Sodium sulfate wastewater treatment system
A treatment system, sodium sulfate technology, applied in water/sewage multi-stage treatment, water/sludge/sewage treatment, alkali metal sulfite/sulfate purification, etc., can solve the pungent and unpleasant smell of waste gas, the energy efficiency of coking wastewater Reduce pollution, air pollution and other problems, achieve resource utilization, realize economic benefits, and reduce equipment investment
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Embodiment 1
[0038] (1) The degreasing device includes the following process steps:
[0039] Step 1, the sodium sulfate wastewater enters the first stirring tank of the air flotation device 101 to adjust the acid and control the pH to 3;
[0040] Step 2: Flow the waste water after air flotation into the inclined plate sedimentation tank 102 to remove the unsettled suspended solids, and then flow into the influent buffer tank 103 .
[0041] (2) The extracting and dephenolizing device comprises the following process steps:
[0042] Step 1, the sodium sulfate wastewater after precipitation and 20% extractant flow into the first stirred tank 202 through the first mixer 201 for forced mixing, the rotating speed is 50 rpm, and the extractant is selected from triisooctylamine;
[0043]Step 2, the mixed sodium sulfate wastewater and extractant enter the extraction tower 203 for oil-water separation, the extraction tower 203 packing height is 6 meters, the interface height is 1m, and the raffinate...
Embodiment 2
[0046] In Example 2, the step 1 in the extraction and dephenolization device was adjusted, and the extraction agent was adjusted to triisooctylamine, and the extraction agent was a combination of triisooctylamine and N,N-dioctylacetamide, and the ratio of the extraction agent was 15. %, others are consistent with Example 1.
[0047] After treatment, the phenol of sewage is 253ppm, COD4020mg / l, and the recovery rate of phenol is 93%.
Embodiment 3
[0049] In embodiment 3, adjustments were made to step 2 in the extraction and dephenolization device, the residence time of the first oil-water separator 204 and the second oil-water separator 205 were both adjusted to 120min, the ratio of the extractant was 10%, and the others were the same as in embodiment 1 be consistent.
[0050] After treatment, the phenol in the sewage is 444ppm, the COD is 4762mg / l, and the recovery rate of phenol is 91%.
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