Multistage blowdown valve for a compressor system

Information

  • Patent Grant
  • 6283716
  • Patent Number
    6,283,716
  • Date Filed
    Thursday, October 21, 1999
    25 years ago
  • Date Issued
    Tuesday, September 4, 2001
    23 years ago
Abstract
A multi-stage blowdown valve is provided that uses a single control signal to simultaneously decompress the interstage and the second stage in a compressor system. The valve uses a series of sliding spools located linearly within a single bore to either prevent or allow fluid communication between two isolated passageways each having an inlet port and a discharge port. The valve, when used as a two stage blowdown valve in a multi-stage compressor system, can prevent compressor failure from occurring by ensuring that both the interstage and the second stages are decompressed, not only the interstage.
Description




FIELD OF THE INVENTION




The present application relates generally to a control valve. More specifically, it relates to a control valve used with compressors. Most specifically, it relates to a blowdown valve used with one or more oil free two stage screw compressors.




BACKGROUND OF THE INVENTION




Power consumption for a two stage dry (oil free) screw compressor is significantly reduced if the interstage and the second stage are both decompressed when the compressor is running unloaded. The problem with decompressing both stages, however, is that if the second stage blowdown valve malfunctions, the interstage blowdown valve will decompress the interstage and leave a large differential pressure on the second stage. This large differential pressure will raise the temperature of the second stage, possibly leading to compressor failure.




Previous compressors avoided the above problem by only unloading pressure from the second stage and not from both stages. The disadvantage, however, of unloading pressure only from the second stage when running the compressor unloaded is that the compressor's power consumption is greater than if both stages are unloaded.




Previous valve mechanisms for compressors have not adequately addressed the problem of simultaneously decompressing two isolated stages. U.S. Pat. No. 3,260,444 to Williams discloses valve mechanisms 104 and 110 which are controlled by the same control line 158 and operate in a similar manner. With valve 104, for example, control line 158 can move piston 130 to control whether pipe 106 is in communication with pipe 113 or pipe 102. The disadvantage with using these valves as blowdown valves for a two stage compressor is that if one valve should malfunction, the other valve may continue to function, possibly leading to compressor failure.




What is desired, therefore, is a reliable mechanism for a two stage dry screw compressor to decompress the interstage blowdown valve when the second stage blowdown valve is activated.




SUMMARY OF THE INVENTION




Accordingly, it is a primary object of the present invention to provide a blowdown valve for two stages of a multi-stage compressor such that the valve reliably decompresses the interstage when the second stage is decompressed.




The object of the invention is achieved by a blowdown valve that uses a single control signal to simultaneously decompress the interstage when the second stage is decompressed. The valve uses a series of sliding spools located linearly within a single bore to either prevent or allow fluid communication between two isolated passageways each having an inlet port and a discharge port. The valve can be reliably used as a two stage blowdown valve in a multi-stage compressor system.











BRIEF DESCRIPTION OF THE DRAWINGS





FIGS. 1A and 1B

each show an isometric cross-sectional view of the multistage blowdown valve of the present invention wherein the valve is in a closed position and an open position, respectively.





FIGS. 2A and 2B

each show an isometric cross-sectional view of a second embodiment of the multistage blowdown valve of the present invention wherein the valve is in a closed position and an open position, respectively.





FIGS. 3A and 3B

are front cross-sectional and side cross-sectional views, respectively, of the valve of FIG.


2


A.





FIG. 4

is a diagram showing the multistage blowdown valve of

FIGS. 1A and 1B

used with a compressor system.





FIG. 5

is a partial exploded view of the improved operative connections of a compressor system of

FIG. 4

used with the multistage blowdown valve of FIGS.


1


A and


1


B.











DETAILED DESCRIPTION OF THE INVENTION





FIGS. 1A and 1B

show the preferred embodiment for the multistage blowdown valve


50


of the present invention. Referring to these figures, the multistage blowdown valve


50


has two inlet ports,


26


,


30


and two discharge ports


28


,


32


. When the valve


50


is in a closed position as shown in

FIG. 1A

, all ports


26


,


28


,


30


and


32


are fluidly isolated from one another. When the valve


50


′ is in an open position as shown in

FIG. 1B

, inlet port


26


is in fluid communication only with discharge port


28


and inlet port


30


is in fluid communication only with discharge port


32


. It should be apparent that the valve


50


could operate in a reverse direction with the inlet ports


26


,


30


acting as discharge ports and discharge ports


28


,


32


acting as inlet ports.




The multistage blowdown valve


50


has a main bore


68


that can have a single diameter, but preferably has three diameters


68


′,


68


″ and


68


′″. Larger diameter


68


″ facilitates a larger volume of fluid passage through the valve and also prolongs the life of the rings


36


. Thus, for example, the life of ring


36


on spool


17


will be prolonged by avoiding repeated contact with the edges of inlet


26


as the spool reciprocates through the bore


14


. The smaller diameter


68


′″ helps to center the spring


24


within the bore


68


.




Within the bore


68


are a plurality of spools


60


,


62


, and


64


that linearly abut each other within the bore. Spools


60


and


64


each have a leg portion


42


bounded by two head portions


40


. Spool


62


has one head portion


40


bounded by two leg portions


42


. Adjacent spools are preferably coupled through the use of a mortise and a tenon. For example, each leg portion


42


of spool


62


can have a tenon


44


for fitting into a mortise


46


in a head portion of adjacent spools


60


and


64


.




Each head portion


40


further preferably has one or more rubber rings


36


inserted into a corresponding annular groove in the head portion such that each spool has airtight contact within the bore


14


as the spools move within the bore. The preferred type of ring used for ring


36


on the spools


16


-


20


or


60


,


62


and


64


are sometimes referred to as V-rings or U-rings which refer to the ability of the ring to fold when placed in a bore. The beneficial properties of the folding ring design include reduced sticking when the spools move in bore


14


, reduced sliding forces which allow lower and reapeatable control forces, improved sealing by the ring unfolding under pressure, and durability in that all of the desirable properties of the folding ring continue even after partial ring wear. The folding ring design also provides reliable operation when the spools move within the various diameters of the bore, for example, from diameter


14


′ to


14


″ or


68


′ to


68


″ and then back again.




The movement of spools


60


,


62


and


64


is controlled through pneumatic pressure applied against the head


40


of spool


64


through control port


34


. A spring


24


is located within the bore preferably at an opposite end of the control port


34


and extends laterally through the bore. The spring


24


abuts the head


40


from spool


60


to bias the valve to a closed position (see FIG.


1


A). Furthermore, spring means, such as compression spring


24


, counteracts the force of the control signal when the valve is in an open position (see

FIG. 1B

) and returns the blowdown valve to a closed position when the control signal is inactive. Alternatively, a tension spring and the control port could operate together at the same end of the bore, although those skilled in the art will realize that the control signal will operate in an inverse manner.





FIGS. 2A

,


2


B,


3


A and


3


B show another embodiment of the multistage blowdown valve


10


and


10


′ of the present invention.

FIG. 2B

shows the blowdown valve


10


′ in an open position and

FIGS. 2A

,


3


A and


3


B show the blowdown valve


10


in a closed position. The multistage blowdown valve


10


generally differs from multistage blowdown valve


50


in that it has a different configuration of spools


16


-


20


and does not have a smaller bore near the compression spring


24


. Instead, the multistage blowdown valve


10


has a main bore


14


with two diameters


14


′ and


14


″.




Referring to

FIGS. 2A

,


2


B,


3


A and


3


B, within bore


14


are a plurality of spools


16


-


20


that linearly abut each other within the bore. Each spool


16


-


20


has a leg portion


42


and a head portion


40


. Adjacent spools are preferably coupled through the use of a mortise and a tenon. For example, each head portion


40


of each spool


1620


can have a mortise


46


for fitedly receiving a tenon


44


on the leg portion


42


of the adjacent spool.




Although the present invention uses a plurality of spools within the bore, a single spool could also be used for the same function. However, a plurality of individual spools


16


-


20


or


60


,


62


and


64


are preferably used because they create a better seal by reacting to both the control pressure and internal pressures produced from the inlet ports. However, it is more preferable to use the spools


60


,


62


and


64


shown in

FIGS. 1A and 1B

because less linear deviations will occur during spool movement than with the configuration of spools


16


-


20


shown in

FIGS. 2A and 2B

.




It should be apparent to those skilled in the art that although the valve described herein is for a two-stage compressor, the valve can be adapted for compressors having three or more stages. To create a multi-stage blowdown valve, the valve described herein merely needs a longer bore, additional spools and extra inlet and discharge ports.





FIGS. 4 and 5

show the multistage blowdown valve used with a dual stage compressor system


1002


. The dual stage compressor system


1002


described herein is best described in U.S. patent application Ser. No. 09/179,523. The multistage blowdown valve


10


can have many applications and be used with many compressor systems. Thus, it should be understood that the compressor system


1002


described herein is merely given as an example and not meant to be limiting.




The operation of compressor system


1002


will now be briefly described. Referring to

FIG. 4

, the first-stage compressor


102


compresses the air to approximately thirty (30) psi. The compressed air is transmitted from the first stage compressor


102


into the innerstage piping


104


. The compressed air flows through the piping


104


to an innerstage cooler


106


. The cooler


106


drops the air temperature by approximately three hundred degrees Fahrenheit (300° F.). The cooler


106


is connected to the discharge of the first stage compressor


102


via a coupling plate


108


.




The compressed air is transmitted through the innerstage cooler


106


into another innerstage pipe


112


. The pipe


112


is connected to a moisture trap


110


via coupling plates


108


A. The moisture trap


110


is connected to the innerstage piping that leads to the second stage compressor


114


via innerstage pipe


116


, which is also connected to the moisture trap


110


via coupling plates


108


B.




This compressed air is transmitted into the inlet of the second stage compressor


114


. The second stage compressor


114


compresses the air approximately another seventy (70) psi, which brings the air up to approximately one hundred (100) psi. The compressed air is transmitted from the second stage compressor


114


into the second stage compressor discharge pipe


118


. The pipe


118


is connected to another discharge pipe


118


A leading to a compressor package discharge cooler


120


. The cooler


120


again drops the temperature of the compressed air transmitted therethrough by approximately three hundred degrees Fahrenheit (300° F.).




Innerstage pipe


116


has a bung


150


welded thereto, which connects the innerstage pipe


116


to the inlet port


26


of the multistage blowdown valve


10


. The connection to inlet port


26


is through a pipe elbow


151


, pipe nipple


152


, pipe coupling


153


, and pipe nipple


154


. A muffler


450


is attached to the discharge port


28


of the blowdown valve


10


. The purpose of the muffler


450


is to reduce the amount of noise that would be created when any trapped air pressure is vented to atmosphere.




Discharge pipe


130


B is attached to the moisture trap


126


, has a T shaped bung


170


A welded thereto, and has a package temperature probe


2010


is located within it. One end of the T-shaped bung


170


A has one end of a pipe elbow


128


A coupled thereto. The other end of the pipe elbow


128


A is coupled to the discharge pipe


130


A. A pipe nipple


171


is connected to the other end of the bung


170


A, which is threaded onto a coupling


172


, which is connected to pipe nipple


173


. The inlet port


30


of the multistage blowdown valve


10


is connected to the pipe nipple


173


. The discharge port


32


of valve


10


has an exhaust muffler


440


operatively connected thereto. The muffler


440


reduces the amount of noise created when any trapped air pressure is vented to atmosphere.




The multistage blowdown valve


10


of the present invention will exhaust any trapped pressure at shutdown or unload of the two stage compressor


1002


that might be trapped in innerstage pipe


116


and in the discharge piping


130


B from the second stage compressor


114


. Due to the integration of the interstage and second stage blowdown valves, the interstage and the second stage will be decompressed simultaneously. Therefore, if the second stage blowdown valve malfunctions and fails to open, the innerstage blowdown valve will remain open thus averting possible compressor failure.




Additional modifications need to be made to the compressor system


1002


to use it with the multistage blowdown valve


10


of the present invention. Tubing elbow


180


, which was attached to the moisture trap


126


, is now attached to a shuttle check valve


492


. One side of the shuttle check valve


492


is connected to the moisture trap


126


through a pipe fitting


494


. The other side of the shuttle check valve


492


is connected to a tubing elbow


490


which is connected to tubing


488


. Tubing


488


has an elbow


480


connected to its other end which is connected to a first end of tubing T


460


. Previously, tube fitting


190


was operatively connected to check valve


128


A, but is now connected to a second end of tubing T


460


. The third end of tubing T


460


is connected through a pipe fitting


470


to check valve


128


A.




The dual blowdown valve


10


,


50


of the present invention lowers the pressure ratio across the second stage, i.e., the value of the pressure across the second stage minus the pressure across the interstage, divided by the value of the pressure across the interstage. Through testing, it has been determined that using the dual blowdown valve of the present invention can lower the second stage pressure ratio under normal operating conditions from a value above six to a value below three.




One of the benefits of maintaining a low-pressure ratio across the second stage compressor during normal operations is that it lowers operating temperatures in the second stage compressor. Tests of the dual blowdown concept have shown that a standard blowdown system had a second stage compressor discharge as high as 360 degrees F. during normal cycling operation. Under the same cycling operation, the dual blowdown system had a maximum second stage compressor discharge temperature of 295 degrees F. In this test, the dual blowdown system ran 22 percent cooler than the standard system. These cooler operating temperatures obtained from using the dual blowdown valve


10


,


50


can lead to a longer compressor lifespan.




It should be understood that the foregoing is illustrative and not limiting and that obvious modifications may be made by those skilled in the art without departing from the spirit of the invention. Accordingly, reference should be made primarily to the accompanying claims, rather than the foregoing specification, to determine the scope of the invention.



Claims
  • 1. A valve for being controlled by a single control signal from a compressor system, the valve comprising:a bore; a plurality of spools located linearly within the bore, the plurality of spools having a first position when the control signal is in a first state, the plurality of spools having a second position when the control signal is in a second state; spring means for biasing the plurality of spools; a first inlet port being in fluid communication with a first discharge port when the control signal is in the second state, the first inlet port being fluidly isolated from the first discharge port when the control signal is in the first state; and a second inlet port being in fluid communication with a second discharge port when the control signal is in the second state, the second inlet port being fluidly isolated from the second discharge port when the control signal is in the first state; wherein the first inlet port and the first discharge port are fluidly isolated from both the second inlet port and the second discharge port.
  • 2. The valve of claim 1, wherein the control signal comprises pneumatic pressure.
  • 3. The valve of claim 1, wherein the spring means comprises a compression spring and wherein the first and the second states of the control signal comprise low and high pneumatic pressure, respectively, and the compression spring biases the plurality of spools to the first position.
  • 4. The valve of claim 1, wherein the spring means comprises a tension spring and wherein the first and the second states of the control signal comprise high and low pneumatic pressure, respectively, and the tension spring biases the plurality of spools to the second position.
  • 5. The valve of claim 1, wherein adjacent spools are coupled linearly by the use of a mortise and a tenon.
  • 6. The valve of claim 1, further comprising an oil less, two stage compressor system having an interstage and a second stage compressor, wherein the valve is coupled to the compressor system.
  • 7. The valve of claim 6, further comprising:a first muffler coupled to the first discharge port; and a second muffler coupled to the second discharge port; wherein the first inlet port is effectively coupled to the interstage and the second inlet port is effectively coupled to the second stage compressor discharge.
  • 8. A blowdown valve for being controlled by a single pneumatic pressure signal from a compressor system having an interstage and a second stage compressor, wherein the pneumatic pressure signal can be a low pressure or a high pressure, the valve comprising:a bore; a plurality of spools located linearly within the bore, the plurality of spools having a first position when the pneumatic pressure signal is the low pressure, the plurality of spools having a second position when the pneumatic pressure signal is the high pressure; a compression spring for biasing the plurality of spools to the closed position; a first inlet port being in fluid communication with a first discharge port when the pneumatic pressure signal is the high pressure, the first inlet port being fluidly isolated from the first discharge port when the pneumatic pressure signal is the low pressure; a second inlet port being in fluid communication with a second discharge port when the pneumatic pressure signal is the high pressure, the second inlet port being fluidly isolated from the second discharge port when the pneumatic pressure signal is the low pressure; a first muffler coupled to the first discharge port; and a second muffler coupled to the second discharge port; wherein the first inlet port is effectively coupled to the interstage compressor and the second inlet port is effectively coupled to the second stage compressor; wherein the first inlet port and the first discharge port are fluidly isolated from both the second inlet port and the second discharge port.
  • 9. The blowdown valve of claim 8, wherein adjacent spools are coupled linearly by the use of a mortise and a tenon.
  • 10. An electronic control system for a single or a network of oil free, two stage compressor packages, operatively connected to a pressure system in which pressure is to be maintained within a desired pressure range, for controlling the operation of the single or the network of compressor packages, the system comprising:measuring means, operatively connected to a first and a second compressor stage, for determining an air pressure exiting the first and the second compressor stages; processing means, operatively connected to the measuring means for receiving signals from the measuring means, for comparing the determined pressure exiting the first compressor and the second compressor stages with a predetermined range of possible pressures; means, operatively connected to the oil free, two stage compressor package and the processing means, for shutting down the compressor package before the compressor package is damaged; and a single valve for simultaneously releasing the pressure from the first and the second compressor stages, the single valve being controlled from a single control signal.
  • 11. The system of claim 10 wherein, if the air pressure exiting the first and the second compressor stages goes above the predetermined range of possible pressures, the control system will shut down the compressor package.
  • 12. The system of claim 11 wherein, the air pressure exiting the first and the second compressor stages is established by computing a value by measuring the second stage compressor discharge pressure and the first stage compressor discharge pressure, such that when a ratio of an effective second stage compressor discharge pressure to an effective first stage compressor discharge pressure is greater than 3.5, for a period of about three (3) seconds, an alarm is flagged and the control system shuts down the compressor package.
  • 13. The system of claim 10 further comprising:measuring means, operatively connected to the first and the second compressor stages, for determining the temperature of the air exiting the first and the second compressor stages, wherein the processing means compares the determined temperature exiting the first compressor and the second compressor stages with a predetermined temperature limit; and means, operatively connected to the oil free, two stage compressor package and the processor means, for shutting the compressor package down before the package is damaged, if the exiting temperatures exceed such predetermined temperature.
  • 14. The system of claim 13 wherein, the predetermined temperature limit of the air exiting the first compressor and the second compressor stages is set at about four hundred thirty five degrees Fahrenheit (435° F.).
  • 15. The system of claim 13 wherein, the predetermined temperature limit of the air entering the second stage compressor and the compressor package discharge temperatures is set at about one hundred twenty degrees Fahrenheit (120° F.).
  • 16. The system of claim 13 wherein, after shutting down the compressor package, the control system records which of the four measured temperatures was responsible for shutting down the compressor package, and at what time and date the shutdown occurred.
  • 17. The system of claim 10 further comprising:at least one cooling means, operatively positioned between the first compressor stage and the second compressor stage, for cooling the air prior to the air entering the second stage compressor; at least a second cooling means, operatively positioned between a stage two compressor exit and a compressor package exit, for cooling the air prior to the air entering an end user air system; means, operatively connected to each cooling means, for establishing a high predetermined temperature limit for the temperature of the air exiting each cooling means; and measuring means, operatively connected to each cooling means for measuring the temperature of the air exiting each cooling means; and means, operatively connected to each measuring means and the processor means, for shutting the compressor package down before the package is damaged, if either of the exiting temperatures exceed the predetermined high temperature limit.
  • 18. The system of claim 10 further comprising:lubricating oil containing means, operatively positioned in the first compressor stage and the second compressor stage, for lubricating parts isolated from each compressor compression chamber; measuring means, operatively connected to the each lubricating oil containing means, for measuring an oil pressure thereof; means, operatively connected to each lubricating oil containing means measuring means and to the processing means for establishing a range of operating oil pressures; and means, operatively connected to each measuring means and the processor means, for shutting the compressor package down before the package is damaged, if the oil pressure deviates from the predetermined oil pressure range.
  • 19. The system of claim 10 further comprising:means, operatively connected to the processing means, for measuring the pressure of the air exiting the compressor package after the second stage cooling means; means, operatively connected to the processing means, for measuring the temperature of the air exiting the compressor package after the second stage cooling means; means, operatively connected to the processing means, for establishing a range of compressor package discharge temperatures and pressures; and means, operatively connected to the package exiting temperature and pressure measuring means, for shutting down the compressor package if either the temperature or the pressure exceeds a predetermined limit.
  • 20. The system of claim 19 wherein, the package discharge pressure is used to determine when to unload and load the two compressor stages.
RELATED APPLICATIONS

This application is a continuation-in-part of commonly owned U.S. patent application Ser. No. 09/179,523, filed Oct. 27, 1998, of Centers et al., which is a continuation-in-part of commonly owned U.S. Provisional Patent Application Ser. No. 60/066,008, filed Oct. 28, 1997, of Centers et al., the disclosures of which are herein incorporated by reference.

US Referenced Citations (21)
Number Name Date Kind
3260444 Williams et al. Jul 1966
3756753 Persson et al. Sep 1973
3927708 Hulme Dec 1975
3936239 Shaw Feb 1976
4076468 Persson et al. Feb 1978
4084618 Gurries Apr 1978
4105064 Toro et al. Aug 1978
4155535 Seamone May 1979
4339233 Krueger Jul 1982
4646785 Ruedle et al. Mar 1987
4678406 Pillis et al. Jul 1987
5044894 Field et al. Sep 1991
5163478 Fries Nov 1992
5335696 McKenzie Aug 1994
5655379 Jaster et al. Aug 1997
5713724 Centers et al. Feb 1998
5738497 Hensley Apr 1998
5833925 Shu et al. Nov 1998
5860801 Timuska Jan 1999
6053421 Chockley Apr 2000
6102665 Centers et al. Aug 2000
Provisional Applications (1)
Number Date Country
60/066008 Oct 1997 US
Continuation in Parts (1)
Number Date Country
Parent 09/179523 Oct 1998 US
Child 09/422284 US