Method for converting kitchen waste into wastewater denitrification carbon source through catalytic wet oxidation
A technology for catalyzing wet oxidation and kitchen waste, applied in the field of wet waste recycling, can solve the problems of low conversion rate, long cycle, low resource utilization efficiency, etc., and achieves short conversion time, reduction of nitrogen and phosphorus, and good economy. Effect
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Embodiment 1
[0031] This embodiment provides a method for catalytic wet oxidation of food waste into waste water denitrification carbon source, the process flow is as follows figure 1 As shown, the specific implementation steps are as follows: Take 50L of food waste, use screens, magnetic separation, etc. to screen out debris, and then crush the food waste into 10-50mm particle size by mechanical extrusion, shearing, etc.; The kitchen waste is broken into small particles for water replenishment. The mass ratio of food waste to water replenishment is 1:1 (the mass ratio of food waste to water replenishment is 1:1 to 1:2, preferably 1:1 in this embodiment), which is convenient Mix evenly with replenishing water; pump the material into the reactor, acid hydrolyze at 100°C (temperature range is 100-150°C, preferably 100°C in this embodiment) for 120min, and add FeSO 4 , the addition amount is 0.5% of the total mass of kitchen waste, promotes the hydrolysis and acidification reaction with the p...
Embodiment 2
[0033] Using the liquid prepared in Example 1 as a waste water denitrification carbon source to treat waste water containing nitrate nitrogen
[0034] The activated sludge of a sewage treatment plant in Wuhan was inoculated into a 10L SBR reactor for domestication, and the artificially prepared sewage was used for denitrification experiments. The experimental temperature was normal temperature, and the sludge concentration in the reactor was maintained at VSS=2500mg / L. Sodium is as nitrate (30mg / L nitrate radical), and add respectively the liquid carbon source (0.25g / L) that methyl alcohol (0.25g / L), glucose carbon source (0.25g / L) and embodiment 1 prepare, denitrification The reaction is carried out under the condition of micro-oxygen or anoxic (dissolved oxygen is less than 0.1mg / L). Each cycle of the experiment is 5h, and the corresponding carbon source is added at one time at the beginning of the reaction. The reaction stage is 4h, followed by 1h of precipitation. During ...
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