Pressurized gas lifting and gas rejuvenation
Devices, processes, systems, and articles of manufacture adapted to treat contaminated fluid, such as organic wastewater, are described. These are described to include lifting contaminated fluids, treating contaminated fluids, or both, through gas application. In certain designs, gas, such as pressurized air, may be used to lift contaminated fluids, such as organic wastewater (i.e., water having contaminating organics of some kind, e.g. residential septic wastewater). In certain designs, gas, such as pressurized air, may also be used to treat fluids interfacing with the gas.
1. A method comprising:
providing a vessel having
an inlet for receiving pressurizing gas,
an inlet for receiving wastewater to be accumulated in the vessel, and
an exit port having an intake opening within the vessel, where wastewater and the pressurizing gas may flow from the intake opening within the vessel and into a wastewater infiltration system;
flowing wastewater into the vessel, the wastewater accumulating in the vessel;
flowing pressurizing gas into the vessel above a top surface of the accumulating wastewater in the vessel, the pressurizing gas developing a pressure above wastewater in the vessel; and
flowing a dose of wastewater upwards from the intake opening and then flowing a dose of the gas upwards from the intake opening and out of the exit port of the vessel, the dose of the gas flowing out of the exit port after the dose of wastewater, and the wastewater and the gas each flowing towards the wastewater infiltration system,
wherein pressurized gas flowing from the inlet into the vessel does not flow out of the exit port when the level of wastewater flowing into the vessel is above the intake opening.
2. The method of claim 1 wherein the pressurizing gas serves to rejuvenate an interface between components of the wastewater infiltration system and surrounding materials.
3. The method of claim 1 wherein the pressurizing gas serves to reduce sludge or other biomass in or around the wastewater infiltration system.
4. The method of claim 1 further comprising:
pressure balancing the vessel by venting through the exit port.
5. The method of claim 1 further comprising:
energizing a compressed gas supply supplying the pressurizing gas to the vessel, the supply activated using a signal input from a level sensor signaling the wastewater level inside the vessel.
6. The method of claim 1 wherein the wastewater entering the vessel is from a residential home.
7. The method of claim 1 further comprising:
maintaining internal gas pressure in the vessel at a level sufficient to prevent wastewater from entering the vessel.
8. The method of claim 1 wherein the pressurizing gas flows from a compressed air or oxygen supply and flows into the vessel.
9. The method of claim 1 further comprising:
varying a cycle time comprising flowing wastewater and pressurizing gas out of the vessel, based on the wastewater organic constituents or based on the oxygen content in the pressurizing gas or based on both.
10. A pressure vessel for accumulating and discharging wastewater comprising:
an inlet configured to receive pressurizing gas;
an inlet positioned to receive pretreated wastewater to be accumulated in the pressure vessel;
an exit port where wastewater and the pressurizing gas flow from the pressure vessel after a target pressure for pressurizing gas is reached in the pressure vessel; and
an exit port intake within the pressure vessel, the exit port intake fluidly coupled to the exit port,
wherein the pressure vessel is further configured to accumulate wastewater and to develop gas pressure above a top surface of the wastewater in the pressure vessel as the wastewater accumulates in the pressure vessel,
wherein the pressure vessel is further configured to dose wastewater followed by nonentrained gas when pressure of the gas above the wastewater in the pressure vessel reaches a pressure value sufficient to displace the wastewater out of the pressure vessel,
wherein pressurized gas flowing from the inlet into the pressure vessel does not flow out of the exit port when the level of wastewater flowing into the pressure vessel is above the exit port intake, and
wherein dosing the wastewater includes lifting the wastewater from the exit port intake within the pressure vessel to an elevation higher than the exit port intake elevation.
11. The pressure vessel of claim 10 wherein the exit port intake is in fluid communication with a wastewater infiltration system.
12. The pressure vessel of claim 10 further comprising: a wastewater level sensor.
13. The pressure vessel of claim 10 wherein the inlet for receiving pressurizing gas and the inlet for receiving wastewater is in the same multi-purpose coupling.
14. The pressure vessel of claim 13 wherein the multi-purpose coupling also includes the exit port and a clean out.
15. The pressure vessel of claim 13 wherein the inlet for receiving pressuring gas is coupled to a blower or compressor or other source of compressed gas.
16. The pressure vessel of claim 10 wherein the inlet configured to receive pressurizing gas is coupled to a blower or a compressor or a compressed gas source that is itself configured to be activated by a timer or by using a signal input from a level sensor signaling the wastewater level inside the pressure vessel or both.
17. The pressure vessel of claim 10 wherein the inlet positioned to receive pretreated wastewater is fluidly connected to a pretreatment filter.
18. The pressure vessel of claim 10 wherein the pretreated wastewater is pretreated to remove sludge and foreign debris from wastewater reaching the pressure vessel.