A method for treating salt-containing wastewater in the production process of propylene oxide or epichlorohydrin and device for realizing the method
A technology for the production process of epichlorohydrin, which is applied in the field of salty wastewater treatment, can solve problems such as pollution and low energy consumption, and achieve the effects of good economic benefits, low energy consumption, and low cost
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Embodiment 1
[0047] After cooling the salty wastewater to 36°C in a cooling tower, it is transported to the first settling tank for sedimentation, and then the settled wastewater is placed in a regulating tank for pre-aeration, and then transported to the blast aeration tank Oxygen aeration. The activated sludge is transported to the blast aeration tank, and a part of the activated sludge comes from the second settling tank, and is mixed with the wastewater for aeration and oxygen supply. After the mixed sludge mixture is returned to the second settling tank for settling, the supernatant is placed in the contact oxidation tank for secondary oxidation treatment, and the remaining turbidity in the lower layer is stored in the second settling tank; after secondary oxidation The treated supernatant is placed in the third settling tank for settling treatment and then transported to the solar salt tank. The COD of the pretreated wastewater is 30ppm, and the content of calcium chloride is 3.95% ...
Embodiment 2
[0051] After cooling the salty wastewater to 36.5°C in a cooling tower, it is transported to the first settling tank for sedimentation, and then the settled wastewater is placed in a regulating tank for pre-aeration, and then transported to the blast aeration tank Oxygen aeration. The activated sludge is transported to the blast aeration tank, and a part of the activated sludge comes from the second settling tank, and is mixed with the wastewater for aeration and oxygen supply. After the mixed sludge mixture is returned to the second settling tank for settling, the supernatant is placed in the contact oxidation tank for secondary oxidation treatment, and the remaining turbidity in the lower layer is stored in the second settling tank; after secondary oxidation The treated supernatant is placed in the third settling tank for settling treatment and then transported to the solar salt tank. The COD of the pretreated wastewater is 40ppm. The content of calcium chloride is 5% base...
Embodiment 3
[0055] The salty wastewater is transported to multiple sun-drying ponds through pipelines for drying to obtain a calcium chloride feed liquid with a calcium chloride content of 45wt% based on the total mass of the calcium chloride solution. The impurity COD in the wastewater is reduced to 300ppm, and the calcium chloride The feed liquid is transported to the brine collection pool through the pumping system.
[0056] The calcium chloride feed liquid obtained by sun drying is transported to the feed liquid buffer tank, and the pH is adjusted to 7. After pressure filtration, it enters the solution evaporator through the delivery pump to increase concentration. The temperature during concentration is 220°C, and then enters the high temperature temporary storage tank. At this time, based on the total mass of the calcium chloride solution entering the high-temperature temporary storage tank, the content of calcium chloride is 50.6wt%, and then transported to the spray granulation flu...
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