Apparatuses and methods for gas-solid separations using cyclones
US-8945283-B1 · Feb 3, 2015 · US
US10427172B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10427172-B2 |
| Application number | US-201214365316-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 17, 2012 |
| Priority date | Dec 16, 2011 |
| Publication date | Oct 1, 2019 |
| Grant date | Oct 1, 2019 |
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Separation device comprising a swirler of a sheet material comprising a plurality of vanes (4) with a flow entrance side edge (6) defining an entrance angle (α) and a flow exit side edge (8) defining an exit angle (β). The flow entrance side edge and flow exit side edge extend from a center section (3) to a peripheral edge (9), which extends between end points of the flow entrance edge and the flow exit edge. The entrance angle is larger than the exit angle.
Opening claim text (preview).
That which is claimed is: 1. A separation device, comprising: a swirler cut from a sheet metal blank and comprising at least two stacked sheet metal subswirlers, wherein the at least two stacked sheet metal subswirlers comprises a planar peripheral ring defined by cutting the sheet metal blank, wherein each of the at least two stacked sheet metal subswirlers comprise 2-4 vanes with a flow entrance side edges defining an entrance angle (α) that is at least 70 degrees and flow exit side edges defining an exit angle (β) that is within a range of 20-60 degrees, wherein the flow entrance side edges and flow exit side edges extend from a center section of the swirler to a peripheral edge of the swirler, and wherein the peripheral edge is circular in plan view and extends between end points of the flow entrance side edges and the flow exit side edges, wherein the entrance angle is larger than the exit angle; wherein the flow entrance side edges are truncated to be substantially perpendicular to the flow direction of fluid through the swirler; and wherein the vanes bridge the center section and the planar peripheral ring. 2. A separation device according to claim 1 wherein the entrance angle (α) is at least 80 degrees. 3. A separation device according to claim 1 wherein the exit angle (β) is within a range of 30-60 degrees. 4. A separation device according to claim 1 wherein the subswirlers are positioned relative to each other such that the vanes are at equal distance of each other. 5. A swirler for use in separation devices, wherein the swirler comprises: at least two subswirlers positioned in a stacked relationship, wherein each subswirler comprises a planar sheet metal black, wherein each subswirler has a top surface and bottom surface and cut to define 2-4 vanes with each vane having a peripheral edge that is circular in plan view, wherein each subswirler has a flow entrance section comprising flow entrance edges and a flow exit section having flow exit edges, and cut to define a planar peripheral ring in the planar sheet metal blank; wherein both the flow entrance edges and the flow exit edges extend radially from a center section of the swirler to the planar peripheral ring; wherein each of the vanes are bent to provide a bent vane providing an entrance angle (α) below the bottom surface and between the flow entrance section and the plane of the planar sheet metal blank, wherein the entrance angle (α) is at least 70 degrees, and providing an exit angle (β) above the top surface between the flow exit section and the plane of the planar sheet metal blank, wherein the exit angle (β) is within a range of 20-60 degrees; wherein fluid flow direction through the swirler is from the bottom surface to the top surface; wherein the entrance angle (α) is larger than the exit angle (β); wherein the flow entrance edges are truncated to be substantially perpendicular to the fluid flow direction through the swirler; and wherein each of the vanes are bridged from the center section to the planar peripheral ring. 6. A swirler according to claim 5 , wherein the entrance angle (α) is at least 80 degrees. 7. A swirler according to claim 6 , wherein the exit angle (β) is within a range of 30-60 degrees. 8. A swirler according to claim 5 , wherein the at least two subswirlers are positioned relative to each other such that the vanes are at equal distance of each other.
Inorganic materials other than metals or composite materials · CPC title
generated by the winding course of the gas stream {, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes} · CPC title
Cyclonic chamber constructions · CPC title
Apparatus in which the axial direction of the vortex {flow following a screw-thread type line} remains unchanged {; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct (combined with other devices B04C9/00)} · CPC title
Vane type or other rotary, e.g., fan · CPC title
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