US2929646A - Centrifugal pump seal - Google Patents

Centrifugal pump seal Download PDF

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Publication number
US2929646A
US2929646A US569932A US56993256A US2929646A US 2929646 A US2929646 A US 2929646A US 569932 A US569932 A US 569932A US 56993256 A US56993256 A US 56993256A US 2929646 A US2929646 A US 2929646A
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pump
fluid
shaft
pressure
seal
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US569932A
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Harold S Smith
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Combustion Engineering Inc
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Combustion Engineering Inc
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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
    • F04D29/08Sealings
    • F04D29/10Shaft sealings
    • F04D29/106Shaft sealings especially adapted for liquid pumps
    • F04D29/108Shaft sealings especially adapted for liquid pumps the sealing fluid being other than the working liquid or being the working liquid treated

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  • This invention relates to centrifugal type pumps for use with high temperature high pressure fluids and has pmicular relation to such a pump provided with a seal employing the use of so-called injection or sealing fluid.
  • an injection or sealing fluid is often employed to insure that the high temperature fluid being pumped does not contact the pump seals because of the deleterious effect that this high temperature would have on these seals.
  • This injection fluid is generally introduced into a cavity in the pump housing and through which the pump shaft passes with this fluid being at a pressure slightly higher than the pump pressure.
  • This cavity is generally located between the innermost bearing of the pump, which is preferably constructed to act at least as a partial seal, and the relatively soft seal packing which is located outwardly of this hearing along the pump shaft whereby the high pressure seal fluid prevents leakage of the fluid being pumped outwardly along the pump shaft.
  • the soft packing will not be subjected to the high pressure of the sealing fluid as it is introduced into the cavity a so-called breakdown seal is provided to insure that the pressure of this scaling fluid is greatly reduced before the fluid contacts the packing, with this fluid then being conveyed from the cavity at a location adjacent this packing and at this reduced pressure.
  • the invention comprises an arrangement, construction and combination of the elements of the inventive organization in such a manner as to attain the results desired as hereinafter more particularly set forth in the following detailed description of an illustrative embodiment, said embodiment being shown by the accompanying drawing wherein:
  • Fig. 1 is an axial sectional view of part of a centrifugal pump embodying the present invention.
  • Fig, 2 is an enlarged axial sectional view of the seal organization of this pump.
  • the centrifugal pump illustratively disclosed therein comprises a volute or body into which water or other fluid is admitted at inlet 12 and discharged through out- "ice 7 2 let 14 with this water, in the case of a boiler circulating pump being at a high temperature and pressure.
  • the impeller 18 Positioned within central chamber 16 of body 10 is the impeller 18 which is secured to the lower end of pump shaft 20.
  • This shaft extends upwardly through the cover portion 22 of the pump casing with this cover portion being made in two sections the lower section 24 of which is secured to body 10 by bolts 26 while “the upper portion 28 is secured to this lower portion by bolts 30.
  • pump shaft 20 extends up wardly from cover 22 and is received within suitable thrust and radial bearings and is connected at its upper end to a driving motor with this mechanism being conventional and accordingly not shown in the drawing.
  • the lower end of pump shaft 20 is received within bearing 32 which is positioned at the inner end of cavity 34 provided in cover 22 and is constructed so as to provide suflicient sealing to prevent excessive leakage'from this cavity into the chamber 16.
  • cover 22 At the upper end of cover 22 there is provided a soft packing 36 positioned within a suitable counterbore in the cover and effective to prevent the escape of fluid from cavity 34 outwardly along pump shaft 20 with the adjustable packing gland or nut 33 being operative to compress this packing 36 as desired.
  • Injection or sealing fluid is introduced into cavity 34 through passage 40 at a pressure that is slightly higher than the outlet pressure of the pump or the pressure existing in chamber 16 with this injection fluid being conveyed from cavity 34 by passage 42 and conduit 44.
  • the pressure in cavity 34 immediately above bearing 32 is slightly greater than that existing in pump chamber 16 so that any leakage that takes place will be into and not out of the pump chamber.
  • a suitable breakdown seal is provided and which, in the illustrative organization, comprises flanged sleeve 46 which is positioned in coaxial relation with pump shaft 20 and has its flange secured between the upper and lower portions 28 and 24 respectively of cover 22 in a fluid tight manner.
  • This sleeve has an internal diameter which is slightly larger than the external diameter of pump shaft 20 at the location of the sleeve so that a restricted annular passage 48 is formed through which the injection fluid must flow in passing from inlet passage 40 and the inner end of cavity 34 to the outlet passage 42 with this restricted annular passage being effective to greatly reduce the pressure of the sealing fluid so that the pressure acting against packing 36 is much less than that existing in the inner end of cavity 34.
  • the pump outlet pressure may be 2000 p.s.i. with the temperature of the water being pumped being in the order of 600 F.
  • the injection fluid introduced into cavity 34 through conduit 40 may be 2050 p.s.i. and 300 F.
  • this pressure is reduced to 300 p.s.i. so that it is this 300 pound pressure that packing 36 is subjected to and which it is to retain Within the confines of the pump housing.
  • annular stream of fluid issuing from the upper end of passage 43 is jet-like in that it is traveling at a very high velocity such as 70 or feet per second and since this annular stream is located immediately adjacent to the pump shaft 20 it tends to continue along this pump shaft and impinge upon the packing 36, which must necessarily be relatively soft, usually being made of an asbestos composition with the jet action of this stream damaging this packing.
  • annular collar 50 against which this fluid stream issuing from the end of annular passage 48impinges-thereby dissipating the kinetic energy of the jet and preventing it from contacting packing 36.
  • This collar 50 may be integral with pump shaft 20 or may be a ring shrunk on or otherwise secured to the shaft. It will be noted that the endof the pump shaft that extends through cover 22 is comprised of two parts having an inner or solid member 52 about which is positioned sleeve member '54 which is secured at its inner end to the member 52 in a fluid tight manner as by threading or other suitable means and which may be, replaced when it becomes unduly worn. However,'as emaeaaeee I 7 ployed in this application members 52 and 54 are to- V gether intended to comprise the pump shaft of the centrifugal pump.
  • said breakdown seal including means forming a restricted passage concentric with the shaft and operative to reduce the pressure of said fluid prior to its reaching the stufling box and constructed and arranged so that at its outward end a high velocity stream of the fluid is produced in parallelrelation with and immediately adjacent to said shaft,
  • a stufling box having 'a compressible packing in engagement with V the shaft, a high pressure breakdown seal disposed about said shaft and spaced from the packing, means for introducing a high pressure sealing fluid in the housing at the end of the breakdown seal remote from the stuffing box, said breakdown seal comprising means forming an annular passage of restricted area concentric with theshaft with the outer end of the passage being immediately adjacent said shaft so that a high velocity stream of this fluid is produced in parallel relation with and immediately adjacent said shaft, a deflector for said high velocity stream comprising a collar formed on and secured, to the shaft between the breakdown seal and the 'stufling box ducing a high pressure sealing fluid in the housing at the end of the'breakdown seal remote from the stufling box, said breakdown seal comprising a stationary sleeve concentric -and coaxial with said shaft and forming therewith an annular passage of restricted area through which.

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

Description

H. 5. SMITH 2,929,646
CENTRIFUGAL PUMP SEAL March 22, 1960 IIIH" Fig. l.
INVENTOR Harold S. Smith 7 814M Aha w ATTORNEY H. 8. SMITH CENTRIFUGAL PUMP SEAL March 22, 1960 2 Sheets-Sheet 2 Filed March 6, 1956 INVENTOR Harold S. Smith ATTORNEY United States Patent-O CENTRIFUGAL PUMP SEAL Harold S. Smith, Richmond, Ind., assignor to Combustion Engineering, Inc., New York, N.Y., a corporation of Delaware Application March 6, 1956, Serial No. 569,932
'3 Claims. (Cl. 286--9) This invention relates to centrifugal type pumps for use with high temperature high pressure fluids and has pmicular relation to such a pump provided with a seal employing the use of so-called injection or sealing fluid.
In the art relating to centrifugal pumps that are used to pump high temperature fluids at relative high pressures, such as the circulating pumps used with forced or controlled circulation boilers, an injection or sealing fluid is often employed to insure that the high temperature fluid being pumped does not contact the pump seals because of the deleterious effect that this high temperature would have on these seals. This injection fluid is generally introduced into a cavity in the pump housing and through which the pump shaft passes with this fluid being at a pressure slightly higher than the pump pressure. This cavity is generally located between the innermost bearing of the pump, which is preferably constructed to act at least as a partial seal, and the relatively soft seal packing which is located outwardly of this hearing along the pump shaft whereby the high pressure seal fluid prevents leakage of the fluid being pumped outwardly along the pump shaft. In order that the soft packing will not be subjected to the high pressure of the sealing fluid as it is introduced into the cavity a so-called breakdown seal is provided to insure that the pressure of this scaling fluid is greatly reduced before the fluid contacts the packing, with this fluid then being conveyed from the cavity at a location adjacent this packing and at this reduced pressure. It has been found that in organizations wherein the breakdown seal is so constructed as to pro' duce at its outer end a very high velocity jet of the injection fluid immediately adjacent and in parallel relation with the pump shaft that this jet rapidly destroys the soft packing and it is the purpose of this invention to overcome this problem.
It is therefore an object of the present invention to provide an improved centrifugal pump organization.
Other and further objects of the invention will become apparent to those skilled in the art as the description proceeds.
With the aforementioned objects in view, the invention comprises an arrangement, construction and combination of the elements of the inventive organization in such a manner as to attain the results desired as hereinafter more particularly set forth in the following detailed description of an illustrative embodiment, said embodiment being shown by the accompanying drawing wherein:
Fig. 1 is an axial sectional view of part of a centrifugal pump embodying the present invention.
Fig, 2 is an enlarged axial sectional view of the seal organization of this pump.
Referring now to the drawing, wherein like reference characters are used throughout to designate like elements, the centrifugal pump illustratively disclosed therein comprises a volute or body into which water or other fluid is admitted at inlet 12 and discharged through out- "ice 7 2 let 14 with this water, in the case of a boiler circulating pump being at a high temperature and pressure. Positioned within central chamber 16 of body 10 is the impeller 18 which is secured to the lower end of pump shaft 20. This shaft extends upwardly through the cover portion 22 of the pump casing with this cover portion being made in two sections the lower section 24 of which is secured to body 10 by bolts 26 while "the upper portion 28 is secured to this lower portion by bolts 30. It will be appreciated that pump shaft 20 extends up wardly from cover 22 and is received within suitable thrust and radial bearings and is connected at its upper end to a driving motor with this mechanism being conventional and accordingly not shown in the drawing.
The lower end of pump shaft 20 is received within bearing 32 which is positioned at the inner end of cavity 34 provided in cover 22 and is constructed so as to provide suflicient sealing to prevent excessive leakage'from this cavity into the chamber 16. At the upper end of cover 22 there is provided a soft packing 36 positioned within a suitable counterbore in the cover and effective to prevent the escape of fluid from cavity 34 outwardly along pump shaft 20 with the adjustable packing gland or nut 33 being operative to compress this packing 36 as desired.
Injection or sealing fluid is introduced into cavity 34 through passage 40 at a pressure that is slightly higher than the outlet pressure of the pump or the pressure existing in chamber 16 with this injection fluid being conveyed from cavity 34 by passage 42 and conduit 44. Thus the pressure in cavity 34 immediately above bearing 32 is slightly greater than that existing in pump chamber 16 so that any leakage that takes place will be into and not out of the pump chamber. In order to reduce the pressure of this injection fluid before it contacts packing 36 a suitable breakdown seal is provided and which, in the illustrative organization, comprises flanged sleeve 46 which is positioned in coaxial relation with pump shaft 20 and has its flange secured between the upper and lower portions 28 and 24 respectively of cover 22 in a fluid tight manner. This sleeve has an internal diameter which is slightly larger than the external diameter of pump shaft 20 at the location of the sleeve so that a restricted annular passage 48 is formed through which the injection fluid must flow in passing from inlet passage 40 and the inner end of cavity 34 to the outlet passage 42 with this restricted annular passage being effective to greatly reduce the pressure of the sealing fluid so that the pressure acting against packing 36 is much less than that existing in the inner end of cavity 34.
To illustrate the conditions that may be encountered in such a pump as herein contemplated the pump outlet pressure may be 2000 p.s.i. with the temperature of the water being pumped being in the order of 600 F. The injection fluid introduced into cavity 34 through conduit 40 may be 2050 p.s.i. and 300 F. In passing through the restricted annular passage 48, which may have a radial dimension of .055", this pressure is reduced to 300 p.s.i. so that it is this 300 pound pressure that packing 36 is subjected to and which it is to retain Within the confines of the pump housing.
Because of this large reduction in pressure the annular stream of fluid issuing from the upper end of passage 43 is jet-like in that it is traveling at a very high velocity such as 70 or feet per second and since this annular stream is located immediately adjacent to the pump shaft 20 it tends to continue along this pump shaft and impinge upon the packing 36, which must necessarily be relatively soft, usually being made of an asbestos composition with the jet action of this stream damaging this packing. In order to prevent this from happening there is provided on the pump shaft 20 an annular collar 50 against which this fluid stream issuing from the end of annular passage 48impinges-thereby dissipating the kinetic energy of the jet and preventing it from contacting packing 36. This collar 50 may be integral with pump shaft 20 or may be a ring shrunk on or otherwise secured to the shaft. It will be noted that the endof the pump shaft that extends through cover 22 is comprised of two parts having an inner or solid member 52 about which is positioned sleeve member '54 which is secured at its inner end to the member 52 in a fluid tight manner as by threading or other suitable means and which may be, replaced when it becomes unduly worn. However,'as emaeaaeee I 7 ployed in this application members 52 and 54 are to- V gether intended to comprise the pump shaft of the centrifugal pump. 1 a 7 While I have illustrated and described a preferred embodiment of my invention it is to be understood that such is merely illustrative andnot restrictive and that variations and modifications may be made therein without departing from the spirit and scope of the invention. I therefore do not wish to be limited to the precise details set forth but desire to avail myself of such changes as fall within the purview of-my invention.
WhatI claim is: v
1. In an organization of the type described'the combination of a housing, a'shaft mounted therein, a st'ufling, box having a compressible packing in engagement with the shaft, a high pressure breakdownseal disposed about ,said shaft and spaced from thepacking, means for introducing a high pressure sealing fluid in the housing at the end of the breakdown seal remote from the stufling box,
' said breakdown seal including means forming a restricted passage concentric with the shaft and operative to reduce the pressure of said fluid prior to its reaching the stufling box and constructed and arranged so that at its outward end a high velocity stream of the fluid is produced in parallelrelation with and immediately adjacent to said shaft,
nation of a housing, ashaft mounted therein, a stufling box having 'a compressible packing in engagement with V the shaft, a high pressure breakdown seal disposed about said shaft and spaced from the packing, means for introducing a high pressure sealing fluid in the housing at the end of the breakdown seal remote from the stuffing box, said breakdown seal comprising means forming an annular passage of restricted area concentric with theshaft with the outer end of the passage being immediately adjacent said shaft so that a high velocity stream of this fluid is produced in parallel relation with and immediately adjacent said shaft, a deflector for said high velocity stream comprising a collar formed on and secured, to the shaft between the breakdown seal and the 'stufling box ducing a high pressure sealing fluid in the housing at the end of the'breakdown seal remote from the stufling box, said breakdown seal comprising a stationary sleeve concentric -and coaxial with said shaft and forming therewith an annular passage of restricted area through which. this fluid is forced to pass before reaching the stufling box so that anannular high velocity stream of fluid issues from the endof thepassageway in parallel relation with and immediately adjacent said shaft, and a deflector disposed References Cited in the file of'this patent UNITED STATES [PATENTS 753,986 Krogh Mar. 8, 1904 1,558,630 Reed Oct. 27, 1925 2,386,898 Karassik Oct. 16, 1.945' 2,419,681 Gartmann Apr. 29, 1947
US569932A 1956-03-06 1956-03-06 Centrifugal pump seal Expired - Lifetime US2929646A (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3128103A (en) * 1959-10-02 1964-04-07 Combustion Eng Thermal sleeves for boiler water circulating pumps
US3364523A (en) * 1965-05-28 1968-01-23 Barmag Barmer Maschf Seal packing fluid seals for extrusion machines
US4419015A (en) * 1981-02-19 1983-12-06 General Signal Corporation Agitator having detachable wear sleeve
US5346361A (en) * 1993-04-15 1994-09-13 Goulds Pumps, Incorporated Air seal for pump with vertical shaft
US5368311A (en) * 1976-04-16 1994-11-29 Heyl; Robert D. Shaft seal assembly for a rotary valve
US20180180056A1 (en) * 2016-12-28 2018-06-28 Mikhail Aleksandrovich Zolotukhin Vertical suspended centrifugal pump

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US753986A (en) * 1903-12-04 1904-03-08 Ferdinand W Krogh Pump.
US1558630A (en) * 1924-02-18 1925-10-27 Ingersoll Rand Co Hydraulic seal for rotary engines
US2386898A (en) * 1943-10-30 1945-10-16 Worthington Pump & Mach Corp Centrifugal pump
US2419681A (en) * 1944-01-08 1947-04-29 Laval Steam Turbine Co Circulating pump sealing system

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US753986A (en) * 1903-12-04 1904-03-08 Ferdinand W Krogh Pump.
US1558630A (en) * 1924-02-18 1925-10-27 Ingersoll Rand Co Hydraulic seal for rotary engines
US2386898A (en) * 1943-10-30 1945-10-16 Worthington Pump & Mach Corp Centrifugal pump
US2419681A (en) * 1944-01-08 1947-04-29 Laval Steam Turbine Co Circulating pump sealing system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3128103A (en) * 1959-10-02 1964-04-07 Combustion Eng Thermal sleeves for boiler water circulating pumps
US3364523A (en) * 1965-05-28 1968-01-23 Barmag Barmer Maschf Seal packing fluid seals for extrusion machines
US5368311A (en) * 1976-04-16 1994-11-29 Heyl; Robert D. Shaft seal assembly for a rotary valve
US4419015A (en) * 1981-02-19 1983-12-06 General Signal Corporation Agitator having detachable wear sleeve
US5346361A (en) * 1993-04-15 1994-09-13 Goulds Pumps, Incorporated Air seal for pump with vertical shaft
US20180180056A1 (en) * 2016-12-28 2018-06-28 Mikhail Aleksandrovich Zolotukhin Vertical suspended centrifugal pump

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