US3292845A - Method for preventing surging of compressors - Google Patents

Method for preventing surging of compressors Download PDF

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US3292845A
US3292845A US348974A US34897464A US3292845A US 3292845 A US3292845 A US 3292845A US 348974 A US348974 A US 348974A US 34897464 A US34897464 A US 34897464A US 3292845 A US3292845 A US 3292845A
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controller
compressor
control valve
signal
proportional
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US348974A
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Antonius M Hens
Jelle A Landstra
Nicholaas C Maris
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Shell USA Inc
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Shell Oil Co
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F04—POSITIVE - DISPLACEMENT MACHINES FOR LIQUIDS; PUMPS FOR LIQUIDS OR ELASTIC FLUIDS
    • F04D—NON-POSITIVE-DISPLACEMENT PUMPS
    • F04D27/00—Control, e.g. regulation, of pumps, pumping installations or pumping systems specially adapted for elastic fluids
    • F04D27/02—Surge control
    • F04D27/0207—Surge control by bleeding, bypassing or recycling fluids

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  • the invention relates to a method and apparatus for protecting a centrifugal compressor in order to entirely or substantially prevent the so-called surging of the compressor.
  • Surging may occur in a compressor when, at a certain pump pressure, the gas velocity through the compressor becomes too low, or when, at a certain gas velocity the pressure becomes too high.
  • the compressor is provided with a 'by-pass or a blow-ofl? line, which during normal operation (i.e., when the gas load of the compressor is sufiiciently high), is closed by a control valve.
  • the valve is opened to a greater or lesser extent, so that the gas flow through the compressor increases and surging is avoided. Since the lay-passing or the blow-off of gas through the by-pass or the blow-olf line represents a loss in both power and gas, the valve is only opened when and to the amount necessary to avoid surging.
  • the invention now provides a method by means of which an eflective protection against surging is obtained, even when rapid load variations occur.
  • the controller also operates economically in that the control valve remains open or is opened no further than is necessary to avoid surging.
  • the through-put of the control valve is controlled by the output signal of a relay (auxiliary relay) to which two controllers are connected.
  • Each controller compares two meansured signals, one (Ap) being dependent on the gas flow through the compressor and being measured as a differential pressure signal across an orifice, a venturi or a similar device, the other (p) being dependent on the pressure level of the compressor.
  • One controller has only proportional action and moreover a relatively narrow proportional band, and the other controller has both proportional action and integral action and in addition a relatively wide proportional 'band.
  • the first-mentioned controller is set in such a manner that its operating level lies relatively near to the surge limit of the compressor, and the operating level of the second controller is further away from this surge limit and moreover outside the control range of the first controller.
  • the direction of action of each controller is such that decreasing Ap or increasing p correspond to the opening of the control valve, and the auxiliary relay causes the control valve to be controlled only by that signal which at any moment would cause the greatest opening of the control valve.
  • the difierential pressure is measured at the discharge side of the compressor.
  • the signal dependent on the pressure level is preferably obtained by measuring the discharge pressure of the compressor.
  • Good results are obtained by a combination of Ap measured at the suction side of the compressor (Ap with p measured at the discharge side of the compressor (p or vice versa (Ap and p In practice the best control is achieved by measuring both Ap and p at the discharge side of the compressor (thus with the combination A 2 and P2).
  • each controller is provided with such an amplifier to permit independent adjusting and setting of each controller.
  • an amplifier in one of the signal supply circuits (either for the signal p or for the signal Ap) of each controller is suflicient.
  • a similar result may be achieved by using a controller having in addition to proportional and integral action also derivative action to compare the signals Ap and p.
  • the output signal of this controller controls the control valve and in this case also the direction of action is such that decreasing Ap or increasing p corresponds to the opening of the control valve.
  • the controller should have a relatively wide proportional bands, on the order of IOU-250%.
  • the operating level of the controller can be placed relatively near to the surge limit of the compressor.
  • an adjustable amplifier is inserted in order to be able to adjust the operating level with respect to the surge limit.
  • the protection system according to the invention may use various operating media, for example hydraulical, pneumatical, or electrical; a pneumatic embodiment is often used. If a pneumatic embodiment is employed the output signal of the auxiliary relay, after amplification if necessary may be used in order to supply a signal to that part of the controller which produces the integral action with which one of the controllers is provided.
  • FIG. 1 is a block diagram of a method for the compression of natural gas by means of a centrifugal compressor 1.
  • the gas to be compressed is supplied through a line 2 and leaves the compressor through a line 3.
  • the compressed gas is subsequently cooled by means of a cooler 4 and is freed in a separator 5 from any condensate which may have been formed.
  • the condensate is discharged through a line 6 and the compressed .gas through lines 7 and 8,"
  • an orifice 11 is inserted, which is connected to a diiferential pressure meter 12.
  • This meter produces a pneumatic signal (Ap which is proportional to the differential pressure occurring across the orifice.
  • a pressure sensing device 13 is likewise connected to the line 3 and produces the pneumatic signal 7 which is proportionate to the discharge pressure of the compressor.
  • the output signal of the pressure sensing device 13 is passed to two amplifying pneumatic relays 14a, 14b; the output signal of the amplifying relay 14a is supplied to a pneumatic controller 15a and the output signal of amplifying relay 14b passes to a pneumatic controller 15b.
  • the amplifying relays 14a and 1412 may be Foxboro model M56-6 computing relays manufactured by the Foxboro C0. of Foxboro, Massachusetts.
  • This type of relay supplies an output equal to A times an input signal where.
  • A is a manually set constant.
  • Each of the controllers 15a and 1517 also receives a signal from the differential pressure meter 12.
  • the controller 15a may be a Foxboro model M58 controller with proportional action. Accordingly, in controller 15a the differential pressure signal is compared with A -p whereas in controller 15b the differential pressure signal is compared with A -p
  • the controller 15b may be a Foxboro model M58 Batch Stabil'og Controller having proportional and integral (reset) actions.
  • a and A are the set values of the amplifying relays 14a and 14b respectively.
  • the controller 15a has only proportional action and has moreover a relatively narrow proportional band (for example the controller b on the other hand has both proportional and integral action and moreover a relatively wide proportional band (for example 100 to 250%).
  • the combination relay 14a and controller 15a have been so set that the operating level of controller 15a is relatively near to the surge limit of the compressor 1; the. combination relay 14b and controller 15b have been so set that the operating level of controller 15b is further away from the surge limit than that of controller 15a and moreover lies outside the control range of the controller 15a.
  • the output signals of the controllers'15a and 15b are passed to an auxiliary relay or auctioneering circuit 16 which only .allows the signal to pass through which at any moment would cause the greatest opening of the control valve 10.
  • the auxiliary relay 16 may be a Minneapolis-Honeywell model R-048B Diverting Relay manufactured by Minneapolis-Honeywell Co. of Minneapolis, Minnesota.
  • the output signal 17 of the auxiliary relay 16 controls the control valve 10,
  • the controllers and associated devices are adjusted so that as long as Ap gAp the control valve remains closed.
  • A12 falls below the value A-p (for example owing to the face that no gas or less gas than usual is withdrawn at 8)
  • the control valve is opened to the extent required to prevent surging of the compressor.
  • the signal pressure ' is in general so chosen that when the signal pressure decreases the valve 10 is opened. This also means that the relay 16 in the present embodiment always transmits the smaller of the two signals from the controllers 15a, 15b.
  • the part of the controller 15b which relates to the integral action thereof is preferably supplied by the output signal of the auxiliary relay 16. To this end the figure 18 to this part of the controller 15b. This results in a,
  • controller 15b If the load of the compressor 1 (insofar as it concerns the gas discharge at 8) approaches the surge limit, the controller 15b first comes into action since its relevant operating level is the first to be exceeded. Since the operating level of controller 15b can be placed relatively close to the surge limit the operation of the compressor installation remains economic; for losses as a result of by-passing of gas through the by-pass do not occur as long as the operating level of controller 15b (insofar as it concerns the gas discharge at 8) is not exceeded. The control valve is only slightly opened when the operating level.
  • controller 15b ensures that even I when the compressor must operate permanently with a more or less widely opened control valve, nodifierence.
  • control system said method comprising:
  • An apparauts for protecting a centrifugal compressor from surging comprising:
  • pressure detecting means communicating with the flow stream of the compressor, said pressure detecting means measuring the flow through the compressor and a pressure level;
  • a first controller having a narrow band proportional action, said pressure detecting means being coupled to said first controller to compare said measured flow with said measured pressure level;
  • said pressure detecting means being coupled to said second controller to .5 6 compare said measured flow with said measured pres- References Cited by the Examiner sure level; an auctioneering circuit, said first and second oon- UNITED STATES PATENTS trollers being coupled to said auctioneering circuit 2,490,188 12/1949 Ziebolz 230-415 to pass the signal from the controller that results 5 3,009,631 11/1961 Dimmock 230-115 in the largest control action; 3,047,210 7/1962 Best 230-415 a by-pass line communicating with the discharge and suction sides of said compressor, a flow control FOREIGN PATENTS valve disposed to control flow through said by-pass 1,277,119 0 1 Franceline, said auctioneering circuit being coupled to said 10 control valve to position said control valve.
  • LAURENCE V. EFNER Primary Examiner.

Description

Dec. 20, 1966 HENS ETAL 3,292,845
METHOD FOR PREVENTING SURGING OF COMPRESSORS File'd March 5, 1964 DIFFERENTIAL PRESSURE I SENSOR I I PRESSURE l f 1 I I4b I I I40 4 v AMPLIFYING AMPLIFYING RELAY RELAY k 1 I V I50 K CONTROLLER q I6 I L 7 INVENTORS:
A. M. HENS J. A. LANDSTRA N. C, MARIS BYMZ M THEIR ATTORNEY United States Patent 3,292,845 METHOD FOR PREVENTING SURGING OF COMPRESSORS Antonius M. Hens, The Hague, Jelle A. Landstra, Amsterdam, Netherlands, and Nicolaas C. Maris, Curacao, Netherlands Antilles, assignors to Shell Gil Company, New York, N.Y., a corporation of Delaware Filed Mar. 3, 1964, Ser. No. 348,974 Claims priority, application Netherlands, Mar. 6, 1963,
2 Claims. (Cl. 230-115) The invention relates to a method and apparatus for protecting a centrifugal compressor in order to entirely or substantially prevent the so-called surging of the compressor. Surging may occur in a compressor when, at a certain pump pressure, the gas velocity through the compressor becomes too low, or when, at a certain gas velocity the pressure becomes too high. In order to counteract this surging the compressor is provided with a 'by-pass or a blow-ofl? line, which during normal operation (i.e., when the gas load of the compressor is sufiiciently high), is closed by a control valve. When the possibility of surging arises, the valve is opened to a greater or lesser extent, so that the gas flow through the compressor increases and surging is avoided. Since the lay-passing or the blow-off of gas through the by-pass or the blow-olf line represents a loss in both power and gas, the valve is only opened when and to the amount necessary to avoid surging.
It has already been proposed to operate the control valve by a control system, to which signals dependent on the pressure level of the compressor and of the gas flow through the compressor are supplied. Thus it has been suggested, for example that a signal proportional to the discharge pressure of the compressor be compared in a control system with the sum of two signals, one of which depends on the flow rate of the gas feed and the other being dependent on the flow rate of the gas stream in the by-pass. The control system used is a single controller having only integral action. Such a system operates slowly and provides no protection against surging when rapid load variations occur. In the case of a system having proportional action a relatively wide proportional band is required to ensure stable operation but this means that the compressor unit can only operate economically (i.e., with closed control valve) when the load exceeds to a large extent the surge limit of the compressor.
The invention now provides a method by means of which an eflective protection against surging is obtained, even when rapid load variations occur. The controller also operates economically in that the control valve remains open or is opened no further than is necessary to avoid surging.
According to the invention the through-put of the control valve is controlled by the output signal of a relay (auxiliary relay) to which two controllers are connected. Each controller compares two meansured signals, one (Ap) being dependent on the gas flow through the compressor and being measured as a differential pressure signal across an orifice, a venturi or a similar device, the other (p) being dependent on the pressure level of the compressor. One controller has only proportional action and moreover a relatively narrow proportional band, and the other controller has both proportional action and integral action and in addition a relatively wide proportional 'band. The first-mentioned controller is set in such a manner that its operating level lies relatively near to the surge limit of the compressor, and the operating level of the second controller is further away from this surge limit and moreover outside the control range of the first controller. The direction of action of each controller is such that decreasing Ap or increasing p correspond to the opening of the control valve, and the auxiliary relay causes the control valve to be controlled only by that signal which at any moment would cause the greatest opening of the control valve.
Preferably the difierential pressure is measured at the discharge side of the compressor. The signal dependent on the pressure level is preferably obtained by measuring the discharge pressure of the compressor. Good results are obtained by a combination of Ap measured at the suction side of the compressor (Ap with p measured at the discharge side of the compressor (p or vice versa (Ap and p In practice the best control is achieved by measuring both Ap and p at the discharge side of the compressor (thus with the combination A 2 and P2).
In order to set the operating level of each controller at the proper level (the operating level being Ap=Ap, where A represents a constant) an amplifier is inserted in at least one of the signal supply lines of each controller. By adjusting the amplifier the value of the constant A just mentioned may be altered and thereby adjust the operating level of the controller with respect to the surge limit of the compressor. In general each controller is provided with such an amplifier to permit independent adjusting and setting of each controller. As a rule an amplifier in one of the signal supply circuits (either for the signal p or for the signal Ap) of each controller is suflicient.
A similar result may be achieved by using a controller having in addition to proportional and integral action also derivative action to compare the signals Ap and p. The output signal of this controller controls the control valve and in this case also the direction of action is such that decreasing Ap or increasing p corresponds to the opening of the control valve. In order to ensure a stable operation the controller should have a relatively wide proportional bands, on the order of IOU-250%. The operating level of the controller can be placed relatively near to the surge limit of the compressor. In at least one of the signal supply circuits an adjustable amplifier is inserted in order to be able to adjust the operating level with respect to the surge limit.
The protection system according to the invention may use various operating media, for example hydraulical, pneumatical, or electrical; a pneumatic embodiment is often used. If a pneumatic embodiment is employed the output signal of the auxiliary relay, after amplification if necessary may be used in order to supply a signal to that part of the controller which produces the integral action with which one of the controllers is provided.
The invention will now be further illustrated with reference to the accompanying drawing. The figure is a block diagram of a method for the compression of natural gas by means of a centrifugal compressor 1. The gas to be compressed is supplied through a line 2 and leaves the compressor through a line 3. The compressed gas is subsequently cooled by means of a cooler 4 and is freed in a separator 5 from any condensate which may have been formed. The condensate is discharged through a line 6 and the compressed .gas through lines 7 and 8,"
connected to the discharge side of the compressor at an earlier point, for example, just before the cooler 4, instead of after the separator 5 as is now the case.
In the line 3 an orifice 11 is inserted, which is connected to a diiferential pressure meter 12. This meter produces a pneumatic signal (Ap which is proportional to the differential pressure occurring across the orifice. A pressure sensing device 13 is likewise connected to the line 3 and produces the pneumatic signal 7 which is proportionate to the discharge pressure of the compressor. The output signal of the pressure sensing device 13 is passed to two amplifying pneumatic relays 14a, 14b; the output signal of the amplifying relay 14a is supplied to a pneumatic controller 15a and the output signal of amplifying relay 14b passes to a pneumatic controller 15b. The amplifying relays 14a and 1412 may be Foxboro model M56-6 computing relays manufactured by the Foxboro C0. of Foxboro, Massachusetts. This type of relay supplies an output equal to A times an input signal where. A is a manually set constant. Each of the controllers 15a and 1517 also receives a signal from the differential pressure meter 12. The controller 15a may be a Foxboro model M58 controller with proportional action. Accordingly, in controller 15a the differential pressure signal is compared with A -p whereas in controller 15b the differential pressure signal is compared with A -p The controller 15b may be a Foxboro model M58 Batch Stabil'og Controller having proportional and integral (reset) actions. In this case A and A are the set values of the amplifying relays 14a and 14b respectively. The controller 15a has only proportional action and has moreover a relatively narrow proportional band (for example the controller b on the other hand has both proportional and integral action and moreover a relatively wide proportional band (for example 100 to 250%). The combination relay 14a and controller 15a have been so set that the operating level of controller 15a is relatively near to the surge limit of the compressor 1; the. combination relay 14b and controller 15b have been so set that the operating level of controller 15b is further away from the surge limit than that of controller 15a and moreover lies outside the control range of the controller 15a. The output signals of the controllers'15a and 15b are passed to an auxiliary relay or auctioneering circuit 16 which only .allows the signal to pass through which at any moment would cause the greatest opening of the control valve 10. The auxiliary relay 16 may be a Minneapolis-Honeywell model R-048B Diverting Relay manufactured by Minneapolis-Honeywell Co. of Minneapolis, Minnesota. The output signal 17 of the auxiliary relay 16 controls the control valve 10, The controllers and associated devices are adjusted so that as long as Ap gAp the control valve remains closed. As soon as A12 falls below the value A-p (for example owing to the face that no gas or less gas than usual is withdrawn at 8), the control valve is opened to the extent required to prevent surging of the compressor. In the pneumatic embodiment the signal pressure 'is in general so chosen that when the signal pressure decreases the valve 10 is opened. This also means that the relay 16 in the present embodiment always transmits the smaller of the two signals from the controllers 15a, 15b.
The part of the controller 15b which relates to the integral action thereof is preferably supplied by the output signal of the auxiliary relay 16. To this end the figure 18 to this part of the controller 15b. This results in a,
more rapid operation of the integral action.
The operation of the two controllers is as follows:
If the load of the compressor 1 (insofar as it concerns the gas discharge at 8) approaches the surge limit, the controller 15b first comes into action since its relevant operating level is the first to be exceeded. Since the operating level of controller 15b can be placed relatively close to the surge limit the operation of the compressor installation remains economic; for losses as a result of by-passing of gas through the by-pass do not occur as long as the operating level of controller 15b (insofar as it concerns the gas discharge at 8) is not exceeded. The control valve is only slightly opened when the operating level.
is only slightly exceeded, so that the losses are small.
If, however, a further change in the load brings the compressor closer to or in the danger area, the other con- I troller 15a can immediately come into operation and Without controller 15a there is,
open the control valve. however, a great risk of surging of the compressor, since the controller 15b, as a result of the wide proportional band and the action resulting from the integral action would not be able to open the control valve 10 in time..
If only a controller of the type 15a, i.e., with a narrow proportional band, were employed, an unstable control I This need is avoided since eventually the controller 15b reassumes control, viz. as soon as the inte-,
would result.
gral action of this controller has been able to build up a signal of suitable magnitude. Finally, it is pointed out. that the integral action of controller 15b ensures that even I when the compressor must operate permanently with a more or less widely opened control valve, nodifierence.
between measured value and set value occurs which could otherwise lead to surging of the compressor.
While pnuematic system has been described in detail,
other systems could be used as for example electronic or combination electronic pneumatic. When electronic,
systems are used, operational amplifiers with proper feedback circuits could be substituted for the dividing and controller circuits.
We claim as our invention: 1.- A method for protecting a centrifugal compressor from surging by using a by-pass line having a control valve disposed to control the flow through the by-pass line,
the position of the control valve being controlled by a.
control system, said method comprising:
measuring both the gas flow through the compressor and a pressure level of the compressor flow;
comparing the measured gas flow with the measured,
opening said control valve in response to the one.
signal.
2. An apparauts for protecting a centrifugal compressor from surging comprising:
pressure detecting means communicating with the flow stream of the compressor, said pressure detecting means measuring the flow through the compressor and a pressure level;
a first controller having a narrow band proportional action, said pressure detecting means being coupled to said first controller to compare said measured flow with said measured pressure level;
a second controller having a broad band proportional,
action and integral action, said pressure detecting means being coupled to said second controller to .5 6 compare said measured flow with said measured pres- References Cited by the Examiner sure level; an auctioneering circuit, said first and second oon- UNITED STATES PATENTS trollers being coupled to said auctioneering circuit 2,490,188 12/1949 Ziebolz 230-415 to pass the signal from the controller that results 5 3,009,631 11/1961 Dimmock 230-115 in the largest control action; 3,047,210 7/1962 Best 230-415 a by-pass line communicating with the discharge and suction sides of said compressor, a flow control FOREIGN PATENTS valve disposed to control flow through said by-pass 1,277,119 0 1 Franceline, said auctioneering circuit being coupled to said 10 control valve to position said control valve. LAURENCE V. EFNER, Primary Examiner.

Claims (1)

1. A METHOD FOR PROTECTING A CENTRIFUGAL COMPRESSOR FROM SURGING BY USING A BY-PASS LINE HAVING A CONTROL VALVE DISPOSED TO CONTROL THE FLOW THROUGH THE BY-PASS LINE, THE POSITION OF THE CONTROL VALVE BEING CONTROLLED BY A CONTROL SYSTEM, SAID METHOD COMPRISING: MEASURING BOTH THE GAS FLOW THROUGH THE COMPRESSOR AND A PRESSURE LEVEL OF THE COMPRESSOR FLOW; COMPARING THE MEASURED GAS FLOW WITH THE MEASURED PRESSURE LEVEL TIMES A FIRST CONSTANT IN A FIRST CONTROLLER HAVING ONLY A NARROW PROPORTIONAL ACTION TO OBTAIN A FIRST SIGNAL; COMPARING THE MEASURED GAS FLOW WITH THE MEASURED PRESSURE LEVEL TIMES A SECOND CONSTANT IN A SECOND CONTROLLER HAVING A BROAD PROPORTIONAL AND INTEGRAL ACTION TO OBTAIN A SECOND SIGNAL; COMPARING SAID FIRST AND SECOND SIGNALS TO OBTAIN THE ONE OF SAID FIRST AND SECOND SIGNALS THAT WILL CAUSE THE LARGEST OPENING OF THE CONTROL VALVE; OPENING SAID CONTROL VALVE IN RESPONSE TO THE ONE SIGNAL.
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Cited By (22)

* Cited by examiner, † Cited by third party
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US3411702A (en) * 1967-03-13 1968-11-19 Carrier Corp Controlling gas compression systems
US3737246A (en) * 1971-07-30 1973-06-05 Mitsui Shipbuilding Eng Control method of compressors to be operated at constant speed
US3767318A (en) * 1971-05-10 1973-10-23 Mitsui Shipbuilding Eng Method of controlling multi-casing variable speed compressors
US3876326A (en) * 1974-01-30 1975-04-08 Simmonds Precision Products Surge control system
US3963367A (en) * 1974-08-21 1976-06-15 International Harvester Company Turbine surge detection system
US4135854A (en) * 1976-12-16 1979-01-23 Westinghouse Electric Corp. Control system for variable pitch axial fan for utility boiler
US4139328A (en) * 1977-05-25 1979-02-13 Gutehoffnungshitte Sterkrade Ag Method of operating large turbo compressors
US4164034A (en) * 1977-09-14 1979-08-07 Sundstrand Corporation Compressor surge control with pressure rate of change control
US4164033A (en) * 1977-09-14 1979-08-07 Sundstrand Corporation Compressor surge control with airflow measurement
US4164035A (en) * 1977-09-14 1979-08-07 Sundstrand Corporation Surge control for variable speed-variable geometry compressors
US4203701A (en) * 1978-08-22 1980-05-20 Simmonds Precision Products, Inc. Surge control for centrifugal compressors
US4205941A (en) * 1977-05-16 1980-06-03 Office National D'etudes Et De Recherches Aerospatiales (O.N.E.R.A.) Methods and apparatuses for avoiding surging phenomena in compressors
US4230437A (en) * 1979-06-15 1980-10-28 Phillips Petroleum Company Compressor surge control system
US4413946A (en) * 1981-08-20 1983-11-08 Dresser Industries, Inc. Vented compressor inlet guide
US4452048A (en) * 1981-05-28 1984-06-05 Elliott Turbomachinery Company, Inc. Method and apparatus for starting an FCC power recovery string
US4464720A (en) * 1982-02-12 1984-08-07 The Babcock & Wilcox Company Centrifugal compressor surge control system
US4486142A (en) * 1977-12-01 1984-12-04 Naum Staroselsky Method of automatic limitation for a controlled variable in a multivariable system
EP0175445A1 (en) * 1984-08-20 1986-03-26 International Control Automation Finance S.A. Compressor surge control
US4618310A (en) * 1984-06-07 1986-10-21 Exxon Research & Engineering Co. Method of multi-stage compressor surge control
US4921399A (en) * 1989-02-03 1990-05-01 Phillips Petroleum Company Gas pipeline temperature control
US4930978A (en) * 1988-07-01 1990-06-05 Household Manufacturing, Inc. Compressor stage with multiple vented inducer shroud
WO2010110674A3 (en) * 2009-03-27 2011-04-14 Framo Engineering As Subsea system with subsea cooler and method for cleaning the subsea cooler

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GB2268228A (en) * 1992-06-24 1994-01-05 Rover Group A compressor surge control system.

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FR1277119A (en) * 1961-01-02 1961-11-24 Gutehoffnungshuette Sterkrade Device for automatic regulation of centrifugal compressors
US3047210A (en) * 1958-12-26 1962-07-31 United Aircraft Corp Compressor surge control

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US2490188A (en) * 1945-12-17 1949-12-06 Askania Regulator Co Control system
US3009631A (en) * 1957-04-30 1961-11-21 Power Jets Res & Dev Ltd Control devices for fluid pressure systems
US3047210A (en) * 1958-12-26 1962-07-31 United Aircraft Corp Compressor surge control
FR1277119A (en) * 1961-01-02 1961-11-24 Gutehoffnungshuette Sterkrade Device for automatic regulation of centrifugal compressors

Cited By (25)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3411702A (en) * 1967-03-13 1968-11-19 Carrier Corp Controlling gas compression systems
US3767318A (en) * 1971-05-10 1973-10-23 Mitsui Shipbuilding Eng Method of controlling multi-casing variable speed compressors
US3737246A (en) * 1971-07-30 1973-06-05 Mitsui Shipbuilding Eng Control method of compressors to be operated at constant speed
US3876326A (en) * 1974-01-30 1975-04-08 Simmonds Precision Products Surge control system
US3963367A (en) * 1974-08-21 1976-06-15 International Harvester Company Turbine surge detection system
US4135854A (en) * 1976-12-16 1979-01-23 Westinghouse Electric Corp. Control system for variable pitch axial fan for utility boiler
US4205941A (en) * 1977-05-16 1980-06-03 Office National D'etudes Et De Recherches Aerospatiales (O.N.E.R.A.) Methods and apparatuses for avoiding surging phenomena in compressors
US4139328A (en) * 1977-05-25 1979-02-13 Gutehoffnungshitte Sterkrade Ag Method of operating large turbo compressors
US4164033A (en) * 1977-09-14 1979-08-07 Sundstrand Corporation Compressor surge control with airflow measurement
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