CN111233000B - A kind of synthetic method of low silicon aluminum ratio MTT type molecular sieve - Google Patents
A kind of synthetic method of low silicon aluminum ratio MTT type molecular sieve Download PDFInfo
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- 239000002808 molecular sieve Substances 0.000 title claims abstract description 57
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 57
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 title claims abstract description 13
- 238000010189 synthetic method Methods 0.000 title claims 3
- 239000000203 mixture Substances 0.000 claims abstract description 36
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 29
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 15
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 15
- 238000002425 crystallisation Methods 0.000 claims abstract description 13
- 230000008025 crystallization Effects 0.000 claims abstract description 13
- 238000001308 synthesis method Methods 0.000 claims abstract description 12
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 10
- 239000010703 silicon Substances 0.000 claims abstract description 10
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 9
- 239000002243 precursor Substances 0.000 claims abstract description 8
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 36
- 238000003756 stirring Methods 0.000 claims description 26
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 claims description 16
- 150000001412 amines Chemical class 0.000 claims description 13
- ZMXDDKWLCZADIW-UHFFFAOYSA-N N,N-Dimethylformamide Chemical compound CN(C)C=O ZMXDDKWLCZADIW-UHFFFAOYSA-N 0.000 claims description 12
- ROSDSFDQCJNGOL-UHFFFAOYSA-N Dimethylamine Chemical compound CNC ROSDSFDQCJNGOL-UHFFFAOYSA-N 0.000 claims description 10
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 10
- RWRDLPDLKQPQOW-UHFFFAOYSA-N Pyrrolidine Chemical compound C1CCNC1 RWRDLPDLKQPQOW-UHFFFAOYSA-N 0.000 claims description 9
- 239000011734 sodium Substances 0.000 claims description 9
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 7
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 7
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 5
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 4
- 238000001354 calcination Methods 0.000 claims description 4
- WGYKZJWCGVVSQN-UHFFFAOYSA-N propylamine Chemical compound CCCN WGYKZJWCGVVSQN-UHFFFAOYSA-N 0.000 claims description 4
- HQABUPZFAYXKJW-UHFFFAOYSA-N butan-1-amine Chemical compound CCCCN HQABUPZFAYXKJW-UHFFFAOYSA-N 0.000 claims description 3
- BNGXYYYYKUGPPF-UHFFFAOYSA-M (3-methylphenyl)methyl-triphenylphosphanium;chloride Chemical compound [Cl-].CC1=CC=CC(C[P+](C=2C=CC=CC=2)(C=2C=CC=CC=2)C=2C=CC=CC=2)=C1 BNGXYYYYKUGPPF-UHFFFAOYSA-M 0.000 claims description 2
- DGAQECJNVWCQMB-PUAWFVPOSA-M Ilexoside XXIX Chemical compound C[C@@H]1CC[C@@]2(CC[C@@]3(C(=CC[C@H]4[C@]3(CC[C@@H]5[C@@]4(CC[C@@H](C5(C)C)OS(=O)(=O)[O-])C)C)[C@@H]2[C@]1(C)O)C)C(=O)O[C@H]6[C@@H]([C@H]([C@@H]([C@H](O6)CO)O)O)O.[Na+] DGAQECJNVWCQMB-PUAWFVPOSA-M 0.000 claims description 2
- BPQQTUXANYXVAA-UHFFFAOYSA-N Orthosilicate Chemical compound [O-][Si]([O-])([O-])[O-] BPQQTUXANYXVAA-UHFFFAOYSA-N 0.000 claims description 2
- SMZOGRDCAXLAAR-UHFFFAOYSA-N aluminium isopropoxide Chemical compound [Al+3].CC(C)[O-].CC(C)[O-].CC(C)[O-] SMZOGRDCAXLAAR-UHFFFAOYSA-N 0.000 claims description 2
- VXAUWWUXCIMFIM-UHFFFAOYSA-M aluminum;oxygen(2-);hydroxide Chemical compound [OH-].[O-2].[Al+3] VXAUWWUXCIMFIM-UHFFFAOYSA-M 0.000 claims description 2
- 239000006229 carbon black Substances 0.000 claims description 2
- JJWLVOIRVHMVIS-UHFFFAOYSA-N isopropylamine Chemical compound CC(C)N JJWLVOIRVHMVIS-UHFFFAOYSA-N 0.000 claims description 2
- 235000019353 potassium silicate Nutrition 0.000 claims description 2
- 238000002360 preparation method Methods 0.000 claims description 2
- 229910052708 sodium Inorganic materials 0.000 claims description 2
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims description 2
- KKCBUQHMOMHUOY-UHFFFAOYSA-N Na2O Inorganic materials [O-2].[Na+].[Na+] KKCBUQHMOMHUOY-UHFFFAOYSA-N 0.000 claims 1
- 229910052681 coesite Inorganic materials 0.000 claims 1
- 229910052593 corundum Inorganic materials 0.000 claims 1
- 229910052906 cristobalite Inorganic materials 0.000 claims 1
- 239000000377 silicon dioxide Substances 0.000 claims 1
- 235000012239 silicon dioxide Nutrition 0.000 claims 1
- 229910052682 stishovite Inorganic materials 0.000 claims 1
- 229910052905 tridymite Inorganic materials 0.000 claims 1
- 229910001845 yogo sapphire Inorganic materials 0.000 claims 1
- 239000002253 acid Substances 0.000 abstract description 15
- 238000000034 method Methods 0.000 abstract description 13
- 239000000126 substance Substances 0.000 abstract description 4
- 239000003245 coal Substances 0.000 abstract description 3
- 238000010438 heat treatment Methods 0.000 abstract description 3
- 238000005504 petroleum refining Methods 0.000 abstract description 3
- 230000002194 synthesizing effect Effects 0.000 abstract description 2
- 238000002156 mixing Methods 0.000 abstract 1
- 238000006243 chemical reaction Methods 0.000 description 16
- 229910001220 stainless steel Inorganic materials 0.000 description 14
- 239000010935 stainless steel Substances 0.000 description 14
- 238000012512 characterization method Methods 0.000 description 9
- 239000008367 deionised water Substances 0.000 description 8
- 229910021641 deionized water Inorganic materials 0.000 description 8
- 239000011259 mixed solution Substances 0.000 description 6
- 229920001343 polytetrafluoroethylene Polymers 0.000 description 6
- 239000004810 polytetrafluoroethylene Substances 0.000 description 6
- -1 templates Substances 0.000 description 6
- 238000006555 catalytic reaction Methods 0.000 description 5
- 239000013078 crystal Substances 0.000 description 4
- 239000007864 aqueous solution Substances 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000003786 synthesis reaction Methods 0.000 description 3
- KDSNLYIMUZNERS-UHFFFAOYSA-N 2-methylpropanamine Chemical compound CC(C)CN KDSNLYIMUZNERS-UHFFFAOYSA-N 0.000 description 2
- 230000003197 catalytic effect Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 239000004809 Teflon Substances 0.000 description 1
- 229920006362 Teflon® Polymers 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003054 catalyst Substances 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- BFKJFAAPBSQJPD-UHFFFAOYSA-N tetrafluoroethene Chemical group FC(F)=C(F)F BFKJFAAPBSQJPD-UHFFFAOYSA-N 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C01—INORGANIC CHEMISTRY
- C01B—NON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
- C01B39/00—Compounds having molecular sieve and base-exchange properties, e.g. crystalline zeolites; Their preparation; After-treatment, e.g. ion-exchange or dealumination
- C01B39/02—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof
- C01B39/04—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof; Direct preparation thereof; Preparation thereof starting from a reaction mixture containing a crystalline zeolite of another type, or from preformed reactants; After-treatment thereof using at least one organic template directing agent, e.g. an ionic quaternary ammonium compound or an aminated compound
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- General Life Sciences & Earth Sciences (AREA)
- Geology (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
本发明涉及一种MTT型分子筛合成方法。该合成方法的具体实施步骤如下:将硅源、铝源、模板剂、水充分混合后,加热晶化一定时间制备前体混合物;向前体混合物中再加入一定的铝源、水,继续加热晶化一定时间制得低硅铝比MTT型分子筛。本发明制备的低硅铝比MTT型分子筛,其Si/Al可低至5,具有酸性强,酸量大的特点,在石油炼制与石油化工、煤化工等领域具有潜在的应用。本发明提供的合成方法成本低,操作安全简便,环境友好。The invention relates to a method for synthesizing an MTT molecular sieve. The specific implementation steps of the synthesis method are as follows: After fully mixing the silicon source, aluminum source, template agent, and water, heat and crystallize for a certain period of time to prepare a precursor mixture; add a certain amount of aluminum source and water to the precursor mixture, and continue heating Crystallization for a certain period of time to prepare MTT molecular sieves with low silicon-aluminum ratio. The low-silicon-aluminum ratio MTT molecular sieve prepared by the invention has a Si/Al ratio as low as 5, has the characteristics of strong acidity and large acid content, and has potential applications in petroleum refining, petrochemical, coal chemical and other fields. The synthesis method provided by the invention is low in cost, safe and convenient in operation, and environment-friendly.
Description
技术领域technical field
本发明涉及的是分子筛的合成方法,具体的涉及低硅铝比MTT型分子筛的合成方法。The invention relates to a synthesis method of a molecular sieve, in particular to a synthesis method of an MTT molecular sieve with a low silicon-aluminum ratio.
背景技术Background technique
沸石分子筛是一类无机晶体材料,具有独特的孔道结构、较大的比表面积、可以调控的酸性等特点,在石油炼制与石油化工、煤化工等领域具有广泛的应用。Zeolite molecular sieve is a kind of inorganic crystal material, which has the characteristics of unique pore structure, large specific surface area, and adjustable acidity. It is widely used in petroleum refining, petrochemical, coal chemical and other fields.
MTT型分子筛具有泪珠状十元环窗口的一维孔道,属于高硅分子筛。该结构的分子筛最早于20世纪70年代由C.J.Plank等最先合成得到。具有MTT结构的最具代表性的分子筛为ZSM-23,还有命名为KZ-1、ISI-4、EU-13、SSZ-32等分子筛。除了十元环的孔道窗口,ZSM-23分子筛的孔道直径为0.56nm×0.45nm,骨架中没有交叉的孔道。正是由于其独特的孔道结构能够满足一些反应对择形催化的要求,故而在许多催化反应中表现出优异的催化性能和潜在的应用价值。MTT-type molecular sieves have one-dimensional channels with teardrop-shaped ten-membered ring windows, and belong to high-silicon molecular sieves. Molecular sieves with this structure were first synthesized by C.J.Plank et al. in the 1970s. The most representative molecular sieve with MTT structure is ZSM-23, and there are also molecular sieves named KZ-1, ISI-4, EU-13, SSZ-32 and so on. Except for the channel window of the ten-membered ring, the channel diameter of ZSM-23 molecular sieve is 0.56nm×0.45nm, and there is no intersecting channel in the framework. It is precisely because its unique pore structure can meet the requirements of some reactions for shape-selective catalysis, so it shows excellent catalytic performance and potential application value in many catalytic reactions.
分子筛作用于酸催化反应过程中,其催化性能与酸性密切相关。分子筛酸量越多,催化剂活性越高,达到目标转化率所需要的温度越低。但是,在目前的文献报道中MTT型分子筛的Si/Al一般高于50,从而限制了其酸量的提高。通过使用特殊的模板剂,可以合成出一些低硅铝比的硅铝分子筛。比如,用于硅铝分子筛Corma等人利用在实验室合成的模板剂得到了Si/Al=12的MTW型分子筛(NewJ.Chem.,2016,40,4140);Jintao Li等人利用在实验合成的模板剂得到了Si/Al=8-23的MTW型分子筛(Catalysis Communications,50(2014),97–100)。这些合成低硅铝比硅铝分子筛的方法都需要用到实验室合成的模板剂,合成成本高,限制了其大规模的应用。开发低成本合成酸量多的MTT型分子筛方法,将可能拓展该类分子筛在酸催化反应中的进一步应用。Molecular sieves are used in acid-catalyzed reactions, and their catalytic performance is closely related to acidity. The more molecular sieve acid, the higher the catalyst activity, and the lower the temperature required to achieve the target conversion rate. However, in the current literature reports, the Si/Al of MTT molecular sieves is generally higher than 50, which limits the increase of its acid content. By using a special template agent, some silica-alumina molecular sieves with low silica-alumina ratio can be synthesized. For example, for silica-alumina molecular sieves, Corma et al. have obtained MTW molecular sieves with Si/Al=12 (NewJ.Chem., 2016, 40, 4140) using templates synthesized in the laboratory; Jintao Li et al. The template agent obtained Si/Al=8-23 MTW type molecular sieve (Catalysis Communications, 50 (2014), 97-100). These methods for synthesizing molecular sieves with low silicon-to-alumina ratio require the use of laboratory-synthesized templates, and the high synthesis cost limits their large-scale application. The development of low-cost synthesis of MTT-type molecular sieves with a large amount of acid will likely expand the further application of this type of molecular sieves in acid-catalyzed reactions.
发明内容Contents of the invention
本发明的目的是提供一种低硅铝比MTT型分子筛合成的新方法。The purpose of the present invention is to provide a new method for the synthesis of MTT molecular sieves with low silicon-aluminum ratio.
上述目的,通过以下技术方案实现:Above-mentioned purpose, realize through following technical scheme:
1)制备前体混合物:将硅源、铝源、氢氧化钠、有机胺、水按一定比例混合,搅拌至均匀,形成前体混合物A,A中Al2O3:SiO2:Na2O:有机胺:H2O摩尔比例为1:80-500:1-100:1-200:1000-8000(硅源、铝源、氢氧化钠均按照其氧化物形式计算);1) Preparation of precursor mixture: mix silicon source, aluminum source, sodium hydroxide, organic amine, and water in a certain proportion, stir until uniform, and form precursor mixture A, in A, Al 2 O 3 :SiO 2 :Na 2 O : Organic amine: H 2 O molar ratio is 1:80-500:1-100:1-200:1000-8000 (silicon source, aluminum source, sodium hydroxide are all calculated according to their oxide form);
2)将制得的前体混合物A于80℃-250℃条件下加热晶化5h-72h后,冷却至室温,得到混合物B;2) heating and crystallizing the prepared precursor mixture A at 80°C-250°C for 5h-72h, then cooling to room temperature to obtain mixture B;
3)向混合物B中加入一定量的铝源和水,搅拌至均匀,得到混合物C,C中Al2O3:SiO2:Na2O:有机胺:H2O摩尔比例为1:1-60:1-100:1-200:100-4000(硅源、铝源均按照其氧化物形式计算);3) Add a certain amount of aluminum source and water to mixture B, stir until uniform, and obtain mixture C, in which Al 2 O 3 :SiO 2 :Na 2 O:organic amine:H 2 O molar ratio is 1:1- 60:1-100:1-200:100-4000 (silicon source and aluminum source are calculated according to their oxide form);
4)将混合物C于100℃-250℃条件下加热晶化5h-120h;4) heating and crystallizing the mixture C at 100°C-250°C for 5h-120h;
5)晶化结束后,将混合物冷却至室温,过滤、洗涤并干燥,在300℃-600℃下焙烧5h-36h,得到的固体为低硅铝比MTT型分子筛。5) After the crystallization, the mixture is cooled to room temperature, filtered, washed and dried, and calcined at 300°C-600°C for 5h-36h, and the obtained solid is MTT molecular sieve with low silicon-aluminum ratio.
所述的方法,步骤1)中硅源为硅溶胶、水玻璃、白炭黑、正硅酸乙酯中的一种或二种以上;In the method, the silicon source in step 1) is one or more of silica sol, water glass, white carbon black, orthoethyl silicate;
所述的方法,步骤1)中铝源为异丙醇铝、偏铝酸钠、拟薄水铝石、硫酸铝、硝酸铝中的一种或二种以上;In the method, the aluminum source in step 1) is one or more of aluminum isopropoxide, sodium metaaluminate, pseudoboehmite, aluminum sulfate, and aluminum nitrate;
所述的方法,步骤1)中有机胺为二甲胺、N,N-二甲基甲酰胺、吡咯烷、正丙胺、异丙胺、正丁胺等中的一种或两种以上。In the method, the organic amine in step 1) is one or more of dimethylamine, N,N-dimethylformamide, pyrrolidine, n-propylamine, isopropylamine, n-butylamine and the like.
所述的方法,步骤1)混合物A中Al2O3:SiO2:Na2O:有机胺:H2O摩尔比例为1:80-200:1-50:1-100:3000-6000。In the method, step 1) in the mixture A, the molar ratio of Al 2 O 3 :SiO 2 :Na 2 O:organic amine:H 2 O is 1:80-200:1-50:1-100:3000-6000.
所述的方法,步骤2)混合物A优选的晶化温度为100℃-200℃;优选的晶化时间为10h-48h。In the method, step 2) the preferred crystallization temperature of mixture A is 100°C-200°C; the preferred crystallization time is 10h-48h.
所述的方法,步骤3)混合物C中Al2O3:SiO2:Na2O:有机胺:H2O摩尔比例为1:10-40:1-30:1-50:200-2000。In the method, step 3) the molar ratio of Al 2 O 3 :SiO 2 :Na 2 O:organic amine:H 2 O in the mixture C is 1:10-40:1-30:1-50:200-2000.
所述的方法,步骤4)混合物C优选的晶化温度为100℃-200℃;优选的晶化时间为12h-100h。In the method, step 4) the preferred crystallization temperature of mixture C is 100°C-200°C; the preferred crystallization time is 12h-100h.
所述的方法,步骤5)中优选的焙烧温度为450℃-550℃;优选的焙烧时间为12h-24h。In the method, the preferred calcination temperature in step 5) is 450°C-550°C; the preferred calcination time is 12h-24h.
硅源、铝源、模板剂在一定温度晶化一定时间后生成低结晶度的MTT型分子筛,此时该体系除了含有低结晶度MTT型分子筛,还含有硅铝无定形物质、模板剂和水。向此体系中再加入铝源后,低结晶度的MTT型分子筛起到晶种的作用,在一定温度晶化过程中,所加入的铝源在晶种的作用下,更容易进入分子筛中,导致更多的铝进入到分子筛骨架,晶化结束后制得低硅铝比MTT型分子筛。The silicon source, the aluminum source, and the template are crystallized at a certain temperature for a certain period of time to form a low-crystallinity MTT molecular sieve. At this time, the system not only contains a low-crystallinity MTT molecular sieve, but also contains silicon-aluminum amorphous substances, templates, and water. . After the aluminum source is added to this system, the MTT molecular sieve with low crystallinity acts as a seed crystal. During the crystallization process at a certain temperature, the added aluminum source is more likely to enter the molecular sieve under the action of the seed crystal. As a result, more aluminum enters into the molecular sieve framework, and after crystallization, MTT molecular sieves with low silicon-aluminum ratio are produced.
与现有技术合成的MTT型分子筛相比,本发明的MTT型分子筛合成方法具有以下特点:Compared with the MTT type molecular sieve synthesized by the prior art, the MTT type molecular sieve synthesis method of the present invention has the following characteristics:
(1)提供了一种低硅铝比MTT型分子筛合成的新方法。(1) A new synthesis method for MTT molecular sieves with low silicon-aluminum ratio is provided.
(2)制得的MTT型分子筛具有较多的酸量。(2) The prepared MTT molecular sieve has more acid content.
(3)本合成方法成本低,只需利用商业化的模板剂合成,操作简便,具有较强的经济性。(3) The synthesis method is low in cost, only needs to be synthesized by using a commercial template, and is easy to operate and has strong economic efficiency.
具体实施方式Detailed ways
下面结合具体实施例对本发明作进一步的说明,但需要指出的是,本发明内容并不局限于此。The present invention will be further described below in conjunction with specific examples, but it should be pointed out that the content of the present invention is not limited thereto.
对比例1Comparative example 1
称取氢氧化钠11.9g,二甲胺(40%水溶液)56.8g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入175℃烘箱,晶化4天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 56.8g of dimethylamine (40% aqueous solution), 3.7g of aluminum sulfate, add 256g of water, and after fully stirring, add 100g of 30% silica sol to it, after stirring evenly, move the mixed solution into Put it into a polytetrafluoroethylene-lined stainless steel reaction kettle, put it in an oven at 175°C, crystallize for 4 days, cool to room temperature, wash with deionized water for 3 times, dry it in an oven at 120°C, and bake at 550°C for 12 hours. MTT molecular sieves were prepared. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
对比例2Comparative example 2
称取氢氧化钠11.9g,二甲胺(40%水溶液)56.8g,11.1g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入175℃烘箱,晶化4天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得无定型产物,未得到MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 56.8g of dimethylamine (40% aqueous solution), 11.1g of aluminum sulfate, add 256g of water, and after fully stirring, add 100g of 30% silica sol to it, after stirring evenly, move the mixed solution into Put it into a polytetrafluoroethylene-lined stainless steel reaction kettle, put it in an oven at 175°C, crystallize for 4 days, cool to room temperature, wash with deionized water for 3 times, dry it in an oven at 120°C, and bake at 550°C for 12 hours. Amorphous products were obtained, and MTT molecular sieves were not obtained. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
实施例1Example 1
称取氢氧化钠11.9g,二甲胺(40%水溶液)56.8g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入170℃烘箱,保持1天,冷却至室温取出后,再向其中加入7.4g硫酸铝和水18g,搅拌均匀后将混合液再移入到聚四氟乙烯内衬的不锈钢反应釜中,升温至175℃保持2天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 56.8g of dimethylamine (40% aqueous solution), 3.7g of aluminum sulfate, add 256g of water, and after fully stirring, add 100g of 30% silica sol to it, after stirring evenly, move the mixed solution into Put it into a polytetrafluoroethylene-lined stainless steel reaction kettle, put it in an oven at 170°C, keep it for 1 day, cool to room temperature and take it out, then add 7.4g of aluminum sulfate and 18g of water to it, stir the mixture evenly, and then transfer it to the In a polytetrafluoroethylene-lined stainless steel reaction kettle, heat up to 175°C and keep it for 2 days, then cool to room temperature, wash with deionized water for 3 times, dry in an oven at 120°C, and roast at 550°C for 12 hours to obtain MTT type Molecular sieve. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
实施例2Example 2
称取氢氧化钠11.9g,吡咯烷35.6g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入170℃烘箱,保持1天,冷却至室温取出后,再向其中加入9.6g硫酸铝和水18g,搅拌均匀后将混合液再移入到聚四氟乙烯内衬的不锈钢反应釜中,升温至175℃保持2天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 35.6g of pyrrolidine, 3.7g of aluminum sulfate, add 256g of water, and after stirring fully, add 100g of 30% silica sol to it, after stirring evenly, transfer the mixed solution into polytetrafluoroethylene Put it into a lined stainless steel reaction kettle, put it in an oven at 170°C, keep it for 1 day, cool it to room temperature, take it out, add 9.6g of aluminum sulfate and 18g of water into it, stir it evenly, and then transfer the mixture to the Teflon liner In a stainless steel reaction kettle, the temperature was raised to 175 ° C for 2 days, cooled to room temperature, washed with deionized water for 3 times, dried in an oven at 120 ° C, and roasted at 550 ° C for 12 hours to obtain MTT molecular sieves. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
实施例3Example 3
称取氢氧化钠11.9g,N,N-二甲基甲酰胺36.5g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入175℃烘箱,保持10h,冷却至室温取出后,再向其中加入11.1g硫酸铝和水18g,搅拌均匀后将混合液再移入到聚四氟乙烯内衬的不锈钢反应釜中,升温至175℃保持2天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 36.5g of N,N-dimethylformamide, 3.7g of aluminum sulfate, add 256g of water, stir well, add 100g of 30% silica sol to it, stir evenly, and mix Move it into a polytetrafluoroethylene-lined stainless steel reaction kettle, put it in an oven at 175°C, keep it for 10 hours, cool it to room temperature and take it out, then add 11.1g of aluminum sulfate and 18g of water to it, stir it evenly, and then move the mixture into the In a polytetrafluoroethylene-lined stainless steel reaction kettle, heat up to 175°C and keep it for 2 days, then cool to room temperature, wash with deionized water for 3 times, dry in an oven at 120°C, and roast at 550°C for 12 hours to obtain MTT type Molecular sieve. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
实施例4Example 4
称取氢氧化钠11.9g,N,N-二甲基甲酰胺36.5g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入175℃烘箱,保持18h,冷却至室温取出后,再向其中加入13g硫酸铝和水18g,搅拌均匀后将混合液再移入到聚四氟乙烯内衬的不锈钢反应釜中,升温至175℃保持2天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 36.5g of N,N-dimethylformamide, 3.7g of aluminum sulfate, add 256g of water, stir well, add 100g of 30% silica sol to it, stir evenly, and mix Move it into a polytetrafluoroethylene-lined stainless steel reaction kettle, put it in an oven at 175°C, and keep it for 18 hours. After cooling to room temperature and taking it out, add 13g of aluminum sulfate and 18g of water to it, stir evenly, and then move the mixture into a polytetrafluoroethylene In a stainless steel reaction kettle lined with tetrafluoroethylene, the temperature was raised to 175°C and kept for 2 days, then cooled to room temperature, washed with deionized water for 3 times, dried in an oven at 120°C, and roasted at 550°C for 12 hours to obtain MTT molecular sieves. . The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
实施例5Example 5
称取氢氧化钠11.9g,异丁胺36.5g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入175℃烘箱,保持30h,冷却至室温取出后,再向其中加入29.6g硫酸铝和水36g,搅拌均匀后将混合液再移入到聚四氟乙烯内衬的不锈钢反应釜中,升温至175℃保持30h后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 36.5g of isobutylamine, 3.7g of aluminum sulfate, add 256g of water, and after fully stirring, add 100g of 30% silica sol to it, after stirring evenly, transfer the mixed solution into polytetrafluoroethylene Put it into a lined stainless steel reaction kettle, put it in an oven at 175°C, keep it for 30 hours, cool it to room temperature and take it out, then add 29.6g of aluminum sulfate and 36g of water into it, stir it evenly, and then transfer the mixture to the PTFE liner In a stainless steel reaction kettle, the temperature was raised to 175 ° C for 30 h, cooled to room temperature, washed with deionized water for 3 times, dried in an oven at 120 ° C, and roasted at 550 ° C for 12 h to obtain MTT molecular sieves. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
实施例6Example 6
称取氢氧化钠11.9g,正丁胺36.5g,3.7g硫酸铝,加入256g水,充分搅拌后,向其中加入30%的硅溶胶100g,搅拌均匀后,将混合液移入到聚四氟乙烯内衬的不锈钢反应釜中,放入170℃烘箱,保持30h,冷却至室温取出后,再向其中加入62.9g硫酸铝和水36g,搅拌均匀后将混合液再移入到聚四氟乙烯内衬的不锈钢反应釜中,升温至175℃保持2天后,冷却至室温,用去离子水洗涤3次后置于120℃烘箱中干燥,经过550℃焙烧12h,制得MTT型分子筛。所得MTT型分子筛的Si/Al、酸量表征结果汇总于表1。Weigh 11.9g of sodium hydroxide, 36.5g of n-butylamine, 3.7g of aluminum sulfate, add 256g of water, after fully stirring, add 100g of 30% silica sol to it, after stirring evenly, transfer the mixed solution into polytetrafluoroethylene In the lined stainless steel reaction kettle, put it in an oven at 170°C and keep it for 30 hours. After cooling to room temperature, take it out, then add 62.9g of aluminum sulfate and 36g of water into it, stir it evenly, and then transfer the mixture to the polytetrafluoroethylene lining In a stainless steel reaction kettle, the temperature was raised to 175 ° C for 2 days, cooled to room temperature, washed with deionized water for 3 times, dried in an oven at 120 ° C, and roasted at 550 ° C for 12 hours to obtain MTT molecular sieves. The Si/Al and acid content characterization results of the obtained MTT molecular sieves are summarized in Table 1.
表1对比例和实施例所得分子筛晶型、Si/Al、酸量表征结果The characterization results of molecular sieve crystal form, Si/Al and acid content obtained in Table 1 Comparative Examples and Examples
本发明制备的低硅铝比MTT型分子筛,其Si/Al可低至5,具有酸性强,酸量大的特点,在石油炼制与石油化工、煤化工等领域具有潜在的应用。本发明提供的合成方法成本低,操作安全简便,环境友好。The low silicon-aluminum ratio MTT molecular sieve prepared by the invention has a Si/Al ratio as low as 5, has the characteristics of strong acidity and large acid content, and has potential applications in petroleum refining, petrochemical, coal chemical and other fields. The synthesis method provided by the invention has the advantages of low cost, safe and convenient operation, and environmental friendliness.
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