Preparation method of tert-butyl acrylate
A technology of tert-butyl acrylate and acrylic acid, applied in the field of preparation of tert-butyl acrylate, can solve the problems of complex polymerization inhibitor and high reaction temperature, and achieve the effects of mild reaction, simple process and improved yield
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Embodiment 1
[0022] Put acrylic acid, catalyst, polymerization inhibitor and isobutylene into the reactor, under the conditions of temperature 30°C and pressure 1MPa, esterification reaction occurs at the volume space velocity of isobutylene 1.0 / h to synthesize tert-butyl acrylate;
[0023] Wherein, the molar ratio of acrylic acid, polymerization inhibitor and isobutylene is 1:0.1:0.5, the catalyst is a mixture of sulfonic acid type cation exchange resin and p-toluenesulfonic acid, the mass ratio of the two is 3:1, the total mass of the catalyst It is 10% of the mass of acrylic acid; the polymerization inhibitor is a mixture of tert-butylcatechol and tert-butanol, and the mass ratio of the two is 1:1.
Embodiment 2
[0025] Put acrylic acid, catalyst, polymerization inhibitor and isobutylene into the reactor, under the conditions of temperature 30°C and pressure 1MPa, esterification reaction occurs at the volume space velocity of isobutylene 1.0 / h to synthesize tert-butyl acrylate;
[0026] Wherein, the molar ratio of acrylic acid, polymerization inhibitor and isobutylene is 1:0.1:0.5, the catalyst is a mixture of sulfonic acid modified SBA-15 mesoporous molecular sieve and p-toluenesulfonic acid, the mass ratio of the two is 3:1, The total mass of the catalyst is 10% of the mass of acrylic acid; the polymerization inhibitor is a mixture of tert-butylcatechol and tert-butanol, and the mass ratio of the two is 1:1.
Embodiment 3
[0028] Put acrylic acid, catalyst, polymerization inhibitor and isobutylene into the reactor, under the conditions of temperature 30°C and pressure 1MPa, esterification reaction occurs at the volume space velocity of isobutylene 1.0 / h to synthesize tert-butyl acrylate;
[0029] Wherein, the molar ratio of acrylic acid, polymerization inhibitor and isobutylene is 1:0.2:0.8, the catalyst is a mixture of sulfonic acid modified SBA-15 mesoporous molecular sieve and p-toluenesulfonic acid, the mass ratio of the two is 3:1, The total mass of the catalyst is 8% of the mass of acrylic acid; the polymerization inhibitor is a mixture of tert-butylcatechol and tert-butanol, and the mass ratio of the two is 1:1.
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