Method for producing general superphosphate from waste water of yellow ginger processing by dry method
A technology for superphosphate, processing wastewater, applied in chemical instruments and methods, peroxides/peroxyhydrates/peroxyacids/superoxides/ozone oxides, phosphorus compounds, etc. Unacceptable, large amount of wastewater treatment and other problems, to achieve the effect of low operating cost, reduced salt content, and reduced treatment difficulty
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Embodiment 1
[0026] The hydrolyzate of turmeric hydrolyzed by hydrochloric acid is filtered or centrifuged to obtain high-concentration waste water and filter cake, and the water content of the filter cake is 80%. The filter cake is carried out in the same way as the traditional process. After three times of rinsing and filtration, the eluate is combined into low-concentration wastewater with a concentration of COD=5000mg / L. The wastewater is neutralized by alkali to pH 6-8, supplemented with N and P nutrients, and passed through an anaerobic reactor (anaerobic contact digester), and the COD removal rate of the wastewater reaches 70%. The effluent COD concentration is 1500mg / L, and then the aerobic reactor (SBR) effluent reaches COD=100mg / L for discharge.
[0027] Get 1 kg of high-concentration waste water and combine 0 kg of low-concentration waste water, add 0 kg of defoamer oleic acid, and 0 kg of fluosilicic acid in the superphosphate production process to form a mixed acid solution, w...
Embodiment 2
[0029] The hydrolyzate of turmeric hydrolyzed by sulfuric acid is filtered or centrifuged to obtain high-concentration wastewater and filter cake, so that the water content of the filter cake reaches 72%. The filter cake is carried out in the same way as the traditional process. After rinsing and filtering, the eluate is combined into low-concentration wastewater with a concentration of COD=8000mg / L. The waste water is neutralized by alkali to PH=7, supplemented with N and P nutrients, and passed through an anaerobic reactor (upflow anaerobic sludge bed) to make the waste water treatment rate reach 78%. The effluent COD concentration reaches 1760mg / L, and then the effluent COD reaches 90mg / L to be discharged through the aerobic reactor (oxidation ditch).
[0030] 100 kg of high-concentration waste water is combined with 200 kg of low-concentration waste water, 200 kg of fluosilicic acid in the superphosphate production process is mixed into a mixed acid solution, 0.25 kg of de...
Embodiment 3
[0032] The hydrolyzate of turmeric hydrolyzed by sulfuric acid is filtered or centrifuged to obtain high-concentration wastewater and filter cake, so that the water content of the filter cake reaches 72%. The filter cake is carried out in the same way as the traditional process. After rinsing and filtering, the eluate is combined into low-concentration wastewater with a concentration of COD=8000mg / L. The wastewater is neutralized by alkali to PH=7, supplemented with N and P nutrients, and the wastewater treatment rate reaches 78% through an anaerobic reactor (anaerobic filter). The effluent COD concentration reaches 1760mg / L, and then the aerobic reactor (aerobic aeration tank) effluent COD reaches 90mg / L for discharge
[0033] 100kg of high-concentration waste water and 150kg of 98% concentrated sulfuric acid are prepared into a 60% sulfuric acid solution, which is directly reacted with 300kg of measured ore powder in the chemical formation chamber. Its reaction time, temper...
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