Modified volute pump casing

• US 4,213,742 A
• Filed: 10/17/1977
• Issued: 07/22/1980
• Est. Priority Date: 10/17/1977
• Status: Expired due to Term

• Current Assignee: Union Carbide Corporation (Dow, Inc.)
• Original Assignee: Union Carbide Corporation (Dow, Inc.)
• Inventors: Henshaw, Terry L.
• Primary Examiner(s): Freeh, William L.
• Application Number:
  US05/842,725
• Time in Patent Office: 1,009 Days
• Field of Search: 415/206, 415/207, 415/219 A, 415/219 C
• US Class Current: 415/206
• CPC Class Codes: F04D 29/445 especially adapted for liquid pumps

Abstract

The specification discloses a centrifugal pump in which radial thrust on the impeller shaft is reduced by employing a modified volute casing in which the casing flow area downstream from the cutwater to a point generally opposite the cutwater is significantly greater than would be the flow area of a true volute casing, the area at a point generally opposite the cutwater being significantly less than the flow area of a true volute casing and the area just upstream of the throat back towards the point opposite the cutwater being significantly greater than would be the flow area of a true volute casing.

Claims

1. A centrifugal pump having a casing, inlet, impeller, throat and cutwater, the improvement comprising:

said casing being of a modified volute configuration having in the upstream portion thereof, from the cutwater towards a point generally 180°

from the cutwater, a flow area which is greater than would be the flow area of a true volute casing in the same upstream casing portion;

the flow area of said casing in the downstream portion thereof, from the throat back upstream towards a point generally 180°

from the cutwater, also being greater than would be the flow area of a true volute casing in the same downstream casing portion; and

the flow area of the casing in the juncture portion of the pump extending from the upstream portion through a point 180°

from the cutwater and to the downstream portion being significantly less than would be the flow area of a true volute casing at said juncture portion.

2. The centrifugal pump of claim 1 in which the casing flow area increases relatively rapidly in the upstream portion of the casing as one proceeds from the cutwater until said flow area is approximately 60% of the throat area.

3. The centrifugal pump of claim 2 in which said casing flow area increases from the cutwater and reaches 60% of the throat area at a point approximately 40°

downstream from the cutwater, then continues at about 60% of the throat area until approximately 160°

downstream from the cutwater at which point it begins to decrease.

4. The centrifugal pump of claim 3 in which said casing flow area decreases as one proceeds from the upstream portion of the casing to the juncture portion of the casing until it reaches approximately 45% of the throat area in said juncture portion.

5. The centrifugal pump of claim 4 in which said casing flow area reaches 45% of the throat area at a point approximately 190°

downstream from said cutwater and begins to gradually increase from a point approximately 190°

downstream from said cutwater until it equals the flow area of a true volute casing at a point approximately 240°

downstream from said cutwater.

6. The centrifugal pump of claim 5 in which said casing flow area increases in said downstream portion of said pump until it reaches approximately 100% of the throat area.

7. The centrifugal pump of claim 6 in which said casing flow area at a point approximately 300°

downstream from said cutwater, reaches 100% of throat area and continues at approximately 100% of said throat area from a point 300°

downstream from said cutwater to said throat.

8. The centrifugal pump of claim 1 in which said casing flow area decreases as one proceeds from the upstream portion of the casing to the juncture portion of the casing until it reaches approximately 45% of the throat area in said juncture portion.

9. The centrifugal pump of claim 8 in which said casing flow area reaches 45% of the throat area at a point approximately 190°

downstream from said cutwater and begins to gradually increase from a point approximately 190°

downstream from said cutwater until it equals the flow area of a true volute casing at a point approximately 240°

downstream from said cutwater.

10. The centrifugal pump of claim 1 in which said casing flow area increases in said downstream portion of said pump until it reaches approximately 100% of the throat area.

11. The centrifugal pump of claim 10 in which said casing flow area at a point approximately 300°

downstream from said cutwater, reaches 100% of throat area and continues at approximately 100% of said throat area from a point 300°

downstream from said cutwater to said throat.

12. In a centrifugal pump having an impeller, a casing, an inlet, a cutwater and a throat, the improvement in said pump comprising:

said casing being a modified volute casing having a casing flow area which increases sharply from said cutwater to approximately 60% of the throat area at a point approximately 40°

downstream from said cutwater and continues at approximately 60% of said throat area to about 160°

downstream from said cutwater;

said casing flow area thereafter decreasing sharply to about 45% of said throat area at a point approximately 190°

downstream from said cutwater; and

said casing thereafter increasing gradually to about 100% of said throat area at a point approximately 300°

downstream from said cutwater and continuing at approximately 100% of said throat area to said throat.

13. A centrifugal pump having a casing, inlet, impeller, throat and cutwater, the improvement in said pump comprising:

said casing being generally of a volute configuration but having modified casing flow areas for reducing radial thrust loading of the impeller, said modified casing flow areas defining, in the upstream portion thereof between the cutwater and a point generally 180°

from said cutwater and through the portion located generally 90°

from the cutwater, a flow area which is greater than would be the flow area of true volute casing in the same upstream casing portion.

14. A centrifugal pump having a casing, inlet, impeller, throat and cutwater, the improvement in said pump comprising:

said casing being generally of a volute configuration but having modified casing flow areas for reducing radial thrust loading of the impeller, said modified casing flow areas defining, in the upstream portion thereof between the cutwater and a point generally 180°

from said cutwater, a flow area which is greater than would be the flow area of true volute casing in the same upstream casing portion;

said greater casing flow area increasing relatively rapidly in the upstream portion of the casing as one proceeds from the cutwater until said flow area is approximately 60% of the throat area.

15. The centrifugal pump of claim 14 in which said casing flow area increases from the cutwater and reaches 60% of the throat area at a point approximately 40°

downstream from the cutwater, then continues at about 60% of the throat area until approximately 160°

downstream from the cutwater at which point it begins to decrease.

16. A centrifugal pump having a casing, inlet, impeller, throat and cutwater, the improvement in said pump comprising:

said casing being generally of a volute configuration but having modified casing flow areas for reducing radial thrust loading of the impeller, said modified casing flow areas defining a restricted flow area which is less than would be the flow area of a true volute in that portion of said casing located approximately 180°

downstream from said cutwater and extending further downstream beyond such point, said restricted flow area including at least a portion which is about 45% of the throat area of the casing.

17. The centrifugal pump of claim 16 in which said restricted casing flow area reaches 45% of the throat area at a point approximately 190°

downstream from said cutwater and begins to gradually increase from a point approximately 190°

downstream from said cutwater until it equals the flow area of a true volute casing at a point approximately 240°

downstream from said cutwater.

18. A centrifugal pump having a casing, inlet, impeller, throat and cutwater, the improvement in said pump comprising:

said casing having a modified volute configuration with casing flow areas differing from those of a true volute casing for reducing radial thrust loading of the impeller, said modified casing defining a flow area in the downstream portion thereof, between the throat and a point generally 180°

from the cutwater, which is greater than would be the flow area of true volute casing in the same downstream casing portion.

19. A centrifugal pump having a casing, inlet, impeller, throat and cutwater, the improvement in said pump comprising:

said casing having a modified volute configuration with casing flow areas differing from those of a true volute casing for reducing radial thrust loading of the impeller, said modified casing defining a flow area in the downstream portion thereof, between the throat and a point generally 180°

from the cutwater, which is greater than would be the flow area of true volute casing in the same downstream casing portion;

said casing flow area, at a point approximately 300°

downstream from said cutwater, reaching 100% of throat area and continuing at approximately 100% of said throat area from a point 300°

downstream from said cutwater to said throat.