Process for waste treatment of carbonic acid alkylene ester
An alkylene carbonate and treatment process technology, applied in the field of waste catalytic treatment technology, can solve the problems of low environmental benefit and economic benefit, high direct treatment cost and high viscosity, and achieve good waste treatment effect and good technical effect. , the effect of reducing solid waste emissions
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Embodiment 1
[0021] The waste enters from the bottom of the tower at 1.000kg / h, wherein the mass fraction of ethylene carbonate is 80%, water enters from the tower at 0.2kg / h, the reaction temperature in the tower is 110°C, and the bottom of the tower is filled with polystyrene Loaded imidazolium salt catalyst, the tower is operated with full reflux. After the reaction, the mixed material is ethylene carbonate 1%, water 4.73%, ethylene glycol 69.40%, and other solid waste 24.88%. The mixed material enters the separation tower R2 after cooling at 0.804kg / h. The temperature in R2 is 60°C and the operating pressure is It is 10kPa, the top of the tower is fully condensed, water is produced at 0.038kg / h, the flow rate of the bottom component is 0.766kg / h and enters the separation tower R3, the temperature in R3 is 110°C, and the component is produced at the top of the tower with a flow rate of 0.547kg / h Ethylene glycol, the components in the bottom of the tower containing 3.65% ethylene carbona...
Embodiment 2
[0023] The waste enters from the bottom of the tower at 1kg / h, wherein the mass fraction of ethylene carbonate is 80%, water enters from the tower at 0.25kg / h, the reaction temperature in the tower is 110°C, and the bottom of the tower is filled with tin-doped zsm-5 molecular sieve, the tower is operated with total reflux. After the reaction, the mixed material is ethylene carbonate 0.94%, water 10.3%, ethylene glycol 65.34%, and other solid waste 23.42%. The mixed material enters the separation tower R2 after cooling at 0.854kg / h. The temperature in R2 is 60°C and the operating pressure It is 10kPa, the top of the tower is fully condensed and fully extracted, the extracted component of 0.088kg / h is unreacted water, the flow rate of the bottom component is 0.766kg / h and enters the separation tower R3, the temperature in R3 is 110°C, the top of the tower The component ethylene glycol is produced at a flow rate of 0.547kg / h, and the components in the bottom of the tower contain ...
Embodiment 3
[0025] The waste enters from the bottom of the tower at 1kg / h, wherein the mass fraction of ethylene carbonate is 90%, water enters from the tower at 0.25kg / h, the reaction temperature in the tower is 110°C, the bottom of the tower is filled with D201, and the tower is Full reflux operation. After the reaction, the mixed material contains 1.12% ethylene carbonate, 8.42% unreacted water, 78.03% ethylene glycol and unreacted waste. After cooling down, it enters the separation tower R2 with a mass flow rate of 0.805kg / h. The temperature in R2 is 60°C and the operating pressure is is 10kPa, the top of the tower is fully condensed, unreacted water is produced at 0.068kg / h, the flow rate of the bottom component is 0.737kg / h and enters the separation tower R3, the temperature in R3 is 110 ° C, the operating pressure is 10kPa, the top of the tower is at The flow rate is 0.547kg / h to extract the component ethylene glycol, and the tower bottom component contains ethylene carbonate 7.5%,...
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