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CN104447204B - A kind of method for preparing diol - Google Patents

A kind of method for preparing diol Download PDF

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CN104447204B
CN104447204B CN201310415242.2A CN201310415242A CN104447204B CN 104447204 B CN104447204 B CN 104447204B CN 201310415242 A CN201310415242 A CN 201310415242A CN 104447204 B CN104447204 B CN 104447204B
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catalyzer
alkene
accordance
metal oxide
rare earth
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CN104447204A (en
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王峰
王业红
徐杰
张晓辰
张超锋
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Dalian Institute of Chemical Physics of CAS
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    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C29/00Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
    • C07C29/09Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis
    • C07C29/10Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes
    • C07C29/103Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers
    • C07C29/106Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by hydrolysis of ethers, including cyclic ethers, e.g. oxiranes of cyclic ethers of oxiranes
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J29/00Catalysts comprising molecular sieves
    • B01J29/89Silicates, aluminosilicates or borosilicates of titanium, zirconium or hafnium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2229/00Aspects of molecular sieve catalysts not covered by B01J29/00
    • B01J2229/10After treatment, characterised by the effect to be obtained
    • B01J2229/18After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself
    • B01J2229/186After treatment, characterised by the effect to be obtained to introduce other elements into or onto the molecular sieve itself not in framework positions
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C2601/00Systems containing only non-condensed rings
    • C07C2601/12Systems containing only non-condensed rings with a six-membered ring
    • C07C2601/14The ring being saturated

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  • Organic Chemistry (AREA)
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Abstract

本发明涉及一种以烯烃为原料,以一定量氧化剂作用下,环氧化生成环氧化合物进而水解制备二醇的方法。该方法采用负载稀土金属氧化物的TS-1分子筛为催化剂。具体过程为:在反应容器中加入烯烃与催化剂,在一定量溶剂中,在室温至150℃下反应,色谱测得烯烃的转化率为40%-85%,二醇选择性75%-90%。本发明所涉及的制备二醇的方法,催化剂制备简单,稳定性高,反应条件较为温和,烯烃的转化率与二醇的选择性均较高。The invention relates to a method for epoxidizing olefins to produce epoxy compounds and then hydrolyzing them to prepare diols under the action of a certain amount of oxidant. The method adopts TS-1 molecular sieve loaded with rare earth metal oxide as a catalyst. The specific process is: add olefins and catalysts into the reaction vessel, and react in a certain amount of solvent at room temperature to 150°C. The conversion rate of olefins is 40%-85% and the selectivity of diols is 75%-90% as measured by chromatography. . In the method for preparing diol involved in the present invention, the preparation of the catalyst is simple, the stability is high, the reaction conditions are relatively mild, and the conversion rate of olefin and the selectivity of diol are both high.

Description

一种制备二醇的方法A kind of method for preparing diol

技术领域technical field

本发明涉及一种制备二醇的方法,具体涉及到烯烃环氧化生成环氧化合物进而水解制备二醇的过程。The invention relates to a method for preparing diols, in particular to a process in which olefins are epoxidized to generate epoxy compounds and then hydrolyzed to prepare diols.

背景技术Background technique

二元醇是一类重要的化工产品,具有重要的应用价值。1,2-丙二醇可用作不饱和聚酯树脂的原料,也是增塑剂、表面活性剂、乳化剂和破乳剂的原料,也可用作防霉剂、水果催熟剂、防腐剂、防冻剂及烟草保湿剂。乙二醇可以用来生产聚酯树脂,包括纤维、薄膜及工程塑料,还可直接用作冷却剂和防冻剂,同时也是生产醇酸树脂、增塑剂、油漆、胶粘剂、表面活性剂、炸药及电容器电解液等产品不可缺少的物质。Glycols are an important class of chemical products with important application value. 1,2-Propanediol can be used as a raw material for unsaturated polyester resins, as well as plasticizers, surfactants, emulsifiers and demulsifiers, as well as antifungal agents, fruit ripening agents, preservatives, antifreeze agent and tobacco humectant. Ethylene glycol can be used to produce polyester resins, including fibers, films and engineering plastics, and can also be directly used as coolants and antifreeze agents. It is also used to produce alkyd resins, plasticizers, paints, adhesives, surfactants, explosives And capacitor electrolyte and other products are indispensable substances.

环氧化物是多种工业产品的中间体,也是香料、制药等精细化工领域的重要原料。随着分子筛研究的深入,钛硅沸石(TS-1,Ti-β等)作为一种高效的选择氧化催化材料,使很多烯烃的环氧化可以一步完成,而且反应条件温和,Epoxides are intermediates of various industrial products, and are also important raw materials in fine chemical fields such as spices and pharmaceuticals. With the in-depth research on molecular sieves, titanium silicalite (TS-1, Ti-β, etc.) as an efficient selective oxidation catalyst material can complete the epoxidation of many olefins in one step, and the reaction conditions are mild.

氧化剂安全易得,基本上没有环境污染问题,其中丙烯的环氧化已经实现了工业化,为二元醇的生产提供了发展途径。Oxidants are safe and easy to obtain, and there is basically no environmental pollution problem. Among them, the epoxidation of propylene has been industrialized, which provides a development path for the production of diols.

MasazumiTamura等人(Chem.Eur.J.2011,17,1142811431)报道二氧化铈可以一种有效的催化剂催化水解腈制备酰胺;我们的研究工作(J.Am.Chem.Soc.2013,135,15061515)证明,二氧化铈具有一定的酸性,能水解断裂醚氧键。MasazumiTamura et al. (Chem.Eur.J.2011,17,1142811431) report that cerium dioxide can be an effective catalyst to catalyze the hydrolysis of nitriles to prepare amides; our research work (J.Am.Chem.Soc.2013,135,15061515 ) proves that ceria has a certain acidity and can hydrolyze and break ether oxygen bonds.

虽然关于烯烃环氧化与环氧化物水解已见诸多报道,但是烯烃环氧化水解一步制备二元醇的研究却较少。因此,发展具有双功能的催化剂实现一步制备二元醇引起了研究者的广泛关注。Although there have been many reports on olefin epoxidation and epoxide hydrolysis, there are few studies on the one-step preparation of diols by olefin epoxidation and hydrolysis. Therefore, the development of bifunctional catalysts to achieve one-step preparation of diols has attracted extensive attention of researchers.

发明内容Contents of the invention

本发明的意义在于克服了目前制备二醇过程中存在的缺点,如:制备过程复杂,需两步完成,反应选择性差等。该过程所用稀土金属氧化物负载的TS-1催化剂,具有环氧化和水解性能且制备简单,稳定性高,转化率与选择性均较高。The significance of the present invention is to overcome the shortcomings existing in the current diol preparation process, such as: the preparation process is complicated, it needs two steps to complete, and the reaction selectivity is poor. The TS-1 catalyst supported by the rare earth metal oxide used in the process has epoxidation and hydrolysis properties, is simple to prepare, has high stability, and has high conversion rate and selectivity.

本发明设计的一种二醇制备方案,其特征在于:采用负载稀土金属氧化物的TS-1分子筛作为催化剂,在反应容器中加入烯烃与催化剂,在溶剂中,氧化剂存在条件下获得产物二醇。所述负载稀土金属氧化物的TS-1分子筛中,稀土金属氧化物为:三氧化二镧、三氧化二铈、二氧化铈、三氧化二铕、三氧化二镱;较佳的稀土金属氧化物为二氧化铈、三氧化二铕的一种或两种;金属氧化物于催化剂中的负载量为:1wt%-20wt%;较佳负载量为:5wt%-10wt%。A diol preparation scheme designed by the present invention is characterized in that: TS-1 molecular sieve loaded with rare earth metal oxides is used as a catalyst, olefin and catalyst are added to the reaction vessel, and the product diol is obtained under the condition of the presence of an oxidizing agent in a solvent . In the TS-1 molecular sieve loaded with rare earth metal oxides, the rare earth metal oxides are: lanthanum trioxide, cerium trioxide, cerium dioxide, europium trioxide, and ytterbium trioxide; preferred rare earth metal oxides The compound is one or two kinds of ceria and europium trioxide; the loading amount of the metal oxide in the catalyst is: 1wt%-20wt%; the preferred loading amount is: 5wt%-10wt%.

所述负载稀土金属氧化物的TS-1分子筛的制备过程如下:将TS-1浸泡在含有稀土金属的可溶性盐溶液中,静置3h-48h,干燥、空气气氛中焙烧。所述TS-1的制备可以采用水热合成法、微波辐射加热法、同晶取代法中的一种,其中Ti:Si(wt:wt)=0.5%-2.5%。The preparation process of the TS-1 molecular sieve loaded with rare earth metal oxides is as follows: TS-1 is soaked in a soluble salt solution containing rare earth metals, left standing for 3h-48h, dried and calcined in an air atmosphere. The TS-1 can be prepared by one of hydrothermal synthesis method, microwave radiation heating method and isomorphic substitution method, wherein Ti:Si (wt:wt)=0.5%-2.5%.

所述加入的烯烃为:氯丙烯、丁烯、戊烯、己烯、环己烯、苯乙烯中的一种或二种以上;较佳的烯烃为:氯丙烯、环己烯或是苯乙烯中的一种或二种以上;所述氧化剂为:双氧水、叔丁基过氧化氧化氢、过氧化尿素、过氧化氢异丙苯中的一种或二种以上;较佳的氧化剂为:双氧水与过氧化尿素中的一种或两种;The added olefins are: one or more of chloropropene, butene, pentene, hexene, cyclohexene, and styrene; preferred olefins are: chloropropene, cyclohexene or styrene One or more of them; the oxidizing agent is: one or more of hydrogen peroxide, tert-butyl hydroperoxide, urea peroxide, and cumene hydroperoxide; the preferred oxidizing agent is: hydrogen peroxide with one or both of urea peroxide;

所述加入的烯烃与水的摩尔比为10-1:1,所述加入的烯烃于溶剂的浓度为0.1-1molL-1;催化剂用量为0.05g(g底物)-1-0.5g(g底物)-1;氧化剂与烯烃的摩尔比大于等于1。所述的反应温度为室温至150℃,反应时间为1h-72h.较佳的反应温度为50℃-100℃,反应时间为3h-24h;所述溶剂为:丙酮、乙腈、甲醇中的一种或二种以上与水的混合物,或是纯水,混合物中水的体积含量10-50%。The molar ratio of the added olefin to water is 10-1:1, and the concentration of the added olefin in the solvent is 0.1-1molL -1 ; the catalyst consumption is 0.05g (g substrate) -1 -0.5g (g substrate) -1 ; the molar ratio of the oxidizing agent to the alkene is greater than or equal to 1. The reaction temperature is from room temperature to 150°C, and the reaction time is 1h-72h. The preferred reaction temperature is 50°C-100°C, and the reaction time is 3h-24h; the solvent is: one of acetone, acetonitrile, and methanol Mixture of one or more kinds with water, or pure water, the volume content of water in the mixture is 10-50%.

催化剂的分离可以采用过滤或是离心,催化剂经焙烧后可以重复使用。The catalyst can be separated by filtration or centrifugation, and the catalyst can be reused after roasting.

本发明与公布的无水甲醛制备工艺相比较,具有以下几种优势:1、反应条件较为温和;2、烯烃的转化率与二醇的选择性均较高;3、本反应采用稀土氧化物负载的TS-1作为催化剂,材料易得,制备简单,稳定性高。Compared with the published anhydrous formaldehyde preparation process, the present invention has the following advantages: 1. The reaction conditions are relatively mild; 2. The conversion rate of olefins and the selectivity of diols are high; 3. The reaction uses rare earth oxides The supported TS-1 is used as a catalyst, the material is easy to obtain, the preparation is simple, and the stability is high.

具体实施方式detailed description

为了对本发明进行进一步详细说明,下面给出几个具体实施案例,但本发明不限于这些实施例。In order to further describe the present invention in detail, several specific implementation examples are given below, but the present invention is not limited to these examples.

实施例1Example 1

将7.3g正硅酸乙酯缓慢滴加到12.8mL四丙基氢氧化氨(20%水溶液)与20mL水的溶液中,在室温下剧烈搅拌溶解至澄清,0.13g钛酸四丁酯溶于6mL异丙醇后,氮气保护下,缓慢滴加到前述溶胶中,搅拌约1h。将上述混合物加入至合成釜中,密封,在180℃烘箱中下6h;晶化完成后,骤冷,去离子水反复洗至中性,干燥,550℃焙烧8h,即得TS-1,测得其Ti:Si=1%。将其浸渍在硝酸铈溶液中,制得二氧化铈负载的TS-1,二氧化铈负载量为5wt%。在反应瓶中加入2mmol氯丙烯与0.02g催化剂,加入2mL丙酮与1mL水,在60℃下反应20h,色谱测得氯丙烯转化率为78%,二醇选择性90%。Slowly add 7.3g ethyl orthosilicate dropwise to the solution of 12.8mL tetrapropylammonium hydroxide (20% aqueous solution) and 20mL water, stir vigorously at room temperature until clear, and dissolve 0.13g tetrabutyl titanate in After 6mL of isopropanol, under the protection of nitrogen, it was slowly added dropwise to the aforementioned sol, and stirred for about 1 hour. Add the above mixture into the synthesis kettle, seal it, and place it in an oven at 180°C for 6 hours; after the crystallization is completed, it is quenched, washed with deionized water repeatedly until neutral, dried, and roasted at 550°C for 8 hours to obtain TS-1. Get its Ti:Si=1%. It was immersed in cerium nitrate solution to prepare ceria-supported TS-1 with a ceria loading of 5 wt%. Add 2 mmol of allyl chloride and 0.02 g of catalyst into the reaction flask, add 2 mL of acetone and 1 mL of water, and react at 60 ° C for 20 h. The conversion rate of allyl chloride is 78% and the selectivity of diol is 90% as measured by chromatography.

实施例2Example 2

将9.0g正硅酸乙酯缓慢滴加到16.0mL四丙基氢氧化氨(20%水溶液)与30mL水的溶液中,在室温下剧烈搅拌溶解至澄清,0.28g钛酸四丁酯溶于10mL异丙醇后,氮气保护下,缓慢滴加到前述溶胶中,搅拌约1h。将上述混合物加入至合成釜中,密封,微波辅助加热至150℃,保持3h;加热完成后,骤冷,去离子水反复洗至中性,干燥,500℃焙烧4h,即得TS-1,测得其Ti:Si=1.8%。将其浸渍在硝酸铕溶液中,100℃下蒸干,500℃焙烧2h,制得三氧化二铕负载的TS-1,三氧化二铕的负载量为10wt%。在反应瓶中加入2mmol环己烯与0.02g催化剂,加入2mL乙腈与1mL水,在80℃下反应24h,色谱测得环己烯转化率为60%,二醇选择性85%。Slowly add 9.0g ethyl orthosilicate dropwise into a solution of 16.0mL tetrapropylammonium hydroxide (20% aqueous solution) and 30mL water, stir vigorously at room temperature until clear, and dissolve 0.28g tetrabutyl titanate in After 10mL of isopropanol, under the protection of nitrogen, it was slowly added dropwise to the aforementioned sol, and stirred for about 1 hour. Add the above mixture into the synthesis kettle, seal it, heat it with microwave assistance to 150°C, and keep it for 3 hours; after the heating is completed, it is quenched, washed with deionized water repeatedly until neutral, dried, and calcined at 500°C for 4 hours to obtain TS-1. Its Ti:Si=1.8% was measured. It was immersed in europium nitrate solution, evaporated to dryness at 100°C, and calcined at 500°C for 2 hours to prepare TS-1 loaded with europium trioxide, and the loading amount of europium trioxide was 10wt%. Add 2mmol cyclohexene and 0.02g catalyst into the reaction flask, add 2mL acetonitrile and 1mL water, and react at 80°C for 24h. The conversion rate of cyclohexene is 60% and the selectivity of diol is 85% as measured by chromatography.

实施例3Example 3

将7.3g正硅酸乙酯缓慢滴加到12.8mL四丙基氢氧化氨(20%水溶液)与20mL水的溶液中,在室温下剧烈搅拌溶解至澄清,0.13g钛酸四丁酯溶于6mL异丙醇后,氮气保护下,缓慢滴加到前述溶胶中,搅拌约1h。将上述混合物加入至合成釜中,密封,在180℃烘箱中下6h;晶化完成后,骤冷,去离子水反复洗至中性,干燥,550℃焙烧8h,即得TS-1,测得其Ti:Si=1%。将其浸渍在硝酸镧溶液中,制得二氧化二镧负载的TS-1,负载量为5wt%。在反应瓶中加入2mmol氯丙烯与0.02g催化剂,加入2mL丙酮与1mL水,在60℃下反应20h,色谱测得氯丙烯转化率为75%,二醇选择性90%。Slowly add 7.3g ethyl orthosilicate dropwise to the solution of 12.8mL tetrapropylammonium hydroxide (20% aqueous solution) and 20mL water, stir vigorously at room temperature until clear, and dissolve 0.13g tetrabutyl titanate in After 6mL of isopropanol, under the protection of nitrogen, it was slowly added dropwise to the aforementioned sol, and stirred for about 1 hour. Add the above mixture into the synthesis kettle, seal it, and place it in an oven at 180°C for 6 hours; after the crystallization is completed, it is quenched, washed with deionized water repeatedly until neutral, dried, and roasted at 550°C for 8 hours to obtain TS-1. Get its Ti:Si=1%. It was immersed in a lanthanum nitrate solution to prepare TS-1 loaded with dilanthanum dioxide, and the loading amount was 5wt%. Add 2mmol chloropropene and 0.02g catalyst into the reaction flask, add 2mL acetone and 1mL water, and react at 60°C for 20h. Chromatography shows that the conversion rate of chloropropene is 75%, and the selectivity of diol is 90%.

实施例4Example 4

将9.0g正硅酸乙酯缓慢滴加到16.0mL四丙基氢氧化氨(20%水溶液)与30mL水的溶液中,在室温下剧烈搅拌溶解至澄清,0.28g钛酸四丁酯溶于10mL异丙醇后,氮气保护下,缓慢滴加到前述溶胶中,搅拌约1h。将上述混合物加入至合成釜中,密封,微波辅助加热至150℃,保持3h;加热完成后,骤冷,去离子水反复洗至中性,干燥,500℃焙烧4h,即得TS-1,测得其Ti:Si=1.8%。将其浸渍在硝酸铕溶液中,100℃下蒸干,500℃焙烧2h,制得三氧化二铕负载的TS-1,三氧化二铕的负载量为10wt%。在反应瓶中加入2mmol苯乙烯烯与0.02g催化剂,加入2mL丙酮与1mL水,在80℃下反应48h,色谱测得环己烯转化率为70%,二醇选择性89%。Slowly add 9.0g ethyl orthosilicate dropwise into a solution of 16.0mL tetrapropylammonium hydroxide (20% aqueous solution) and 30mL water, stir vigorously at room temperature until clear, and dissolve 0.28g tetrabutyl titanate in After 10mL of isopropanol, under the protection of nitrogen, it was slowly added dropwise to the aforementioned sol, and stirred for about 1 hour. Add the above mixture into the synthesis kettle, seal it, heat it with microwave assistance to 150°C, and keep it for 3 hours; after the heating is completed, it is quenched, washed with deionized water repeatedly until neutral, dried, and calcined at 500°C for 4 hours to obtain TS-1. Its Ti:Si=1.8% was measured. It was immersed in europium nitrate solution, evaporated to dryness at 100°C, and calcined at 500°C for 2 hours to prepare TS-1 loaded with europium trioxide, and the loading amount of europium trioxide was 10wt%. Add 2mmol styrene ene and 0.02g catalyst into the reaction flask, add 2mL acetone and 1mL water, and react at 80°C for 48h. The conversion rate of cyclohexene is 70% and the selectivity of diol is 89% as measured by chromatography.

实施例5Example 5

将10.6g正硅酸乙酯缓慢滴加到12.8mL四丙基氢氧化氨(20%水溶液)与20mL水的溶液中,在室温下剧烈搅拌溶解至澄清,0.42g钛酸四丁酯溶于8mL异丙醇后,氮气保护下,缓慢滴加到前述溶胶中,搅拌约1h。将上述混合物加入至合成釜中,密封,在185℃烘箱中下8h;晶化完成后,骤冷,去离子水反复洗至中性,干燥,500℃焙烧5h,即得TS-1,测得其Ti:Si=2.1%。将其浸渍在硝酸铈溶液中,制得二氧化铈负载的TS-1,二氧化铈负载量为2wt%。在反应瓶中加入2mmol氯丙烯与0.02g催化剂,加入2mL丙酮与1mL水,在80℃下反应24h,色谱测得氯丙烯转化率为85%,二醇选择性88%。Slowly add 10.6g of ethyl orthosilicate dropwise into a solution of 12.8mL of tetrapropylammonium hydroxide (20% aqueous solution) and 20mL of water, stir vigorously at room temperature until clear, and dissolve 0.42g of tetrabutyl titanate in After 8mL of isopropanol, under the protection of nitrogen, it was slowly added dropwise to the aforementioned sol, and stirred for about 1 hour. Add the above mixture into the synthesis kettle, seal it, and place it in an oven at 185°C for 8 hours; after the crystallization is completed, it is quenched, washed with deionized water repeatedly until neutral, dried, and roasted at 500°C for 5 hours to obtain TS-1. Get its Ti:Si=2.1%. It was immersed in cerium nitrate solution to prepare TS-1 supported by ceria, and the ceria loading was 2 wt%. Add 2mmol of allyl chloride and 0.02g of catalyst into the reaction flask, add 2mL of acetone and 1mL of water, and react at 80°C for 24h. The conversion rate of allyl chloride is 85% and the selectivity of diol is 88% as measured by chromatography.

实施例6Example 6

将10.6g正硅酸乙酯缓慢滴加到12.8mL四丙基氢氧化氨(20%水溶液)与20mL水的溶液中,在室温下剧烈搅拌溶解至澄清,0.42g钛酸四丁酯溶于8mL异丙醇后,氮气保护下,缓慢滴加到前述溶胶中,搅拌约1h。将上述混合物加入至合成釜中,密封,在185℃烘箱中下8h;晶化完成后,骤冷,去离子水反复洗至中性,干燥,500℃焙烧5h,即得TS-1,测得其Ti:Si=2.1%。将其浸渍在硝酸铈溶液中,制得二氧化铈负载的TS-1,二氧化铈负载量为8wt%。在反应瓶中加入2mmol氯丙烯与0.02g催化剂,加入3mL水,在80℃下反应24h,色谱测得氯丙烯转化率为80%,二醇选择性78%。Slowly add 10.6g of ethyl orthosilicate dropwise into a solution of 12.8mL of tetrapropylammonium hydroxide (20% aqueous solution) and 20mL of water, stir vigorously at room temperature until clear, and dissolve 0.42g of tetrabutyl titanate in After 8mL of isopropanol, under the protection of nitrogen, it was slowly added dropwise to the aforementioned sol, and stirred for about 1 hour. Add the above mixture into the synthesis kettle, seal it, and place it in an oven at 185°C for 8 hours; after the crystallization is completed, it is quenched, washed with deionized water repeatedly until neutral, dried, and roasted at 500°C for 5 hours to obtain TS-1. Get its Ti:Si=2.1%. It was immersed in cerium nitrate solution to prepare TS-1 supported by ceria, and the ceria loading was 8 wt%. Add 2 mmol of allyl chloride and 0.02 g of catalyst into the reaction flask, add 3 mL of water, and react at 80 ° C for 24 hours. The conversion rate of allyl chloride is 80% and the selectivity of diol is 78% as measured by chromatography.

Claims (9)

1. prepare a method for glycol, it is characterized in that:
Adopt the TS-1 molecular sieve of supported rare earth metal oxide as catalyzer, in reaction vessel, add alkene and catalyzer, in a solvent, under oxygenant existence condition, obtain product glycol;
Rare-earth oxide is: lanthanum sesquioxide, cerous oxide, cerium dioxide, europiumsesquioxide, yttria; The charge capacity of metal oxide in catalyzer is: 1wt% ~ 20wt%;
The described alkene added is: one or two or more kinds in propenyl chloride, butylene, amylene, hexene, tetrahydrobenzene, vinylbenzene;
Described oxygenant is: one or two or more kinds in hydrogen peroxide, tertbutyl peroxide, carbamide peroxide, hydrogen phosphide cumene;
Described temperature of reaction is room temperature to 150 DEG C, and the reaction times is 1h ~ 72h.
2. in accordance with the method for claim 1, it is characterized in that:
In the TS-1 molecular sieve of described supported rare earth metal oxide, preferably rare-earth oxide be cerium dioxide, europiumsesquioxide one or both; The better charge capacity of metal oxide in catalyzer is: 5wt% ~ 10wt%.
3. in accordance with the method for claim 1, it is characterized in that:
The preparation process of the TS-1 molecular sieve of described supported rare earth metal oxide is as follows: be immersed in by TS-1 in the soluble salt solutions containing rare earth metal, leaves standstill 3h ~ 48h, roasting in drying, air atmosphere.
4., according to the method described in claim 1,2 or 3, it is characterized in that:
The preparation of described TS-1 can adopt the one in hydrothermal synthesis method, microwave heating method, isomorphous substitution method, wherein Ti:Si=0.5wt% ~ 2.5wt%.
5. in accordance with the method for claim 1, it is characterized in that:
Preferably alkene is: one or two or more kinds in propenyl chloride, tetrahydrobenzene or vinylbenzene;
Preferably oxygenant is: one or both in hydrogen peroxide and carbamide peroxide.
6., according to the method described in claim 1 or 5, it is characterized in that:
The mol ratio of the described alkene that adds and water is 10 ~ 1:1, described in the alkene that adds be 0.1 ~ 1molL in the concentration of solvent -1; Catalyst levels is 0.05g (g substrate) -1~ 0.5g (g substrate) -1; The mol ratio of oxygenant and alkene is more than or equal to 1.
7. in accordance with the method for claim 1, it is characterized in that:
Preferably temperature of reaction is 50 DEG C ~ 100 DEG C, and the reaction times is 3h ~ 24h.
8. in accordance with the method for claim 1, it is characterized in that:
The separation of catalyzer can adopt filters or centrifugal, and catalyzer can be reused after roasting.
9. in accordance with the method for claim 1, it is characterized in that:
Described solvent is: the mixture of one or two or more kinds and water in acetone, acetonitrile, methyl alcohol, or pure water, the volume content 10-50% of water in mixture.
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