US4008059A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Centrifugal separator
Assignee: United States Department of the Army
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Filing: 1975-05-06
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Granted: 1977-02-15
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Expires: 1995-05-06
Abstract
Abstract A miniature centrifugal separator for use in an engine air cleaner. Two cn air take-off tubes are coaxially aligned in the main flow tube for successively removing selected fractions of the outer annular portion of the swirling gas stream. The clean air tubes are spaced pre-selected distances downstream from the swirl means such that entrained dust particles are enabled to complete approximately one swirl revolution prior to encountering each take-off tube. The invention seeks to accomplish a relatively high collection efficiency with a relatively short flow tube.
Inventors
- 👤 Donald R. Monson
- 👤 Thomas E. Rosendahl
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-10-28 01:51
CPC Classifications
B; B04; B04C; B04C3/00; B04C3/06; B01; B01D; B01D45/00; B01D45/12; B01D45/14; B01D45/16; B04C2003/006; B04C5/00; B04C5/12; B04C5/13; B04C2005/133
Claims Analysis
Total Claims: 3
Claim 1
Independent Claim
428 words
A miniature centrifugal separator comprising a cylindrical imperforate main flow tube having an upstream end for receiving a stream of dust-laden gas, and a downstream end for discharging concentrated dust; swirl means within the upstream end of the main flow tube for imparting centrifugal force to the dust particles in the dust-laden gas; said swirl means comprising a hub coaxially located in the main flow tube, and helical vanes extending outwardly from said hub at acute angles to the tube axis; the hub diameter being approximately 40% of the main flow tube diameter, and the swirl vanes being angled to the flow tube axis at approximately 65°; said hub having a frusto-conical tail extending downstream beyond the trailing edges of the vanes for a distance that is slightly less than one third the diameter of the main flow tube; a first separator tube coaxially located within the main flow tube downstream from the swirl means; said first separator tube comprising a leading cylindrical section and a trailing frusto-conical section flaring outwardly from its point of connection with the cylindrical section; the cylindrical section of the first separator tube having a diameter that is approximately 1.4 times the hub diameter; the cylindrical section of the first separator tube defining an annular flow separator edge (53) that is spaced downstream from the swirl vanes by a distance that is approximately the same as the diameter of the main flow tube; wall means (50) joining the first separator tube to the main flow tube; said wall means having at least one opening therethrough defining a first dust scavenger port; a second separator tube coaxial with the main flow tube and downstream from the first separator tube; said second separator tube comprising a leading cylindrical section and a trailing frusto-conical section flaring outwardly from its point of connection with the cylindrical section; the cylindrical section of the second separator tube having approximately the same diameter as the cylindrical section of the first separator tube; the cylindrical section of the second flow separator tube defining an annular flow separator edge (54) that cooperates with the inner surface of the frusto-conical section of the first separator tube to define a second dust scavenger port; the second separator tube being telescoped into the first separator tube so that the first scavenger port and second scavenger port having a size ratio of approximately 0.2; and means for producing a scavenger flow force on the first and second ports, whereby dust particles are drawn through the ports while relatively clean gas flows through the second separator tube.
Claim 2
Dependent Claim
428 words
A miniature centrifugal separator comprising a cylindrical imperforate main flow tube having an upstream end for receiving a stream of dust-laden gas, and a downstream end for discharging concentrated dust; swirl means within the upstream end of the main flow tube for imparting centrifugal force to the dust particles in the dust-laden gas; said swirl means comprising a hub coaxially located in the main flow tube, and helical vanes extending outwardly from said hub at acute angles to the tube axis; the hub diameter being approximately 40% of the main flow tube diameter, and the swirl vanes being angled to the flow tube axis at approximately 65°; said hub having a frusto-conical tail extending downstream beyond the trailing edges of the vanes for a distance that is slightly less than one third the diameter of the main flow tube; a first separator tube coaxially located within the main flow tube downstream from the swirl means; said first separator tube comprising a leading cylindrical section and a trailing frusto-conical section flaring outwardly from its point of connection with the cylindrical section; the cylindrical section of the first separator tube having a diameter that is approximately 1.4 times the hub diameter; the cylindrical section of the first separator tube defining an annular flow separator edge (53) that is spaced downstream from the swirl vanes by a distance that is approximately the same as the diameter of the main flow tube; wall means (50) joining the first separator tube to the main flow tube; said wall means having at least one opening therethrough defining a first dust scavenger port; a second separator tube coaxial with the main flow tube and downstream from the first separator tube; said second separator tube comprising a leading cylindrical section and a trailing frusto-conical section flaring outwardly from its point of connection with the cylindrical section; the cylindrical section of the second separator tube having approximately the same diameter as the cylindrical section of the first separator tube; the cylindrical section of the second flow separator tube defining an annular flow separator edge (54) that cooperates with the inner surface of the frusto-conical section of the first separator tube to define a second dust scavenger port; the second separator tube being telescoped into the first separator tube so that the first scavenger port and second scavenger port having a size ratio of approximately 0.2; and means for producing a scavenger flow force on the first and second ports, whereby dust particles are drawn through the ports while relatively clean gas flows through the second separator tube.
Claim 3
Dependent Claim
17 words
The separator of claim 1 wherein the main flow tube has a diameter of approximately 1.5 inches.
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USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1980-02-15 | 1980-08-16 | 1981-02-15 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1984-02-15 | 1984-08-16 | 1985-02-15 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1988-02-15 | 1988-08-16 | 1989-02-15 | $7700.00 | Window Closed / Lapsed |