US3901620A - Method and apparatus for compressor surge control - Google Patents

Method and apparatus for compressor surge control Download PDF

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US3901620A
US3901620A US408809A US40880973A US3901620A US 3901620 A US3901620 A US 3901620A US 408809 A US408809 A US 408809A US 40880973 A US40880973 A US 40880973A US 3901620 A US3901620 A US 3901620A
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compressor
surge
flow
boundary layer
accordance
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US408809A
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Meherwan P Boyce
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Howell Instruments Inc
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Howell Instruments Inc
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Priority to US408809A priority Critical patent/US3901620A/en
Priority to US05/511,705 priority patent/US3930742A/en
Priority to DE19742448841 priority patent/DE2448841A1/en
Priority to CH1385574A priority patent/CH592819A5/xx
Priority to CA211,528A priority patent/CA1025694A/en
Priority to FR7434959A priority patent/FR2248427B1/fr
Priority to GB45470/74A priority patent/GB1481031A/en
Priority to JP49121867A priority patent/JPS5073207A/ja
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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
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02Surge control
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/001Testing thereof; Determination or simulation of flow characteristics; Stall or surge detection, e.g. condition monitoring
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04DNON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02Surge control
    • F04D27/0207Surge control by bleeding, bypassing or recycling fluids

Definitions

  • ABSTRACT A method and apparatus for detecting and controlling impending surge conditions in a compressor.
  • a velocity probe is situated at a compressor outlet adjacent the compressor wall so as to be in the boundary layer of material flowing through the compressor adjacent the wall.
  • Flow reversal in the boundary layer is detected as an indication of an impending surge condition.
  • a bleed line can be connected so as to bleed off a portion of the boundary layer having a reversed flow and feed this portion back to the inlet of the compressor for delaying the onset of surge.
  • the boundary layer flow reversal detection apparatus can also operate a back pressure valve so that the material flow bypasses the compressor when surge conditions are impending in the compressor.
  • a velocity probe is positioned at a compressor outlet near the wall of the compressor in the boundary layerof material flowing through the compressor adjacent to the wall. Flow reversal is detected in the boundary layer which is indicative of an impending surge condition.
  • FIG. 1 is a diagrammatic view of a portion of a centrifugal compressor illustrating one impeller and illustrating flow patterns from the exit of the impeller before surge, near surge, and in a potential surge.
  • FIG. 2 is a diagrammatic illustration similar to FIG. 1 showing a flow reversal detection system in place in a centrifugal compressor and illustrating a bleed line for delaying the onset of surge.
  • FIG. 3 is a diagrammatic illustration of an embodiment of the invention as applied to axial flow compressors.
  • FIG. 4 is a diagrammatic illustration of one form of suitable probe for detecting flow reversal.
  • FIG. 1 there is schematically shown a compressor 11 with one impeller 12 of the compressor being illustrated.
  • the impeller 12 has an eye or entrance 12a and has an exit indicated by reference numeral 12b.
  • the velocity profile or flow pattern of the material flowing throughthe compressor is indicated by curve 13a at the impeller exit 12b.
  • curve 13a Adjacent to the curve 130 there is a curve 13b, which indicates the velocity profile or flow pattern of the material flowing through the impeller when a surge condition is nearing.
  • curve 136 is shown disposed adjacent curve 13b and curve 130 is an indication of the velocity profile or flow pattern of the material flowing out the impeller exit 12b where there is a potential surge.
  • a comparison of the curves 13a, l3b and 130 in FIG. 1 shows that as surge is approached, the velocity of the boundary layer changes from positive to zero and then to negative. That is, there is a flow reversal in the boundary layer at the exit of the impeller as a surge condition is approached.
  • the succession of flow patterns as indicated by the curves 13a through 13c has been confirmed by actual tests on compressors.
  • FIG. 2 there is shown apparatus in accordance with the invention and for practicing the method of the invention installed on a compressor.
  • the same reference numerals are used in FIG. 2 to refer to corresponding portions of the compressor as are used in describing the compressor of FIG. 1.
  • the compressor 11 diagrammatically illustrated in FIG. 2 has an impeller 12 with an eye or inlet 12a and an exit 12b. Situated in the wall of the compressor 11 adjacent the impeller exit is a velocity probe I4.
  • the velocity probe 14 is connected to a flow reversal detector 16.
  • the velocity probe 14, together with the flow reversal detector 16 is adapted to sense the velocity and direction of flow of the boundary layer adjacent the compressor wall at the impeller exit.
  • the velocity probe 14 may comprise any suitable conventional velocity probe, such as a pitot tube, hot wire anemometer, etc.
  • a conventional probe have a flow direction sensing ability at a predetermined portion thereof which may be positioned within the boundary layer and oriented with respect to the expected downstream boundary flow direction so as to produce an output indication whenever the actual boundary layer flow direction substantially reverses.
  • a simple tube having an aperture therein with the aperture positioned to face downstream (i.e., away from the impeller exit) may be provided for achieving this function as shown schematically in the drawings.
  • suction pressure is measured by the probe 14 and the flow reversal detector 16 can, for a simple embodiment, simply be a mercury manometer for providing an indication of the pressure.
  • the relative pressure i.e. relative to a static pressure
  • the probe 14 senses a positive pressure.
  • the probe 14, together with an appropriate flow reversal detector 16 detects flow reversal in the boundary layer to provide an indication of impending surge conditions within the compressor.
  • FIG. 2 also illustrates another feature in accordance with one embodiment of the invention in which bleed can be controlled through a control circuit 19 actuated versal, which it will be recalledis indicative of impend ing surge in the compressor, is obtainedat the flow reversal detector 16.
  • the flow reversal detector 16 then actuatesthrough a control circuit 19 the valve 18 l which opens the bleed line 17 so that a portion of-the flow reversed boundary layer is fed backfrom the outlet orexit of the compressor back into the eye or inlet of the impeller 12. Bleeding back this high pressure boundary layer material when flow reversa l has occurred back to the inlet ofthe compressor relieves the high pressure at the boundary layer at the exit of the compressor and thereby stops flow reversal.
  • the axial flow compressorll schematically illustrated in FIG. 3 includes a stator 22 the case of the centrifugal compressor illustrated in FIGS. 1. and 2; that is, the probe 24 detects reversal of flow in the boundary l ayer at the exit side of the rotor blade tip 23a.
  • the probe 24, as before, is connectedto a flow reversal detector 26.
  • the velocity probe 24 may comprise a pitot tube,l iot wire anemometer, or
  • a simple tube may be used having a hole therein facing downstream with the flow reversal detector in its simplest form being a pressure manometer.
  • a bleed line 27 is provided having a valve 28 therein. The valve 28 maybe actuated through a control circuit 29 by the'flow reversal detector 2 6.
  • the valve 28 is opened so that the high pressure material at the exit side of the rotor blade tip is bled back through bleed line 27 to the inlet side of the rotor blade tip 23a.
  • the bleed line 27 may be of such a diameter so that 2-3 percentof the high pressure material at the exit side of the rotor blade tip is fedback into the inlet side of the rotorblade tip. 0 f
  • valve 28 may be anadjustable valve so that varying amounts of feedback are provided depending practicing the rnethod ofi the invention.
  • FIG. 1 the valve 28 may be anadjustable valve so that varying amounts of feedback are provided depending practicing the rnethod ofi the invention.
  • a probe which comprises a simple tube 3l having an aperture 32 in one side thereof.
  • the probe is positioned in the compressor such that the aperture faces Jdownstream in "the direction of desired flow through the compressor.
  • any positive pressure (relative to a'static pressure) detected as being exerte'd throughthe aperture 32 i'sanindication of flow reversal.
  • the velocity probe gives an indication of flow direction.
  • the probe is adjacent the exit of a compressor stage are situated so asto be in the .boundary-,layer. of the flow at the compressor stage exit.
  • the size of the boundary layer is also dependent upon the pressuresv and speeds atwhich the compressor is operated. It is considered within the skill of those knowledgable in the art to determine for.
  • the backpressurevalve can exhaust air, for example, from the outlet side of the compressor to the atmosphere through a blow off system so that there is always enough air passing through the compressorto keep itin its stablerange away from surge conditions.
  • a back pressure valve is operated by means of a static pressure probe placed some place adjacent the exit side of the compressor.
  • the back pressure valve is actuated to eithe'r'bypass the compressor completely or to exhaust the high pressure air at the outletv side of the machine to the atmosphere so as to lower the pressure on the outlet side of the machine-in accordance with one aspectof the present invention, such.
  • a back pressure valve can be operated-through the flow reversal detecting mechanism of the presentinvention. That is, the back pressure valve isactuated dependent upon flow reversal detected in the boundary layer adjacent the exit side of the machinerather than the static pressure build-up detected by some variety of static pressure probe. Detecting flow reversal for operating .the back pressure valve is a much' more accurate means for preventing surge conditions'than depending upon a static pressure condition, which canvary from compressor to compressor. 7
  • a method of detecting an impending surge condition in a compressor comprising:
  • a method in accordance with claim 1 including the step of bleeding off a portion of the boundary layer at the compressor outlet back into the compressor inlet in response to detected flow reversal in order to delay the onset of surge.
  • a method in accordance with claim 1 including the step of operating a back pressure valve in response to detected flow reversal so that the compressor is bypassed by the flowing material prior to the onset of surge.
  • a method in accordance with claim 1 including the step of operating a back pressure valve in response to detected flow reversal so that high pressures are relieved at the outlet side of the compressor to eliminate flow reversal in the boundary layer and thereby delay the onset of surge.
  • a surge detecting system comprising:
  • a velocity probe mounted to the compressor adjacent a wall thereof near its outlet.
  • said velocity probe having a flow direction sensing ability at a predetermined portion thereof, said predetermined portion being disposed within the boundary layer of material flowing through the compressor at thecompressor outlet adjacent said wall,
  • said predetermined portion also having a predetermined orientation with respect to the expected downstream direction of material flow in said boundary layer under nonsurge conditions to cause a detectable output indication from said velocity probe whenever said material flow substantially reverses in direction from said expected downstream direction, and indicating means connected with said probe for detecting an impending compressor surge condition in response to said output indication from said velocity probe indicating flow reversal of direction in said boundary layer which is, in turn, indicative of impending surge condition.
  • Apparatus in accordance with claim 6 including a bleed line extending between the compressor stage outlet and the compressor stage inlet, said bleed line having a valve positioned therein, said flow reversal indicating means functioning to operate said valve to bleed back a portion of the fluid at the outlet of the compressor back into the inlet when flow reversal occurs so as to eliminate flow reversal and delay the onset of surge conditions.
  • Apparatus in accordance with claim 6 including means responsive to said flow reversal indicating means for operating a back pressure valve for relieving high pressure conditions at the compressor stage outlet.
  • said velocity probe comprises a pressure sensing tube having an aperture therein oriented facing downstream of the desired flow in the compressor and wherein said flow reversal indicating means comprises a pressure sensing apparatus.

Abstract

A method and apparatus for detecting and controlling impending surge conditions in a compressor. A velocity probe is situated at a compressor outlet adjacent the compressor wall so as to be in the boundary layer of material flowing through the compressor adjacent the wall. Flow reversal in the boundary layer is detected as an indication of an impending surge condition. A bleed line can be connected so as to bleed off a portion of the boundary layer having a reversed flow and feed this portion back to the inlet of the compressor for delaying the onset of surge. The boundary layer flow reversal detection apparatus can also operate a back pressure valve so that the material flow bypasses the compressor when surge conditions are impending in the compressor.

Description

[ Aug. 26, 1975 METHOD AND APPARATUS FOR COMPRESSOR SURGE CONTROL [75] Inventor: Meherwan P. Boyce, College Station, Tex.
[73] Assignee: Howell Instruments, Inc., Fort Worth, Tex.
[22] Filed: Oct. 23, 1973 [21] Appl. N0.: 408,809
[52] US. Cl 415/1; 415/26 [51] Int. Cl. F04D 27/02; F04D 27/00 [58] Field of Search 4l5/l, ll, 26, 28; 60/3929, 3928 [56] References Cited UNITED STATES PATENTS 2,470,565 5/1949 Loss I 415/11 2,732,l25 l/l956 Ruby 60/3929 2,863,601 l2/l958 Torell 60/3929 2,930,520 3/1960 Abild 60/3929 2,978,166 4/l96l Hahn 415/28 2,986,327 5/1961 Huntcr 415/11 OTHER PUBLICATIONS D. C. Shepherd, Principles of Turbomachines, MacMillan Co., New York, 1956, TJ267.S35. W. H. Li & S. H. Lam, Principles of Fluid Mechanics,
Raw pwrzew wv wit-m4; 50265 vnmeissae CIA/7'68 Z/IVE Addison-Wesley Publishing Co., lnc., Reading, Mass,
W. H. Hughes & J. A. Brighton, Theory and Problems of Fluid Dynamics, McGrawI-Iill, Inc., 1967.
Primary ExaminerWilliam L. Freeh Assistant ExaminerLouis T. Casaregola Attorney, Agent, or Firm-Cushman, Darby & Cushman [5 7] ABSTRACT A method and apparatus for detecting and controlling impending surge conditions in a compressor. A velocity probe is situated at a compressor outlet adjacent the compressor wall so as to be in the boundary layer of material flowing through the compressor adjacent the wall. Flow reversal in the boundary layer is detected as an indication of an impending surge condition. A bleed line can be connected so as to bleed off a portion of the boundary layer having a reversed flow and feed this portion back to the inlet of the compressor for delaying the onset of surge. The boundary layer flow reversal detection apparatus can also operate a back pressure valve so that the material flow bypasses the compressor when surge conditions are impending in the compressor.
11 Claims, 4 Drawing Figures METHOD AND APPARATUS FOR COMPRESSOR SURGE CONTROL BACKGROUND OF THE INVENTION onset of surge and initiate corrective action because surge conditions in a compressor cancause great damage to a compressor. One of the methods which has been used in the prior art to detect surge is to detect pressure fluctuations in the compressor in order to indicate the onset of surge. This approach suffers the limitation in that different compressors have different signature patterns of pressure fluctuations and thus it is hard to standardize on any kind of detection apparatus.
OBJECTS AND SUMMARY OF THE INVENTION Accordingly, it is an object of this invention to provide a method and apparatus for surge detection which give a positive indication of impending surge conditions.
It is another object of this invention to provide such a method and apparatus for detecting impending surge which can be standardized and not vary in characteristics from compressor to compressor.
It is an additional object of this invention to provide a method and apparatus for detecting impending surge and including means for delaying the onset of surge.
Briefly, in accordance with one embodiment of the invention, a velocity probe is positioned at a compressor outlet near the wall of the compressor in the boundary layerof material flowing through the compressor adjacent to the wall. Flow reversal is detected in the boundary layer which is indicative of an impending surge condition.
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a diagrammatic view of a portion of a centrifugal compressor illustrating one impeller and illustrating flow patterns from the exit of the impeller before surge, near surge, and in a potential surge.
FIG. 2 is a diagrammatic illustration similar to FIG. 1 showing a flow reversal detection system in place in a centrifugal compressor and illustrating a bleed line for delaying the onset of surge.
FIG. 3 is a diagrammatic illustration of an embodiment of the invention as applied to axial flow compressors.
FIG. 4 is a diagrammatic illustration of one form of suitable probe for detecting flow reversal.
DESCRIPTION OF THE PREFERRED EMBODIMENTS Turning now to a consideration of FIG. 1, there is schematically shown a compressor 11 with one impeller 12 of the compressor being illustrated. The impeller 12 has an eye or entrance 12a and has an exit indicated by reference numeral 12b. The velocity profile or flow pattern of the material flowing throughthe compressor is indicated by curve 13a at the impeller exit 12b. The
flow pattern before occurrence of surge is indicated by curve 13a. Adjacent to the curve 130 there is a curve 13b, which indicates the velocity profile or flow pattern of the material flowing through the impeller when a surge condition is nearing. A curve 136 is shown disposed adjacent curve 13b and curve 130 is an indication of the velocity profile or flow pattern of the material flowing out the impeller exit 12b where there is a potential surge. A comparison of the curves 13a, l3b and 130 in FIG. 1 shows that as surge is approached, the velocity of the boundary layer changes from positive to zero and then to negative. That is, there is a flow reversal in the boundary layer at the exit of the impeller as a surge condition is approached. The succession of flow patterns as indicated by the curves 13a through 13c has been confirmed by actual tests on compressors.
Turning now to a consideration of FIG. 2, there is shown apparatus in accordance with the invention and for practicing the method of the invention installed on a compressor. The same reference numerals are used in FIG. 2 to refer to corresponding portions of the compressor as are used in describing the compressor of FIG. 1. Thus the compressor 11 diagrammatically illustrated in FIG. 2 has an impeller 12 with an eye or inlet 12a and an exit 12b. Situated in the wall of the compressor 11 adjacent the impeller exit is a velocity probe I4. The velocity probe 14 is connected to a flow reversal detector 16. The velocity probe 14, together with the flow reversal detector 16, is adapted to sense the velocity and direction of flow of the boundary layer adjacent the compressor wall at the impeller exit. As described hereinafter, the velocity probe 14 may comprise any suitable conventional velocity probe, such as a pitot tube, hot wire anemometer, etc. As will be appreciated, such conventional probes have a flow direction sensing ability at a predetermined portion thereof which may be positioned within the boundary layer and oriented with respect to the expected downstream boundary flow direction so as to produce an output indication whenever the actual boundary layer flow direction substantially reverses. For example, a simple tube having an aperture therein with the aperture positioned to face downstream (i.e., away from the impeller exit) may be provided for achieving this function as shown schematically in the drawings. At high velocities of the boundary layer (no surge), suction pressure is measured by the probe 14 and the flow reversal detector 16 can, for a simple embodiment, simply be a mercury manometer for providing an indication of the pressure. As the flow pattern of the boundary layer nears surge, the relative pressure (i.e. relative to a static pressure) sensed by the probe 14 would drop to zero; that is, the boundary layer would have zero velocity. As a potential surge then occurs flow reversal takes place within the boundary layer and the probe 14 senses a positive pressure. Thus the probe 14, together with an appropriate flow reversal detector 16, detects flow reversal in the boundary layer to provide an indication of impending surge conditions within the compressor.
FIG. 2 also illustrates another feature in accordance with one embodiment of the invention in which bleed can be controlled through a control circuit 19 actuated versal, which it will be recalledis indicative of impend ing surge in the compressor, is obtainedat the flow reversal detector 16. The flow reversal detector 16 then actuatesthrough a control circuit 19 the valve 18 l which opens the bleed line 17 so that a portion of-the flow reversed boundary layer is fed backfrom the outlet orexit of the compressor back into the eye or inlet of the impeller 12. Bleeding back this high pressure boundary layer material when flow reversa l has occurred back to the inlet ofthe compressor relieves the high pressure at the boundary layer at the exit of the compressor and thereby stops flow reversal. This has the effect of delaying the onset of surgeconditions iii the compressor. In accordance with the invention, it is only necessary to feed backthr ough the bleed line a relatively small portion of the high pressure material (air, for example) at the impeller exit. In actual tests in accordance with the invention, it has been found that bleeding back 2 percent to 3 percent of the high pressure material at the impeller exit does have the effect of delaying the onset of surge. Of course, besides the automatic actuation of the bleed line 17 through the valve 18, the flow reversal detector 16 can also provide anappropriate warning to an operator or control center of impending surge in the compressorx Referring now to FIG. 3, there is shown a schematic embodimentof application of the invention to an axial flow compressor. Thus, the axial flow compressorll schematically illustrated in FIG. 3 includes a stator 22 the case of the centrifugal compressor illustrated in FIGS. 1. and 2; that is, the probe 24 detects reversal of flow in the boundary l ayer at the exit side of the rotor blade tip 23a. The probe 24, as before, is connectedto a flow reversal detector 26. As was the case in the previous embodiment discussed herein, the velocity probe 24may comprise a pitot tube,l iot wire anemometer, or
other conventionaldevice having a flow direction sensing ability at a predetermined portion thereof. For example, a simple tube may be used having a hole therein facing downstream with the flow reversal detector in its simplest form being a pressure manometer. ln accordance with one embodiment of the invention, as applied to axial flow compressors, a bleed line 27 is provided having a valve 28 therein. The valve 28 maybe actuated through a control circuit 29 by the'flow reversal detector 2 6. Thus, when the flow reversal detector 26 detects aflow reversal int he boundary layer adjacent the exit side of the rotorblade tip 23a, the valve 28 is opened so that the high pressure material at the exit side of the rotor blade tip is bled back through bleed line 27 to the inlet side of the rotor blade tip 23a. This relieves the high pressure at the exit side of therotor blade tip, stops flow reversal, and therefore delays the onset of surge. As before, the bleed line 27 may be of such a diameter so that 2-3 percentof the high pressure material at the exit side of the rotor blade tip is fedback into the inlet side of the rotorblade tip. 0 f
course, the valve 28 may be anadjustable valve so that varying amounts of feedback are provided depending practicing the rnethod ofi the invention. Thus, in FIG.
4, a probe is shown which comprises a simple tube 3l having an aperture 32 in one side thereof. The probe is positioned in the compressor such that the aperture faces Jdownstream in "the direction of desired flow through the compressor. Thus, any positive pressure (relative to a'static pressure) detected as being exerte'd throughthe aperture 32 i'sanindication of flow reversal. :The velocity probegives an indication of flow direction. In accordance w ith the invention the probe is adjacent the exit of a compressor stage are situated so asto be in the .boundary-,layer. of the flow at the compressor stage exit. Thus, in accordance with one particular embodimentjof'ithe inventionyfor a centrifugal compressor having a Z-inchthroat orimpeller exit, a probe-was provided which extended 0.2 inch into the compressor throat This placed theprobe in the boundary layer of the material flow. at the compressor throat. Of course, there are larger boundary layers for compressors having larger throats-and smaller boundary layers forcompressors having smaller throats. The size of the boundary layer is also dependent upon the pressuresv and speeds atwhich the compressor is operated. It is considered within the skill of those knowledgable in the art to determine for. a particular instance where prevent surge, or the backpressurevalve can exhaust air, for example, from the outlet side of the compressor to the atmosphere through a blow off system so that there is always enough air passing through the compressorto keep itin its stablerange away from surge conditions. Typically a back pressure valve is operated by means of a static pressure probe placed some place adjacent the exit side of the compressor. Thus, when thestatic pressure probe detects a build-up of high pressure to an extent that might be deleterious to the compressor, the back pressure valve is actuated to eithe'r'bypass the compressor completely or to exhaust the high pressure air at the outletv side of the machine to the atmosphere so as to lower the pressure on the outlet side of the machine-in accordance with one aspectof the present invention, such. a back pressure valve can be operated-through the flow reversal detecting mechanism of the presentinvention. That is, the back pressure valve isactuated dependent upon flow reversal detected in the boundary layer adjacent the exit side of the machinerather than the static pressure build-up detected by some variety of static pressure probe. Detecting flow reversal for operating .the back pressure valve is a much' more accurate means for preventing surge conditions'than depending upon a static pressure condition, which canvary from compressor to compressor. 7
Thus, while there have been described particular embodiments of the invention by way of example, it is obvious that variations and modifications of the particular disclosed embodiments may be made by those skilled in the art without departing from the true spirit and scope of the invention.
What is claimed is:
l. A method of detecting an impending surge condition in a compressor comprising:
positioning a velocity probe adjacent the wall of the compressor outlet, said velocity probe having a flow direction sensing ability at a predetermined portion thereof,
positioning said predetermined portion of said velocity probe within the boundary layer of material flowing through the compressor and adjacent the wall of the compressor,
orienting said predetermined portion of said velocity probe at a predetermined orientation with respect to the expected downstream direction of material flow in said boundary layer under non-surge conditions to cause a detectable output indication from said velocity probe whenever said material flow substantially reverses in direction from said expected downstream direction, and
detecting an impending compressor surge condition in response to said output indication from said velocity probe indicating flow reversal in the boundary layer which is, in turn, indicative of impending surge conditions.
2. A method in accordance with claim 1 including the step of bleeding off a portion of the boundary layer at the compressor outlet back into the compressor inlet in response to detected flow reversal in order to delay the onset of surge.
3. A method in accordance with claim 1 including the step of operating a back pressure valve in response to detected flow reversal so that the compressor is bypassed by the flowing material prior to the onset of surge.
4. A method in accordance with claim 1 including the step of operating a back pressure valve in response to detected flow reversal so that high pressures are relieved at the outlet side of the compressor to eliminate flow reversal in the boundary layer and thereby delay the onset of surge.
5. A method in accordance with claim 2 in which 5 percent or less of the output of the compressor is bled back into the input in order to delay the onset of surge.
6. In a compressor including a stage having an inlet and an outlet and adapted for fluid flow through the compressor, a surge detecting system comprising:
a velocity probe mounted to the compressor adjacent a wall thereof near its outlet.
said velocity probe having a flow direction sensing ability at a predetermined portion thereof, said predetermined portion being disposed within the boundary layer of material flowing through the compressor at thecompressor outlet adjacent said wall,
said predetermined portion also having a predetermined orientation with respect to the expected downstream direction of material flow in said boundary layer under nonsurge conditions to cause a detectable output indication from said velocity probe whenever said material flow substantially reverses in direction from said expected downstream direction, and indicating means connected with said probe for detecting an impending compressor surge condition in response to said output indication from said velocity probe indicating flow reversal of direction in said boundary layer which is, in turn, indicative of impending surge condition.
7. Apparatus in accordance with claim 6 including a bleed line extending between the compressor stage outlet and the compressor stage inlet, said bleed line having a valve positioned therein, said flow reversal indicating means functioning to operate said valve to bleed back a portion of the fluid at the outlet of the compressor back into the inlet when flow reversal occurs so as to eliminate flow reversal and delay the onset of surge conditions.
8. Apparatus in accordance with claim 6 including means responsive to said flow reversal indicating means for operating a back pressure valve for relieving high pressure conditions at the compressor stage outlet.
9. Apparatus in accordance with claim 6 wherein said velocity probe comprises a pressure sensing tube having an aperture therein oriented facing downstream of the desired flow in the compressor and wherein said flow reversal indicating means comprises a pressure sensing apparatus.
10. Apparatus in accordance with claim 6 wherein said compressor stage is a centrifugal compressor stage and wherein said velocity probe is mounted adjacent the impeller exit of the compressor stage.
11. Apparatus in accordance with claim 6 wherein said compressor stage is an axial flow compressor stage and wherein said velocity probe is mounted adjacent the exit side of the rotor blade tips.

Claims (11)

1. A method of detecting an impending surge condition in a compressor comprising: positioning a velocity proBe adjacent the wall of the compressor outlet, said velocity probe having a flow direction sensing ability at a predetermined portion thereof, positioning said predetermined portion of said velocity probe within the boundary layer of material flowing through the compressor and adjacent the wall of the compressor, orienting said predetermined portion of said velocity probe at a predetermined orientation with respect to the expected downstream direction of material flow in said boundary layer under non-surge conditions to cause a detectable output indication from said velocity probe whenever said material flow substantially reverses in direction from said expected downstream direction, and detecting an impending compressor surge condition in response to said output indication from said velocity probe indicating flow reversal in the boundary layer which is, in turn, indicative of impending surge conditions.
2. A method in accordance with claim 1 including the step of bleeding off a portion of the boundary layer at the compressor outlet back into the compressor inlet in response to detected flow reversal in order to delay the onset of surge.
3. A method in accordance with claim 1 including the step of operating a back pressure valve in response to detected flow reversal so that the compressor is bypassed by the flowing material prior to the onset of surge.
4. A method in accordance with claim 1 including the step of operating a back pressure valve in response to detected flow reversal so that high pressures are relieved at the outlet side of the compressor to eliminate flow reversal in the boundary layer and thereby delay the onset of surge.
5. A method in accordance with claim 2 in which 5 percent or less of the output of the compressor is bled back into the input in order to delay the onset of surge.
6. In a compressor including a stage having an inlet and an outlet and adapted for fluid flow through the compressor, a surge detecting system comprising: a velocity probe mounted to the compressor adjacent a wall thereof near its outlet, said velocity probe having a flow direction sensing ability at a predetermined portion thereof, said predetermined portion being disposed within the boundary layer of material flowing through the compressor at the compressor outlet adjacent said wall, said predetermined portion also having a predetermined orientation with respect to the expected downstream direction of material flow in said boundary layer under nonsurge conditions to cause a detectable output indication from said velocity probe whenever said material flow substantially reverses in direction from said expected downstream direction, and indicating means connected with said probe for detecting an impending compressor surge condition in response to said output indication from said velocity probe indicating flow reversal of direction in said boundary layer which is, in turn, indicative of impending surge condition.
7. Apparatus in accordance with claim 6 including a bleed line extending between the compressor stage outlet and the compressor stage inlet, said bleed line having a valve positioned therein, said flow reversal indicating means functioning to operate said valve to bleed back a portion of the fluid at the outlet of the compressor back into the inlet when flow reversal occurs so as to eliminate flow reversal and delay the onset of surge conditions.
8. Apparatus in accordance with claim 6 including means responsive to said flow reversal indicating means for operating a back pressure valve for relieving high pressure conditions at the compressor stage outlet.
9. Apparatus in accordance with claim 6 wherein said velocity probe comprises a pressure sensing tube having an aperture therein oriented facing downstream of the desired flow in the compressor and wherein said flow reversal indicating means comprises a pressure sensing apparatus.
10. Apparatus in accordance with claim 6 wherein said compressor stage is a centriFugal compressor stage and wherein said velocity probe is mounted adjacent the impeller exit of the compressor stage.
11. Apparatus in accordance with claim 6 wherein said compressor stage is an axial flow compressor stage and wherein said velocity probe is mounted adjacent the exit side of the rotor blade tips.
US408809A 1973-10-23 1973-10-23 Method and apparatus for compressor surge control Expired - Lifetime US3901620A (en)

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US408809A US3901620A (en) 1973-10-23 1973-10-23 Method and apparatus for compressor surge control
US05/511,705 US3930742A (en) 1973-10-23 1974-10-03 Velocity probe for compressor surge control
DE19742448841 DE2448841A1 (en) 1973-10-23 1974-10-14 METHOD AND DEVICE FOR MONITORING FLASHBACKS IN A COMPRESSOR
CA211,528A CA1025694A (en) 1973-10-23 1974-10-16 Method and apparatus for compressor surge control
CH1385574A CH592819A5 (en) 1973-10-23 1974-10-16
FR7434959A FR2248427B1 (en) 1973-10-23 1974-10-17
GB45470/74A GB1481031A (en) 1973-10-23 1974-10-21 Method and apparatus for compressor surge control
JP49121867A JPS5073207A (en) 1973-10-23 1974-10-22

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GB (1) GB1481031A (en)

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US9382911B2 (en) 2013-11-14 2016-07-05 Danfoss A/S Two-stage centrifugal compressor with extended range and capacity control features
US20160215778A1 (en) * 2013-09-12 2016-07-28 Ebara Corporation Apparatus and method for alleviating and preventing cavitation surge of water supply conduit system
US9567942B1 (en) * 2010-12-02 2017-02-14 Concepts Nrec, Llc Centrifugal turbomachines having extended performance ranges
US20170198707A1 (en) * 2016-01-12 2017-07-13 Daikin Applied Americas Inc. Centrifugal compressor with hot gas injection
US20190024528A1 (en) * 2016-01-25 2019-01-24 Nuovo Pignone Tecnologie Srl Compressor train start-up using variable inlet guide vanes
US10962022B2 (en) * 2016-10-24 2021-03-30 Nuovo Pignone Tecnologie—S.R.L. Diaphragm for a centrifugal compressor
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US4504188A (en) * 1979-02-23 1985-03-12 Carrier Corporation Pressure variation absorber
US4662817A (en) * 1985-08-20 1987-05-05 The Garrett Corporation Apparatus and methods for preventing compressor surge
US4743161A (en) * 1985-12-24 1988-05-10 Holset Engineering Company Limited Compressors
US4930979A (en) * 1985-12-24 1990-06-05 Cummins Engine Company, Inc. Compressors
US4708584A (en) * 1986-10-09 1987-11-24 Rockwell International Corporation Shrouded inducer pump
US4930978A (en) * 1988-07-01 1990-06-05 Household Manufacturing, Inc. Compressor stage with multiple vented inducer shroud
US5456115A (en) * 1988-11-28 1995-10-10 Hitachi, Ltd. Method of counterflow through a pump and method of controlling the operation of a pump in a pumping installation
US4975024A (en) * 1989-05-15 1990-12-04 Elliott Turbomachinery Co., Inc. Compressor control system to improve turndown and reduce incidents of surging
US4976588A (en) * 1989-05-15 1990-12-11 Elliott Turbomachinery Co., Inc. Compressor control system to improve turndown and reduce incidents of surging
US5892145A (en) * 1996-12-18 1999-04-06 Alliedsignal Inc. Method for canceling the dynamic response of a mass flow sensor using a conditioned reference
US20030138317A1 (en) * 1998-12-10 2003-07-24 Mark Barnett Casing treatment for a fluid compressor
US6231301B1 (en) * 1998-12-10 2001-05-15 United Technologies Corporation Casing treatment for a fluid compressor
US6619909B2 (en) * 1998-12-10 2003-09-16 United Technologies Corporation Casing treatment for a fluid compressor
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US20020012586A1 (en) * 2000-02-23 2002-01-31 Bahram Nikpour Compressor
US6699008B2 (en) 2001-06-15 2004-03-02 Concepts Eti, Inc. Flow stabilizing device
US20050265822A1 (en) * 2002-10-24 2005-12-01 Peter Fledersbacher Method of operating a compressor near the compressor pumping limit and compressor
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US7608353B2 (en) * 2003-10-29 2009-10-27 Gm Global Technology Operations, Inc. Method for detecting compressor surge in a fuel cell system using a mass flow meter
US7025557B2 (en) 2004-01-14 2006-04-11 Concepts Eti, Inc. Secondary flow control system
US20050152775A1 (en) * 2004-01-14 2005-07-14 Concepts Eti, Inc. Secondary flow control system
US20060045772A1 (en) * 2004-08-31 2006-03-02 Slovisky John A Compressor including an aerodynamically variable diffuser
US8122724B2 (en) 2004-08-31 2012-02-28 Honeywell International, Inc. Compressor including an aerodynamically variable diffuser
US7780422B2 (en) 2004-10-07 2010-08-24 Ebm-Papst St. Georgen Gmbh & Co. Kg Assembly for transporting fluids
WO2009015635A3 (en) * 2007-07-31 2009-03-26 Mtu Aero Engines Gmbh Closed-loop control for a gas turbine with actively stabilized compressor
US20100196137A1 (en) * 2007-07-31 2010-08-05 Mtu Aero Engines Gmbh Closed-loop control for a gas turbine with actively stabilized compressor
US8550767B2 (en) 2007-07-31 2013-10-08 Mtu Aero Engines Gmbh Closed-loop control for a gas turbine with actively stabilized compressor
EP2080908A3 (en) * 2008-01-17 2011-07-13 Rolls-Royce Deutschland Ltd & Co KG Radial compressor with removal and return of air in the casing
US20120100011A1 (en) * 2009-06-05 2012-04-26 Johnson Controls Technology Company Control system
US11378088B2 (en) * 2009-06-05 2022-07-05 Johnson Controls Tyco IP Holdings LLP Control system for centrifugal compressor
US20110255963A1 (en) * 2010-04-19 2011-10-20 Chun Kyung Kim Centrifugal compressor
US8814499B2 (en) * 2010-04-19 2014-08-26 Korea Fluid Machinery Co., Ltd. Centrifugal compressor
US20110274537A1 (en) * 2010-05-09 2011-11-10 Loc Quang Duong Blade excitation reduction method and arrangement
WO2012060825A1 (en) * 2010-11-03 2012-05-10 Danfoss Turbocor Compressors B.V. Centrifugal compressor with fluid injector diffuser
CN103201462A (en) * 2010-11-03 2013-07-10 丹佛斯特波科尔压缩机有限公司 Centrifugal compressor with fluid injector diffuser
CN103201462B (en) * 2010-11-03 2015-08-05 丹佛斯公司 A kind of centrifugal compressor and refrigeration system
US10197064B2 (en) 2010-11-03 2019-02-05 Danfoss A/S Centrifugal compressor with fluid injector diffuser
US9567942B1 (en) * 2010-12-02 2017-02-14 Concepts Nrec, Llc Centrifugal turbomachines having extended performance ranges
US20120213627A1 (en) * 2011-01-25 2012-08-23 Jeffrey Carter Compressor
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CN102297149A (en) * 2011-09-08 2011-12-28 上海中科高等研究院 Device and method for widening stable operation area of centrifugal compressor, and centrifugal compressor
US20160032932A1 (en) * 2012-08-17 2016-02-04 Dresser-Rand Company System and method for detecting stall or surge in radial compressors4
US10371158B2 (en) * 2012-08-17 2019-08-06 Dresser-Rand Company System and method for detecting stall or surge in radial compressors
US10184481B2 (en) 2013-01-31 2019-01-22 Danfoss A/S Centrifugal compressor with extended operating range
US9157446B2 (en) 2013-01-31 2015-10-13 Danfoss A/S Centrifugal compressor with extended operating range
US20160215778A1 (en) * 2013-09-12 2016-07-28 Ebara Corporation Apparatus and method for alleviating and preventing cavitation surge of water supply conduit system
US11378084B2 (en) 2013-09-12 2022-07-05 Ebara Corporation Apparatus and method for alleviating and preventing cavitation surge of water supply conduit system
US9382911B2 (en) 2013-11-14 2016-07-05 Danfoss A/S Two-stage centrifugal compressor with extended range and capacity control features
US20160097297A1 (en) * 2014-10-07 2016-04-07 Cummins Ltd. Compressor and turbocharger
US20170198707A1 (en) * 2016-01-12 2017-07-13 Daikin Applied Americas Inc. Centrifugal compressor with hot gas injection
US10113553B2 (en) * 2016-01-12 2018-10-30 Daikin Applied Americas Inc. Centrifugal compressor with hot gas injection
US20190024528A1 (en) * 2016-01-25 2019-01-24 Nuovo Pignone Tecnologie Srl Compressor train start-up using variable inlet guide vanes
US11692452B2 (en) * 2016-01-25 2023-07-04 Nuovo Pignone Tecnologie—S.R.L. Compressor train start-up using variable inlet guide vanes
US10962016B2 (en) 2016-02-04 2021-03-30 Danfoss A/S Active surge control in centrifugal compressors using microjet injection
US10962022B2 (en) * 2016-10-24 2021-03-30 Nuovo Pignone Tecnologie—S.R.L. Diaphragm for a centrifugal compressor

Also Published As

Publication number Publication date
CA1025694A (en) 1978-02-07
JPS5073207A (en) 1975-06-17
DE2448841A1 (en) 1975-04-24
GB1481031A (en) 1977-07-27
CH592819A5 (en) 1977-11-15
FR2248427B1 (en) 1979-03-30
FR2248427A1 (en) 1975-05-16

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