A method for excess sludge treatment and resource recovery and a method for improving the yield of vfas
A technology of excess sludge and resource recovery, applied in the field of organic solid waste recycling, can solve the problem of long anaerobic fermentation of sludge and denitrification and phosphorus removal, increasing subsequent treatment steps of fermentation broth, unfavorable process operation and management, etc. problems, to achieve the effect of simplifying the process flow, reducing the subsequent processing process, and improving the yield
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Embodiment 1
[0029] (1) The first stage (UASB liquid fermentation without adding nitrogen and phosphorus removal device): use deionized water to adjust the total solid concentration (TS) of the remaining sludge (Wuxi Shuofang Sewage Plant, Jiangsu) to 75g / L, and use The NaOH solution adjusts its pH to 12, and after sealing, it is placed under the condition of 90-105° C. and stirred slowly for 12 hours for pretreatment. The pretreatment hydrolyzate is centrifuged, separated liquid (organic load is 8kg COD / m 3 / d) Continuously feed into a 5L UASB reactor (inoculation seed sludge occupies 20% of the volume) for fermentation. During fermentation, the temperature in the reactor is controlled at 35±2°C, the pH is controlled at 9-10, and the yields of ammonia nitrogen, total phosphorus, and TVFA are as follows: figure 2 , 3 Shown in the first stage of . The concentrations of ammonia nitrogen and total phosphorus were 991.60±3.23mg / L and 532.16±1.59mg / L respectively during smooth operation, an...
Embodiment 2
[0032] UASB liquid fermentation with nitrogen and phosphorus removal device added:
[0033] Use deionized water to adjust the total solids concentration (TS) of the remaining sludge (Wuxi Shuofang Sewage Plant, Jiangsu) to 75g / L, and adjust its pH to 12 with NaOH solution, seal it and place it at 95°C for 12 hours with slow stirring preprocessing. The pretreatment hydrolyzate is centrifuged, separated liquid (organic load is 8kg COD / m 3 / d) Continuously feed into a 5L UASB reactor (inoculation seed sludge occupies 20% of the volume) for fermentation. During the fermentation, the temperature in the reactor is controlled at 35±2° C., and the pH is controlled at 9-10. Among them, the fermented liquid of UASB enters the nitrogen and phosphorus removal device with a reflux ratio of 0.8 and an HRT of 2.0h, and the nitrogen and phosphorus removal device maintains Mg 2+ Dosing concentration is 1000±5.0mg / L, temperature and pH are the same as UASB. During smooth operation, the ammo...
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