PTA oxidation residue comprehensive utilization process
A residue and process technology, which is applied in the field of comprehensive utilization of PTA oxidation residue, can solve the problems of waste gas and dust pollution, environmental pollution threat, low utilization rate, etc., and achieve the effect of saving energy, reducing octanol consumption and improving utilization rate
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Embodiment 1
[0180] Take Jiaxing Tongkun PTA oxidation residue 1000g (dry basis) into the reactor, add 2001g of octanol, start heating and stirring. When the temperature of the material rises to 184°C, add 3.45g of tetrabutyl titanate catalyst, at this time, the octanol is refluxed with water, wait for the temperature in the kettle to rise to about 220°C and at the same time no water drops are extracted, which is regarded as the end point of the esterification reaction. When it is detected that the acid value of the esterification solution is below 0.5, the esterification reaction is over. When the temperature of the esterification liquid is lowered to 90°C, start to filter to obtain a transparent esterification liquid, and start to enter the rectification step.
[0181] Pour the transparent esterification liquid into the still of the rectification tower. When the vacuum at the top of the tower reaches 0.15kpa, heat the still. When the temperature at the top of the tower rises and stabiliz...
Embodiment 2
[0185] Take Shanghai Yadong PTA oxidation residue 1000g (dry basis) into the reactor, add octanol 2001g, start heating and stirring. When the temperature of the material rises to 184°C, add 3.45g of tetrabutyl titanate catalyst, at this time, the octanol is refluxed with water, wait for the temperature in the kettle to rise to about 220°C and at the same time no water drops are extracted, which is regarded as the end point of the esterification reaction. When it is detected that the acid value of the esterification solution is below 0.5, the esterification reaction is over. When the temperature of the esterification liquid is lowered to 90°C, start to filter to obtain a transparent esterification liquid, and start to enter the rectification step.
[0186] Pour the transparent esterification liquid into the still of the rectification tower. When the vacuum at the top of the tower reaches 0.15kpa, heat the still. When the temperature at the top of the tower rises and stabilizes ...
Embodiment 3
[0190] Take Jiangyin Hailun PTA oxidation residue 1000g (dry basis) into the reactor, add 2001g of octanol, start heating and stirring. When the temperature of the material rises to 184°C, add 3.45g of tetrabutyl titanate catalyst, at this time, the octanol is refluxed with water, wait for the temperature in the kettle to rise to about 220°C and at the same time no water drops are extracted, which is regarded as the end point of the esterification reaction. When it is detected that the acid value of the esterification solution is below 0.5, the esterification reaction is over. When the temperature of the esterification liquid is lowered to 90°C, start to filter to obtain a transparent esterification liquid, and start to enter the rectification step.
[0191] Pour the transparent esterification liquid into the still of the rectification tower. When the vacuum at the top of the tower reaches 0.15kpa, heat the still. When the temperature at the top of the tower rises and stabiliz...
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