US3667247A - Refrigeration system with evaporator outlet control valve - Google Patents

Refrigeration system with evaporator outlet control valve Download PDF

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US3667247A
US3667247A US53861A US3667247DA US3667247A US 3667247 A US3667247 A US 3667247A US 53861 A US53861 A US 53861A US 3667247D A US3667247D A US 3667247DA US 3667247 A US3667247 A US 3667247A
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pressure
coil
valve
control valve
evaporator
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Robert H Proctor
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Eaton Corp
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Controls Company of America
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B41/00Fluid-circulation arrangements
    • F25B41/30Expansion means; Dispositions thereof
    • F25B41/31Expansion valves
    • F25B41/33Expansion valves with the valve member being actuated by the fluid pressure, e.g. by the pressure of the refrigerant
    • F25B41/335Expansion valves with the valve member being actuated by the fluid pressure, e.g. by the pressure of the refrigerant via diaphragms
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2341/00Details of ejectors not being used as compression device; Details of flow restrictors or expansion valves
    • F25B2341/06Details of flow restrictors or expansion valves
    • F25B2341/068Expansion valves combined with a sensor
    • F25B2341/0683Expansion valves combined with a sensor the sensor is disposed in the suction line and influenced by the temperature or the pressure of the suction gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2500/00Problems to be solved
    • F25B2500/15Hunting, i.e. oscillation of controlled refrigeration variables reaching undesirable values
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2600/00Control issues
    • F25B2600/21Refrigerant outlet evaporator temperature

Definitions

  • the expansion valve may be the bulbless type or the externally equalized type.
  • the outlet control valve may respond to "refrigerant temperature at the coil outlet, or to fin temperature, or may be an evaporator pressure regulator valve.
  • the expansion valve can be designed to approach superheat at low suction pressures. This results in either liquid refrigerant or gaseous refrigerant at saturation temperature leaving the evaporator coil to provide additional (and necessary) cooling and lubrication to the compressor.
  • the evaporator outlet control valve even functions as an expansion valve of sorts and the liquid entering the suction line creates an artificial load by cooling the suction line and expands in the compressor cylinder (reducing the compressor capacity).
  • the ability to maintain 0 superheat at low suction pressures also results in the then'nostatic expansion valve opening more and more often and thus aids the evaporator outlet control valve in maintaining the desired pressure in the evaporator coil.
  • the point of novelty is the use of a cross charged thermo static expansion valve in a refrigeration system to regulate flow to the evaporator coil in accordance with temperature and pressure conditions downstream of an evaporator outlet control valve.
  • thermostatic expansion valve is charged with the same medium as used as the refrigerant in the system. Such a valve is designated system charged.
  • a cross charged expansion valve is charged with a medium having a temperature-pressure curve other than the temperature-pressure curve of the refrigerant.
  • FIG. I is a schematic of a refrigeration system incorporating an evaporator outlet control valve and a bulbless thermostatic expansion valve with the latter being shown in vertical section.
  • FIG. 2 is a pressure-temperature curve of the thermostatic expansion valve cross charged in accordance with this invention and incorporated in the system of FIG. 1.
  • thermostatic expansion valve shown in the drawings simplifies the disclosure of the means for sensing both pressure and temperature at a point downstream from the evaporator control valve.
  • An external equalizer type of thermostatic expansion valve could be used with its feeler bulb positioned on the suction line downstream of the evaporator outlet control valve and with the equalizer connection also being in the suction line downstream of the control valve. Since externally equalized thermostatic expansion valves are well known in the art, it is not deemed necessary to illustrate this variation. As pointed out hereinafter, either type thermostatic expansion valve is cross charged in this system.
  • the ball type valve 18 controls the flow through the partition 20 to outlet 22.
  • Valve 18 rests on spring seat 24 and is biased upwardly towards its seated position by spring 26 which may be adjusted (superheat adjustment) by turning seat 28.
  • the valve is actuated by push pin 30 which in turn is actuated by diaphragm rider pin 32 fixed to diaphragm pad 34 and having an end projecting through the pad and diaphragm 36 to communicate with head chamber 38.
  • Pin 30 has a close sliding fit in bore 41 to minimize the leakage along this portion since any such leakage would constitute a bypass.
  • Flow from the valve outlet flows to the evaporator coil 39 and then passes through the evaporator outlet control valve 40 which may be an evaporator pressure regulator valve or may be a tin temperature sensing valve or may be responsive to refrigerant temperature at the coil outlet.
  • Any of these evaporator outlet control valves operates in one way or another to control flow from the evaporator coil to prevent freeze-up of the coil under low load/high capacity conditions. All these valves function to control the pressure (and temperature since they are related) in the coil just above the coil freezing conditions.
  • Flow from the control valve 40 enters a suction line 42 to the upper return conduit of the expansion valve at inlet 44 and passes through conduit 46 over the rider pin to the outlet 48 and then to the suction line 50 leading to the compressor intake.
  • the control valve can be designed to lead directly to the return conduit 46 of the expansion valve (that is, the line 42 can be omitted).
  • Pressure in the return conduit in the expansion valve can communicate with chamber 52 below the diaphragm through port 54 and the upper wall 56 of the valve body. Leakage between the rider pin and wall 56 is desired.
  • Diaphragm 36 is mounted between the domed head 58 and support cup 60 threaded into the upper end of the valve body and sealed with respect thereto by means of O-ring 62. Head chamber 38 is cross charged witha temperature responsive charge through capillary tube 64 which is then sealed off.
  • the cross charge terminology connotes that the charging medium has a temperature/pressure curve other than the temperature/pressure curve of the refrigerant. In this instance it is selected to approach 0 superheat for the thermostatic expansion valve as the suction line pressure (sensed in return conduit 36) approaches 0 PSIG.
  • rider pin 32 is provided with a blind hole 66 which terminates at approximately the midpoint of the return flow path through the upper portion of the valve body.
  • the blind hole in effect, provides a small temperature sensing chamber 68 inside the rider pin and located in the system return path downstream of the evaporator outlet control valve 40.
  • Pin chamber 68 will always be colder than head chamber 38 and, therefore, the refrigerant charge will tend to condense in chamber 68 and the control point will be at this location which is ideally situated. Since there is not much mass involved in the rider pin, the response of the valve would tend to be too rapid.
  • a low thermoconductivity sleeve 70 of Delrin which is self-lubricating
  • capillary restricter 72 is fitted in the upper end of the rider pin. This then provides a very small capillary hole connecting the rider pin chamber 68 to head chamber 38. This is adequate for transfer of pressure changes but will minimize migration of any condensed refrigerant in chamber 68 to the head chamber should the valve be mounted upside down. Without this restricter there could be such migration with the result that the liquid refrigerant migrating to the head chamber (which is warmer) would flash to gas (increasing the pressure) and then promptly be recondensed in chamber 68. This would induce hunting in the system. With the restricter the hunting is minimized.
  • FIG. 2 shows the curve of a cross charged thermostatic expansion valve opening superheat versus the suction pressure influencing the thermostatic expansion valve. It will be noted that as the suction pressure (the pressure in chamber 52) falls, the superheat opening temperature of the expansion valve also falls. This is contrary to the performance of a system charged expansion valve which tendsto increase the superheat temperature as the pressure falls.
  • the chambers 38 and 68 may be charged (through capillary 64) to 3 l PSIG with S0, with the complete valve at 75 F. The S0, source is thenshut off close to the valve by means of a hand valve. Then the charging fixture is evacuated and the entire'valve is immersed in a 32 F. bath. Argon at 32 PSIG is then applied to the charging fixture and the hand valve is opened to apply the Argon to the chambers. Then the capillary is crimped and sealed. Other proportions or refrigerants can be used.
  • this system utilizes an evaporator outlet control valve which will operate to keep the pressure (and temperature) of evaporator coil 39 to prevent icing the coil even through the compressor capacity exceeds the evaporator capacity, the compressor 10 will tend to pull down the pressure in the suction line 42-50 to very low levels. This low pressure is sensed in chamber 52 and exerts a force on the diaphragm tending to open the valve. Due to the cross charge in the diaphragm and rider pin chambers giving the operating characteristic shown in FIG. 2 the valve 18 opens at a desired low suction pressure rather than having less tendency to open. In FIG.
  • the net effect of the cooler refrigerant and liquid refrigerant reaching the compressor coupled with the artificial load of the suction line is to virtually eliminate the possibility of damage to the compressor.
  • the curve of FIG. 2 also shows that the thermostatic expansion valve will pass liquid well before the compressor can reduce the suction line pressure to 0 P816. Experience shows no harm to the compressor receiving substantial liquid even enough to show liquid in the line going to the condenser.
  • FIG. 2 points up a further advantage in this system in that the superheat setting of the cross charged thermostatic expansion valve increases as higher pressures exist in the suction line. This is contrary to a system charged valve. Therefore, on initial start-up with a high pressure in the suction line the valve operates at increased superheat and, therefore, facilitates rapid pull down of the pressure which means more rapid cool- This system, therefore, functions to protect the compressor and also gives better performance during pull down. Benefits are realized both under the low load/high capacity condition and under the high load condition of pull down. In normal load situations the superheat of the valve is normal and operation is normal.
  • a refrigeration system comprising,
  • a compressor a condenser receiving compressed compressor, an evaporator coil, a thermostatic expansion valve regulating flow from the condenser to the evaporator coil,
  • a suction line connecting the coil to the compressor i nlet, an evaporator outlet control valve In the suction line and operative in response to a control condition to regulate flow from the coil to prevent freeze-up of the coil, said thermostatic expansion valve being responsive to both temperature and pressure in the suction line downstream of the evaporator outlet control valve and being cross charged to reduce the coil outlet superheat as the suction line pressure is reduced.
  • thermostatic expansionvalve has a valve regulating flow to the coil and actuated by a diaphragm one side of which is subjected to pressure in a chamber cross changed with a medium responsive to temperature in the suction line downstream of the evaporator outlet control valve and the other side of the diaphragm being subjected to pressure in a chamber which pressure is a function of the suction line pressure downstream of the evaporator outlet control valve.
  • a refrigeration system in which the evaporator outlet control valve is responsive to temperature or pressure to throttle flow from the coil to maintain minimum temperature and pressure conditions in the coil preventing freeze-up.
  • a refrigeration system in which the evaporator outlet control valve responds to evaporator pressure.
  • a refrigeration system in which the evaporator outlet control valve responds to the temperature of the coil fins.
  • a refrigeration system in which the evaporator outlet control valve responds to refrigerant temperature in the coil.
  • thermostatic expansion valve includes a valve actuating pin connecting the diaphragm to the valve and the pin is hollowed out and communicates with the chamber on said one side of the diaphragm,

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  • Physics & Mathematics (AREA)
  • Engineering & Computer Science (AREA)
  • Fluid Mechanics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Temperature-Responsive Valves (AREA)

Abstract

Refrigerant flows from the compressor and condenser to the evaporator by a thermostatic expansion valve having its pressure and temperature sensing points in the suction line downstream of the evaporator outlet control valve which regulates the evaporator pressure relatively independently of the suction line conditions. When the compressor capacity significantly exceeds evaporator capacity this system provides additional compressor cooling at low suction pressures. The expansion valve may be the bulbless type or the externally equalized type. The outlet control valve may respond to refrigerant temperature at the coil outlet, or to fin temperature, or may be an evaporator pressure regulator valve.

Description

United States Patent Proctor [4 1 June 6, 1972 54] REFRIGERATION SYSTEM WITH 3,450,345 6/1969 Orth .Q. ..62/225 EVAPORATQR OUTLET CONTROL 3,537,645 11/1970 Treder ..62/210 VALVE [72] lnventor: Robert H. Proctor, Richmond, lnd.
[73] Assignee: Controls Company of America, Melrose Park, ill.
[22] Filed: July 10, 1970 21 Appl. No.2 53,861
[52] US. Cl ..62/217, 62/225 [51] Int. Cl ..F25b 41/04 [58] Field of Search ..62/205, 209, 210, 211, 212, 62/224, 225, 217
[56] References Cited UNITED STATES PATENTS 2,766,593 10/1956 Mitchell ..62/217 2,986,015 5/196] Mitchell ..62/210 Primary Examiner-Meyer Perlin Attorney-John W. Michael, Gerrit D. Foster, Bayard H. Michael, Paul R. Puerner, Joseph A. Gemignani. Andrew 0. Riteris and Spencer B. Michael [57] ABSTRACT Refrigerant flows from the compressor and condenser to the evaporator by a thermostatic expansion valve having its pressure and temperature sensing points in the suction line downstream of the evaporator outlet control valve which regulates the evaporator pressure relatively independently of the suction line conditions. When the compressor capacity significantly exceeds evaporator capacity this system provides additional compressor cooling at low suction pressures. The expansion valve may be the bulbless type or the externally equalized type. The outlet control valve may respond to "refrigerant temperature at the coil outlet, or to fin temperature, or may be an evaporator pressure regulator valve.
8 Claims, 2 Drawing Figures REFRIGERATION SYSTEM WITH EVAPORATOR OUTLET CONTROL VALVE BACKGROUND OF INVENTION In refrigeration systems having compremor capacity which may greatly exceed the evaporator capacity or load such as typical of automotive air conditioning systems, especially those required to run continuously, provision against icing the evaporator coil typically uses an evaporator outlet control valve located downstream of the temperature sensing point of the thermostatic expansion valve. This typically results in lesser refrigerant flow as the load decreases resulting in warmer refrigerant going to the compressor at lower pressures. This reduces cooling and lubrication of the compressor and may damage the compressor.
SUMMARY OF INVENTION By controlling a cross charged thermostatic expansion valve in accordance with temperature and pressure downstream of the evaporator outlet control valve as described in the Abstract the expansion valve can be designed to approach superheat at low suction pressures. This results in either liquid refrigerant or gaseous refrigerant at saturation temperature leaving the evaporator coil to provide additional (and necessary) cooling and lubrication to the compressor. The evaporator outlet control valve even functions as an expansion valve of sorts and the liquid entering the suction line creates an artificial load by cooling the suction line and expands in the compressor cylinder (reducing the compressor capacity). The ability to maintain 0 superheat at low suction pressures also results in the then'nostatic expansion valve opening more and more often and thus aids the evaporator outlet control valve in maintaining the desired pressure in the evaporator coil.
The point of novelty is the use of a cross charged thermo static expansion valve in a refrigeration system to regulate flow to the evaporator coil in accordance with temperature and pressure conditions downstream of an evaporator outlet control valve.
The usual thermostatic expansion valve is charged with the same medium as used as the refrigerant in the system. Such a valve is designated system charged. A cross charged expansion valve is charged with a medium having a temperature-pressure curve other than the temperature-pressure curve of the refrigerant. By selection of the cross charge the suction pressure corresponding to 0 superheat can be selected to suit the particular system. Since the superheat/pressure curve is reversed the rapid pull down benefits are realized. Under normal conditions normal operation is obtained.
DESCRIPTION OF DRAWINGS FIG. I is a schematic of a refrigeration system incorporating an evaporator outlet control valve and a bulbless thermostatic expansion valve with the latter being shown in vertical section.
FIG. 2 is a pressure-temperature curve of the thermostatic expansion valve cross charged in accordance with this invention and incorporated in the system of FIG. 1.
DESCRIPTION OF PREFERRED EMBODIMENT At the outset it should be noted that the bulbless thermostatic expansion valve shown in the drawings simplifies the disclosure of the means for sensing both pressure and temperature at a point downstream from the evaporator control valve. An external equalizer type of thermostatic expansion valve could be used with its feeler bulb positioned on the suction line downstream of the evaporator outlet control valve and with the equalizer connection also being in the suction line downstream of the control valve. Since externally equalized thermostatic expansion valves are well known in the art, it is not deemed necessary to illustrate this variation. As pointed out hereinafter, either type thermostatic expansion valve is cross charged in this system.
Refrigerant flows from compressor 10 to condenser 12 and from the condenser may flow either to a receiver (not shown) or directly into inlet 14 of thethennostatic expansion valve 16. The ball type valve 18 controls the flow through the partition 20 to outlet 22. Valve 18 rests on spring seat 24 and is biased upwardly towards its seated position by spring 26 which may be adjusted (superheat adjustment) by turning seat 28.
The valve is actuated by push pin 30 which in turn is actuated by diaphragm rider pin 32 fixed to diaphragm pad 34 and having an end projecting through the pad and diaphragm 36 to communicate with head chamber 38. Pin 30 has a close sliding fit in bore 41 to minimize the leakage along this portion since any such leakage would constitute a bypass. Flow from the valve outlet flows to the evaporator coil 39 and then passes through the evaporator outlet control valve 40 which may be an evaporator pressure regulator valve or may be a tin temperature sensing valve or may be responsive to refrigerant temperature at the coil outlet. Any of these evaporator outlet control valves operates in one way or another to control flow from the evaporator coil to prevent freeze-up of the coil under low load/high capacity conditions. All these valves function to control the pressure (and temperature since they are related) in the coil just above the coil freezing conditions.
Flow from the control valve 40 enters a suction line 42 to the upper return conduit of the expansion valve at inlet 44 and passes through conduit 46 over the rider pin to the outlet 48 and then to the suction line 50 leading to the compressor intake. If desired, the control valve can be designed to lead directly to the return conduit 46 of the expansion valve (that is, the line 42 can be omitted). Pressure in the return conduit in the expansion valve can communicate with chamber 52 below the diaphragm through port 54 and the upper wall 56 of the valve body. Leakage between the rider pin and wall 56 is desired. Diaphragm 36 is mounted between the domed head 58 and support cup 60 threaded into the upper end of the valve body and sealed with respect thereto by means of O-ring 62. Head chamber 38 is cross charged witha temperature responsive charge through capillary tube 64 which is then sealed off.
As mentioned above, the cross charge terminology connotes that the charging medium has a temperature/pressure curve other than the temperature/pressure curve of the refrigerant. In this instance it is selected to approach 0 superheat for the thermostatic expansion valve as the suction line pressure (sensed in return conduit 36) approaches 0 PSIG.
It will be noted that rider pin 32 is provided with a blind hole 66 which terminates at approximately the midpoint of the return flow path through the upper portion of the valve body. The blind hole, in effect, provides a small temperature sensing chamber 68 inside the rider pin and located in the system return path downstream of the evaporator outlet control valve 40. Pin chamber 68 will always be colder than head chamber 38 and, therefore, the refrigerant charge will tend to condense in chamber 68 and the control point will be at this location which is ideally situated. Since there is not much mass involved in the rider pin, the response of the valve would tend to be too rapid. To damp the hunting effect a low thermoconductivity sleeve 70 of Delrin (which is self-lubricating) is mounted over the rider pin.
To make the valve mountable in all positions capillary restricter 72 is fitted in the upper end of the rider pin. This then provides a very small capillary hole connecting the rider pin chamber 68 to head chamber 38. This is adequate for transfer of pressure changes but will minimize migration of any condensed refrigerant in chamber 68 to the head chamber should the valve be mounted upside down. Without this restricter there could be such migration with the result that the liquid refrigerant migrating to the head chamber (which is warmer) would flash to gas (increasing the pressure) and then promptly be recondensed in chamber 68. This would induce hunting in the system. With the restricter the hunting is minimized.
FIG. 2 shows the curve of a cross charged thermostatic expansion valve opening superheat versus the suction pressure influencing the thermostatic expansion valve. It will be noted that as the suction pressure (the pressure in chamber 52) falls, the superheat opening temperature of the expansion valve also falls. This is contrary to the performance of a system charged expansion valve which tendsto increase the superheat temperature as the pressure falls. As an example of cross charging, the chambers 38 and 68 may be charged (through capillary 64) to 3 l PSIG with S0, with the complete valve at 75 F. The S0, source is thenshut off close to the valve by means of a hand valve. Then the charging fixture is evacuated and the entire'valve is immersed in a 32 F. bath. Argon at 32 PSIG is then applied to the charging fixture and the hand valve is opened to apply the Argon to the chambers. Then the capillary is crimped and sealed. Other proportions or refrigerants can be used.
Since, this system utilizes an evaporator outlet control valve which will operate to keep the pressure (and temperature) of evaporator coil 39 to prevent icing the coil even through the compressor capacity exceeds the evaporator capacity, the compressor 10 will tend to pull down the pressure in the suction line 42-50 to very low levels. This low pressure is sensed in chamber 52 and exerts a force on the diaphragm tending to open the valve. Due to the cross charge in the diaphragm and rider pin chambers giving the operating characteristic shown in FIG. 2 the valve 18 opens at a desired low suction pressure rather than having less tendency to open. In FIG. 2 it is shown that with a suction pressure about l l-% pounds the valve will open at superheat which means that at the point the expansion valve will start passing liquid to the evaporator coil and the evaporator outlet control valve will open and pass liquid or gaseous refrigerant (at saturation temperature) to the suction line. Thus the refrigerant in the suction line is at a lower temperature (than in other systems) which facilitates cooling the compressor and liquid refrigerant will actually reach the compressor and expand in the compressor adding further cooling. Furthermore, the entire suction line from the control valve 40 to the compressor has now been made, in effect, an additional coil and introduces an artificial additional load on the system. The net effect of the cooler refrigerant and liquid refrigerant reaching the compressor coupled with the artificial load of the suction line is to virtually eliminate the possibility of damage to the compressor. The curve of FIG. 2 also shows that the thermostatic expansion valve will pass liquid well before the compressor can reduce the suction line pressure to 0 P816. Experience shows no harm to the compressor receiving substantial liquid even enough to show liquid in the line going to the condenser.
FIG. 2 points up a further advantage in this system in that the superheat setting of the cross charged thermostatic expansion valve increases as higher pressures exist in the suction line. This is contrary to a system charged valve. Therefore, on initial start-up with a high pressure in the suction line the valve operates at increased superheat and, therefore, facilitates rapid pull down of the pressure which means more rapid cool- This system, therefore, functions to protect the compressor and also gives better performance during pull down. Benefits are realized both under the low load/high capacity condition and under the high load condition of pull down. In normal load situations the superheat of the valve is normal and operation is normal.
I claim: 1. A refrigeration system comprising,
a compressor, a condenser receiving compressed compressor, an evaporator coil, a thermostatic expansion valve regulating flow from the condenser to the evaporator coil,
a suction line connecting the coil to the compressor i nlet, an evaporator outlet control valve In the suction line and operative in response to a control condition to regulate flow from the coil to prevent freeze-up of the coil, said thermostatic expansion valve being responsive to both temperature and pressure in the suction line downstream of the evaporator outlet control valve and being cross charged to reduce the coil outlet superheat as the suction line pressure is reduced.
2. A refrigeration system according to claim I in which the thermostatic expansionvalve has a valve regulating flow to the coil and actuated by a diaphragm one side of which is subjected to pressure in a chamber cross changed with a medium responsive to temperature in the suction line downstream of the evaporator outlet control valve and the other side of the diaphragm being subjected to pressure in a chamber which pressure is a function of the suction line pressure downstream of the evaporator outlet control valve.
3. A refrigeration system according to claim 2 in which the evaporator outlet control valve is responsive to temperature or pressure to throttle flow from the coil to maintain minimum temperature and pressure conditions in the coil preventing freeze-up.
4. A refrigeration system according to claim 3 in which the evaporator outlet control valve responds to evaporator pressure.
5. A refrigeration system according to claim 3 in which the evaporator outlet control valve responds to the temperature of the coil fins.
6. A refrigeration system according to claim 3 in which the evaporator outlet control valve responds to refrigerant temperature in the coil.
7. The refrigeration system according to claim 2 in which the refrigerant fiow from the evaporator outlet control valve passes directly over the temperature sensing point of the thermostatic expansion valve.
8. The refrigeration system according to claim 7 in which the thermostatic expansion valve includes a valve actuating pin connecting the diaphragm to the valve and the pin is hollowed out and communicates with the chamber on said one side of the diaphragm,
a return conduit through the thermostatic expansion valve and forming part of the suction line, thev hollowed portion of the pin being located in the return conduit whereby the temperature is sensed at the pin and the pressure in the return conduit communicates with the chamber on said other side of the diaphragm.
refrigerant from the 23 UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION Patent No. 3,667 ,247 Dated June 6, 1972 Inventor(g) Robert H. Proctor It is certified that error appears in the above-identified patent and that said Letters Patent are hereby corrected as shown below:
(first occurrence) Column 3, line 30, "the/ should read that Column 4, line 25, "changed" should read charged Signed and sealed this 12th day of September 1972.
(SEAL) Attest:
EDWARD M.FLETCHER,JR. ROBERT GOTT SCHALK Attesting Officer Commissioner of Patents

Claims (8)

1. A refrigeration system comprising, a compressor, a condenser receiving compressed refrigerant from the compressor, an evaporator coil, a thermostatic expansion valve regulating flow from the condenser to the evaporator coil, a suction line connecting the coil to the compressor inlet, an evaporator outlet control valve in the suction line and operative in response to a control condition to regulate flow from the coil to prevent freeze-up of the coil, said thermostatic expansion valve being responsive to both temperature and pressure in the suction line downstream of the evaporator outlet control valve and being cross charged to reduce the coil outlet superheat as the suction line pressure is reduced.
2. A refrigeration system according to claim 1 in which the thermostatic expansion valve has a valve regulating flow to the coil and actuated by a diaphragm one side of which is subjected to pressure in a chamber cross changed with a medium responsive to temperature in the suction line downstream of the evaporator outlet control valve and the other side of the diaphragm being subjected to pressure in a chamber which pressure is a function of the suction line pressure downstream of the evaporator outlet control valve.
3. A refrigeration system according to claim 2 in which the evaporator outlet control valve is responsive to temperature or pressure to throttle flow from the coil to maintain minimum temperature and pressure conditions in the coil preventing freeze-up.
4. A refrigeration system according to claim 3 in which the evaporator outlet control valve responds to evaporator pressure.
5. A refrigeration system according to claim 3 in which the evaporator outlet control valve responds to the temperature of the coil fins.
6. A refrigeration system according to claim 3 in which the evaporator outlet control valve responds to refrigerant temperature in the coil.
7. The refrigeration system according to claim 2 in which the refrigerant flow from the evaporator outlet control valve passes directly over the temperature sensing point of the thermostatic expansion valve.
8. The refrigeration system according to claim 7 in which the thermostatic expansion valve includes a valve actuating pin connecting the diaphragm to the valve and the pin is hollowed out and communicates with the chamber on said one side of the diaphragm, a return conduit through the thermostatic expansion valve and forming part of the suction line, the hollowed portion of the pin being located in the return conduit whereby the temperature is sensed at the pin and the pressure in the return conduit communicates with the chamber on said other side of the diaphragm.
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Cited By (17)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3810366A (en) * 1972-07-31 1974-05-14 Controls Co Of America Refrigeration valve
US3817053A (en) * 1972-11-10 1974-06-18 Controls Co Of America Refrigerating system including flow control valve
US4024888A (en) * 1974-11-01 1977-05-24 The Singer Company Evaporator pressure regulator
US4049410A (en) * 1974-07-29 1977-09-20 Allan Sinclair Miller Gas compressors
US4333317A (en) * 1980-08-04 1982-06-08 General Electric Company Superheat controller
US5269459A (en) * 1991-10-17 1993-12-14 Eaton Corporation Thermally responsive expansion valve
US5303864A (en) * 1991-05-14 1994-04-19 Deutsche Controls Gmbh Expansion valve
US5361597A (en) * 1993-04-22 1994-11-08 Fuji Koki Manufacturing Co., Ltd. Thermostatic expansion valve
EP0829690A1 (en) * 1996-09-12 1998-03-18 Fujikoki Corporation Expansion valve
EP0836061A1 (en) * 1996-10-11 1998-04-15 Fujikoki Corporation Expansion valve
US5943871A (en) * 1996-09-02 1999-08-31 Denso Corporation Thermal expansion valve
US6321995B1 (en) 1999-10-21 2001-11-27 Parker-Hannifin Corporation Thermostatic expansion valve
EP1302733A1 (en) * 2001-10-10 2003-04-16 TGK CO., Ltd. Expansion valve
EP1375215A3 (en) * 2002-06-26 2004-06-16 Delphi Technologies, Inc. Thermostatic expansion valve and air conditioning system for low refrigerant charge
US20040129008A1 (en) * 2002-10-18 2004-07-08 Dianetti Eugene A. Refrigeration expansion valve with thermal mass power element
US20050235692A1 (en) * 2004-01-08 2005-10-27 Nungesser Roy J Expansion valve with mounting bracket
US20170197490A1 (en) * 2014-06-18 2017-07-13 Denso Corporation Refrigeration cycle device

Families Citing this family (2)

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Publication number Priority date Publication date Assignee Title
JP3321713B2 (en) * 1991-10-17 2002-09-09 イートン コーポレーション Thermal response expansion valve
FR2959004B1 (en) * 2010-04-16 2016-02-05 Valeo Systemes Thermiques THERMOPLASTIC RELIEF DEVICE AND AIR CONDITIONING LOOP COMPRISING SUCH A THERMOPLASTIC RELIEF DEVICE

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US2766593A (en) * 1955-06-03 1956-10-16 Mitchell Co John E Automatic refrigeration system
US2986015A (en) * 1958-02-03 1961-05-30 John E Mitchell Company Inc Refrigeration system control
US3450345A (en) * 1967-10-02 1969-06-17 Controls Co Of America Bulbless thermostatic expansion valve
US3537645A (en) * 1969-01-16 1970-11-03 Controls Co Of America Bulbless expansion valve

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US2766593A (en) * 1955-06-03 1956-10-16 Mitchell Co John E Automatic refrigeration system
US2986015A (en) * 1958-02-03 1961-05-30 John E Mitchell Company Inc Refrigeration system control
US3450345A (en) * 1967-10-02 1969-06-17 Controls Co Of America Bulbless thermostatic expansion valve
US3537645A (en) * 1969-01-16 1970-11-03 Controls Co Of America Bulbless expansion valve

Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3810366A (en) * 1972-07-31 1974-05-14 Controls Co Of America Refrigeration valve
US3817053A (en) * 1972-11-10 1974-06-18 Controls Co Of America Refrigerating system including flow control valve
US4049410A (en) * 1974-07-29 1977-09-20 Allan Sinclair Miller Gas compressors
US4024888A (en) * 1974-11-01 1977-05-24 The Singer Company Evaporator pressure regulator
US4333317A (en) * 1980-08-04 1982-06-08 General Electric Company Superheat controller
US5303864A (en) * 1991-05-14 1994-04-19 Deutsche Controls Gmbh Expansion valve
US5269459A (en) * 1991-10-17 1993-12-14 Eaton Corporation Thermally responsive expansion valve
US5361597A (en) * 1993-04-22 1994-11-08 Fuji Koki Manufacturing Co., Ltd. Thermostatic expansion valve
US5943871A (en) * 1996-09-02 1999-08-31 Denso Corporation Thermal expansion valve
US6056202A (en) * 1996-09-12 2000-05-02 Fujikoki Corporation Expansion valve
EP0829690A1 (en) * 1996-09-12 1998-03-18 Fujikoki Corporation Expansion valve
US6206294B1 (en) 1996-09-12 2001-03-27 Fujikoki Corporation Expansion valve
EP0836061A1 (en) * 1996-10-11 1998-04-15 Fujikoki Corporation Expansion valve
US5957376A (en) * 1996-10-11 1999-09-28 Fujikori Corporation Expansion valve
US6189800B1 (en) * 1996-10-11 2001-02-20 Fujikoki Corporation Expansion valve
US6321995B1 (en) 1999-10-21 2001-11-27 Parker-Hannifin Corporation Thermostatic expansion valve
EP1302733A1 (en) * 2001-10-10 2003-04-16 TGK CO., Ltd. Expansion valve
US6612503B2 (en) 2001-10-10 2003-09-02 Tgk Co., Ltd. Expansion valve
EP1375215A3 (en) * 2002-06-26 2004-06-16 Delphi Technologies, Inc. Thermostatic expansion valve and air conditioning system for low refrigerant charge
US20040129008A1 (en) * 2002-10-18 2004-07-08 Dianetti Eugene A. Refrigeration expansion valve with thermal mass power element
US6848624B2 (en) 2002-10-18 2005-02-01 Parker-Hannifin Corporation Refrigeration expansion valve with thermal mass power element
US20050235692A1 (en) * 2004-01-08 2005-10-27 Nungesser Roy J Expansion valve with mounting bracket
US7089761B2 (en) 2004-01-08 2006-08-15 Parker-Hannifin Corporation Expansion valve with mounting bracket
US20170197490A1 (en) * 2014-06-18 2017-07-13 Denso Corporation Refrigeration cycle device

Also Published As

Publication number Publication date
DE2134409B2 (en) 1977-09-15
DE2134409A1 (en) 1972-01-20
FR2100500A5 (en) 1972-03-17
JPS5514343B1 (en) 1980-04-15
DE2134409C3 (en) 1978-05-24
CA919445A (en) 1973-01-23

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