Treatment method of sulfide in basic residue sewage
A treatment method, sulfide technology, applied in the direction of oxidized water/sewage treatment, etc., can solve the problems of complex operation, long treatment time, and various equipment, and achieve the effect of simple operation process, low treatment cost and long service life
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Embodiment 1
[0033] This embodiment is used to illustrate the treatment method of sulfide in alkali slag sewage of the present invention.
[0034] At 30°C and 0.1 MPa, a certain alkali slag sewage (sulfide content is 28.5% by weight, COD is 359000mg / L) is catalyzed and oxidized in the presence of hollow titanium silicon molecular sieve HTS and hydrogen peroxide (concentration is 30% by weight), Compared with the alkali slag sewage, the dosage of hollow titanium-silicon molecular sieve HTS is 1000mg / L, calculated as hydrogen peroxide, the dosage of hydrogen peroxide is 1mg / L, react for 60min, measure the sulfide content and COD in the sewage after the reaction, and calculate the sulfide The results are shown in Table 1.
Embodiment 2
[0036] This embodiment is used to illustrate the treatment method of sulfide in alkali slag sewage of the present invention.
[0037] At 20°C and 0.15MPa, make a certain alkali slag sewage (sulfide content 25.1% by weight, COD 301850mg / L) in the presence of hollow titanium silicon molecular sieve HTS and ozone-containing gas (30% by volume, the rest is air) Catalytic oxidation is carried out under the condition of alkali slag sewage. The dosage of hollow titanium-silicon molecular sieve HTS is 2000mg / L. In terms of ozone, the dosage of ozone-containing gas is 1.2mg / L. The reaction is 50min, and the sulfide in the sewage is measured after the reaction. content and COD, and calculate the sulfide removal rate and COD removal rate, the results are shown in Table 1.
Embodiment 3
[0039] This embodiment is used to illustrate the treatment method of sulfide in alkali slag sewage of the present invention.
[0040] At 40°C and 0.05MPa, a certain alkali slag sewage (sulfide content is 19.7% by weight, COD is 267600mg / L) is catalytically oxidized in the presence of hollow titanium silicon molecular sieve HTS and hydrogen peroxide (concentration is 50% by weight), Compared with the alkali slag sewage, the dosage of hollow titanium-silicon molecular sieve HTS is 500mg / L, calculated as hydrogen peroxide, the dosage of hydrogen peroxide is 0.8mg / L, react for 70min, measure the sulfide content and COD in the sewage after the reaction, and calculate The results of sulfide removal rate and COD removal rate are shown in Table 1.
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