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CN115894168B - Perfluoroalkyl ethanol and preparation method thereof - Google Patents

Perfluoroalkyl ethanol and preparation method thereof Download PDF

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CN115894168B
CN115894168B CN202211302371.6A CN202211302371A CN115894168B CN 115894168 B CN115894168 B CN 115894168B CN 202211302371 A CN202211302371 A CN 202211302371A CN 115894168 B CN115894168 B CN 115894168B
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perfluoroalkyl ethanol
sulfuric acid
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CN115894168A (en
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肖旺钏
林明穗
程德书
李奇勇
夏浩涵
蔡雅婷
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Sanming University
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Abstract

The invention provides perfluoroalkyl ethanol and a preparation method thereof, and relates to the technical field of fluorine-containing compound synthesis. The method comprises the following steps: firstly, reacting fluorine-containing olefin with concentrated sulfuric acid under the atmosphere of nitrogen to obtain an addition product; then adding the addition product into a high-pressure reaction kettle with magnetic stirring, slowly adding water for hydrolysis reaction, standing, layering, taking the lower transparent solution, washing with water, and drying to obtain the perfluoroalkyl alcohol. The invention firstly utilizes sulfuric acid to carry out addition reaction with fluorine-containing olefin, and then carries out hydrolysis reaction on the obtained addition product, thus obtaining the perfluoroalkyl alcohol. The method can well control the reaction process, greatly shortens the reaction time, has stable yield of the perfluoroalkyl ethanol, and is suitable for industrialized mass production.

Description

一种全氟烷基乙醇及其制备方法A kind of perfluoroalkylethanol and preparation method thereof

技术领域Technical Field

本发明涉及含氟化合物合成技术领域,且特别涉及一种全氟烷基乙醇及其制备方法。The invention relates to the technical field of fluorine-containing compound synthesis, and in particular to a perfluoroalkylethanol and a preparation method thereof.

背景技术Background Art

全氟烷基乙醇是氟原子取代碳氢键上氢原子的一类醇。由于氟原子的引入,全氟烷基乙醇表现出优越的特性,使其成为一类重要的脂肪族含氟中间体。含氟烷基乙醇的用途广泛,主要用于农药、医药合成、染料合成、有机合成、材料、含氟表面活性剂、含氟乳化剂和含氟醚制备等领域。Perfluoroalkylethanol is a type of alcohol in which fluorine atoms replace hydrogen atoms on carbon-hydrogen bonds. Due to the introduction of fluorine atoms, perfluoroalkylethanol exhibits superior properties, making it an important class of aliphatic fluorinated intermediates. Fluorinated alkylethanol has a wide range of uses, mainly in the fields of pesticides, pharmaceutical synthesis, dye synthesis, organic synthesis, materials, fluorinated surfactants, fluorinated emulsifiers and fluorinated ether preparation.

现有的全氟烷基乙醇的制备方法有加氢还原法、氧化法、水解法和调聚法。其中,对于加氢还原方法来说,目前在合成三氟乙醇的路线上研究较多。气相法的优点是反应速率快,气态反应物能充分与催化剂接触,且接触时间一般小于1min,反应温度为100~200℃,可连续生产。液相法加氢还原路线常用于高收率合成三氟乙醇、六氟异丙醇等全氟烷基乙醇。液相法的优点在于反应温度较低,避免了副反应的深度进行,氢气等物质的量加入,延长反应时间可使其充分反应。氧化法合成全氟烷基乙醇一般采用臭氧、空气、氧气或者氧气和氮气的混合气作为氧化剂。水解法是通过先将含氟烃酯化,再水解制备得到全氟烷基乙醇。其中,酯化过程和水解过程可以分步进行,也可以一步到位。但是,两步法的酯化过程易受水分影响,须使用无水溶剂,否则溶剂中的水分会使副产物增加,减慢反应速率,甚至可导致反应不能进行。而一步法一般不使用有机溶剂,而是在特定的催化剂存在下直接使用水作为溶剂。该方法虽然缩短了反应时间和减少了催化剂用量,但是反应压力过高,加大了对反应设备的要求。调聚法是在一定温度和压力下,由光、热或过氧化物引发的自由基聚合反应。利用调聚反应可将一些简单的烯类化合物和调聚剂在引发剂的存在下,形成一系列低分子量的聚合物。调聚法在全氟烷基乙醇的合成中应用越来越广泛,是一条具有工业化前景的合成道路。但是目前利用调聚法制备全氟烷基乙醇的反应时间较长且产率不稳定,进程控制难度较大。The existing preparation methods of perfluoroalkylethanol include hydrogenation reduction method, oxidation method, hydrolysis method and polymerization method. Among them, for the hydrogenation reduction method, the route of synthesizing trifluoroethanol is currently studied more. The advantage of the gas phase method is that the reaction rate is fast, the gaseous reactants can fully contact with the catalyst, and the contact time is generally less than 1min, the reaction temperature is 100-200°C, and continuous production can be achieved. The liquid phase hydrogenation reduction route is often used to synthesize perfluoroalkylethanol such as trifluoroethanol and hexafluoroisopropanol with high yield. The advantage of the liquid phase method is that the reaction temperature is low, which avoids the depth of side reactions. The amount of hydrogen and other substances is added, and the reaction time is extended to make it fully react. The oxidation method for synthesizing perfluoroalkylethanol generally uses ozone, air, oxygen or a mixture of oxygen and nitrogen as an oxidant. The hydrolysis method is to prepare perfluoroalkylethanol by first esterifying the fluorine-containing hydrocarbon and then hydrolyzing it. Among them, the esterification process and the hydrolysis process can be carried out step by step or in one step. However, the esterification process of the two-step method is easily affected by moisture, and anhydrous solvents must be used, otherwise the moisture in the solvent will increase the by-products, slow down the reaction rate, and even cause the reaction to fail. The one-step method generally does not use organic solvents, but directly uses water as a solvent in the presence of a specific catalyst. Although this method shortens the reaction time and reduces the amount of catalyst, the reaction pressure is too high, which increases the requirements for the reaction equipment. The telomerization method is a free radical polymerization reaction initiated by light, heat or peroxide at a certain temperature and pressure. Using the telomerization reaction, some simple olefin compounds and telomerization agents can be formed into a series of low molecular weight polymers in the presence of an initiator. The telomerization method is increasingly widely used in the synthesis of perfluoroalkylethanol and is a synthetic route with industrial prospects. However, the reaction time for preparing perfluoroalkylethanol using the telomerization method is long and the yield is unstable, and the process control is difficult.

发明内容Summary of the invention

本发明的目的在于提供一种全氟烷基乙醇及其制备方法,首先利用浓硫酸与含氟烯烃进行加成反应,然后再进行水解反应,即可得到全氟烷基乙醇,该方法不仅能够很好地控制反应进程,大大地缩短了反应时间,而且全氟烷基乙醇的产率稳定,适用于工业化大规模生产。The object of the present invention is to provide a perfluoroalkyl ethanol and a preparation method thereof. First, concentrated sulfuric acid is used to carry out an addition reaction with a fluorine-containing olefin, and then a hydrolysis reaction is carried out to obtain the perfluoroalkyl ethanol. The method can not only well control the reaction process and greatly shorten the reaction time, but also has a stable yield of the perfluoroalkyl ethanol, and is suitable for industrial large-scale production.

本发明解决其技术问题是采用以下技术方案来实现的。The present invention solves the technical problem by adopting the following technical solutions.

本发明提出一种全氟烷基乙醇的制备方法,包括以下步骤:The present invention provides a method for preparing perfluoroalkylethanol, comprising the following steps:

S1、含氟烯烃和浓硫酸在氮气氛围下反应,得到加成产物;S1, fluorinated olefin and concentrated sulfuric acid react under a nitrogen atmosphere to obtain an addition product;

S2、在带磁力搅拌的高压反应釜中加入所述加成产物后,缓慢加入水进行水解反应,静置、分层后,取下层透明溶液经水洗、干燥,得到全氟烷基乙醇。S2. After adding the addition product into a high-pressure reactor with magnetic stirring, slowly adding water to carry out a hydrolysis reaction. After standing and stratification, taking the lower layer of transparent solution, washing with water, and drying, to obtain perfluoroalkylethanol.

进一步地,所述含氟烯烃为CF3(CF2)nCH=CH2,其中,n为3,5,7,9中的一个。Furthermore, the fluorine-containing olefin is CF 3 (CF 2 ) n CH=CH 2 , wherein n is one of 3, 5, 7 and 9.

进一步地,所述浓硫酸的质量百分比为96~99%。Furthermore, the mass percentage of the concentrated sulfuric acid is 96-99%.

进一步地,所述含氟烯烃和所述浓硫酸的摩尔比为1:1~2。Furthermore, the molar ratio of the fluorine-containing olefin to the concentrated sulfuric acid is 1:1-2.

进一步地,反应温度为80~160℃,反应时间为12~24h。Furthermore, the reaction temperature is 80-160° C., and the reaction time is 12-24 hours.

进一步地,所述水和所述含氟烯烃的体积比为0.1~1:1。Furthermore, the volume ratio of the water to the fluorine-containing olefin is 0.1 to 1:1.

进一步地,水解反应的温度为160~180℃,反应时间为12~18h。Furthermore, the temperature of the hydrolysis reaction is 160-180° C., and the reaction time is 12-18 hours.

进一步地,所述干燥的步骤具体包括:所述下层透明溶液经水洗后加入无水硫酸镁吸水干燥,得到全氟烷基乙醇。Furthermore, the drying step specifically includes: the lower transparent solution is washed with water, and then anhydrous magnesium sulfate is added to absorb water and dry to obtain perfluoroalkylethanol.

本发明提出一种全氟烷基乙醇,其根据所述的制备方法制得,所述全氟烷基乙醇的化学结构式如下:The present invention provides a perfluoroalkylethanol, which is prepared according to the preparation method, and the chemical structure of the perfluoroalkylethanol is as follows:

其中,n为3,5,7,9中的一个。 Here, n is one of 3, 5, 7, and 9.

本发明实施例的全氟烷基乙醇及其制备方法的有益效果是:The beneficial effects of the perfluoroalkylethanol and the preparation method thereof according to the embodiment of the present invention are:

本发明先利用浓硫酸与含氟烯烃进行加成反应,得到的产物再进行水解反应,即可得到全氟烷基乙醇。该方法不仅能够很好地控制反应进程,大大地缩短了反应时间,而且全氟烷基乙醇的产率稳定。The present invention firstly uses concentrated sulfuric acid to carry out addition reaction with fluorine-containing olefins, and then carries out hydrolysis reaction on the obtained product to obtain perfluoroalkyl ethanol. The method can not only well control the reaction process and greatly shorten the reaction time, but also stabilize the yield of perfluoroalkyl ethanol.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

为了更清楚地说明本发明实施例的技术方案,下面将对实施例中所需要使用的附图作简单地介绍,应当理解,以下附图仅示出了本发明的某些实施例,因此不应被看作是对范围的限定,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他相关的附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the drawings required for use in the embodiments are briefly introduced below. It should be understood that the following drawings only show certain embodiments of the present invention and therefore should not be regarded as limiting the scope. For ordinary technicians in this field, other related drawings can be obtained based on these drawings without creative work.

图1为本发明实施例2的全氟己基乙醇的气相色谱图;FIG1 is a gas chromatogram of perfluorohexylethanol of Example 2 of the present invention;

图2为本发明的全氟烷基乙醇的制备流程图。FIG. 2 is a flow chart of the preparation of perfluoroalkylethanol of the present invention.

具体实施方式DETAILED DESCRIPTION

为使本发明实施例的目的、技术方案和优点更加清楚,下面将对本发明实施例中的技术方案进行清楚、完整地描述。实施例中未注明具体条件者,按照常规条件或制造商建议的条件进行。所用试剂或仪器未注明生产厂商者,均为可以通过市售购买获得的常规产品。In order to make the purpose, technical scheme and advantages of the embodiments of the present invention clearer, the technical scheme in the embodiments of the present invention will be described clearly and completely below. If the specific conditions are not specified in the embodiments, they are carried out according to conventional conditions or conditions recommended by the manufacturer. If the manufacturer of the reagents or instruments used is not specified, they are all conventional products that can be purchased commercially.

下面对本发明实施例的全氟烷基乙醇及其制备方法进行具体说明。The perfluoroalkylethanol according to the embodiment of the present invention and the preparation method thereof are described in detail below.

参照图2所示,本发明实施例提供的一种全氟烷基乙醇的制备方法,包括以下步骤:2, a method for preparing perfluoroalkylethanol provided in an embodiment of the present invention comprises the following steps:

S1、含氟烯烃和浓硫酸在氮气氛围下反应,得到加成产物。S1, fluorinated olefin and concentrated sulfuric acid react under a nitrogen atmosphere to obtain an addition product.

进一步地,在本发明较佳实施例中,所述含氟烯烃为CF3(CF2)nCH=CH2,其中,n为3,5,7,9中的一个。Furthermore, in a preferred embodiment of the present invention, the fluorine-containing olefin is CF 3 (CF 2 ) n CH=CH 2 , wherein n is one of 3, 5, 7 and 9.

进一步地,在本发明较佳实施例中,所述浓硫酸的质量百分比为96~99%。优选地,浓硫酸的质量百分比为98%。Furthermore, in a preferred embodiment of the present invention, the mass percentage of the concentrated sulfuric acid is 96-99%. Preferably, the mass percentage of the concentrated sulfuric acid is 98%.

进一步地,在本发明较佳实施例中,所述含氟烯烃和所述浓硫酸的摩尔比为1:1~2。Furthermore, in a preferred embodiment of the present invention, the molar ratio of the fluorine-containing olefin to the concentrated sulfuric acid is 1:1-2.

进一步地,在本发明较佳实施例中,反应温度为80~160℃,反应时间为12~24h。Furthermore, in a preferred embodiment of the present invention, the reaction temperature is 80-160° C., and the reaction time is 12-24 hours.

S2、在带磁力搅拌的高压反应釜中加入所述加成产物后,缓慢加入水进行水解反应,静置、分层后,取下层透明溶液经水洗、干燥,得到全氟烷基乙醇。S2. After adding the addition product into a high-pressure reactor with magnetic stirring, slowly adding water to carry out a hydrolysis reaction. After standing and stratification, taking the lower layer of transparent solution, washing with water, and drying, to obtain perfluoroalkylethanol.

进一步地,在本发明较佳实施例中,所述水和所述含氟烯烃的体积比为0.1~1:1。Furthermore, in a preferred embodiment of the present invention, the volume ratio of the water to the fluorine-containing olefin is 0.1 to 1:1.

进一步地,在本发明较佳实施例中,水解反应的温度为160~180℃,反应时间为12~18h。Furthermore, in a preferred embodiment of the present invention, the temperature of the hydrolysis reaction is 160-180° C., and the reaction time is 12-18 hours.

进一步地,在本发明较佳实施例中,所述干燥的步骤具体包括:所述下层透明溶液经水洗后加入无水硫酸镁吸水干燥,得到全氟烷基乙醇。Furthermore, in a preferred embodiment of the present invention, the drying step specifically includes: the lower transparent solution is washed with water, and then anhydrous magnesium sulfate is added to absorb water and dry to obtain perfluoroalkylethanol.

本发明先利用硫酸与含氟烯烃进行加成反应,然后再进行水解反应,即可得到全氟烷基乙醇。该方法不仅能够很好地控制反应进程,大大地缩短了反应时间,而且全氟烷基乙醇的产率稳定。The present invention firstly utilizes sulfuric acid and fluorine-containing olefins to carry out addition reaction, and then carries out hydrolysis reaction to obtain perfluoroalkyl ethanol. The method can not only well control the reaction process and greatly shorten the reaction time, but also stabilize the yield of perfluoroalkyl ethanol.

本发明还提出了一种全氟烷基乙醇,其根据所述的制备方法制得,所述全氟烷基乙醇的化学结构式如下:The present invention also provides a perfluoroalkylethanol, which is prepared according to the preparation method, and the chemical structure of the perfluoroalkylethanol is as follows:

其中,n为3,5,7,9中的一个。 Here, n is one of 3, 5, 7, and 9.

以下结合实施例对本发明的特征和性能作进一步的详细描述。The features and performance of the present invention are further described in detail below in conjunction with the embodiments.

实施例1Example 1

本实施例提供的一种全氟烷基乙醇,其根据以下方法制备得到:A perfluoroalkylethanol provided in this embodiment is prepared according to the following method:

(1)将含氟烯烃和浓度为98%的浓硫酸加入到三口烧瓶中,通氮气,在80℃的温度下反应18h。其中,含氟烯烃为CF3(CF2)3CH=CH2,含氟烯烃和浓硫酸的摩尔比为1:1。(1) Add fluorinated olefin and 98% concentrated sulfuric acid into a three-necked flask, pass nitrogen, and react at 80°C for 18 hours. The fluorinated olefin is CF 3 (CF 2 ) 3 CH=CH 2 , and the molar ratio of the fluorinated olefin to the concentrated sulfuric acid is 1:1.

(2)在带磁力搅拌的高压反应釜中,加入经过步骤S1反应得到的产品,并在高压釜中缓慢加入水并在160℃下反应12h。其中,高压反应釜中加入的水与含氟烯烃的体积比为0.1:1。反应结束后静置,分层,取下层透明溶液水洗后加入无水硫酸镁吸水干燥,得到全氟烷基乙醇,其化学结构式如下所示:(2) Add the product obtained in step S1 to a high-pressure reactor with magnetic stirring, slowly add water to the autoclave and react at 160° C. for 12 hours. The volume ratio of water to fluorinated olefin added to the autoclave is 0.1:1. After the reaction is completed, let it stand, separate the layers, take the transparent solution layer, wash it with water, add anhydrous magnesium sulfate to absorb water and dry it, and obtain perfluoroalkylethanol, whose chemical structure is as follows:

实施例2Example 2

本实施例中提供了一种全氟烷基乙醇,其根据以下方法制备得到:In this embodiment, a perfluoroalkylethanol is provided, which is prepared according to the following method:

(1)将含氟烯烃和浓度为98%的浓硫酸加入到三口烧瓶中,通氮气,在160℃的温度下反应20h。其中,含氟烯烃为CF3(CF2)5CH=CH2,含氟烯烃和浓硫酸的摩尔比为1:1.2。(1) Add fluorinated olefin and 98% concentrated sulfuric acid into a three-necked flask, pass nitrogen, and react at 160°C for 20 hours. The fluorinated olefin is CF 3 (CF 2 ) 5 CH=CH 2 , and the molar ratio of the fluorinated olefin to the concentrated sulfuric acid is 1:1.2.

(2)在带磁力搅拌的高压反应釜中,加入经过步骤S1反应得到的产品,并在高压釜中缓慢加入水并在165℃下反应18h。其中,高压反应釜中加入的水与含氟烯烃的体积比为0.5:1。反应结束后静置,分层,取下层透明溶液水洗后加入无水硫酸镁吸水干燥,得到全氟烷基乙醇(全氟己基乙醇,图1所示为其气相色谱图),其化学结构式如下所示:(2) Add the product obtained by the reaction in step S1 to a high-pressure reactor with magnetic stirring, slowly add water to the autoclave and react at 165° C. for 18 hours. The volume ratio of water to fluorinated olefin added to the autoclave is 0.5:1. After the reaction is completed, let it stand and separate into layers. Wash the lower layer of transparent solution with water, add anhydrous magnesium sulfate to absorb water and dry it to obtain perfluoroalkylethanol (perfluorohexylethanol, FIG1 shows its gas chromatogram), and its chemical structure is as follows:

实施例3Example 3

本实施例中提供了一种全氟烷基乙醇,其根据以下方法制备得到:In this embodiment, a perfluoroalkylethanol is provided, which is prepared according to the following method:

(1)将含氟烯烃和浓度为98%的浓硫酸加入到三口烧瓶中,通氮气,在100℃的温度下反应24h。其中,含氟烯烃为CF3(CF2)7CH=CH2,含氟烯烃和浓硫酸的摩尔比为1:1.5。(1) Add fluorinated olefin and 98% concentrated sulfuric acid into a three-necked flask, pass nitrogen, and react at 100°C for 24 hours. The fluorinated olefin is CF 3 (CF 2 ) 7 CH=CH 2 , and the molar ratio of the fluorinated olefin to the concentrated sulfuric acid is 1:1.5.

(2)在带磁力搅拌的高压反应釜中,加入经过步骤S1反应得到的产品,并在高压釜中缓慢加入水并在170℃下反应16h。其中,高压反应釜中加入的水与含氟烯烃的体积比为0.8:1。反应结束后静置,分层,取下层透明溶液水洗后加入无水硫酸镁吸水干燥,得到全氟烷基乙醇,其化学结构式如下所示:(2) Add the product obtained in step S1 to a high-pressure reactor with magnetic stirring, slowly add water to the autoclave and react at 170° C. for 16 hours. The volume ratio of water to fluorinated olefin added to the autoclave is 0.8:1. After the reaction is completed, let it stand, separate the layers, take the transparent solution layer, wash it with water, add anhydrous magnesium sulfate to absorb water and dry it, and obtain perfluoroalkylethanol, whose chemical structure is as follows:

实施例4Example 4

本实施例中提供了一种全氟烷基乙醇,其根据以下方法制备得到:In this embodiment, a perfluoroalkylethanol is provided, which is prepared according to the following method:

(1)将含氟烯烃和浓度为98%的浓硫酸加入到三口烧瓶中,通氮气,在120℃的温度下反应12h。其中,含氟烯烃为CF3(CF2)9CH=CH2,含氟烯烃和浓硫酸的摩尔比为1:2。(1) Add fluorinated olefin and 98% concentrated sulfuric acid into a three-necked flask, pass nitrogen, and react at 120° C. for 12 h. The fluorinated olefin is CF 3 (CF 2 ) 9 CH=CH 2 , and the molar ratio of the fluorinated olefin to the concentrated sulfuric acid is 1:2.

(2)在带磁力搅拌的高压反应釜中,加入经过步骤S1反应得到的产品,并在高压釜中缓慢加入水并在180℃下反应15h。其中,高压反应釜中加入的水与含氟烯烃的体积比为1:1。反应结束后静置,分层,取下层透明溶液水洗后加入无水硫酸镁吸水干燥,得到全氟烷基乙醇,其化学结构式如下所示:(2) Add the product obtained in step S1 to a high-pressure reactor with magnetic stirring, slowly add water to the autoclave and react at 180° C. for 15 hours. The volume ratio of water to fluorinated olefin added to the autoclave is 1:1. After the reaction is completed, let it stand, separate the layers, take the transparent solution layer, wash it with water, add anhydrous magnesium sulfate to absorb water and dry it, and obtain perfluoroalkylethanol, whose chemical structure is as follows:

以上所描述的实施例是本发明一部分实施例,而不是全部的实施例。本发明的实施例的详细描述并非旨在限制要求保护的本发明的范围,而是仅仅表示本发明的选定实施例。基于本发明中的实施例,本领域普通技术人员在没有作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。The embodiments described above are part of the embodiments of the present invention, rather than all of the embodiments. The detailed description of the embodiments of the present invention is not intended to limit the scope of the invention claimed for protection, but merely represents selected embodiments of the present invention. Based on the embodiments of the present invention, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the present invention.

Claims (7)

1. A method for preparing perfluoroalkyl ethanol, which is characterized by comprising the following steps:
S1, reacting fluorine-containing olefin with concentrated sulfuric acid under a nitrogen atmosphere to obtain an addition product, wherein the fluorine-containing olefin is CF 3(CF2)nCH=CH2, and n is one of 3,5,7 and 9;
S2, adding the addition product into a high-pressure reaction kettle with magnetic stirring, slowly adding water for hydrolysis reaction, standing, layering, taking a lower transparent solution, washing with water, and drying to obtain perfluoroalkyl ethanol, wherein the chemical structural formula of the perfluoroalkyl ethanol is as follows:
Wherein n is one of 3,5,7, 9.
2. The method for producing perfluoroalkyl ethanol according to claim 1, wherein in step S1, the mass percentage of the concentrated sulfuric acid is 96-99%.
3. The method for producing perfluoroalkyl ethanol according to claim 1, wherein in step S1, the molar ratio of the fluoroolefin to the concentrated sulfuric acid is 1:1-2.
4. The process for producing perfluoroalkyl ethanol according to claim 1, wherein in step S1, the reaction temperature is 80-160 ℃ and the reaction time is 12-24 hours.
5. The method for producing perfluoroalkyl ethanol according to claim 1, wherein the volume ratio of the water to the fluorine-containing olefin is 0.1-1:1.
6. The process for producing perfluoroalkyl ethanol according to claim 1, wherein in step S2, the hydrolysis reaction is carried out at 160 to 180 ℃ for 12 to 18 hours.
7. The method for producing perfluoroalkyl ethanol according to claim 1, wherein in step S2, the step of drying specifically comprises: and washing the lower transparent solution with water, adding anhydrous magnesium sulfate, and drying to obtain the perfluoroalkyl alcohol.
CN202211302371.6A 2022-10-24 2022-10-24 Perfluoroalkyl ethanol and preparation method thereof Active CN115894168B (en)

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Publication number Priority date Publication date Assignee Title
CN105732328A (en) * 2016-04-19 2016-07-06 四川西艾氟科技有限公司 Method for preparing perfluoroalkyl alcohol from perfluoroalkyl ethylene

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105732328A (en) * 2016-04-19 2016-07-06 四川西艾氟科技有限公司 Method for preparing perfluoroalkyl alcohol from perfluoroalkyl ethylene

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