Preparation method of alpha-cyanacrylate for controlling powder size of paraformaldehyde
A technology of cyanoacrylate and alkyl cyanoacrylate, which is applied in the field of preparation of α-alkyl cyanoacrylate, can solve the problems of decreased yield of main reaction, low product purity, slow condensation reaction rate, etc. , achieve the effects of reduced condensation reaction time, obvious economic benefits, and wide application prospects
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Embodiment 1
[0017] The preparation of embodiment 1.α-ethyl cyanoacrylate
[0018] (1). Mix ethyl cyanoacetate and paraformaldehyde (with a particle size of 40-100 mesh) in a reactor, and react in the presence of a hexahydropyridine catalyst at a temperature of 60±5°C without a dehydrating agent. The initial temperature is 35mmHg, and the condensation reaction is carried out under 1-3mmHg vacuum at the end of the reaction. After the dehydration is complete, add phosphorus pentoxide and hydroquinone polymerization inhibitor, and then in a vacuum with a vacuum degree of 1-5mmHg and a temperature of 160-195°C Carry out cracking distillation under the condition of;
[0019] Wherein, the molar ratio of ethyl cyanoacetate and paraformaldehyde is 1.05: 1.00; the addition of phosphorus pentoxide is 5g / mol paraformaldehyde, and the addition of hydroquinone is 2g / mol paraformaldehyde; The addition amount of hexahydropyridine is 3ml / mol paraformaldehyde.
[0020] (2). The crude monomer of α-ethyl c...
Embodiment 2
[0020] (2). The crude monomer of α-ethyl cyanoacrylate obtained in step (1) is rectified again to obtain the refined monomer of α-ethyl cyanoacrylate with a purity of more than 99%, and the yield is in the range of More than 65%. The preparation of embodiment 2.α-methoxy ethyl cyanoacrylate
[0021] (1). Mix methoxyethyl cyanoacetate and paraformaldehyde (with a particle size of 40 to 100 mesh) in a reaction kettle, and in the presence of a hexahydropyridine catalyst, in the absence of a dehydrating agent, the temperature is 60 ± 5 ℃ and 30mmHg at the beginning of the reaction, and the condensation reaction is carried out under 1mmHg vacuum at the end of the reaction. After the dehydration is complete, add phosphorus pentoxide and hydroquinone polymerization inhibitor, and then in a vacuum with a vacuum degree of 0.1-25mmHg and a temperature of 160-200 Cracking distillation is carried out under the condition of ℃;
[0022] Wherein, the molar ratio of methoxyethyl cyanoacetat...
Embodiment 3
[0025] (1). Mix methyl cyanoacetate and paraformaldehyde (60-120 mesh particle size) in a reaction kettle, add toluene solvent under normal pressure in the presence of sodium hydroxide catalyst, and add toluene solvent at a temperature of 100°C Carry out condensation reaction; after dehydration is complete, add phosphorus pentoxide, catechol and p-tert-butylphenol polymerization inhibitor, recover the dehydrating agent toluene and then put it in a vacuum with a vacuum degree of 0.5-25mmHg and a temperature of 160-190°C Cracking distillation under conditions;
[0026] Wherein, the molar ratio of methyl cyanoacetate and paraformaldehyde is 1.05: 1.00; the add-on of phosphorus pentoxide is 4g / mol paraformaldehyde, and the add-on of catechol and p-tert-butylphenol is 1g / mol paraformaldehyde; the addition amount of sodium hydroxide is 1.0-1.5g / mol paraformaldehyde, and the addition amount of dehydration solvent toluene is 30-40ml / mol paraformaldehyde.
[0027] (2). The crude monom...
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