Preparation method and application of mordenite with high silica-alumina ratio
阅读说明：本技术 一种高硅铝比丝光沸石的制备方法及应用 (Preparation method and application of mordenite with high silica-alumina ratio ) 是由 裴仁彦 夏春晖 吕新新 王国建 刘骆安 王建 刘勇 王辉 于 2020-12-28 设计创作，主要内容包括：本申请公开了一种高硅铝比丝光沸石的制备方法及其应用。所述高硅铝比丝光沸石的制备方法,包含以下三个步骤：(1)将铝源、硅源、碱源、模板剂R1和水在一定条件下进行预晶化,得到高硅铝比前驱体；(2)将铝源、硅源、碱源、模板剂R2和水(或晶化后滤液)按一定比例在一定温度下搅拌陈化后制成结构导向溶胶；(3)将高硅铝比前驱体和导向溶胶按一定比例混合,水热晶化,得到高硅铝比丝光沸石。用该方法不但有效的利用了晶化后滤液,减少污染,还可以制备出硅铝比在15～50的丝光沸石,其二甲醚羰基化合成乙酸甲酯性能优异。(The application discloses a preparation method and application of mordenite with a high silica-alumina ratio. The preparation method of the mordenite with the high silica-alumina ratio comprises the following three steps: (1) pre-crystallizing an aluminum source, a silicon source, an alkali source, a template agent R1 and water under a certain condition to obtain a precursor with a high silicon-aluminum ratio; (2) stirring and aging an aluminum source, a silicon source, an alkali source, a template agent R2 and water (or filtrate after crystallization) according to a certain proportion at a certain temperature to prepare structure-oriented sol; (3) and mixing the precursor with the high silica-alumina ratio and the guiding sol according to a certain proportion, and carrying out hydrothermal crystallization to obtain the mordenite with the high silica-alumina ratio. By the method, the filtrate after crystallization is effectively utilized, pollution is reduced, mordenite with the silicon-aluminum ratio of 15-50 can be prepared, and the methyl acetate synthesized by carbonylation of dimethyl ether has excellent performance.)
1. A preparation method of mordenite with high silica-alumina ratio is characterized by comprising the following steps:
(1) pre-crystallizing a mixture I containing an aluminum source, a silicon source, an alkali source, a template agent R1 and water to obtain a silicon-aluminum precursor solution;
the mixture I comprises the following raw materials in a molar ratio:
M2O:SiO2:Al2O3:R1:H2O＝0.05～0.3:1.00:0.01～0.05:0.05～1.0:10～40；
(2) aging a mixture II containing an aluminum source, a silicon source, an alkali source, a template agent R2 and a substance A to obtain structure-oriented sol;
the molar ratio of the raw materials in the mixture II is as follows:
M2O:SiO2:Al2O3:R2:H2O＝0.05～0.4:1.00:0.02～0.05:0.05～1.0:10～40；
(3) mixing the silicon-aluminum precursor solution with the structure-oriented sol to obtain a sol mixture, and carrying out hydrothermal crystallization to obtain a crystallized filtrate and the mordenite with the high silicon-aluminum ratio;
in the step (2), the substance A comprises water and/or crystallized filtrate;
in the steps (1) and (2), the alkali source is at least one selected from hydroxides of alkali metals M in an amount of M contained therein2Calculating the mole number of O;
the aluminum source is used in an amount of Al contained therein2O3Calculating the mole number of the active carbon;
the silicon source is used as SiO contained in the silicon source2Calculating the mole number of the active carbon;
the dosage of the template agent is calculated by the mole number of the template agent;
the amount of water used is calculated as its own moles.
2. The process of claim 1, wherein the SiO of the high silica to alumina ratio mordenite is2/Al2O3The molar ratio is 30-120.
3. The method according to claim 1, wherein the substance A in the step (2) is a filtrate after crystallization in the step (3).
4. The production method according to claim 1, wherein in the step (1) and the step (2), the templating agent R1 and the templating agent R2 are independently selected from at least one of cetyltrimethylammonium bromide, dodecyltrimethylammonium bromide, tetrapropylammonium bromide, tetraethylammonium bromide, tetramethylammonium bromide, hexadecyltrimethylammonium chloride, dodecyltrimethylammonium chloride, tetrapropylammonium chloride, tetraethylammonium chloride, tetramethylammonium chloride, hexadecyltrimethylammonium hydroxide, dodecyltrimethylammonium hydroxide, tetrapropylammonium hydroxide, tetraethylammonium hydroxide, tetramethylammonium hydroxide, triethylamine, isopropylamine, diisopropylamine, triisopropylamine, n-butylamine, cyclohexylamine, caprolactam, hexamethyleneimine, heptamethyleneimine, cycloheptaneamine, and cyclopentylamine;
preferably, in step (1) and step (2), the aluminum source is independently selected from at least one of sodium aluminate, aluminum isopropoxide, aluminum hydroxide, aluminum sulfate, aluminum chloride and aluminum nitrate;
in the step (1) and the step (2), the silicon source is independently selected from at least one of white carbon black, silica sol and sodium silicate.
5. The method according to claim 1, wherein in the step (1), the conditions for the pre-crystallization are as follows: the temperature is 100-190 ℃, and the time is 8-48 hours;
preferably, in the step (2), the aging conditions are as follows: the temperature is 30-110 ℃ and the time is 4-24 hours.
6. The preparation method according to claim 1, wherein in the step (3), the mass ratio of the silicon-aluminum precursor solution to the structure-oriented sol is 4-90: 1;
the mass of the silicon-aluminum precursor solution and the structure-oriented sol respectively refers to Al contained in the silicon-aluminum precursor solution and the structure-oriented sol2O3And (4) calculating the mass.
7. The preparation method according to claim 1, wherein the conditions of the hydrothermal crystallization are as follows: the temperature is 150-200 ℃ and the time is 6-72 hours.
8. The mordenite with high silica-alumina ratio prepared by the preparation method of any one of claims 1-7.
9. A dimethyl ether carbonylation catalyst, wherein at least one of the mordenite with high silica alumina ratio prepared by the preparation process according to any one of claims 1 to 7 is obtained by ammonium exchange.
10. A method for preparing methyl acetate by dimethyl ether carbonylation is characterized in that raw material gas containing dimethyl ether, nitrogen and carbon monoxide is contacted with a dimethyl ether carbonylation catalyst for reaction to obtain methyl acetate;
the dimethyl ether carbonylation catalyst is selected from the dimethyl ether carbonylation catalyst of claim 9;
the volume ratio of the dimethyl ether to the nitrogen to the carbon monoxide is 1: 40-55: 3-10;
the reaction conditions are as follows: the volume airspeed is 1500-5000 h-1The temperature is 180-220 ℃, and the pressure is 1-3 MPa.
Technical Field
The application relates to a preparation method and application of mordenite with a high silica-alumina ratio, belonging to the technical field of catalysis.
Background
Mordenite is a crystalline microporous aluminosilicate, has a regular pore structure, proper acidity and good hydrothermal stability, is an important chemical catalytic material, and has important industrial application value in the fields of catalytic cracking, alkylation, hydroisomerization, dimethyl ether carbonylation and the like.
Mordenite is a better catalyst carrier for synthesizing methyl acetate by dimethyl ether carbonylation, and the pore channels of the 12-membered ring and the 8-membered ring provide proper reaction conditions for dimethyl ether carbonylation reaction. However, the low silica alumina ratio mordenite is more likely to undergo carbon deposition reaction due to more acid sites, and the high silica alumina ratio mordenite has a longer service life and better stability.
The traditional synthesis method of mordenite is in Na2O-SiO2-Al2O3-H2Hydrothermal crystallization synthesis in an O reaction mixture system. According to most of the existing synthesis techniques, most of the SiO is prepared without using a template agent2/Al2O3Low-silicon mordenite with a molar ratio of 5-12. The high-silicon mordenite can be further obtained by a dealuminization method through water vapor, acid, a complex and the like, the operation process is complex, and the physical indexes of the product are not easy to uniformly control.
The better method is to use an organic template agent as a structure directing agent to directly synthesize the high-silicon zeolite by hydrothermal synthesis. The prior art discloses a method for synthesizing high-silicon mordenite by using long-chain biquaternary ammonium salt as a template agent, wherein the template agent molecules contain more hydrophilic N-containing groups and O-containing groups or contain pyrrolidinium, and the molecules are relatively complex; in the prior art, the mordenite with high silica-alumina ratio is synthesized by using pentasil as a seed crystal; the prior art discloses a method for synthesizing mordenite by three-stage crystallization of halogen compounds and organic templates; the prior art discloses a method for synthesizing mordenite by using a fluorine-containing system; the prior art discloses a method for synthesizing mordenite by using caprolactam as a template agent; the prior art discloses a method for synthesizing mordenite by using naphthenic amine as a template agent; the prior art discloses a method for synthesizing high-silicon (silicon-aluminum molecular sieve ratio is 15-30) mordenite without amine.
The prior art discloses a method for regulating and controlling the proportion of the number of B acid centers in twelve-membered ring channels in the total number of B acid centers of a mordenite molecular sieve, and the prior art discloses that an additional reagent with different structures and charge densities and an optional fluorination reagent are introduced into a synthetic gel, and the obtained MOR zeolite B acid centers are preferentially positioned in a side pocket of an 8-membered ring communicated with a 12-membered ring channel.
Disclosure of Invention
Aiming at the problem that the silicon-aluminum ratio of the product of the molecular sieve hydrothermal synthesis in the prior art is generally lower than the silicon-aluminum ratio of the raw materials fed, and the silicon-aluminum ratio (SiO) of the raw materials is used for synthesizing the high-silicon zeolite2/Al2O3Molar ratio) is high, the cost is increased because raw materials cannot be completely utilized, and in addition, a lot of reaction materials are left in filtrate after crystallization, and the emission pollution is serious.
According to the invention, a high-silica-alumina ratio precursor with a Kenyaite structure is firstly synthesized, and is easy to dissolve and participate in crystallization under the synthesis condition, and experiments show that Kenyaite is an excellent high-silica mordenite synthesis raw material, and plays a role in limiting the aluminum atom placement for obtaining mordenite with higher carbonylation activity. In the synthetic mother liquor, inorganic species in the mother liquor are mostly transformed into species of secondary structural units of a target product crystal structure from an amorphous state after hydrothermal crystallization, and the secondary structural units can guide and generate the mordenite with more 8-membered ring aluminum falling positions, so that the generation of the mordenite guided to the aluminum falling positions can be obviously improved. In addition, organic species in the crystallized filtrate are still good structure-oriented species, and the repeated utilization of the crystallized filtrate is significant.
The invention provides a method for synthesizing mordenite with a high silica-alumina ratio, which not only effectively utilizes filtrate after crystallization, but also can prepare the mordenite with the silica-alumina ratio of 30-120. The catalyst is used for synthesizing methyl acetate by carbonylation of dimethyl ether, the conversion rate of the dimethyl ether is higher, and the stability of the catalyst is obviously superior to that of mordenite with high silica-alumina ratio synthesized by a one-step method under the same conditions.
According to a first aspect of the present application, there is provided a process for the preparation of a high silica to alumina ratio mordenite.
A preparation method of mordenite with high silica-alumina ratio comprises the following steps:
(1) pre-crystallizing a mixture I containing an aluminum source, a silicon source, an alkali source, a template agent R1 and water to obtain a silicon-aluminum precursor solution;
the mixture I comprises the following raw materials in a molar ratio:
M2O:SiO2:Al2O3:R1:H2O＝0.05～0.3:1.00:0.01～0.05:0.05～1.0:10～40；
(2) aging a mixture II containing an aluminum source, a silicon source, an alkali source, a template agent R2 and a substance A to obtain structure-oriented sol;
the molar ratio of the raw materials in the mixture II is as follows:
M2O:SiO2:Al2O3:R1:H2O＝0.05～0.4:1.00:0.02～0.05:0.05～1.0:10～40；
(3) mixing the silicon-aluminum precursor solution and the structure-oriented sol to obtain a sol mixture, carrying out hydrothermal crystallization, removing water, and drying to obtain a crystallized filtrate and the mordenite with the high silicon-aluminum ratio;
in the step (2), the substance A comprises water and \ crystallized filtrate;
in the steps (1) and (2), the alkali source is at least one selected from hydroxides of alkali metals M in an amount of M contained therein2Calculating the mole number of O;
the aluminum source is used in an amount of Al contained therein2O3Calculating the mole number of the active carbon;
the silicon source is used as SiO contained in the silicon source2Calculating the mole number of the active carbon;
the dosage of the template agent is calculated by the mole number of the template agent;
the amount of water used is calculated as its own moles.
Optionally, in the step (3), the silicon-aluminum precursor solution and the structure-oriented sol are mixed to obtain a sol mixture, hydrothermal crystallization is performed, water is removed, and drying is performed to obtain a crystallized filtrate and the mordenite with the high silicon-aluminum ratio.
Optionally, the step (3) is mixing the silicon-aluminum precursor solution and the structure-oriented sol to obtain a sol mixture, performing hydrothermal crystallization, and filtering to obtain a crystallized filtrate and the mordenite with the high silicon-aluminum ratio.
Optionally, the molar ratio of the raw materials in the mixture I is:
M2O:SiO2:Al2O3:R1:H2O＝0.08～0.3:1.00:0.01～0.03:0.09～0.4:12～35。
optionally, the molar ratio of the raw materials in the mixture II is:
M2O:SiO2:Al2O3:R1:H2O＝0.12～0.2:1.00:0.02～0.04:0.12～0.25:10～25。
optionally, in the step (1), a mixture I of an aluminum source, a silicon source, an alkali source, a template agent R1 and water is subjected to pre-crystallization to obtain a silicon-aluminum precursor solution.
Optionally, in the step (2), the mixture II of the aluminum source, the silicon source, the alkali source, the templating agent R2, and the substance a is aged to obtain the structure-oriented sol.
Alternatively, in the mixture I, M2O:SiO2Is independently selected from any value of 0.05:1, 0.06:1, 0.07:1, 0.08:1, 0.1:1, 0.12:1, 0.15:1, 0.17:1, 0.2:1, 0.22:1, 0.25:1, 0.27:1, 0.3:1 or a range between any two.
Alternatively, in mixture I, SiO2:Al2O3The molar ratio of (a) is independently selected from any value of 1:0.01, 1:0.012, 1:0.015, 1:0.017, 1:0.02, 1:0.022, 1:0.025, 1:0.027, 1:0.03, 1:0.032, 1:0.035, 1:0.037, 1:0.04, 1:0.042, 1:0.045, 1:0.047, 1:0.05 or a range between any two values.
Alternatively, in mixture I, SiO2:R1The molar ratio of (a) is independently selected from any value of 1:0.05, 1:0.06, 1:0.07, 1:0.08, 1:0.09, 1:0.1, 1:0.15, 1:0.2, 1:0.25, 1:0.3, 1:0.35, 1:0.4, 1:0.45, 1:0.5, 1:0.55, 1:0.6, 1:0.65, 1:0.7, 1:0.75, 1:0.8, 1:0.85, 1:0.9, 1:0.95, 1:1 or a range between any two of them.
Alternatively, in mixture I, SiO2:H2The molar ratio of O is independently selected from any value of 1:10, 1:12, 1:15, 1:17, 1:20, 1:22, 1:25, 1:27, 1:30, 1:32, 1:35, 1:37, 1:40, or a range between any two.
Alternatively, in mixture II, M2O:SiO2Independently selected from any value of 0.05:1, 0.06:1, 0.07:1, 0.08:1, 0.1:1, 0.12:1, 0.15:1, 0.17:1, 0.2:1, 0.22:1, 0.25:1, 0.27:1, 0.3:1, 0.32:1, 0.35:1, 0.37:1, 0.4:1 or a range between any two.
Alternatively, in mixture II, SiO2:Al2O3Is independently selected from any value of 1:0.02, 1:0.022, 1:0.025, 1:0.027, 1:0.03, 1:0.032, 1:0.035, 1:0.037, 1:0.04, 1:0.042, 1:0.045, 1:0.047, 1:0.05 or a range between any two.
Alternatively, in mixture II, SiO2R2 is independently selected from any value of 1:0.05, 1:0.06, 1:0.07, 1:0.08, 1:0.09, 1:0.1, 1:0.12, 1:0.15, 1:0.2, 1:0.22, 1:0.25, 1:0.3, 1:0.35, 1:0.4, 1:0.45, 1:0.5, 1:0.55, 1:0.6, 1:0.65, 1:0.7, 1:0.75, 1:0.8, 1:0.85, 1:0.9, 1:0.95, 1:1 or a range between any two of them.
Alternatively, in mixture II, SiO2:H2The molar ratio of O is independently selected from any value of 1:10, 1:12, 1:15, 1:17, 1:20, 1:22, 1:25, 1:27, 1:30, 1:32, 1:35, 1:37, 1:40, or a range between any two.
Optionally, the SiO of the high silica to alumina ratio mordenite2/Al2O3The molar ratio is 30-120.
Optionally, the high silica to alumina ratio mercerization boilingSiO of stone2/Al2O3The molar ratio is 50-120.
Optionally, the SiO of the high silica to alumina ratio mordenite2/Al2O3The molar ratio is 50-90.
Optionally, the SiO of the high silica to alumina ratio mordenite2/Al2O3The molar ratio is independently selected from any of 30, 40, 50, 55, 60, 65, 70, 75, 80, 85, 90, 100, 110, 120, or a range between any two.
Alternatively, the high-silicon aluminum precursor solution with the Kenyaite structure is obtained in the step (1). Kenyaite is an excellent high-silicon mordenite synthesis raw material, and plays a role in limiting the aluminum atom placement for obtaining mordenite with higher carbonylation activity.
Optionally, the substance A in the step (2) is the filtrate after crystallization in the step (3).
Optionally, in the step (3), after hydrothermal crystallization of the sol mixture, water removal and drying are performed, and the obtained crystallized filtrate has strong basicity and contains unreacted template agent; and (3) the water in the step (2) is partially or completely replaced by the filtrate after crystallization.
According to the method, in the process of preparing the mordenite, the crystallized filtrate obtained by dewatering and separating is continuously recycled, so that the mordenite with the high silica-alumina ratio can be obtained, the pollution of mother liquor discharge to the environment is avoided, and the preparation cost is also reduced.
Alternatively, in step (1) and step (2), the templating agent R1 and templating agent R2 are independently selected from at least one of cetyltrimethylammonium bromide, dodecyltrimethylammonium bromide, tetrapropylammonium bromide, tetraethylammonium bromide, tetramethylammonium bromide, hexadecyltrimethylammonium chloride, dodecyltrimethylammonium chloride, tetrapropylammonium chloride, tetraethylammonium chloride, tetramethylammonium chloride, hexadecyltrimethylammonium hydroxide, dodecyltrimethylammonium hydroxide, tetrapropylammonium hydroxide, tetraethylammonium hydroxide, tetramethylammonium hydroxide, triethylamine, isopropylamine, diisopropylamine, triisopropylamine, n-butylamine, cyclohexylamine, caprolactam, hexamethyleneimine, heptamethyleneimine, cycloheptaneamine, and cyclopentylamine.
Optionally, in step (1) and step (2), the aluminum source is independently selected from at least one of sodium aluminate, aluminum isopropoxide, aluminum hydroxide, aluminum sulfate, aluminum chloride, and aluminum nitrate.
Optionally, in the step (1) and the step (2), the silicon source is independently selected from at least one of silica white, silica sol and sodium silicate.
Optionally, in step (1), the conditions of the pre-crystallization are as follows: the temperature is 100-190 ℃ and the time is 8-48 hours.
Optionally, in step (1), the conditions of the pre-crystallization are as follows: the temperature is 110-170 ℃ and the time is 18-48 hours.
Optionally, the temperature of the pre-crystallization is independently selected from any value of 100 ℃, 110 ℃, 120 ℃, 130 ℃, 140 ℃, 150 ℃, 160 ℃, 170 ℃, 180 ℃, 190 ℃ or a range value between any two.
Optionally, the pre-crystallization time is independently selected from any value of 8h, 10h, 15h, 18h, 22h, 26h, 30h, 32h, 35h, 36h, 40h, 44h, 48h or a range value between any two.
Optionally, in the step (2), the aging conditions are as follows: the temperature is 30-110 ℃ and the time is 4-24 hours.
Optionally, in the step (2), the aging conditions are as follows: the temperature is 30-60 ℃, and the time is 8-24 hours.
Optionally, the temperature of aging is independently selected from any of 30 ℃, 40 ℃, 50 ℃, 60 ℃, 70 ℃, 80 ℃, 90 ℃, 100 ℃, 110 ℃ or a range between any two.
Optionally, the aging time is independently selected from any of 4h, 6h, 8h, 10h, 12h, 15h, 16h, 18h, 20h, 22h, 24h, or a range between any two.
In the application, through ageing, can make the material mix more evenly, silicon, the slow inter-combination of aluminium molecule, interact more is favorable to follow-up mordenite's growth.
Optionally, in the step (3), the mass ratio of the silicon-aluminum precursor solution to the structure-oriented sol is 4-90: 1;
the mass of the silicon-aluminum precursor solution and the structure-oriented sol respectively refers to Al contained in the silicon-aluminum precursor solution and the structure-oriented sol2O3And (4) calculating the mass.
Optionally, in the step (3), the mass ratio of the silicon-aluminum precursor solution to the structure-oriented sol is 10-80: 1.
In the application, the mass ratio of the silicon-aluminum precursor solution to the structure-oriented sol is 4-90: 1; if the mass ratio is too high, pure mordenite cannot be obtained; if the mass ratio is too low, mordenite with a higher silica-alumina ratio cannot be obtained.
Optionally, the mass ratio of the silicon-aluminum precursor solution and the structure-oriented sol is independently selected from any value of 4:1, 5:1, 8:1, 10:1, 20:1, 30:1, 40:1, 50:1, 60:1, 70:1, 80:1, 90:1, or a range between any two.
Optionally, the hydrothermal crystallization conditions are as follows: the temperature is 150-200 ℃ and the time is 6-72 hours.
Optionally, the hydrothermal crystallization conditions are as follows: the temperature is 170-180 ℃ and the time is 24-60 hours.
Optionally, the temperature of the hydrothermal crystallization is independently selected from any value of 150 ℃, 155 ℃, 160 ℃, 165 ℃, 170 ℃, 175 ℃, 180 ℃, 185 ℃, 190 ℃, 195 ℃, 200 ℃ or a range value between any two.
Optionally, the hydrothermal crystallization time is independently selected from any value of 6h, 12h, 18h, 24h, 30h, 36h, 42h, 48h, 54h, 60h, 66h, 72h or a range value between any two.
Optionally, the preparation method comprises the following three steps: (a) pre-crystallizing an aluminum source, a silicon source, an alkali source, a template agent R and water under a certain condition to obtain a high-silica-alumina ratio precursor with a kenyaite structure; (b) then stirring and aging an aluminum source, a silicon source, an alkali source, a template agent R and water (or filtrate after crystallization) according to a certain proportion at a certain temperature to prepare structure-oriented sol; (c) and mixing the precursor with the high silica-alumina ratio and the guiding sol according to a certain proportion, performing hydrothermal crystallization, washing and drying to obtain the mordenite with the high silica-alumina ratio.
According to a second aspect of the present application there is provided a high silica to alumina ratio mordenite.
The mordenite with high silica-alumina ratio prepared by the preparation method is provided. The silicon-aluminum ratio of the mordenite with the high silicon-aluminum ratio is 30-120.
Optionally, the high silica to alumina ratio mordenite is in a short columnar packed structure.
Optionally, the size of the mordenite with high silica-alumina ratio is 30-60 multiplied by 200-500 nm.
Optionally, the high silica to alumina ratio mordenite has a relative crystallinity of 90% or greater.
According to a third aspect of the present application there is provided a dimethyl ether carbonylation catalyst.
The dimethyl ether carbonylation catalyst is obtained by ammonium exchange of at least one of the mordenite with high silica-alumina ratio prepared by the preparation method.
According to a fourth aspect of the present application there is provided a process for the carbonylation of dimethyl ether to produce methyl acetate.
A method for preparing methyl acetate by dimethyl ether carbonylation comprises the following steps of carrying out contact reaction on raw material gas containing dimethyl ether, nitrogen and carbon monoxide and a dimethyl ether carbonylation catalyst to obtain methyl acetate;
the dimethyl ether carbonylation catalyst is selected from the dimethyl ether carbonylation catalysts;
the volume ratio of the dimethyl ether to the nitrogen to the carbon monoxide is 1: 40-55: 3-10;
the reaction conditions are as follows: the volume airspeed is 1500-5000 h-1The temperature is 180-220 ℃, and the pressure is 1-3 MPa.
Optionally, the volume ratio of the dimethyl ether to the nitrogen to the carbon monoxide is 1: 40-50: 4-7.
Optionally, the reaction conditions are: the volume airspeed is 1600-4800 h-1The temperature is 190-210 ℃, and the pressure is 1-3 MPa.
The beneficial effects that this application can produce include:
according to the preparation method of the mordenite with the high silica-alumina ratio, firstly, a silicon-aluminum raw material is pre-crystallized according to a normal feeding mode to obtain a precursor with the structures of the kenyaite and the mordenite; secondly, preparing structure-oriented sol; finally, the mordenite and the mordenite are mixed according to a certain proportion, and then the mordenite with high silica-alumina ratio is obtained after crystallization, post-treatment, drying and roasting. The preparation method can fully utilize the crystallized filtrate, save raw materials, reduce cost, protect environment and be economical. The mordenite with the silicon-aluminum ratio higher than 50 is prepared by the method, the used raw materials are common and easy to obtain, the conversion rate of dimethyl ether is higher when the mordenite is applied to the reaction of synthesizing methyl acetate by carbonylation of dimethyl ether, the stability of the mordenite is obviously superior to that of the mordenite with the high silicon-aluminum ratio synthesized by a one-step method under the same condition, and the mordenite shows better catalytic activity than the mordenite prepared by other methods.
Drawings
Fig. 1 is an SEM picture of a silicon-aluminum precursor corresponding to sample 1.
Fig. 2 is an XRD spectrum of the corresponding silicon-aluminum precursor of sample 1.
Figure 3 is an XRD spectrum of high silica to alumina ratio mordenite sample 1.
Figure 4 is an SEM picture of high silica to alumina ratio mordenite sample 1.
Detailed Description
The present application will be described in detail with reference to examples, but the present application is not limited to these examples.
Unless otherwise specified, the raw materials in the examples of the present application were purchased commercially, and if not specified, the test methods were performed by conventional methods, and the equipment settings were set according to the manufacturer's recommendations.
Examples 1 to 6
The method comprises the following steps: weighing a certain amount of sodium hydroxide, sodium aluminate, silica sol and hexadecyl trimethyl ammonium bromide, mixing the sodium hydroxide, the sodium aluminate, the silica sol and the hexadecyl trimethyl ammonium bromide with water, uniformly stirring, and transferring the mixture into a stainless steel high-pressure hydrothermal reaction kettle for pre-crystallization to obtain a high-silica-alumina ratio precursor solution with a kenyaite structure. Step two: mixing sodium hydroxide, sodium aluminate and water, adding silica sol and tetraethyl ammonium hydroxide, stirring and aging to obtain the structure-oriented sol. Step three: mixing the silicon-aluminum precursor solution and the structure-oriented sol obtained in the step two according to a certain proportion, uniformly stirring, and transferring into a stainless steel high-pressure hydrothermal reaction kettle for crystallization; and (3) carrying out filter pressing on the product after crystallization is finished to obtain crystallized filtrate, continuously washing the product to be neutral by using deionized water, drying the product for 12 hours at 120 ℃, and roasting the product for 4 hours in a muffle furnace at 550 ℃ to obtain Na-MOR. Step four: weighing a certain amount of the Na-MOR molecular sieve, placing the Na-MOR molecular sieve in a beaker, and adding 2mol/L of ammonium nitrate solution at the temperature of 80 ℃ in a solid-liquid mass ratio of 1: 8, performing ammonium ion exchange for 3 hours, repeating the ammonium ion exchange for 3 times, drying at 120 ℃ for 12 hours, and then roasting for 4 hours at the roasting temperature of 550 ℃ to obtain the H-MOR molecular sieve catalyst.
Example 7
The raw materials, the proportion and the test conditions are the same as those of the first step, the second step, the third step and the fourth step in the example 1. Wherein, the water in the second step is completely replaced by the filtrate obtained after crystallization in the third step in the example 1.
In the preparation process of the samples 1-7, the raw material molar amount, the pre-crystallization temperature and the pre-crystallization time of the silicon-aluminum precursor containing the kenyaite and the mordenite are shown in table 1 in detail.
In the preparation process of samples 1-7, the raw material molar amount, crystallization temperature and time of the structure-oriented sol and comparative sample 1 are detailed in table 2.
The mass ratio of the silicon-aluminum precursor of samples 1-7 to the structure-oriented sol and the silicon-aluminum molar ratio of the mordenite sample obtained by the final detection of the comparative sample 1 are shown in table 3.
TABLE 1 preparation conditions of Si-Al precursors of mordenite samples 1-7
a, taking sodium hydroxide as an alkali source, taking silica sol as a silicon source, taking sodium aluminate as an aluminum source and taking hexadecyl trimethyl ammonium bromide as a template agent;
b, taking sodium hydroxide as an alkali source, sodium silicate as a silicon source, sodium aluminate as an aluminum source and tetraethylammonium chloride as a template agent;
c, taking sodium hydroxide as an alkali source, taking silica sol as a silicon source, taking aluminum sulfate as an aluminum source, and taking hexadecyl trimethyl ammonium bromide as a template agent;
d, taking sodium hydroxide as an alkali source, taking silica sol as a silicon source, taking sodium aluminate as an aluminum source and taking tetraethylammonium bromide as a template agent;
e, taking sodium hydroxide as an alkali source, sodium silicate as a silicon source, aluminum sulfate as an aluminum source and cetyl trimethyl ammonium bromide as a template agent;
f, taking sodium hydroxide as an alkali source, taking silica sol as a silicon source, taking sodium aluminate as an aluminum source and taking hexadecyl trimethyl ammonium bromide as a template agent;
and g, taking sodium hydroxide as an alkali source, taking silica sol as a silicon source, taking sodium aluminate as an aluminum source, and taking hexadecyl trimethyl ammonium bromide as a template agent.
TABLE 2 preparation conditions of Structure-oriented sols of mordenite samples 1 to 7 and comparative sample 1
a', the alkali source is sodium hydroxide, the silicon source is silica sol, the aluminum source is sodium aluminate, and the template agent is tetraethyl ammonium hydroxide;
b', the alkali source is sodium hydroxide, the silicon source is silica sol, the aluminum source is aluminum isopropoxide, and the template agent is hexadecyl trimethyl ammonium bromide;
c', the alkali source is potassium hydroxide, the silicon source is sodium silicate, the aluminum source is aluminum sulfate, and the template agent is n-butylamine;
d', the alkali source is sodium hydroxide, the silicon source is silica sol, the aluminum source is sodium aluminate, and the template agent is tetraethyl ammonium hydroxide;
e', the alkali source is potassium hydroxide, the silicon source is sodium silicate, the aluminum source is aluminum sulfate, and the template agent is tetraethylammonium hydroxide;
f', the alkali source is sodium hydroxide, the silicon source is silica sol, the aluminum source is sodium aluminate, and the template agent is hexadecyl trimethyl ammonium bromide;
g', the alkali source is sodium hydroxide, the silicon source is silica sol, the aluminum source is sodium aluminate, the template agent is tetraethyl ammonium hydroxide, and the filtrate after crystallization is the filtrate after crystallization obtained in the third step in the embodiment 1;
in comparative sample 1, the alkali source is sodium hydroxide, the silicon source is silica sol, the aluminum source is sodium aluminate, and the template agent is cetyltrimethylammonium bromide.
TABLE 3 Mass ratios of Si-Al precursor to structure-oriented sol of samples 1-7 and Si-Al molar ratios of the mordenite samples obtained
Preparation of comparative sample 1
Comparative example 1
Mixing sodium hydroxide, sodium aluminate and water, adding 30% silica sol, cetyl trimethyl ammonium bromide (CTMAB) and seed crystal (MOR), wherein the dosage of the seed crystal is 5 wt%, stirring uniformly, transferring the gel into a stainless steel high-pressure hydrothermal reaction kettle for crystallization, and the crystallization temperature is 175 ℃, and the crystallization time is 36 hours. After crystallization, the post-treatment (drying and roasting) and ammonium ion exchange conditions of the product are the same as those of the third step and the fourth step of the samples 1-6.
Preparation of comparative sample 2
Comparative example 2
Commercial Na-MOR, purchased from catalyst works at southern KAI university, was subjected to ammonium ion exchange and drying under the same calcination conditions as in sample 1, and the final molecular sieve had a silica to alumina ratio of 20.
Preparation of comparative sample 3
Comparative example 3
According to the preparation method (CN102718231A) of the layered nano mordenite disclosed by the patent, the post-treatment conditions and the process of the product are the same as those of the third step and the fourth step of the sample 1, and the silicon-aluminum ratio of the finally obtained molecular sieve is 22.
Preparation of comparative sample 4
Comparative example 4
The procedure is the same as in example 2, except that the structure-oriented sol was prepared without aging, and the silica-alumina ratio of comparative sample 4 was 79.4.
Example 7
The sample of mordenite with high silica alumina ratio prepared in the above example was subjected to X-ray powder diffraction (XRD) analysis, which was characterized by using X' Pert PRO X-ray diffractometer from PANalytical, the netherlands, a Cu target, a K α radiation source (λ ═ 0.15418nm), a voltage of 40KV and a current of 40 mA.
Taking sample 1 prepared in example 1 as an example, fig. 2 is an XRD spectrum of a silicon-aluminum precursor corresponding to sample 1, and fig. 3 is an XRD spectrum of sample 1. As can be seen from fig. 2, the sample has obvious structural characteristics of mordenite, but characteristic peaks of the zeolite structure of the ferrihydrite appear at the positions of 4.38 °, 8.91 °, 25.81 ° and 27.66 °. As can be seen from fig. 3, the sample has distinct peaks characteristic of the mordenite structure, and the crystallinity is higher and the sample is purer.
Example 8
Scanning Electron Microscope (SEM) is carried out on the mordenite sample with the high silica-alumina ratio prepared in the embodiment, an instrument adopted by the SEM test is a Hitachi SU8020 field emission scanning electron microscope, and the accelerating voltage is 2 kV.
Taking sample 1 prepared in example 1 as an example, fig. 1 is an SEM photograph (500nm) of a silica-alumina precursor corresponding to sample 1, and fig. 4 is an SEM photograph (1 μm) of sample 1. As can be seen from figure 1, the sample has two zeolite structures of different sizes, with the size of the ferrihydrite zeolite being much larger. As can be seen from FIG. 4, the finally obtained mordenite with high silica-alumina ratio is in a short column-shaped stacking structure, and the size of the mordenite is 30-60 multiplied by 200-500 nm.
Example 9
The mordenite catalyst samples prepared in the above examples and comparative examples are tableted, crushed and sieved, and 1g of 20-40 mesh catalyst is weighed and loaded into a fixed bed reactor, and N is carried out at 380 DEG C2In-situ pretreatment is carried out for 3 hours, the temperature is reduced to 190 ℃, the reaction pressure is adjusted to 2.0MPa for activity evaluation, and the feeding volume ratio is DME: n is a radical of2: 1-CO: 45: 4, the volume space velocity is 1600h-1And reacting for 12 hours. The evaluation results of the catalyst for the carbonylation of dimethyl ether to methyl acetate are shown in Table 4.
Product analysis was performed on a FuliGC 9790 gas chromatograph, HP-PLOT/Q column, FID detector; the dimethyl ether (DME) conversion rate and Methyl Acetate (MA) selectivity data are calculated according to an area normalization method.
Both the conversion of dimethyl ether and the selectivity to methyl acetate were calculated based on the carbon moles of dimethyl ether:
conversion rate of dimethyl ether ═ [ (mole number of dimethyl ether carbon in raw material gas) - (mole number of dimethyl ether carbon in product) ]/(mole number of dimethyl ether carbon in raw material gas) × (100%);
methyl acetate selectivity is (2/3) × (methyl acetate carbon moles in product) ÷ [ (dimethyl ether carbon moles in feed gas) - (dimethyl ether carbon moles in product) ] × (100%).
TABLE 4 results of evaluation of different samples of dimethyl ether carbonylation catalysts
Name (R)
DME conversion (%)
MA selectivity (%)
Sample 1
73.2
99.6
Sample 2
77.5
99.8
Sample 3
82.3
99.9
Sample No. 4
83.1
99.8
Sample No. 5
84.8
99.7
Sample No. 6
86.3
99.6
Sample 7
74.7
99.5
Comparative sample 1
68.8
98.4
Comparative sample 2
54.3
96.5
Comparative sample 3
62.6
96.7
Comparative sample 4
69.1
98.9
As can be seen from Table 4, the mordenite with high silica-alumina ratio, which is synthesized by using the filtrate obtained after the crystallization of the mordenite through a three-step method and is used as the catalyst for the carbonylation of dimethyl ether in the application, has better catalytic activity and selectivity compared with the mordenite with the silica-alumina ratio of 29.8, which is directly synthesized by a one-step method under the same conditions. Under the same preparation conditions, the structure-oriented sol is not aged, and the carbonylation activity and selectivity of the prepared mordenite with high silica-alumina ratio are lower than those of a sample prepared after aging. For the mordenite with high silicon-aluminum ratio, after the mordenite with high silicon-aluminum ratio is prepared into the dimethyl ether carbonylation catalyst by ammonium exchange, the higher the silicon-aluminum ratio is needed to have catalytic activity, but the better the higher the silicon-aluminum ratio is, and the lower the silicon-aluminum ratio of the mordenite is in a certain range, the higher the conversion rate of dimethyl ether carbonylation is.
Examples 10 to 12
Taking sample 6 as an example, the following results were obtained by changing the evaluation conditions of the dimethyl ether carbonylation catalyst, and are detailed in table 5.
TABLE 5 results of catalyst Performance under various evaluation conditions
Although the present application has been described with reference to a few embodiments, it should be understood that various changes, substitutions and alterations can be made herein without departing from the spirit and scope of the application as defined by the appended claims.
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