Starting method of process for synchronously removing carbon, nitrogen and suspended matter in low carbon source wastewater through membrane bioreactor
A membrane bioreactor, suspended solids technology, applied in chemical instruments and methods, biological water/sewage treatment, aerobic and anaerobic process treatment, etc., can solve the problem of low nitrogen removal rate and difficult simultaneous and efficient removal of various pollutants and other problems, to achieve the effect of reducing COD and total nitrogen, saving capital investment and operation management, and saving the number of reactors
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specific Embodiment approach 1
[0015] Specific implementation mode 1: The start-up method of the process of synchronously removing carbon, nitrogen and suspended solids in low-carbon source wastewater by using a membrane bioreactor in this embodiment is carried out according to the following steps:
[0016] 1. Establish a membrane bioreactor water treatment system. The system includes an inlet peristaltic pump 1, a membrane bioreactor 2, an outlet peristaltic pump 3 and an air pump 4. The membrane bioreactor is equipped with a stirrer 2-1 and a membrane module 2- 2. Air distribution device 2-3, DO measuring instrument 2-4, pH measuring instrument 2-5 and liquid level controller 2-6; water inlet peristaltic pump 1 is connected to the water inlet of membrane bioreactor 2, and water outlet peristaltic pump It is connected with the membrane module 2-2 in the membrane bioreactor, and the air pump 3 is connected with the air distribution device 2-3 in the membrane bioreactor;
[0017] 2. Turn on the influent peri...
specific Embodiment approach 2
[0025] Specific embodiment 2: The difference between this embodiment and specific embodiment 1 is that the ammonia nitrogen concentration in the artificial water distribution described in step 3 is 215 mg / L. Others are the same as in the first embodiment.
specific Embodiment approach 3
[0026] Embodiment 3: The difference between this embodiment and Embodiment 1 or 2 is that the carbon-to-nitrogen ratio of the influent in Step 4 is 0.8:1. Others are the same as in the first or second embodiment.
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