CN115611806A - A kind of preparation method of 4-trifluoromethyl-3-cyanopyridine - Google Patents

A kind of preparation method of 4-trifluoromethyl-3-cyanopyridine Download PDF

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CN115611806A
CN115611806A CN202211395719.0A CN202211395719A CN115611806A CN 115611806 A CN115611806 A CN 115611806A CN 202211395719 A CN202211395719 A CN 202211395719A CN 115611806 A CN115611806 A CN 115611806A
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金玉存
张健
张璞
陈文新
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Jiangsu Flag Chemical Industry Co ltd
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    • C07D213/02Heterocyclic compounds containing six-membered rings, not condensed with other rings, with one nitrogen atom as the only ring hetero atom and three or more double bonds between ring members or between ring members and non-ring members having three double bonds between ring members or between ring members and non-ring members
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Abstract

本发明涉及有机合成领域,尤其涉及一种4‑三氟甲基‑3‑氰基吡啶的制备方法,包括如下步骤:以2,6‑二氯‑3‑氰基‑4‑(三氟甲基)吡啶为起始原料,二异丙基乙基胺为缚酸剂,在氢气和催化剂的作用下,脱氯制备4‑三氟甲基‑3‑氰基吡啶。本发明在加氢脱氯过程中以二异丙基乙基胺为缚酸剂,选择性高,无副反应,反应时间短、产品收率、纯度高,后处理简单,适合工业化生产。

Figure 202211395719

The present invention relates to the field of organic synthesis, in particular to a preparation method of 4-trifluoromethyl-3-cyanopyridine, comprising the following steps: using 2,6-dichloro-3-cyano-4-(trifluoromethyl Base) pyridine as starting raw material, diisopropylethylamine as acid binding agent, under the effect of hydrogen and catalyst, dechlorination prepares 4-trifluoromethyl-3-cyanopyridine. The invention uses diisopropylethylamine as an acid-binding agent in the hydrodechlorination process, has high selectivity, no side reaction, short reaction time, high product yield and purity, simple post-treatment, and is suitable for industrial production.

Figure 202211395719

Description

一种4-三氟甲基-3-氰基吡啶的制备方法A kind of preparation method of 4-trifluoromethyl-3-cyanopyridine

技术领域technical field

本发明涉及有机合成技术领域,尤其涉及一种4-三氟甲基-3-氰基吡啶的制备方法。The invention relates to the technical field of organic synthesis, in particular to a preparation method of 4-trifluoromethyl-3-cyanopyridine.

背景技术Background technique

4-三氟甲基-3-氰基吡啶是有用的合成中间体,经过一步碱解反应可以合成4-三氟甲基烟酸。4-三氟甲基烟酸是含三氟甲基芳香化合物,具有独特的生物活性,它可以作为制备其他农药或医药的前体物质,具有重要的价值。4-trifluoromethyl-3-cyanopyridine is a useful synthetic intermediate, and 4-trifluoromethylnicotinic acid can be synthesized through one-step alkali hydrolysis. 4-Trifluoromethylnicotinic acid is an aromatic compound containing trifluoromethyl, which has unique biological activity. It can be used as a precursor for preparing other pesticides or medicines, and has important value.

目前,3-氰基-4-三氟甲基吡啶的合成是以2,6-二氯-3-氰基-4-三氟甲基吡啶为原料,通过加氢催化反应制得。At present, 3-cyano-4-trifluoromethylpyridine is synthesized from 2,6-dichloro-3-cyano-4-trifluoromethylpyridine through hydrogenation catalytic reaction.

专利CN101851193A、CN107286086A、CN108191749A、CN112110855A在加氢催化反应中均采用的是三乙胺作为缚酸剂,但在实际研究中发现,2,6-二氯-3-氰基-4-三氟甲基吡啶与三乙胺在常温常压条件下即可发生反应,反应式如下:Patents CN101851193A, CN107286086A, CN108191749A, and CN112110855A all use triethylamine as an acid-binding agent in the catalytic hydrogenation reaction, but it is found in actual research that 2,6-dichloro-3-cyano-4-trifluoromethyl Pyridine and triethylamine can react under normal temperature and pressure conditions, and the reaction formula is as follows:

Figure BDA0003931790430000011
Figure BDA0003931790430000011

因此,以三乙胺为缚酸剂,存在严重的副反应干扰,选择性差,收率偏低。Therefore, using triethylamine as an acid-binding agent has serious side reaction interference, poor selectivity, and low yield.

专利CN108586328A、CN109232407A在加氢催化反应中采用无机碱碳酸钠为缚酸剂,但是碳酸钠在非极性溶剂中溶解度差,效果不明显,需要配合甲醇或者乙醇等溶剂使用,但经实验证明,甲醇或者乙醇与2,6-二氯-3-氰基-4-三氟甲基吡啶可以发生以下反应:Patents CN108586328A and CN109232407A use inorganic alkali sodium carbonate as an acid-binding agent in the hydrogenation catalytic reaction, but sodium carbonate has poor solubility in non-polar solvents, and the effect is not obvious. It needs to be used with solvents such as methanol or ethanol, but it has been proved by experiments that Methanol or ethanol reacts with 2,6-dichloro-3-cyano-4-trifluoromethylpyridine as follows:

Figure BDA0003931790430000012
Figure BDA0003931790430000012

因此,碳酸钠为缚酸剂、甲醇或乙醇为溶剂,对于3-氰基-4-三氟甲基吡啶的合成也存在较多问题。而且碳酸钠碱性相对较强,容易引起2,6-二氯-3-氰基-4-三氟甲基吡啶的水解。Therefore, sodium carbonate is an acid-binding agent, and methanol or ethanol is a solvent, and there are many problems for the synthesis of 3-cyano-4-trifluoromethylpyridine. Moreover, sodium carbonate is relatively alkaline, which easily causes the hydrolysis of 2,6-dichloro-3-cyano-4-trifluoromethylpyridine.

发明内容Contents of the invention

本发明的目的是针对现有技术存在的问题提供一种反应时间短、产品收率、纯度高,后处理简单的4-三氟甲基-3-氰基吡啶的制备方法。The object of the present invention is to provide a kind of preparation method of 4-trifluoromethyl-3-cyanopyridine with short reaction time, high product yield, high purity and simple aftertreatment in view of the problems existing in the prior art.

为了达到上述目的,本发明的技术方案是:一种4-三氟甲基-3-氰基吡啶的制备方法,包括如下步骤:In order to achieve the above object, the technical scheme of the present invention is: a kind of preparation method of 4-trifluoromethyl-3-cyanopyridine, comprises the steps:

以2,6-二氯-3-氰基-4-(三氟甲基)吡啶为起始原料,二异丙基乙基胺为缚酸剂,甲苯和水为混合溶剂,在催化剂和氢气的作用下,反应制备4-三氟甲基-3-氰基吡啶,具体反应式如下:With 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine as starting material, diisopropylethylamine as acid-binding agent, toluene and water as mixed solvent, in catalyst and hydrogen Under the effect of reaction preparation 4-trifluoromethyl-3-cyanopyridine, concrete reaction formula is as follows:

Figure BDA0003931790430000021
Figure BDA0003931790430000021

优选的,制备方法包括:在高压反应釜中,加入2,6-二氯-3-氰基-4-(三氟甲基)吡啶、二异丙基乙基胺、甲苯和水、钯碳催化剂,氮气置换后充入氢气,升温反应,取样分析,反应合格后加水,过滤除去催化剂,母液分层,油层脱溶后减压蒸馏得4-三氟甲基-3-氰基吡啶。Preferably, the preparation method comprises: in an autoclave, add 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, diisopropylethylamine, toluene and water, palladium carbon Catalyst, nitrogen replacement, filled with hydrogen, temperature rise reaction, sampling analysis, after the reaction is qualified, add water, filter to remove the catalyst, layer the mother liquor, desolventize the oil layer, and distill under reduced pressure to obtain 4-trifluoromethyl-3-cyanopyridine.

优选的,2,6-二氯-3-氰基-4-(三氟甲基)吡啶与二异丙基乙基胺的摩尔比为1:1-10。优选的,2,6-二氯-3-氰基-4-(三氟甲基)吡啶与二异丙基乙基胺的摩尔比为1:1-5。Preferably, the molar ratio of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine to diisopropylethylamine is 1:1-10. Preferably, the molar ratio of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine to diisopropylethylamine is 1:1-5.

优选的,混合溶剂甲苯和水的质量比为45:1~3,混合溶剂甲苯和水的质量是2,6-二氯-3-氰基-4-(三氟甲基)吡啶质量的1-10倍。优选的,混合溶剂甲苯和水的质量是2,6-二氯-3-氰基-4-(三氟甲基)吡啶质量的1-5倍。Preferably, the mass ratio of the mixed solvent toluene to water is 45:1-3, and the mass of the mixed solvent toluene and water is 1 of the mass of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine -10 times. Preferably, the mass of the mixed solvent toluene and water is 1-5 times the mass of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine.

优选的,钯碳催化剂Pd的含量为0.5%-10%;Pd/C的用量为2,6-二氯-3-氰基-4-(三氟甲基)吡啶质量的0.05%-10%。Preferably, the content of the palladium carbon catalyst Pd is 0.5%-10%; the amount of Pd/C is 0.05%-10% of the mass of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine .

优选的,钯碳催化剂Pd的含量为0.5%-10%;Pd/C的用量为2,6-二氯-3-氰基-4-(三氟甲基)吡啶质量的0.05%-5%。优选的,Pd/C的用量为2,6-二氯-3-氰基-4-(三氟甲基)吡啶质量的0.5%-5%。Preferably, the palladium-carbon catalyst Pd content is 0.5%-10%; the amount of Pd/C is 0.05%-5% of the mass of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine . Preferably, the amount of Pd/C used is 0.5%-5% of the mass of 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine.

优选的,氢气的压力为0.1Mpa-10Mpa。Preferably, the pressure of hydrogen is 0.1Mpa-10Mpa.

优选的,氢气的压力为0.1Mpa-5Mpa。优选的,氢气的压力为0.1Mpa-3Mpa。Preferably, the pressure of hydrogen is 0.1Mpa-5Mpa. Preferably, the pressure of hydrogen is 0.1Mpa-3Mpa.

优选的,加氢过程中反应温度为20℃-120℃。优选的,加氢过程中反应温度为50℃-100℃。Preferably, the reaction temperature during hydrogenation is 20°C-120°C. Preferably, the reaction temperature during hydrogenation is 50°C-100°C.

优选的,加氢反应时间为1-10h。优选的,加氢反应时间为1-5h。Preferably, the hydrogenation reaction time is 1-10 h. Preferably, the hydrogenation reaction time is 1-5h.

本发明的有益效果为:本发明提供的一种4-三氟甲基-3-氰基吡啶的制备方法,以二异丙基乙基胺为缚酸剂,甲苯和水为混合溶剂的反应体系。二异丙基乙基胺因其位阻较大的缘故,不会与2,6-二氯-3-氰基-4-三氟甲基吡啶发生副反应,其碱性适中,能较好的与生成的氯化氢形成盐酸盐。二异丙基乙基胺提高了反应的选择性和反应速度,提高了反应收率,从而降低了生产成本。二异丙基乙基胺形成盐酸盐后,可以通过加碱中和盐酸的方式重新生成二异丙基乙基胺,可以回收套用。二异丙基乙基胺与水几乎不溶,稳定性较三乙胺好,回收过程中几乎不产生损失,适合用于工业生产。使用甲苯和水的混合溶剂体系,避免了醇类物质与2,6-二氯-3-氰基-4-(三氟甲基)吡啶的副反应,简化了反应后处理流程,优化了反应操作。甲苯中混合的少量水,可以有效溶解反应过程中产生的二异丙基乙基胺盐酸盐,使其以液态的形式分散在反应体系中,避免了二异丙基乙基胺盐酸盐以固体形式析出。二异丙基乙基胺盐酸盐的析出会包裹钯碳催化剂,导致催化剂失活。因此,甲苯和水的混合溶剂体系,与单独的甲苯或者醇类溶剂相比,可以有效避免钯碳催化剂失活的问题,也不会有类似醇类溶剂的副反应发生。该方法原料易得,成本低廉,步骤短,简化了工艺流程,产品含量、收率高,可以大大降低成本,提高产量,适合工业化生产。The beneficial effect of the present invention is: a kind of preparation method of 4-trifluoromethyl-3-cyanopyridine provided by the present invention, using diisopropylethylamine as acid-binding agent, toluene and water as mixed solvent system. Due to its large steric hindrance, diisopropylethylamine will not react with 2,6-dichloro-3-cyano-4-trifluoromethylpyridine. Its basicity is moderate and its energy is good. and the resulting hydrogen chloride to form hydrochloride. The diisopropylethylamine improves the selectivity and the reaction speed of the reaction, increases the reaction yield, thereby reduces the production cost. After diisopropylethylamine forms hydrochloride, diisopropylethylamine can be regenerated by adding alkali to neutralize hydrochloric acid, which can be recycled and used mechanically. Diisopropylethylamine is almost insoluble in water, has better stability than triethylamine, and almost no loss in the recovery process, so it is suitable for industrial production. Using a mixed solvent system of toluene and water avoids side reactions between alcohols and 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, simplifies the post-reaction treatment process, and optimizes the reaction operate. A small amount of water mixed in toluene can effectively dissolve the diisopropylethylamine hydrochloride produced in the reaction process, making it dispersed in the reaction system in liquid form, avoiding the diisopropylethylamine hydrochloride Precipitated in solid form. The precipitation of diisopropylethylamine hydrochloride will wrap the palladium carbon catalyst, leading to catalyst deactivation. Therefore, the mixed solvent system of toluene and water, compared with a single toluene or alcohol solvent, can effectively avoid the problem of palladium carbon catalyst deactivation, and there will be no side reactions similar to alcohol solvents. The method has easy-to-obtain raw materials, low cost, short steps, simplified technological process, high product content and high yield, can greatly reduce cost, increase output, and is suitable for industrialized production.

附图说明Description of drawings

图1为实施例1的4-三氟甲基-3-氰基吡啶核磁图谱;Fig. 1 is the nuclear magnetic spectrum of 4-trifluoromethyl-3-cyanopyridine of embodiment 1;

图2为实施例1的4-三氟甲基-3-氰基吡啶气质图谱。Fig. 2 is the mass spectrum of 4-trifluoromethyl-3-cyanopyridine of embodiment 1.

具体实施方式detailed description

实施例1Example 1

高压反应釜中加入450g甲苯、1.47g 5%钯碳催化剂、144.60g 2,6-二氯-3-氰基-4-(三氟甲基)吡啶、155.08g二异丙基乙基胺、10.0g水,置换氢气三次,加压至0.5MPa,升温至50-60℃反应。反应2h后取样分析(GC),原料含量小于0.3%视为反应合格;Add 450g toluene, 1.47g 5% palladium carbon catalyst, 144.60g 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, 155.08g diisopropylethylamine, 10.0g of water, replace the hydrogen three times, pressurize to 0.5MPa, and raise the temperature to 50-60°C to react. Sampling analysis (GC) after 2 hours of reaction, the raw material content is less than 0.3% as the reaction is qualified;

反应完成后,加入300g冰水搅拌10min,降温至室温,过滤除去钯碳催化剂;过滤后的母液进行分液,上层为油相,下层为水相;After the reaction was completed, add 300 g of ice water and stir for 10 min, cool to room temperature, and remove the palladium-carbon catalyst by filtration; the filtered mother liquor is separated, the upper layer is an oil phase, and the lower layer is an aqueous phase;

油相进行常压蒸馏脱溶,脱除大部分甲苯溶剂后,进行减压蒸馏,蒸出产品101.20g,收率98.0%,含量99%。The oil phase was subjected to normal pressure distillation precipitation, and after most of the toluene solvent was removed, vacuum distillation was performed to distill 101.20 g of the product, with a yield of 98.0% and a content of 99%.

核磁数据为1HNMR(400MHz,CDCl3):9.12(s,1H),9.06(d,J=5.12Hz,1H),7.79(d,J=5.12Hz,1H)。气质图谱显示产物保留时间为6.044min,对应分子量为172.1(实际分子量为172.11),以此确定产物为4-三氟甲基-3-氰基吡啶。The nuclear magnetic data is 1 HNMR (400MHz, CDCl 3 ): 9.12 (s, 1H), 9.06 (d, J=5.12Hz, 1H), 7.79 (d, J=5.12Hz, 1H). The mass spectrogram shows that the retention time of the product is 6.044min, and the corresponding molecular weight is 172.1 (the actual molecular weight is 172.11), so it is determined that the product is 4-trifluoromethyl-3-cyanopyridine.

实施例2Example 2

高压反应釜中加入450g甲苯、1.00g 10%钯碳催化剂、144.60g 2,6-二氯-3-氰基-4-(三氟甲基)吡啶、155.08g二异丙基乙基胺、10.0g水,置换氢气三次,加压至0.5MPa,升温至50-60℃反应。反应2h后取样分析(GC),原料含量小于0.3%视为反应合格;Add 450g toluene, 1.00g 10% palladium carbon catalyst, 144.60g 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, 155.08g diisopropylethylamine, 10.0g of water, replace the hydrogen three times, pressurize to 0.5MPa, and raise the temperature to 50-60°C to react. Sampling analysis (GC) after 2 hours of reaction, the raw material content is less than 0.3% as the reaction is qualified;

反应完成后,加入300g冰水搅拌10min,降温至室温,过滤除去钯碳催化剂;过滤后的母液进行分液,上层为油相,下层为水相;After the reaction was completed, add 300 g of ice water and stir for 10 min, cool to room temperature, and remove the palladium-carbon catalyst by filtration; the filtered mother liquor is separated, the upper layer is an oil phase, and the lower layer is an aqueous phase;

油相进行常压蒸馏脱溶,脱除大部分甲苯溶剂后,进行减压蒸馏,蒸出产品100.17g,收率97.0%,含量99%。The oil phase was subjected to normal pressure distillation and precipitation, and after removing most of the toluene solvent, it was subjected to vacuum distillation, and 100.17 g of the product was distilled out, with a yield of 97.0% and a content of 99%.

实施例3Example 3

高压反应釜中加入450g甲苯、5.00g 1%钯碳催化剂、144.60g 2,6-二氯-3-氰基-4-(三氟甲基)吡啶、155.08g二异丙基乙基胺、10.0g水,置换氢气三次,加压至0.8MPa,升温至60-70℃反应。反应4h后取样分析(GC),原料含量小于0.3%视为反应合格;Add 450g toluene, 5.00g 1% palladium carbon catalyst, 144.60g 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, 155.08g diisopropylethylamine, 10.0g water, replace hydrogen three times, pressurize to 0.8MPa, heat up to 60-70°C to react. Sampling analysis (GC) after reaction 4h, raw material content is less than 0.3% and is regarded as reaction qualified;

反应完成后,加入300g冰水搅拌10min,降温至室温,过滤除去钯碳催化剂;过滤后的母液进行分液,上层为油相,下层为水相;After the reaction was completed, add 300 g of ice water and stir for 10 min, cool to room temperature, and remove the palladium-carbon catalyst by filtration; the filtered mother liquor is separated, the upper layer is an oil phase, and the lower layer is an aqueous phase;

油相进行常压蒸馏脱溶,脱除大部分甲苯溶剂后,进行减压蒸馏,蒸出产品99.14g,收率96.0%,含量99%。The oil phase was subjected to normal pressure distillation precipitation, and after most of the toluene solvent was removed, vacuum distillation was performed to distill 99.14 g of the product, with a yield of 96.0% and a content of 99%.

实施例4Example 4

高压反应釜中加入450g甲苯、1.47g 5%钯碳催化剂、144.60g 2,6-二氯-3-氰基-4-(三氟甲基)吡啶、155.08g二异丙基乙基胺、10.0g水,置换氢气三次,加压至2.0MPa,升温至50℃反应。反应2h后取样分析(GC),原料含量小于0.3%视为反应合格;Add 450g toluene, 1.47g 5% palladium carbon catalyst, 144.60g 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, 155.08g diisopropylethylamine, 10.0g of water, replaced by hydrogen three times, pressurized to 2.0MPa, heated to 50°C for reaction. Sampling analysis (GC) after 2 hours of reaction, the raw material content is less than 0.3% as the reaction is qualified;

反应完成后,加入300g冰水搅拌10min,降温至室温,过滤除去钯碳催化剂;过滤后的母液进行分液,上层为油相,下层为水相;After the reaction was completed, add 300 g of ice water and stir for 10 min, cool to room temperature, and remove the palladium-carbon catalyst by filtration; the filtered mother liquor is separated, the upper layer is an oil phase, and the lower layer is an aqueous phase;

油相进行常压蒸馏脱溶,脱除大部分甲苯溶剂后,进行减压蒸馏,蒸出产品100.17g,收率97.0%,含量99%。The oil phase was subjected to normal pressure distillation and precipitation, and after removing most of the toluene solvent, it was subjected to vacuum distillation, and 100.17 g of the product was distilled out, with a yield of 97.0% and a content of 99%.

实施例5Example 5

高压反应釜中加入450g甲苯、1.47g 5%钯碳催化剂、144.60g 2,6-二氯-3-氰基-4-(三氟甲基)吡啶、155.08g二异丙基乙基胺、10.0g水,置换氢气三次,加压至0.5MPa,升温至100℃反应。反应1.5h后取样分析(GC),原料含量小于0.3%视为反应合格;Add 450g toluene, 1.47g 5% palladium carbon catalyst, 144.60g 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, 155.08g diisopropylethylamine, 10.0g of water, replaced by hydrogen three times, pressurized to 0.5MPa, heated to 100°C for reaction. Sampling analysis (GC) after 1.5h of reaction, the raw material content is less than 0.3% as the reaction is qualified;

反应完成后,加入300g冰水搅拌10min,降温至室温,过滤除去钯碳催化剂;过滤后的母液进行分液,上层为油相,下层为水相;After the reaction was completed, add 300 g of ice water and stir for 10 min, cool to room temperature, and remove the palladium-carbon catalyst by filtration; the filtered mother liquor is separated, the upper layer is an oil phase, and the lower layer is an aqueous phase;

油相进行常压蒸馏脱溶,脱除大部分甲苯溶剂后,进行减压蒸馏,蒸出产品95.00g,收率92.0%,含量99%。The oil phase was subjected to normal pressure distillation and precipitation, and after removing most of the toluene solvent, it was subjected to vacuum distillation, and 95.00 g of the product was distilled out, with a yield of 92.0% and a content of 99%.

实施例6Example 6

高压反应釜中加入450g甲苯、1.47g 5%钯碳催化剂、144.60g 2,6-二氯-3-氰基-4-(三氟甲基)吡啶、300.00g二异丙基乙基胺、30.0g水,置换氢气三次,加压至0.5MPa,升温至50-60℃反应。反应2.5h后取样分析(GC),原料含量小于0.3%视为反应合格;Add 450g toluene, 1.47g 5% palladium carbon catalyst, 144.60g 2,6-dichloro-3-cyano-4-(trifluoromethyl)pyridine, 300.00g diisopropylethylamine, 30.0g water, replace hydrogen three times, pressurize to 0.5MPa, heat up to 50-60°C to react. Sampling analysis (GC) after 2.5 hours of reaction, the raw material content is less than 0.3% as the reaction is qualified;

反应完成后,加入300g冰水搅拌10min,降温至室温,过滤除去钯碳催化剂;过滤后的母液进行分液,上层为油相,下层为水相;After the reaction was completed, add 300 g of ice water and stir for 10 min, cool to room temperature, and remove the palladium-carbon catalyst by filtration; the filtered mother liquor is separated, the upper layer is an oil phase, and the lower layer is an aqueous phase;

油相进行常压蒸馏脱溶,脱除大部分甲苯溶剂后,进行减压蒸馏,蒸出产品100.17g,收率97.0%,含量99%。The oil phase was subjected to normal pressure distillation and precipitation, and after removing most of the toluene solvent, it was subjected to vacuum distillation, and 100.17 g of the product was distilled out, with a yield of 97.0% and a content of 99%.

以上所述,仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到的变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应以所述权利要求的保护范围为准。The above is only a specific embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Anyone skilled in the art can easily think of changes or substitutions within the technical scope disclosed in the present invention. All should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.

Claims (10)

1. A preparation method of 4-trifluoromethyl-3-cyanopyridine is characterized by comprising the following steps:
the method comprises the following steps of taking 2, 6-dichloro-3-cyano-4- (trifluoromethyl) pyridine as a starting material, diisopropylethylamine as an acid binding agent, and toluene and water as a mixed solvent, and reacting under the action of a catalyst and hydrogen to prepare the 4-trifluoromethyl-3-cyanopyridine, wherein the specific reaction formula is as follows:
Figure FDA0003931790420000011
2. the method of claim 1, wherein the method of making comprises: adding 2, 6-dichloro-3-cyano-4- (trifluoromethyl) pyridine, diisopropylethylamine, toluene, water and a palladium carbon catalyst into a high-pressure reaction kettle, introducing hydrogen after nitrogen replacement, heating for reaction, sampling and analyzing, adding water after the reaction is qualified, filtering to remove the catalyst, layering mother liquor, desolventizing an oil layer, and carrying out reduced pressure distillation to obtain the 4-trifluoromethyl-3-cyanopyridine.
3. The process according to claim 1, wherein the molar ratio of 2, 6-dichloro-3-cyano-4- (trifluoromethyl) pyridine to diisopropylethylamine is 1 to 10.
4. The method according to claim 1, wherein the mass ratio of the mixed solvent toluene to water is 45:1 to 3, the mass of the mixed solvent toluene and water is 1 to 10 times of the mass of 2, 6-dichloro-3-cyano-4- (trifluoromethyl) pyridine.
5. The method of claim 2, wherein the palladium on carbon catalyst is 0.5% to 10% Pd; the dosage of Pd/C is 0.05-10% of the mass of 2, 6-dichloro-3-cyano-4- (trifluoromethyl) pyridine.
6. The method as claimed in claim 5, wherein the palladium on carbon catalyst Pd is present in an amount of 0.5% to 10%; the dosage of Pd/C is 0.05-5% of the mass of 2, 6-dichloro-3-cyano-4- (trifluoromethyl) pyridine.
7. The method of claim 2, wherein the pressure of the hydrogen gas is 0.1Mpa to 10Mpa.
8. The method of claim 7, wherein the pressure of the hydrogen gas is 0.1Mpa to 5Mpa.
9. The process of claim 2, wherein the reaction temperature during hydrogenation is in the range of 20 ℃ to 120 ℃.
10. The process of claim 2, wherein the hydrogenation reaction time is from 1 to 10 hours.
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