CN116161674B - Hydrothermal preparation method of nano Ti-Beta molecular sieve - Google Patents
Hydrothermal preparation method of nano Ti-Beta molecular sieve Download PDFInfo
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- 239000002808 molecular sieve Substances 0.000 title claims abstract description 53
- 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 53
- 238000002360 preparation method Methods 0.000 title claims abstract description 12
- 238000000034 method Methods 0.000 claims abstract description 31
- 239000010936 titanium Substances 0.000 claims abstract description 29
- RTAQQCXQSZGOHL-UHFFFAOYSA-N Titanium Chemical compound [Ti] RTAQQCXQSZGOHL-UHFFFAOYSA-N 0.000 claims abstract description 26
- 229910052719 titanium Inorganic materials 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 27
- 239000000843 powder Substances 0.000 claims description 20
- 229910001868 water Inorganic materials 0.000 claims description 20
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims description 19
- 229910052710 silicon Inorganic materials 0.000 claims description 19
- 239000010703 silicon Substances 0.000 claims description 19
- 239000008367 deionised water Substances 0.000 claims description 12
- 229910021641 deionized water Inorganic materials 0.000 claims description 12
- 239000000443 aerosol Substances 0.000 claims description 11
- 238000001354 calcination Methods 0.000 claims description 11
- UGACIEPFGXRWCH-UHFFFAOYSA-N [Si].[Ti] Chemical compound [Si].[Ti] UGACIEPFGXRWCH-UHFFFAOYSA-N 0.000 claims description 10
- 238000001035 drying Methods 0.000 claims description 9
- 239000007788 liquid Substances 0.000 claims description 9
- 239000012686 silicon precursor Substances 0.000 claims description 8
- 239000007787 solid Substances 0.000 claims description 8
- 229940073455 tetraethylammonium hydroxide Drugs 0.000 claims description 7
- LRGJRHZIDJQFCL-UHFFFAOYSA-M tetraethylazanium;hydroxide Chemical compound [OH-].CC[N+](CC)(CC)CC LRGJRHZIDJQFCL-UHFFFAOYSA-M 0.000 claims description 7
- 238000005406 washing Methods 0.000 claims description 7
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 5
- BOTDANWDWHJENH-UHFFFAOYSA-N Tetraethyl orthosilicate Chemical group CCO[Si](OCC)(OCC)OCC BOTDANWDWHJENH-UHFFFAOYSA-N 0.000 claims description 5
- 229910010413 TiO 2 Inorganic materials 0.000 claims description 3
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 3
- 239000013078 crystal Substances 0.000 claims description 2
- 238000001704 evaporation Methods 0.000 claims description 2
- 239000000203 mixture Substances 0.000 claims 2
- 238000002156 mixing Methods 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 239000002243 precursor Substances 0.000 abstract description 16
- 230000015572 biosynthetic process Effects 0.000 abstract description 12
- 238000003786 synthesis reaction Methods 0.000 abstract description 12
- 238000001308 synthesis method Methods 0.000 abstract description 6
- 238000009826 distribution Methods 0.000 abstract description 5
- 230000002194 synthesizing effect Effects 0.000 abstract description 5
- 239000003795 chemical substances by application Substances 0.000 abstract description 4
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 abstract description 2
- 238000003912 environmental pollution Methods 0.000 abstract description 2
- 238000005265 energy consumption Methods 0.000 abstract 1
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 24
- 238000002425 crystallisation Methods 0.000 description 16
- 230000008025 crystallization Effects 0.000 description 16
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 13
- 229910052681 coesite Inorganic materials 0.000 description 12
- 229910052906 cristobalite Inorganic materials 0.000 description 12
- 239000000377 silicon dioxide Substances 0.000 description 12
- 235000012239 silicon dioxide Nutrition 0.000 description 12
- 229910052682 stishovite Inorganic materials 0.000 description 12
- 229910052905 tridymite Inorganic materials 0.000 description 12
- 238000001027 hydrothermal synthesis Methods 0.000 description 8
- 238000004821 distillation Methods 0.000 description 6
- 239000000047 product Substances 0.000 description 5
- 239000002253 acid Substances 0.000 description 3
- 238000012512 characterization method Methods 0.000 description 3
- 238000001228 spectrum Methods 0.000 description 3
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 description 2
- 101100012902 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) FIG2 gene Proteins 0.000 description 2
- 238000002441 X-ray diffraction Methods 0.000 description 2
- 229910021536 Zeolite Inorganic materials 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 238000003837 high-temperature calcination Methods 0.000 description 2
- 238000010348 incorporation Methods 0.000 description 2
- 239000004005 microsphere Substances 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000002371 ultraviolet--visible spectrum Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 1
- 101001121408 Homo sapiens L-amino-acid oxidase Proteins 0.000 description 1
- 102100026388 L-amino-acid oxidase Human genes 0.000 description 1
- 101100233916 Saccharomyces cerevisiae (strain ATCC 204508 / S288c) KAR5 gene Proteins 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- YHWCPXVTRSHPNY-UHFFFAOYSA-N butan-1-olate;titanium(4+) Chemical compound [Ti+4].CCCC[O-].CCCC[O-].CCCC[O-].CCCC[O-] YHWCPXVTRSHPNY-UHFFFAOYSA-N 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 239000012141 concentrate Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000006735 epoxidation reaction Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 229910052731 fluorine Inorganic materials 0.000 description 1
- 239000011737 fluorine Substances 0.000 description 1
- 239000003292 glue Substances 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 230000001590 oxidative effect Effects 0.000 description 1
- 238000000634 powder X-ray diffraction Methods 0.000 description 1
- 238000001556 precipitation Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 238000001878 scanning electron micrograph Methods 0.000 description 1
- 239000011734 sodium Substances 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000001694 spray drying Methods 0.000 description 1
- 230000003068 static effect Effects 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
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- 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
- C01B39/06—Preparation of isomorphous zeolites characterised by measures to replace the aluminium or silicon atoms in the lattice framework by atoms of other elements, i.e. by direct or secondary synthesis
- C01B39/08—Preparation of isomorphous zeolites characterised by measures to replace the aluminium or silicon atoms in the lattice framework by atoms of other elements, i.e. by direct or secondary synthesis the aluminium atoms being wholly replaced
- C01B39/085—Group IVB- metallosilicates
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Abstract
本发明公开了一种纳米Ti‑Beta分子筛的水热制备方法。本发明的方法是一种通过制备前体来一步水热直接快速合成性能优异的Ti‑Beta分子筛,与直接合成Ti‑Beta分子筛的传统方法相比,该方法模板剂用量小,合成时间短,且无需添加氟化物,可有效减少能源消耗和环境污染。此外,所得Ti‑Beta分子筛具有良好的钛分布。本发明提供的合成方法快速简单,可重复性强,与已有方法相比具有显著的技术先进性。
The present invention discloses a hydrothermal preparation method of nano Ti-Beta molecular sieve. The method of the present invention is a one-step hydrothermal direct and rapid synthesis of Ti-Beta molecular sieves with excellent performance by preparing a precursor. Compared with the traditional method of directly synthesizing Ti-Beta molecular sieves, the method has a small amount of template agent, a short synthesis time, and no need to add fluoride, which can effectively reduce energy consumption and environmental pollution. In addition, the obtained Ti-Beta molecular sieve has a good titanium distribution. The synthesis method provided by the present invention is fast and simple, has strong repeatability, and has significant technical advancement compared with existing methods.
Description
技术领域Technical Field
本发明涉及一种制备Ti-Beta分子筛的新方法,具体来说本发明是一种通过制备前体来一步水热直接快速合成性能优异的Ti-Beta分子筛。The invention relates to a new method for preparing Ti-Beta molecular sieve, and specifically to a method for directly and rapidly synthesizing Ti-Beta molecular sieve with excellent performance in one step by preparing a precursor through hydrothermal method.
背景技术Background Art
Ti-Beta是具有0.77x0.67nm孔直径的十二元环直通道结构的分子筛,因其硅铝比范围大、孔道大、酸位点丰富、稳定性好等特点,在环氧化、醇选择性氧化、氧化脱硫等领域都具有广阔的应用前景。目前为止,Ti-Beta分子筛的制备方法主要有水热合成法,凝胶合成法,后合成法。Ti-Beta is a molecular sieve with a twelve-membered ring straight channel structure with a pore diameter of 0.77x0.67nm. Due to its wide range of silicon-aluminum ratios, large pores, abundant acid sites, and good stability, it has broad application prospects in the fields of epoxidation, alcohol selective oxidation, and oxidative desulfurization. So far, the preparation methods of Ti-Beta molecular sieves mainly include hydrothermal synthesis, gel synthesis, and post-synthesis.
Blasco T等分别在有晶种(Chem.Commun,1996,20,2367-368.)与无晶种(J.Phys.Chem.B,1998,102(1):75-88)条件下水热合成了Ti-Beta分子筛:在晶化体系中加入硅源、钛源、去离子水以及模板剂等,在一定温度下晶化一定的时间得到最终产物。在Ti-Beta的水热合成方法中,晶化体系大致可分为含氟体系与羟基体系(高PH)。使用含氟化合物作矿化剂的中性环境晶化,不需要晶种导向,也无需含铝物质的添加。但所合成分子筛晶粒较大、矿化剂的毒性对环境会造成极大负担。羟基体系强碱性条件下的水热合成则晶种与含铝物质二者至少取其一,而铝会引入B酸酸位,影响催化性能。此外,传统水热法具有模板剂用量大、晶化废液排放量大,晶化时间长等弊端,需要进一步改进。Blasco T et al. hydrothermally synthesized Ti-Beta molecular sieve under the conditions of seeding (Chem. Commun, 1996, 20, 2367-368.) and seeding-free (J. Phys. Chem. B, 1998, 102 (1): 75-88): silicon source, titanium source, deionized water and template agent were added to the crystallization system, and the final product was obtained by crystallization at a certain temperature and for a certain period of time. In the hydrothermal synthesis method of Ti-Beta, the crystallization system can be roughly divided into a fluorine-containing system and a hydroxyl system (high pH). Crystallization in a neutral environment using fluorine-containing compounds as mineralizers does not require seeding guidance or the addition of aluminum-containing substances. However, the synthesized molecular sieve has large grains and the toxicity of the mineralizer will cause a great burden on the environment. In the hydrothermal synthesis under the strong alkaline conditions of the hydroxyl system, at least one of the seed and the aluminum-containing substance is selected, and aluminum will introduce B acid sites, affecting the catalytic performance. In addition, the traditional hydrothermal method has disadvantages such as large amount of template used, large amount of crystallization waste liquid discharged, and long crystallization time, which need further improvement.
Camblor M A等(catalysis.A,General,1995,133(2):L185-L189)使用“湿”凝胶制备Ti-Beta分子筛:首先制备出TiO2-SiO2凝胶,再用模板导向剂浸渍,最后晶化合成Ti-Beta分子筛。此方法晶化过程同样需要铝或含铝晶种的加入,仍排出大量废液,晶化时间需一周以上。Jappar N等(Journal of catalysis,1998,180(2):132-141.)首次使用干胶法制备Ti-Beta分子筛。该方法凝胶粉末与水不直接接触,而是转移到特制晶化釜中,利用水蒸气辅助作用合成Ti-Beta分子筛。此干胶方法不光需添加铝,还必须添加少量钠,而钠含量会影响分子筛的结晶度与Ti的掺入量。干胶法虽然模板剂用量与废液产量少于水热法,但它合成晶粒较大(微米级别),重复性较差,尚未有工业应用。。Camblor MA et al. (catalysis. A, General, 1995, 133 (2): L185-L189) used "wet" gel to prepare Ti-Beta molecular sieve: first, TiO 2 -SiO 2 gel was prepared, then impregnated with a template directing agent, and finally crystallized to synthesize Ti-Beta molecular sieve. This method also requires the addition of aluminum or aluminum-containing seed crystals during the crystallization process, and still discharges a large amount of waste liquid. The crystallization time requires more than one week. Jappar N et al. (Journal of catalysis, 1998, 180 (2): 132-141.) used the dry gel method to prepare Ti-Beta molecular sieve for the first time. In this method, the gel powder is not in direct contact with water, but is transferred to a special crystallization kettle, and the Ti-Beta molecular sieve is synthesized using the auxiliary effect of water vapor. This dry gel method requires not only the addition of aluminum, but also a small amount of sodium, and the sodium content will affect the crystallinity of the molecular sieve and the amount of Ti incorporated. Although the amount of template used and the amount of waste liquid produced by the dry glue method are less than those of the hydrothermal method, its synthesized grains are larger (micrometer level) and its repeatability is poor, so it has not yet been applied in industry.
后合成法即通过将Beta沸石脱铝、掺钛两步来合成Ti-Beta分子筛,目前大致分为气固、固固、液固同晶取代的方式来制备。后合成方法普遍合成时间短,基本在1-2天内即可制备Ti-Beta分子筛。The post-synthesis method is to synthesize Ti-Beta molecular sieve by dealuminizing Beta zeolite and doping titanium in two steps. At present, it is roughly divided into gas-solid, solid-solid, and liquid-solid isomorphous substitution methods. The post-synthesis method generally has a short synthesis time, and Ti-Beta molecular sieve can be prepared in 1-2 days.
将Ti掺入Beta沸石骨架难度远比TS-1要高,因此,Ti-Beta的晶化与骨架钛的掺入量是工业化生产要面临的两个关键问题。水热法与凝胶法的晶化时间均在7-14天,且它们的骨架钛掺入量有限。后合成法用时短、钛掺入量高是它的优势,但无论采用哪种后合成方法,都难以控制钛的配位状态,有大量非骨架钛与锐钛矿的存在;另外缺陷位不能被完全占据,导致B酸的生成,影响催化性能。It is much more difficult to incorporate Ti into the framework of Beta zeolite than TS-1. Therefore, the crystallization of Ti-Beta and the amount of titanium incorporated into the framework are two key issues faced by industrial production. The crystallization time of the hydrothermal method and the gel method is 7-14 days, and their framework titanium incorporation is limited. The advantages of the post-synthesis method are its short time and high titanium incorporation, but no matter which post-synthesis method is used, it is difficult to control the coordination state of titanium, and there is a large amount of non-framework titanium and anatase; in addition, the defect sites cannot be completely occupied, resulting in the formation of B acid, which affects the catalytic performance.
因此,能够针对现有工艺的不足,研究新的Ti-Beta制备方法具有重要的现实意义。Therefore, it is of great practical significance to study new Ti-Beta preparation methods in view of the shortcomings of existing processes.
发明内容Summary of the invention
本发明的目的是提供一种步骤简单、耗时短、无需额外添加氟化物和铝源,且钛物种分布好的制备方法水热合成纳米Ti-Beta分子筛。The purpose of the present invention is to provide a preparation method for hydrothermally synthesizing nano Ti-Beta molecular sieves with simple steps, short time consumption, no need for additional addition of fluoride and aluminum source, and good distribution of titanium species.
一种纳米Ti-Beta分子筛的水热制备方法,该方法包含以下步骤:A hydrothermal preparation method of nano Ti-Beta molecular sieve, the method comprising the following steps:
(1)硅源以SiO2计,钛源以TiO2计,按照SiO2:TiO2:H2O:HCl=1:0.01~0.05:20~80:0.033~0.135的摩尔比充分混合,室温搅拌20min;之后将溶液使用气溶胶发生器在220℃下,经过喷雾干燥得到钛硅前驱体粉末;(1) The silicon source is calculated as SiO 2 , and the titanium source is calculated as TiO 2 , and the molar ratio of SiO 2 :TiO 2 :H 2 O:HCl=1:0.01-0.05:20-80:0.033-0.135 is fully mixed, and stirred at room temperature for 20 minutes; then the solution is spray-dried at 220° C. using an aerosol generator to obtain a titanium silicon precursor powder;
(2)将钛硅前驱体粉末在550℃温度条件下焙烧3~6h得到固体粉末;加入模板剂四乙基氢氧化铵,然后加入相当于硅源质量2%~5%的Beta分子筛晶种,将混合液体在60~80℃水浴锅中蒸水浓缩,达到摩尔比为SiO2:TiO2:H2O:TEAOH=1:0.01~0.05:3~10:0.2~0.55;(2) calcining the titanium silicon precursor powder at 550°C for 3-6 hours to obtain a solid powder; adding a template agent, tetraethylammonium hydroxide, and then adding Beta molecular sieve seeds equivalent to 2%-5% of the mass of the silicon source, and distilling and concentrating the mixed liquid in a water bath at 60-80°C to achieve a molar ratio of SiO2 : TiO2 : H2O :TEAOH=1:0.01-0.05:3-10:0.2-0.55;
(3)将得到的浑浊液移至高压釜内,于130~150℃晶化3~7d,经去离子水洗涤、干燥、煅烧后得到Ti-Beta分子筛。(3) The obtained turbid liquid is transferred to an autoclave and crystallized at 130-150° C. for 3-7 days. After washing with deionized water, drying and calcining, a Ti-Beta molecular sieve is obtained.
步骤1中,所用硅源为正硅酸四乙酯或硅溶胶。所用钛源为钛酸四正丁酯。In step 1, the silicon source used is tetraethyl orthosilicate or silica sol, and the titanium source used is tetra-n-butyl titanate.
步骤3中,干燥温度为110℃,焙烧温度为550℃,焙烧时间为6h。In step 3, the drying temperature is 110° C., the calcination temperature is 550° C., and the calcination time is 6 h.
本发明的有益效果:Beneficial effects of the present invention:
与现有的Ti-Beta分子筛制备技术相比,该方法具有以下显著优点:Compared with the existing Ti-Beta molecular sieve preparation technology, this method has the following significant advantages:
a.本发明的特殊前体制备方法:在酸性条件下将硅源和钛源进行水解,通过气溶胶喷雾干燥与高温焙烧相结合的方式制备钛硅微球前体,在晶化前就有效调控了钛物种的配位状态,解决了Ti-Beta分子筛合成的首要难题;将钛硅微球前体用模板剂溶解,合适的配比是能否合成的关键所在。此外见步骤2,市面可购四乙基氢氧化铵浓度在25%~35%,无法达到此方法配比要求,故需要额外蒸发水量;而工业化可采用百分之九十以上浓度的模板剂,用本方法同样可找到合理配比,且省去蒸水浓缩步骤,合成路径可进一步简化。气溶胶前体经高温焙烧处理,以达到减少合成水量、消除前体中酸量影响、优化钛分布的目的。a. The special precursor preparation method of the present invention: hydrolyze the silicon source and the titanium source under acidic conditions, and prepare the titanium silicon microsphere precursor by combining aerosol spray drying with high temperature calcination. The coordination state of the titanium species is effectively regulated before crystallization, solving the primary problem of Ti-Beta molecular sieve synthesis; the titanium silicon microsphere precursor is dissolved with a template agent, and the appropriate ratio is the key to whether it can be synthesized. In addition, see step 2, the concentration of tetraethylammonium hydroxide available on the market is 25% to 35%, which cannot meet the ratio requirements of this method, so additional water evaporation is required; and industrialization can use a template agent with a concentration of more than 90%. The method can also find a reasonable ratio, and the water distillation and concentration step is omitted, and the synthesis path can be further simplified. The aerosol precursor is treated with high temperature calcination to achieve the purpose of reducing the amount of synthesis water, eliminating the influence of the acid content in the precursor, and optimizing the titanium distribution.
b.本方法水热合成Ti-Beta分子筛,对钛源硅源无需做额外处理,合成过程简洁便利,各个环节对条件并无苛刻要求,可重复性很强。此外,该方法的晶化时间明显少于传统水热法。b. The hydrothermal synthesis of Ti-Beta molecular sieve by this method does not require additional treatment of the titanium source and silicon source. The synthesis process is simple and convenient, and there are no stringent requirements for conditions in each link, and the repeatability is very strong. In addition, the crystallization time of this method is significantly shorter than that of the traditional hydrothermal method.
c.本合成方法不额外添加氟源、铝源和碱金属(Na),最大限度降低资源浪费和环境污染。c. This synthesis method does not add additional fluorine source, aluminum source and alkali metal (Na), which minimizes resource waste and environmental pollution.
附图说明BRIEF DESCRIPTION OF THE DRAWINGS
图1和图3为实施例中XRD对发明合成的Ti-Beta分子筛表征结果。FIG. 1 and FIG. 3 are XRD characterization results of the Ti-Beta molecular sieve synthesized in the present invention in the examples.
图2为本发明合成的Ti-Beta分子筛钛物种调控对比的UV-vis图。FIG. 2 is a UV-vis graph showing the control comparison of titanium species of the Ti-Beta molecular sieve synthesized in the present invention.
图4为本发明合成的Ti-Beta分子筛的SEM图。FIG. 4 is a SEM image of the Ti-Beta molecular sieve synthesized in the present invention.
具体实施方式DETAILED DESCRIPTION
下面通过实施例详述本发明,但本发明并不局限于这些实施例。The present invention is described in detail below by way of examples, but the present invention is not limited to these examples.
以下实施例中晶化过程为本领域所公知的晶化过程,该晶化过程为静态晶化过程。The crystallization process in the following embodiments is a crystallization process known in the art, and the crystallization process is a static crystallization process.
以下实施例中所述的洗涤、干燥、焙烧方法为本领域技术人员所公知的方法。例如采用去离子水洗涤至PH为中性,在110℃下干燥3~10小时.The washing, drying and roasting methods described in the following examples are well known to those skilled in the art. For example, washing with deionized water until the pH is neutral, and drying at 110°C for 3 to 10 hours.
以下实施例中硅源的摩尔质量以SiO2计、钛源的摩尔质量以TiO2计、模板剂的摩尔质量以TEA+计,硅源的质量以所含的SiO2计。In the following examples, the molar mass of the silicon source is calculated as SiO2 , the molar mass of the titanium source is calculated as TiO2 , the molar mass of the template is calculated as TEA + , and the mass of the silicon source is calculated as the contained SiO2 .
实施例1Example 1
本实施例用于说明一种纳米Ti-Beta分子筛的制备方法。This example is used to illustrate a method for preparing nano-Ti-Beta molecular sieve.
将钛源、硅源(正硅酸四乙酯)、去离子水、盐酸按照SiO2:TiO2:H2O:HCl=1:0.016:20:0.135的摩尔比充分混合,室温搅拌20min;之后将溶液使用气溶胶发生器在220℃下,经过喷雾干燥得到钛硅前驱体粉末;将前驱体粉末550℃下焙烧6h得到固体粉末,加入四乙基氢氧化铵11.61g当中,然后加入相当于硅源质量5%的Beta分子筛晶种,将混合液体在70℃水浴锅中蒸水浓缩,达到摩尔比为SiO2:TiO2:H2O:TEAOH=1:0.016:3.4:0.55;最后将得到的浑浊液移至高压釜内,于140℃晶化5d,经去离子水洗涤、干燥、煅烧后得到Ti-Beta分子筛,产品记为“样品1”。其XRD谱图如图1所示;其UV-vis谱图如图2中“调控后”所示,即制备的气溶胶粉末经高温焙烧;SEM如图3所示。The titanium source, silicon source (tetraethyl orthosilicate), deionized water and hydrochloric acid were fully mixed in a molar ratio of SiO2:TiO2:H2O:HCl=1:0.016:20:0.135, and stirred at room temperature for 20 minutes; the solution was then spray-dried at 220°C using an aerosol generator to obtain a titanium silicon precursor powder; the precursor powder was calcined at 550°C for 6 hours to obtain a solid powder, 11.61 g of tetraethylammonium hydroxide was added, and then Beta molecular sieve seeds equivalent to 5% of the mass of the silicon source were added, and the mixed liquid was concentrated by distillation in a 70°C water bath to reach a molar ratio of SiO2:TiO2:H2O:TEAOH=1:0.016:3.4:0.55; finally, the obtained turbid solution was transferred to an autoclave, crystallized at 140°C for 5 days, and Ti-Beta molecular sieve was obtained after washing with deionized water, drying and calcining. The product was recorded as "Sample 1". Its XRD spectrum is shown in FIG1 ; its UV-vis spectrum is shown in FIG2 “after regulation”, that is, the prepared aerosol powder is calcined at high temperature; and its SEM is shown in FIG3 .
实施例2Example 2
本实施例对比实施例1:用于进一步说明该发明对于钛物种配位状态的调控This example is compared with Example 1: used to further illustrate the regulation of the coordination state of titanium species by the present invention
将钛源、硅源、去离子水、盐酸按照SiO2:TiO2:H2O:HCl=1:0.016:20:0.135的摩尔比充分混合,室温搅拌20min;之后将溶液使用气溶胶发生器在220℃下,经过喷雾干燥得到钛硅前驱体粉末;将得到的前驱体粉末不作处理,直接加入四乙基氢氧化铵11.61g当中,然后加入相当于硅源质量5%的Beta分子筛晶种,将混合液体在70℃水浴锅中蒸水浓缩,达到摩尔比为SiO2:TiO2:H2O:TEAOH=1:0.016:3.4:0.55;最后将得到的浑浊液移至高压釜内,于140℃晶化5d,经去离子水洗涤、干燥、煅烧后得到Ti-Beta分子筛。其UV-vis谱图如图2中“调控前”所示,即制备的气溶胶粉末不做焙烧处理,直接投料进行晶化。The titanium source, silicon source, deionized water and hydrochloric acid were fully mixed in a molar ratio of SiO2:TiO2:H2O:HCl=1:0.016:20:0.135, and stirred at room temperature for 20 minutes; the solution was then spray-dried at 220°C using an aerosol generator to obtain a titanium silicon precursor powder; the obtained precursor powder was directly added to 11.61g of tetraethylammonium hydroxide without treatment, and then Beta molecular sieve seeds equivalent to 5% of the mass of the silicon source were added, and the mixed liquid was concentrated by distillation in a 70°C water bath to reach a molar ratio of SiO2:TiO2:H2O:TEAOH=1:0.016:3.4:0.55; finally, the obtained turbid solution was transferred to an autoclave, crystallized at 140°C for 5 days, and the Ti-Beta molecular sieve was obtained after washing with deionized water, drying and calcining. Its UV-vis spectrum is shown in “before regulation” in FIG2 , that is, the prepared aerosol powder is not subjected to calcination treatment and is directly fed into the feed for crystallization.
实施例3Example 3
本实施例对比实施例1:用于进一步验证该发明的独特性This example is compared with Example 1: used to further verify the uniqueness of the invention
将钛源、硅源(正硅酸四乙酯)、去离子水、盐酸按照SiO2:TiO2:H2O:HCl=1:0.016:20:0.135的摩尔比充分混合,室温搅拌20min;之后将溶液使用气溶胶发生器在220℃下,经过喷雾干燥得到钛硅前驱体粉末;将前驱体粉末550℃下焙烧6h得到固体粉末,加入四乙基氢氧化铵11.61g当中,然后加入相当于硅源质量5%的Beta分子筛晶种,将混合液体在室温下搅拌均匀;最后将得到的浑浊液移至高压釜内,于140℃晶化5d,经去离子水洗涤、干燥、煅烧后得到Ti-Beta分子筛,即前体模板剂不进行浓缩,产品记为“样品2”,其XRD谱图如图1所示。通过X射线粉末衍射表征,将样品1结晶度作为参照,样品2的相对结晶度仅为46%,另外由于合成路径中有Beta晶种添加,与得到的产量结合判断仅有极微量或无Ti-Beta分子筛合成。The titanium source, silicon source (tetraethyl orthosilicate), deionized water and hydrochloric acid were fully mixed in a molar ratio of SiO2:TiO2:H2O:HCl=1:0.016:20:0.135, and stirred at room temperature for 20 minutes; the solution was then spray-dried at 220°C using an aerosol generator to obtain a titanium silicon precursor powder; the precursor powder was calcined at 550°C for 6 hours to obtain a solid powder, 11.61 g of tetraethylammonium hydroxide was added, and then Beta molecular sieve seeds equivalent to 5% of the mass of the silicon source were added, and the mixed liquid was stirred evenly at room temperature; finally, the obtained turbid solution was transferred to an autoclave, crystallized at 140°C for 5 days, and Ti-Beta molecular sieve was obtained after washing with deionized water, drying and calcining, that is, the precursor template was not concentrated, and the product was recorded as "sample 2", and its XRD spectrum is shown in Figure 1. Through X-ray powder diffraction characterization, the crystallinity of sample 1 was used as a reference, and the relative crystallinity of sample 2 was only 46%. In addition, due to the addition of Beta seeds in the synthesis route, combined with the obtained yield, it was judged that only a very small amount or no Ti-Beta molecular sieve was synthesized.
由实施例1、2、3相互佐证可知,本发明制备Ti-Beta分子筛具有鲜明特色:单纯借助气溶胶技术不焙烧会使钛物种的分布变差,而不进行模板剂的浓缩则会直接导致无法合成Ti-Beta分子筛。前体制备的每个过程相辅相成,缺一不可。As can be seen from the mutual support of Examples 1, 2, and 3, the preparation of Ti-Beta molecular sieves in the present invention has distinct characteristics: the distribution of titanium species will be deteriorated by simply using aerosol technology without calcination, and the failure to concentrate the template will directly lead to the inability to synthesize Ti-Beta molecular sieves. Each process of precursor preparation complements each other and is indispensable.
实施例4Example 4
本实例用于说明本方法可以使用不同模板剂用量合成Ti-Beta分子筛This example is used to illustrate that this method can be used to synthesize Ti-Beta molecular sieves with different template dosages.
重复实施例1,但在最终蒸水浓缩步骤中达到摩尔比为SiO2:TiO2:H2O:TEAOH=1:0.016:4.5:0.2/0.3/0.4。得到产品记为“样品3”、“样品4”、“样品5”,其XRD谱图如图3所示。将样品1结晶度作为参照,样品3-5的相对结晶度分别达到70%、90%、115%。可见本发明的模板剂用量在0.4时即可达到最佳,少于传统水热法模板剂用量(0.55)。Example 1 was repeated, but in the final water distillation and concentration step, the molar ratio was SiO2: TiO2: H2O: TEAOH = 1: 0.016: 4.5: 0.2/0.3/0.4. The products obtained were recorded as "sample 3", "sample 4" and "sample 5", and their XRD spectra were shown in Figure 3. Taking the crystallinity of sample 1 as a reference, the relative crystallinity of samples 3-5 reached 70%, 90% and 115% respectively. It can be seen that the template dosage of the present invention can reach the best at 0.4, which is less than the template dosage of the traditional hydrothermal method (0.55).
实施例5Example 5
本实例用于说明本方法可以经过不同晶化时长合成Ti-Beta分子筛。This example is used to illustrate that the present method can be used to synthesize Ti-Beta molecular sieves through different crystallization times.
重复实施例1,但在最终晶化时长采用140℃下,3d、4d、6d、7d。得到产品记为“样品6”、“样品7”、“样品8”、“样品9”,其XRD谱图如图3所示。将样品1结晶度作为参照,样品6-9的相对结晶度分别达到80%、89%、114%、102%。可知本发明在晶化6天时达到最佳结晶状态,但在晶化3天时相对结晶度已达到80%,使用本发明合成Ti-Beta分子筛所需晶化时间远小于传统水热法直接合成Ti-Beta分子筛。Example 1 was repeated, but the final crystallization time was 140°C for 3d, 4d, 6d, and 7d. The products obtained were recorded as "Sample 6", "Sample 7", "Sample 8", and "Sample 9", and their XRD spectra are shown in Figure 3. Taking the crystallinity of sample 1 as a reference, the relative crystallinity of samples 6-9 reached 80%, 89%, 114%, and 102%, respectively. It can be seen that the present invention reaches the best crystallization state after 6 days of crystallization, but the relative crystallinity has reached 80% after 3 days of crystallization. The crystallization time required for synthesizing Ti-Beta molecular sieve using the present invention is much shorter than the traditional hydrothermal method for directly synthesizing Ti-Beta molecular sieve.
实施例5Example 5
本实例用于说明可以采取不同时长煅烧喷粉末前体合成Ti-Beta分子筛。This example is used to illustrate that the powdered precursor can be calcined for different lengths of time to synthesize Ti-Beta molecular sieve.
重复实施例1,但在550℃下煅烧喷粉末前体3h、4h、5h。得到样品表征结果与实施例1差别不大,可见煅烧时间长短对制备Ti-Beta分子筛影响不大。Example 1 was repeated, but the spray powder precursor was calcined at 550°C for 3h, 4h, and 5h. The sample characterization results obtained were not much different from those in Example 1, which shows that the calcination time has little effect on the preparation of Ti-Beta molecular sieve.
实施例6Example 6
本实例用于说明可以采取不同Ti含量制备Ti-Beta分子筛。This example is used to illustrate that Ti-Beta molecular sieve can be prepared with different Ti contents.
重复实施例1,但钛源、硅源(正硅酸四乙酯)、去离子水、盐酸需按照SiO2:TiO2:H2O:HCl=1:0.05/0.025/0.0125/0.01:20:0.135的摩尔比充分混合;同理,在最终蒸水浓缩步骤中达到的摩尔比为SiO2:TiO2:H2O:TEAOH=1:0.05/0.025/0.0125/0.01:4.5:0.55,成功制备出不同Ti含量的Ti-Beta分子筛。可见使用本发明可以按需制备不同钛负载量的Ti-Beta分子筛。Example 1 was repeated, but the titanium source, silicon source (tetraethyl orthosilicate), deionized water, and hydrochloric acid were fully mixed in a molar ratio of SiO2: TiO2: H2O: HCl = 1: 0.05/0.025/0.0125/0.01: 20: 0.135; similarly, the molar ratio reached in the final distillation and concentration step was SiO2: TiO2: H2O: TEAOH = 1: 0.05/0.025/0.0125/0.01: 4.5: 0.55, and Ti-Beta molecular sieves with different Ti contents were successfully prepared. It can be seen that the present invention can be used to prepare Ti-Beta molecular sieves with different titanium loadings as needed.
实施例7Example 7
本实例用于说明在不脱离本发明技术方案范围内,可做出些许改动或修饰仍能制备Ti-Beta分子筛。本实例采取换用硅源、不添加晶种的方式制备Ti-Beta分子筛。This example is used to illustrate that Ti-Beta molecular sieve can be prepared by making some changes or modifications without departing from the technical solution of the present invention. In this example, Ti-Beta molecular sieve is prepared by replacing the silicon source and not adding seed crystals.
将0.386g钛酸四正丁酯、2.5g去离子水、1.0g过氧化氢(31wt%)室温搅拌1h使溶液混合均匀不产生沉淀之后,再加入7.1g硅溶胶搅拌1.5h至溶液均匀澄清;之后将溶液使用气溶胶发生器在220℃下,经过喷雾干燥得到钛硅前驱体粉末;将前驱体粉末550℃下焙烧6h得到固体粉末,加入四乙基氢氧化铵11.61g当中,将混合液体在70℃水浴锅中蒸水浓缩,达到摩尔比为SiO2:TiO2:H2O:TEAOH=1:0.016:3.4:0.55;最后将得到的浑浊液移至高压釜内,于140℃晶化5d,经去离子水洗涤、干燥、煅烧后得到Ti-Beta分子筛。得到产品记为“样品10”,其XRD谱图如图3所示。0.386g of tetrabutyl titanate, 2.5g of deionized water, and 1.0g of hydrogen peroxide (31wt%) were stirred at room temperature for 1h to make the solution uniform without precipitation, and then 7.1g of silica sol was added and stirred for 1.5h until the solution was uniform and clear; then the solution was spray-dried at 220°C using an aerosol generator to obtain titanium silicon precursor powder; the precursor powder was roasted at 550°C for 6h to obtain solid powder, added to 11.61g of tetraethylammonium hydroxide, and the mixed liquid was concentrated in a 70°C water bath by distillation to reach a molar ratio of SiO2:TiO2:H2O:TEAOH=1:0.016:3.4:0.55; finally, the obtained turbid solution was transferred to an autoclave, crystallized at 140°C for 5d, washed with deionized water, dried, and calcined to obtain Ti-Beta molecular sieve. The obtained product was recorded as "sample 10", and its XRD spectrum is shown in Figure 3.
通过以上得到数据可知,本发明提供的特殊前体水热直接合成的Ti-Beta分子筛方法,用较少晶化时间,得到具有较高结晶度、钛物种分配状态良好的纳米Ti-Beta分子筛,可重复性强。综合以上分析,本发明方法具备了使Ti-Beta分子筛实现大规模工业化的特点,使合成成本和环境负荷大大降低,大幅提高了Ti-Beta分子筛的应用领域。From the above data, it can be seen that the special precursor hydrothermal direct synthesis Ti-Beta molecular sieve method provided by the present invention uses less crystallization time to obtain nano Ti-Beta molecular sieve with high crystallinity and good titanium species distribution state, and has strong repeatability. Based on the above analysis, the method of the present invention has the characteristics of realizing large-scale industrialization of Ti-Beta molecular sieve, greatly reducing the synthesis cost and environmental load, and greatly improving the application field of Ti-Beta molecular sieve.
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