US4337068A
Expired / Lapsed
US
⏱️ 0.0 years remaining
Methods for removing entrained solids from gases
Assignee: Texaco Inc
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Filing: 1980-10-20
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Granted: 1982-06-29
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Expires: 2000-10-20
Abstract
Abstract A method for the removal of entrained solids from gases in a cyclone separator having a dipleg attached to the bottom thereof comprises the basic steps of, (1) injecting the gases with the entrained solids in an inlet (54) of cyclone separator in the range of substantially 52 feet per second (16 m/s) to 80 feet per second (24 m/s), (2) spinning the injected gases with the entrained solids around and down the cyclone separator to the inlet (70) of the dipleg (34) by a vertical distance (L) below the gas outlet (74) proportional to the diameter (D) of the top of the separator by an amount of L/D=4.49-1.09 (O/I) or about 4, and (3) ejecting the solids-free-gases through a gas outlet (74) in the range of substantially 52 feet per second (16 m/s) to 200 feet per second (61 m/s) having an area (O) in proportion to the area (I) of the separator inlet (54) in the range of substantially O/I=0.4/1 to 1/1, for providing a maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Inventors
- 👤 John P. MacLean
- 👤 J. Edward Cantwell
- 👤 John D. Brown
- 👤 Harold D. Hoy
Bibliographic Details
Application Number
—
Jurisdiction
US
Data Source
google_patents
Last Synchronized
2026-11-08 19:20
CPC Classifications
B; B04; B04C; B04C5/00; B04C5/24; B04C5/28; B01; B01D; B01D45/00; B01D45/12
Claims Analysis
Total Claims: 8
Claim 1
Independent Claim
229 words
A method for removal of entrained solids from gases in an upright cyclone separator (33, FIG. 2) comprising an upper cylindrical portion having a diameter D, and a lower conical portion, said upper cylindrical portion having an inlet (54) with a cross-sectional area (I), and an outlet (74) with a cross-sectional area (O), a dust bowl (33) connected to said cyclone lower conical portion having a barrel section (64) and a conical section (66) connected thereto at a junction, said cyclone lower conical portion having an apex passing substantially to or below said junction, and a dipleg (34) attached to the conical section of the dust bowl comprising the steps, (a) injecting the gases with entrained solids in the inlet (54) of the cyclone separator in the range of substantially 52 feet per second to 80 feet per second, (b) spinning the injected gases with the entrained solids around and down the cyclone separator to a vertical distance (L) comprising the distance between the gas outlet (74) and the inlet (70) of the dipleg, whereby L/D=about 4, and (c) ejecting the solids-free-gases through the gas outlet (74) in the range of substantially 52 feet per second to 200 feet per second, whereby the range of O/I=0.4/1 to 1/1 for providing a maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Claim 2
Independent Claim
229 words
A method for removal of entrained solids from gases in an upright cyclone separator (33, FIG. 2) comprising an upper cylindrical portion having a diameter D, and a lower conical portion, said upper cylindrical portion having an inlet (54) with a cross-sectional area (I), and an outlet (74) with a cross-sectional area (O), a dust bowl (33) connected to said cyclone lower conical portion having a barrel section (64) and a conical section (66) connected thereto at a junction, said cyclone lower conical portion having an apex passing substantially to or below said junction, and a dipleg (34) attached to the conical section of the dust bowl comprising the steps, (a) injecting the gases with entrained solids in the inlet (54) of the cyclone separator in the range of substantially 52 feet per second to 80 feet per second, (b) spinning the injected gases with the entrained solids around and down the cyclone separator to a vertical distance (L) comprising the distance between the gas outlet (74) and the inlet (70) of the dipleg, whereby L/D=about 4, and (c) ejecting the solids-free-gases through the gas outlet (74) in the range of substantially 52 feet per second to 200 feet per second, whereby the range of O/I=0.4/1 to 1/1 for providing a maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Claim 3
Dependent Claim
37 words
A method as recited in claim 1 wherein the first method step comprises further, (a) injecting the gases with the entrained solids into the cyclone separator inlet (54) at a velocity of substantially 80 feet per second.
Claim 4
Dependent Claim
65 words
A method as recited in claim 1 wherein the third method step comprises further, (a) ejecting the solids-free-gases into a gas outlet (74) in the upper portion of the separator housing shaped for receiving the solids-free-gas at a velocity of substantially 178 feet per second for providing maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Claim 5
Dependent Claim
62 words
A method as recited in claim 1 wherein the third method step comprises further, (a) ejecting the solids-free-gases through the gas outlet having an area (O) in proportion to the separator inlet area (I) in the range of substantially O/I=0.45/1 to 0.6/1 for providing maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Claim 6
Dependent Claim
67 words
A method as recited in claim 1 wherein the second method step comprises further, (a) spinning the injected gases with the entrained solids around and down the cyclone separator to the dipleg inlet (70) having a diameter substantially in the range of 0.05 D to 0.2 D for providing maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Claim 7
Dependent Claim
74 words
A method as recited in claim 1 wherein the second method step comprises further, (a) spinning the injected gases with the entrained solids around and down the cyclone separator to the dipleg inlet by a distance (L) below the gas outlet proportional to the separator maximum diameter (D) by an amount of substantially L/D=4 for providing maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
Claim 8
Dependent Claim
80 words
A method as recited in claim 1 wherein the second method step comprises further, (a) spinning the injected gases with the entrained solids around and down the cyclone separator to the dipleg inlet by a vertical distance (L) below the gas outlet proportional to the separator maximum diameter (D) of the separator top by an amount of substantially L/D=4.49-1.09 (O/I) for providing maximum efficiency with minimum erosion of both the cyclone separator internal wall surface and of the separated solids.
References Cited (Backward Citations)
USPTO Annuity & Maintenance Windows
| Annuity Stage | Window Opens | Payment Deadline | Surcharge Period Until | Estimated Fee | Status |
|---|---|---|---|---|---|
| 3.5 Years (Year 4) | 1985-06-28 | 1985-12-28 | 1986-06-29 | $2000.00 | Window Closed / Lapsed |
| 7.5 Years (Year 8) | 1989-06-28 | 1989-12-28 | 1990-06-29 | $3760.00 | Window Closed / Lapsed |
| 11.5 Years (Year 12) | 1993-06-28 | 1993-12-28 | 1994-06-29 | $7700.00 | Window Closed / Lapsed |