Method for two-stage anaerobic digestion treatment of molasses alcohol wastewater
A technology of molasses alcohol wastewater and anaerobic digestion, applied in anaerobic digestion treatment, chemical instruments and methods, natural water treatment, etc., can solve the adverse effects of anaerobic digestion treatment effects, adverse effects of reactor operation, and affect anaerobic fermentation Biogas production and other issues, to achieve the effect of improving biogas production rate and biomass energy recovery rate, good research and application prospects, and improving anaerobic treatment effect
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Embodiment 1
[0018] Embodiment 1 Experimental device diagram
[0019] The temperature of the reaction system of the two-stage UASB reactor for the treatment of molasses alcohol wastewater is 35°C, and the initial pH of the influent is adjusted to 7.20-7.50 with sodium carbonate solution. The generated biogas is desulfurized by a water-sealed bottle, measured by a wet gas flow meter, and then collected by a gas collection bag to determine the gas composition and content. Before and after the anaerobic digestion reaction, the pH, COD concentration, sulfate concentration and sulfide concentration of the wastewater were measured; after the reaction, the biogas volume and methane content were measured, and the determination methods were analyzed by national standard methods (Table 1 ).
[0020] Table 1 Analysis items and methods
[0021]
[0022] The experimental design is that the effective volume of the primary anaerobic UASB reactor is 12L, the volume of the reaction zone is 7.7L, the v...
Embodiment 2
[0023] Example 2 Changes in pH of anaerobic effluent
[0024] Depend on figure 2 It can be seen that the pH of the effluent of the two-stage anaerobic reactor is higher than the pH of the influent, and it shows an upward trend as the load increases. The reason for the increase of effluent pH value may be that the concentration of organic acids in the influent water is high. During the anaerobic digestion process, MPB and SRB directly use the organic acids in the wastewater to carry out metabolic activities such as methane production and sulfate radical reduction. The acid-producing bacteria are in In a weak position, the metabolic activity is inhibited, and the concentration of organic acids in the wastewater is reduced.
Embodiment 3
[0025] Example 3 Changes of influent and effluent COD concentration and COD removal rate
[0026] The degradation of wastewater COD is as follows: image 3 shown. Depend on image 3 -a It can be seen that with the increase of influent COD concentration, the removal of COD in the first-stage anaerobic digestion process first increases, then decreases and gradually stabilizes at about 45%. The COD removal rate of the primary anaerobic process was low at the initial stage of reactor operation, which may be due to the fact that the microorganisms in the sludge had not yet adapted to the molasses alcohol wastewater; when the reactor ran to the 9th day, the primary COD removal rate rose to 58.3%, indicating that the microorganisms had not yet adapted to the molasses alcohol wastewater; It basically adapts to wastewater, and can effectively use the organic matter in wastewater for metabolic activities; when the reactor runs to the 18th day, the primary COD removal rate reaches a ma...
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