CN115594192B - NaY zeolite with high silicon-aluminum ratio and preparation method and application thereof - Google Patents
NaY zeolite with high silicon-aluminum ratio and preparation method and application thereof Download PDFInfo
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- 239000010457 zeolite Substances 0.000 title claims abstract description 161
- 229910021536 Zeolite Inorganic materials 0.000 title claims abstract description 159
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 title claims abstract description 159
- 238000002360 preparation method Methods 0.000 title claims abstract description 57
- CSDREXVUYHZDNP-UHFFFAOYSA-N alumanylidynesilicon Chemical compound [Al].[Si] CSDREXVUYHZDNP-UHFFFAOYSA-N 0.000 title claims description 19
- 229910052782 aluminium Inorganic materials 0.000 claims abstract description 176
- 229910052710 silicon Inorganic materials 0.000 claims abstract description 164
- 239000010703 silicon Substances 0.000 claims abstract description 164
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 claims abstract description 163
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 claims abstract description 160
- 239000003513 alkali Substances 0.000 claims abstract description 99
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 82
- 230000032683 aging Effects 0.000 claims abstract description 51
- 239000013078 crystal Substances 0.000 claims abstract description 51
- 238000002425 crystallisation Methods 0.000 claims abstract description 33
- 230000008025 crystallization Effects 0.000 claims abstract description 33
- 159000000000 sodium salts Chemical class 0.000 claims abstract description 33
- 239000007864 aqueous solution Substances 0.000 claims abstract description 25
- 239000011734 sodium Substances 0.000 claims description 160
- 229910052708 sodium Inorganic materials 0.000 claims description 143
- 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 95
- 239000000499 gel Substances 0.000 claims description 75
- 229910018072 Al 2 O 3 Inorganic materials 0.000 claims description 72
- 235000019353 potassium silicate Nutrition 0.000 claims description 68
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 claims description 68
- 229910004298 SiO 2 Inorganic materials 0.000 claims description 53
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 46
- 238000000034 method Methods 0.000 claims description 37
- 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 28
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 20
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 claims description 20
- 230000008569 process Effects 0.000 claims description 14
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 13
- 239000011780 sodium chloride Substances 0.000 claims description 10
- 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 6
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 6
- 239000003054 catalyst Substances 0.000 claims description 6
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 claims description 5
- 239000000741 silica gel Substances 0.000 claims description 5
- 229910002027 silica gel Inorganic materials 0.000 claims description 5
- 239000006229 carbon black Substances 0.000 claims description 4
- 239000000243 solution Substances 0.000 claims description 3
- 239000003463 adsorbent Substances 0.000 claims description 2
- 239000000377 silicon dioxide Substances 0.000 claims 2
- 239000004411 aluminium Substances 0.000 claims 1
- 238000009776 industrial production Methods 0.000 abstract description 4
- 230000003647 oxidation Effects 0.000 abstract 1
- 238000007254 oxidation reaction Methods 0.000 abstract 1
- 238000003756 stirring Methods 0.000 description 50
- 239000008367 deionised water Substances 0.000 description 29
- 229910021641 deionized water Inorganic materials 0.000 description 29
- 239000011541 reaction mixture Substances 0.000 description 24
- 230000000052 comparative effect Effects 0.000 description 21
- JHJLBTNAGRQEKS-UHFFFAOYSA-M sodium bromide Chemical compound [Na+].[Br-] JHJLBTNAGRQEKS-UHFFFAOYSA-M 0.000 description 18
- FVAUCKIRQBBSSJ-UHFFFAOYSA-M sodium iodide Chemical compound [Na+].[I-] FVAUCKIRQBBSSJ-UHFFFAOYSA-M 0.000 description 18
- 238000006243 chemical reaction Methods 0.000 description 15
- 239000000203 mixture Substances 0.000 description 15
- 238000002441 X-ray diffraction Methods 0.000 description 12
- 239000000523 sample Substances 0.000 description 11
- 239000002253 acid Substances 0.000 description 9
- 238000012512 characterization method Methods 0.000 description 9
- 239000000463 material Substances 0.000 description 5
- 239000002585 base Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 229910052760 oxygen Inorganic materials 0.000 description 4
- 239000002243 precursor Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000010907 mechanical stirring Methods 0.000 description 3
- 238000002156 mixing Methods 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000001308 synthesis method Methods 0.000 description 3
- 238000004458 analytical method Methods 0.000 description 2
- 229910052792 caesium Inorganic materials 0.000 description 2
- 238000004523 catalytic cracking Methods 0.000 description 2
- -1 cesium ions Chemical class 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000005342 ion exchange Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 239000000376 reactant Substances 0.000 description 2
- 239000011343 solid material Substances 0.000 description 2
- 238000010561 standard procedure Methods 0.000 description 2
- 229910016523 CuKa Inorganic materials 0.000 description 1
- 229910003902 SiCl 4 Inorganic materials 0.000 description 1
- DNEHKUCSURWDGO-UHFFFAOYSA-N aluminum sodium Chemical compound [Na].[Al] DNEHKUCSURWDGO-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O ammonium group Chemical group [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004364 calculation method Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000000571 coke Substances 0.000 description 1
- 150000003983 crown ethers Chemical class 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000002431 foraging effect Effects 0.000 description 1
- 239000000295 fuel oil Substances 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 238000010899 nucleation Methods 0.000 description 1
- 230000006911 nucleation Effects 0.000 description 1
- 239000006259 organic additive Substances 0.000 description 1
- 238000005504 petroleum refining Methods 0.000 description 1
- 238000006116 polymerization reaction Methods 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 239000013074 reference sample Substances 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 238000004904 shortening Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
- 230000002194 synthesizing effect Effects 0.000 description 1
- 238000005406 washing Methods 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
- C01B39/20—Faujasite type, e.g. type X or Y
- C01B39/24—Type Y
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- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Inorganic Chemistry (AREA)
- Catalysts (AREA)
- Silicates, Zeolites, And Molecular Sieves (AREA)
Abstract
本发明属于NaY沸石材料技术领域,公开一种高硅铝比NaY沸石及其制备方法和应用,所述制备方法为:将硅源A、铝源A和钠盐均匀分散于水溶液A中,陈化后获得导向剂A;将导向剂A与硅源B、铝源B和碱源A均匀分散于水溶液B中,陈化后,于85~100℃下进行晶化,获得沸石凝胶晶种;将硅源C和铝源C均匀分散于水溶液C中,陈化后,获得导向剂B;将导向剂B与硅源D、沸石凝胶晶种、碱源B和铝源D均匀分散于水溶液D中,陈化后,于85~100℃下进行晶化,即获得所述高硅铝比NaY沸石。本发明制备方法简单、绿色环保,制备周期短,且制备的高硅铝比NaY沸石的结晶度可达90%以上、硅铝比为5.5~7.0,适合于工业化生产。
The invention belongs to the technical field of NaY zeolite materials and discloses a high silicon-to-aluminum ratio NaY zeolite and its preparation method and application. The preparation method is: uniformly disperse silicon source A, aluminum source A and sodium salt in aqueous solution A, and then After oxidation, the directing agent A is obtained; the directing agent A, the silicon source B, the aluminum source B and the alkali source A are evenly dispersed in the aqueous solution B. After aging, crystallization is carried out at 85 to 100°C to obtain zeolite gel seed crystals. ; Evenly disperse silicon source C and aluminum source C in aqueous solution C, and after aging, obtain directing agent B; uniformly disperse directing agent B, silicon source D, zeolite gel seed crystal, alkali source B and aluminum source D in In aqueous solution D, after aging, crystallization is performed at 85 to 100°C to obtain the high silicon to aluminum ratio NaY zeolite. The preparation method of the present invention is simple, green and environmentally friendly, has a short preparation cycle, and the prepared high silicon to aluminum ratio NaY zeolite has a crystallinity of more than 90% and a silicon to aluminum ratio of 5.5 to 7.0, and is suitable for industrial production.
Description
技术领域Technical field
本发明涉及NaY沸石材料技术领域,尤其涉及一种高硅铝比NaY沸石及其制备方法和应用。The present invention relates to the technical field of NaY zeolite materials, and in particular to a high silicon to aluminum ratio NaY zeolite and its preparation method and application.
背景技术Background technique
Y沸石,因其具有发达的三维孔道、可调变酸性、良好的热及水热稳定性等优势被广泛应用于石油炼化等领域。结晶度和硅铝比(SiO2/Al2O3)是影响Y沸石性质和功能的最主要的因素之一。较高的结晶度意味着Y沸石具有更高的稳定性和更多的活性中心,较高的硅铝比不仅意味着Y沸石具有更高的稳定性,而且也意味着Y沸石具有酸密度低,强酸中心多,催化裂化活性高,焦炭选择型好等优点。Y zeolite is widely used in petroleum refining and other fields because of its advantages such as developed three-dimensional pores, adjustable acidity, and good thermal and hydrothermal stability. Crystallinity and silicon-to-aluminum ratio (SiO 2 /Al 2 O 3 ) are one of the most important factors affecting the properties and functions of Y zeolite. Higher crystallinity means that Y zeolite has higher stability and more active centers. A higher silicon-to-aluminum ratio not only means that Y zeolite has higher stability, but also means that Y zeolite has low acid density. , many strong acid centers, high catalytic cracking activity, good coke selection and other advantages.
NaY沸石作为生产超稳Y沸石(USY分子筛)、SiCl4气相超稳Y沸石、介孔Y沸石的主要原料,其性质直接影响着上述生产得到的材料的性能,进而影响着催化剂的性能。NaY zeolite is the main raw material for the production of ultra-stable Y zeolite (USY molecular sieve), SiCl 4 gas phase ultra-stable Y zeolite, and mesoporous Y zeolite. Its properties directly affect the performance of the above-mentioned materials produced, and then affect the performance of the catalyst.
目前,现有技术中主要采用导向剂法制备NaY沸石,但该方法制备得到的NaY沸石的结晶度为83%左右,且其硅铝(SiO2/Al2O3)摩尔比较低,仅在5.0左右,导致该方法制备的NaY沸石无法承受后改性过程复杂严苛的条件,在处理过程中结晶度损失大,难以满足高性能催化剂生产的要求。At present, the directing agent method is mainly used to prepare NaY zeolite in the prior art. However, the crystallinity of the NaY zeolite prepared by this method is about 83%, and its silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is low. 5.0 or so, the NaY zeolite prepared by this method cannot withstand the complex and harsh conditions of the post-modification process. The crystallinity loss is large during the treatment process, making it difficult to meet the requirements for high-performance catalyst production.
为了解决上述技术问题,本领域技术人员试图提高NaY沸石的硅铝比和结晶度,且本领域技术人员提出了无模板剂法和模板剂法这两类高硅铝比NaY沸石的合成方法。其中,无模板剂法是在反应物凝胶中添加金属铯离子,合成出硅铝比在5.0-7.0之间的高硅铝比Y沸石,但是,该方法需要通过多次离子交换和焙烧的方法将铯离子除去。相对于无模板剂法,模板剂的使用合成得到的高硅铝比NaY沸石,在进行后续改性时,NaY沸石更容易进行离子交换,所以模板剂法合成高硅铝比NaY沸石得到了广泛的研究。模板剂法又分为有机模板剂法和无有机模板剂法。采用有机模板剂法合成NaY沸石,其硅铝比高达6.0-18.2。有机模板剂的选择主要集中在有机铵类和冠醚类。有机模板剂的添加往往会延长高硅铝比NaY沸石的晶化时间,有的甚至需要晶化十几天或一个月。而且,有机模板剂的二次利用仍然是一个难题,目前的处理方法一般是通过焙烧将有机模板剂除去,这样会造成环境污染,增加能耗和生产成本。所以,无有机模板剂法合成高硅铝比NaY沸石受到了工业的青睐。例如,CN101767799A公开了一种高硅铝比NaY沸石的合成方法,该方法选择在相对较低的温度下(0-10℃)搅拌24h合成导向剂,并在较低的温度下(15-80℃)进行反应物凝胶的晶化,合成得到了硅铝比6.0以上的NaY沸石。但是,由于导向剂在凝胶中分散性差,其样品的结晶度低于90%,而且导向剂合成温度较低,不适于工业应用。In order to solve the above technical problems, those skilled in the art try to improve the silica-aluminum ratio and crystallinity of NaY zeolite, and those skilled in the art have proposed two types of synthesis methods of high-silica-aluminum ratio NaY zeolite, the template-free method and the template method. Among them, the template-free method adds metal cesium ions to the reactant gel to synthesize a high silica-aluminum ratio Y zeolite with a silica-aluminum ratio between 5.0-7.0. However, this method requires multiple ion exchanges and roasting. method to remove cesium ions. Compared with the template-free method, the high silica-aluminum ratio NaY zeolite synthesized using the template agent is easier to undergo ion exchange during subsequent modification. Therefore, the template method is widely used to synthesize high-silica-aluminum ratio NaY zeolite. Research. The template method is further divided into organic template method and organic template method. The organic template method is used to synthesize NaY zeolite, with a silicon-to-aluminum ratio as high as 6.0-18.2. The selection of organic template agents mainly focuses on organic ammoniums and crown ethers. The addition of organic templates often prolongs the crystallization time of high silicon to aluminum ratio NaY zeolite, and some even require crystallization for more than ten days or a month. Moreover, the secondary utilization of organic templates is still a problem. The current treatment method is generally to remove the organic templates through roasting, which will cause environmental pollution, increase energy consumption and production costs. Therefore, the organic template-free method for synthesizing high-silica-to-aluminum ratio NaY zeolite has been favored by the industry. For example, CN101767799A discloses a synthesis method of NaY zeolite with a high silicon-aluminum ratio. This method chooses to stir at a relatively low temperature (0-10°C) for 24 hours to synthesize a directing agent, and at a lower temperature (15-80°C) ℃) to crystallize the reactant gel, and synthesized NaY zeolite with a silicon-to-aluminum ratio of 6.0 or more. However, due to the poor dispersion of the directing agent in the gel, the crystallinity of the sample is less than 90%, and the synthesis temperature of the directing agent is low, making it unsuitable for industrial applications.
为此,本发明提出一种高硅铝比NaY沸石及其制备方法和应用。To this end, the present invention proposes a high silicon to aluminum ratio NaY zeolite and its preparation method and application.
发明内容Contents of the invention
为了解决上述现有技术中的不足,本发明提供一种高硅铝比NaY沸石及其制备方法和应用,且本发明的合成方法晶化时间短、操作方便,无需改变现有生产设备,且制备获得的NaY沸石结晶度及硅铝比高。In order to solve the above deficiencies in the prior art, the present invention provides a high silicon to aluminum ratio NaY zeolite and its preparation method and application. The synthesis method of the present invention has a short crystallization time, is easy to operate, and does not need to change existing production equipment, and The prepared NaY zeolite has high crystallinity and silicon-to-aluminum ratio.
本发明的一种高硅铝比NaY沸石及其制备方法和应用是通过以下技术方案实现的:A kind of high silicon to aluminum ratio NaY zeolite of the present invention and its preparation method and application are realized through the following technical solutions:
本发明的第一个目的是提供一种高硅铝比NaY沸石的制备方法,包括以下步骤:The first object of the present invention is to provide a preparation method of high silicon to aluminum ratio NaY zeolite, which includes the following steps:
步骤1,制备沸石凝胶晶种Step 1, prepare zeolite gel seed crystal
按照(5.0×10-2-20)钠盐:(8-20)Na2O:Al2O3:(10-20)SiO2:(100-350)H2O的摩尔比,将硅源A、铝源A和钠盐均匀分散于水溶液A中,经第一次陈化处理后,获得导向剂A;According to the molar ratio of (5.0×10 -2 -20) sodium salt: (8-20) Na 2 O: Al 2 O 3 : (10-20) SiO 2 : (100-350) H 2 O, the silicon source A. Aluminum source A and sodium salt are evenly dispersed in aqueous solution A. After the first aging treatment, directing agent A is obtained;
随后,按照(2-4)Na2O:Al2O3:(6-15)SiO2:(100-300)H2O的摩尔比,将导向剂A与硅源B、铝源B和碱源A均匀分散于水溶液B中,经第二次陈化处理后,于85~100℃下进行第一次晶化处理,获得沸石凝胶晶种;Subsequently, according to the molar ratio of (2-4)Na 2 O: Al 2 O 3 : (6-15) SiO 2 : (100-300) H 2 O, the directing agent A, silicon source B, aluminum source B and Alkali source A is evenly dispersed in aqueous solution B. After the second aging treatment, the first crystallization treatment is performed at 85-100°C to obtain zeolite gel seed crystals;
步骤2,晶化形成高硅铝比NaY沸石Step 2, crystallization to form high silicon to aluminum ratio NaY zeolite
按照(10-20)Na2O:Al2O3:(10-20)SiO2:(100-350)H2O的摩尔比,将硅源C和铝源C均匀分散于水溶液C中,经第三次陈化处理后,获得导向剂B;According to the molar ratio of (10-20)Na 2 O: Al 2 O 3 : (10-20) SiO 2 : (100-350) H 2 O, the silicon source C and the aluminum source C are evenly dispersed in the aqueous solution C, After the third aging treatment, the guiding agent B is obtained;
随后,按照(2-4)Na2O:Al2O3:(7-12)SiO2:(100-300)H2O的摩尔比,将导向剂B与硅源D、沸石凝胶晶种、碱源B和铝源D均匀分散于水溶液D中,经第四次陈化处理后,于85~100℃下进行第二次晶化处理,即获得所述高硅铝比NaY沸石。Subsequently, according to the molar ratio of (2-4)Na 2 O: Al 2 O 3 : (7-12) SiO 2 : (100-300) H 2 O, the directing agent B, the silicon source D, and the zeolite gel crystal are The seed, alkali source B and aluminum source D are evenly dispersed in the aqueous solution D. After the fourth aging treatment, the second crystallization treatment is performed at 85 to 100°C to obtain the high silicon to aluminum ratio NaY zeolite.
进一步地,所述硅源A和硅源B均选自水玻璃和碱性硅溶胶中的一种或两种。Further, the silicon source A and silicon source B are selected from one or both of water glass and alkaline silica sol.
进一步地,所述铝源A和铝源B均选自偏铝酸钠和高碱偏铝酸钠中的一种或两种。Further, both the aluminum source A and the aluminum source B are selected from one or both of sodium metaaluminate and overbased sodium metaaluminate.
进一步地,所述钠盐为NaCl、NaBr和NaI中的一种或多种。Further, the sodium salt is one or more of NaCl, NaBr and NaI.
进一步地,所述硅源C和硅源D均选自硅溶胶、水玻璃、白炭黑和硅胶中的一种或多种。Further, the silicon source C and the silicon source D are both selected from one or more of silica sol, water glass, white carbon black and silica gel.
进一步地,所述铝源C和铝源D均选自偏铝酸钠、高碱偏铝酸钠、硫酸铝、硝酸铝和氢氧化铝中的一种或多种。Further, the aluminum source C and the aluminum source D are each selected from one or more of sodium metaaluminate, over-based sodium metaaluminate, aluminum sulfate, aluminum nitrate and aluminum hydroxide.
进一步地,所述钠盐的用量占所述导向剂A的3wt%~18wt%。Further, the dosage of the sodium salt accounts for 3 wt% to 18 wt% of the guiding agent A.
进一步地,所述沸石凝胶晶种的用量占所述导向剂B的1wt%~20wt%。Further, the usage amount of the zeolite gel seed crystal accounts for 1 wt% to 20 wt% of the directing agent B.
进一步地,所述第一次陈化处理的温度为20~35℃,陈化时间为12~24h。Further, the temperature of the first aging treatment is 20-35°C, and the aging time is 12-24 hours.
进一步地,所述第二次陈化处理的温度为30~60℃,陈化时间为1~12h。Further, the temperature of the second aging treatment is 30-60°C, and the aging time is 1-12 hours.
进一步地,所述第一次晶化处理的时间为6~60h。Further, the time of the first crystallization treatment is 6 to 60 hours.
进一步地,所述第三次陈化处理的温度为20~35℃,陈化时间为12~24h。Further, the temperature of the third aging treatment is 20-35°C, and the aging time is 12-24 hours.
进一步地,所述第四次陈化处理的温度为30~65℃,陈化时间为1~12h。Further, the temperature of the fourth aging treatment is 30-65°C, and the aging time is 1-12 hours.
进一步地,所述第二次晶化处理的时间为12~60h。Further, the time of the second crystallization treatment is 12 to 60 hours.
本发明的第二个目的是提供一种上述制备方法制备的高硅铝比NaY沸石。The second object of the present invention is to provide a high silicon to aluminum ratio NaY zeolite prepared by the above preparation method.
进一步地,所述高硅铝比NaY沸石的结晶度≥90%,硅铝比为5.5-7.0。Further, the crystallinity of the high silicon to aluminum ratio NaY zeolite is ≥90%, and the silicon to aluminum ratio is 5.5-7.0.
本发明的第三个目的是提供一种上述高硅铝比NaY沸石在制备吸附剂和催化剂中的应用。The third object of the present invention is to provide an application of the above-mentioned high silicon to aluminum ratio NaY zeolite in the preparation of adsorbents and catalysts.
本发明与现有技术相比,具有以下有益效果:Compared with the prior art, the present invention has the following beneficial effects:
本发明首先以由钠盐、硅源A、铝源A和水制得的导向剂A作为沸石凝胶晶种的导向剂,将其与硅源B、铝源B和碱源A反应形成含有丰富的高硅晶核前驱物的沸石凝胶晶种,然后以获得的沸石凝胶晶种作为前驱体材料,调控晶体生长过程硅铝物质的聚合反应,其中,沸石凝胶晶种中由于含有丰富的高硅晶核前驱物,不仅为沸石晶化过程提供了丰富的晶核,进而缩短晶化时间;而且还具有调控凝胶硅铝环境,促进硅进入沸石骨架的作用,使得沸石骨架中的硅铝比高,进而最终能够改善高硅铝比NaY沸石的性质。In the present invention, the directing agent A prepared from sodium salt, silicon source A, aluminum source A and water is first used as the directing agent for the zeolite gel seed crystal, and is reacted with the silicon source B, the aluminum source B and the alkali source A to form a zeolite gel seed containing The zeolite gel seed crystal is rich in high silicon crystal nucleus precursor, and then the obtained zeolite gel seed crystal is used as a precursor material to regulate the polymerization reaction of silicon and aluminum substances during the crystal growth process. Among them, the zeolite gel seed crystal contains rich The high-silicon crystal nucleation precursor not only provides abundant crystal nuclei for the zeolite crystallization process, thereby shortening the crystallization time; it also has the function of regulating the gel silicon-alumina environment and promoting the entry of silicon into the zeolite framework, making the silicon-aluminum ratio in the zeolite framework High, which can ultimately improve the properties of high silicon to aluminum ratio NaY zeolite.
本发明的制备方法无需添加任何有机模板剂或有机添加剂,工艺简单、绿色环保,并且能够实现快速制备,且本发明的制备方法在现有工业生产装置中即可实现制备,无需增加其他设备,适合于工业化生产。The preparation method of the present invention does not require the addition of any organic templates or organic additives, has a simple process, is green and environmentally friendly, and can achieve rapid preparation, and the preparation method of the present invention can be prepared in existing industrial production equipment without adding other equipment. Suitable for industrial production.
本发明方法制备的高硅铝比NaY沸石结晶度在90%以上、硅铝比为5.5-7.0,且具有热稳定性和酸性优势,对提升催化裂化催化剂的性能具有非常重要的意义。The high silicon to aluminum ratio NaY zeolite prepared by the method of the present invention has a crystallinity of more than 90%, a silicon to aluminum ratio of 5.5-7.0, and has thermal stability and acidity advantages, which is of great significance for improving the performance of the catalytic cracking catalyst.
附图说明Description of the drawings
图1为本发明实施例1的高硅铝比NaY沸石的XRD图;Figure 1 is an XRD pattern of high silicon to aluminum ratio NaY zeolite in Example 1 of the present invention;
图2为本发明实施例2的高硅铝比NaY沸石的XRD图;Figure 2 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite in Example 2 of the present invention;
图3为本发明实施例3的高硅铝比NaY沸石的XRD图;Figure 3 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite in Example 3 of the present invention;
图4为本发明实施例4的高硅铝比NaY沸石的XRD图;Figure 4 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite in Example 4 of the present invention;
图5为本发明实施例5的高硅铝比NaY沸石的XRD图;Figure 5 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite in Example 5 of the present invention;
图6为本发明实施例6的高硅铝比NaY沸石的XRD图;Figure 6 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite in Example 6 of the present invention;
图7为本发明对比例1的高硅铝比NaY沸石的XRD图;Figure 7 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite of Comparative Example 1 of the present invention;
图8为本发明对比例2的高硅铝比NaY沸石的XRD图;Figure 8 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite of Comparative Example 2 of the present invention;
图9为本发明对比例3的高硅铝比NaY沸石的XRD图。Figure 9 is an XRD pattern of the high silicon to aluminum ratio NaY zeolite of Comparative Example 3 of the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention.
本发明提供一种高硅铝比NaY沸石,且其制备方法包括以下步骤:The invention provides a high silicon to aluminum ratio NaY zeolite, and its preparation method includes the following steps:
步骤1,制备沸石凝胶晶种Step 1, prepare zeolite gel seed crystal
1.1制备导向剂A1.1 Preparation of guiding agent A
将硅源A、铝源A和钠盐均匀分散于水溶液A中,经第一次陈化处理后,获得导向剂A;Evenly disperse silicon source A, aluminum source A and sodium salt in aqueous solution A, and obtain directing agent A after the first aging treatment;
需要说明的是,本发明不限制硅源A、铝源A和钠盐的具体类型,只要能够使硅源A、铝源A和钠盐与水溶液A形成的混合物中,钠盐、Na2O、Al2O3、SiO2和H2O的摩尔比为(5.0×10-2-20)钠盐:(8-20)Na2O:Al2O3:(10-20)SiO2:(100-350)H2O即可,其中,Na2O来源于硅源A和铝源A,Al2O3来源于铝源A,SiO2来源于硅源A。且本发明中,硅源A选自水玻璃和碱性硅溶胶中的一种或两种;铝源A选自偏铝酸钠和高碱偏铝酸钠中的一种或两种;钠盐为NaCl、NaBr和NaI中的任意一种。It should be noted that the present invention does not limit the specific types of silicon source A, aluminum source A and sodium salt, as long as the mixture of silicon source A, aluminum source A, sodium salt and aqueous solution A can be made, the sodium salt, Na 2 O , Al 2 O 3 , SiO 2 and H 2 O molar ratio is (5.0×10 -2 -20) sodium salt: (8-20) Na 2 O: Al 2 O 3 : (10-20) SiO 2 : (100-350) H 2 O is sufficient, where Na 2 O is derived from silicon source A and aluminum source A, Al 2 O 3 is derived from aluminum source A, and SiO 2 is derived from silicon source A. And in the present invention, the silicon source A is selected from one or both of water glass and alkaline silica sol; the aluminum source A is selected from one or both of sodium metaaluminate and high-alkali sodium metaaluminate; sodium The salt is any one of NaCl, NaBr and NaI.
本发明不限制第一次陈化处理的具体工艺参数,只要能够使得硅源A、铝源A和钠盐与水溶液A充分接触形成组分均一的导向剂A即可,可选的,本发明于20~35℃的温度下陈化12~24h。且为了使得硅源A、铝源A和钠盐与水溶液A接触地更加充分,采用机械搅拌的方式进行混合,其中,本发明不具体限制搅拌的具体工艺参数,根据实际情况确定,只要使物料搅拌起来即可,时间一般为1~2h。The present invention does not limit the specific process parameters of the first aging treatment, as long as the silicon source A, the aluminum source A and the sodium salt can be fully contacted with the aqueous solution A to form the directing agent A with uniform components. Optionally, the present invention Aging at a temperature of 20 to 35°C for 12 to 24 hours. In order to make the silicon source A, aluminum source A and sodium salt more fully contact with the aqueous solution A, mechanical stirring is used for mixing. The present invention does not specifically limit the specific process parameters of stirring, which are determined according to the actual situation, as long as the materials are Just stir it up, the time is usually 1 to 2 hours.
1.2形成沸石凝胶晶种1.2 Formation of zeolite gel seeds
将导向剂A与硅源B、铝源B和碱源A均匀分散于水溶液B中,经第二次陈化处理后,于85~100℃下进行第一次晶化处理,获得沸石凝胶晶种;Directing agent A, silicon source B, aluminum source B and alkali source A are uniformly dispersed in aqueous solution B. After the second aging treatment, the first crystallization treatment is performed at 85-100°C to obtain zeolite gel. seed crystal;
需要说明的是,本发明不限制硅源B、铝源B和碱源A的具体类型,只要能够使导向剂A与硅源B、铝源B和碱源A与水溶液B形成的混合物中,Na2O、Al2O3、SiO2和H2O的摩尔比为(2-4)Na2O:Al2O3:(6-15)SiO2:(100-300)H2O即可,其中,硅源B选自水玻璃和碱性硅溶胶中的一种或两种;铝源B选自偏铝酸钠和高碱偏铝酸钠中的一种或两种,且以偏铝酸钠和/或高碱偏铝酸钠作为铝源B时,由于偏铝酸钠和高碱偏铝酸钠具有强碱性,同时也作为碱源A存在,因此无需额外添加碱源;钠盐的用量占导向剂A的3wt%~18wt%。It should be noted that the present invention does not limit the specific types of silicon source B, aluminum source B and alkali source A, as long as the directing agent A can be mixed with silicon source B, aluminum source B, alkali source A and aqueous solution B to form a mixture, The molar ratio of Na 2 O, Al 2 O 3 , SiO 2 and H 2 O is (2-4)Na 2 O: Al 2 O 3 : (6-15) SiO 2 : (100-300) H 2 O, that is Yes, the silicon source B is selected from one or both of water glass and alkaline silica sol; the aluminum source B is selected from one or both of sodium metaaluminate and high-alkali sodium metaaluminate, and When sodium metaaluminate and/or overbased sodium metaaluminate is used as aluminum source B, since sodium metaaluminate and overbased sodium metaaluminate are highly alkaline and also exist as alkali source A, there is no need to add an additional alkali source. ; The amount of sodium salt accounts for 3wt% to 18wt% of the guiding agent A.
本发明不限制第二次陈化处理的具体工艺参数,只要能够使得导向剂A与硅源B、铝源B和碱源A与水溶液B充分接触形成组分均一的沸石凝胶晶种前驱体即可,可选的,本发明于30~60℃的温度下陈化1~12h。且为了使得导向剂A与硅源B、铝源B和碱源A与水溶液B接触地更加充分,采用机械搅拌的方式进行混合,其中,本发明不具体限制搅拌的具体工艺参数,根据实际情况确定,只要使物料搅拌起来即可,时间一般为1~2h。The present invention does not limit the specific process parameters of the second aging treatment, as long as the directing agent A and the silicon source B, the aluminum source B, the alkali source A and the aqueous solution B can be fully contacted to form a zeolite gel seed crystal precursor with uniform components. That is, optionally, the present invention is aged at a temperature of 30 to 60°C for 1 to 12 hours. In order to make the directing agent A and the silicon source B, the aluminum source B and the alkali source A and the aqueous solution B more fully contact, mechanical stirring is used for mixing. The present invention does not specifically limit the specific process parameters of stirring. According to the actual situation To confirm, just stir the materials, usually for 1 to 2 hours.
本发明不限制第一次晶化处理的具体工艺参数,只要制备得到沸石凝胶晶种固体材料即可,可选的,本发明于85~100℃的温度下晶化处理6~60h。The present invention does not limit the specific process parameters of the first crystallization treatment, as long as the zeolite gel seed solid material is prepared. Optionally, the present invention performs the crystallization treatment at a temperature of 85 to 100° C. for 6 to 60 hours.
步骤2,晶化形成高硅铝比NaY沸石Step 2, crystallization to form high silicon to aluminum ratio NaY zeolite
2.1制备导向剂B2.1 Preparation of guiding agent B
将硅源C和铝源C均匀分散于水溶液C中,经第三次陈化处理后,获得导向剂B;The silicon source C and the aluminum source C are evenly dispersed in the aqueous solution C, and after the third aging treatment, the directing agent B is obtained;
需要说明的是,本发明不限制硅源C和铝源C的具体类型,只要能够使硅源C和铝源C与水溶液C形成的混合物中,Na2O、Al2O3、SiO2和H2O的摩尔比为(10-20)Na2O:Al2O3:(10-20)SiO2:(100-350)H2O即可,其中,硅源C选自硅溶胶、水玻璃、白炭黑和硅胶中的一种或多种;铝源C选自偏铝酸钠、高碱偏铝酸钠、硫酸铝、硝酸铝和氢氧化铝中的一种或多种。It should be noted that the present invention does not limit the specific types of silicon source C and aluminum source C, as long as the mixture of silicon source C, aluminum source C and aqueous solution C can be made, Na 2 O, Al 2 O 3 , SiO 2 and The molar ratio of H 2 O is (10-20)Na 2 O: Al 2 O 3 : (10-20) SiO 2 : (100-350) H 2 O, where the silicon source C is selected from silica sol, One or more of water glass, white carbon black and silica gel; aluminum source C is selected from one or more of sodium metaaluminate, high-alkali sodium metaaluminate, aluminum sulfate, aluminum nitrate and aluminum hydroxide.
本发明不限制第三次陈化处理的具体工艺参数,只要能够使硅源C和铝源C与水溶液C充分接触形成均一的导向剂B即可,可选的,本发明于第20~35℃的温度下陈化12~24h。且为了使得硅源C和铝源C与水溶液C接触地更加充分,采用机械搅拌的方式进行混合,其中,本发明不具体限制搅拌的具体工艺参数,根据实际情况确定,只要使物料搅拌起来即可,时间一般为1~2h。The present invention does not limit the specific process parameters of the third aging treatment, as long as the silicon source C and aluminum source C can be fully contacted with the aqueous solution C to form a uniform directing agent B. Optionally, the present invention is based on the 20th to 35th steps. Aging at ℃ for 12 to 24 hours. In order to make the silicon source C and aluminum source C more fully contact with the aqueous solution C, mechanical stirring is used for mixing. The present invention does not specifically limit the specific process parameters of stirring, which are determined according to the actual situation, as long as the materials are stirred. Yes, the time is generally 1 to 2 hours.
2.2形成高硅铝比NaY沸石2.2 Formation of high silicon to aluminum ratio NaY zeolite
将导向剂B与硅源D、沸石凝胶晶种、碱源B和铝源D均匀分散于水溶液D中,经第四次陈化处理后,于85~100℃下进行第二次晶化处理,即获得高硅铝比NaY沸石;Directing agent B, silicon source D, zeolite gel seed crystal, alkali source B and aluminum source D are evenly dispersed in aqueous solution D. After the fourth aging treatment, the second crystallization is performed at 85-100°C. After treatment, NaY zeolite with high silicon to aluminum ratio is obtained;
需要说明的是,本发明不限制硅源D、沸石凝胶晶种、碱源B和铝源D的具体类型,只要能够使导向剂B与硅源D、沸石凝胶晶种、碱源B和铝源D与水溶液C形成的混合物中,Na2O、Al2O3、SiO2和H2O的摩尔比为(2-4)Na2O:Al2O3:(7-12)SiO2:(100-300)H2O即可,其中,硅源D选自硅溶胶、水玻璃、白炭黑和硅胶中的一种或多种;铝源D选自偏铝酸钠、高碱偏铝酸钠、硫酸铝、硝酸铝和氢氧化铝中的一种或多种,且以偏铝酸钠和/或高碱偏铝酸钠作为铝源D时,由于偏铝酸钠和高碱偏铝酸钠具有强碱性,同时也作为碱源B存在,因此无需额外添加碱源也可实现反应;并且,沸石凝胶晶种的用量占导向剂B的1wt%~20wt%。It should be noted that the present invention does not limit the specific types of silicon source D, zeolite gel seed crystal, alkali source B and aluminum source D, as long as the directing agent B can be combined with silicon source D, zeolite gel seed crystal, alkali source B In the mixture of aluminum source D and aqueous solution C, the molar ratio of Na 2 O, Al 2 O 3 , SiO 2 and H 2 O is (2-4)Na 2 O: Al 2 O 3 : (7-12) SiO 2 : (100-300)H 2 O is enough, where the silicon source D is selected from one or more of silica sol, water glass, white carbon black and silica gel; the aluminum source D is selected from sodium metaaluminate, One or more of high-based sodium metaaluminate, aluminum sulfate, aluminum nitrate and aluminum hydroxide, and when sodium metaaluminate and/or high-based sodium metaaluminate is used as the aluminum source D, due to sodium metaaluminate It has strong alkalinity with high-alkali sodium metaaluminate and also exists as alkali source B, so the reaction can be achieved without adding an additional alkali source; and the amount of zeolite gel seed crystal accounts for 1wt% to 20wt% of the directing agent B. .
本发明不限制第二次晶化处理的具体工艺参数,只要制备得到高硅铝比NaY沸石固体材料即可,可选的,本发明于85~100℃的温度下晶化处理12~60h。The present invention does not limit the specific process parameters of the second crystallization treatment, as long as a high silicon to aluminum ratio NaY zeolite solid material is prepared. Optionally, the present invention performs the crystallization treatment at a temperature of 85 to 100°C for 12 to 60 hours.
实施例1Example 1
本实施例提供一种高硅铝比NaY沸石,且其制备方法如下:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and its preparation method is as follows:
S1,沸石凝胶晶种的制备:S1, Preparation of zeolite gel seed crystals:
S1.1制备导向剂AS1.1 Preparation of guiding agent A
取30.08g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.50g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)、10.40g NaCl和8.56g去离子水混合均匀后,于35℃下,以150r/min的搅拌速率搅拌1h后,静置陈化12h,即获得导向剂A;其中,以水玻璃为硅源A,以高碱偏铝酸钠为铝源A,以NaCl作为钠盐A。Take 30.08g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.50g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%), 10.40g NaCl and 8.56g deionized water are mixed evenly, stirred for 1 hour at 35°C at a stirring rate of 150 r/min, and then left to stand for 12 hours to obtain the guiding agent A; wherein, water glass is used It is silicon source A, high-based sodium metaaluminate is used as aluminum source A, and NaCl is used as sodium salt A.
S1.2获得NaY沸石凝胶晶种S1.2 Obtain NaY zeolite gel seed crystal
取118.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于60℃水浴,搅拌条件下,加入上述导向剂A、23.90g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和24g去离子水,以150r/min的搅拌速率搅拌30分钟后,再加入79.20g硫酸铝(Al2O3含量为7.6wt%)继续以150r/min的搅拌速率搅拌30分钟混合均匀,随后静置陈化1h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中并于90℃的烘箱中晶化6h,然后过滤、洗涤干燥得到NaY沸石凝胶晶种,其中,以水玻璃为硅源B、以高碱偏铝酸钠和硫酸铝共同为铝源B,且同时水玻璃和高碱偏铝酸钠共同作为碱源A。Take 118.32g water glass (SiO 2 content is 27.6wt%, Na 2O content is 8.96wt%), put it into a beaker, and place it in a 60°C water bath. Under stirring conditions, add the above-mentioned directing agent A and 23.90g high alkali. Sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 24g deionized water, stir at a stirring speed of 150r/min for 30 minutes, then add 79.20g aluminum sulfate (Al 2 O 3 content is 7.6wt%) continue to stir at a stirring rate of 150r/min for 30 minutes to mix evenly, and then let it stand for aging for 1 hour to prepare a reaction mixture gel; put the above reaction mixture gel into the reaction kettle and put it in the reaction kettle. Crystallize in an oven at 90°C for 6 hours, then filter, wash and dry to obtain NaY zeolite gel seed crystals, in which water glass is used as silicon source B, high-alkali sodium metaaluminate and aluminum sulfate are used as aluminum source B, and at the same time Water glass and high-alkali sodium metaaluminate together serve as alkali source A.
S2,高硅铝比NaY沸石的制备Preparation of S2, high silicon to aluminum ratio NaY zeolite
S2.1制备导向剂BS2.1 Preparation of guiding agent B
取18.85g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.80g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和6.56g水混合均匀后,在25℃下搅拌均匀,陈化24h,制成导向剂B;其中,以水玻璃为硅源C,以高碱偏铝酸钠为铝源C。Take 18.85g of water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), and add 20.80g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%) and 6.56g of water were mixed evenly, stirred evenly at 25°C, and aged for 24 hours to prepare the directing agent B; wherein, water glass was used as the silicon source C, and high-alkali sodium metaaluminate was used as the aluminum source C.
S2.2获得高硅铝比NaY沸石S2.2 obtains high silicon to aluminum ratio NaY zeolite
取104.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于60℃水浴,搅拌条件下,加入上述导向剂B和5g步骤(1)中制备得到的沸石凝胶晶种、18.15g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和24g水,搅拌30分钟后再加入59.83g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化12h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在90℃下晶化24h,然后过滤、洗涤干燥得到高硅铝比NaY沸石,其中,以水玻璃为硅源D、以高碱偏铝酸钠和硫酸铝为铝源D,且同时水玻璃和高碱偏铝酸钠共同作为碱源B。Take 104.32g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), put it into a beaker, and place it in a 60°C water bath. Under stirring conditions, add the above-mentioned directing agent B and 5g of step (1 ), 18.15g of high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 24g water, stir for 30 minutes and then add 59.83 g of aluminum sulfate (Al 2 O 3 content is 7.6 wt%), stir and mix evenly, and age for 12 hours to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle, crystallize at 90°C for 24 hours, and then filter , washing and drying to obtain high silicon-aluminum ratio NaY zeolite, in which water glass is used as the silicon source D, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source D, and at the same time, water glass and high-alkali sodium metaaluminate are used as a base. Source B.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图1所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 1;
本实施例制备得到的样品的相对结晶度为93%,硅铝(SiO2/Al2O3)摩尔比为6.65。The relative crystallinity of the sample prepared in this example is 93%, and the silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is 6.65.
实施例2Example 2
本实施例提供一种高硅铝比NaY沸石,且其制备方法如下:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and its preparation method is as follows:
S1,沸石凝胶晶种的制备:S1, Preparation of zeolite gel seed crystals:
S1.1制备导向剂AS1.1 Preparation of guiding agent A
取20.88g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.50g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)、1.70g NaBr和8.56g水混合均匀后,在25℃下搅拌均匀,陈化24h,制成导向剂A;其中,以水玻璃为硅源A,以高碱偏铝酸钠为铝源A,以NaBr作为钠盐A。Take 20.88g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.50g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%), 1.70g NaBr and 8.56g water were mixed evenly, stirred evenly at 25°C, and aged for 24h to prepare the directing agent A; among them, water glass was used as the silicon source A, and high-alkali sodium metaaluminate was used as the silicon source A. Aluminum source A uses NaBr as sodium salt A.
S1.2获得NaY沸石凝胶晶种S1.2 Obtain NaY zeolite gel seed crystal
取118.18g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于30℃水浴,搅拌条件下,加入上述导向剂A、5.90g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和37.02g去离子水,搅拌30分钟后再加入49.20g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化12h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在100℃下晶化24h,然后过滤、洗涤干燥得到NaY沸石凝胶晶种,其中,以水玻璃为硅源B、以高碱偏铝酸钠和硫酸铝共同作为铝源B,且同时水玻璃和高碱偏铝酸钠还共同作为碱源A存在。Take 118.18g water glass (SiO 2 content is 27.6wt%, Na 2O content is 8.96wt%), put it into a beaker, and place it in a 30°C water bath. Under stirring conditions, add the above-mentioned directing agent A and 5.90g high alkali. Sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 37.02g deionized water, stir for 30 minutes and then add 49.20g aluminum sulfate (Al 2 O 3 content is 7.6wt %) stir and mix evenly, and age for 12 hours to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 100°C for 24 hours, then filter, wash and dry to obtain NaY zeolite gel seed crystals, where , water glass is used as the silicon source B, high-alkali sodium metaaluminate and aluminum sulfate are used together as the aluminum source B, and at the same time, water glass and high-alkali sodium metaaluminate are also present together as the alkali source A.
S2,高硅铝比NaY沸石的制备Preparation of S2, high silicon to aluminum ratio NaY zeolite
S2.1制备导向剂BS2.1 Preparation of guiding agent B
取16.80g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入18.65g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和8.86g去离子水混合均匀后,在20℃下搅拌均匀,陈化12h,制成导向剂B;其中,以水玻璃为硅源C,以高碱偏铝酸钠为铝源C。Take 16.80g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 18.65g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%) and 8.86g deionized water, stir evenly at 20°C, and age for 12 hours to prepare the guiding agent B; among them, water glass is used as the silicon source C, and high-alkali sodium metaaluminate is used as the aluminum source. C.
S2.2获得高硅铝比NaY沸石S2.2 obtains high silicon to aluminum ratio NaY zeolite
取114.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于30℃水浴,搅拌条件下,加入上述导向剂B和3g步骤(1)中制备得到的沸石凝胶晶种、13.44g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和18.51g去离子水,搅拌30分钟后再加入29.33g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化1h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在90℃下晶化12h,然后过滤、洗涤干燥得到高硅铝比NaY沸石,其中,以水玻璃为硅源D、以高碱偏铝酸钠和硫酸铝为铝源D,且同时水玻璃和高碱偏铝酸钠共同作为碱源B。Take 114.32g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), put it into a beaker, and place it in a 30°C water bath. Under stirring conditions, add the above-mentioned directing agent B and 3g of step (1 ), 13.44g of overbased sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 18.51g deionized water, after stirring for 30 minutes Then add 29.33g aluminum sulfate (Al 2 O 3 content is 7.6wt%), stir and mix evenly, and age for 1 hour to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 90°C for 12 hours. , then filtered, washed and dried to obtain high silicon-aluminum ratio NaY zeolite, in which water glass is used as the silicon source D, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source D, and water glass and high-alkali sodium metaaluminate are used at the same time Together as an alkali source B.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图2所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 2;
本实施例制备得到的样品的相对结晶度为92%,硅铝(SiO2/Al2O3)摩尔比为5.96。The relative crystallinity of the sample prepared in this example is 92%, and the molar ratio of silicon to aluminum (SiO 2 /Al 2 O 3 ) is 5.96.
实施例3Example 3
本实施例提供一种高硅铝比NaY沸石,且其制备方法如下:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and its preparation method is as follows:
S1,沸石凝胶晶种的制备:S1, Preparation of zeolite gel seed crystals:
S1.1制备导向剂AS1.1 Preparation of guiding agent A
取20.88g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.50g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)、8.50g NaI和8.56g去离子水混合均匀后,在20℃下搅拌均匀,陈化16h,制成导向剂A;其中,以水玻璃为硅源A,以高碱偏铝酸钠为铝源A,以NaI作为钠盐A。Take 20.88g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.50g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%), 8.50g NaI and 8.56g deionized water were mixed evenly, stirred evenly at 20°C, and aged for 16 hours to prepare the directing agent A; among them, water glass was used as the silicon source A, and high-alkali metaaluminic acid was used Sodium is aluminum source A, and NaI is sodium salt A.
S1.2获得NaY沸石凝胶晶种S1.2 Obtain NaY zeolite gel seed crystal
取108.18g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于50℃水浴,搅拌条件下,加入上述导向剂A、10.90g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和27.02g去离子水,搅拌30分钟后再加入54.48g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化1h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在96℃下晶化40h,然后过滤、洗涤干燥得到NaY沸石凝胶晶种,本实施例中,其中,以水玻璃为硅源B、以高碱偏铝酸钠和硫酸铝共同为铝源B,且同时水玻璃和高碱偏铝酸钠共同作为碱源A。Take 108.18g of water glass (SiO 2 content is 27.6wt%, Na 2O content is 8.96wt%), put it into a beaker, and place it in a 50°C water bath. Under stirring conditions, add the above-mentioned directing agent A and 10.90g high alkali. Sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 27.02g deionized water, stir for 30 minutes and then add 54.48g aluminum sulfate (Al 2 O 3 content is 7.6wt %) Stir and mix evenly, and age for 1 hour to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 96°C for 40 hours, then filter, wash and dry to obtain NaY zeolite gel seed crystals. In the embodiment, water glass is used as the silicon source B, over-based sodium metaaluminate and aluminum sulfate are used together as the aluminum source B, and at the same time, water glass and high-based sodium metaaluminate are used together as the alkali source A.
S2,高硅铝比NaY沸石的制备Preparation of S2, high silicon to aluminum ratio NaY zeolite
S2.1制备导向剂BS2.1 Preparation of guiding agent B
取20.80g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.65g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和8.36g去离子水混合均匀后,在35℃下搅拌均匀,陈化18h,制成导向剂B;其中,以水玻璃为硅源C,以高碱偏铝酸钠为铝源C。Take 20.80g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.65g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%) and 8.36g of deionized water, stir evenly at 35°C, and age for 18 hours to prepare the guiding agent B; among them, water glass is used as the silicon source C, and high-alkali sodium metaaluminate is used as the aluminum source. C.
S2.2获得高硅铝比NaY沸石S2.2 obtains high silicon to aluminum ratio NaY zeolite
取110.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于50℃水浴,搅拌条件下,加入上述导向剂B和5g步骤(1)中制备得到的沸石凝胶晶种、10.44g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和20.51g去离子水,搅拌30分钟后再加入49.33g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化3h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在100℃下晶化15h,然后过滤、洗涤干燥得到高硅铝比NaY沸石,其中,以水玻璃为硅源D、以高碱偏铝酸钠和硫酸铝为铝源D,且同时水玻璃和高碱偏铝酸钠共同作为碱源B。Take 110.32g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), put it into a beaker, and place it in a 50°C water bath. Under stirring conditions, add the above-mentioned directing agent B and 5g of step (1 ), 10.44g of overbased sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 20.51g deionized water, after stirring for 30 minutes Then add 49.33g aluminum sulfate (Al 2 O 3 content is 7.6wt%), stir and mix evenly, and age for 3 hours to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 100°C for 15 hours. , then filtered, washed and dried to obtain high silicon-aluminum ratio NaY zeolite, in which water glass is used as the silicon source D, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source D, and water glass and high-alkali sodium metaaluminate are used at the same time Together as an alkali source B.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图3所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 3;
本实施例制备得到的样品的相对结晶度为94%,硅铝(SiO2/Al2O3)摩尔比为6.03。The relative crystallinity of the sample prepared in this example is 94%, and the silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is 6.03.
实施例4Example 4
本实施例提供一种高硅铝比NaY沸石,且其制备方法如下:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and its preparation method is as follows:
S1,沸石凝胶晶种的制备:S1, Preparation of zeolite gel seed crystals:
S1.1制备导向剂AS1.1 Preparation of guiding agent A
取30.08g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.50g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)、5.20g NaCl和8.56g去离子水混合均匀后,在25℃下搅拌均匀,陈化20h,制成导向剂A;其中,以水玻璃为硅源A,以高碱偏铝酸钠为铝源A,以NaCl作为钠盐A。Take 30.08g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.50g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%), 5.20g NaCl and 8.56g deionized water were mixed evenly, stirred evenly at 25°C, and aged for 20h to prepare the guiding agent A; among them, water glass was used as the silicon source A, and high-alkali metaaluminic acid was used Sodium is aluminum source A, and NaCl is used as sodium salt A.
S1.2获得NaY沸石凝胶晶种S1.2 Obtain NaY zeolite gel seed crystal
取118.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于50℃水浴,搅拌条件下,加入上述导向剂A、23.90g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和24g去离子水,搅拌30分钟后再加入79.20g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化6h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在98℃下晶化30h,然后过滤、洗涤干燥得到NaY沸石凝胶晶种,其中,以水玻璃为硅源B、以高碱偏铝酸钠和硫酸铝共同为铝源B,且同时水玻璃和高碱偏铝酸钠共同作为碱源A。Take 118.32g water glass (SiO 2 content is 27.6wt%, Na 2O content is 8.96wt%), put it into a beaker, and place it in a 50°C water bath. Under stirring conditions, add the above-mentioned directing agent A and 23.90g high alkali. Sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 24g deionized water, stir for 30 minutes and then add 79.20g aluminum sulfate (Al 2 O 3 content is 7.6wt% ) Stir and mix evenly, and age for 6 hours to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 98°C for 30 hours, then filter, wash and dry to obtain NaY zeolite gel seed crystals, wherein, Water glass is used as the silicon source B, high-alkali sodium metaaluminate and aluminum sulfate are used together as the aluminum source B, and at the same time, water glass and high-alkali sodium metaaluminate are used together as the alkali source A.
S2,高硅铝比NaY沸石的制备Preparation of S2, high silicon to aluminum ratio NaY zeolite
S2.1制备导向剂BS2.1 Preparation of guiding agent B
取18.85g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.80g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和6.56g去离子水混合均匀后,在32℃下搅拌均匀,陈化18h,制成导向剂B;其中,以水玻璃为硅源C,以高碱偏铝酸钠为铝源C。Take 18.85g of water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), and add 20.80g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%) and 6.56g of deionized water, stir evenly at 32°C, and age for 18 hours to prepare the guiding agent B; among them, water glass is used as the silicon source C, and high-alkali sodium metaaluminate is used as the aluminum source. C.
S2.2获得高硅铝比NaY沸石S2.2 obtains high silicon to aluminum ratio NaY zeolite
取104.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于50℃水浴,搅拌条件下,加入上述导向剂B和5g步骤(1)中制备得到的沸石凝胶晶种、18.15g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和24g去离子水,搅拌30分钟后再加入59.83g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化6h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在98℃下晶化24h,然后过滤、洗涤干燥得到高硅铝比NaY沸石,其中,以水玻璃为硅源D、以高碱偏铝酸钠和硫酸铝为铝源D,且同时水玻璃和高碱偏铝酸钠共同作为碱源B。Take 104.32g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), put it into a beaker, and place it in a 50°C water bath. Under stirring conditions, add the above-mentioned directing agent B and 5g of step (1 ), 18.15g of high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 24g deionized water, stir for 30 minutes and then Add 59.83g aluminum sulfate (Al 2 O 3 content is 7.6wt%), stir and mix evenly, and age for 6 hours to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 98°C for 24 hours. Then filter, wash and dry to obtain high silicon to aluminum ratio NaY zeolite, in which water glass is used as the silicon source D, high alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source D, and at the same time, water glass and high alkali sodium metaaluminate are used together. As an alkali source B.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图4所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 4;
本实施例制备得到的样品的相对结晶度为92%,硅铝(SiO2/Al2O3)摩尔比为5.88。The relative crystallinity of the sample prepared in this example is 92%, and the molar ratio of silicon to aluminum (SiO 2 /Al 2 O 3 ) is 5.88.
实施例5Example 5
本实施例提供一种高硅铝比NaY沸石,且其制备方法如下:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and its preparation method is as follows:
S1,沸石凝胶晶种的制备:S1, Preparation of zeolite gel seed crystals:
S1.1制备导向剂AS1.1 Preparation of guiding agent A
取20.88g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.50g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)、5.00g NaBr和8.56g去离子水混合均匀后,在25℃下搅拌均匀,陈化24h,制成导向剂A;其中,以水玻璃为硅源A,以高碱偏铝酸钠为铝源A,以NaBr作为钠盐A。Take 20.88g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.50g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%), 5.00g NaBr and 8.56g deionized water were mixed evenly, stirred evenly at 25°C, and aged for 24h to prepare the directing agent A; among them, water glass was used as the silicon source A, and high-alkali metaaluminic acid was used Sodium is the aluminum source A, and NaBr is the sodium salt A.
取118.18g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于30℃水浴,搅拌条件下,加入上述导向剂A、5.90g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和37.02g去离子水,搅拌30分钟后再加入49.20g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化12h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在100℃下晶化8h,然后过滤、洗涤干燥得到NaY沸石凝胶晶种,其中,以水玻璃为硅源B、以高碱偏铝酸钠和硫酸铝共同为铝源B,且同时水玻璃和高碱偏铝酸钠共同作为碱源A。Take 118.18g water glass (SiO 2 content is 27.6wt%, Na 2O content is 8.96wt%), put it into a beaker, and place it in a 30°C water bath. Under stirring conditions, add the above-mentioned directing agent A and 5.90g high alkali. Sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 37.02g deionized water, stir for 30 minutes and then add 49.20g aluminum sulfate (Al 2 O 3 content is 7.6wt %) stir and mix evenly, and age for 12 hours to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 100°C for 8 hours, then filter, wash and dry to obtain NaY zeolite gel seed crystals, where , water glass is used as the silicon source B, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source B, and at the same time, water glass and high-alkali sodium metaaluminate are used as the alkali source A.
S2,高硅铝比NaY沸石的制备Preparation of S2, high silicon to aluminum ratio NaY zeolite
S2.1制备导向剂BS2.1 Preparation of guiding agent B
取16.80g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入18.65g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和8.86g去离子水混合均匀后,在20℃下搅拌均匀,陈化12h,制成导向剂B;其中,以水玻璃为硅源C,以高碱偏铝酸钠为铝源C。Take 16.80g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 18.65g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%) and 8.86g deionized water, stir evenly at 20°C, and age for 12 hours to prepare the guiding agent B; among them, water glass is used as the silicon source C, and high-alkali sodium metaaluminate is used as the aluminum source. C.
S2.2获得高硅铝比NaY沸石S2.2 obtains high silicon to aluminum ratio NaY zeolite
取114.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于30℃水浴,搅拌条件下,加入上述导向剂B和5.00g步骤(1)中制备得到的沸石凝胶晶种、13.44g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和18.51g去离子水,搅拌30分钟后再加入29.33g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化1h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在96℃下晶化28h,然后过滤、洗涤干燥得到高硅铝比NaY沸石,其中,以水玻璃为硅源D、以高碱偏铝酸钠和硫酸铝为铝源D,且同时水玻璃和高碱偏铝酸钠共同作为碱源B。Take 114.32g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), put it into a beaker, and place it in a 30°C water bath. Under stirring conditions, add the above-mentioned directing agent B and 5.00g step ( The zeolite gel seed crystal prepared in 1), 13.44g overbased sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 18.51g deionized water, stir for 30 minutes Then add 29.33g aluminum sulfate (Al 2 O 3 content is 7.6wt%), stir and mix evenly, and age for 1 hour to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 96°C. 28h, then filter, wash and dry to obtain high silicon-to-aluminum ratio NaY zeolite, in which water glass is used as the silicon source D, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source D, and water glass and high-alkali metaaluminic acid are used at the same time Sodium together acts as a base source B.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图5所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 5;
本实施例制备得到的样品的相对结晶度为95%,硅铝(SiO2/Al2O3)摩尔比为6.08。The relative crystallinity of the sample prepared in this example is 95%, and the molar ratio of silicon to aluminum (SiO 2 /Al 2 O 3 ) is 6.08.
实施例6Example 6
本实施例提供一种高硅铝比NaY沸石,且其制备方法如下:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and its preparation method is as follows:
S1,沸石凝胶晶种的制备:S1, Preparation of zeolite gel seed crystals:
S1.1制备导向剂AS1.1 Preparation of guiding agent A
取20.88g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.50g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)、10.00g NaI和8.56g去离子水混合均匀后,在20℃下搅拌均匀,陈化16h,制成导向剂A;;其中,以水玻璃为硅源A,以高碱偏铝酸钠为铝源A,以NaI作为钠盐A。Take 20.88g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.50g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%), 10.00g NaI and 8.56g deionized water were mixed evenly, stirred evenly at 20°C, and aged for 16h to prepare the guiding agent A; wherein, water glass was used as the silicon source A, and high-alkali partial aluminum Sodium acid is aluminum source A, and NaI is sodium salt A.
取108.18g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于50℃水浴,搅拌条件下,加入上述导向剂A、10.90g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和27.02g去离子水,搅拌30分钟后再加入54.48g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化1h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在96℃下晶化20h,然后过滤、洗涤干燥得到NaY沸石凝胶晶种,其中,以水玻璃为硅源B、以高碱偏铝酸钠和硫酸铝共同为铝源B,且同时水玻璃和高碱偏铝酸钠共同作为碱源A。Take 108.18g of water glass (SiO 2 content is 27.6wt%, Na 2O content is 8.96wt%), put it into a beaker, and place it in a 50°C water bath. Under stirring conditions, add the above-mentioned directing agent A and 10.90g high alkali. Sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 27.02g deionized water, stir for 30 minutes and then add 54.48g aluminum sulfate (Al 2 O 3 content is 7.6wt %) Stir and mix evenly, and age for 1 hour to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 96°C for 20 hours, then filter, wash and dry to obtain NaY zeolite gel seed crystals, where , water glass is used as the silicon source B, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source B, and at the same time, water glass and high-alkali sodium metaaluminate are used as the alkali source A.
S2,高硅铝比NaY沸石的制备Preparation of S2, high silicon to aluminum ratio NaY zeolite
S2.1制备导向剂BS2.1 Preparation of guiding agent B
取20.80g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),加入20.65g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和8.36g去离子水混合均匀后,在35℃下搅拌均匀,陈化18h,制成导向剂B;其中,以水玻璃为硅源C,以高碱偏铝酸钠为铝源C。Take 20.80g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), add 20.65g high-alkali sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11 wt%) and 8.36g of deionized water, stir evenly at 35°C, and age for 18 hours to prepare the guiding agent B; among them, water glass is used as the silicon source C, and high-alkali sodium metaaluminate is used as the aluminum source. C.
S2.2获得高硅铝比NaY沸石S2.2 obtains high silicon to aluminum ratio NaY zeolite
取110.32g水玻璃(SiO2含量为27.6wt%,Na2O含量为8.96wt%),放入烧杯中,并置于50℃水浴,搅拌条件下,加入上述导向剂B和10.00g步骤(1)中制备得到的沸石凝胶晶种、10.44g高碱偏铝酸钠(Al2O3含量为3.16wt%,Na2O含量为21.11wt%)和20.51g去离子水,搅拌30分钟后再加入49.33g硫酸铝(Al2O3含量为7.6wt%)搅拌混合均匀,陈化1h,制得反应混合物凝胶;将上述反应混合物凝胶装入反应釜中在100℃下晶化26h,然后过滤、洗涤干燥得到高硅铝比NaY沸石,其中,以水玻璃为硅源D、以高碱偏铝酸钠和硫酸铝为铝源D,且同时水玻璃和高碱偏铝酸钠共同作为碱源B。Take 110.32g water glass (SiO 2 content is 27.6wt%, Na 2 O content is 8.96wt%), put it into a beaker, and place it in a 50°C water bath. Under stirring conditions, add the above-mentioned directing agent B and 10.00g step ( The zeolite gel seed crystal prepared in 1), 10.44g high-base sodium metaaluminate (Al 2 O 3 content is 3.16wt%, Na 2 O content is 21.11wt%) and 20.51g deionized water, stir for 30 minutes Then add 49.33g aluminum sulfate (Al 2 O 3 content is 7.6wt%), stir and mix evenly, and age for 1 hour to prepare a reaction mixture gel; put the above reaction mixture gel into a reaction kettle and crystallize it at 100°C. 26h, then filter, wash and dry to obtain high silicon to aluminum ratio NaY zeolite, in which water glass is used as the silicon source D, high-alkali sodium metaaluminate and aluminum sulfate are used as the aluminum source D, and water glass and high-alkali metaaluminic acid are used at the same time Sodium together acts as a base source B.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图6所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 6;
本实施例制备得到的样品的相对结晶度为90%,硅铝(SiO2/Al2O3)摩尔比为6.25。The relative crystallinity of the sample prepared in this example is 90%, and the silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is 6.25.
实施例7Example 7
本实施例提供了一种高硅铝比NaY沸石,且其制备方法与实施例1的区别仅在于:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and the only difference between its preparation method and Example 1 is:
S1.1中,按照5.0×10-2钠盐:8Na2O:Al2O3:10SiO2:100H2O的摩尔比,将硅源A、铝源A和钠盐均匀分散于去离子水中;且本实施例中,硅源A为碱性硅溶胶;铝源A为偏铝酸钠;且钠盐的用量占导向剂A的3wt%;In S1.1, according to the molar ratio of 5.0×10 -2 sodium salt: 8Na 2 O: Al 2 O 3 : 10SiO 2 : 100H 2 O, silicon source A, aluminum source A and sodium salt are evenly dispersed in deionized water. ; And in this embodiment, the silicon source A is alkaline silica sol; the aluminum source A is sodium metaaluminate; and the amount of sodium salt accounts for 3wt% of the directing agent A;
第一次陈化处理的温度为20℃,陈化时间为12h;The temperature of the first aging treatment is 20°C, and the aging time is 12 hours;
S1.2中,按照2Na2O:Al2O3:6SiO2:100H2O的摩尔比,将导向剂A与硅源B、铝源B和碱源A均匀分散于去离子水中;且本实施例中,硅源B为碱性硅溶胶;铝源B为偏铝酸钠,且偏铝酸钠与碱性硅溶胶同时作为碱源A存在;In S1.2, according to the molar ratio of 2Na 2 O: Al 2 O 3 : 6SiO 2 : 100H 2 O, the directing agent A, silicon source B, aluminum source B and alkali source A are evenly dispersed in deionized water; and this In the embodiment, silicon source B is alkaline silica sol; aluminum source B is sodium metaaluminate, and sodium metaaluminate and alkaline silica sol exist simultaneously as alkali source A;
第二次陈化处理的温度为30℃,陈化时间为1h;第一次晶化处理的温度为60℃,晶化时间为6h。The temperature of the second aging treatment is 30°C, and the aging time is 1 hour; the temperature of the first crystallization treatment is 60°C, and the crystallization time is 6 hours.
S2.1中,按照10Na2O:Al2O3:10SiO2:100H2O的摩尔比,将硅源C和铝源C均匀分散于去离子水中;且本实施例中,以硅溶胶为硅源C;In S2.1, the silicon source C and the aluminum source C are evenly dispersed in deionized water according to the molar ratio of 10Na 2 O: Al 2 O 3 : 10SiO 2 : 100H 2 O; and in this example, silica sol is used as Silicon source C;
第三次陈化处理的温度为20℃,陈化时间为12h。The temperature of the third aging treatment is 20°C, and the aging time is 12 hours.
S2.2中,按照2Na2O:Al2O3:7SiO2:100H2O的摩尔比,将导向剂B与硅源D、沸石凝胶晶种、碱源B和铝源D均匀分散于去离子水中;且本实施例中,以硅溶胶为硅源D,以高碱偏铝酸钠和硝酸铝为铝源C,且硅溶胶与高碱偏铝酸钠同时作为碱源B存在,且沸石凝胶晶种的用量占导向剂B的1wt%;In S2.2, according to the molar ratio of 2Na 2 O: Al 2 O 3 : 7SiO 2 : 100H 2 O, the directing agent B, the silicon source D, the zeolite gel seed crystal, the alkali source B and the aluminum source D are evenly dispersed in Deionized water; and in this example, silica sol is used as the silicon source D, high-alkali sodium metaaluminate and aluminum nitrate are used as the aluminum source C, and the silica sol and high-alkali sodium metaaluminate exist simultaneously as the alkali source B, And the dosage of zeolite gel seed crystal accounts for 1wt% of directing agent B;
第四次陈化处理的温度为30℃,陈化时间为1h;The temperature of the fourth aging treatment is 30°C, and the aging time is 1 hour;
第二次晶化处理的时间为12h。The time of the second crystallization treatment is 12h.
实施例8Example 8
本实施例提供了一种高硅铝比NaY沸石,且其制备方法与实施例1的区别仅在于:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and the only difference between its preparation method and Example 1 is:
S1.1中,按照20钠盐:20Na2O:Al2O3:20SiO2:350H2O的摩尔比,将硅源A、铝源A和钠盐均匀分散于去离子水中;且本实施例中,硅源A为碱性硅溶胶;铝源A为偏铝酸钠;且钠盐的用量占导向剂A的18wt%;In S1.1, silicon source A, aluminum source A and sodium salt are evenly dispersed in deionized water according to the molar ratio of 20 sodium salt: 20Na 2 O: Al 2 O 3 : 20SiO 2 : 350H 2 O; and this implementation In this example, silicon source A is alkaline silica sol; aluminum source A is sodium metaaluminate; and the amount of sodium salt accounts for 18wt% of directing agent A;
第一次陈化处理的温度为35℃,陈化时间为24h。The temperature of the first aging treatment is 35°C, and the aging time is 24 hours.
S1.2中,按照4Na2O:Al2O3:15SiO2:300H2O的摩尔比,将导向剂A与硅源B、铝源B和碱源A均匀分散于去离子水中;且本实施例中,硅源B为碱性硅溶胶;铝源B为偏铝酸钠,且偏铝酸钠与碱性硅溶胶同时作为碱源A存在;In S1.2, according to the molar ratio of 4Na 2 O: Al 2 O 3 : 15SiO 2 : 300H 2 O, the directing agent A, silicon source B, aluminum source B and alkali source A are evenly dispersed in deionized water; and this In the embodiment, silicon source B is alkaline silica sol; aluminum source B is sodium metaaluminate, and sodium metaaluminate and alkaline silica sol exist simultaneously as alkali source A;
第二次陈化处理的温度为60℃,陈化时间为12h;The temperature of the second aging treatment is 60°C, and the aging time is 12 hours;
第一次晶化处理的温度为100℃,时间为60h。The temperature of the first crystallization treatment is 100°C and the time is 60h.
S2.1中,按照20Na2O:Al2O3:20SiO2:350H2O的摩尔比,将硅源C和铝源C均匀分散于去离子水中;且本实施例中,以硅溶胶为硅源C;In S2.1, the silicon source C and aluminum source C are evenly dispersed in deionized water according to the molar ratio of 20Na 2 O: Al 2 O 3 : 20SiO 2 : 350H 2 O; and in this example, silica sol is used as Silicon source C;
第三次陈化处理的温度为35℃,陈化时间为24h。The temperature of the third aging treatment is 35°C, and the aging time is 24 hours.
S2.2中,按照4Na2O:Al2O3:12SiO2:300H2O的摩尔比,将导向剂B与硅源D、沸石凝胶晶种、碱源B和铝源D均匀分散于去离子水中;且本实施例中,以硅溶胶为硅源D,以高碱偏铝酸钠和硝酸铝为铝源C,且硅溶胶与高碱偏铝酸钠同时作为碱源B存在,且沸石凝胶晶种的用量占导向剂B的20wt%;In S2.2, according to the molar ratio of 4Na 2 O: Al 2 O 3 : 12SiO 2 : 300H 2 O, the directing agent B, the silicon source D, the zeolite gel seed crystal, the alkali source B and the aluminum source D are evenly dispersed in Deionized water; and in this example, silica sol is used as the silicon source D, high-alkali sodium metaaluminate and aluminum nitrate are used as the aluminum source C, and the silica sol and high-alkali sodium metaaluminate exist simultaneously as the alkali source B, And the dosage of zeolite gel seed crystal accounts for 20wt% of directing agent B;
第四次陈化处理的温度为65℃,陈化时间为12h;The temperature of the fourth aging treatment is 65°C, and the aging time is 12 hours;
第二次晶化处理的时间为60h。The time of the second crystallization treatment is 60h.
实施例9Example 9
本实施例提供了一种高硅铝比NaY沸石,且其制备方法与实施例1的区别仅在于:This embodiment provides a high silicon to aluminum ratio NaY zeolite, and the only difference between its preparation method and Example 1 is:
本实施例中,硅源C和硅源D均选自硅胶;铝源C和铝源D均选自偏铝酸钠和氢氧化铝。In this embodiment, silicon source C and silicon source D are both selected from silica gel; aluminum source C and aluminum source D are both selected from sodium metaaluminate and aluminum hydroxide.
对比例1Comparative example 1
本对比例提供了一种高硅铝比NaY沸石,且其制备方法与实施例1的区别仅在于:This comparative example provides a high silicon to aluminum ratio NaY zeolite, and the only difference between its preparation method and Example 1 is:
本对比例中,不添加钠盐(NaCl、NaBr和NaI),且不添加沸石凝胶晶种。In this comparative example, no sodium salts (NaCl, NaBr and NaI) were added, and no zeolite gel seeds were added.
本实施例制备得到的高硅铝比NaY沸石的XRD表征结果如图7所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this example are shown in Figure 7;
本实施例制备得到的样品的相对结晶度为85%,硅铝(SiO2/Al2O3)摩尔比为5.41。The relative crystallinity of the sample prepared in this example is 85%, and the silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is 5.41.
对比例2Comparative example 2
本对比例提供了一种高硅铝比NaY沸石,且其制备方法与实施例2的区别仅在于:This comparative example provides a high silicon to aluminum ratio NaY zeolite, and the only difference between its preparation method and Example 2 is:
本对比例中,不添加钠盐(NaCl、NaBr和NaI),且不添加沸石凝胶晶种。In this comparative example, no sodium salts (NaCl, NaBr and NaI) were added, and no zeolite gel seeds were added.
第二次晶化处理的温度为100℃,晶化时间为40h。The temperature of the second crystallization treatment is 100°C, and the crystallization time is 40 hours.
本对比例制备得到的高硅铝比NaY沸石的XRD表征结果如图8所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this comparative example are shown in Figure 8;
本对比例制备得到的样品的相对结晶度为70%,且含有NaP杂晶,硅铝(SiO2/Al2O3)摩尔比为5.31。The relative crystallinity of the sample prepared in this comparative example is 70%, and it contains NaP miscellaneous crystals, and the silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is 5.31.
对比例3Comparative example 3
本对比例提供了一种高硅铝比NaY沸石,且其制备方法与实施例2的区别仅在于:This comparative example provides a high silicon to aluminum ratio NaY zeolite, and the only difference between its preparation method and Example 2 is:
本对比例中,不添加钠盐(NaCl、NaBr和NaI),且不添加沸石凝胶晶种;In this comparative example, no sodium salt (NaCl, NaBr and NaI) is added, and no zeolite gel seed crystal is added;
第二次晶化处理的温度为100℃,晶化时间为40h。The temperature of the second crystallization treatment is 100°C, and the crystallization time is 40 hours.
本对比例制备得到的高硅铝比NaY沸石的XRD表征结果如图9所示;The XRD characterization results of the high silicon to aluminum ratio NaY zeolite prepared in this comparative example are shown in Figure 9;
本对比例制备得到的样品的相对结晶度为85%,且含有NaP杂晶,硅铝(SiO2/Al2O3)摩尔比为5.30。The relative crystallinity of the sample prepared in this comparative example is 85%, and it contains NaP miscellaneous crystals, and the silicon-aluminum (SiO 2 /Al 2 O 3 ) molar ratio is 5.30.
需要说明的是,本发明上述各个实施例和对比例中,合成出的NaY沸石的相对结晶度和硅铝比的测定采用BRUKER D8 ADVANCE(德国Bruker)型X射线衍射仪,实验条件为:CuKa辐射(0.1541nm),管电压30kV,管电流20mA。相对结晶度的测定是根据SH/T 0340-92标准方法(《化学工业标准汇编》),中国标准出版社,2000年出版)进行的。硅铝比的测定是根据SH/T 0339-92标准方法(《化学工业标准汇编》,中国标准出版社,2000年出版)进行,并根据式(1)计算NaY沸石的晶胞常数后,按Breck-Flanigen公式:Si/Al=(25.858-α)/(α-24.191)计算得出的。It should be noted that in the above-mentioned embodiments and comparative examples of the present invention, the relative crystallinity and silicon-aluminum ratio of the synthesized NaY zeolite were measured using a BRUKER D8 ADVANCE (Germany Bruker) X-ray diffractometer, and the experimental conditions were: CuKa Radiation (0.1541nm), tube voltage 30kV, tube current 20mA. The determination of relative crystallinity was carried out according to the SH/T 0340-92 standard method ("Chemical Industry Standard Compilation"), China Standards Press, published in 2000). The determination of the silicon-aluminum ratio is carried out according to the SH/T 0339-92 standard method ("Chemical Industry Standard Compilation", published by China Standard Press, 2000), and after calculating the unit cell constant of NaY zeolite according to formula (1), press Calculated by Breck-Flanigen formula: Si/Al=(25.858-α)/(α-24.191).
其中,in,
a—晶胞常数, a—Unit cell constant,
λ-CuKα1辐射波长 λ-CuKα1 radiation wavelength
h2+k2+l2—X射线衍射密勒指数平方和。h2+k2+l2—sum of squares of X-ray diffraction Miller indices.
实施例和对比例中所使用的作为结晶实施例和对比例中所使用的作为结晶度标准的沸石标样来自于工业NaY参比样,用X光衍射法测得该沸石的SiO2/Al2O3为5.0,并将其结晶度设定为100%。The zeolite standard sample used as the crystallization standard in the Examples and Comparative Examples is from the industrial NaY reference sample, and the SiO 2 /Al of the zeolite is measured using the X-ray diffraction method. 2O3 is 5.0 and its crystallinity is set to 100%.
本发明实施例1-6均制得高结晶度的、适合于工业化生产的高硅铝比NaY沸石,且效果平行,下面以实施例1-6制得的高硅铝比NaY沸石为例,与对比例1-3进行对比研究,具体研究结果如表1所示:Examples 1-6 of the present invention all produced NaY zeolite with high crystallinity and high silicon-aluminum ratio suitable for industrial production, and the effects were parallel. The following takes the high-silica-aluminum ratio NaY zeolite prepared in Examples 1-6 as an example. A comparative study was conducted with Comparative Examples 1-3. The specific research results are shown in Table 1:
表1实施例1-6、对比例1-3相对结晶度、硅铝比、晶胞常数和晶相分析表Table 1 Examples 1-6 and Comparative Examples 1-3 relative crystallinity, silicon to aluminum ratio, unit cell constant and crystal phase analysis table
根据图1-图9样品的XRD图,计算分析得到表1所示相关数据,结果表明,本发明制备得到的NaY沸石具有高结晶度、高硅铝比的优势,以本发明制备得到的NaY沸石作为后改性原材料,制备得到的催化剂,将具有更高的稳定性和更多的强酸中心,也将更有利于重油分子的转化。According to the XRD patterns of the samples in Figures 1 to 9, the relevant data shown in Table 1 were obtained through calculation and analysis. The results show that the NaY zeolite prepared by the present invention has the advantages of high crystallinity and high silicon-to-aluminum ratio. Zeolite is used as a post-modification raw material, and the catalyst prepared will have higher stability and more strong acid centers, and will also be more conducive to the conversion of heavy oil molecules.
显然,上述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。Obviously, the above-mentioned embodiments are only some of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts fall within the scope of protection of the present invention.
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