Impeller, a diffuser and an arrangement using such impeller and diffuser in a flotation tank
US-2022347635-A1 · Nov 3, 2022 · US
US9656218B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9656218-B2 |
| Application number | US-201615274507-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 23, 2016 |
| Priority date | Dec 1, 2011 |
| Publication date | May 23, 2017 |
| Grant date | May 23, 2017 |
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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.
Opening claim text (preview).
We claim: 1. An apparatus for injecting a gas into a liquid comprising: a draft tube adapted to be submerged in a liquid and having at least one inlet opening situated at one end of the draft tube and a discharge opening located at the other end thereof; a helical impeller located within the draft tube; a motor connected to the draft tube and a shaft projecting into the draft tube from the one end of the draft tube and connected to the helical impeller to rotate the helical impeller and thereby to create a liquid flow by drawing the liquid into the draft tube from the at least one inlet opening and discharging the liquid flow from a discharge opening; means for injecting gas bubbles of the gas into the liquid flow, within the draft tube, in at least one location situated above or below or alongside the helical impeller 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; wherein the means for injecting gas bubbles has at least one injector opening and comprises an inner porous section of a sparger located within the draft tube and having a ring-like configuration, and means for supplying the gas to the means for injecting gas bubbles at a predetermined flow rate, the at least one injector opening sized to produce the gas bubbles within the liquid with the uniform diameter at the predetermined flow rate; and the means for injecting gas bubbles configured to inject the gas bubbles with at least a substantially 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 impeller configured and the motor able to rotate the impeller at a sufficient speed such that the liquid drawn into the draft tube has a minimum 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 drawn into the draft tube. 2. The apparatus of claim 1 , wherein: the sparger having an inlet for the gas penetrating a sidewall of the draft tube; the ring-like element having an outer solid section and the inner porous section connected to the outer solid section and formed by a metallic, sintered metal or polymeric ultrafine bubble surface layer to provide the plurality of injector openings; and the plurality of injector openings are sized to produce the gas bubbles within the liquid, at the predetermined flow rate, with the uniform diameter within a range of between about 10 microns and about 500 microns.
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