Separation method of butyric acid oxidized hydrogen-producing acetogenic dominant microorganisms
A hydrogen-producing acetic acid-producing bacteria and a technology for hydrogen-producing and acetic acid-producing are applied in the directions of microorganism-based methods, biochemical equipment and methods, bacteria, etc., and can solve the problems of low hydrogen production rate and difficult separation of hydrogen-producing acetogenic bacteria, and achieve Improve the treatment efficiency, the method is simple and easy to implement, and the effect of COD removal rate enhancement
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specific Embodiment approach 1
[0012] Specific embodiment 1: The method for isolating the dominant flora of butyric acid oxidation, hydrogen production and acetic acid production in this embodiment is realized according to the following steps: 1. First, the soybean protein waste water with a COD concentration of 2000-10000 mg / L is used as influent water, and then four compartments The chamber anaerobic baffle reactor is used as a model, and then the anaerobic activated sludge is initially domesticated under the conditions of influent pH of 7.0-7.5, temperature of 35°C and HRT of 48h; 2. Several glass balls will be installed Introduce nitrogen into the 120mL sterilized serum bottle, then add 30-60mL of anaerobic activated sludge in the anaerobic baffle reactor in the third chamber after acclimatization, seal it, and then heat it at a temperature of 35°C and a speed of 130r / min. Shake at a high vibration speed for 1 to 2 hours to obtain bacterial suspension A; 3. Use a sterile syringe to take 10 to 20 mL of ba...
specific Embodiment approach 2
[0015] Embodiment 2: This embodiment differs from Embodiment 1 in that the COD concentration of soybean protein wastewater in step 1 is 3000-8000 mg / L. Other steps and parameters are the same as those in Embodiment 1.
specific Embodiment approach 3
[0016] Embodiment 3: The difference between this embodiment and Embodiment 1 is that the COD concentration of soybean protein wastewater in step 1 is 5000 mg / L. Other steps and parameters are the same as those in Embodiment 1.
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