Process of recycling terephthalic acid to produce DOTP (dioctyl terephthalate) by using polyester alkaline to reduce wastewater
A technology of alkali reduction wastewater and terephthalic acid, applied in the field of plasticizers, can solve the problems of different purity and color, waste, uneven process level, etc., to shorten the process flow, reduce energy consumption and waste water generation volume effect
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Embodiment 1
[0020] Put TA recycled material of white embryo polyester fabric with terephthalic acid content of 92% into the reaction kettle, put isooctyl alcohol in a mass ratio of 1:2.6, start stirring and raise the temperature to 160°C, when the water output is significantly reduced, add the following The catalyst of tetraisopropyl titanate and tetrabutyl titanate mixed in a ratio of 4:1 is added in an amount of 5‰ of the mass of TA recycled material, and at the same time, activated carbon with a mass of TA recycled material of 5‰ is added, and the temperature is controlled continuously by stirring and heating. At 200°C, keep water and iso-octanol reflux during the period. When the acidity reaches ≤0.05%, the reaction is considered to be over. Turn on the vacuum to -0.09MPa and use the remaining temperature to remove the excess iso-octanol. The still was heated to 285°C for 2.5 hours under reduced pressure, and the vacuum was maintained at -0.1MPa to obtain the crude ester. After the vac...
Embodiment 2
[0023] Put TA recycled fabric containing colored fiber with terephthalic acid content of 84.7% in the reaction kettle, put in isooctyl alcohol 2.2 times its weight, start stirring and raise the temperature to 120°C, add TA recycled material when the water output is significantly reduced 3‰ of the weight of tetraisopropyl titanate and tetrabutyl titanate catalyst mixed in a ratio of 3.5:1, and add activated carbon with 1% of the mass of TA recycled material, keep stirring and heating up, and control the temperature at 190°C. Keep the iso-octanol reflux and continuously drain the reaction water. When the acidity reaches ≤0.05%, the reaction is considered to be over. Turn on the vacuum to -0.08MPa and use the remaining temperature to remove the remaining iso-octanol. The still was heated up to 275°C for 4 hours under reduced pressure, and the vacuum was maintained at -0.1MPa under reduced pressure to obtain the crude ester. Turn off the vacuum, and then add 50% H 2 o 2 And use t...
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