Method for hydraulic dehydration and anaerobic fermentation to treat sludge from urban domestic sewage treatment plants
A technology of urban domestic sewage and anaerobic fermentation, which is applied in the field of resource treatment of sludge in urban domestic sewage treatment plants, can solve the problems of not mentioning the dehydration effect of the device, and achieve the reduction of external energy dependence, a wide range of sources, and combustion calorific value. big effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0058] The first stage—hydraulic deep dehydration stage: Weigh 55g of sludge (water content about 80%), 1.2g of CaO, and 12.5mL of deionized water, mix them evenly, and wrap them with 80-100 mesh nylon filter cloth. The hydraulic pipe pressure is 5.0Mpa, and the sludge is dehydrated. The water content of the obtained dewatered sludge is 58%, the press filtrate pH7.12, COD4563mg / L, NH 4 + -N52mg / L.
[0059] The second stage—the anaerobic fermentation hydrogen production stage using the press-filtrate as the substrate: add 0.2% (based on the quality of the press-filtrate) iron powder, then add 0.2g / L-press-filtrate BESA, and let it stand for 24 hours. The fermentation temperature is 37±1°C, and the HRT is 3 days. The obtained hydrogen production rate was 585mL / (L·d), the effluent pH was 6.92, the COD was 1354mg / L, the COD removal rate was 70.3%, and the NH 4 + -N is 9mg / L, NH 4 + -N removal rate was 82.7%.
Embodiment 2
[0061] The first stage—hydraulic deep dehydration stage: Weigh 50g of sludge (moisture content about 80%), CaO0.8g, deionized water 12.5mL, mix well, and wrap with 80-100 mesh nylon filter cloth. The hydraulic pipe pressure is 4.5MPa, and the sludge is dehydrated. The water content of the obtained dewatered sludge is 53%, the press filtrate pH7.05, COD4468mg / L, NH 4 + -N48mg / L.
[0062] The second stage—the anaerobic fermentation hydrogen production stage using the press-filtrate as the substrate: add 0.2% (based on the quality of the press-filtrate) iron powder, then add 0.2g / L-press-filtrate BESA, and let it stand for 24 hours. The fermentation temperature is 37±1°C, and the HRT is 3 days. The obtained hydrogen production rate was 570mL / (L·d), the effluent pH was 6.87, the COD was 1254mg / L, the COD removal rate was 71.9%, and the NH 4 + -N11mg / L, NH 4 + -N removal rate was 77.1%.
Embodiment 3
[0064] The first stage—hydraulic deep dehydration stage: Weigh 50g of sludge (moisture content about 80%), CaO 1.0g, and deionized water 12.5mL, mix well, and wrap with 80-100 mesh nylon filter cloth. The hydraulic pipe pressure is 5.5MPa, and the sludge is dehydrated. The moisture content of the obtained dewatered sludge is 49%, the press filtrate pH7.17, COD4863mg / L, NH 4 + -N56mg / L.
[0065] The second stage—the anaerobic fermentation hydrogen production stage using the press-filtrate as the substrate: add 0.2% (based on the quality of the press-filtrate) iron powder, then add 0.2g / L-press-filtrate BESA, and let it stand for 24 hours. The fermentation temperature is 37±1°C, and the HRT is 3 days. The obtained hydrogen production rate was 614mL / (L·d), the pH of the effluent was 6.95, the COD was 1396mg / L, the COD removal rate was 71.3%, and the NH 4 + -N13mg / L, NH 4 + -N removal rate was 76.8%.
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 

