Treatment method for salt-containing wastewater
A technology for salt-containing wastewater and treatment methods, which is applied in the fields of water/sewage multi-stage treatment, water/sludge/sewage treatment, chemical instruments and methods, etc. problems, to achieve the effect of improving the utilization rate of industrial water, saving treatment costs, and achieving good treatment effects
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Embodiment 1
[0047] A 1.4 million tons / year catalytic cracking unit in an oil refinery, with a flue gas volume of 150,000 NM 3 / h, temperature 200℃, using wet flue gas desulfurization technology, 20 tons / hour reverse osmosis concentrated water enters the cooling water washing tower, adopts figure 1 Shown technological process, its operation condition is as follows:
[0048] After the reverse osmosis concentrated water reacts in the cooling water washing tower for 2 minutes, it enters the oxidation flocculation tank for aeration and oxidation. The volume ratio of air and water is 3:1, the amount of flocculant polyaluminum chloride is 9 mg / L, and the residence time is 20 minutes. .
[0049] The reverse osmosis concentrated water enters the neutralization sedimentation tank from the oxidation flocculation tank, and sodium hydroxide is added to adjust the pH to 7.5, and the residence time is 30 minutes. After the inclined plate settles, it enters the multimedia filter with coal and quartz sand...
Embodiment 2
[0054] A 1.4 million tons / year catalytic cracking unit in an oil refinery, with a flue gas volume of 150,000 NM 3 / h, temperature 200°C, using wet flue gas desulfurization technology, mixing 40 tons / h of reverse osmosis concentrated water, circulating water sewage, reclaimed water reverse osmosis concentrated water, electrodialysis concentrated water and other salty wastewater Water is used as the process water of the washing tower, using figure 1 Shown technological process, its operation condition is as follows:
[0055] The reverse osmosis concentrated water reacts in the cooling water washing tower for 5 minutes, and then enters the oxidation flocculation tank, adding 40 mg / L of oxidant ozone, 9 mg / L of polymerized ferric sulfate as a flocculant, and 10 minutes of residence time.
[0056] The wastewater enters the neutralization sedimentation tank from the oxidation flocculation tank, and potassium hydroxide is added to adjust the pH to 8, and the residence time is 30 min...
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