Method for strengthening raw water biological pretreatment biological membrane enrichment and operating performance stability
A technology of biological pretreatment and operational performance, applied in sustainable biological treatment, biological water/sewage treatment, chemical instruments and methods, etc., can solve the problems of ineffective removal of organic matter and nitrogen, etc., and is conducive to biomass enrichment. , The effect of large specific surface area and high adsorption performance
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Embodiment 1
[0019] An upflow biofilm reactor with an overflow weir with an effective volume of 15.0 L was used. Inoculate raw water (river water), the average turbidity is 15NTU, the carrier filler is porous polyurethane filler, and the specific surface area is 2395m 2 / m 3 , the porosity is 90%, the solid volume filling rate is 3.47%, and the bulk filling rate is 70%. Start the reactor in the internal circulation continuous water feeding mode. The start-up period is 15 days. The internal circulating water is replaced every 5 days, and the circulating water is replaced 3 times. The total circulating water is 2.7 times the effective volume of the reactor, and the hydraulic retention time is 4h. During the start-up stage of the reactor, 200 grams of diatomite (13.3g / L effective volume of the reactor) was added at a time. The alginate is mixed evenly with the carrier. Ammonium sulfate is added to provide ammonia nitrogen at a concentration of 5mg / LNH 4 + -N, the added easily biodegradab...
Embodiment 2
[0022] A columnar biofilm reactor with an effective volume of 15.0 L was used. Influent composition, carrier filler, start-up method and time, addition of ammonia nitrogen and organic matter levels are the same as in Example 1. Add 50 grams of diatomaceous earth (3.3g / L) at one time during the operation stage of the reactor (day 53). The particle size of diatomite is about 0.1mm. Mechanical stirring is used to mix the diatomaceous earth and the carrier evenly.
[0023] After 16 days of operation, the start-up of the reactor was successfully completed, and the ammonia nitrogen oxidation rate was changed from 0.46 mg / L / d increased to 6.71mg / L / d. During operation, when diatomite is not added, although the effluent ammonia nitrogen can meet the requirements of GB5749-2006 water quality standard under low operating load conditions, but when the influent load is 6.4-18.64mg / L / d, the concentration of ammonia nitrogen in the effluent reaches 0.54-1.79mg / L, which is higher th...
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