Gas injection method and apparatus

Patent metadata

Field	Value
Publication number	US-9486750-B2
Application number	US-201213587128-A
Country	US
Kind code	B2
Filing date	Aug 16, 2012
Priority date	Dec 1, 2011
Publication date	Nov 8, 2016
Grant date	Nov 8, 2016

Abstract

A method and apparatus for injecting a gas into a liquid in which a rotating helical impeller within a draft tube submerged in the liquid creates a liquid flow within the draft tube. Gas bubbles are injected into the draft tube either above or below or alongside the helical impeller or in all three locations. The liquid is drawn into the draft tube with a superficial velocity greater than a substantially uniform terminal ascent velocity of the gas bubbles to allow entrainment of undissolved gas bubbles in the bulk liquid into the liquid being drawn into the draft tube. The gas bubbles are injected with a uniform diameter of between about 10.0 microns and about 1.0 millimeters. The small bubble size enhances the dissolution of the gas into the liquid and also allow the entrainment of the gas into the liquid being drawn into the draft tube.

First claim

We claim:

1. A method of injecting a gas into a liquid comprising:
rotating a helical impeller within a draft tube located in the liquid to create a liquid flow by drawing the liquid into the draft tube from at least one inlet opening situated at one end of the draft tube and discharging the liquid flow from a discharge opening of the draft tube located at the other end thereof;
injecting gas bubbles of the gas into the liquid flow in the draft tube, in at least one location situated above or below or alongside the helical impeller wherein the bubbles are injected from a plurality of spargers in the draft tube, or from an inner porous section of a sparger located within the draft tube and having a ring-like configuration, or from a plurality of nozzles located inside the draft tube, such that a portion of the gas bubbles dissolve in the liquid flow inside of the draft tube and a remaining portion of the gas bubbles are discharged from the discharge opening and are carried into the liquid, within the liquid flow, where part of the remaining portion of the gas bubbles dissolve in the liquid and a further part of the remaining portion of the gas bubbles is entrained into the liquid drawn into the draft tube through the at least one inlet opening;
the gas bubbles injected into the liquid flow with a uniform diameter of between about 10.0 microns and about 1.0 millimeter to enhance the surface area of the gas bubbles and therefore, a dissolution rate of the gas within the liquid and to impart a buoyancy to the further part of the remaining portion of the gas bubbles that will result in at least a substantially uniform terminal ascent velocity thereof; and
the liquid drawn into the draft tube with a superficial velocity greater than the substantially uniform terminal ascent velocity of the gas bubbles to enable the entrainment of the further part of the remaining portion of the gas bubbles into the liquid.

2. The method of claim 1 , wherein:
the gas bubbles are injected from a plurality of spargers located inside the draft tube at radially spaced locations thereof; and
the uniform diameter is between about 10.0 microns and about 500.0 microns.

3. The method of claim 2 , wherein:
the gas bubbles are injected from an inner porous section of a sparger located within the draft tube and having a ring-like configuration; and
the uniform diameter is between about 10.0 microns and about 500.0 microns.

4. The method of claim 1 , wherein:
the uniform diameter is between about 500.0 microns and about 1.0 millimeter;
the gas is supplied to a plurality of nozzles located inside the draft tube at radially spaced locations thereof; and
the gas bubbles of the gas are injected from the plurality of nozzles.

5. The method of claim 1 , wherein, where the gas is oxygen, an ozone containing mixture or carbon dioxide.

Assignees

• Fabiyi Malcolm E
• Connery Karen
• Wattanapanom Mark Witawat
• Novak Richard A
• Praxair Technology Inc

Inventors

• Fabiyi Malcolm E
• Connery Karen
• Wattanapanom Mark Witawat
• Novak Richard A

Classifications

• Y02W10/10

  Biological treatment of water, waste water, or sewage · CPC title

• B01F7/00733

  Operations & Transport · mapped topic

• B01F2215/0431

  Numerical size values, e.g. diameter of a hole or conduit, area, volume, length, width, or ratios thereof · CPC title

• Y02W10/15

  Cross-Sectional Technologies · mapped topic

• B01F3/04609

  Operations & Transport · mapped topic