阅读说明：本技术 一种动态合成GaKL分子筛的方法及应用 (Method for dynamically synthesizing GaKL molecular sieve and application ) 是由 张文赟 于 2021-09-01 设计创作，主要内容包括：一种动态合成GaKL分子筛的方法及应用,涉及沸石制备技术领域。该方法将镓源、碱源、铝源、硅源和水按摩尔比混合制得溶胶,于一定条件下动态晶化,得到高结晶度的GaKL分子筛。本发明可在低硅铝比投料、不加模板剂和结构导向剂的条件下,合成出具有高结晶度和多级孔结构的GaKL分子筛。将本发明所提供的GaKL分子筛用于低碳烷烃芳构化反应中,可以明显提高芳烃收率特别是C8芳烃收率。与传统方法相比,该方法制备工艺简单,原料利用率高,成本低,具有广阔的应用前景。(A method for dynamically synthesizing a GaKL molecular sieve and application thereof relate to the technical field of zeolite preparation. The method comprises the steps of mixing a gallium source, an alkali source, an aluminum source, a silicon source and water according to a molar ratio to prepare sol, and dynamically crystallizing under a certain condition to obtain the GaKL molecular sieve with high crystallinity. The invention can synthesize the GaKL molecular sieve with high crystallinity and a hierarchical pore structure under the conditions of feeding with low silicon-aluminum ratio and without adding a template agent and a structure directing agent. The GaKL molecular sieve provided by the invention is used in the aromatization reaction of low-carbon alkane, and can obviously improve the yield of aromatic hydrocarbon, particularly the yield of C8 aromatic hydrocarbon. Compared with the traditional method, the method has the advantages of simple preparation process, high utilization rate of raw materials, low cost and wide application prospect.)

1. A method for dynamically synthesizing a GaKL molecular sieve is characterized by comprising the following steps: mixing a gallium source, a potassium source, an aluminum source, a silicon source and water to prepare sol, aging and crystallizing to obtain the GaKL molecular sieve, comprising the following steps,

(1) ga is mixed with a gallium source, a potassium source, an aluminum source, a silicon source and water₂O₃:K₂O:Al₂O₃:SiO₂:H₂Mixing O = 0.001-10: 0.1-9: 1: 1-20: 50-500 molar ratio to prepare sol;

(2) stirring and aging the sol prepared in the step (1);

(3) and (3) placing the sol prepared in the step (2) in a closed container, and dynamically crystallizing for 12 h-10 d at the temperature of 110-250 ℃ to obtain the GaKL molecular sieve.

2. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the molar ratio of the gallium source, the potassium source, the aluminum source, the silicon source and the water is Ga₂O₃:K₂O:Al₂O₃:SiO₂:H₂O= 0.001~4: 0.5~5 : 1 : 3~16 : 70~400。

3. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the volume of the closed container is 30 mL-1 m³。

4. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the crystallization temperature in the dynamic crystallization process is 120-185 ℃, and the crystallization time is 6-36 h.

5. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the aging temperature is room temperature, and the aging time is 4-24 h.

6. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the gallium source is one or more of gallium nitrate, gallium carbonate, gallium sulfate, gallium oxalate and gallium oxide.

7. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the potassium source is one or more of potassium hydroxide, potassium chloride and potassium oxide.

8. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the aluminum source is one or more than two of pseudo-boehmite, activated alumina, aluminum hydroxide, aluminum isopropoxide, hydrated alumina, potassium aluminate, aluminum trichloride, aluminum sulfate and aluminum nitrate.

9. The method for dynamically synthesizing a GaKL molecular sieve according to claim 1, wherein: the silicon source is one or more than two of silica sol, ethyl orthosilicate, white carbon black and water glass.

10. The use of a GaKL molecular sieve prepared by the method for dynamically synthesizing a GaKL molecular sieve according to any one of claims 1 to 9, wherein: the GaKL molecular sieve is used as a carrier for preparing a catalyst for aromatization of low-carbon alkane.

Technical Field

The invention relates to the technical field of molecular sieves, in particular to a method for dynamically synthesizing a GaKL molecular sieve and application thereof.

Background

The LTL molecular sieve belongs to a hexagonal system, a framework consists of cancrinite cages (CAN cages) and hexagonal column cages (D6R), the CAN cages and the D6R cages are alternately connected around the direction of a six-fold axis of a C axis, and then the cage rotates according to the six-fold axis to generate a one-dimensional twelve-membered ring circular pore channel structure with a twelve-membered ring, so that the molecular sieve has good hydrothermal stability. The main channel pore diameter is about 13A at the widest point and about 7.1A at the narrowest point, and is a large pore zeolite (Monatsheftete fur Chemie/Chemical Monthly, 2005, 136(1): 77-89). The LTL zeolite has unique adsorption performance and catalytic performance, has good thermal stability, is a catalytic material with excellent thermal stability, and can be used for preparing catalysts for hydrocarbon conversion processes such as cracking, isomerization, aromatization, alkylation, lubricating oil hydrocracking and the like. Research on the synthesis and synthesis method of LTL molecular sieves has been a focus of attention of many scholars, and so far, the methods used for synthesizing LTL molecular sieves are mainly hydrothermal synthesis methods and mainly synthesis under static conditions, and such methods cannot be applied to industrial mass production. In industrial production, due to the need of mass and heat transfer, the production of molecular sieves usually adopts a dynamic crystallization mode, so the synthesis of LTL molecular sieves under the dynamic crystallization condition needs to be researched. Compared with a static hydrothermal crystallization mode, a dynamic hydrothermal crystallization mode has the advantages of short crystallization time, high stability, good repeatability and the like, and the dynamic hydrothermal synthesis mode is widely applied to synthesis of molecular sieves. The dynamic synthesis of the ZSM-22 molecular sieve and the Nu-10 molecular sieve can effectively avoid the generation of MFI mixed crystals (the scientific science of university of Hunan province, 2012,6: 62-66). And when the Nu-10 molecular sieve is synthesized, reactants can be uniformly mixed by adopting a dynamic hydrothermal synthesis mode, and the crystallization time is reduced (US: 4900528 and US: 4818509).

The Pt/LTL catalyst is a base-catalyzed aromatization catalyst with excellent aromatization performance, and has the advantages of high liquid yield and high aromatic yield compared with acid-catalyzed aromatization. However, the low selectivity of the catalyst to aromatics and the short single-pass life are the main defects, and the industrial application of the catalyst is limited. To improve catalyst stability, LTL zeolites have been modified in a number of ways.

For example, patent US5773381 produces a Cs-containing L zeolite by adding Cs ions during the synthesis of LTL zeolite, which can be used for aromatic isomerization or aromatization reactions. However, the above method still has the problem of carbon deposition and the like, which adversely affects the arylation.

Ge, Ga, B, Fe, Ti and other elements are doped into the molecular sieve to isomorphously replace four coordinated Al or Si atoms on the framework of the molecular sieve, so that the molecular sieve modification method is an effective means for molecular sieve modification. Through the synthesis of the heteroatom molecular sieve, not only can the physicochemical properties of the molecular sieve be systematically adjusted so as to improve the catalytic performance for specific reactions, but also a novel molecular sieve-like material can be prepared.

Many studies have reported the synthesis and application of different Ga-doped molecular sieves. Kim et al (Microporous MeOporous Mater., 2008, 114: 343-. GaPO was successfully synthesized by Microporous MeOporus Mater, 2009, 120: 278-₄-LTA equimolecular sieves. Wu et Al (applied. Catal. A, 2010, 375: 279-one 288) synthesized Ga-substituted Al ZSM-12 molecular sieves using methyltriethylammonium bromide (MTEA) template and used in the methylation reaction of NAPH. In addition, Ga atoms can isomorphously replace Si atoms in the molecular sieve framework so as to regulate the acidity of the surface of the molecular sieve. Meepraert et al (Microporous Mesoporous Mater., 2013, 175: 99-106) studied Ga by density functional theory³⁺Isomorphously substituted Si³⁺The Si atom on the twelve-membered ring was found to be most easily substituted after LTL molecular sieve (K) and Ga^{3 +}Substituted Si³⁺Thereafter bransted acid sites are generated (Materials, 2013, 6: 4139-. The synthesis of the Ga-substituted L-shaped molecular sieve is expected to improve the aromatization efficiency of the catalyst.

In the process of synthesizing KL zeolite, how to improve the yield of KL zeolite is always a concern, and researchers have done a lot of work.

For example, patent CN1070383A reports that zeolite L can be synthesized by adding a directing agent under the conditions of lower silica-alumina ratio and alkali-silica ratio. Although the directing agent provides crystal nuclei for the synthesis of the L zeolite, thereby accelerating the crystallization speed, the directing agent needs 72 hours for aging, and the time is long, so that the industrial production efficiency is influenced.

For example, patent US3947482 describes that L zeolite can be synthesized by adding an organic templating agent to the substrate, but the introduction of the templating agent increases the difficulty of post-treatment, adversely affects the zeolite crystal structure during removal of the templating agent, and increases the synthesis cost.

Disclosure of Invention

The invention aims to overcome the defects of the prior art, improve the yield of the L-type zeolite and reduce the synthesis cost; the diffusion path of molecules is shortened, so that the aromatic selectivity of the catalyst is improved, and the one-way service life of the catalyst is prolonged; hetero atoms are introduced to improve the performance of the molecular sieve carrier; successfully performs pilot experiments on the synthesis process, and leads the synthesis process to be closer to industrialization, a method for dynamically synthesizing the GaKL molecular sieve.

The scheme for solving the technical problems is as follows:

a dynamically synthesized GaKL molecular sieve having an LTL structure as defined by the International Zeolite Association, the synthesis method characterized by: mixing a gallium source, a potassium source, an aluminum source, a silicon source and water to prepare sol, aging and crystallizing to obtain the GaKL molecular sieve with high crystallinity, comprising the following steps,

(1) ga is mixed with a gallium source, a potassium source, an aluminum source, a silicon source and water₂O₃:K₂O:Al₂O₃:SiO₂:H₂O = 0.001-10: 0.1-9: 1: 1-20: 50-500 by mole ratio,

(2) stirring and aging the sol prepared in the step (1),

(3) and (3) placing the sol prepared in the step (2) in a closed container, and dynamically crystallizing for 12 h-10 d at 110-250 ℃ to obtain the high-crystallinity LTL molecular sieve.

The molar ratio of the gallium source, the potassium source, the aluminum source, the silicon source and the water is preferably Ga₂O₃:K₂O:Al₂O₃:SiO₂:H₂O = 0.001-4: 0.5-5: 1: 3-16: 70-400. The silicon-aluminum ratio of the fed materials is low, the crystallization of the product is good, and the yield can reach 85 percent at most.

The volume of the closed container is 30 mL-1 m³From pilot to pilot.

Generally, industrially produced zeolites are dynamically crystallized. The dynamic crystallization of the invention simulates the industrial production condition and is between 10L and 1m³And successfully crystallizing in a closed kettle to obtain the GaKL type molecular sieve with high crystallinity.

The dynamic crystallization is that reactants are mixed and then put into a high-pressure kettle with stirring for heating crystallization, and the reactants are in a stirring state in the crystallization process.

The crystallization temperature in the crystallization process is 120-185 ℃, and the crystallization time is 6-36 h.

The aging temperature is room temperature, and the time is 4-24 hours.

The gallium source is one or more than two of gallium nitrate, gallium carbonate, gallium sulfate, gallium oxalate and gallium oxide; the potassium source is one or more of potassium hydroxide, potassium chloride and potassium oxide; the aluminum source is one or more than two of pseudo-boehmite, activated alumina, aluminum hydroxide, aluminum isopropoxide, hydrated alumina, potassium aluminate, aluminum trichloride, aluminum sulfate and aluminum nitrate; the silicon source is one or more than two of silica sol, ethyl orthosilicate, white carbon black and water glass.

The catalyst for aromatization of low-carbon alkane is prepared by adopting the nano GaKL molecular sieve as a carrier. One or more than two metals of Pt, Ru, Pd and Sn are loaded on the carrier, and the metal loading amount is 0.05-4.0%.

The aromatization of the normal alkane can be carried out in a fixed bed reactor, and the number of carbon atoms in the normal alkane is 6, 7 or 8.

The reaction conditions of the aromatization may specifically be: the mass space velocity of the n-alkane is 0.8-4 h^-1The molar ratio of the hydrogen to the n-alkane is 0.2-6.0: 1, the reaction pressure is 0.1-3 MPa, and the reaction temperature is 250-550 ℃.

The invention has the beneficial effects that: ga is the same group element of Al in the periodic table, and the chemical structure is similar to Al, therefore Ga can be used in the synthesis process of the molecular sieve³⁺Isomorphous substitution of Al³⁺Synthesis and synthesisThe molecular sieve has a heteroatom molecular sieve of the same structure. Under the conditions of low silicon-aluminum ratio feeding and no addition of a template agent and a structure directing agent, the GaKL molecular sieve with high crystallinity and a hierarchical pore structure is synthesized. The GaKL molecular sieve provided by the invention is used in the aromatization reaction of low-carbon alkane, and can obviously improve the yield of aromatic hydrocarbon, particularly the yield of C8 aromatic hydrocarbon. Compared with the traditional method, the method has the advantages of simple preparation process, high utilization rate of raw materials, high yield up to 85 percent, low cost and wide application prospect.

Drawings

FIG. 1 is an XRD spectrum of a sample of example 1 of the present invention.

FIG. 2 is a graph showing the physical adsorption of the sample in example 1 of the present invention.

FIG. 3 is an SEM photograph of a sample in example 1 of the present invention.

Detailed Description

The following examples further illustrate the invention but are not intended to limit the invention thereto.

TABLE 1 Synthesis conditions of examples 1 to 5 of the present invention

Examples

Ga2O3:K2O:SiO2:Al2O3:H2O

Time of crystallization

Crystallization temperature

Metal source

Scale of

Yield of

1

0.001:2.0 : 7.1 : 1.0 : 190

18 h

170 °C

Gallium nitrate

200 mL

85%

2

0.005:0.5 : 8.5 : 1.0 : 70

6 h

185 °C

Gallium carbonate

30 mL

80%

3

0.01:5.0 : 16 : 1.0 : 400

24 h

120°C

Gallium sulfate

2 L

65%

4

4:3.0 : 3.0 : 1.0 : 250

36 h

175°C

Oxalic acid gallium salt

10 L

55%

5

1:2.5 : 8.0 : 1.0 : 210

22 h

175°C

Gallium oxide

1 m3

82%

Example 1

12.25 g KOH was weighed in a 500 mL beaker, 10 g pure water was added, and after stirring well, 7.06 g Al (OH) was added₃And heating to 95 ℃ and stirring to clarify the solution. After the solution was cooled, 117.12 g of pure water was added, and 0.0121g of gallium nitrate was added thereto and the mixture was further stirred. 49.48 g of silica sol was weighed into another 500 mL beaker, and the clear Al (OH) was added via a separatory funnel₃The solution was added dropwise to the silica sol and stirring was continued for 8 h. Stopping stirring, and filling the gel into a 200 mL crystallization kettle. And (4) placing the crystallization kettle into an oven, and dynamically crystallizing at 170 ℃ for 18 h. After crystallization is finished, the crystallization kettle is taken out, and then the sample is centrifugally washed by pure water until the pH value is 7 or 8. The sample was transferred to a crucible and placed in a 120 ℃ oven for drying for 12 h.

Grinding the molecular sieve into powder, and analyzing by XRD spectrogram, wherein the molecular sieve is GaKL molecular sieve and contains mesopores as shown in figures 1 and 2. The resulting molecular sieve was cylindrical, as shown in FIG. 3.

The catalyst is prepared by loading metal Pt (0.5 wt%) on the GaKL molecular sieve, and the aromatization performance of the catalyst is evaluated in a fixed bed reactor by taking n-octane as a raw material. The mass space velocity (WHSV) is 1h^-1The hydrogen-hydrocarbon ratio was 6 (molar ratio), the reaction pressure was 1MPa, and the reaction temperature was 500 ℃. Wherein the liquid phase product is analyzed off line after being condensed, and the gas phase product is analyzed on line.

The catalyst prepared by the carrier shows excellent catalytic performance in the aromatization reaction of n-octane, and under the condition of 95 percent of conversion rate, the yield of aromatic hydrocarbon reaches 62 percent, the yield of C8 aromatic hydrocarbon reaches 30 percent, the yield of methylbenzene reaches 19 percent, the yield of benzene reaches 17 percent, and the yield of liquid reaches 88 percent. From the data, the catalyst prepared by the GaKL molecular sieve has higher aromatic hydrocarbon yield and liquid yield in the aromatization reaction of n-octane,

example 2

1.53 g KOH was weighed in a 100 mL beaker, 2g pure water was added, and after stirring well, 3.53 g Al (OH) was added₃And heating to 95 ℃ and stirring to clarify the solution. After the solution was cooled, 9 g of pure water was added, and 0.0303g of gallium carbonate was added and the stirring was continued. 30 g of silica sol was weighed into another 100 mL beaker, and the clear Al (OH) was added via a separatory funnel₃The solution was added dropwise to the silica sol and stirring was continued for 24 h. Stopping stirring, and filling the gel into a 30 mL crystallization kettle. And (4) putting the crystallization kettle into an oven, and dynamically crystallizing for 6 hours at 185 ℃. After crystallization is finished, the crystallization kettle is taken out, and then the sample is centrifugally washed by pure water until the pH value is 7 or 8. The sample was transferred to a crucible and placed in a 120 ℃ oven for drying for 12 h. The molecular sieve has LTL topological structure through XRD spectrogram analysis.

Example 3

130.13 g of KOH were weighed in a 2000 mL beaker, 100 g of pure water was added, and after stirring well, 30 g of Al (OH) was added₃And heating to 95 ℃ and stirring to clarify the solution. After the solution was cooled, 1030 g of pure water was added, and 0.5152g of gallium sulfate was added and the stirring was continued. 473.79 g of silica sol was weighed into a 2000 mL beaker, and the clear Al (OH) was added via a separatory funnel₃The solution was added dropwise to the silica sol and stirring was continued for 4 h. Stopping stirring, and filling the gel into a 2L crystallization kettle. And (3) putting the crystallization kettle into an oven, and dynamically crystallizing for 24 hours at the temperature of 120 ℃. After crystallization is finished, the crystallization kettle is taken out, and then the sample is centrifugally washed by pure water until the pH value is 7 or 8. The sample was transferred to a crucible and placed in a 120 ℃ oven for drying for 12 h. The molecular sieve has LTL topological structure through XRD spectrogram analysis.

Example 4

781 g KOH was weighed in a 10L bucket, 800 g pure water was added, and after stirring well, 300 g Al (OH) was added₃And heating to 95 ℃ and stirring to clarify the solution. After the solution was cooled, 7454.3 g of pure water was added, 2060g of gallium oxalate was added, and the stirring was continued. 473.79 g of silica sol was weighed into another 10L bucket, and then clarified Al (OH)₃The solution was added dropwise to the silica sol and stirring was continued for 10 h. Stopping stirring, and filling the gel into a 10L crystallization kettle. Putting the crystallization kettle into an oven, and carrying out dynamic reaction at 175 DEG CAnd crystallizing for 36 h. After crystallization is finished, the crystallization kettle is taken out, and then the sample is centrifugally washed by pure water until the pH value is 7 or 8. The sample was transferred to a crucible and placed in a 120 ℃ oven for drying for 12 h. The molecular sieve has LTL topological structure through XRD spectrogram analysis.

Example 5

672.35kg KOH was weighed, 152kg pure water was added, and 310kg Al (OH) was added after stirring well₃And heating to 95 ℃ and stirring to clarify the solution. After the solution was cooled, 6000.33kg of pure water was added, 532.37kg of gallium oxide was added and stirring was continued. 2447.91 kg of silica sol were weighed out and the clear Al (OH)₃The solution was added dropwise to the silica sol and stirring was continued for 17 h. Stopping stirring, and filling the gel at 1m³In a crystallization kettle. And (4) putting the crystallization kettle into an oven, and dynamically crystallizing for 22 h at 175 ℃. After crystallization is finished, the crystallization kettle is taken out, and then the sample is centrifugally washed by pure water until the pH value is 7 or 8. The sample was transferred to a crucible and placed in a 120 ℃ oven for drying for 12 h. The molecular sieve has LTL topological structure through XRD spectrogram analysis.

The GaKL molecular sieves obtained in examples 2 to 5 above were used as carriers to support metal Pt (0.1 wt%, 0.5 wt%, 1 wt%, 2 wt%, 3 wt%, 3.5 wt%) to prepare catalysts, and the aromatization performance thereof was evaluated in a fixed bed reactor using n-octane as a raw material. Experiments prove that the catalyst prepared by the carrier shows excellent catalytic performance in the aromatization reaction of n-octane, and under the condition of 95 percent of conversion rate, the yield of aromatic hydrocarbon reaches about 60 percent, the yield of C8 aromatic hydrocarbon is about 30 percent, the yield of methylbenzene is about 20 percent, the yield of benzene is about 20 percent, and the yield of liquid is about 90 percent. The catalyst prepared by the KL molecular sieve has higher aromatic hydrocarbon yield and liquid yield in the normal octane aromatization reaction.

The above embodiments are only some of the embodiments of the present invention, and the embodiments are not intended to limit the scope of the present invention, and all equivalent changes made by using the contents of the present invention are covered by the scope of the present invention claimed in the claims.