Hypolimnion oxygenation

• US 3,956,124 A
• Filed: 11/25/1974
• Issued: 05/11/1976
• Est. Priority Date: 11/25/1974
• Status: Expired due to Term

• Current Assignee: Praxair Technology Incorporated (Linde Plc)
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Pietruszewski, John Joseph, Fast, Arlo Wade, Grunert, William Edward
• Primary Examiner(s): Hart, Charles N.
• Assistant Examiner(s): Castel, Benoit
• Application Number:
  US05/527,158
• Time in Patent Office: 533 Days
• Field of Search: 210/220, 210/221, 210/15, 210/170, 210/63, 261/36 R, 261/DIG. 75
• US Class Current: 210/600
• CPC Class Codes: A01K 63/042 Introducing gases into the water, e.g. aerators, air pumps
• CPC Class Codes: B01F 23/454 by injecting a mixture of liquid and gas
• CPC Class Codes: C02F 3/1294 "Venturi" aeration means
• CPC Class Codes: C02F 3/26 using pure oxygen or oxygen-rich gas
• CPC Class Codes: C02F 7/00 Aeration of stretches of water
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage

Abstract

The hypolimnion of thermally stratified water bodies is oxygenated by withdrawing water therefrom at rate of 10-200 percent of the hypolimnion volume per month, pressurizing the withdrawn water to superatmospheric pressure below 125 psig, injecting at least 80 percent oxygen gas at rate of 5-300 lbs. O₂ per million pounds withdrawn water but less than a rate to result in O₂ supersaturation at the remixing point, returning the mixture through conduit means and remixing same at rate to produce specified frictional head loss.

Claims

1. A process for oxygenation of the hypolimnion of thermally stratified water bodies comprising the steps of:

Withdrawing water from the hypolimnion at rate between 10 and 200 percent of the hypolimnion volume per month;

pressurizing the withdrawn water to superatmospheric pressure below 125 psig;

injecting at least 80 percent oxygen (by volume) gas in the withdrawn pressurized water at rate between 5 and 300 lbs. oxygen per million pounds withdrawn water but less than a rate resulting in oxygen supersaturation of the withdrawn water at the pressure in the hypolimnion at the point of remixing;

returning the oxygen gas - water mixture through conduit means to and remixing same with the hypolimnion at rate to produce frictional head loss of at least 4 psi per 100 feet length of said conduit means, and also at least 0.15 psi per pound of injected gas per one million pounds withdrawn water.

2. A process according to claim 1 wherein the oxygen gas - water mixture is returned to the hypolimnion at least 25 feet below the top of the hypolimnion, and the water withdrawal rate therefrom is at least 40 percent of the hypolimnion volume per month.

3. A process according to claim 1 wherein the oxygen gas - water mixture is returned to the hypolimnion at less than 15 feet below the top of the hypolimnion, and the water withdrawal rate therefrom is less than 30 percent of the hypolimnion volume per month.

4. A process according to claim 1 wherein the remixing head loss across the return conduit discharge end is less than 15 psi.

5. A process according to claim 1 wherein the oxygen gas is injected in the withdrawn pressurized water at rate between 20 and 100 lbs. oxygen per million pounds withdrawn water.

6. A process according to claim 1 wherein water is withdrawn from the hypolimnion at rate between 20 and 100 percent of the hypolimnion volume per month.

7. A process according to claim 1 wherein at least 90 percent oxygen (by volume) gas is injected in the withdrawn pressurized water.

8. A process according to claim 1 wherein water is withdrawn from the hypolimnion at rate between 20 and 100 percent of the hypolimnion volume per month and at least 90 percent oxygen (by volume) gas is injected in the withdrawn pressurized water at rate between 20 and 100 lbs. oxygen per million pounds withdrawn water.