Accelerant facilitating growth of salt-resistive nitrifying bacteria in high-salt wastewater
A technology of high-salt wastewater and accelerator, applied in the directions of bacteria, water pollutants, chemical instruments and methods, etc., can solve undisclosed problems, and achieve the effect of improving removal rate and rapid reproduction and growth.
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Embodiment 1
[0014] Dosing the accelerator of the present invention into high-salt wastewater of a marine petrochemical industry, the specific conditions are as follows: the quality of the influent water is COD=357mg / l, NH3-N=98.5mg / l, the salt content is about 3%, and the pH The value is between 7.5-8.5. The SBR process is used for treatment, and an operation cycle is 13-24 hours. In each operation cycle, water intake is 30 minutes, aeration is 10-20 hours, sedimentation is 1-2 hours, drainage is 1 hour, and the remaining time is idle period. The temperature is 30°C. The ratio of adding the accelerator of the present invention in waste water is 10ml / l (the control group does not add this accelerator), and the composition of this accelerator comprises: every 1000ml water contains sodium chloride 40g, ammonium sulfate 0.2g, heptahydrate Magnesium sulfate 0.01g, dipotassium hydrogen phosphate 0.8g, ferrous sulfate heptahydrate 0.01g calcium chloride 7g, sodium bicarbonate 1g, vitamin soluti...
Embodiment 2
[0019] The accelerator of the present invention is added to a marine petrochemical high-salt wastewater, and the specific conditions are as follows: the influent water quality is COD=369mg / l, NH3-N=97.8mg / l, the salt content is about 3%, and the pH The value is between 7.5-8.5. The SBR process is used for treatment, and an operation cycle is 13-24 hours. In each operation cycle, water intake is 30 minutes, aeration is 10-20 hours, sedimentation is 1-2 hours, drainage is 1 hour, and the remaining time is idle period. The temperature is 30°C. The ratio of adding the accelerator of the present invention in waste water is 20ml / l (the control group does not add this accelerator), and the composition of this accelerator comprises: every 1000ml water contains sodium chloride 35g, ammonium sulfate 0.5g, heptahydrate Magnesium sulfate 0.03g, dipotassium hydrogen phosphate 1.2g, ferrous sulfate heptahydrate 0.05g calcium chloride 7.5g, sodium bicarbonate 1.5g, sodium nitrite 0.5g, vita...
Embodiment 3
[0024] The accelerator of the present invention is added to a marine petrochemical high-salt wastewater, and the specific conditions are as follows: the influent water quality is COD=347mg / l, NH3-N=98.2mg / l, the salt content is about 3%, and the pH The value is between 7.5-8.5. The SBR process is used for treatment, and an operation cycle is 13-24 hours. In each operation cycle, water intake is 30 minutes, aeration is 10-20 hours, sedimentation is 1-2 hours, drainage is 1 hour, and the remaining time is idle period. The temperature is 30°C. The ratio of adding the accelerator of the present invention in waste water is 30ml / l (the control group does not add this accelerator), and the composition of this accelerator comprises: every 1000ml water contains sodium chloride 30g, ammonium sulfate 0.5g, heptahydrate Magnesium sulfate 0.03g, dipotassium hydrogen phosphate 1.4g, ferrous sulfate heptahydrate 0.03g calcium chloride 7.5g, sodium bicarbonate 1.6g, vitamin solution 3ml (vit...
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