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CN118702543B - Pentafluoropentanol and method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane - Google Patents

Pentafluoropentanol and method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane Download PDF

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CN118702543B
CN118702543B CN202411203278.9A CN202411203278A CN118702543B CN 118702543 B CN118702543 B CN 118702543B CN 202411203278 A CN202411203278 A CN 202411203278A CN 118702543 B CN118702543 B CN 118702543B
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pentafluoropentanol
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pentafluoroethane
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CN118702543A (en
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夏凯
曾佳鑫
窦志群
董崔
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Zibo Feiyuan Chemical Co ltd
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Abstract

本发明属于氟化工技术领域,具体涉及五氟戊醇以及利用副产五氟氯乙烷合成五氟戊醇的方法。本发明所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:将副产五氟氯乙烷加入醚类溶剂中,得到溶液A;将镁屑加入到醚类溶剂中,得到溶液B;在60℃将1/5‑1/3体积的溶液A加入到溶液B中,引发反应;将剩余溶液A加入到溶液B中,进行格氏反应,得到五氟乙烷氯化镁溶液;将五氟乙烷氯化镁溶液降温至0℃,加入氧杂环丁烷,进行开环反应,反应结束后,处理得到五氟戊醇粗品;将五氟戊醇粗品精馏,得到五氟戊醇。本发明提供的利用副产五氟氯乙烷合成五氟戊醇的方法,节约成本,过程环保,反应速度快,所合成的五氟戊醇收率高。The present invention belongs to the technical field of fluorine chemical industry, and in particular to pentafluoropentanol and a method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane. The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane of the present invention comprises the following steps: adding by-product pentafluorochloroethane to an ether solvent to obtain solution A; adding magnesium chips to an ether solvent to obtain solution B; adding 1/5-1/3 volume of solution A to solution B at 60°C to initiate a reaction; adding the remaining solution A to solution B, performing a Grignard reaction, and obtaining a pentafluoroethane magnesium chloride solution; cooling the pentafluoroethane magnesium chloride solution to 0°C, adding oxetane, performing a ring-opening reaction, and after the reaction is terminated, processing to obtain a crude pentafluoropentanol product; rectifying the crude pentafluoropentanol product to obtain pentafluoropentanol. The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane provided by the present invention saves costs, has an environmentally friendly process, has a fast reaction speed, and has a high yield of the synthesized pentafluoropentanol.

Description

五氟戊醇以及利用副产五氟氯乙烷合成五氟戊醇的方法Pentafluoropentanol and method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane

技术领域Technical Field

本发明属于氟化工技术领域,具体涉及五氟戊醇以及利用副产五氟氯乙烷合成五氟戊醇的方法。The invention belongs to the technical field of fluorine chemical industry, and specifically relates to pentafluoropentanol and a method for synthesizing pentafluoropentanol by utilizing by-product pentafluorochloroethane.

背景技术Background Art

五氟戊醇,又称为4,4,5,5,5-五氟戊醇,无色液体,分子量为178.1,沸点为62℃-64℃,密度:1.35g/mL,结构式为Pentafluoropentanol, also known as 4,4,5,5,5-pentafluoropentanol, is a colorless liquid with a molecular weight of 178.1, a boiling point of 62°C-64°C, a density of 1.35g/mL, and a structural formula of .

五氟戊醇是氟维司群(雌激素受体拮抗剂)的关键中间体,该化合物也是表面活性剂、染料和功能材料单体的重要原料,应用非常广泛。目前主要的合成方法主要有四种:一是以4,4,5,5,5-五氟-2-碘-1-戊醇或4,4,5,5,5-五氟-2-碘戊-2-烯-1-醇为原料经过还原合成五氟戊醇。二是以3-溴-1,1,1,2,2-五氟丙烷为原料做成格氏试剂,再与环氧乙烷开环并酸化合成五氟戊醇。三是以五氟碘乙烷为原料与蒜醇,在催化剂和配体的作用下,合成五氟戊醇。四是以1,1,1,2,2-五氟戊烷为原料,在催化剂存在下与过氧化氢异丙苯反应,合成五氟戊醇。但以上方法都各自存在缺点。Pentafluoropentanol is a key intermediate of Fulvestrant (estrogen receptor antagonist). This compound is also an important raw material for surfactants, dyes and functional material monomers, and is widely used. There are four main synthesis methods: one is to synthesize pentafluoropentanol by reduction using 4,4,5,5,5-pentafluoro-2-iodo-1-pentanol or 4,4,5,5,5-pentafluoro-2-iodopent-2-ene-1-ol as raw materials. The second is to use 3-bromo-1,1,1,2,2-pentafluoropropane as raw material to make Grignard reagent, and then open the ring with ethylene oxide and acidify to synthesize pentafluoropentanol. The third is to use pentafluoroiodoethane as raw material and allicinol, in the presence of catalysts and ligands, to synthesize pentafluoropentanol. The fourth is to use 1,1,1,2,2-pentafluoropentane as raw material, and react with isopropylbenzene hydroperoxide in the presence of a catalyst to synthesize pentafluoropentanol. However, the above methods all have their own shortcomings.

公开专利CN111004091A提到,在负载贵金属复合催化剂Pt/AlF3、溶剂和氧化剂存在下,80℃反应2h,一步法催化氧化1,1,1,2,2-五氟丙烷合成五氟戊醇,具有反应操作简单、选择性高等优点。但是使用的铂催化剂价格昂贵,成本较高,大规模工业应用受到限制。Patent publication CN111004091A mentions that in the presence of a loaded precious metal composite catalyst Pt/AlF 3 , a solvent and an oxidant, the reaction is carried out at 80°C for 2 hours to catalyze and oxidize 1,1,1,2,2-pentafluoropropane to synthesize pentafluoropentanol in one step, which has the advantages of simple reaction operation and high selectivity. However, the platinum catalyst used is expensive and has high cost, which limits its large-scale industrial application.

公开专利CN114853568A提到,在室温下将催化剂和配体溶解在有机溶剂中,反应一定时间后,加入烯丙醇、碱、氟源和氢供体,进行反应,得到4,4,5,5,5-五氟戊醇。该路线具有环保等优点,但是需要提前制备催化剂和配体,操作繁琐,并且烯丙醇为剧毒物质,操作不便,具有较大风险。Patent publication CN114853568A mentions that the catalyst and ligand are dissolved in an organic solvent at room temperature, reacted for a certain period of time, and then allyl alcohol, alkali, fluorine source and hydrogen donor are added to react to obtain 4,4,5,5,5-pentafluoropentanol. This route has advantages such as environmental protection, but it requires the preparation of catalysts and ligands in advance, the operation is cumbersome, and allyl alcohol is a highly toxic substance, which is inconvenient to operate and has great risks.

公开专利CN107501044A提到的五氟戊醇的制备方法,以及2019年Williams,Jason等人在Organic Letters(2019,vol.21,13,p.5341-5345)上发表的论文中,以丙烯醇和五氟碘乙烷或五氟溴乙烷为原料,通过自由基引发剂合成4,4,5,5,5-五氟-2-溴-1-戊醇或者4,4,5,5,5-五氟-2-碘-1-戊醇,再经过过渡金属催化剂催化脱卤反应得到五氟戊醇。该工艺用到的自由基引发剂,反应不容易控制,大量生产时会有较高的安全风险。The preparation method of pentafluoropentanol mentioned in the patent CN107501044A, and the paper published by Williams, Jason et al. in Organic Letters (2019, vol. 21, 13, p. 5341-5345) in 2019, allyl alcohol and pentafluoroiodoethane or pentafluorobromoethane are used as raw materials, and 4,4,5,5,5-pentafluoro-2-bromo-1-pentanol or 4,4,5,5,5-pentafluoro-2-iodo-1-pentanol is synthesized by free radical initiator, and then pentafluoropentanol is obtained by dehalogenation reaction catalyzed by transition metal catalyst. The free radical initiator used in this process is not easy to control the reaction, and there will be a high safety risk in mass production.

1994年Shankar M.Singh等人在Tetrahedron Letters(Tetrahedron Letters,1994,vol.35,#49,p.9141-9144)公开的在亚硫酸氢钠存在下,将全氟乙基碘化物定量自由基加成炔丙醇,得到E/Z-2-碘-4,4,5,5,5-五氟-2-戊烯-1-醇,在三乙胺存在下,通过催化氢化氧化铂,一步转化为4,4,5,5,5-五氟戊烷-1-醇。该路线应用了昂贵的Pt催化剂,不适合工业化。In 1994, Shankar M. Singh et al. published in Tetrahedron Letters (Tetrahedron Letters, 1994, vol. 35, #49, p. 9141-9144) that in the presence of sodium bisulfite, perfluoroethyl iodide was subjected to quantitative free radical addition to propargyl alcohol to obtain E/Z-2-iodo-4,4,5,5,5-pentafluoro-2-pentene-1-ol, which was converted into 4,4,5,5,5-pentafluoropentane-1-ol in one step by catalytic hydrogenation of platinum oxide in the presence of triethylamine. This route uses expensive Pt catalysts and is not suitable for industrialization.

公开专利CN116162016A提到,以丙酰氯为原料,生成的全氟丙酰氟与硼氢化钠、甲醇反应生成2,2,3,3,3-五氟丙醇,2,2,3,3,3-五氟丙醇与三溴化磷发生取代反应,生成1-溴-2,2,3,3,3-五氟丙烷,1-溴-2,2,3,3,3-五氟丙烷与镁粉反应生成格氏试剂,与环氧乙烷生成五氟戊醇粗品,精馏得到高纯五氟戊醇。采用的硼氢化钠和三溴化磷在工业上使用存在较大的安全风险,硼氢化钠价格较昂贵。Patent CN116162016A mentioned that propionyl chloride is used as raw material, and the generated perfluoropropionyl fluoride reacts with sodium borohydride and methanol to generate 2,2,3,3,3-pentafluoropropanol, 2,2,3,3,3-pentafluoropropanol and phosphorus tribromide undergo substitution reaction to generate 1-bromo-2,2,3,3,3-pentafluoropropane, 1-bromo-2,2,3,3,3-pentafluoropropane reacts with magnesium powder to generate Grignard reagent, and reacts with ethylene oxide to generate crude pentafluoropentanol, and high-purity pentafluoropentanol is obtained by distillation. The sodium borohydride and phosphorus tribromide used have great safety risks in industrial use, and the price of sodium borohydride is relatively expensive.

发明内容Summary of the invention

本发明要解决的技术问题是克服现有技术存在的上述缺陷,提供利用副产五氟氯乙烷合成五氟戊醇的方法,节约成本,过程环保,反应速度快,所合成的五氟戊醇收率高。The technical problem to be solved by the present invention is to overcome the above-mentioned defects of the prior art and provide a method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane, which saves costs, is environmentally friendly, has a fast reaction speed, and has a high yield of the synthesized pentafluoropentanol.

本发明所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane of the present invention comprises the following steps:

(1)将副产五氟氯乙烷加入溶剂中,得到溶液A,质量分数≥5%;(1) Add the by-product pentafluorochloroethane into the solvent to obtain solution A with a mass fraction of ≥5%;

(2)将镁屑加入到醚类溶剂中,得到溶液B,质量分数≥5%;(2) Add magnesium chips to an ether solvent to obtain solution B with a mass fraction of ≥5%;

(3)在40℃-80℃,将1/5-1/3体积的溶液A以50mL/min速度加入到溶液B中,引发反应;(3) At 40°C-80°C, add 1/5-1/3 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,进行格氏反应,得到五氟乙烷氯化镁溶液;(4) adding the remaining solution A to solution B at a rate of 30 mL/min to carry out a Grignard reaction to obtain a pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至-10℃-0℃,加入氧杂环丁烷,进行开环反应,反应结束后,处理得到五氟戊醇粗品;(5) Cooling the pentafluoroethane magnesium chloride solution to -10°C to 0°C, adding oxetane to carry out a ring-opening reaction, and after the reaction is completed, treating to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品精馏,得到五氟戊醇。(6) The crude pentafluoropentanol is distilled to obtain pentafluoropentanol.

所述的副产五氟氯乙烷与镁屑的摩尔比为1:(1-2),优选1:1.2。The molar ratio of the by-product pentafluorochloroethane to the magnesium chips is 1:(1-2), preferably 1:1.2.

步骤(5)所述的五氟乙烷氯化镁理论产出量与氧杂环丁烷的摩尔比为1:(1-1.2),优选1:1.05。The molar ratio of the theoretical output of pentafluoroethane magnesium chloride to oxetane in step (5) is 1:(1-1.2), preferably 1:1.05.

步骤(1)和步骤(2)所述的溶剂为醚类溶剂或者烃类溶剂中的一种,醚类溶剂为四氢呋喃或乙醚,烃类溶剂为苯、甲苯、正己烷、环己烷中的一种。The solvent in step (1) and step (2) is one of an ether solvent or a hydrocarbon solvent, the ether solvent is tetrahydrofuran or diethyl ether, and the hydrocarbon solvent is one of benzene, toluene, n-hexane, and cyclohexane.

步骤(3)控制的引发反应的温度为40-70℃,时间为5-30min。The temperature of the initiation reaction controlled in step (3) is 40-70°C and the time is 5-30 minutes.

步骤(4)的格氏反应温度为30℃-60℃,优选60℃,反应时间为8h-12h,优选8h。The Grignard reaction temperature of step (4) is 30°C-60°C, preferably 60°C, and the reaction time is 8h-12h, preferably 8h.

步骤(5)所述的处理步骤为:将反应结束后的溶液泄压,加水淬灭,蒸馏。The treatment steps described in step (5) are: depressurizing the solution after the reaction is completed, quenching with water, and distilling.

所述的蒸馏温度为60℃-70℃。The distillation temperature is 60°C-70°C.

步骤(5)的开环反应的温度为30℃-50℃,优选30℃,反应时间为2h-4h,优选2h。The temperature of the ring-opening reaction in step (5) is 30°C-50°C, preferably 30°C, and the reaction time is 2h-4h, preferably 2h.

步骤(6)精馏,收集62℃-64℃的馏分。Step (6) distillation, collecting the fraction at 62°C-64°C.

一种五氟戊醇是利用所述的利用副产五氟氯乙烷合成五氟戊醇的方法合成的。A pentafluoropentanol is synthesized by utilizing the method for synthesizing pentafluoropentanol by utilizing by-product pentafluorochloroethane.

具体的,所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:Specifically, the method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane comprises the following steps:

(1)将副产五氟氯乙烷加入3L无水溶剂中,得到溶液A;(1) Add the by-product pentafluorochloroethane into 3 L of anhydrous solvent to obtain solution A;

(2)在高压反应釜上,加装冷凝器和滴液漏斗,加入镁屑、无水醚类溶剂,混合得到溶液B;(2) Install a condenser and a dropping funnel on the high-pressure reactor, add magnesium chips and anhydrous ether solvent, and mix to obtain solution B;

(3)在40℃-80℃,将1/5-1/3体积的溶液A以50mL/min速度加入到溶液B中,引发反应,开启搅拌回流降温,控制反应温度40-70℃和反应时间5-30min;(3) At 40°C-80°C, add 1/5-1/3 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction, start stirring and reflux to cool down, and control the reaction temperature to 40-70°C and the reaction time to 5-30 min;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,30℃-60℃进行格氏反应8h-12h,得到五氟乙烷氯化镁溶液;(4) adding the remaining solution A to solution B at a rate of 30 mL/min, and carrying out a Grignard reaction at 30°C-60°C for 8h-12h to obtain a pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至-10℃-0℃,以1滴/s加入氧杂环丁烷,30℃-50℃进行开环反应2h-4h,反应结束后,泄压,加500g水淬灭,60-70℃蒸馏,得到五氟戊醇粗品;(5) Cool the pentafluoroethane magnesium chloride solution to -10°C-0°C, add oxetane at 1 drop/s, and carry out a ring-opening reaction at 30°C-50°C for 2h-4h. After the reaction is completed, release the pressure, add 500g of water to quench, and distill at 60-70°C to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品加入到精馏塔进行精馏,收集62℃-64℃的馏分,得到高纯五氟戊醇。(6) The crude pentafluoropentanol is added to a distillation tower for distillation, and the fraction at 62° C.-64° C. is collected to obtain high-purity pentafluoropentanol.

本发明首先将五氟氯乙烷通入干燥的醚类溶剂中,缓慢加入到含有镁屑和醚类溶剂的反应容器中经格氏反应制备五氟乙烷氯化镁,再将氧杂环丁烷中缓慢加入到制备的格氏试剂中,经过升温开环,淬灭,粗蒸馏,最终精馏得到最终产物五氟戊醇。The invention firstly introduces pentafluorochloroethane into a dry ether solvent, slowly adds the solvent into a reaction container containing magnesium chips and the ether solvent to prepare pentafluoroethane magnesium chloride through a Grignard reaction, then slowly adds oxetane into the prepared Grignard reagent, performs ring opening by heating, quenching, crude distillation and finally rectification to obtain the final product pentafluoropentanol.

与现有技术相比,本发明具有的有益效果是:Compared with the prior art, the present invention has the following beneficial effects:

(1)本发明的利用副产五氟氯乙烷合成五氟戊醇的方法,反应速度快,满足绿色化学的特点,适合工业化。(1) The method of the present invention for synthesizing pentafluoropentanol using by-product pentafluorochloroethane has a fast reaction speed, meets the characteristics of green chemistry, and is suitable for industrialization.

(2)本发明的利用副产五氟氯乙烷合成五氟戊醇的方法,为处理五氟氯乙烷处理提供新的方法。(2) The method of the present invention for synthesizing pentafluoropentanol using by-product pentafluorochloroethane provides a new method for treating pentafluorochloroethane.

(3)采用本发明的方法合成的五氟戊醇,收率高,纯度高。(3) The pentafluoropentanol synthesized by the method of the present invention has high yield and high purity.

具体实施方式DETAILED DESCRIPTION

下面结合具体实施例对本发明作进一步说明。The present invention will be further described below in conjunction with specific embodiments.

以下实施例和对比例所采用的原料与试剂均为市售产品,其采用的装置均为现有装置。The raw materials and reagents used in the following examples and comparative examples are all commercially available products, and the devices used are all existing devices.

本发明所采用的副产五氟氯乙烷含量≥99%,来自于全氟乙烷氟化过程的副产。本发明所采用的镁屑为正常市售产品,一般常规的尺寸为2mm×3mm×0.6mm,但不仅仅限于此尺寸,只要是市售镁屑都可以满足要求,以下实施例和对比例均采用最常规的镁屑尺寸为常规的2mm×3mm×0.6mm,且本领域技术人员在正常市售购买时,是可以明确分清镁屑和镁粉的,不存在混淆的问题。采用镁屑(2mm×3mm×0.6mm)代替镁粉(粒径0.5mm),经过实验采用镁粉时(其他步骤与实施例1相同),转化率只有70%,五氟戊醇收率只有30.3%。The by-product pentafluorochloroethane used in the present invention has a content of ≥99%, which is a by-product from the fluorination process of perfluoroethane. The magnesium chips used in the present invention are normal commercial products, and the general conventional size is 2mm×3mm×0.6mm, but it is not limited to this size. As long as it is commercially available magnesium chips, it can meet the requirements. The following embodiments and comparative examples all use the most conventional magnesium chips with a conventional size of 2mm×3mm×0.6mm, and those skilled in the art can clearly distinguish magnesium chips and magnesium powder when they are purchased in the normal market, and there is no confusion. Magnesium chips (2mm×3mm×0.6mm) are used instead of magnesium powder (particle size 0.5mm). After experiments using magnesium powder (other steps are the same as in Example 1), the conversion rate is only 70%, and the yield of pentafluoropentanol is only 30.3%.

实施例1Example 1

所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane comprises the following steps:

(1)将4016g(25.99mol)副产五氟氯乙烷加入3L无水四氢呋喃中,得到溶液A;(1) 4016 g (25.99 mol) of by-product pentafluorochloroethane was added to 3 L of anhydrous tetrahydrofuran to obtain solution A;

(2)在高压反应釜上,加装冷凝器和滴液漏斗,加入镁屑(31.19mol)、1L无水四氢呋喃溶剂,混合得到溶液B;(2) A condenser and a dropping funnel were installed on the high pressure reactor, and magnesium chips (31.19 mol) and 1 L of anhydrous tetrahydrofuran solvent were added and mixed to obtain solution B;

(3)在60℃,将1/5体积的溶液A以50mL/min速度加入到溶液B中,引发反应,开启搅拌回流降温,控制反应温度50℃,反应时间10min;(3) At 60°C, add 1/5 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction, start stirring and reflux to cool down, control the reaction temperature to 50°C, and the reaction time to 10 min;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,45℃进行格氏反应9h,得到五氟乙烷氯化镁溶液;(4) Add the remaining solution A to solution B at a rate of 30 mL/min, and carry out Grignard reaction at 45°C for 9 h to obtain pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至0℃,1滴/s加入氧杂环丁烷25.99mol,40℃进行开环反应3h,反应结束后,泄压,加500g水淬灭,65℃蒸馏,得到五氟戊醇粗品;(5) Cool the pentafluoroethane magnesium chloride solution to 0°C, add 25.99 mol of oxetane at 1 drop/s, and carry out a ring-opening reaction at 40°C for 3 hours. After the reaction is completed, release the pressure, add 500 g of water to quench, and distill at 65°C to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品加入到精馏塔进行精馏,收集62℃-64℃的馏分,得到高纯五氟戊醇。(6) The crude pentafluoropentanol is added to a distillation tower for distillation, and the fraction at 62° C.-64° C. is collected to obtain high-purity pentafluoropentanol.

实施例2Example 2

述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane comprises the following steps:

(1)将4016g(25.99mol)副产五氟氯乙烷加入3L无水正己烷中,得到溶液A;(1) 4016 g (25.99 mol) of by-product pentafluorochloroethane was added to 3 L of anhydrous n-hexane to obtain solution A;

(2)在高压反应釜上,加装冷凝器和滴液漏斗,加入镁屑(43.188mol)、1L无水正己烷,混合得到溶液B;(2) Install a condenser and a dropping funnel on the autoclave, add magnesium chips (43.188 mol) and 1 L of anhydrous n-hexane, and mix to obtain solution B;

(3)在70℃,将1/5体积的溶液A以50mL/min速度加入到溶液B中,引发反应,开启搅拌回流降温,控制反应温度70℃,反应时间8min;(3) At 70°C, add 1/5 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction, start stirring and reflux to cool down, control the reaction temperature to 70°C, and the reaction time to 8 min;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,60℃进行格氏反应12h,得到五氟乙烷氯化镁溶液;(4) Add the remaining solution A to solution B at a rate of 30 mL/min, and carry out Grignard reaction at 60°C for 12 h to obtain pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至0℃,以1滴/s加入氧杂环丁烷,30℃进行开环反应4h,反应结束后,泄压,加500g水淬灭,60℃蒸馏,得到五氟戊醇粗品;(5) Cool the pentafluoroethane magnesium chloride solution to 0°C, add oxetane at 1 drop/s, and carry out a ring-opening reaction at 30°C for 4 hours. After the reaction is completed, release the pressure, add 500 g of water to quench, and distill at 60°C to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品加入到精馏塔进行精馏,收集62℃-64℃的馏分,得到高纯五氟戊醇。(6) The crude pentafluoropentanol is added to a distillation tower for distillation, and the fraction at 62° C.-64° C. is collected to obtain high-purity pentafluoropentanol.

实施例3Example 3

所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane comprises the following steps:

(1)将4016g(25.99mol)副产五氟氯乙烷加入3L无水四氢呋喃溶剂中,得到溶液A;(1) 4016 g (25.99 mol) of by-product pentafluorochloroethane was added to 3 L of anhydrous tetrahydrofuran solvent to obtain solution A;

(2)在高压反应釜上,加装冷凝器和滴液漏斗,加入镁屑(35mol)、1L无水四氢呋喃溶剂,混合得到溶液B;(2) Install a condenser and a dropping funnel on the high pressure reactor, add magnesium chips (35 mol) and 1 L of anhydrous tetrahydrofuran solvent, and mix to obtain solution B;

(3)在40℃,将1/3体积的溶液A以50mL/min速度加入到溶液B中,引发反应,开启搅拌回流降温,控制反应温度40℃,反应时间30min;(3) At 40°C, add 1/3 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction, start stirring and reflux to cool down, control the reaction temperature to 40°C, and the reaction time to 30 min;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,30℃进行格氏反应12h,得到五氟乙烷氯化镁溶液;(4) Add the remaining solution A to solution B at a rate of 30 mL/min, and carry out Grignard reaction at 30°C for 12 h to obtain pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至0℃,1滴/s加入氧杂环丁烷27mol,30℃进行开环反应4h,反应结束后,泄压,加500g水淬灭,70℃蒸馏,得到五氟戊醇粗品;(5) Cool the pentafluoroethane magnesium chloride solution to 0°C, add 27 mol of oxetane at 1 drop/s, and carry out a ring-opening reaction at 30°C for 4 hours. After the reaction is completed, release the pressure, add 500 g of water to quench, and distill at 70°C to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品加入到精馏塔进行精馏,收集62℃-64℃的馏分,得到高纯五氟戊醇。(6) The crude pentafluoropentanol is added to a distillation tower for distillation, and the fraction at 62° C.-64° C. is collected to obtain high-purity pentafluoropentanol.

实施例4Example 4

所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane comprises the following steps:

(1)将4016g(25.99mol)副产五氟氯乙烷加入3L无水甲苯中,得到溶液A;(1) 4016 g (25.99 mol) of by-product pentafluorochloroethane was added to 3 L of anhydrous toluene to obtain solution A;

(2)在高压反应釜上,加装冷凝器和滴液漏斗,加入镁屑(34mol)、1L无水甲苯溶剂,混合得到溶液B;(2) Install a condenser and a dropping funnel on the high-pressure reactor, add magnesium chips (34 mol) and 1 L of anhydrous toluene solvent, and mix to obtain solution B;

(3)在80℃,将1/5体积的溶液A以50mL/min速度加入到溶液B中,引发反应,开启搅拌回流降温,控制反应温度60℃,反应时间5min;(3) At 80°C, add 1/5 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction, start stirring and reflux to cool down, control the reaction temperature to 60°C, and the reaction time to 5 min;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,60℃进行格氏反应9h,得到五氟乙烷氯化镁溶液;(4) Add the remaining solution A to solution B at a rate of 30 mL/min, and carry out Grignard reaction at 60°C for 9 h to obtain pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至0℃,1滴/s加入氧杂环丁烷27mol,50℃进行开环反应2h,反应结束后,泄压,加500g水淬灭,65℃蒸馏,得到五氟戊醇粗品;(5) Cool the pentafluoroethane magnesium chloride solution to 0°C, add 27 mol of oxetane at 1 drop/s, and carry out a ring-opening reaction at 50°C for 2 h. After the reaction is completed, release the pressure, add 500 g of water to quench, and distill at 65°C to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品加入到精馏塔进行精馏,收集62℃-64℃的馏分,得到高纯五氟戊醇。(6) The crude pentafluoropentanol is added to a distillation tower for distillation, and the fraction at 62° C.-64° C. is collected to obtain high-purity pentafluoropentanol.

实施例5Example 5

所述的利用副产五氟氯乙烷合成五氟戊醇的方法,包括以下步骤:The method for synthesizing pentafluoropentanol using by-product pentafluorochloroethane comprises the following steps:

(1)将4016g(25.99mol)副产五氟氯乙烷加入3L无水乙醚溶剂中,得到溶液A;(1) 4016 g (25.99 mol) of by-product pentafluorochloroethane was added to 3 L of anhydrous ether solvent to obtain solution A;

(2)在高压反应釜上,加装冷凝器和滴液漏斗,加入镁屑(31.19mol)、1L无水乙醚,混合得到溶液B;(2) Install a condenser and a dropping funnel on the autoclave, add magnesium chips (31.19 mol) and 1 L of anhydrous ether, and mix to obtain solution B;

(3)在60℃,将1/3体积的溶液A以50mL/min速度加入到溶液B中,引发反应,开启搅拌回流降温,控制反应温度50℃,反应时间10min;(3) At 60°C, add 1/3 volume of solution A to solution B at a rate of 50 mL/min to initiate the reaction, start stirring and reflux to cool down, control the reaction temperature to 50°C, and the reaction time to 10 min;

(4)将剩余溶液A以30mL/min速度加入到溶液B中,60℃进行格氏反应8h,得到五氟乙烷氯化镁溶液;(4) Add the remaining solution A to solution B at a rate of 30 mL/min, and carry out Grignard reaction at 60°C for 8 h to obtain pentafluoroethane magnesium chloride solution;

(5)将五氟乙烷氯化镁溶液降温至-10℃,1滴/s加入氧杂环丁烷25.99mol,40℃进行开环反应3h,反应结束后,泄压,加500g水淬灭,70℃蒸馏,得到五氟戊醇粗品;(5) Cool the pentafluoroethane magnesium chloride solution to -10°C, add 25.99 mol of oxetane at 1 drop/s, and carry out a ring-opening reaction at 40°C for 3 hours. After the reaction is completed, release the pressure, add 500 g of water to quench, and distill at 70°C to obtain a crude pentafluoropentanol;

(6)将五氟戊醇粗品加入到精馏塔进行精馏,收集62℃-64℃的馏分,得到高纯五氟戊醇。(6) The crude pentafluoropentanol is added to a distillation tower for distillation, and the fraction at 62° C.-64° C. is collected to obtain high-purity pentafluoropentanol.

对比例1Comparative Example 1

本对比例与实施例1相同,将步骤(1)的溶剂替换为二甲基甲酰胺,其他制备相同。This comparative example is the same as Example 1, except that the solvent in step (1) is replaced by dimethylformamide, and the other preparations are the same.

对比例2Comparative Example 2

本对比例与实施例1相同,将步骤(3)的“反应温度50℃”替换为“反应温度20℃”,其他制备相同。This comparative example is the same as Example 1, except that the "reaction temperature of 50° C." in step (3) is replaced by "reaction temperature of 20° C.", and the other preparations are the same.

将以上实施例和对比例制备的五氟戊醇,所得的纯度和转化率以五氟氯乙烷为基准,转化率=五氟氯乙烷实际消耗量/五氟氯乙烷加入总量,纯度结果通过气相色谱确定,所得的收率通过精馏后计算得到,其检测结果如表1所示。The purity and conversion rate of pentafluoropentanol prepared in the above examples and comparative examples were based on pentafluorochloroethane, conversion rate = actual consumption of pentafluorochloroethane/total amount of pentafluorochloroethane added, the purity result was determined by gas chromatography, and the yield was calculated after distillation, and the test results are shown in Table 1.

表1检测结果Table 1 Test results

由表1可以看出,采用本发明的合成方法,不仅将副产五氟氯乙烷得到高效利用,节约了原料成本,反应速度快,所合成的五氟戊醇收率高、纯度高,具有较高的经济效益和环保价值。As can be seen from Table 1, the synthesis method of the present invention not only makes efficient use of the by-product pentafluorochloroethane, saves the cost of raw materials, has a fast reaction speed, and the synthesized pentafluoropentanol has a high yield and high purity, and has high economic benefits and environmental value.

Claims (8)

1. A method for synthesizing pentafluoropentanol by utilizing byproduct pentafluoroethane is characterized in that: the method comprises the following steps:
(1) Adding byproduct pentafluoroethane into a solvent to obtain a solution A;
(2) Adding magnesium chips into a solvent to obtain a solution B;
The solvent in the step (1) and the solvent in the step (2) are both one of ether solvents or hydrocarbon solvents; the ether solvent is tetrahydrofuran or diethyl ether, and the hydrocarbon solvent is one of benzene, toluene, n-hexane and cyclohexane;
(3) Adding 1/5-1/3 volume of the solution A into the solution B at the temperature of 40-80 ℃ to initiate the reaction;
(4) Adding the residual solution A into the solution B, and carrying out Grignard reaction to obtain pentafluoroethane magnesium chloride solution;
(5) Cooling pentafluoroethane magnesium chloride solution to-10-0 ℃, adding oxetane, carrying out ring-opening reaction, and processing after the reaction is finished to obtain a coarse product of pentafluoroethyl alcohol;
(6) And rectifying the crude product of the pentafluoropentanol to obtain the pentafluoropentanol.
2. The method for synthesizing pentafluoropentanol by using by-produced pentafluoroethane as claimed in claim 1, wherein: the molar ratio of the byproduct pentafluoroethane to magnesium turnings is 1:1-2.
3. The method for synthesizing pentafluoropentanol by using by-produced pentafluoroethane as claimed in claim 1, wherein: the theoretical yield of pentafluoroethane magnesium chloride and the mol ratio of oxetane are 1:1-1.2.
4. The method for synthesizing pentafluoropentanol by using by-produced pentafluoroethane as claimed in claim 1, wherein: the Grignard reaction temperature in the step (4) is 30-60 ℃ and the reaction time is 8-12 h.
5. The method for synthesizing pentafluoropentanol by using by-produced pentafluoroethane as claimed in claim 1, wherein: the processing steps of the step (5) are as follows: and (3) decompressing the solution after the reaction is finished, adding water for quenching, and distilling.
6. The method for synthesizing pentafluoropentanol using by-produced pentafluoroethane as claimed in claim 5, wherein: the distillation temperature is 60-70 ℃.
7. The method for synthesizing pentafluoropentanol by using by-produced pentafluoroethane as claimed in claim 1, wherein: the temperature of the ring-opening reaction in the step (5) is 30-50 ℃ and the reaction time is 2-4 h.
8. The method for synthesizing pentafluoropentanol by using by-produced pentafluoroethane as claimed in claim 1, wherein: and (6) rectifying and collecting fractions at 62-64 ℃.
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1136550A (en) * 1995-03-17 1996-11-27 埃尔夫阿托化学有限公司 Hydrogenolysis method for full substituted hydrocarbon containing Cl-F and hydrocarbon containing Cl-F
CN116162016A (en) * 2023-01-09 2023-05-26 山东重山光电材料股份有限公司 Preparation method of high-purity pentafluoropentanol

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1136550A (en) * 1995-03-17 1996-11-27 埃尔夫阿托化学有限公司 Hydrogenolysis method for full substituted hydrocarbon containing Cl-F and hydrocarbon containing Cl-F
CN116162016A (en) * 2023-01-09 2023-05-26 山东重山光电材料股份有限公司 Preparation method of high-purity pentafluoropentanol

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