Patent Application
20130118977
This disclosure generally relates to fluid treatment apparatuses, and more particularly to a process and apparatus capable of enriching a liquid with a gas and introducing the gas-enriched liquid into a second liquid.
Systems are known that make use of liquids enriched with a gas. For example, U.S. Pat. No. 2,713,026 to Kelly et al. appears to disclose the use of a gas-enriched fluid for wastewater treatment, and in particular the introduction of an air-supersaturated fluid into a pool of wastewater to suspend solids in the wastewater and facilitate their removal. Another example is U.S. Pat. No. 4,192,742 to Bernard et al., which appears to teach that the biodegradation of wastewater can be promoted by treating the wastewater within a treatment chamber maintained at a pressure above atmospheric pressure to achieve super oxygenation of the wastewater.
Methods and equipment for enriching a liquid with a gas are also known. For example, U.S. Pat. No. 3,957,585 to Malick appears to disclose that atomized liquid can be introduced into a reaction zone to effect intimate contact of the atomized liquid with a gas phase. A particular type of atomizing spray head for this purpose is disclosed in U.S. patent application Ser. No. 13/602,793 to Eppink et al., filed Sep. 4, 2012, whose contents are fully incorporated herein by reference (“Eppink”). As explained in Eppink et al., such spray heads are adapted to introduce an atomized fluid (for example, potable water or sewage water) into a chamber containing oxygen at a high pressure, with the result that the fluid becomes saturated with oxygen. The oxygen-saturated fluid can then be introduced into a stream of wastewater with the result that the wastewater contains sufficiently high levels of oxygen to promote the activity of aerobic microorganisms capable of biodegrading waste in the wastewater.
U.S. Pat. Nos. 7,008,535 and 7,294,278, each to Spears et al., appear to disclose that a gas-supersaturated fluid can be introduced into a wastewater so that the gas-supersaturated liquid is introduced in a substantially bubble-free manner. For this purpose, Spears et al. discloses the use of one or more fluid exit nozzles containing capillaries through which the gas-supersaturated liquid can be injected into the wastewater. U.S. Pat. No. 7,294,278 to Spears et al. discloses capillaries having diameters of about 150 to about 450 micrometers in nozzles having a plate-like construction, and capillary diameters of about 0.005 inch (about 125 micrometers) in nozzles having a more conventional spray head-type configuration. A drawback of the capillaries is that they may be prone to becoming plugged by solids and reaction products that may be entrained within the gas-supersaturated fluid.
Methods and apparatuses are described for enriching a first liquid with a gas and introducing the gas-enriched first liquid into a second liquid. In an embodiment, the apparatus comprises a vessel containing the gas at an elevated pressure, a liquid fluid inlet into the vessel such that the first liquid enters the vessel and becomes enriched with the gas, a variable internal valve defining an opening through which the gas-enriched first liquid flows after exiting the vessel, the internal valve opening adapted to generate bubbles of the gas within the gas-enriched first liquid as the gas-enriched first liquid flows therethrough, and a tube through which the gas-enriched first liquid flows into the second liquid, the tube comprising an inlet section comprising an inlet, a coiled section fluidically coupled to the inlet section, an outlet section fluidically coupled to the coiled section, and an outlet fluidically coupled to the outlet section, the tube adapted to maintain the bubbles of the oxygen-containing gas generated within the gas-enriched first liquid by the valve.
Various embodiments of the present invention together with arrangement given illustrative purposes only will now be described, by way of example only, and with reference to the accompanying drawings in which:
In an implementation, the gas-enriched liquid contains the gas at sufficiently high levels to enable the subsequent generation of bubbles of the gas within the gas-enriched liquid. In an implementation, the apparatus 10 is adapted so that bubbles of a desired quantity and size are generated in a controlled manner within the gas-enriched liquid prior to the liquid being introduced into the second liquid (for example, wastewater).
With continued reference to
In an implementation, the gas-enriched liquid accumulates within the vessel 12 at a level within a prescribed range before being withdrawn from the vessel 12. The effect of maintaining the gas-enriched liquid at an appropriate level within the vessel 12 is to promote the ability of the atomized liquid to absorb and retain the enrichment gas. In an implementation, including the apparatus 10 of
In an implementation, the gas-enriched liquid is drawn from the vessel 12 through an analog valve 18 that has an opening (not shown) that can be selectively sized (i.e., provide a variable internal valve opening) between a completely closed state up to and including a maximum size for the opening. In an implementation, the valve 18 is operated so that its valve opening causes bubbles to be generated in the gas-enriched liquid as it is drawn from the vessel 12. As a non-limiting example, if oxygen is used as the enrichment gas, the gas-enriched liquid is water supersaturated with oxygen, and liquid flow through the valve 18 is at a rate of substantially at or between about 15-20 gallons/minute, the valve 18 can be partially opened to generate an effective volume fraction of bubbles in a size range of substantially at or between about 100 to about 200 micrometers in diameter. In an implementation, to optimize control of the volume fraction and size of the bubbles, the valve 18 is controlled with an electronic controller (not shown), which can use feedback from appropriate sensors (not shown) to control the volume fraction and size of the bubbles.
In an implementation, one or more zone valves 20 are provided downstream from the valve 18. After exiting the valve 18, the gas-enriched liquid containing the entrained bubbles can be delivered to various applications via the one or more of zone valves 20. In the example in which the enrichment gas is oxygen and the intended use of the gas-enriched liquid is to biodegrade waste in wastewater and create dense separation for decanting, the one or more zone valves 20 are used to route the gas-enriched liquid for introduction into one or more bodies or streams of wastewater (not shown) to promote the activity of aerobic microorganisms. To maintain the volume fraction and size of bubbles generated with the analog valve 18, the gas-enriched liquid and its entrained bubbles are introduced into the wastewater through a tube 22 of a type represented in
In an implementation, the length and internal diameter of the tube 22 and the diameter and number of coils 34 within the coil section 28 are preferably selected so that flow of the gas-enriched liquid through the tube 22 is laminar which, in combination with surface friction within the coil section 28, is believed to maintain the entrainment of the bubbles in the gas-enriched liquid. For this purpose, suitable lengths and diameters for the tube 22, suitable numbers of coils 34, and suitable diameters for the coil section 28 will depend in part on the pressure and flow velocity of the gas-enriched liquid through the tube 22 and the saturation level of the gas in the liquid. In practice, suitable results have been obtained with an exemplary tube 22 having a total length of substantially at or between about 24 to about 48 inches and an internal diameter of larger than substantially at or between about 0.05 and 0.15 inches (e.g., at or about 0.10 inches), when used in combination with a coil section 28 having three coils 34 and a generally constant coil diameter of substantially at or between about 1.5 to about 2 inches.
While the disclosure hereof has described a method and product in n terms of a specific embodiment, it is apparent that other forms could be adopted by one skilled in the art. For example, the apparatus 10 and its components could differ in appearance and construction from the embodiment shown in the Figures, the functions of each component of the apparatus 10 could be performed by components of different construction but capable of a similar (though not necessarily equivalent) function, and various processes and materials could be employed to manufacture the apparatus 10 and its components. Accordingly, it should be understood that the invention is not limited to the specific embodiment illustrated in the Figures. It should also be understood that the phraseology and terminology employed above are for the purpose of disclosing the illustrated embodiment, and do not necessarily serve as limitations to the scope of the invention. Finally, while the appended claims recite certain aspects believed to be associated with the invention, they do not necessarily serve as limitations to the scope of the invention.
| Number | Date | Country | |
|---|---|---|---|
| 61558260 | Nov 2011 | US |
