Compact microfluidic structures for manipulating fluids
US-2016310945-A1 · Oct 27, 2016 · US
US9956532B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9956532-B2 |
| Application number | US-201414534263-A |
| Country | US |
| Kind code | B2 |
| Filing date | Nov 6, 2014 |
| Priority date | Nov 7, 2013 |
| Publication date | May 1, 2018 |
| Grant date | May 1, 2018 |
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An apparatus and method for generating a swirl is disclosed that is used to induce an axi-symmetric swirling flow to an incoming flow. The disclosed subject matter induces a uniform and axi-symmetric swirl, circumferentially around a discharge location, thus imparting a more accurate, repeatable, continuous, and controllable swirl and mixing condition of interest. Moreover, the disclosed subject matter performs the swirl injection at a lower pressure drop in comparison to a more traditional methods and devices.
Opening claim text (preview).
What is claimed is: 1. A method of creating an axially-symmetric swirling flow, comprising: passing a main flow lacking axially-symmetric swirling flow through a chamber having an upstream nozzle and a downstream nozzle; injecting a second flow into a plenum; passing the second flow from the plenum into a slot connecting at a first end with the plenum and connecting radially tangentially at a second end with the chamber; discharging the second flow through the slot and into the main flow, wherein the step of discharging the second flow into the main flow mixes the second flow with the main flow to impart a predefined swirling component to the main flow to generate an axially-symmetric uniform flow field; wherein a rotation of the axially-symmetric swirling flow is either a clockwise swirl or a counterclockwise swirl, and further comprising switching the rotation of the axially-symmetric swirling flow by re-orienting the chamber. 2. The method of claim 1 , further comprising injecting the second flow into the plenum in a direction perpendicular to the main flow. 3. The method of claim 1 , further comprising reducing a hydraulic diameter of the downstream nozzle. 4. The method of claim 1 , further comprising adding a first chemical reactant to the plenum. 5. The method of claim 4 , further comprising adding a second chemical reactant to the main flow. 6. The method of claim 1 , further comprising increasing a velocity of the axially-symmetric swirling flow by reducing a hydraulic diameter of a discharge gap. 7. The method of claim 6 , wherein reducing the hydraulic diameter of the discharge gap comprises: increasing a dimension of an inner spacer connected to an outer surface of the downstream nozzle, wherein the inner spacer includes an inner spacer depth; and increasing a dimension of an outer spacer connected to an inner surface of the downstream nozzle, wherein the outer spacer includes an outer spacer depth. 8. The method of claim 7 , further comprising computing the hydraulic diameter as a function of the inner spacer depth and outer spacer depth, and a Reynolds number. 9. The method of claim 1 , wherein the second end of the slot includes an adjustable converging discharge gap.
Numerical speed values · CPC title
Relationships between different variables defining features or parameters of the apparatus or process · CPC title
Operations & Transport · mapped topic
Operations & Transport · mapped topic
Numerical size values, e.g. diameter of a hole or conduit, area, volume, length, width, or ratios thereof · CPC title
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