Quick start-up method of integrated autotrophic denitrification system
An autotrophic denitrification and rapid start-up technology, applied in chemical instruments and methods, water treatment parameter control, water/sludge/sewage treatment, etc., can solve the problems of long start-up time, unstable operation, and low total nitrogen removal load, etc. problem, to achieve the effect of short start-up time, stable operation, and inhibition of proliferation
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Patents(China)
- Current Assignee / Owner
- Publication Date
- 2019-06-11
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Abstract
Description
technical field
[0001] The invention relates to a quick start-up method of an integrated autotrophic denitrification system, belonging to the technical field of high ammonia nitrogen sewage treatment. technical background
[0002] In 1994, Mulder et al. published an article in the journal Microbiology Ecology saying that they discovered the oxidation reaction of ammonia under anaerobic conditions in a denitrification fluidized bed reactor, and called the process anaerobic ammonium oxidation reaction. Later studies found that the microorganisms involved in this reaction were anammox bacteria, which is a kind of autotrophic bacteria that can use ammonia nitrogen and nitrite nitrogen to generate nitrogen gas, so as to achieve the purpose of sewage denitrification. After the discovery of anammox bacteria, it has attracted great attention from sewage treatment workers. The new denitrification process based on anammox bacteria has become a research hotspot in recent years. Compar...
Examples
Embodiment Construction
[0024] The first step, the establishment of an integrated autotrophic denitrification system
[0025] 1. Inoculate 3.5L of short-range nitrification sludge and 3L of anammox sludge cultivated in this laboratory into an SBR reactor with a total volume of 8L and an effective volume of 7L (see figure 1 ), the sludge concentration in the reactor after inoculation was 3480mgSS / L.
[0026] 2. According to the measured nitrite nitrogen accumulation rate and consumption rate, the operation mode of the SBR reactor is determined as follows: each cycle is: water inflow 20min, reaction 360min (3 aeration / anoxic sections, each aeration time 30min, anoxic time 90min), stirring and degassing for 60min, sedimentation for 30min, effluent for 5min, idle for 5min; 3 cycles per day, each cycle is 8 hours.