Technology for anaerobic treatment of high concentration desizing wastewater through utilizing pulverized fuel ash
A technology for desizing wastewater and anaerobic treatment, applied in anaerobic digestion treatment, aerobic and anaerobic process treatment, water/sewage multi-stage treatment, etc. The effect of reducing production, facilitating implementation and popularization
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0015] Before the desizing wastewater is discharged into the anaerobic tank, the fly ash and anaerobic effluent are mixed according to the mass ratio of fly ash: anaerobic effluent is 5:95, fully stirred, floating beads are removed, and the fly ash is adsorbed and saturated After the surface is covered by anaerobic bacteria, the mixed solution is pumped into the pulse tank and put into the anaerobic internal circulation reactor. At the same time, industrial glucose with a COD concentration of 2% is added to the mixed solution, and the water temperature is controlled at 35±2°C. The hydraulic retention time of oxygen is 5 days, and the ascending velocity is 6m / h.
[0016] The effluent of the anaerobic internal circulation reactor and the aerobic nitrification liquid discharged from the aerobic tank are discharged into the intermittent anoxic tank. The aeration method of the anoxic tank is microporous aeration, and the hydraulic retention time is 2-2.5 days. The supernatant in th...
Embodiment 2
[0022] Before the desizing wastewater is discharged into the anaerobic tank, the fly ash and the anaerobic effluent are mixed according to the ratio of fly ash: anaerobic effluent is 4: 96 by weight, fully stirred, and the floating beads are removed, and the fly ash is adsorbed and saturated After the surface is covered by anaerobic bacteria, the mixed solution is pumped into the pulse tank and put into the anaerobic internal circulation reactor. At the same time, industrial glucose with a COD concentration of 2% is added to the mixed solution, and the water temperature is controlled at 38±2°C. The hydraulic retention time of oxygen is 6 days, and the ascending velocity is 8m / h.
[0023] The effluent from the anaerobic internal circulation reactor and the aerobic nitrification liquid discharged from the aerobic tank are jointly discharged into the intermittent anoxic tank. The supernatant in the anoxic tank is discharged into the aerobic tank, and the remaining sludge in the a...
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 