Apparatus and process for the aeration of water

• US 5,525,242 A
• Filed: 10/19/1994
• Issued: 06/11/1996
• Est. Priority Date: 10/19/1994
• Status: Expired due to Fees

• Current Assignee: Robert C.J. Kerecz
• Original Assignee: Robert C.J. Kerecz
• Inventors: Kerecz, Robert C. J.
• Primary Examiner(s): McCarthy, Neil
• Application Number:
  US08/325,062
• Time in Patent Office: 601 Days
• Field of Search: 261/DIG. 75, 261/76, 261/79.2, 366/339, 48/189.5, 210/749, 210/758, 210/220
• US Class Current: 210/758
• CPC Class Codes: B01F 23/23 by introducing gases into liquid media, e.g. for producing aerated liquids
• CPC Class Codes: B01F 23/237612 Oxygen
• CPC Class Codes: B01F 25/3121 with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
• CPC Class Codes: B01F 25/3131 with additional mixing means other than injector mixers, e.g. screens, baffles or rotating elements
• CPC Class Codes: B01F 25/431971 Mounted on the wall
• CPC Class Codes: C02F 1/20 by degassing, i.e. liberation of dissolved gases degasification of liquids in general B01D19/00; arrangement of degassing apparatus in boiler feed supply F22D
• CPC Class Codes: C02F 1/72 by oxidation C02F1/4672 takes precedence
• CPC Class Codes: C02F 1/76 with halogens or compounds of halogens C02F1/4674 takes precedence
• CPC Class Codes: C02F 3/1294 "Venturi" aeration means
• CPC Class Codes: Y02W 10/10 Biological treatment of water, waste water, or sewage
• CPC Class Codes: Y10S 261/75 Flowing liquid aspirates gas

Abstract

This invention relates to improved apparatus and to an improved process for the treatment of liquids, and particularly water for domestic consumption. The improved process for treating water to remove hydrogen sulfide and soluble mineral compounds while saturating the water with oxygen comprises feeding the liquid through a nozzle and contacting the liquid with an oxygen containing gas, e.g., air comprises utilizing a venturi nozzle having a nozzle extension that retains the water and air in the form of a confined stream as it is discharged therefrom. The nozzle extension preferably is equipped with restrictor means for directing water from the interior walls of the nozzle chamber toward the center and the nozzle extension directed so that the stream of water containing air is directly discharged from the nozzle extension into the water retained within the tank.

Claims

1. In a process for the aeration of domestic water contaminated with trace levels of dissolved gas and/or an oxidizable mineral salt wherein said contaminated water is passed through a venturi nozzle retained within a vessel, contacted with an oxygen containing gas under conditions for oxidizing and/or removing said gas and/or oxidizing said mineral salt, discharged from the venturi nozzle and then the resultant aerated water collected within the vessel, the improvement for improving the taste and removing objectionable odor from the water which comprises:

utilizing a venturi nozzle having a nozzle chamber in which water and oxygen containing gas are contacted, the contaminated water passing through the venturi nozzle and discharging into the nozzle chamber, said venturi nozzle having a nozzle extension in communication with the nozzle chamber and venturi nozzle which retains the water mixed with oxygen containing gas in the form of a confined steam, discharging the confined stream therefrom and venting gases from the vessel, said nozzle extension having a restrictor therein, said restrictor located within said nozzle extension, said restrictor comprising an annular element of constant inner diameter that is smaller than a constant inner diameter of the nozzle extension upstream from said restrictor, and wherein said nozzle extension resumes downstream from said restrictor at the same constant inner diameter of said nozzle extension upstream from said restrictor.

2. The process of claim 1 wherein the venturi nozzle comprises a tee having a water inlet that discharges into a nozzle chamber and an inlet for oxidizing gas which discharges into said nozzle chamber at an angle to said water inlet.

3. The process of claim 1 wherein the confined stream discharged from the nozzle extension is directed toward the water retained in the lower part of the vessel.

4. The process of claim 3 wherein the restrictor reduces the cross sectional area of the nozzle extension by about 10 to 30% and said restrictor is located proximate a discharge end of the nozzle extension.

5. The process of claim 4 wherein the tee is substantially cylindrical with nozzle extension having a spiral groove extending along its length.

6. The process of claim 4 wherein the venturi nozzle has a tip diameter of from about 3/16 to 1/2 inch.

7. The process of claim 6 wherein the diameter of said inlet for oxidizing gas is from about 3/4 to 11/2 inches and the diameter of the nozzle extension is from about 3/4 to 11/2 inches.

8. The process of claim 7 wherein the inlet for oxidizing gas is an air inlet and is approximately 90°

to said water inlet.

9. The process of claim 8 wherein a halogen source is added to said aerated water.