Method for treating high-calcium and high-salt industrial wastewater
A technology for industrial wastewater and a treatment method, applied in the field of water treatment, can solve problems such as undisclosed salt-containing wastewater treatment, and achieve the effect of reducing the tendency of wastewater scaling
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Embodiment 1
[0129] Salinity content (TDS) 3.0%, COD 1250mg / L, NH 3 -The industrial waste water of N 37.6mg / L enters the high-calcium, high-salinity industrial waste water treatment system of the present invention;
[0130] a. Pretreatment system,
[0131] ①Mixed flocculation and settling unit: adding flocculant, the reaction time is 10 minutes, and the settling time is 60 minutes;
[0132] ② Pre-oxidation unit: use compressed air to aerate, control the dissolved oxygen between 1.0-2.0mg / L; adjust the pH and control the pH value between 6.0-6.5; built-in iron shavings, its porosity is 55%-95% ;
[0133] b. The hydrolytic acidification tank of the hydrolytic acidification anaerobic biochemical treatment system is divided into two sections I and II, and the structural characteristics are as follows:
[0134] ① Section I pool occupies about 3 / 5 of the volume of the pool, and adopts an intensity-controllable submerged agitator;
[0135] ②The second-stage pool accounts for about 2 / 5 of the ...
Embodiment 2
[0173] According to the method and step of embodiment 1, process index is as follows:
[0174] The salinity content (TDS) of industrial wastewater entering the system is 2.0%, COD 1126mg / L, NH 3 -N41.3mg / L,
[0175] a. Pretreatment system,
[0176] ①Mixed flocculation and settling unit: adding flocculant, the reaction time is 10 minutes, and the settling time is 120 minutes;
[0177] ② Pre-oxidation unit: use compressed air to aerate, control the dissolved oxygen between 1.0-2.0mg / L; adjust the pH and control the pH value between 6.0-6.5; built-in iron shavings, its porosity is 55%-95% ;
[0178] b. The hydrolytic acidification tank of the hydrolytic acidification anaerobic biochemical treatment system is divided into two sections I and II, and the structural characteristics are as follows:
[0179] ① Section I pool occupies about 3 / 5 of the volume of the pool, and adopts an intensity-controllable submerged agitator;
[0180] ②The second-stage pool accounts for about 2 / 5 ...
Embodiment 3
[0218] According to the method and step of embodiment 1, process index is as follows:
[0219] The salinity content (TDS) of industrial wastewater entering the system is 1.51%, COD 881.0mg / L, NH 3 -N 11.7mg / L,
[0220] a. Pretreatment system,
[0221] ①Mixed flocculation and settling unit: adding flocculant, the reaction time is 10 minutes, and the settling time is 120 minutes;
[0222] ② Pre-oxidation unit: use compressed air to aerate, control the dissolved oxygen between 1.0-2.0mg / L; adjust the pH and control the pH value between 6.0-6.5; built-in iron shavings, its porosity is 55%-95% ;
[0223] b. The hydrolytic acidification tank of the hydrolytic acidification anaerobic biochemical treatment system is divided into two sections I and II, and the structural characteristics are as follows:
[0224] ① Section I pool occupies about 3 / 5 of the volume of the pool, and adopts an intensity-controllable submerged agitator;
[0225] ②The second-stage pool accounts for about 2...
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