based on the molar number of SiO.sub.2. More preferably, the functionalized organosilane: additional silicon source is 115:3.
(18) Preferably, in step a), the inorganic phosphorus compound is selected from at least one of orthophosphoric acid, metaphosphoric acid, phosphate and phosphite.
(19) Preferably, in step a), the aluminum source is selected from at least one of aluminum isopropoxide, pseudoboehmite and aluminum hydroxide.
(20) Preferably, in step a), the additional silicon source is selected from at least one of silica sol, active silica, orthosilicate and metakaolin.
(21) Preferably, in step a), the organic amine is one or more selected from triethylamine, tetraethylammonium hydroxide, morpholine, diethylamine, di-n-propylamine and diisopropylamine. More preferably, in step a), the organic amine is selected from triethylamine (abbreviated as TEA).
(22) Preferably, in step b), the time for the crystallization is 17 days.
(23) As a preferred embodiment, the method for synthesizing nano SAPO-34 molecular sieve comprises the following steps:
(24) 1) dissolving the functionalized organosilane in water and stirring at room temperature for 424 hours;
(25) 2) adding subsequently an aluminum source, a phosphorus source, an organic amine and an additional silicon source to the solution from step 1) and stirring at room temperature for 124 hours, with the molar ratio of respective component in the mixed solution being as follows: (0.21.2) SiO.sub.2:(0.51.5) P.sub.2O.sub.5:(0.61.4) Al.sub.2O.sub.3:(1.55.5) organic amine:(50200) H.sub.2O, wherein the molar ratio of the functionalized organosilane to the additional silicon source is 115:3;
(26) 3) crystallizing the mixed solution of step 2) for 0.410 days at 150220 C.;
(27) 4) after the crystallization of step 3), separating the solid product by centrifugation, washing it with deionized water to neutral, and drying it in air at 120 C. to obtain the nano SAPO-34 molecular sieve raw powder.
(28) According to another aspect, the present application provides a SAPO-34 molecular sieve catalyst (or acid catalyst), wherein the SAPO-34 molecular sieve catalyst is obtained by calcining the nano SAPO-34 molecular sieve synthesized according to any of the above-described methods in air at 400700 C.
(29) According to yet another aspect, the present application provides the application of the SAPO-34 molecular sieve catalyst in the conversion of oxygenated compounds to olefins.
EXAMPLES
(30) Hereinafter, the present application is illustrated in detail by way of Examples, but the present application is not limited to these Examples.
(31) Unless specially stated otherwise, the test conditions in the present application are as follows:
(32) Elemental composition was determined on Magix-601 type X-ray fluorescence analyzer (XRF) (Philips company).
(33) X-ray powder diffraction phase analysis (XRD) was conducted on X'Pert PRO type X-ray diffractometer from PANalytical company of the Netherlands, Cu target, K radiation source (=0.15418 nm), voltage 40 KV, current 40 mA.
(34) SEM morphology was analyzed on SU8020 type scanning electron microscope from the scientific instrument factory of the Chinese Academy of Sciences.
(35) N.sub.2 physical adsorption analysis was determined on Micromeritics ASAP 2020 type physical adsorption analyzer from Mike company of USA.
(36) The functionalized organosilane and n-octyl trimethoxysilane used in the Examples were purchased from Shanghai Dibai Chemical Technology Co., Ltd. Octadecyl dimethyl trimethoxysilyl propyl ammonium chloride was purchased from Sigma Aldridge (Shanghai) Co., Ltd. As a nonrestrictive example, in Formula I, R.sup.1 is methyl; R.sup.2 is methyl; R.sup.3 is any one of piperazinyl, pyridyl and morpholinyl groups; x=1; y=2; n=38; and the functionalized organosilane with R.sup.3 being piperazinyl group is abbreviated as PiSi-n; the functionalized organosilane with R.sup.3 being pyridyl group is abbreviated as BiSi-n; the functionalized organosilane with R.sup.3 being morpholinyl group is abbreviated as MoSi-n, wherein the n takes the value of corresponding n. For example, PiSi-3 denotes the functionalized organosilane compound with a chemical structure of n=3, R.sup.1 is methyl, R.sup.2 is methyl, R.sup.3 is piperazinyl, x=1 and y=2 in Formula I.
Example 1
(37) The molar ratio of respective raw materials, the crystallization condition and the elemental composition are shown in Table 1. The specific batching process is as follows:
(38) 9.28 g PiSi-3 and 71.40 g deionized water were mixed and stirred for 1 hour, then 135.64 g pseudoboehmite (72.5% Al.sub.2O.sub.3, mass percentage content), 34.58 g phosphoric acid (85% H.sub.3PO.sub.4, mass percentage content), 20.24 g triethylamine and 8.33 g tetraethyl orthosilicate were added sequentially, followed by being stirred and aged for 24 hours. Subsequently, the gel mixture was transferred into a stainless steel reactor. The molar ratio of respective component in the synthesis system is 0.8 SiO.sub.2:1.5P.sub.2O.sub.5:0.8 Al.sub.2O.sub.3:2 TEA:80 H.sub.2O, and the molar ratio of PiSi-3 to tetraethyl orthosilicate is 1:1.
(39) After the reactor was put into an oven, the programmed temperature was raised to 200 C., and the static crystallization was carried out for 48 h. After the reaction, the solid product was centrifuged, washed repeatedly with deionized water, and dried in air at 120 C. to obtain the nano SAPO-34 molecular sieve sample.
(40) The morphology of the obtained sample was characterized by scanning electron microscopy. The electron microscopic photograph of the sample is shown in
(41) The elemental composition of the obtained sample was analyzed by XRF. The results are shown in Table 1.
Comparative Example 1
(42) The batching proportion and synthesis process were the same as in Example 1, but no piperazine-based organosilane PiSi-3 was added, and the piperazine-based organosilane PiSi-3 in Example 1 was replaced by tetraethyl orthosilicate with SiO.sub.2 of the same molar number.
(43) The morphology of the sample obtained in Comparative Example 1 was characterized by scanning electron microscopy. The electron microscopic photograph of the sample is shown in
(44) The XRD diffraction pattern of the raw powder of the sample in Comparative Example 1 is also shown in
Comparative Example 2
(45) The batching proportion and synthesis process were the same as in Example 1, but no piperazine-based organosilane PiSi-3 was added, and the piperazine-based organosilane PiSi-3 in Example 1 was replaced by a quaternary ammonium surfactant of octadecyl dimethyl trimethoxysilyl propyl ammonium chloride (TPOAC) with SiO.sub.2 of the same molar number.
(46) The XRD diffraction pattern of the raw powder of the sample in Comparative Example 2 is shown in
Comparative Example 3
(47) The batching proportion and synthesis process were the same as in Example 1, but no piperazine-based organosilane PiSi-3 was added, and the piperazine-based organosilane PiSi-3 in Example 1 was replaced by n-octyl trimethoxysilane, which has no organic functional groups, with P.sub.2O.sub.5 of the same molar number.
(48) The XRD diffraction pattern of the raw powder of the sample in Comparative Example 3 is shown in
Examples 212
(49) The specific batching proportions and crystallization conditions are shown in Table 1, and the specific batching processes are the same as in Example 1.
(50) The results of XRD analysis for the samples obtained in Examples 212 are similar to those in table 2, that is, the positions and shapes of the peaks are the same, and the relative peak intensities of the peaks fluctuate within a range of 10% according to the variation in synthetic condition, indicating that the synthesized products have the characteristics of SAPO-34 structure.
(51) The XRF elemental compositions of the samples in Examples 212 were analyzed, and the results are shown in Table 1.
(52) The morphologies of the samples in Examples 212 were analyzed by scanning electron microscopy, and the obtained electron microscopic photographs are similar to that in
(53) TABLE-US-00001 TABLE 1 Synthesis batching, crystallization condition and elemental composition of molecular sieves Additional Phosphorus Organosilane silicon source Aluminum Organic and source and and P.sub.2O.sub.5 source and amine H.sub.2O Crystal- Crystal- Exam- SiO.sub.2 molar SiO.sub.2 molar molar Al.sub.2O.sub.3 molar molar molar lization lization Elemental composition ple number number number number number number temperature time analysis result of product 1 PiSi-3 tetraethyl orthophosphoric pseudoboehmite 0.20 mol 8.0 mol 200 C. 48 h (Si.sub.0.14Al.sub.0.45P.sub.0.41)O.sub.2 0.04 mol orthosilicate acid 0.08 mol 0.04 mol 0.15 mol 2 BiSi-3 silica sol orthophosphoric aluminum 0.45 mol 5.5 mol 210 C. 60 h (Si.sub.0.15Al.sub.0.45P.sub.0.40)O.sub.2 0.02 mol 0.06 mol acid isopropoxide 0.12 mol 0.12 mol 3 MoSi-4 carbon-white orthophosphoric aluminum 0.35 mol 15.0 mol 180 C. 96 h (Si.sub.0.06Al.sub.0.48P.sub.0.46)O.sub.2 0.01 mol 0.01 mol acid isopropoxide 0.05 mol 0.06 mol 4 BiSi-7 tetraethyl orthophosphoric aluminum 0.15 mol 20.0 mol 200 C. 24 h (Si.sub.0.17Al.sub.0.45P.sub.0.38)O.sub.2 0.04 mol orthosilicate acid hydroxide 0.08 mol 0.08 mol 0.12 mol 5 PiSi-4 carbon-white metaphosphoric aluminum 0.20 mol 5.0 mol 190 C. 120 h (Si.sub.0.04Al.sub.0.55P.sub.0.41)O.sub.2 0.05 mol 0.03 mol acid hydroxide 0.10 mol 0.14 mol 6 PiSi-5 silica sol metaphosphoric pseudoboehmite 0.55 mol 10.0 mol 150 C. 168 h (Si.sub.0.08Al.sub.0.49P.sub.0.43)O.sub.2 0.01 mol 0.03 mol acid 0.08 mol 0.08 mol 7 MoSi-8 silica sol ammonium pseudoboehmite 0.20 mol 12.0 mol 210 C. 48 h (Si.sub.0.10Al.sub.0.47P.sub.0.43)O.sub.2 0.02 mol 0.04 mol hydrogen 0.12 mol phosphate 0.09 mol 8 PiSi-6 tetraethyl metaphosphoric aluminum 0.28 mol 9.0 mol 200 C. 96 h (Si.sub.0.18Al.sub.0.45P.sub.0.37)O.sub.2 0.05 mol orthosilicate acid isopropoxide 0.06 mol 0.05 mol 0.12 mol 9 MoSi-6 carbon-white Ammonium pseudoboehmite 0.35 mol 16.0 mol 220 C. 12 h (Si.sub.0.19Al.sub.0.44P.sub.0.37)O.sub.2 0.10 mol 0.02 mol dihydrogen 0.10 mol phosphate 0.12 mol 10 PiSi-3 tetraethyl Ammonium pseudoboehmite 0.40 mol 20.0 mol 200 C. 48 h (Si.sub.0.12Al.sub.0.46P.sub.0.42)O.sub.2 0.03 mol orthosilicate dihydrogen 0.12 mol 0.04 mol phosphate 0.10 mol 11 PiSi-4 silica sol orthophosphoric aluminum 0.30 mol 10.5 mol 190 C. 24 h (Si.sub.0.13Al.sub.0.48P.sub.0.39)O.sub.2 0.05 mol 0.05 mol acid hydroxide 0.10 mol 0.07 mol 12 BiSi-8 carbon-white metaphosphoric aluminum 0.50 mol 16.0 mol 160 C. 36 h (Si.sub.0.10Al.sub.0.46P.sub.0.44)O.sub.2 0.02 mol 0.04 mol acid isopropoxide 0.08 mol 0.10 mol
(54) TABLE-US-00002 TABLE 2 XRD results of sample obtained in Example 1 No. 2 d() 100*I/I.sub.0 1 9.493116 9.31665 92.35 2 12.84392 6.89261 28.9 3 13.99115 6.32991 6.72 4 15.99025 5.54277 47.72 5 17.93924 4.94473 20.31 6 20.55734 4.32053 100 7 22.18501 4.00708 6.43 8 23.05264 3.8582 6.76 9 25.16641 3.53873 23.32 10 25.85266 3.44633 25.98 11 27.61156 3.2302 4.38 12 29.48936 3.02908 3.57 13 30.5581 2.92553 41.07 14 31.15588 2.87075 20.74 15 34.45969 2.60271 8.54 16 36.22659 2.47972 3.39 17 39.63702 2.27387 3.8 18 43.40979 2.08459 5.02
(55) wherein represents the XRD diffraction angle, d represents the interplanar crystal spacing, I represents the relative diffraction peak intensity, and I.sub.0 represents the relative maximum diffraction peak intensity.
Example 13
(56) The samples obtained in Examples 14 and Comparative Example 1 were calcined in air at 600 C. for 4 hours, and then subject to N.sub.2 physical adsorption analysis. The results are shown in Table 3. From the results in Table 3, it can be seen that the samples obtained in Examples 1 to 4 have significantly increased external specific surface area and mesoporous volume, compared with the data from Comparative Example 1.
(57) TABLE-US-00003 TABLE 3 Specific surface area and pore volume of samples Specific surface area (m.sup.2/g) V.sub.micropore V.sub.mesopore.sup.b Sample S.sub.BET S.sub.micropore.sup.a S.sub.mesopore (cm.sup.3/g) (cm.sup.3/g) Comparative 572 566 6 0.24 0.01 Example 1 Example 1 577 478 99 0.22 0.17 Example 2 577 475 102 0.22 0.18 Example 3 582 493 89 0.23 0.13 Example 4 597 488 109 0.22 0.17 .sup.acalculated by t-plot method .sup.bcalculated by BJH method
(58) wherein V.sub.micropore represents the volume of micropores in material, S.sub.BET represents the BET surface area of material, S.sub.micropore represents the specific surface area of micropores in material, and S.sub.mesopore represents the specific surface area of mesopores in material
Example 14
(59) The samples obtained in Examples 14 and Comparative Example 1 were calcined in air at 600 C. for 4 hours, and then tableted and crushed to 4060 meshes. 0.3 g of each sample was charged into a fixed bed reactor and subject to MTO reaction for evaluation. The sample was activated for 1 hour at 550 C. under nitrogen, and then cooled to 450 C. for the reaction. Methanol was carried by nitrogen. The flow rate of nitrogen was 42 ml/min, and the mass hourly space velocity of methanol was 4 h.sup.1. The reaction products were analyzed by on-line gas chromatography (Varian 3800, FID detector, capillary column PoraPLOT Q-HT). The results are shown in Table 4.
(60) TABLE-US-00004 TABLE 4 Reaction results of samples for conversion of methanol to olefins Service Selectivity (mass %) Sample life (min).sup.a CH.sub.4 C.sub.2H.sub.4 C.sub.2H.sub.6 C.sub.3H.sub.6 C.sub.3H.sub.8 C.sub.2H.sub.4 + C.sub.3H.sub.6.sup.b C.sub.4-C.sub.6 Comparative 160 3.89 44.40 0.72 32.12 1.81 76.51 17.06 Example 1 Example 1 330 2.04 49.37 0.39 33.65 0.60 83.02 13.92 Example 2 300 2.24 50.15 0.46 32.93 0.67 83.07 13.54 Example 3 460 1.23 50.19 0.41 34.83 0.74 85.02 9.87 Example 4 360 2.24 49.87 0.47 32.88 0.76 82.76 13.76 .sup.aThe reaction time during which the conversion of methanol was 100%. .sup.bThe highest (ethylene + propylene) selectivity when the conversion of methanol was 100%
(61) Although the present application is disclosed with preferred embodiments as above, it does not mean that the present application is limited by them. Without departing from the inventive concept of the present application, any slight variations and modifications made by those skilled in the art who is familiar with this major by utilizing the above disclosures are all equal to the equivalent embodiments and fall into the scope of the technical solutions of the present application.