Production method for preparing environment-friendly plasticizer by adopting continuous method
An environment-friendly, plasticizer technology, applied in the preparation of carboxylate, chemical instruments and methods, preparation of organic compounds, etc., can solve the problems of large area of the reactor, limited application scope, uncontinuous esterification reaction, etc.
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Embodiment 1
[0031] Control the molar ratio of terephthalic acid and isooctyl alcohol entering the configuration kettle 3 to 1:1.5, the temperature of isooctyl alcohol entering the configuration kettle 3 is 160°C, and the raw material reaction liquid in the configuration kettle 3 is maintained at 160°C. The prepared raw material reaction solution is mixed with the catalyst tetrabutyl titanate to form a mixed raw material solution, and the tetrabutyl titanate is 0.25% of the mass of terephthalic acid. The mixed raw material liquid and the first-stage reaction liquid are mixed and enter the first-stage reaction liquid heater 13 to be heated to 230°C, and then enter the clapboard tower reactor 7 and disperse on the filler a through the liquid distributor d at the top of the first-stage reaction chamber. Circulating iso-octanol enters the middle of the reaction chambers at all levels and disperses to the liquid surface of the reaction chamber through liquid nozzle b. The molar ratio of circulat...
Embodiment 2
[0033] Control the molar ratio of trimellitic anhydride and isopropanol entering the configuration kettle 3 to 1:4, the temperature of isooctyl alcohol entering the configuration kettle 3 is 75°C, and the raw material reaction liquid in the configuration kettle 3 is maintained at 75°C. The prepared raw material reaction liquid is mixed with the catalyst tetraisopropyl titanate to form a mixed raw material liquid, and the tetraisopropyl titanate is 0.30% of the mass of trimellitic anhydride. The mixed raw material liquid and the first-stage reaction liquid are mixed and enter the first-stage reaction liquid heater 13 to be heated to 190°C, and then enter the clapboard tower reactor 7 and disperse on the filler a through the liquid distributor d at the top of the first-stage reaction chamber. Circulating isopropanol enters the middle of the reaction chambers at all levels and disperses to the liquid surface of the reaction chamber through liquid nozzle b. The molar ratio of circu...
Embodiment 3
[0035]The molar ratio of phthalic acid and n-butanol entering the configuration kettle 3 is controlled to be 1:2, the temperature of isooctyl alcohol entering the configuration kettle 3 is 100°C, and the raw material reaction liquid in the configuration kettle 3 is maintained at 100°C. The prepared raw material reaction liquid is mixed with the catalyst tetrabutyl titanate to form a mixed raw material liquid, and the tetrabutyl titanate is 0.75% of the mass of trimellitic anhydride. The mixed raw material liquid and the first-stage reaction liquid are mixed and enter the first-stage reaction liquid heater 13 to be heated to 210°C, and then enter the clapboard tower reactor 7 and disperse on the filler a through the liquid distributor d at the top of the first-stage reaction chamber. Circulating n-butanol respectively enters the middle of the reaction chamber at each stage and disperses to the liquid surface of the reaction chamber through the liquid nozzle b. The molar ratio of...
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