Method for enhancing aerobiotic ammonia oxidizing bacterium gathering through N-acylated homoserine lactones
An aerobic ammonia oxidizing bacteria, acyl homoserine technology, applied in chemical instruments and methods, water/sludge/sewage treatment, biological water/sewage treatment, etc. AOB and quorum sensing less problems, to achieve the effect of efficient and stable operation, reduce loss, and shorten the required time
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Embodiment 1
[0025] Inorganic ammonia nitrogen (NH 4 Cl) The artificial wastewater domesticates the activated sludge with AOB as the single dominant bacterium in the SBR reactor. After the domestication, the inorganic ammonia nitrogen volume load of the sludge reaches 0.81g / (L·d), and the ammonia nitrogen degradation efficiency is close to 100%. The average particle size of the mud is 175.03 μm, and the flora structure is AOB as the single dominant bacterium (content is 25%). 5mlOD 600 =0.1 bacterial suspension was added to the microwell plate, and nitrogen source (100mgNH 4 + -N / L), trace elements and 2μM 3-oxo-C 6 -HSL, after being placed in an incubator (28°C) for 24h and 48h respectively, the biomass of the biofilm was measured. The 24h in this embodiment means that the microwell plate is put into the incubator and then continuously cultured, and the biomass of the biofilm is taken out after 24h; 48h means that the nitrogen source, trace elements and 3-oxo of the same load are adde...
Embodiment 2
[0028] Inorganic ammonia nitrogen (NH 4 Cl) The artificial wastewater domesticates the activated sludge with AOB as the single dominant bacterium in the SBR reactor. After the domestication, the inorganic ammonia nitrogen volume load of the sludge reaches 1.5g / (L·d), and the ammonia nitrogen degradation efficiency is close to 100%. The average particle size of the mud is 168.5 μm, and the flora structure is AOB as the single dominant bacterium (content is 40%). 5mlOD 600 =0.2 bacteria suspension was added into the microwell plate, and nitrogen source (100mgNH 4 + -N / L), trace elements and 2μM AHLs with different chemical structures were placed in an incubator (35°C) for 12h and 24h respectively, and then the biomass of the biofilm was measured to investigate the effect of the chemical structure of AHLs on the ability of AOB to attach and grow . The AHLs selected in this embodiment are respectively C 6 -HSL, C 8 -HSL, C 10 -HSL and 3-oxo-C 6 -HSL, 3-oxo-C 8 -HSL, 3-oxo...
Embodiment 3
[0031] The activated sludge (60% content) in which AOB is the dominant bacterium was cleaned and then inoculated into three identical columnar reactors (effective volume 200ml, height 160mm, inner diameter 40mm). The initial inoculated sludge concentration was 2.36gMLSS / L, MLVSS1.87g / L, and the ammonia nitrogen load was 0.4kg / (m 3 d). Sequenced batch operation is carried out. A cycle of sequenced batch operation includes water intake, aeration, sedimentation and drainage stages, and the hydraulic retention time is 24h. The influent of one of the reactors only contained nitrogen source and trace elements, and no AHL signal molecules were added. In addition to nitrogen source and trace elements, the influent water of the other two reactors also added 3-oxo-C 6 -HSL and C 6 -HSL. During the aeration phase, keep DO>2mg / L and pH between 7-8. After first settling for 1-10 minutes, drain the loose and slow-settling sludge on the upper layer, then settle for 20-30 minutes, and the...
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