System for wastewater treatment through controlling microorganism purification functions
View Patent ↗Increased control and efficiency over the wastewater purification can be achieved through creating conditions that allow to selectively prioritize the digestive function of microorganism in the activated sludge. The gas-dispersion return sludge is created using pure oxygen or oxygen containing trace amounts of ozone as a reactive gas, which is blended with return sludge to create a mixture of gas and liquid, which is passed through an atomizer or a cavitation pump to instantly render the reactive gas in the mixture to an ultra-fine bubble state. At least a portion of the ultra-fine bubbles dissolve within the gas-dispersion return sludge, activating the dormant microorganisms. Due to a complete or an almost complete absence of digestable organic material in the gas-dispersion return sludge, the microorganism prioritize their digestive function, and when exposed to organic pollutants present in wastewater, digest the pollutants into water and carbon dioxide at an increased rate.
1. A system for wastewater treatment through controlling microorganism purification functions, comprising:
a gas generator configured to provide at least one reactive gas into a return sludge that comprises aerobic microorganisms capable of exhibiting at least one of a reproductive function, by which the microorganisms absorb organic pollutants and multiply using the absorbed pollutants, and a digestive function, by which the microorganisms digest the organic pollutants as a source of energy into water molecules and molecules that comprise carbon, wherein the return sludge is substantially free of the organic pollutants and wherein at least a majority of the microorganisms are in a dormant state before the at least one reactive gas is provided;
a machine comprising one of an atomizer or a cavitation pump and configured to form a gas-dispersion return sludge by rendering the at least one reactive gas into ultra-fine bubbles within the return sludge, wherein a portion of the ultra-fine bubbles dissolves within the return sludge, wherein the at least one dissolved reactive gas activates at least a portion of the dormant microorganisms, and wherein the gas-dispersion return sludge is substantially free of the organic pollutants; and
a controller in control of the machine and configured to:
obtain an amount of the return sludge to be produced by the microorganisms;
determine a ratio of a volume of wastewater comprising at least some of the organic pollutants to a volume of the gas-dispersion return sludge necessary to produce the amount of the return sludge; and
control the machine to form a mixed liquor by combining the gas-dispersion return sludge with the wastewater in accordance with the ratio, wherein the microorganisms prioritize one of the digestive or the reproduction function based on an availability of the organic pollutants in the mixed liquor.
2. A system according to claim 1 , wherein the ratio is determined based on experimental data.
3. A system according to claim 1 , wherein the ratio depends on one or more of an identity of one or more strain of the microorganisms, a concentration of the gas-dispersion return sludge, and a concentration of the organic pollutants within the wastewater.
4. A system according to claim 1 , further comprising:
a mixer through into which the gas-dispersion return sludge is provided by the machine and which distributes the gas-dispersion return sludge into one or more aerobic reaction vessels in which the mixed liquor is formed.
5. A system according to claim 1 , wherein the gas-dispersion return sludge is pumped directly by the machine into the one or more aerobic reaction vessels where the mixed liquor is formed.
6. A system according to claim 1 , further comprising:
a treated water processing unit which receives supernatant derived from the mixed liquor and is configured to perform sterilization of the supernatant.
7. A system according to claim 6 , wherein the sterilized supernatant is expelled as drinking water.
8. A system according to claim 1 , wherein the at least one reactive gas comprises one of oxygen and oxygen with a trace of ozone.
9. A system according to claim 8 , wherein a concentration of the oxygen dissolved within the gas-dispersion return sludge is at least 10 mg/L.
10. A system according to claim 8 , wherein a concentration of the ozone dissolved within the gas-dispersion return sludge is 0.01 mg/L to 0.5 mg/L.
11. A system according to claim 1 , wherein the cavitation pump produces the ultra-fine bubbles via cavitation produced by an impeller of the pump.
12. A system according to claim 1 , wherein rotation of the impeller of the pump slices larger bubbles into the ultra-fine bubbles.
13. A system according to claim 1 , wherein the controller is interfaced to an Internetwork and receives user input via the Internetwork.
14. A system according to claim 1 , wherein the controller receives user input through an on-site user interface.
15. A system according to claim 1 , wherein the volume of the gas-dispersion return sludge is at least 10% of the volume of the wastewater to be treated.
16. A system according to claim 1 , wherein the microorganisms exercise the reproductive function upon a satiation of the digestive function in a presence of the organic pollutants remaining in the mixed liquor following the satiation of the digestive function.
17. A system according to claim 16 , wherein the exercise of the reproductive function produces additional return sludge.
18. A system according to claim 17 , the additional return sludge is used for treatment of additional wastewater.
19. A system according to claim 1 , wherein the ratio is determined based on experimental data associated with a geographic location from which the wastewater originates and a time.
20. A system according to claim 1 , wherein at least a portion of the microorganisms enter the dormant state following exercise of at least one of the digestive function and the reproductive function.