High-temperature hydrogen production and microalgae oil production coupling capacity method
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Embodiment 1
[0037] This example provides a method for coupling production capacity of high-temperature hydrogen production and microalgae oil production, which is carried out according to the following steps:
[0038] Step 1: Using the CSTR anaerobic reactor as a high-temperature hydrogen production reactor, pass wastewater into the high-temperature hydrogen production reactor and inoculate the sludge from the secondary sedimentation tank after high-temperature acclimation and cultivation. Continuous high-temperature hydrogen production reaction under the condition of oxygen;
[0039] Step 2: During the high-temperature hydrogen production reaction, the fermentation broth that has been separated and treated by the CSTR anaerobic reactor is continuously transported to the microalgae growth reactor through a peristaltic pump as a microalgae culture fluid, and will be separated and treated by the CSTR anaerobic reactor During the continuous delivery of the final fermentation broth to the mic...
Embodiment 2
[0045] This example provides a method for coupling production capacity of high-temperature hydrogen production and microalgae oil production, which is carried out according to the following steps:
[0046] Step 1: Using the CSTR anaerobic reactor as a high-temperature hydrogen production reactor, pass the wastewater into the high-temperature hydrogen production reactor and inoculate the sludge from the secondary sedimentation tank after high-temperature acclimation and cultivation. Continuous high-temperature hydrogen production reaction under the condition of oxygen;
[0047] Step 2: During the high-temperature hydrogen production reaction, the fermentation broth that has been separated and treated by the CSTR anaerobic reactor is continuously transported to the microalgae growth reactor through a peristaltic pump, and the fermentation broth that has been separated and treated by the CSTR anaerobic reactor is continuously During the process of transporting to the microalgae g...
Embodiment 3
[0052] This example provides a method for coupling production capacity of high-temperature hydrogen production and microalgae oil production, which is carried out according to the following steps:
[0053] Step 1: Using the CSTR anaerobic reactor as a high-temperature hydrogen production reactor, pass wastewater into the high-temperature hydrogen production reactor and inoculate the sludge from the secondary sedimentation tank after high-temperature acclimation and cultivation. Under the condition of continuous high temperature hydrogen production reaction;
[0054] Step 2: During the high-temperature hydrogen production reaction, the fermentation broth that has been separated and treated by the CSTR anaerobic reactor is continuously transported to the microalgae growth reactor through a peristaltic pump, and the fermentation broth that has been separated and treated by the CSTR anaerobic reactor is continuously During the process of transporting to the microalgae growth react...
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Abstract
Description
Claims
Application Information
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