A process for realizing zero discharge of chemical sewage
A technology for chemical sewage and process methods, applied in chemical instruments and methods, water/sewage multi-stage treatment, water/sludge/sewage treatment, etc., can solve the problems of filtration and multi-effect evaporation operation, bacterial death, multi-effect evaporation Problems such as high energy consumption
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[0166] In a specific embodiment of the present invention, the heat balance of evaporation and distillation is realized in the manner described, the first chemical sewage is in the sewage / condensed water heat exchanger, and the circulating waste water is recycled in the partial condensation cooler and heater. 90-95% of the heat required for distillation, the second evaporation steam and the distillation steam are compressed, and the heat of compression makes the total heat of the compressed steam be 100-103% of the heat required for evaporation and distillation. 84-88% of the total heat is used for evaporation heat supply, and the remaining 12-16% is used for distillation heat supply.
[0167] The 75°C chemical sewage from outside the boundary area is heat-exchanged to 98°C by the steam condensate in the sewage / condensate heat exchanger 10, and then in the chemical sewage / wastewater heat exchanger with the 123°C waste water from the bottom of the distillation tower The heat is ...
Embodiment 1
[0183] Attached according to the invention figure 1 During the zero discharge process of chemical sewage, the chemical sewage is first heated by steam condensate in the chemical sewage / condensate heat exchanger 10, and then in the chemical sewage / wastewater heat exchanger 11, it exchanges heat with the high-temperature wastewater from the bottom of the distillation tower After that, it enters the upper part of the distillation column 1.
[0184] Ammonia vapor (containing hydrogen sulfide, etc.) escapes from the top of the distillation tower 1, and after being condensed and cooled by the circulating waste water from the evaporator 3 in the partial condensation cooler 2, it is sent to the outside of the boundary area.
[0185] The high-temperature wastewater at the bottom of the distillation tower 1 enters the evaporator 3 for evaporation after being cooled by the chemical wastewater in the chemical wastewater / wastewater heat exchanger 11 .
[0186] The steam from the top of t...
Embodiment 2
[0193] Attached according to the invention figure 2 During the zero-discharge process of chemical sewage, 80-90% of the chemical sewage enters the upper part of the distillation tower 1 after being heated by steam condensate in the sewage / condensate heat exchanger 10. 10-20% of chemical sewage directly enters the top of the distillation tower in the form of cold material.
[0194] After the hydrogen sulfide gas is condensed and cooled by the cold chemical sewage at the top of the distillation tower 1, it is sent outside the boundary area.
[0195] The ammonia vapor from the side line of the distillation tower is sent to the outside of the boundary area after being condensed by the subcondenser; the condensed liquid is returned to the chemical sewage.
[0196] The high-temperature waste water at the bottom of the distillation tower 1 is directly evaporated in the evaporator 3 . The fresh steam heats the circulating waste water from the bottom of the distillation tower 1 in t...
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