US2127865A - Seal for centrifugal pumps - Google Patents

Seal for centrifugal pumps Download PDF

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Publication number
US2127865A
US2127865A US742251A US74225134A US2127865A US 2127865 A US2127865 A US 2127865A US 742251 A US742251 A US 742251A US 74225134 A US74225134 A US 74225134A US 2127865 A US2127865 A US 2127865A
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vanes
impeller
shaft
centrifugal
liquid
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US742251A
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Robert H Goddard
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Priority to US180783A priority patent/US2158182A/en
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D29/00Details, component parts, or accessories
    • F04D29/18Rotors
    • F04D29/22Rotors specially for centrifugal pumps
    • F04D29/2261Rotors specially for centrifugal pumps with special measures
    • F04D29/2266Rotors specially for centrifugal pumps with special measures for sealing or thrust balance
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S60/00Power plants
    • Y10S60/915Collection of goddard patents
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10TTECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T403/00Joints and connections
    • Y10T403/36Three or more serial joints, at least one diverse
    • Y10T403/364Separable intermediate joint

Definitions

  • This invention relates to centrifugal pumps and particularly to pumps designed for handling low temperature liquids, such as liquid air,
  • FIG. 1 is an enlargedsectional front elevation of a portion of a centrifugal pump embodying my improvements
  • Fig. 2 is a sectional end elevation, taken along the line 2--2 in Fig. 1.
  • a centrifugal pump comprising a casing 20, and enclosed impeller 2
  • the shaft 23 is connected to the impeller shaft 22 by a special heat-insulated coupling constructed as follows: I
  • a flange 26 is threaded on one end of the impeller shaft 22 and a similar flange 21 is threaded on the adjacent end of the supporting shaft 23.
  • the flanges 26 and 21 are connected by bolts 28, each provided with a sleeve 29, washers 30 and a collar 3
  • the pump casing 20 (Fig. 1) is provided with an axial extension 40, having an intake opening or connection 4
  • is discharged through the usual volute delivery passage.
  • the vanes 50 are preferably connected by annular ribs 54 and 55 and the vanes 5
  • the annular ribs 54, 55, 56 and 51 are pro- 0 vided to serve as dampers and to reduce the surging which might otherwise occur with respect to the liquid between the vanes 50 at one side of the impeller or between the vanes 5
  • vanes 10 (Fig. 1) on the inside of the casing extension 40 and I also provide an internal fixed partition 12 within the extension 40.
  • a flange or disc 14 is fixed to the shaft 22 and is provided with short vanes IS on its outer face and longer vanes 16 on its inner face. These vanes may be radial, but are preferably rearwardly inclined with respect to the direction of rotation of the shaft 22, as shown in Fig. 2.
  • Annular rings I8 and 15 may be provided to prevent surging as previously described.
  • I preferably provide a suitable air-seal device indicated generally by the numeral 98 (Fig. 1).
  • a centrifugal pump having an impeller shaft and a suction chamber maintained at less than atmospheric pressure
  • a casing for said chamber having an end wall and having an internal partition
  • a disc on said shaft rotatable between said end wall and said partition
  • a plurality of short outwardly extending vanes on the outer side of said disc and adjacent said shaft
  • a plurality of longer vanes onthe inner side of said disc and rotatable closely adjacent the outer side of said partition
  • a plurality of fixed vanes on the end wall of said casing and positioned radially outward beyond said short movable vanes, said'flxed vanes being positioned closely adjacent the smooth outer portion of the outer surface of said disc.

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  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Structures Of Non-Positive Displacement Pumps (AREA)

Description

Aug. 23, 1938. H GODDARD 2,127,865
SEAL FOR CENTRIFUGAL PUMPS Filed Aug. 31, 1934 /l A l 7a- 22 flc a; jobei ffioaa az g 6 WWW Patented Au 23, 1938 PATENT OFFICE SEAL FOR CENTRIFUGAL PUMPS Robert H. Goddard, Worcester, Mass.
Application August 31, 1934,.Serial No. 742,251
2 Claims.
This invention relates to centrifugal pumps and particularly to pumps designed for handling low temperature liquids, such as liquid air,
at or near their very low boiling points. In pumps designed for such purposes it is obviously necessary to reduce all heat losses to a minimum.
It is the general object of my present invention to provide a construction in a centrifugal pump by which the friction of solid bodies in running contact is entirely avoided. More specifically, I provide a construction by which a liquid is rendered effective by centrifugal force to serve as packing for the pump and shaft, all other packing being avoided.
My invention further relates to arrangements and combinations of parts which will be hereinafter described and more particularly pointed out in the appended claims.
A preferred form of my invention is shown in the drawing, in which Fig. 1 is an enlargedsectional front elevation of a portion of a centrifugal pump embodying my improvements; and
Fig. 2 is a sectional end elevation, taken along the line 2--2 in Fig. 1.
Referring particularly to Fig. 1, I have shown a portion of a centrifugal pump comprising a casing 20, and enclosed impeller 2|, an impeller shaft 22, and a supporting or driving shaft 23 rotatably mounted in a bearing 25. The shaft 23 is connected to the impeller shaft 22 by a special heat-insulated coupling constructed as follows: I
A flange 26 is threaded on one end of the impeller shaft 22 and a similar flange 21 is threaded on the adjacent end of the supporting shaft 23. The flanges 26 and 21 are connected by bolts 28, each provided with a sleeve 29, washers 30 and a collar 3|, all of suitable nonconducting and heatinsulating material. By this construction any heat generated by the shaft 23 in its bearing 25 is prevented from transfer to the impeller shaft 22.
The pump casing 20 (Fig. 1) is provided with an axial extension 40, having an intake opening or connection 4|. The liquid delivered from the peripheral openings 43 of the impeller 2| is discharged through the usual volute delivery passage.
I will now describe the special construction which I have provided for preventing leakage or back flow of liquid between the outer faces of the impeller 2| and the adjacent faces of the casing 20. For this p se I provide radial vanes 50 at the intake side of the impeller 2|, and radial vanes at the opposite side of the impeller 2|.
The vanes 50 are preferably connected by annular ribs 54 and 55 and the vanes 5| are preferably similarly connected by annular ribs 56 and 5 51. These vanes and ribs rotate with close clearances but without actual contact with the easing 20.
These sets of vanes operate in effect like additional centrifugal pumps and tend to build up 10 pressure at their outer extremities, which on account of the very slight radial flow is normally greater than that produced by the impeller. vanes. Consequently short-circuit losses due to leakage of high pressure liquid from the volute to the intake are prevented by the centrifugal action of the radial vanes 50, and leakage from the volute to the space beyond the casing is prevented by the action of the radial vanes 5|.
The annular ribs 54, 55, 56 and 51 are pro- 0 vided to serve as dampers and to reduce the surging which might otherwise occur with respect to the liquid between the vanes 50 at one side of the impeller or between the vanes 5| at the opposite side. Otherwise the opposed action of the centrifugal force produced by the impeller 2| and the centrifugal force produced by the vanes 50 or 5| would tend to cause undesirable surging of the packing liquid in its attempt to maintain a hydrostatic balance between liquids 80 acted on by these two forces.
I have found by experiment that the pressure head produced by the vanes 50 and 5| on the outside of the impeller is sufficient to eliminate all leakage past the impeller as soon as the pump is operating at or near full speed.
If the pump is operated with suction at the intake side, provision must be made for preventing inflow of air around the impeller shaft 22. For this purpose I provide fixed vanes 10 (Fig. 1) on the inside of the casing extension 40 and I also provide an internal fixed partition 12 within the extension 40. A flange or disc 14 is fixed to the shaft 22 and is provided with short vanes IS on its outer face and longer vanes 16 on its inner face. These vanes may be radial, but are preferably rearwardly inclined with respect to the direction of rotation of the shaft 22, as shown in Fig. 2. Annular rings I8 and 15 may be provided to prevent surging as previously described.
The operation of this centrifugal packing construction is as follows: Liquid between the moving vanes 16 is forced outward to produce a pressure head in the space between the partition 1! and the end wall of the casing extension ll sumcient to overcome atmospheric pressure and thus prevent inflow of air to the impeller casing even when the pump is operating under suction. Any excess of pressure thus developed which might tend to force the liquid out of the end of the casing I is prevented by the mass of liquid held between the fixed vanes 10 and subjected to pressure developed by the short external moving vanes II. A balance of pressures is thus maintained which prevents either inflow of air or outflow of liquid along the shaft 22.
It is necessary to prevent leakage of air into the suction chamber before the pump comes up to speed, as otherwise the inflow of air would destroy the action of the priming liquid. To prevent such air leakage under these conditions, I preferably provide a suitable air-seal device indicated generally by the numeral 98 (Fig. 1).
Having thus described my invention, it will be seen that I have provided a construction by which liquids may be pumped by a liquid-sealed centrifugal impeller which is heat-insulated from any moving part having frictional contact with a stationary part. The development of heat by the impeller itself or by transfer from supporting members is reduced to a minimum, and a centrifugal pump is thus rendered capable of pumping liquids having very low boiling points and at temperatures much below the temperature of the atmosphere in which the pump operates.-
The heat-insulated shaft-coupling shown at the left in Fig. l is not claimed herein but forms the subject matter of a divisional application, Serial No. 180,783, filed by me December 20, 1937.
Having thus described my invention and the advantages thereof, I do not wish to be limited to the details herein disclosed, otherwise than as set forth in the claims, but what I claim is:--
1. In a centrifugal pump operating under suction and having separate intake and discharge portions, an impeller shaft having a disc thereon, a casing having a partition, vanes fixed on said casing at the side of said disc more remote from the pump intake, and additional vanes mounted on each side of said movable disc, the movable vanes on the side of the disc adjacent the hated vanes being of less outside diameter than the inner diameter of said fixed vanes.
2. In a centrifugal pump having an impeller shaft and a suction chamber maintained at less than atmospheric pressure, in combination, a casing for said chamber having an end wall and having an internal partition, a disc on said shaft rotatable between said end wall and said partition, a plurality of short outwardly extending vanes on the outer side of said disc and adjacent said shaft, a plurality of longer vanes onthe inner side of said disc and rotatable closely adjacent the outer side of said partition, and a plurality of fixed vanes on the end wall of said casing and positioned radially outward beyond said short movable vanes, said'flxed vanes being positioned closely adjacent the smooth outer portion of the outer surface of said disc.
ROBERT H. GODDARD.
US742251A 1934-08-31 1934-08-31 Seal for centrifugal pumps Expired - Lifetime US2127865A (en)

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US742251A US2127865A (en) 1934-08-31 1934-08-31 Seal for centrifugal pumps
US180783A US2158182A (en) 1934-08-31 1937-12-20 Heat insulating coupling

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Cited By (20)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2516462A (en) * 1946-10-17 1950-07-25 Daniel And Florence Guggenheim Double jacket means for feeding two liquids to a rotating combustion chamber
US2541850A (en) * 1946-06-10 1951-02-13 Gen Electric Shaft seal arrangement
US2573425A (en) * 1947-06-23 1951-10-30 Ethel K Haferkamp Seal for centrifugal machines
US2606044A (en) * 1950-05-25 1952-08-05 Battelle Development Corp Seal
US2663262A (en) * 1942-12-16 1953-12-22 Jonkopings Mek Werkstads Aktie Centrifugal pump with sealing device
US2764945A (en) * 1949-08-02 1956-10-02 Heep Heinrich Pump and liquid shaft seal therefor
DE964742C (en) * 1945-07-07 1957-05-29 Joenkoepings Mek Werkstads Akt Centrifugal pump with vertical shaft and a hydraulic device for sealing the shaft
US2911240A (en) * 1956-08-30 1959-11-03 Mixing Equipment Co Inc Sealing means for receptacle shaft opening
US2963307A (en) * 1954-12-28 1960-12-06 Gen Electric Honeycomb seal
US3028181A (en) * 1958-12-26 1962-04-03 Thompson Lee Lavere Seals for rotating shafts
US3073249A (en) * 1958-02-14 1963-01-15 Yokota Hidekuni Multistage self-suction type centrifugal pump
US3139831A (en) * 1962-08-28 1964-07-07 Ingersoll Rand Co Self-cleaning wearing ring for centrifugal pump pumping mixture of liquid and solid
US3160108A (en) * 1962-08-27 1964-12-08 Allis Chalmers Mfg Co Thrust carrying arrangement for fluid handling machines
US3526465A (en) * 1968-09-10 1970-09-01 Acf Ind Inc Impeller for a submerged centrifugal fuel pump
US3535051A (en) * 1968-12-03 1970-10-20 Ellicott Machine Corp Recessed expeller vanes
US4014626A (en) * 1975-09-08 1977-03-29 Grenn James F Centrifugal pump means
DE3627778A1 (en) * 1986-08-16 1988-02-18 Bbc Brown Boveri & Cie CONTACT-FREE CENTRIFUGAL SEALING DEVICE FOR A ROTATING MACHINE PART
EP0288500A1 (en) * 1986-10-07 1988-11-02 Warman Int Ltd Impellers for centrifugal pumps.
DE10004263A1 (en) * 2000-02-01 2001-08-02 Leybold Vakuum Gmbh Seal between stationary and rotating component in vacuum pump consists of blades arranged in herringbone pattern attached to each component
US10890353B2 (en) * 2016-10-10 2021-01-12 Aspen Pumps Limited Centrifugal pump flow modifier

Cited By (23)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2663262A (en) * 1942-12-16 1953-12-22 Jonkopings Mek Werkstads Aktie Centrifugal pump with sealing device
DE964742C (en) * 1945-07-07 1957-05-29 Joenkoepings Mek Werkstads Akt Centrifugal pump with vertical shaft and a hydraulic device for sealing the shaft
US2541850A (en) * 1946-06-10 1951-02-13 Gen Electric Shaft seal arrangement
US2516462A (en) * 1946-10-17 1950-07-25 Daniel And Florence Guggenheim Double jacket means for feeding two liquids to a rotating combustion chamber
US2573425A (en) * 1947-06-23 1951-10-30 Ethel K Haferkamp Seal for centrifugal machines
US2764945A (en) * 1949-08-02 1956-10-02 Heep Heinrich Pump and liquid shaft seal therefor
US2606044A (en) * 1950-05-25 1952-08-05 Battelle Development Corp Seal
US2963307A (en) * 1954-12-28 1960-12-06 Gen Electric Honeycomb seal
US2911240A (en) * 1956-08-30 1959-11-03 Mixing Equipment Co Inc Sealing means for receptacle shaft opening
US3073249A (en) * 1958-02-14 1963-01-15 Yokota Hidekuni Multistage self-suction type centrifugal pump
US3028181A (en) * 1958-12-26 1962-04-03 Thompson Lee Lavere Seals for rotating shafts
US3160108A (en) * 1962-08-27 1964-12-08 Allis Chalmers Mfg Co Thrust carrying arrangement for fluid handling machines
US3139831A (en) * 1962-08-28 1964-07-07 Ingersoll Rand Co Self-cleaning wearing ring for centrifugal pump pumping mixture of liquid and solid
US3526465A (en) * 1968-09-10 1970-09-01 Acf Ind Inc Impeller for a submerged centrifugal fuel pump
US3535051A (en) * 1968-12-03 1970-10-20 Ellicott Machine Corp Recessed expeller vanes
US4014626A (en) * 1975-09-08 1977-03-29 Grenn James F Centrifugal pump means
DE3627778A1 (en) * 1986-08-16 1988-02-18 Bbc Brown Boveri & Cie CONTACT-FREE CENTRIFUGAL SEALING DEVICE FOR A ROTATING MACHINE PART
FR2602846A1 (en) * 1986-08-16 1988-02-19 Bbc Brown Boveri & Cie NON-CONTACT CENTRIFUGAL SEALING DEVICE FOR A ROTATING MACHINE
EP0288500A1 (en) * 1986-10-07 1988-11-02 Warman Int Ltd Impellers for centrifugal pumps.
EP0288500A4 (en) * 1986-10-07 1988-11-24 Warman Int Ltd Impellers for centrifugal pumps.
DE10004263A1 (en) * 2000-02-01 2001-08-02 Leybold Vakuum Gmbh Seal between stationary and rotating component in vacuum pump consists of blades arranged in herringbone pattern attached to each component
US6705844B2 (en) 2000-02-01 2004-03-16 Leybold Vakuum Gmbh Dynamic seal
US10890353B2 (en) * 2016-10-10 2021-01-12 Aspen Pumps Limited Centrifugal pump flow modifier

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