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CN115974690A - A kind of preparation method of 4-acetoxy-2-methyl-2-buten-1-aldehyde - Google Patents

A kind of preparation method of 4-acetoxy-2-methyl-2-buten-1-aldehyde Download PDF

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CN115974690A
CN115974690A CN202211689159.XA CN202211689159A CN115974690A CN 115974690 A CN115974690 A CN 115974690A CN 202211689159 A CN202211689159 A CN 202211689159A CN 115974690 A CN115974690 A CN 115974690A
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methyl
chloride
acetoxy
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quaternary ammonium
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CN115974690B (en
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吴世林
张贵东
黄海青
梁庭枝
邸维龙
江华峰
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Guangzhou Wisdom Bio Technology Co ltd
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Abstract

本发明涉及有机化工技术领域,本发明公开了一种4‑乙酰氧基‑2‑甲基‑2‑丁烯‑1‑醛的制备方法,包括以下步骤:S1、将氯化物与乌洛托品与水相混合,在一定温度下反应8个小时,反应结束后静置分层,分去未反应的氯化物,得到季铵盐溶液;S2、在季铵盐溶液中加入一定量的酸进行PH的调节;S3、向季铵盐溶液中加入有机相溶剂,并加入一定量的铜催化剂,一定温度下进行水解,反应结束后分取有机相;S4、向S3的产物中加入1%浓度的碳酸钠调到中性,将有机相回收,通过减压蒸馏得到五碳醛。本发明通过氯化物与乌洛托品与水相混合得到季铵盐,将季铵盐中加入有机相和铜催化剂得到五碳醛,通过铜催化碳‑氮键的水解,可以降低反应温度,提高水解的选择性与收率。The invention relates to the technical field of organic chemical industry. The invention discloses a preparation method of 4-acetoxy-2-methyl-2-butene-1-aldehyde, which comprises the following steps: The product is mixed with water, and reacted at a certain temperature for 8 hours. After the reaction, it is left to stand for stratification, and the unreacted chloride is separated to obtain a quaternary ammonium salt solution; S2, a certain amount of acid is added to the quaternary ammonium salt solution. Adjust the pH; S3, add an organic phase solvent to the quaternary ammonium salt solution, and add a certain amount of copper catalyst, perform hydrolysis at a certain temperature, and separate the organic phase after the reaction; S4, add 1% to the product of S3 The concentration of sodium carbonate is adjusted to neutral, the organic phase is recovered, and five-carbon aldehyde is obtained by distillation under reduced pressure. In the present invention, the quaternary ammonium salt is obtained by mixing the chloride and urotropine with the water phase, and the organic phase and the copper catalyst are added to the quaternary ammonium salt to obtain the pentacarbon aldehyde, and the reaction temperature can be lowered by copper catalyzing the hydrolysis of the carbon-nitrogen bond. Improve the selectivity and yield of hydrolysis.

Description

一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法A kind of preparation method of 4-acetoxy-2-methyl-2-butene-1-al

技术领域technical field

本发明涉及有机化工技术领域,具体为一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法。The invention relates to the technical field of organic chemical industry, in particular to a preparation method of 4-acetoxy-2-methyl-2-butene-1-aldehyde.

背景技术Background technique

4-乙酰氧基-2-甲基-2-丁烯-1-醛简称五碳醛,为化学合成产品,是维生素A的中间体。储存条件是室温且密封储存,五碳醛在室温且密封条件下稳定,但要忌与强氧化物、强酸、强碱混储。对眼睛、皮肤、呼吸道具刺激作用,吞入有毒。4-Acetoxy-2-methyl-2-buten-1-aldehyde, referred to as five-carbon aldehyde, is a chemical synthesis product and an intermediate of vitamin A. The storage conditions are room temperature and sealed storage. Pentacarbonaldehyde is stable at room temperature and sealed conditions, but it should not be mixed with strong oxides, strong acids, and strong alkalis. Irritating to eyes, skin and respiratory props, poisonous if swallowed.

一般情况下,通过Sommelet反应制备芳香醛时有较好的收率,制备脂肪醛时收率普遍不高,专利GB736488(1955)报道,将式3在水溶液中水解得到目标产物式1,收率仅有约20%;专利US5471004A为了提高收率,将水解反应在两相中进行,同时采取酸催化,在较高温度反应,收率明显提高,但是产物在酸性条件下较高温度水解,产物复杂,需要采取柱层析纯化或者用亚硫酸氢钠纯化除杂,工业化不方便,损失较大;专利CN1919825A报道通过微波反应器可以提高水解收率,但是微波催化反应在工业化大生产中还不能实现。In general, there is a good yield when aromatic aldehyde is prepared by Sommelet reaction, and the yield is generally not high when aliphatic aldehyde is prepared. Patent GB736488 (1955) reports that formula 3 is hydrolyzed in aqueous solution to obtain target product formula 1, yield Only about 20%; in order to improve the yield, the patent US5471004A carries out the hydrolysis reaction in two phases, and adopts acid catalysis at the same time, reacts at a higher temperature, and the yield is obviously improved, but the product is hydrolyzed at a higher temperature under acidic conditions, and the product Complicated, it needs to be purified by column chromatography or purified by sodium bisulfite to remove impurities, which is inconvenient for industrialization and has a large loss; patent CN1919825A reports that the hydrolysis yield can be improved through microwave reactors, but microwave catalytic reactions cannot be used in large-scale industrial production. accomplish.

发明内容Contents of the invention

(一)解决的技术问题(1) Solved technical problems

针对现有技术的不足,本发明提供了一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法,通过铜催化碳-氮键的水解,可以降低反应温度,提高水解的选择性与收率;另外产物纯度高,只要简单蒸馏即可得到高纯度产物。Aiming at the deficiencies in the prior art, the present invention provides a preparation method of 4-acetoxy-2-methyl-2-buten-1-aldehyde, which can reduce the reaction temperature through the hydrolysis of copper-catalyzed carbon-nitrogen bond , to improve the selectivity and yield of hydrolysis; in addition, the product has high purity, and a high-purity product can be obtained by simple distillation.

(二)技术方案(2) Technical solution

为实现上述目的,本发明提供如下技术方案:一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法,包括以下步骤:In order to achieve the above object, the present invention provides the following technical scheme: a preparation method of 4-acetoxy-2-methyl-2-buten-1-aldehyde, comprising the following steps:

S1、将氯化物与乌洛托品与水相混合,在一定温度下反应8个小时,反应结束后静置分层,分去未反应的氯化物,得到季铵盐溶液,

Figure BDA0004020464730000021
S1, the chloride is mixed with urotropine and water, and reacted at a certain temperature for 8 hours. After the reaction, the stratification is left to stand, and the unreacted chloride is separated to obtain a quaternary ammonium salt solution.
Figure BDA0004020464730000021

S2、在季铵盐溶液中加入一定量的酸进行PH的调节;S2, adding a certain amount of acid to the quaternary ammonium salt solution to adjust the pH;

S3、向季铵盐溶液中加入有机相溶剂,并加入一定量的铜催化剂,在一定温度下进行水解,反应时间为6个小时,反应结束后分取有机相,

Figure BDA0004020464730000022
S3, add organic phase solvent in the quaternary ammonium salt solution, and add a certain amount of copper catalyst, carry out hydrolysis at a certain temperature, the reaction time is 6 hours, divide and take organic phase after reaction finishes,
Figure BDA0004020464730000022

S4、向S3的产物中加入1%浓度的碳酸钠调到中性,将有机相回收,通过减压蒸馏得到五碳醛。S4, adding 1% sodium carbonate to the product of S3 to adjust to neutrality, recovering the organic phase, and obtaining pentacarbon aldehyde by distillation under reduced pressure.

作为优选方案,在S1中,氯化物与乌洛托品的摩尔比为1:1~1.5。As a preferred solution, in S1, the molar ratio of chloride to urotropine is 1:1-1.5.

作为优选方案,在S1中,氯化物与乌洛托品在水相中反应温度为25℃~80℃,较好温度在30℃~45℃之间。As a preferred solution, in S1, the reaction temperature of the chloride and urotropine in the aqueous phase is 25°C-80°C, preferably between 30°C-45°C.

作为优选方案,在S1中,水的用量是氯化物质量的1~10倍,较好的量是2~4倍。As a preferred solution, in S1, the amount of water used is 1 to 10 times the mass of the chloride, preferably 2 to 4 times.

作为优选方案,在S3中,所用到的有机相为甲苯、二甲苯、正庚烷、正己烷、环己烷、乙酸乙酯、丙酸乙酯、甲基叔丁基醚和二乙烷中的一种,且有机相的用量是水相体积的1~3倍。As a preferred version, in S3, the organic phase used is in toluene, xylene, n-heptane, n-hexane, cyclohexane, ethyl acetate, ethyl propionate, methyl tert-butyl ether and diethane One, and the amount of the organic phase is 1 to 3 times the volume of the aqueous phase.

作为优选方案,在S2中,通过酸调节Ph=2~6,较好PH=2.5~3.0。As a preferred solution, in S2, adjust Ph=2-6 by acid, preferably pH=2.5-3.0.

作为优选方案,在S3中,所用到铜催化剂为硫酸铜、醋酸铜、氯化亚铜、氯化铜中的一种,较好的铜催化剂是醋酸铜,且铜催化剂在水相中的浓度(m/v)为0.5%~5%之间,较好浓度在0.8%~1.5%之间。As a preferred version, in S3, the copper catalyst used is one of copper sulfate, copper acetate, cuprous chloride, cupric chloride, the preferred copper catalyst is copper acetate, and the concentration of the copper catalyst in the aqueous phase (m/v) is between 0.5% and 5%, preferably between 0.8% and 1.5%.

作为优选方案,在S3中,反应温度在20℃~60℃,较好的温度在25℃~35℃之间。As a preferred solution, in S3, the reaction temperature is between 20°C and 60°C, preferably between 25°C and 35°C.

(三)有益效果(3) Beneficial effects

本发明提供了一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法,有益效果在于:The present invention provides a kind of preparation method of 4-acetoxy-2-methyl-2-buten-1-al, the beneficial effect is:

本发明通过氯化物与乌洛托品与水相在一定温度下混合得到季铵盐,再将季铵盐水解,水解过程中加入有机相和铜催化剂得到五碳醛,通过铜催化碳-氮键的水解,可以降低反应温度,提高水解的选择性与收率,另外产物纯度高,只要简单蒸馏即可得到高纯度产物。In the present invention, the quaternary ammonium salt is obtained by mixing the chloride, urotropine and the water phase at a certain temperature, and then the quaternary ammonium salt is hydrolyzed, and an organic phase and a copper catalyst are added in the hydrolysis process to obtain pentacarbon aldehyde, and carbon-nitrogen is catalyzed by copper. The hydrolysis of the bond can reduce the reaction temperature, improve the selectivity and yield of hydrolysis, and the product has high purity, and a high-purity product can be obtained by simple distillation.

具体实施方式Detailed ways

为了更好地了解本发明的目的、结构及功能,对本发明一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法做进一步详细的描述。In order to better understand the purpose, structure and function of the present invention, a preparation method of 4-acetoxy-2-methyl-2-buten-1-al of the present invention will be further described in detail.

一种4-乙酰氧基-2-甲基-2-丁烯-1-醛的制备方法,包括以下步骤:A preparation method of 4-acetoxy-2-methyl-2-buten-1-aldehyde, comprising the following steps:

S1、将氯化物与乌洛托品与水相混合,在一定温度下反应8个小时,反应结束后静置分层,分去未反应的氯化物,得到季铵盐溶液,S1, the chloride is mixed with urotropine and water, and reacted at a certain temperature for 8 hours. After the reaction, the layers are left to stand, and the unreacted chloride is separated to obtain a quaternary ammonium salt solution.

Figure BDA0004020464730000031
Figure BDA0004020464730000031

S2、在季铵盐溶液中加入一定量的酸进行PH的调节;S2, adding a certain amount of acid to the quaternary ammonium salt solution to adjust the pH;

S3、向季铵盐溶液中加入有机相溶剂,并加入一定量的铜催化剂,在一定温度下进行水解,反应时间为6个小时,反应结束后分取有机相,S3, add organic phase solvent in the quaternary ammonium salt solution, and add a certain amount of copper catalyst, carry out hydrolysis at a certain temperature, the reaction time is 6 hours, divide and take organic phase after reaction finishes,

Figure BDA0004020464730000041
Figure BDA0004020464730000041

S4、向S3的产物中加入1%浓度的碳酸钠调到中性,将有机相回收,通过减压蒸馏得到五碳醛。S4, adding 1% sodium carbonate to the product of S3 to adjust to neutrality, recovering the organic phase, and obtaining pentacarbon aldehyde by distillation under reduced pressure.

作为优选方案,在S1中,氯化物与乌洛托品的摩尔比为1:1~1.5。As a preferred solution, in S1, the molar ratio of chloride to urotropine is 1:1-1.5.

作为优选方案,在S1中,氯化物与乌洛托品在水相中反应温度为25℃~80℃,较好温度在30℃~45℃之间。As a preferred solution, in S1, the reaction temperature of the chloride and urotropine in the aqueous phase is 25°C-80°C, preferably between 30°C-45°C.

作为优选方案,在S1中,水的用量是氯化物质量的1~10倍,较好的量是2~4倍。As a preferred solution, in S1, the amount of water used is 1 to 10 times the mass of the chloride, preferably 2 to 4 times.

作为优选方案,在S3中,所用到的有机相为甲苯、二甲苯、正庚烷、正己烷、环己烷、乙酸乙酯、丙酸乙酯、甲基叔丁基醚和二乙烷中的一种,且有机相的用量是水相体积的1~3倍。As a preferred version, in S3, the organic phase used is in toluene, xylene, n-heptane, n-hexane, cyclohexane, ethyl acetate, ethyl propionate, methyl tert-butyl ether and diethane One, and the amount of the organic phase is 1 to 3 times the volume of the aqueous phase.

作为优选方案,在S2中,通过酸调节Ph=2~6,较好PH=2.5~3.0。As a preferred solution, in S2, adjust Ph=2-6 by acid, preferably pH=2.5-3.0.

作为优选方案,在S3中,所用到铜催化剂为硫酸铜、醋酸铜、氯化亚铜、氯化铜中的一种,较好的铜催化剂是醋酸铜,且铜催化剂在水相中的浓度(m/v)为0.5%~5%之间,较好浓度在0.8%~1.5%之间。As a preferred version, in S3, the copper catalyst used is one of copper sulfate, copper acetate, cuprous chloride, cupric chloride, the preferred copper catalyst is copper acetate, and the concentration of the copper catalyst in the aqueous phase (m/v) is between 0.5% and 5%, preferably between 0.8% and 1.5%.

作为优选方案,在S3中,反应温度在20℃~60℃,较好的温度在25℃~35℃之间。As a preferred solution, in S3, the reaction temperature is between 20°C and 60°C, preferably between 25°C and 35°C.

实施例1Example 1

取氯化物65g(0.4mol),乌洛托品84g(0.6mol),加195g水,在30℃反应8小时,然后静置分层,分去未参加反应的氯化物6.2克,水相加3克50%盐酸调PH=3.5,加入氯化亚铜0.98克,再加入390ml正庚烷,在35℃反应6小时,反应结束后分取有机相,用1%浓度的碳酸钠调到中性,回收有机相,再减压蒸馏粗产物,得到4-乙酰氧基-2-甲基-2-丁烯-1-醛41.62g,气相含量97.71%,以实际反应的氯化物计算收率为81%;Take 65g (0.4mol) of chloride, 84g (0.6mol) of urotropine, add 195g of water, react at 30°C for 8 hours, then let it stand for stratification, remove 6.2g of chloride that has not participated in the reaction, add the water phase 3 grams of 50% hydrochloric acid to adjust the pH to 3.5, add 0.98 grams of cuprous chloride, then add 390 ml of n-heptane, react at 35 ° C for 6 hours, separate the organic phase after the reaction, and adjust it to neutral with 1% sodium carbonate. properties, recover the organic phase, and then distill the crude product under reduced pressure to obtain 41.62 g of 4-acetoxy-2-methyl-2-buten-1-aldehyde, with a gas phase content of 97.71%, and the yield is calculated based on the actual reacted chloride 81%;

4-乙酰氧基-2-甲基-2-丁烯-1-醛核磁数据:1H-NMR(CDCl3,300MHz):δ9.48(s,-CHO);6.51(t,H,-CH=);4-Acetoxy-2-methyl-2-buten-1-aldehyde NMR data: 1 H-NMR (CDCl 3 , 300MHz): δ9.48(s,-CHO); 6.51(t,H,- CH=);

4.91(d,2H,-CH2-);2.15(s,3H,-CH3);1.80(s,3H,=C-CH3);4.91(d,2H,-CH2-); 2.15(s,3H,-CH3); 1.80(s,3H,=C-CH3);

实施例2Example 2

取氯化物65g(0.4mol),乌洛托品67.2g(0.48mol),加240g水,在30℃反应8小时,然后静置分层,分去未参加反应的氯化物6.5克,水相加4克乙酸调PH=3.0,加入醋酸铜2.4克,再加入300ml甲苯,在30℃反应6小时,反应结束后分取有机相,用1%浓度的碳酸钠调到中性,回收有机相,再减压蒸馏粗产物,得到4-乙酰氧基-2-甲基-2-丁烯-1-醛43.45g,气相含量97.65%,以实际反应的氯化物计算收率为85%。Take 65g (0.4mol) of chloride, 67.2g (0.48mol) of urotropine, add 240g of water, react at 30°C for 8 hours, then let it stand and separate the layers, remove 6.5g of chloride that has not participated in the reaction, and the water phase Add 4 grams of acetic acid to adjust the pH to 3.0, add 2.4 grams of copper acetate, then add 300 ml of toluene, react at 30 ° C for 6 hours, separate the organic phase after the reaction, adjust it to neutral with 1% sodium carbonate, and recover the organic phase , and then distill the crude product under reduced pressure to obtain 43.45 g of 4-acetoxy-2-methyl-2-butene-1-al, with a gas phase content of 97.65%, and a yield of 85% based on the actual reacted chloride.

可以理解,本发明是通过一些实施例进行描述的,本领域技术人员知悉的,在不脱离本发明的精神和范围的情况下,可以对这些特征和实施例进行各种改变或等效替换。另外,在本发明的教导下,可以对这些特征和实施例进行修改以适应具体的情况及材料而不会脱离本发明的精神和范围。因此,本发明不受此处所公开的具体实施例的限制,所有落入本申请的权利要求范围内的实施例都属于本发明所保护的范围内。It can be understood that the present invention is described through some embodiments, and those skilled in the art know that various changes or equivalent substitutions can be made to these features and embodiments without departing from the spirit and scope of the present invention. In addition, the features and examples may be modified to adapt a particular situation and material to the teachings of the invention without departing from the spirit and scope of the invention. Therefore, the present invention is not limited by the specific embodiments disclosed here, and all embodiments falling within the scope of the claims of the present application belong to the protection scope of the present invention.

Claims (8)

1. A preparation method of 4-acetoxyl-2-methyl-2-butene-1-aldehyde is characterized by comprising the following steps:
s1, mixing chloride, urotropine and water, reacting for 8 hours at a certain temperature, standing for layering after the reaction is finished, removing unreacted chloride to obtain a quaternary ammonium salt solution,
Figure FDA0004020464720000011
s2, adding a certain amount of acid into the quaternary ammonium salt solution to adjust the PH;
s3, adding an organic phase solvent into the quaternary ammonium salt solution, adding a certain amount of copper catalyst, hydrolyzing at a certain temperature for 6 hours, separating an organic phase after the reaction is finished,
Figure FDA0004020464720000012
and S4, adding 1% of sodium carbonate into the product of the S3 to adjust to be neutral, recovering an organic phase, and carrying out reduced pressure distillation to obtain the pentanal.
2. The process according to claim 1 for producing 4-acetoxy-2-methyl-2-buten-1-al, which comprises: in S1, the mol ratio of chloride to urotropine is 1:1 to 1.5.
3. The process according to claim 1 for producing 4-acetoxy-2-methyl-2-buten-1-al, which comprises: in S1, the reaction temperature of chloride and urotropine in the water phase is 25-80 ℃.
4. The process according to claim 1 for producing 4-acetoxy-2-methyl-2-buten-1-al, which comprises: in S1, the amount of water is 1 to 10 times the amount of the chloride.
5. The process for producing 4-acetoxy-2-methyl-2-butene-1-al according to claim 1, wherein: in S3, the organic phase is one of toluene, xylene, n-heptane, n-hexane, cyclohexane, ethyl acetate, ethyl propionate, methyl tert-butyl ether and dichloroethane, and the amount of the organic phase is 1 to 3 times of the volume of the aqueous phase.
6. The process for producing 4-acetoxy-2-methyl-2-butene-1-al according to claim 1, wherein: in S2, ph =2 to 6 is adjusted by an acid.
7. The process according to claim 1 for producing 4-acetoxy-2-methyl-2-buten-1-al, which comprises: in S3, the used copper catalyst is one of copper sulfate, copper acetate, cuprous chloride and copper chloride, and the concentration (m/v) of the copper catalyst in the water phase is between 0.5 and 5 percent.
8. The process according to claim 1 for producing 4-acetoxy-2-methyl-2-buten-1-al, which comprises: in S3, the reaction temperature is 20-60 ℃.
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