Method for delivery of gas-enriched fluids

Specialized metallurgical processes – compositions for use therei – Processes – Producing or treating free metal

Reexamination Certificate

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Details

C075S559000, C048S1970FM, C062S066000, C134S042000, C162S001000, C210S758000, C435S818000

Reexamination Certificate

active

06241802

ABSTRACT:

FIELD OF THE INVENTION
The present invention generally relates to a system and method for delivering gas-supersaturated fluids. More specifically, the present invention relates to a system and method for delivering gas-supersaturated fluids to a gas-depleted site without the premature formation of bubbles.
BACKGROUND OF THE INVENTION
In many industrial and clinical environments, it is desirable to deliver a gas-enriched fluid to a site of interest, and/or increase the gas concentration of a fluid without a significant increase in the fluid volume.
For example, a fire may be extinguished by delivering an inflammable or an inert gas, such as carbon dioxide or nitrogen, rapidly to the fire via a fluid transporting medium. Environmental problems presented by toxic site cleanups may be ameliorated by delivering a high concentration of a neutralizing or cleansing gaseous agent to the toxic site. The oxygenation level of ponds used in fish farms, and the oxygenation level of waste streams (prior to their release into the environment) may also be increased by delivery of oxygen-enriched fluids to the ponds or streams.
One method of obtaining an increase in the gas concentration level without significant increase in fluid volume is by directly pumping a desired gas into a fluid site of interest. However, such direct pumping is not always efficient and may thereby result in an insufficient increase in gas concentration. Where a noxious gas is used, direct pumping also poses waste engineering problems and/or health hazard due to the presence of any unabsorbed noxious gas.
Another method of obtaining an increase in the gas concentration level without significant increase in fluid volume is by infusing a gas-enriched fluid, such as a gas-supersaturated fluid, into the site of interest. To create a gas-supersaturated fluid, high pressure compression of a gas-liquid mixture can be performed, for example, with the use of a high pressure gas exchanger. Prior art systems for producing gas-supersaturated fluids typically require the use of a high pressure vessel to provide dwell time for dissolving gas nuclei in the fluid outputted from the high pressure gas exchanger. Two such prior art systems are U.S. Pat. No. 5,407,426, “Method and Apparatus For Delivering Oxygen Into Blood” to Spears and U.S. Pat. No. 5,569,180, “Method For Delivering A Gas-Supersaturated Fluid To A Gas-Depleted Site And Use Thereof” to Spears.
In addition, gas nuclei may be present in the fluid prior to supersaturating the fluid with gas. For example, gas nuclei may be dust particles suspended in the fluid or crevices in the container wall in which gas is trapped or absorbed. The presence of gas nuclei facilitates cavitation inception (or, bubble formation), resulting in release of gas from the liquid and thereby decreasing the gas concentration of the fluid.
Furthermore, some prior art systems also require a high pressure (>70 bar) fluid pump to deliver the gas-supersaturated fluid. Particularly in industrial applications (where it may be necessary to deliver large volumes of a gas-enriched fluid to a site of interest), such prior art systems may prove impractical because of the overall complexity, cost, and time associated with operating them.
Another problem associated some of the prior art devices in infusing gas-supersaturated fluid from a high pressure vessel into a site of interest is that cavitation inception at or near the exit ports often results. Cavitation inception may occur because ejection of the fluid into an atmospheric environment results in a decrease in the hydrostatic pressure of the fluid below the gas partial pressure. Disturbances at or near the exit ports may further facilitate cavitation inception. When cavitation takes place, gas is released from the fluid, decreasing its gas concentration. Furthermore, the presence of bubbles in the fluid generates turbulence and impedes the flow of the fluid beyond the exit ports.
Accordingly, there remains a need in the art for a simple, efficient and cost-effective system and method for producing and delivering gas-supersaturated fluid to a site of interest which does not require a high pressure vessel to provide dwell time and which does not require a high pressure fluid pump for delivery of the gas-supersaturated fluid. There remains a further need for a system and method for producing and delivering gas-supersaturated fluid to a site of interest without cavitation inception in the fluid during ejection, particularly at or near the exit ports.
SUMMARY OF THE INVENTION
Preferred embodiments of the present invention meet the foregoing needs by providing a system and method for delivering gas-enriched fluid to a site of interest. Such a system includes a fluid reservoir, a fluid pump, a gas source, a high pressure gas exchanger, and one or more arrays of capillary channels for delivery of gas-supersaturated fluid. Differential pressure gauges and other suitable controls may be provided to maintain a near constant hydrostatic pressure of the fluid throughout the delivery system that is approximately 1% to 20% higher than the gas pressure within the housing of the high pressure gas exchanger. The delivery system may also include a fluid filter for filtering the fluid before it enters the fluid reservoir.
The system and method of the present invention requires relatively low hydrostatic pressures and eliminates the need for a high pressure vessel for providing a dwell time for dissolving gas nuclei in the fluid. The system and method of the present invention also eliminates the need for a high pressure fluid pump for high output delivery of the gas-supersaturated fluid. Furthermore, the system and method of the present invention reduces or eliminates gas nuclei on the inner surface of the exit ports through which the gas-supersaturated fluid exits, in part by providing exit ports with a relatively small diameter.


REFERENCES:
patent: 4071443 (1978-01-01), Gorski et al.
patent: 4442843 (1984-04-01), Rasor et al.
patent: 4657756 (1987-04-01), Rasor et al.
patent: 4664680 (1987-05-01), Weber
patent: 4681119 (1987-07-01), Rasor et al.
patent: 4973558 (1990-11-01), Wilson et al.
patent: 5407426 (1995-04-01), Spears
patent: 5569180 (1996-10-01), Spears
patent: 5599296 (1997-02-01), Spears
patent: 5670094 (1997-09-01), Sasaki et al.
patent: 5693017 (1997-12-01), Spears et al.
patent: 5730935 (1998-03-01), Spears
patent: 5735934 (1998-04-01), Spears
patent: 4105726C1 (1992-09-01), None
patent: 2 320 908 (1977-03-01), None

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