TON molecular sieve, preparation method and application thereof, and TON molecular sieve composition and application thereof
By using 3-diethylamino-1-propanol as a template to prepare TON molecular sieve under static conditions, the problems of low purity and high cost in the existing technology under high-speed stirring are solved, and the preparation of high-purity and low-cost TON molecular sieve is achieved. Heteroatom elements are introduced to improve catalytic activity.
Patent Information
- Application Number
- CN202111233224.3
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Filing Date
- 2021-10-22
- Publication Date
- 2025-09-26
- Estimated Expiration
- 2041-10-22
AI Technical Summary
The existing preparation method of TON molecular sieve needs to be carried out under high-speed stirring conditions, has poor reproducibility and is prone to the formation of impurity crystals, resulting in low product purity and high cost.
3-Diethylamino-1-propanol is used as an organic template, combined with a silicon source, a fluorine source and a heteroatom element X source to carry out a crystallization reaction under static conditions to prepare TON molecular sieve. The molar ratio of SiO2:XOm/2 is 1:0-0.05, and the heteroatom element X is Al, Ti, Zr, Fe, etc. The synthesis process does not require high-speed stirring, and the product purity is high.
The high-purity preparation of TON molecular sieves was achieved, the synthesis process was simplified, the cost was reduced, and different catalytic active centers were generated by introducing heteroatom elements to meet the needs of different catalytic reactions.
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Abstract
Description
Technical Field
[0001] The present invention relates to the technical field of molecular sieves, and in particular to a TON molecular sieve and a preparation method and application thereof, and a TON molecular sieve composition and application thereof. Technical Background
[0002] TON molecular sieve is a mesoporous molecular sieve with one-dimensional elliptical straight pores, with 10-membered ring openings measuring 0.46 x 0.57 nm. Due to its mild acidic properties and steric shape selectivity, ZSM-22 molecular sieves are used in the isomerization of linear alkanes, methanol to olefins, aromatic alkylation, hydrocracking, catalytic dewaxing, and alkane aromatization.
[0003] Molecular sieves with a TON structure include Theta-1, ZSM-22, KZ-2, NU-10, and ISI-1. US Patent 5342596 discloses a method for preparing a molecular sieve named Theta-1. The process uses a halogenated derivative of a nitrogen-containing heterocyclic compound as a template. The synthesis generally requires a dynamic crystallization reactor, and impurities such as ZSM-5 or white silica are easily present in the product. US Patent 4481177 discloses a method for synthesizing ZSM-22 using N-ethylpyrrole bromide as a template. The preparation requires vigorous stirring and has poor synthetic reproducibility. US Patent 4900528 discloses a method for synthesizing a molecular sieve named NU-10, which uses an organic template of the structure L1-(CH2)n-L2, where L1 and L2 are hydroxyl groups and / or amino groups. US Patent 4483835 discloses a molecular sieve named ISI-1, which uses a salt of a derivative of a nitrogen-containing heterocyclic compound as a template. Most of these syntheses need to be carried out under high-speed stirring, otherwise the synthesis is likely to fail. Summary of the Invention
[0004] The present invention aims to provide a TON molecular sieve and a preparation method and application thereof. The preparation method of the molecular sieve is simple, does not require high-speed stirring conditions, has high product purity, and has low synthesis cost.
[0005] In order to achieve the above object, the first aspect of the present invention provides a method for preparing TON molecular sieve, which comprises: mixing a silicon source, a fluorine source, an organic template agent Q, water and an optional heteroatom element X source to carry out a crystallization reaction; the organic template agent is 3-diethylamino-1-propanol, the silicon source in terms of SiO2, the organic template agent in terms of X ... m / 2 The X source is calculated, m is the oxidation state of the X element, and the molar ratio is SiO2:XO m / 2 1:0~0.05, preferably SiO2:XO m / 2 It is 1:0.005~0.04.
[0006] The second aspect of the present invention provides a TON molecular sieve prepared by the preparation method of the TON molecular sieve of the present invention, wherein the TON molecular sieve has the formula: SiO2·1 / x XO m / 2 The schematic chemical composition shown in the figure, wherein X is a heteroatom element, m is the oxidation state of the X element, m = 1 to 7, SiO2 / XO m / 2 The molar ratio x≥20.
[0007] A third aspect of the present invention provides a TON molecular sieve composition, which contains the TON molecular sieve described in the present invention and a binder.
[0008] A fourth aspect of the present invention provides a use of the TON molecular sieve of the present invention or the TON molecular sieve composition of the present invention as an adsorbent or catalyst.
[0009] The preparation method of the TON molecular sieve provided by the present invention has the advantages of a simple organic template structure, no need for high-speed stirring during synthesis, and high product purity. Furthermore, heteroatoms (e.g., Al, Ti, Zr, Fe, and other elements) can be introduced into the framework to generate different catalytically active centers to meet the needs of different catalytic reactions. BRIEF DESCRIPTION OF THE DRAWINGS
[0010] Figure 1 is the X-ray diffraction (XRD) pattern of the sample obtained in Example 1;
[0011] Figure 2 This is a scanning electron microscope (SEM) image of the sample obtained in Example 1;
[0012] Figure 3 is the X-ray diffraction (XRD) pattern of the sample obtained in Example 2;
[0013] Figure 4 This is a scanning electron microscope (SEM) image of the sample obtained in Example 2. DETAILED DESCRIPTION
[0014] The endpoints of the ranges and any values disclosed herein are not limited to the precise ranges or values, and these ranges or values should be understood to include values close to these ranges or values. For numerical ranges, the endpoints of each range, the endpoints of each range and individual point values, and the individual point values can be combined with each other to obtain one or more new numerical ranges, which should be considered to be specifically disclosed herein.
[0015] The present invention provides a preparation method of TON molecular sieve, which comprises: mixing a silicon source, a fluorine source, an organic template agent Q, water and an optional heteroatom element X source, and performing a crystallization reaction; the organic template agent is 3-diethylamino-1-propanol, the silicon source in terms of SiO2, the XO in terms of XO2, and the like. m / 2 The X source is calculated in molar ratio, SiO2:XO m / 2 is 1:0~0.05, m is the oxidation state of element X, preferably SiO2:XO m / 2 The ratio is 1:0.005-0.04. This preparation method has the advantages of a simple organic template structure, no need for high-speed stirring during synthesis, and high product purity. Heteroatom elements X can be introduced into the framework to create different catalytic active centers to meet the needs of different catalytic reactions.
[0016] According to a preferred embodiment of the present invention, the heteroatom element X is at least one selected from aluminum, boron, gallium, germanium, titanium, zirconium, hafnium, tin, zinc, iron, indium, and chromium. Introducing the heteroatom element X into the molecular sieve framework can generate different catalytically active centers to meet the needs of different catalytic reactions.
[0017] According to a preferred embodiment of the present invention, the organic template Q, the silicon source calculated as SiO2, the silicon source calculated as XO m / 2 The molar ratio of the X source in terms of F, the fluorine source in terms of F and water is Q:SiO2:XO m / 2 :F:H2O=0.15~4:1:0~0.05:0.2~4:5~30, preferably Q:SiO2:XO m / 2 :F:H2O=0.5~2:1:0.005~0.04:0.35~2.5:6~20.
[0018] According to a preferred embodiment of the present invention, the silicon source is selected from at least one of water glass, silica sol, solid silica gel, fumed silica, amorphous silica, diatomaceous earth, zeolite molecular sieve and tetraalkoxysilane.
[0019] According to a preferred embodiment of the present invention, the fluorine source is selected from at least one of hydrofluoric acid, ammonium fluoride, sodium fluoride and potassium fluoride, preferably at least one of hydrofluoric acid and ammonium fluoride.
[0020] According to a preferred embodiment of the present invention, when the heteroatom element X is aluminum, the source is selected from at least one of aluminum sulfate, sodium aluminate, aluminum nitrate, aluminum chloride, pseudo-boehmite, aluminum oxide, aluminum hydroxide, silica-aluminum zeolite molecular sieve, aluminum carbonate, elemental aluminum, aluminum isopropoxide and aluminum acetate; when the heteroatom element X is boron, the source of boron is selected from at least one of boric acid, sodium tetraborate, amorphous boron oxide, potassium borate, sodium metaborate, ammonium tetraborate and organic boron ester; when the heteroatom element X is germanium, the source of germanium is selected from at least one of germanium oxide, germanium nitrate and tetraalkoxygermanium; when the heteroatom element X is titanium, the source of titanium is selected from alkyl titanates (such as tetramethyl titanate, tetraethyl titanate, tetrapropyl titanate, titanate esters, etc.). When the heteroatom element X is tin, the tin source is selected from at least one of tin tetrachloride, stannous chloride, alkyl tin, alkoxy tin and organic stannate; when the heteroatom element X is iron, the iron source is selected from at least one of ferric sulfate, ferric nitrate, iron halide (such as ferric chloride), ferrocene and ferric citrate; when the heteroatom element X is zinc, zirconium, hafnium, gallium, indium and chromium, the zinc source, zirconium source, hafnium source, gallium source, indium source and chromium source are selected from conventional substances in the art, such as zinc sulfate, zinc acetate, zirconium nitrate, zirconium oxychloride, hafnium sulfate, gallium oxide, gallium nitrate, indium oxide, indium nitrate, chromium chloride and chromium nitrate.
[0021] According to a preferred embodiment of the present invention, the conditions of the crystallization reaction include: a crystallization temperature of 100-200°C; preferably 110-190°C, more preferably 160-175°C.
[0022] According to a preferred embodiment of the present invention, the conditions of the crystallization reaction include: a crystallization time of 24 to 300 hours, preferably 36 to 250 hours, and preferably 120 to 180 hours.
[0023] According to a preferred embodiment of the present invention, the crystallization reaction conditions include crystallization at 100-200° C. for 24-300 hours; preferably crystallization at 110-190° C. for 36-250 hours.
[0024] According to a preferred embodiment of the present invention, the crystallization is carried out under static conditions. The preparation method of the TON molecular sieve provided by the present invention has the advantages of simple organic template structure and high product purity can be obtained without high-speed stirring conditions.
[0025] According to a preferred embodiment of the present invention, after the crystallization reaction is completed, conventional post-treatment is performed, such as filtering, washing, and drying to obtain the molecular sieve; and optionally, the molecular sieve is calcined.
[0026] The present invention provides a TON molecular sieve prepared by the preparation method of the TON molecular sieve of the present invention, wherein the TON molecular sieve has the formula: SiO2·1 / x XO m / 2 The schematic chemical composition shown in the figure, wherein X is a heteroatom element, m is the oxidation state of the X element, m = 1 to 7, SiO2 / XO m / 2 The molar ratio x≥20.
[0027] According to a preferred embodiment of the present invention, the TON molecular sieve is preferably a needle-shaped crystal.
[0028] According to a preferred embodiment of the present invention, the X-ray diffraction pattern of the TON molecular sieve includes characteristic peaks as shown in the following table:
[0029]
[0030] In the present invention, in the X-ray diffraction pattern, vw, w, m, s, and vs represent the diffraction peak intensity, vw is very weak, w is weak, m is medium, s is strong, and vs is very strong; generally speaking, vw is less than 5%, w is 5%-20%, m is 20%-40% (including 20% and 40%), s is 40%-70%, and vs is greater than 70% (including 70%).
[0031] The data in the above table represent the interplanar spacing of TON molecular sieve at 2θ(°) of 8.15±0.2. It is 10.85±0.50, and the relative intensity (%) (I / I0)×100 is vs (very strong), and so on. Those skilled in the art are well aware of the representation method of the table, and the present invention will not explain them one by one here.
[0032] The present invention provides a TON molecular sieve composition, which contains the TON molecular sieve of the present invention and a binder.
[0033] The present invention has no particular limitation on the adhesive, and any adhesive in the art can be used as the adhesive described in the present invention.
[0034] The present invention provides a use of the TON molecular sieve of the present invention or the TON molecular sieve composition of the present invention as an adsorbent or catalyst.
[0035] In the context of this specification, the structure of the molecular sieve is determined by X-ray diffraction pattern (XRD), which is measured by X-ray powder diffractometer using a Cu-Kα ray source with a Kα1 wavelength of λ = 1.5405980 angstroms. Nickel filter.
[0036] In the present invention, an X'Pert PRO X-ray powder diffraction (XRD) instrument from PANalytical (Netherlands) was used, operating at 40 kV, 40 mA, and a scanning range of 5-40°. The product morphology was photographed using an S-4800 field emission scanning electron microscope (Fe-SEM) from HITACHI (Japan).
[0037] It should be noted that two or more aspects (or implementation methods) disclosed in the context of this specification can be arbitrarily combined with each other, and the technical solutions (such as methods or systems) thus formed are part of the original disclosure of this specification and also fall within the scope of protection of the present invention.
[0038] Unless otherwise specified, all percentages, parts, ratios, etc. mentioned in this specification are based on weight, unless the weight basis does not conform to the general understanding of those skilled in the art.
[0039] In order to facilitate the understanding of the present invention, the present invention lists the following embodiments, but the embodiments are only used to help understand the present invention and should not be regarded as specific limitations of the present invention.
[0040] Example 1
[0041] 5.25 g of 3-diethylamino-1-propanol (DEAP), 0.6 g of water, and 6 g of Ludox silica sol (SiO2 40 wt%) were mixed uniformly and stirred at room temperature for 3 hours. 2 g of hydrofluoric acid (40 wt%) was added and stirred for 1 hour. The mixture was then placed in a polytetrafluoroethylene-lined crystallization kettle and placed in a 170°C oven for static crystallization for 120 hours. The reaction solid was filtered, washed with distilled water, and dried at 100°C to obtain a raw powder solid. The raw powder solid was placed in a muffle furnace and calcined at 550°C for 5 hours to obtain the final product. The XRD pattern is shown below. Figure 1 As shown by Figure 1 It can be seen that the product is TON molecular sieve, the spectrum data is shown in Table 1, and the SEM photos are shown in Figure 2 As shown by Figure 2 It can be seen that the TON molecular sieve is a needle-shaped crystal. The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0042] Table 1
[0043]
[0044]
[0045] Example 2
[0046] 2.62g of 3-diethylamino-1-propanol (DEAP), 4.1g of water, and 6g of Ludox silica sol (SiO2 40wt%) were mixed uniformly and stirred at room temperature for 3 hours. 1.5g of hydrofluoric acid (40wt%) was added and stirred for 1 hour. The mixture was then placed in a polytetrafluoroethylene-lined crystallization kettle and placed in a 175°C oven for static crystallization for 144 hours. The solid after the reaction was filtered, washed, dried, and calcined to obtain the final product. The XRD pattern is shown in FIG. Figure 3 As shown by Figure 3 It can be seen that the product is TON molecular sieve, the spectrum data is shown in Table 2, and the SEM photos are shown in Figure 4 As shown by Figure 4 It can be seen that the TON molecular sieve is a needle-shaped crystal. The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0047] Table 2
[0048]
[0049] Example 3
[0050] 5.25g 3-diethylamino-1-propanol (DEAP) was mixed with 2.4g water, and 0.133g aluminum sulfate 18hydrate was added. After dissolving, 6g Ludox silica sol (SiO2 40wt%) was slowly added under stirring. After stirring at room temperature for 3h, 2g hydrofluoric acid (40wt%) was added. After stirring for 1 hour, the mixture was placed in a crystallization kettle with a polytetrafluoroethylene lining and placed in a 165℃ oven for static crystallization for 132 hours. The solid after reaction was filtered, washed, dried and calcined to obtain the final Al-TON molecular sieve product. The XRD pattern was the same as that of the solid. Figure 1 The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0051] Example 4
[0052] 6.3g of 3-diethylamino-1-propanol (DEAP), 7.2g of water, and 0.058g of pseudo-boehmite (70wt%) of Al2O3 were mixed uniformly. 3g of Ludox silica sol (40wt%) of SiO2 and 1.27g of white carbon black (95wt%) of SiO2 were slowly added under stirring. After stirring at room temperature for 3h, 3g of hydrofluoric acid (40wt%) was added. After stirring for 1h, the mixture was placed in a polytetrafluoroethylene-lined crystallization kettle and placed in an oven at 180°C for static crystallization for 156h. The solid after reaction was filtered, washed, dried, and calcined to obtain the final Al-TON molecular sieve product. The XRD spectrum data are shown in Table 3. The raw material composition of the synthesis of this molecular sieve is shown in Table 5.
[0053] Table 3
[0054]
[0055]
[0056] Example 5
[0057] 2.62g 3-diethylamino-1-propanol (DEAP) was mixed with 0.66g water, and 0.21g germanium oxide was added. After dissolving, 6g Ludox silica sol (SiO2 40wt%) was slowly added under stirring. After stirring for 3h at room temperature, 1g hydrofluoric acid (40wt%) and 2g hydrofluoric acid (37wt%) were added. After stirring for 1 hour, the mixture was placed in a crystallization kettle with a polytetrafluoroethylene lining and placed in a 165℃ oven for static crystallization for 168 hours. The solid after reaction was filtered, washed, dried and calcined to obtain the final TON molecular sieve product. The XRD pattern was consistent with that of the TON molecular sieve. Figure 1 The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0058] Example 6
[0059] 5.25g 3-diethylamino-1-propanol (DEAP) was mixed evenly with 3.6g water, and 0.405g aluminum nitrate nonahydrate was added. After dissolving, 3g Ludox silica sol (SiO2 40wt%) and 1.27g white carbon black (SiO2 95wt%) were slowly added under stirring. After stirring at room temperature for 3h, 1g hydrofluoric acid (40wt%) and 2g hydrofluoric acid solution (37wt%) were added. After stirring for 1 hour, the above mixture was placed in a crystallization kettle with a polytetrafluoroethylene lining and placed in a 160℃ oven for static crystallization for 144 hours. The solid after reaction was filtered, washed, dried and calcined to obtain the final Fe-TON molecular sieve product. The XRD pattern was the same as that of the product. Figure 1 The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0060] Example 7
[0061] 3.93g of 3-diethylamino-1-propanol (DEAP) was mixed with 9.9g of water. 6g of Ludox silica sol (SiO2 40wt%) and 0.34g of tetrabutyl titanate were slowly added under stirring. After stirring at room temperature for 3h, 1.5g of hydrofluoric acid (40wt%) was added. After stirring for 1h, the mixture was placed in a polytetrafluoroethylene-lined crystallization kettle and placed in a 170°C oven for static crystallization for 168h. The solid after reaction was filtered, washed, dried, and calcined to obtain the final Ti-TON molecular sieve product. The XRD spectrum data are shown in Table 4. The raw material composition of the synthesized molecular sieve is shown in Table 5.
[0062] Table 4
[0063]
[0064] Example 8
[0065] 5.25g 3-diethylamino-1-propanol (DEAP) was mixed evenly with 9.8g water, and 0.204g titanium sulfate and 0.033g boric acid were added. After dissolution, 4g Ludox silica sol (SiO2 40wt%) and 0.84g white carbon black (SiO295wt%) were slowly added under stirring. After stirring at room temperature for 3h, 1.5g hydrofluoric acid (40wt%) and 2g hydrofluoric acid (37wt%) were added. After stirring for 1 hour, the above mixture was placed in a crystallization kettle with a polytetrafluoroethylene lining and placed in a 175℃ oven for static crystallization for 180 hours. The solid after reaction was filtered, washed, dried and calcined to obtain the final B-Ti-TON molecular sieve product. The XRD pattern was the same as that of the solid. Figure 1 The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0066] Example 9
[0067] 5.25g of 3-diethylamino-1-propanol (DEAP), 0.6g of water and 6g of Ludox silica sol (SiO2 40wt%) were mixed evenly and stirred at room temperature for 3h. Then 2g of hydrofluoric acid (40wt%) was added and stirred for 1h. The mixture was placed in a crystallization kettle lined with polytetrafluoroethylene and placed in a 170℃ oven for dynamic crystallization for 120h (30 rpm). The solid after reaction was filtered, washed, dried and calcined to obtain the final product, TON molecular sieve. The XRD pattern was consistent with that of the Figure 1 The composition of the raw materials for synthesizing the molecular sieve is shown in Table 5.
[0068] Table 5 Example molecular sieve raw material molar ratio composition
[0069]
[0070]
[0071] Where, X 1 Refers to a heteroatom element, X 2 refers to another miscellaneous element, and so on.
[0072] Comparative Example 1
[0073] 0.35g of aluminum sulfate 18-hydrate, 0.70g of potassium hydroxide, and 2.1g of 1,8-octanediamine were added to 30g of water and stirred to dissolve. 7.15g of Ludox silica sol (SiO2 40wt%) was then added. Stirring was continued for 30 minutes. The mixture was then placed in a polytetrafluoroethylene-lined crystallization kettle and placed in a 160°C oven (400 rpm) for dynamic crystallization for 72 hours. The resulting solid was filtered, washed, dried, and calcined to obtain the final product, TON molecular sieve containing a small amount of MEL impurities.
[0074] This comparative example shows that the traditional synthesis of TON molecular sieves requires high-speed stirring and is prone to the presence of impurities in the product. In the present invention, the synthesis of TON molecular sieves only requires static stirring and the product has high crystallinity and purity.
[0075] Comparative Example 2
[0076] 0.35g of aluminum sulfate 18-hydrate, 0.70g of potassium hydroxide, and 2.1g of 1,8-octanediamine were added to 30g of water and stirred to dissolve. 7.15g of Ludox silica sol (SiO2 40wt%) was then added. Stirring was continued for 30 minutes. The mixture was then placed in a polytetrafluoroethylene-lined crystallization kettle and statically crystallized in a 160°C oven for 72 hours. The resulting solid was filtered, washed, dried, and calcined to obtain the final product, MEL molecular sieve.
[0077] This comparative example shows that the traditional method for synthesizing TON molecular sieves in a static state is prone to failure and other products are obtained. In the present invention, the TON molecular sieve product synthesized in a static state has high crystallinity and purity and is simple to operate.
[0078] The preferred embodiments of the present invention have been described in detail above, but the present invention is not limited thereto. Within the technical concept of the present invention, various simple variations of the technical solution of the present invention may be made, including combining the various technical features in any other appropriate manner. These simple variations and combinations should also be regarded as disclosed in the present invention and fall within the scope of protection of the present invention.
Claims
1. A method for preparing TON molecular sieve, characterized in that: The method comprises: mixing a silicon source, a fluorine source, an organic template agent Q, water and an optional heteroatom element X source to carry out a crystallization reaction; the organic template agent is 3-diethylamino-1-propanol, the organic template agent Q, the silicon source calculated as SiO2, the XO m / 2 The molar ratio of the X source in terms of F, the fluorine source in terms of F and water is Q: SiO2: XO m / 2 : F: H2O= 0.15~4: 1: 0~0.05: 0.2~4: 5~30, m is the oxidation state of element X; The crystallization is performed under static conditions.
2. The preparation method according to claim 1, wherein The heteroatom element X is at least one selected from aluminum, boron, gallium, germanium, titanium, zirconium, hafnium, tin, zinc, iron, indium and chromium.
3. The preparation method according to claim 1, wherein Q: SiO2: XO m / 2 : F: H2O= 0.5~2: 1: 0.005~0.04: 0.35~2.5: 6~20。 4. The preparation method according to claim 1, wherein The silicon source is selected from at least one of water glass, silica sol, solid silica gel, fumed silica, amorphous silica, diatomaceous earth, zeolite molecular sieve and tetraalkoxysilane.
5. The preparation method according to claim 1, wherein The fluorine source is selected from at least one of hydrofluoric acid, ammonium fluoride, sodium fluoride and potassium fluoride.
6. The preparation method according to claim 5, wherein The fluorine source is selected from at least one of hydrofluoric acid and ammonium fluoride.
7. The preparation method according to claim 1, wherein The conditions of the crystallization reaction include: a crystallization temperature of 100 to 200°C; and / or The crystallization time is 24~300 hours.
8. The preparation method according to claim 7, wherein The conditions of the crystallization reaction include: a crystallization temperature of 110-190°C; and / or The crystallization time is 36~250 hours.
9. The preparation method according to claim 8, wherein The conditions of the crystallization reaction include: a crystallization temperature of 160-175°C; and / or The crystallization time is 120-180 hours.
10. The TON molecular sieve prepared by the preparation method according to any one of claims 1 to 9, wherein the TON molecular sieve has the formula: SiO2·1 / x XO m / 2 The schematic chemical composition shown, wherein, X is a heteroatom element, m is the oxidation state of element X, m =1~7, SiO2 / XO m / 2 The molar ratio x≥20.
11. The TON molecular sieve according to claim 10, wherein The TON molecular sieve is a needle-shaped crystal.
12. The TON molecular sieve according to claim 10 or 11, wherein The morphology of the TON molecular sieve is needle-like; and / or The X-ray diffraction pattern of the TON molecular sieve includes characteristic peaks as shown in the following table: 。 13. A TON molecular sieve composition, characterized in that The composition contains the TON molecular sieve according to any one of claims 10 to 12 and a binder.
14. Use of the TON molecular sieve according to any one of claims 10 to 12 or the TON molecular sieve composition according to claim 13 as an adsorbent or catalyst.
Citation Information
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