Polyetheramine and its preparation method
A technology of polyether amine and polyether, which is applied in the field of polyether amine and its preparation, can solve the problems such as the decrease of the average molecular weight of polyether chain polyether amine, affecting the application of polyether amine, and the widening of molecular weight distribution, so as to reduce fracture , Improve ammoniation conversion rate and narrow molecular weight distribution
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Embodiment 1
[0056] A) Preparation of polyether
[0057] In a pressure reactor, add 100 parts of nonylphenol and 0.2% KOH by weight of nonylphenol, replace the air in the kettle with nitrogen for 3 times, raise the temperature to 110°C, dehydrate for 30min in a vacuum environment below -0.09MPa, and then raise the temperature To 120°C, slowly feed propylene oxide, the molar ratio of propylene oxide to nonylphenol is 17:1, and the polymerization reaction is carried out at a pressure of 0.25MPa and a temperature of 130°C. After the feeding is completed, when the pressure in the reactor is When it does not decrease within 30min, the reaction ends and a crude polyether is produced; when the reactant is cooled to 90°C, add 85wt% phosphoric acid to neutralize to a pH value of 4.0, add an adsorbent magnesium silicate for adsorption, and then depressurize After distillation and dehydration, refined polyether is obtained after filtration. After chemical analysis, the molecular weight of the refine...
Embodiment 2
[0065] A) Preparation of polyether
[0066] In the pressure reactor, add 100 parts of dodecylphenol and 0.3% NaOH by weight of dodecylphenol, replace the air in the kettle with nitrogen for 3 times, raise the temperature to 110°C, and dehydrate in a vacuum environment below -0.09MPa 40min, then raise the temperature to 120°C, slowly feed in propylene oxide, the molar ratio of propylene oxide to dodecylphenol is 20:1, carry out the polymerization reaction at a pressure of 0.35MPa and a temperature of 140°C, and the feeding is over Finally, when the pressure in the reactor no longer drops within 30 minutes, the reaction ends and the crude polyether is generated; when the reactant is cooled to 90°C, 85wt% phosphoric acid is added to neutralize the pH to 5.0, and the adsorbent magnesium silicate is added Adsorption is carried out, and then dehydration is carried out by vacuum distillation, and refined polyether is obtained after filtration. After chemical analysis, the molecular ...
Embodiment 3
[0074] A) Preparation of polyether
[0075] In the pressure reactor, add 100 parts of isomerized tridecyl alcohol and isomeric tridecanol weight 0.25% NaOCH 3 , Replace the air in the kettle with nitrogen for 3 times, raise the temperature to 110°C, dehydrate for 50min in a vacuum environment below -0.09MPa, then raise the temperature to 120°C, slowly pass in propylene oxide, propylene oxide and isomeric tridecyl alcohol The molar ratio is 24:1, and the polymerization reaction is carried out at a pressure of 0.25MPa and a temperature of 145°C. After the feeding is completed, when the pressure in the reactor does not drop within 30 minutes, the reaction ends and a crude polyether is produced; the reactant When cooling to 80°C, add 85wt% phosphoric acid to neutralize to a pH value of 4.5, add an adsorbent magnesium silicate for adsorption, then distill and dehydrate under reduced pressure, and obtain refined polyether after filtration. After chemical analysis, the molecular wei...
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