Method for treating epoxypropane wastewater
A technology for propylene oxide and waste water, applied in chemical instruments and methods, heating water/sewage treatment, water/sludge/sewage treatment, etc., can solve the problem of high energy consumption
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Embodiment 1
[0051] This embodiment adopts figure 1 The process flow shown is carried out.
[0052] The propylene glycol content in the propylene glycol wastewater raw material is 0.3% by mass; after being heated to 100°C by steam condensate, it enters the alcohol concentration tower;
[0053] Alcohol concentration tower: the pressure at the top of the tower is 2KPa, the temperature at the top of the tower is 100°C, and the reflux ratio is 0.01;
[0054] Compressor: the compression ratio is 1.05; the stream temperature after compression is 113°C;
[0055] The overhead stream of the alcohol concentration tower enters the shell-side heat exchange of the reboiler of the alcohol concentration tower, and the water vapor in the shell side is cooled into a condensate, which is thermally coupled with the waste water raw material, and then enters the steam condensate cooler to be cooled to 80°C;
[0056] The mass percent content of propylene glycol in the production liquid of the alcohol concent...
Embodiment 2
[0058] This embodiment adopts figure 1 The process flow shown is carried out.
[0059] The content of propylene glycol in the propylene glycol wastewater raw material is 3% by mass, 0.5% by mass of ethylene glycol, and 0.1% by mass of dipropylene glycol; after being heated to 90°C by steam condensate, it enters the alcohol concentration tower;
[0060] Alcohol concentration tower: the pressure at the top of the tower is 50KPa, the temperature at the top of the tower is 103°C, and the reflux ratio is 0.05;
[0061] Compressor: the compression ratio is 1.5; the stream temperature after compression is 118°C;
[0062] The overhead stream of the alcohol concentration tower enters the shell-side heat exchange of the reboiler of the alcohol concentration tower, and the water vapor in the shell side is cooled into a condensate, which is thermally coupled with the waste water raw material, and then enters the steam condensate cooler to be cooled to 70°C;
[0063] The total mass perc...
Embodiment 3
[0065] This embodiment adopts figure 1 The process flow shown is carried out.
[0066] The propylene glycol content in the propylene glycol wastewater raw material is 10% by mass; after being heated to 90°C by steam condensate, it enters the alcohol concentration tower;
[0067] Alcohol concentration tower: the pressure at the top of the tower is 100KPa, the temperature at the top of the tower is 112°C, and the reflux ratio is 1;
[0068] Compressor: the compression ratio is 2; the stream temperature after compression is 132°C;
[0069] The overhead stream of the alcohol concentration tower enters the shell-side heat exchange of the reboiler of the alcohol concentration tower, and the water vapor in the shell side is cooled into a condensate, which is thermally coupled with the waste water raw material, and then enters the steam condensate cooler to be cooled to 70°C;
[0070] The mass percent content of propylene glycol in the production liquid of the alcohol concentration...
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