A kind of preparation method of cyclohexane-1,2-dicarboxylate plasticizer
A technology of diformate and cyclohexane, which is applied in the field of preparation of environmentally friendly plasticizers, can solve the problems of troublesome post-processing, high yield per kettle, dark product color, etc., achieves low equipment requirements, and reduces energy consumption , the effect of easy industrial control
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Embodiment 1
[0025] Synthesis of dibutyl cyclohexane-1,2-dicarboxylate: the composite catalyst is sodium bisulfate-iron powder, wherein the mass ratio of sodium bisulfate to iron powder is 5:1, and the particle size of the iron powder is 80 mesh. The raw materials cyclohexane-1,2-dicarboxylic acid and n-butanol are added to the stainless steel esterification reactor according to the acid-alcohol molar ratio of 1:2.5, and the composite catalyst accounting for 0.1% of the total mass of the material is added to the stainless steel esterification reactor at normal pressure, 145 ℃ for 5 hours, the water in the water separator did not increase significantly, stop the reaction, lower the temperature, separate the solid and liquid, the reaction liquid is colorless, the ester yield is 79%, recover the excess alcohol, add acid alcohol to the required molar ratio, continue next cycle.
[0026] Synthesis of dioctyl cyclohexane-1,2-dicarboxylate: the composite catalyst is sodium bisulfate-iron powder, ...
Embodiment 2
[0028] Synthesis of dibutyl cyclohexane-1,2-dicarboxylate: The composite catalyst is potassium hydrogen sulfate-iron powder, wherein the mass ratio of potassium hydrogen sulfate to iron powder is 5:1, and the particle size of the iron powder is 80 mesh. The raw materials cyclohexane-1,2-dicarboxylic acid and n-butanol are added to the stainless steel esterification reactor according to the acid-alcohol molar ratio of 1:2.5, and the composite catalyst accounting for 0.1% of the total mass of the material is added to the stainless steel esterification reactor at normal pressure, 145 ℃ for 4 hours, the water in the water separator did not increase significantly, stop the reaction, lower the temperature, separate the solid and liquid, the reaction liquid is colorless, the ester yield is 81%, recover the excess alcohol, add acid alcohol to the required molar ratio, continue next cycle.
[0029] Synthesis of dioctyl cyclohexane-1,2-dicarboxylate: the composite catalyst is potassium ...
Embodiment 3
[0031] Synthesis of dibutyl cyclohexane-1,2-dicarboxylate: The composite catalyst is potassium bisulfate-aluminum powder, wherein the mass ratio of potassium bisulfate to aluminum powder is 5:2, and the particle size of the aluminum powder is 80 mesh. The raw material cyclohexane-1,2-dicarboxylic acid and n-butanol are added to the stainless steel esterification reactor according to the acid-alcohol molar ratio of 1:2.5, and the composite catalyst accounting for 0.3% of the total mass of the material is added to the stainless steel esterification reactor at normal pressure, 155 ℃ for 4 hours, the water in the water separator did not increase significantly, stop the reaction, lower the temperature, separate the solid and liquid, the reaction liquid is colorless, the ester yield is 81%, recover the excess alcohol, add acid alcohol to the required molar ratio, continue next cycle.
[0032] Synthesis of dioctyl cyclohexane-1,2-dicarboxylate: the composite catalyst is potassium hyd...
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