Method for producing hydrogen by biomass cascade fermentation
A biomass and fermentation technology, applied in fermentation and other directions, can solve the problems of low conversion rate of biological hydrogen production, and achieve the effect of improving the conversion rate of hydrogen and solving the problem of low conversion rate of hydrogen.
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specific Embodiment approach 1
[0007] Specific Embodiment 1: The method for hydrogen production by cascade fermentation of biomass in this embodiment is realized according to the following steps: 1. Anaerobic granular sludge is shaken for 5 to 6 hours to obtain anaerobic activated sludge, which is then placed in a container and filled with nitrogen Seal after 10-20 minutes, heat treatment at 110-130°C for 20-40 minutes; 2. Adjust the pH value of the effluent water from the fermentation process to 7.0-8.0, then add 2-bromoethanesulfonate sodium, and then Pump into the continuous flow stirred tank type acidogenic fermentation hydrogen production reaction equipment as the base material, and then inoculate the anaerobic activated sludge after heat treatment; 3. Continuously fill the continuous flow stirred tank type acidogenic fermentation hydrogen production reaction equipment Nitrogen with a purity of 99.99% and a flow rate of 100ml / min, run for 50 to 60 days under the conditions of a reaction equipment temper...
specific Embodiment approach 2
[0008] Specific embodiment two: the difference between this embodiment and specific embodiment one is that in the step one, the anaerobic granular sludge is shaken and cultivated for 5.5 hours to obtain anaerobic activated sludge, which is then placed in a container, filled with nitrogen for 15 minutes and then sealed. Heat treatment at 120°C for 30min. Other steps and parameters are the same as those in Embodiment 1.
[0009] In this embodiment, the anaerobic granular sludge shaking culture is to put the anaerobic granular sludge into a serum bottle containing dozens of glass beads, seal it with a stopper, and place it in a full-temperature shaking flask at 35°C and 120-180r / min. shake culture in the cabinet.
specific Embodiment approach 3
[0010] Embodiment 3: The difference between this embodiment and Embodiment 1 is that in step 2, the pH value of the effluent of the fermentation biological hydrogen production is adjusted to 7.5. Other steps and parameters are the same as those in Embodiment 1.
[0011] In this embodiment, the reagent used for pH adjustment is KOH or NaOH.
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