Method for continuously dissolving urea and propylene glycol (or ethylene glycol)
A technology of propylene glycol and ethylene glycol, applied in the direction of organic chemistry, etc., can solve problems such as environmental pollution, potential safety hazards, and no stable, safe and continuous dissolution method of urea and propylene (or ethylene) glycol.
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Embodiment 1
[0028] In the 40,000 tons / year urea two-step dimethyl carbonate production plant, the continuous dissolution of urea and propylene glycol is carried out in a single tank. The volume of the stirred tank is 25m 3 , urea at 3705kg / h and propylene glycol at 8447kg / h are continuously added to the stirring tank, the urea feeding pipe is immersed 100cm below the liquid surface, the stirring tank is heated to 100°C with steam, and the pressure is kept at 90kPa through the vacuum regulating valve, and the generated propylene glycol is saturated The vapor pressure and ammonia gas enter the condenser, the condensation temperature is -5°C, the condensed propylene glycol liquid is returned to the stirring tank, and the non-condensable ammonia gas enters the subsequent recovery device. The material in the stirred tank (urea has been completely dissolved) is transported to the subsequent urea alcoholysis reactor through the pump at the bottom of the tank, and the liquid level of the stirred ...
Embodiment 2
[0030]In the 100,000 tons / year urea two-step dimethyl carbonate production plant, two tanks are connected in series for continuous dissolution of urea and propylene glycol. The volumes of the stirred tank (1) and the tank (2) are both 30m 3 , urea at 9530kg / h and propylene glycol at 16900kg / h are continuously added to the stirring tank (1), the urea feeding pipe is immersed 80cm below the liquid surface, the stirring tank is heated to 90°C by steam, and the pressure is kept at 95kPa through the vacuum regulating valve, resulting in The saturated vapor pressure of propylene glycol and ammonia gas enter the condenser (2), the condensation temperature is 0°C, the condensed propylene glycol liquid is returned to the stirring tank, and the ammonia gas enters the subsequent recovery device. The material in the kettle (1) automatically flows into the kettle (2) through the pipeline at the bottom of the kettle. The kettle (2) is heated to 90°C with steam, and the pressure is kept at 9...
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