[go: up one dir, main page]

CN105883847A - Preparation method of iron-containing Y-shaped zeolite - Google Patents

Preparation method of iron-containing Y-shaped zeolite Download PDF

Info

Publication number
CN105883847A
CN105883847A CN201410776003.4A CN201410776003A CN105883847A CN 105883847 A CN105883847 A CN 105883847A CN 201410776003 A CN201410776003 A CN 201410776003A CN 105883847 A CN105883847 A CN 105883847A
Authority
CN
China
Prior art keywords
iron
preparation
type zeolite
water
directing agent
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
CN201410776003.4A
Other languages
Chinese (zh)
Inventor
纪妍妍
刘强
李江
吴维鹏
车振宁
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tiangong University
Original Assignee
Tianjin Polytechnic University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tianjin Polytechnic University filed Critical Tianjin Polytechnic University
Priority to CN201410776003.4A priority Critical patent/CN105883847A/en
Publication of CN105883847A publication Critical patent/CN105883847A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/10Process efficiency

Landscapes

  • Silicates, Zeolites, And Molecular Sieves (AREA)

Abstract

本发明属于杂原子改性微孔沸石的制备领域,具体涉及一种负载氧化铁改性Y型沸石的制备方法。该方法具体为:首先用硅源、铝源、氢氧化钠、与水充分混合并老化,配制导向剂溶液;将偏铝酸钠、氢氧化钠、水与导向剂溶液混合均匀形成初始凝胶,将硝酸铁直接加入其中,抽滤含铁水凝胶得半干固体,将其在水热条件下进行晶化反应,固体经洗涤、过滤、干燥、焙烧后得到产品。通过本发明,直接将Fe3+引入Y型沸石合成的初始凝胶之中,能够避免浸渍、离子交换等后处理步骤,操作简便;先抽干再晶化的方法,能够大幅减少传统技术合成沸石材料时水热处理过程中的含水量,提高单釜分子筛产量,这一过程可以提高能效,节约生产成本,有工业实用价值。The invention belongs to the field of preparation of heteroatom-modified microporous zeolite, and in particular relates to a preparation method of iron oxide-loaded modified Y-type zeolite. The method is specifically as follows: first, fully mix and age silicon source, aluminum source, sodium hydroxide, and water to prepare a directing agent solution; mix sodium metaaluminate, sodium hydroxide, water and the directing agent solution evenly to form an initial gel , adding ferric nitrate directly to it, and suction-filtering the iron-containing hydrogel to obtain a semi-dry solid, which is crystallized under hydrothermal conditions, and the solid is washed, filtered, dried, and roasted to obtain the product. Through the present invention, Fe 3+ is directly introduced into the initial gel synthesized by Y-type zeolite, which can avoid post-treatment steps such as impregnation and ion exchange, and is easy to operate; the method of first draining and recrystallizing can greatly reduce the amount of synthesis by traditional techniques. The water content in the hydrothermal treatment process of the zeolite material can increase the yield of single-pot molecular sieves. This process can improve energy efficiency, save production costs, and has industrial practical value.

Description

一种含铁Y型沸石的制备方法A kind of preparation method of iron-containing Y-type zeolite

技术领域technical field

本发明属于杂原子改性微孔沸石的制备领域,具体涉及一种负载氧化铁改性Y型沸石的制备方法。The invention belongs to the field of preparation of heteroatom-modified microporous zeolite, and in particular relates to a preparation method of iron oxide-loaded modified Y-type zeolite.

背景技术Background technique

随着石化、冶金、印染等工业的迅速发展,产生了大量含难降解有机污染物的工业废水,成为水环境污染的主要来源之一。对高浓度难降解有机污染物的去除,认识当前水处理领域的一大难题。With the rapid development of petrochemical, metallurgy, printing and dyeing industries, a large amount of industrial wastewater containing refractory organic pollutants has been produced, which has become one of the main sources of water environmental pollution. For the removal of high-concentration refractory organic pollutants, understand a major problem in the current water treatment field.

采用均相催化剂(如Fenton试剂、亚铁盐等)催化H2O2氧化,可使有机污染物降解至CO2和H2O,因此利用羟基自由基降解和矿化有机污染物的深度氧化技术受到广泛关注。但该法使用的均相催化剂难以与反应介质分离,带来活性成分流失和二次污染等问题。采用非均相固体催化剂代替均相铁盐,可克服均相法的不足,成为当前的研究热点。Using homogeneous catalysts (such as Fenton's reagent, ferrous salt, etc. ) to catalyze the oxidation of H2O2 can degrade organic pollutants to CO2 and H2O , so the deep oxidation of organic pollutants can be degraded and mineralized by hydroxyl radicals Technology gets a lot of attention. However, the homogeneous catalyst used in this method is difficult to separate from the reaction medium, which brings problems such as loss of active components and secondary pollution. The use of heterogeneous solid catalysts instead of homogeneous iron salts can overcome the shortcomings of the homogeneous method, and has become a current research hotspot.

沸石分子筛是一类非常重要的无机多孔材料,具有高的热及水热稳定性、大比表面积、良好的离子交换性能、以及具有分子尺寸大小(通常为0.3~2.0nm)的孔道结构等性质,被广泛地应用于许多工业领域,如择形催化剂、吸附剂、离子交换剂等。将铁氧化物负载于沸石结构之中制成含铁沸石非均相催化剂用于催化降解有机污染物(如苯酚、染料废水),具有很好的降解效果。但是传统的沸石合成工艺多为硅源、铝源与碱源溶液充分混合形成初始凝胶,将此初始凝胶经水热反应,晶化得到固体。掺杂铁的方法有浸渍法、离子交换法、共沉淀法等,均为采用铁盐溶液对沸石原料进行后处理的方法,涉及诸多操作步骤,不利于工业实施和降低成本。在沸石合成之初将铁物种引入其初始凝胶中,继而进行晶化,则可以简化合成步骤。Zeolite molecular sieves are a very important class of inorganic porous materials, with high thermal and hydrothermal stability, large specific surface area, good ion exchange performance, and pore structure with molecular size (usually 0.3-2.0nm). , are widely used in many industrial fields, such as shape-selective catalysts, adsorbents, ion exchangers, etc. Loading iron oxides in the zeolite structure to make iron-containing zeolite heterogeneous catalysts is used to catalyze the degradation of organic pollutants (such as phenol, dye wastewater), and has a good degradation effect. However, in the traditional zeolite synthesis process, the silicon source, the aluminum source and the alkali source solution are fully mixed to form an initial gel, and the initial gel is hydrothermally reacted and crystallized to obtain a solid. Iron doping methods include impregnation method, ion exchange method, co-precipitation method, etc., all of which use iron salt solution to post-treat zeolite raw materials, involving many operating steps, which are not conducive to industrial implementation and cost reduction. The introduction of iron species into the initial gel of zeolite synthesis, followed by crystallization, can simplify the synthesis steps.

此外在晶体生长的水热反应过程中,大量的水作为溶剂,釜内大部分体积被溶剂水所占,使得单釜产量有限,耗能较大。如果能够减少水热反应过程中的含水量,则能够提高单釜中固含量,提高单釜分子筛产量,减少能耗,节约成本。对工业生产,生产成本的降低即意味着经济效益的提高,同时,低能耗也是绿色环保的要求。In addition, in the hydrothermal reaction process of crystal growth, a large amount of water is used as a solvent, and most of the volume in the kettle is occupied by solvent water, which makes the output of a single kettle limited and consumes a lot of energy. If the water content in the hydrothermal reaction process can be reduced, the solid content in the single kettle can be increased, the yield of molecular sieve in the single kettle can be increased, energy consumption can be reduced, and cost can be saved. For industrial production, the reduction of production costs means the improvement of economic benefits. At the same time, low energy consumption is also a requirement for green environmental protection.

发明内容Contents of the invention

本发明旨在提供一种含铁Y型沸石的制备方法,该方法直接将Fe3+引入Y型沸石合成的初始凝胶之中,避免浸渍、离子交换等后处理步骤,并采用对含铁初始凝胶进行抽干,再进行高温晶化的方法,减少水热反应过程中的水含量,提高含铁分子筛的单釜产量,该技术工艺简单,易于操作,便于工业化实施。本发明具体技术方案为:The present invention aims to provide a preparation method of iron-containing Y-type zeolite, which directly introduces Fe into the initial gel of Y-type zeolite synthesis, avoids post-treatment steps such as impregnation and ion exchange, and adopts iron-containing The initial gel is drained and then crystallized at high temperature to reduce the water content in the hydrothermal reaction process and increase the single-pot yield of the iron-containing molecular sieve. This technology is simple in process, easy to operate, and convenient for industrial implementation. Concrete technical scheme of the present invention is:

1)导向剂的配制1) Preparation of directing agent

将水玻璃、偏铝酸钠、氢氧化钠和水,充分混合,形成一澄清透明溶液,室温静置老化24~60小时,即得导向剂溶液。在该导向剂溶液中,各反应原料的添加量摩尔比例为:Na2O/Al2O3/SiO2/H2O=12~20/1/19/300~400。Water glass, sodium metaaluminate, sodium hydroxide and water are thoroughly mixed to form a clear and transparent solution, which is aged at room temperature for 24 to 60 hours to obtain the directing agent solution. In the directing agent solution, the molar ratio of the added amount of each reaction raw material is: Na 2 O/Al 2 O 3 /SiO 2 /H 2 O=12˜20/1/19/300˜400.

2)初始凝胶的制备2) Preparation of initial gel

将一定量偏铝酸钠、氢氧化钠和水混合,向其中缓慢滴加上述导向剂,充分搅拌15~60分钟,形成初始凝胶,所述各反应原料的添加量应使初始凝胶中各成分的摩尔比例为:Na2O/Al2O3/SiO2/H2O=3.2~4.5/1/3/120~180;Mix a certain amount of sodium metaaluminate, sodium hydroxide and water, slowly add the above-mentioned directing agent dropwise, and stir thoroughly for 15-60 minutes to form an initial gel. The molar ratio of each component is: Na 2 O/Al 2 O 3 /SiO 2 /H 2 O=3.2~4.5/1/3/120~180;

3)铁的掺入3) Incorporation of iron

向上述初始凝胶中缓慢加入一定量铁盐(Fe(NO3)3·9H2O),使初始凝胶中Fe2O3与SiO2的摩尔比例为0.1~1.0∶3,继续搅拌30~60分钟,得含铁水凝胶;Slowly add a certain amount of iron salt (Fe(NO 3 ) 3 9H 2 O) to the above initial gel, so that the molar ratio of Fe 2 O 3 to SiO 2 in the initial gel is 0.1-1.0:3, and continue stirring for 30 ~60 minutes to obtain iron-containing hydrogel;

4)抽干晶化合成含铁Y型沸石4) Drying and crystallization to synthesize iron-containing Y-type zeolite

将上述含铁水凝胶进行抽滤,至无液体滴下,得到的半干固体在80~100℃进行水热反应,静置晶化18~24小时;Suction filter the above-mentioned iron-containing hydrogel until there is no liquid dripping, and the obtained semi-dry solid undergoes a hydrothermal reaction at 80-100°C, and stands to crystallize for 18-24 hours;

5)过滤、洗涤、干燥、焙烧5) Filtration, washing, drying, roasting

晶化完成后,将得到的产品洗涤、抽滤,并在80℃干燥20小时以上。干燥完成后将产品置于550℃的马弗炉中焙烧5小时After the crystallization is completed, the obtained product is washed, suction-filtered, and dried at 80° C. for more than 20 hours. After the drying is completed, the product is baked in a muffle furnace at 550°C for 5 hours

有益效果:本发明提供的含铁Y型沸石的合成方法,由于直接将Fe3+引入Y型沸石合成的初始凝胶之中,避免了浸渍、离子交换等后处理引入铁的步骤,操作简便;采用对含铁初始凝胶进行抽干,再进行高温晶化的方法,能够大幅减少传统水热处理过程中的水含量,使单釜中含铁分子筛的固体含量增加,这一过程可以提高能效,节约生产成本,有巨大的工业实用价值和应用前景。Beneficial effects: the synthesis method of iron-containing Y-type zeolite provided by the present invention, because Fe 3+ is directly introduced into the initial gel synthesized by Y-type zeolite, avoids the steps of impregnation, ion exchange and other post-treatments to introduce iron, and is easy to operate ;The method of draining the iron-containing initial gel and then carrying out high-temperature crystallization can greatly reduce the water content in the traditional hydrothermal treatment process, and increase the solid content of the iron-containing molecular sieve in the single kettle. This process can improve energy efficiency , saving production cost, has huge industrial practical value and application prospect.

具体实施方式detailed description

以下是本发明的具体实施例,是对本发明的进一步描述。但具体实施例不限制本发明权利要求。The following are specific embodiments of the present invention, which are further descriptions of the present invention. However, the specific embodiments do not limit the claims of the present invention.

具体实施例中使用到的原料如下:The raw material used in the specific embodiment is as follows:

水玻璃:天津市津南聚兴泡花碱厂生产,其中氧化硅质量分数为20.3%;Water glass: produced by Tianjin Jinnan Juxing Soda Soda Factory, wherein the mass fraction of silicon oxide is 20.3%;

偏铝酸钠:天津市光复精细化工研究所生产;Sodium metaaluminate: produced by Tianjin Guangfu Fine Chemical Research Institute;

氢氧化钠:天津市北方天医化学试剂厂生产。Sodium hydroxide: produced by Tianjin Beifang Tianyi Chemical Reagent Factory.

实施例1:Example 1:

导向剂的制备:将0.7克偏铝酸钠溶于10.0毫升水中,加入3克氢氧化钠,搅拌至澄清,向其中滴加22.5克水玻璃,机械搅拌约30分钟,得一澄清透明溶液,室温下静置老化24小时,得导向剂。Preparation of guiding agent: Dissolve 0.7 g of sodium metaaluminate in 10.0 ml of water, add 3 g of sodium hydroxide, stir until clear, add 22.5 g of water glass dropwise, and stir mechanically for about 30 minutes to obtain a clear and transparent solution. Standing and aging at room temperature for 24 hours, the directing agent was obtained.

含铁Y型沸石的制备:将3.5克偏铝酸钠溶于38.5毫升水中,加入41.5克水玻璃,搅拌均匀,向其中缓慢滴加33.5克导向剂溶液,机械搅拌约30分钟,混合均匀后得到初始凝胶,向其中加入1.2克九水合硝酸铁,继续搅拌60分钟,将得到的凝胶抽滤,至不再有液体滴落,将此半干固体装入反应釜中,在100℃静置反应24小时,得到的产品经洗涤、抽滤,并于80℃干燥20小时,干燥完成后将产品置于550℃的马弗炉中焙烧5小时,得到最终产物。Preparation of iron-containing Y-type zeolite: Dissolve 3.5 grams of sodium metaaluminate in 38.5 milliliters of water, add 41.5 grams of water glass, stir evenly, slowly add 33.5 grams of directing agent solution to it, stir mechanically for about 30 minutes, and mix well To obtain the initial gel, add 1.2 g of ferric nitrate nonahydrate to it, and continue to stir for 60 minutes. The obtained gel is suction-filtered until there is no more liquid dripping. After standing for 24 hours to react, the obtained product was washed, suction filtered, and dried at 80°C for 20 hours. After drying, the product was roasted in a muffle furnace at 550°C for 5 hours to obtain the final product.

实施例2:Example 2:

导向剂的制备:将0.7克偏铝酸钠溶于10.0毫升水中,加入3克氢氧化钠,搅拌至澄清,向其中滴加22.5克水玻璃,机械搅拌约30分钟,得一澄清透明溶液,室温下静置老化40小时,得导向剂。Preparation of guiding agent: Dissolve 0.7 g of sodium metaaluminate in 10.0 ml of water, add 3 g of sodium hydroxide, stir until clear, add 22.5 g of water glass dropwise, and stir mechanically for about 30 minutes to obtain a clear and transparent solution. Standing and aging at room temperature for 40 hours, the directing agent was obtained.

含铁Y型沸石的制备:将2.4克偏铝酸钠溶于26毫升水中,加入30克水玻璃,混合均匀,向其中缓慢滴加16克导向剂溶液,机械搅拌约30分钟,混合均匀后得到初始凝胶,向其中加入2.5克九水合硝酸铁,继续搅拌60分钟,将得到的凝胶抽滤,至不再有液体滴落,将此半干固体装入反应釜中,在100℃静置反应24小时,得到的产品经洗涤、抽滤,并于80℃干燥20小时,干燥完成后将产品置于550℃的马弗炉中焙烧5小时,得到最终产物。Preparation of iron-containing Y-type zeolite: Dissolve 2.4 grams of sodium metaaluminate in 26 milliliters of water, add 30 grams of water glass, mix well, slowly add 16 grams of directing agent solution to it, stir mechanically for about 30 minutes, and mix well To obtain the initial gel, add 2.5 grams of ferric nitrate nonahydrate to it, continue to stir for 60 minutes, filter the obtained gel with suction, until no more liquid drips, put the semi-dry solid into the reaction kettle, and heat it at 100°C After standing for 24 hours to react, the obtained product was washed, suction filtered, and dried at 80°C for 20 hours. After drying, the product was roasted in a muffle furnace at 550°C for 5 hours to obtain the final product.

实施例3:Example 3:

导向剂的制备:将0.7克偏铝酸钠溶于10.0毫升水中,加入3克氢氧化钠,搅拌至澄清,向其中滴加22.5克水玻璃,机械搅拌约30分钟,得一澄清透明溶液,室温下静置老化24小时,得导向剂。Preparation of guiding agent: Dissolve 0.7 g of sodium metaaluminate in 10.0 ml of water, add 3 g of sodium hydroxide, stir until clear, add 22.5 g of water glass dropwise, and stir mechanically for about 30 minutes to obtain a clear and transparent solution. Standing and aging at room temperature for 24 hours, the directing agent was obtained.

含铁Y型沸石的制备:将3.2克偏铝酸钠溶于37毫升水中,加入1.6克氢氧化钠,47.2克水玻璃,混合均匀,向其中缓慢滴加4克导向剂溶液,机械搅拌约30分钟,混合均匀后得到初始凝胶,向其中加入3.6克九水合硝酸铁,继续搅拌60分钟,将得到的凝胶抽滤,至不再有液体滴落,将此半干固体装入反应釜中,在100℃静置反应24小时,得到的产品经洗涤、抽滤,并于80℃干燥20小时,干燥完成后将产品置于550℃的马弗炉中焙烧5小时,得到最终产物。Preparation of iron-containing Y-type zeolite: Dissolve 3.2 grams of sodium metaaluminate in 37 milliliters of water, add 1.6 grams of sodium hydroxide and 47.2 grams of water glass, mix well, slowly add 4 grams of directing agent solution dropwise, and mechanically stir for about After 30 minutes, mix evenly to obtain the initial gel, add 3.6 grams of ferric nitrate nonahydrate to it, continue to stir for 60 minutes, filter the obtained gel until there is no more liquid dripping, put the semi-dry solid into the reaction In the kettle, stand at 100°C for 24 hours, the obtained product is washed, filtered, and dried at 80°C for 20 hours. After drying, the product is baked in a muffle furnace at 550°C for 5 hours to obtain the final product .

以上所述,仅是本发明的几种实施案例,并非对本发明做任何形式上的限制,任何熟悉本专业的技术人员,在不脱离本发明技术方案范围内,当可利用上述揭示的结构及技术内容作出些许更动或修饰为等同变化的等效实施案例。但是凡是未脱离本发明技术方案的内容,依据本发明的技术实质对以上实施案例所做的任何简单修改,等同变化与修饰,均仍属本发明技术方案范围内。The above are only several implementation examples of the present invention, and are not intended to limit the present invention in any form. Any skilled person who is familiar with the profession can use the structure disclosed above and Equivalent implementation cases with minor changes or modifications to equivalent changes in technical content. However, any simple modifications, equivalent changes and modifications made to the above implementation cases according to the technical essence of the present invention are still within the scope of the technical solutions of the present invention.

Claims (7)

1.一种含铁Y型沸石的制备方法,其特征在于,具体包括下列步骤:1. a preparation method of iron-containing Y type zeolite, is characterized in that, specifically comprises the following steps: 1)导向剂的制备1) Preparation of directing agent 首先将硅源、铝源、碱源和水,按照一定比例进行充分混合,室温下静置老化24~60小时,即得到所需导向剂;First, fully mix the silicon source, aluminum source, alkali source and water according to a certain ratio, and leave to age at room temperature for 24 to 60 hours to obtain the required directing agent; 2)初始凝胶的制备2) Preparation of initial gel 将一定量硅源、铝源、碱源和水混合,向其中缓慢滴加上述导向剂,充分搅拌15~60分钟,得到初始凝胶;Mix a certain amount of silicon source, aluminum source, alkali source and water, slowly add the above-mentioned directing agent dropwise, and stir thoroughly for 15-60 minutes to obtain the initial gel; 3)铁的掺入3) Incorporation of iron 向上述初始凝胶中缓慢加入一定量铁盐,继续搅拌30~60分钟,得含铁水凝胶;Slowly add a certain amount of iron salt to the above initial gel, and continue stirring for 30 to 60 minutes to obtain an iron-containing hydrogel; 4)抽干晶化法合成含铁Y型沸石4) Synthesis of iron-containing Y-type zeolite by draining and crystallization 将上述含铁水凝胶进行抽滤,至无液体滴下,将抽滤得到的半干固体在80~100℃进行水热反应,静置晶化18~24小时;The above-mentioned iron-containing hydrogel is suction-filtered until no liquid drops, and the semi-dry solid obtained by suction filtration is subjected to a hydrothermal reaction at 80-100°C, and left to stand for crystallization for 18-24 hours; 5)过滤、洗涤、干燥、焙烧5) Filtration, washing, drying, roasting 晶化完成后,将得到的产品洗涤、抽滤,并在80℃干燥20小时以上,干燥完成后将产品置于550℃的马弗炉中焙烧5小时。After the crystallization is completed, the obtained product is washed, suction-filtered, and dried at 80°C for more than 20 hours. After drying, the product is baked in a muffle furnace at 550°C for 5 hours. 2.根据权利要求1所述的含铁Y型沸石的制备方法,其特征在于,合成中所使用的硅源为水玻璃。2. the preparation method of iron-containing Y-type zeolite according to claim 1 is characterized in that, the silicon source used in the synthesis is water glass. 3.根据权利要求1所述的含铁Y型沸石的制备方法,其特征在于,合成中所使用的铝源为偏铝酸钠。3. the preparation method of iron-containing Y-type zeolite according to claim 1 is characterized in that, the aluminum source used in the synthesis is sodium metaaluminate. 4.根据权利要求1所述的含铁Y型沸石的制备方法,其特征在于,合成中所使用的碱源为氢氧化钠。4. the preparation method of iron-containing Y-type zeolite according to claim 1 is characterized in that, the alkali source used in the synthesis is sodium hydroxide. 5.根据权利要求1所述的含铁Y型沸石的制备方法,其特征在于,合成中所使用的水为去离子水。5. the preparation method of iron-containing Y-type zeolite according to claim 1 is characterized in that, the water used in the synthesis is deionized water. 6.根据权利要求1所述的含铁Y型沸石的制备方法,其特征在于,所述各反应原料的添加量应使导向剂中各成分的摩尔比例为:在Na2O/Al2O3/SiO2/H2O=12~20/1/19/300~400。6. the preparation method of iron-containing Y-type zeolite according to claim 1 is characterized in that, the addition amount of each reaction raw material should make the molar ratio of each composition in the directing agent be: in Na 2 O/Al 2 O 3 /SiO 2 /H 2 O=12-20/1/19/300-400. 7.根据权利要求1所述的含铁Y型沸石的制备方法,其特征在于,所述各反应原料的添加量应使初始凝胶中各成分的摩尔比例为:Fe2O3/Na2O/Al2O3/SiO2/H2O=0.1~1.0/3.2~4.5/1/3/120~180。7. the preparation method of iron-containing Y-type zeolite according to claim 1 is characterized in that, the addition amount of each reaction raw material should make the molar ratio of each composition in the initial gel be: Fe 2 O 3 /Na 2 O/Al 2 O 3 /SiO 2 /H 2 O=0.1-1.0/3.2-4.5/1/3/120-180.
CN201410776003.4A 2014-12-16 2014-12-16 Preparation method of iron-containing Y-shaped zeolite Pending CN105883847A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201410776003.4A CN105883847A (en) 2014-12-16 2014-12-16 Preparation method of iron-containing Y-shaped zeolite

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201410776003.4A CN105883847A (en) 2014-12-16 2014-12-16 Preparation method of iron-containing Y-shaped zeolite

Publications (1)

Publication Number Publication Date
CN105883847A true CN105883847A (en) 2016-08-24

Family

ID=56700215

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201410776003.4A Pending CN105883847A (en) 2014-12-16 2014-12-16 Preparation method of iron-containing Y-shaped zeolite

Country Status (1)

Country Link
CN (1) CN105883847A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106732747A (en) * 2016-11-28 2017-05-31 天津工业大学 A kind of molecular sieve fenton catalyst and high-efficiency synthesis method for eliminating organic dyestuff pollution
CN107265475A (en) * 2017-06-19 2017-10-20 太原理工大学 A kind of iron series element micro porous molecular sieve and preparation method and application
CN112939013A (en) * 2021-03-10 2021-06-11 中国石油大学(北京) High-silicon small-grain Y-type molecular sieve and preparation method and application of template-free molecular sieve

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4309313A (en) * 1980-05-23 1982-01-05 W. R. Grace & Co. Synthesis of cesium-containing zeolite, CSZ-1
US4333859A (en) * 1980-10-27 1982-06-08 W. R. Grace & Co. High silica faujasite polymorph - CSZ-3 and method of synthesizing
CN101134576A (en) * 2006-09-01 2008-03-05 中国石油大学(北京) Method for Improving Hydrothermal Stability of Y Molecular Sieve Using Skeleton Heteroatoms
CN101190795A (en) * 2006-11-21 2008-06-04 中国石油大学(北京) Method for preparing NaY molecular sieve by solid-phase transformation
CN101898144A (en) * 2009-05-27 2010-12-01 中国石油天然气股份有限公司 Catalytic cracking catalyst of Y-type molecular sieve containing framework heteroatom and preparation method thereof
CN103539151A (en) * 2012-07-11 2014-01-29 中国石油大学(北京) Preparation method of high silica-alumina ratio Y type zeolite rich in secondary pores

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4309313A (en) * 1980-05-23 1982-01-05 W. R. Grace & Co. Synthesis of cesium-containing zeolite, CSZ-1
US4333859A (en) * 1980-10-27 1982-06-08 W. R. Grace & Co. High silica faujasite polymorph - CSZ-3 and method of synthesizing
CN101134576A (en) * 2006-09-01 2008-03-05 中国石油大学(北京) Method for Improving Hydrothermal Stability of Y Molecular Sieve Using Skeleton Heteroatoms
CN101190795A (en) * 2006-11-21 2008-06-04 中国石油大学(北京) Method for preparing NaY molecular sieve by solid-phase transformation
CN101898144A (en) * 2009-05-27 2010-12-01 中国石油天然气股份有限公司 Catalytic cracking catalyst of Y-type molecular sieve containing framework heteroatom and preparation method thereof
CN103539151A (en) * 2012-07-11 2014-01-29 中国石油大学(北京) Preparation method of high silica-alumina ratio Y type zeolite rich in secondary pores

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
沈志虹 等: "骨架杂原子对Y型分子筛结构稳定性的影响", 《分子催化》 *
鞠雅娜 等: "FeY分子筛的合成 、表征及其加氢裂化活性", 《石油化工》 *

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106732747A (en) * 2016-11-28 2017-05-31 天津工业大学 A kind of molecular sieve fenton catalyst and high-efficiency synthesis method for eliminating organic dyestuff pollution
CN107265475A (en) * 2017-06-19 2017-10-20 太原理工大学 A kind of iron series element micro porous molecular sieve and preparation method and application
CN107265475B (en) * 2017-06-19 2019-04-26 太原理工大学 A kind of iron series element microporous molecular sieve and preparation method and application
CN112939013A (en) * 2021-03-10 2021-06-11 中国石油大学(北京) High-silicon small-grain Y-type molecular sieve and preparation method and application of template-free molecular sieve
CN112939013B (en) * 2021-03-10 2022-11-01 中国石油大学(北京) High-silicon small-grain Y-type molecular sieve and preparation method and application of template-free molecular sieve

Similar Documents

Publication Publication Date Title
CN104128184B (en) A kind of float type CoFe2O4/TiO2/ float bead composite photochemical catalyst and preparation method thereof
CN104722302B (en) Acidified mixed crystal TiO2Nanowire supported photocatalyst and preparation and application thereof
CN105330681B (en) A kind of rare earth cluster metal organic anion skeleton of micropore and its preparation method and application
CN101157050A (en) A kind of Ti/MCM-22/MCM-41 composite material and its preparation method and application
CN106732747A (en) A kind of molecular sieve fenton catalyst and high-efficiency synthesis method for eliminating organic dyestuff pollution
CN104692410A (en) Method for synthesizing A molecular sieve by crystallizing wet gel
CN105107505A (en) A kind of magnetic TiO2-porous carbon-Fe3O4 composite visible light catalyst and preparation method thereof
CN105883847A (en) Preparation method of iron-containing Y-shaped zeolite
CN103816902B (en) A kind of magnetic carries TiO 2the preparation method of photocatalysis composite
CN110479343A (en) A kind of Fe2O3/g-C3N4The one-step synthesis preparation method of composite photocatalyst material
CN104785270A (en) Visible light catalysts used for treatment of methylene blue dye waste water and a preparing method thereof
CN104759288B (en) A kind of heterogeneous Cu Mn Ce type Fenton catalysts and its production and use
CN105921153B (en) A kind of composite photo-catalyst and preparation method thereof
CN107324352A (en) A kind of method that blast furnace slag prepares ordered mesoporous silica dioxide
CN102921402B (en) Normal temperature preparation method of hydrated molybdenum trioxide photocatalyst
CN108043443A (en) A kind of synthetic method of hud typed ZnO/ZnO@NC photochemical catalysts and application
CN103332711A (en) Deep desilicication method of high-alumina fly ash
CN102502685B (en) Preparation method of mesoporous LTA zeolite
CN108325496A (en) A method of grinding auxiliary permeates synthesizing efficient catalytic degradation methylene blue metal mesopore silicon oxide certainly
CN105642320A (en) A samarium-doped KMgF3 perovskite-type visible light-responsive catalyst and its preparation method
CN110586178B (en) SAPO-34 molecular sieve and Cu/SAPO-34 denitration catalyst, preparation method and application thereof, denitration method
CN106542584A (en) A kind of preparation method of rich defect cobalt oxide photocatalyst
CN103043745A (en) Method for degrading in-water typical antibiotics through catalysis under visible light
CN108114736B (en) A kind of zeolite-supported Ag-doped BiFeO3/Bi2Fe4O9 composite material and its preparation method and application
CN104383960A (en) Preparation method and application of hierarchical porous mordenite modified by titanium

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20160824

WD01 Invention patent application deemed withdrawn after publication