[go: up one dir, main page]
More Web Proxy on the site http://driver.im/

US2952137A - Low pressure refrigerating systems - Google Patents

Low pressure refrigerating systems Download PDF

Info

Publication number
US2952137A
US2952137A US784683A US78468359A US2952137A US 2952137 A US2952137 A US 2952137A US 784683 A US784683 A US 784683A US 78468359 A US78468359 A US 78468359A US 2952137 A US2952137 A US 2952137A
Authority
US
United States
Prior art keywords
tank
refrigerant
evaporator
liquid refrigerant
liquid
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
US784683A
Inventor
John E Watkins
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Individual
Original Assignee
Individual
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to US784683A priority Critical patent/US2952137A/en
Application granted granted Critical
Publication of US2952137A publication Critical patent/US2952137A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • 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
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/16Receivers
    • 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
    • F25B2400/00General features or devices for refrigeration machines, plants or systems, combined heating and refrigeration systems or heat-pump systems, i.e. not limited to a particular subgroup of F25B
    • F25B2400/23Separators

Definitions

  • One object of the invention is to provide a refrigerating system of the above general character Ywhich is simpler in construction, easier and cheaper ,to mantainand more efficient in operation-'than refrigerating systems heretofore available.
  • 9 l 1 Anotherobject is to provide arefrigerating system in which flash gas entering the evaporator is minimized to insure higher coil eiliciency and to permit vthe use Vof liquid lines of minimumV diameter.
  • Y f Y y Another object -is to provide a fsystern ⁇ in'which the components are interrelated in a novely manner whichl reduces superheating ofthe spent refrigerant and 4enables the compressorlto operate withhigher volumetric elliciency and reduced power cost.
  • Still another object is to provide a refrigerating system in which the evaporator is continuously fed. an excess of liquid refrigerant and in which theiexcess ⁇ refrigerant is trapped and -recirculated through' the evaporator withd 2,952,137!- Patented Sept. 13, ⁇ 1960 a connecting line 19 to a receiver 20in which the refrigerant is temporarily stored.
  • the receiver thus pro-v
  • this pressure reduction isV effected in the accumulator 14 into which the liquid refrigerant from the receiver is introduced and combined with excess refrigerant passing through the evaporator-.f
  • the pressure reduction effectively removes all ash gas from the liquid refrigerant and further reduces the tem# perature or supercools the trapped liquid refrigerant. Further, in accordance with the invention, novel means is provided -for repressurzing the supercooled liquid for feeding it through theevaporator coils.
  • the receiver -20 is connected to the accumulator 14 by a liquid line 21.
  • Flow of liquid to the accumulator is controlled by-a Valve VI actuated'by a solenoid SOL-1.
  • a hand-operated metering valve MV may be interposed between the valve VI and the :accumulator Vto provide for manual-.adjustmentl of the feed rate and insure smooth liquidfeed.
  • the solenoid valve V1 is so arranged that the' valve is l closed when the solenoid is deenergized.
  • the accumuf lator tank is equipped with a level control switch LS1I out requiring the usual complicated and expensive pumps tion of the preferred embodiment ⁇ illustrated inthe accompanying single drawing figure.
  • one or more evaporator coils areconnected to receive a supply of liquid refrigerant from a feed line 12.
  • the feed device may be a conventional feed valve or a simple orilice.
  • the feed device is adjusted or dimensioned to overfeed the evaporator, thatl is to supply liquid refrigerant in excess of the amount evaporated in the coil 10.
  • Gaseous refrigerant evaporated in the' coil 10 and excess liquid refrigerant passing throughthe coil. is carried by one sectionV 13 of a suction ⁇ line to atank 14, usually called an accumulator.
  • 'Liquid refrigerant is trapped in the accumulator While gaseous refrigerant is drawn off through Vthe other section 15 of the suction line to the intake side of a ⁇ compressor 16.
  • the compressor isdriven, in lthis instance, by'an electric motor M;
  • Pressurized refrigerant gas discharged from the compressor is delivered by way of ahotgas vline 17 tothe condenser 18 in which the refrigerantiscooled and having a level responsive actuator located a predetermined distance from the bottom of the tank.
  • the switch normally open but closes when the liquid level falls below the position in which the switch actator'is mounted. While a lloat device or other suitable level responsive means may be utilized for actuating the switch, the exemplary system is shown as equipped withtem'- perature responsive level control devices of the type dis'- closed in my copending application, Serial No.V 707,753, filed January 8, 1958.
  • the energizing circuit for the valve solenoid SOL-1 is also under control of a relay R which additionally controls the pump motor M.
  • a level control switch LS2 installed near the top of the accumulatortank is effective when closed to connect the relayacross the Y and relay R is energized.
  • Liquid refrigerant collecting in the accumulator 14 drains continuously by gravity ow to one or theother of two pumping tanks 25 and 26.
  • the tank 25 isV con# nected to the lower end of the accumulator by a line V27.
  • a check valve CVI interposed in this line prevents flow of gas or liquid back to the accumulator.
  • At itslower end the tank 25 is connected by a line 28 with the feed line 12.
  • a check valve CVZ interposed in the line 28 prevents flow of gas or liquid from the feed line tothe tank.
  • a vertically disposed riser or pipe 29 closed at its upper end opens at its lower end to the lowerporliquefied.Y
  • the liquid refrigerant then" passes by way of tion ofthe tank 25.
  • the pipe 29 also communicates' with the upper end of the tank 25 througha branch connection 30.
  • the pumping tank 26 is Similarly connected to the lower end of the-accumulator by a line Tal-equipped with a check valve CV3 preventing gas or liquid ow ⁇ back to the accumulaton
  • the lower end of the tank ⁇ 26 connects through a line 32 and check valve CV4 with the feedline 12.
  • a riser or pipe 33 alongside the tank 26 opens into the lower end of the tank and communicates with the upper end of the tank through a branch connection 34.
  • the pipe 33 is closed at its upper end.
  • Such venting is effected through a vent line 35 connected at one end to the section 13 of the suction line and at the otherV end by branch lines 36 and 37 with .the risers 29 'and 33.
  • Valves V2 and V3 in the branch lines control the opening and closing of the ventto the respective pumping tanks.
  • the valves are respectively provided with operating solenoids SOL-2 aud SOL-3.
  • a branch line 40 is extended from the liquid line 21 to a pressure reducing valve RV which has its outlet connected by a line 41 and branches 42 and 43 with the risers 29 and 33, respectively.
  • Valves V4 and V5 in the branch lines 42 and 43 control the flow of gas to the respective risers and their associated pumping tanks.
  • Solenoids SOL-4 and SOL- are provided for operating the valves.
  • the invention provides simple yet elective control means for operating the various valves to condition the system so that the tanks 25 and 26 alternately receive liquid refrigerant from the accumulator and then discharge it under pressure to the feed line. More particularly, the valves are operated in a sequence such that when one pumping tank is being lled the other is discharging into the feed line, thus providing a continuous supply of super-cooled liquid refrigerant to the evaporator.
  • the controls for effecting the desired sequence of valve operations include a control relay CR and a pair of level responsive switches LS3 and LS4. These switches are installed in the riser 29 to operate in accordance with the level of liquid refrigerant in the pumping tank 25.
  • the arrangement is such that the switches normally tend to close and ⁇ open only when their associated level responsive actuating means is immersed in liquid refrigerant.
  • the switch LS3 closes when substantially all of the liquid refrigerant is forced from the tank 25.
  • Slv/izh LS4 is closed until the tank 25 is completely
  • the operation of the refrigerating system constructed and arranged in the above manner is completely automatic.
  • valve Solenoids SOL-3 and SOL-4 The opening of switch contacts CR-2 by the relay CR interrupts the circuits for valve Solenoids SOL-3 and SOL-4.
  • Valve V3 closes to interrupt the venting of tank 26 and valve V4 closes tol shut off the supply of pressurizing uid to the tank 25.
  • the closure of switch contacts CR-3 completes energizing circuits for valve Solenoids SOL-2 and SOL-5.
  • Valve V2 opens to vent tank 25 and thus condition it to receive liquid refrigerant by gravity ow from the accumulator.
  • Valve V5 opens to admit pressurizing uid to the tank 26 to force the liquid refrigerant from it through the feed line to the evaporator.
  • level switch LS4Y opens to interrupt the holding circuit for relay CR.
  • the relay becomes deenergized, opens the circuits for Solenoids SOL-2 and SOL-5 and closes the circuits for Solenoids SOL-4 and SOL-3.
  • Valves V2 and V5 accordingly close and valves V4 and V3 are opened. This returns the system to the condition rst described with tank 26 vented and receiving liquid refrigerant from the accumulator.
  • Tank 25, on the other hand, is sealed off from the suction line and receives pressurized gas from the reducing valve RV. Liquid refrigerant is accordingly supplied from the evaporator to the pumping tank 25.
  • the above sequence of operations continues with first one pumping tank supplying liquid refrigerant to the evaporator while ⁇ the other tank receives a fresh supply of liquid from the accumulator. Then at the proper time the other tank takes up the feeding job while .the first tank is being relled.
  • a refrigeratiug system including a suction line for returning gaseous refrigerant from an evaporator to a compressor and a feed line for liquid refrigerant, an accumulator tank connected to both of said lines operative to collect liquid refrigerant entrained with the gaseous refrigerant in the suction line and to flash off gas and reduce the pressure of liquid refrigerant received from the feed line,- a .pumping tank connected to receive acumulated liquid refrigerant from said accumulator tank,
  • a reftigerating system in combination, an evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator while permitting gaseous refrigerant 'to return to the compressor, a condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, means including conduits operative to deliver the liquid refrigerant to said accumulator tank, a pair of pumping tanks connected to said accumulator tank for receiving liquid refrigerant therefrom by gravity ow, conduit means connecting said pumping tanks with the inlet side of said evaporator, and means for pressurizing said pumping tanks alternately to force the liquid refrigerant therein to said evaporator.
  • a refrigerating system in combination, an evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator while permitting gaseous refrigerant to return to the compressor, a condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, a receiver connected to receive and store refrigerant liquefied in said condenser, said receiver being connected todeliver liquid refrigerant to said accumulator tank, a pair of pumping tanks connected to said accumulator tank for receiving liquid refrigerant therefrom by gravity ow, conduit means connecting said pumping tanks with the inlet side of said evaporator, conduit means connecting said pumping tanks to receive pressurized refrigerant from said receiver, and valve means operable to direct the flow of pressurized refrigerant to said pumping
  • a refrigerating system in combination, an evaporator, a compressor, a suction line for returning spent gaseous refrigerant from the loutlet side of the evaporator to the suction side of the compressor, an accumulator tank interposed in said suction line operative to separate the liquid from the gaseous refrigerant received from said evaporator, a condenser connected to receive and liquefy compressed gaseous refrigerant received from said compressor, a receiver connectedvto receive and store the refrigerant liquefied in said condenser, a feed line connecting said receiver with said accumulator tank,
  • t valve means in said feed line, liquid level responsive said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator while permitting gaseous refrigerant vto return to the compressor, av condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, a receiver connected to receive and store refrigerant liquefied in said condenser, said receiver being connected to deliver liquid refrigerant to said accumulator tank, a pair of pumping tanks connected to said accumulator tank for receiving liquid refrigerant therefrom by gravity ow, conduit means connecting said Y pumping tanks with the inlet side of said evaporator, and means for introducing pressurized refrigerant from said receiver into saidv pumping tanks alternately to force the liquid refrigerant therein to said evaporator.
  • a refrigerating system in combination, an evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator While permitting gaseous refrigerant to return to the compressor, a condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, a receiver connected to receive and store refrigerant liquefied in said condenser, said receiver being connected to deliver liquid refrigerant to said accumulator tank, a pumping tank connected to receive liquid refrigerant from said accumulator tank by gravity flow, conduit means connecting said pumping tank with the inlet side of said evaportor, conduit means connecting said pumping tank to receive flashed liquid refrigerant from said receiver for forcing the liquid refrigerant in means operative to open said valve and admit liquid refrigerant Ifrom said receiver to
  • a refrigerating system in combination, an evaporator, a compressor, a suction line for returning spent gaseous refrigerant from the outlet side of the evaporator to the suction side of the compressor, an accumulator tank interposed in said suction line operative to separate the liquid from the gaseous refrigerant received from said evaporator, a condenser connected to receive and liquefy compressed gaseous refrigerant received from said compressor, a receiver connected to receive and store the refrigerant liquefied in said condenser, a feed line con- ⁇ necting said receiver with said accumulator tank, valve means in said feed line, liquid level responsive means operative to open said valve and admit liquid refrigerant from said receiver to said accumulator tank when the liquid in the tank falls below a predetermined level, the pressure of the admitted liquid being reduced to suction line pressure with a consequent removal of Hash gas and supercooling of the liquid refrigerant, means for drawing off the supercooled liquid refrigerant
  • a refrigerating system in combination, an evaporator, a compressor, a suction line for returning spent gaseous refrigerant from the outlet side of the evaporator to the suction side of the compressor, an accumulator tank interposed in said suction line operative to separate the liquid from the gaseous refrigerant received from said evaporator, a condenser connected to receive and liquefy compressed gaseous refrigerant received from said compressor, a receiver connected to receive and store the refrigerant liquefied in said condenser, a feed line connecting said receiver with said accumulator tank, valve means in said feed line, control means operative to open said valve and admit liquid refrigerant to said accumulator tank as it collects in the condenser or receiver, the pressure of the admitted liquid being reduced to suction line pressure with'a consequent removal of flash gas and supercooling of the liquid refrigerant, means for drawing ot the supercooled liquid refrigerant at suction line pressure, and means for

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Compression-Type Refrigeration Machines With Reversible Cycles (AREA)

Description

Sept. 13, 1960 J. E. wATKlNs LOW PRESSURE REFRIGERATING SYSTEMS Filed Jan. 2, 1959 R w ma n m w E f if. N E D N I'l W O), AY ed mio m 1 ad@ M R o L v C w M MA w E E C MN w wm 5 m m, s w U l c m /I Vl R l wx. m www A L m P w H Z. w l: E
United ,States Patent 2,952,131 Low PRESSURE REFRIGERATING SYSTEMS John E. Watkins, 307 Lake Sit., Maywood, Ill.V Filed Jan. z, 1959, ser. No. 784,683 9 claims.L (ci. Yisz- 174) The invention relates to refrigerating systems vgenerally, and more vparticularly to large capacity refrigerating systems suitable for commercial installation.
One object of the invention is to provide a refrigerating system of the above general character Ywhich is simpler in construction, easier and cheaper ,to mantainand more efficient in operation-'than refrigerating systems heretofore available. 9 l 1 Anotherobject is to provide arefrigerating system in which flash gas entering the evaporator is minimized to insure higher coil eiliciency and to permit vthe use Vof liquid lines of minimumV diameter. Y f Y y Another object -is to provide a fsystern` in'which the components are interrelated in a novely manner whichl reduces superheating ofthe spent refrigerant and 4enables the compressorlto operate withhigher volumetric elliciency and reduced power cost. l I
Still another object is to provide a refrigerating system in which the evaporator is continuously fed. an excess of liquid refrigerant and in which theiexcess `refrigerant is trapped and -recirculated through' the evaporator withd 2,952,137!- Patented Sept. 13,` 1960 a connecting line 19 to a receiver 20in which the refrigerant is temporarily stored. The receiver thus pro-v To obtain maximum eiciency, this pressure reduction isV effected in the accumulator 14 into which the liquid refrigerant from the receiver is introduced and combined with excess refrigerant passing through the evaporator-.f
The pressure reduction effectively removes all ash gas from the liquid refrigerant and further reduces the tem# perature or supercools the trapped liquid refrigerant. Further, in accordance with the invention, novel means is provided -for repressurzing the supercooled liquid for feeding it through theevaporator coils.
YIn carrying out the inventionthe receiver -20 is connected to the accumulator 14 by a liquid line 21. Flow of liquid to the accumulator is controlled by-a Valve VI actuated'by a solenoid SOL-1. A hand-operated metering valve MV may be interposed between the valve VI and the :accumulator Vto provide for manual-.adjustmentl of the feed rate and insure smooth liquidfeed.-
The solenoid valve V1 is so arranged that the' valve is l closed when the solenoid is deenergized. In the present instancel provisionismade for energizing the solenoid when the liquid refrigerant in the accumulator tank falls to a predetermined level. For this purpose the accumuf lator tank is equipped with a level control switch LS1I out requiring the usual complicated and expensive pumps tion of the preferred embodiment `illustrated inthe accompanying single drawing figure.
While the invention is susceptibleof various modifications and alternative constructions, a single preferred embodiment has been shown in the1drawing and will be described in detail herein. Thereis no intention to limit the invention to the specific form disclosed but the intention is to cover all modifications andadaptations falling vwithin the spirit and scope of vthe invention as more broadly or generallycharacterized in the appended claims. Y
In the exemplary refrigerating system one or more evaporator coils, of which only one coil 10 and itsfeed device have been shown, areconnected to receive a supply of liquid refrigerant from a feed line 12. The feed device may be a conventional feed valve or a simple orilice. As the invention contemplates operation of the evaporator in a Hooded condition, the feed device is adjusted or dimensioned to overfeed the evaporator, thatl is to supply liquid refrigerant in excess of the amount evaporated in the coil 10.
Gaseous refrigerant evaporated in the' coil 10 and excess liquid refrigerant passing throughthe coil. is carried by one sectionV 13 of a suction` line to atank 14, usually called an accumulator. 'Liquid refrigerant is trapped in the accumulator While gaseous refrigerant is drawn off through Vthe other section 15 of the suction line to the intake side of a `compressor 16. The compressor isdriven, in lthis instance, by'an electric motor M;
Pressurized refrigerant gas discharged from the compressor is delivered by way of ahotgas vline 17 tothe condenser 18 in which the refrigerantiscooled and having a level responsive actuator located a predetermined distance from the bottom of the tank. The switchis normally open but closes when the liquid level falls below the position in which the switch actator'is mounted. While a lloat device or other suitable level responsive means may be utilized for actuating the switch, the exemplary system is shown as equipped withtem'- perature responsive level control devices of the type dis'- closed in my copending application, Serial No.V 707,753, filed January 8, 1958.
The energizing circuit for the valve solenoid SOL-1 is also under control of a relay R which additionally controls the pump motor M. A level control switch LS2 installed near the top of the accumulatortank is effective when closed to connect the relayacross the Y and relay R is energized.
conductors L1, -L2 of a power supplyv line. As long as the liquid level in the accumulator is below the ,level at which the switch LS2 is installed as it is during normal operation of the system, the switch remains closed Relay R when energized closes switch R-1 to complete the running circuit for the pump motor M. It also closes a switch R-2 to prepare the circuit for solenoid SOL-1. If for any reason the level of liquid in the accumulator rises to the upper level responsive means, switch vLSZ` opens to deenergize relay R and thus stop the compressor motor. By opening the switch R-2, inadvertent energization ofthe valve solenoid SOL-l and opening of the valve V1 is effectively prevented.
Liquid refrigerant collecting in the accumulator 14 drains continuously by gravity ow to one or theother of two pumping tanks 25 and 26. The tank 25 isV con# nected to the lower end of the accumulator by a line V27. A check valve CVI interposed in this line prevents flow of gas or liquid back to the accumulator. At itslower end the tank 25 is connected by a line 28 with the feed line 12. A check valve CVZ interposed in the line 28 prevents flow of gas or liquid from the feed line tothe tank. A vertically disposed riser or pipe 29 closed at its upper end opens at its lower end to the lowerporliquefied.Y The liquid refrigerant then" passes by way of tion ofthe tank 25. The pipe 29 also communicates' with the upper end of the tank 25 througha branch connection 30.
The pumping tank 26 is Similarly connected to the lower end of the-accumulator by a line Tal-equipped with a check valve CV3 preventing gas or liquid ow `back to the accumulaton The lower end of the tank `26 connects through a line 32 and check valve CV4 with the feedline 12. A riser or pipe 33 alongside the tank 26 opens into the lower end of the tank and communicates with the upper end of the tank through a branch connection 34. The pipe 33, of course, is closed at its upper end.
Provision is made for venting the pumping .tanks 25 andr26 alternately to the suction side of the system to equalize the pressure with that in the accumulator andV thus permit gravity flow of liquid .refrigerant into the vented pumping tank. Such venting is effected through a vent line 35 connected at one end to the section 13 of the suction line and at the otherV end by branch lines 36 and 37 with .the risers 29 'and 33. Valves V2 and V3 in the branch lines control the opening and closing of the ventto the respective pumping tanks. The valves are respectively provided with operating solenoids SOL-2 aud SOL-3.
Provision is also made for introducing pressurized ygase'ous refrigerant into the pumping tanks alternately to force the liquid refrigerant therein through the feed lines 12 to the evaporator. For this purpose, a branch line 40 is extended from the liquid line 21 to a pressure reducing valve RV which has its outlet connected by a line 41 and branches 42 and 43 with the risers 29 and 33, respectively. Valves V4 and V5 in the branch lines 42 and 43 control the flow of gas to the respective risers and their associated pumping tanks. Solenoids SOL-4 and SOL- are provided for operating the valves.
The invention provides simple yet elective control means for operating the various valves to condition the system so that the tanks 25 and 26 alternately receive liquid refrigerant from the accumulator and then discharge it under pressure to the feed line. More particularly, the valves are operated in a sequence such that when one pumping tank is being lled the other is discharging into the feed line, thus providing a continuous supply of super-cooled liquid refrigerant to the evaporator.
The controls for effecting the desired sequence of valve operations include a control relay CR and a pair of level responsive switches LS3 and LS4. These switches are installed in the riser 29 to operate in accordance with the level of liquid refrigerant in the pumping tank 25. The arrangement is such that the switches normally tend to close and `open only when their associated level responsive actuating means is immersed in liquid refrigerant. Thus, the switch LS3 closes when substantially all of the liquid refrigerant is forced from the tank 25. Slv/izh LS4 is closed until the tank 25 is completely The operation of the refrigerating system constructed and arranged in the above manner is completely automatic. Assume by way of example, that operation is proceeding with the pumping tank 25 supplying refrigerant to the feed line 12 and the evaporator. Relay CR is deenergized. Valve V2 is closed, sealing off the tank 25 from the suction line and valve V4 is open, admitting pressurized fluid to the tank to drive out the liquid refrigerant. At the same time, valve V3 is open, venting pumping tank 26 and valve V5 is closed, shutting olf the ow of pressurized fluid to the tank. Liquid refrigerant accordingly flows by gravity from the accumulator 14 into the tank 26.
The above conditions prevail until the liquid level in the tank 25 falls below the level switch LS3. When that occurs, the switch closes to connect the winding of relay CR across the line conductors L1-L2. Relay CR upon energizing closes switch contacts CR-l to complete a holding circuit for itself by way of level switch LS4 which is closed and vremains closed until the tank 25 is again filled with liquid refrigerant to the level of that switch.
The opening of switch contacts CR-2 by the relay CR interrupts the circuits for valve Solenoids SOL-3 and SOL-4. Valve V3 closes to interrupt the venting of tank 26 and valve V4 closes tol shut off the supply of pressurizing uid to the tank 25. The closure of switch contacts CR-3 completes energizing circuits for valve Solenoids SOL-2 and SOL-5. Valve V2 opens to vent tank 25 and thus condition it to receive liquid refrigerant by gravity ow from the accumulator. Valve V5 opens to admit pressurizing uid to the tank 26 to force the liquid refrigerant from it through the feed line to the evaporator.
The tanks 25 and 26 and their connections are so proportioned that the filling of the tank 25 proceeds at a slightly greater rate than the emptying of the tank 26. When liquid level in the tank 25 reaches the upper level responsive device, level switch LS4Y opens to interrupt the holding circuit for relay CR. The relay becomes deenergized, opens the circuits for Solenoids SOL-2 and SOL-5 and closes the circuits for Solenoids SOL-4 and SOL-3. Valves V2 and V5 accordingly close and valves V4 and V3 are opened. This returns the system to the condition rst described with tank 26 vented and receiving liquid refrigerant from the accumulator. Tank 25, on the other hand, is sealed off from the suction line and receives pressurized gas from the reducing valve RV. Liquid refrigerant is accordingly supplied from the evaporator to the pumping tank 25.
The above sequence of operations continues with first one pumping tank supplying liquid refrigerant to the evaporator while `the other tank receives a fresh supply of liquid from the accumulator. Then at the proper time the other tank takes up the feeding job while .the first tank is being relled.
The operating economies realizable with the improved system described above will be readily apparent to those skilled in the art. Power consumption is reduced to a minimum since only a small pressure differential between the high and low sides of the system is required to provide an ample flow of refrigerant through the evaporator. The compressor and Vthe condenser can therefore be operated at the lowest pressure level that will produce the quantity of liquid refrigerant required. Furthermore, the complete removal of flash gas from the liquid refrigerant and its supercooling in the process allows the evaporator to operate at peak e'lciency.
It is to be particularly noted that unusually high operating eiciency is attained without complicating the system. Actually, the plant equipment is greatly simplified. The components ofthe system are all of the simple, durable type which are little subject to wear and which require maintenance attention only at long intervals. mechanical pumps for circulating liquid coolant are dispensed with. Since `the feed liquid is supercooled and completely freed of ash gas, the liquid and suction lines may be of minimum size. Moreover, the accumulator and pumping drums may be assembled in a compact unit and installed in the engine room close to the compressor. When so installed, superheating of the suction gas is held to a negligible amount, thus enabling the compressor to operate the maximum volumetric eiciency.
I claim as my invention:
v1. lIn a refrigeratiug system including a suction line for returning gaseous refrigerant from an evaporator to a compressor and a feed line for liquid refrigerant, an accumulator tank connected to both of said lines operative to collect liquid refrigerant entrained with the gaseous refrigerant in the suction line and to flash off gas and reduce the pressure of liquid refrigerant received from the feed line,- a .pumping tank connected to receive acumulated liquid refrigerant from said accumulator tank,
and connections for introducing refrigerantfrom said feed line into said pumping tank to force the liquid refrigerant therein to said evaporator. q y
2. In a refrigerating system,in combination, Van evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, 'an accumulator tank'interposed in'said suction line operative to collect liquid refrigerantpassing through 'the evaporator Vwhileiperrnitting gaseous refrigerant to return to the compressor, a condenser connected tothe outlet of said compressor operative to cool and liquefy.compressed'refrigerant gas received from the accumulator, means'including conduits operative todeliver the liquid refrigerant to saidA accumulator tank, `a pumping tank connected to receive liquid refrigerant from said acc-umula't'or tank by gravity flow, conduitvmeans connecting said pumping tank with the inlet side of said evaporator, and means for pressurizing said pumping tank to force the liquid refrigerant therefrom through said evaporator.
3. In a reftigerating system, in combination, an evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator while permitting gaseous refrigerant 'to return to the compressor, a condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, means including conduits operative to deliver the liquid refrigerant to said accumulator tank, a pair of pumping tanks connected to said accumulator tank for receiving liquid refrigerant therefrom by gravity ow, conduit means connecting said pumping tanks with the inlet side of said evaporator, and means for pressurizing said pumping tanks alternately to force the liquid refrigerant therein to said evaporator.
4. In a refrigerating system, in combination, an evaporator, a compressor, 'a suction line connecting the discharge side of said evaporator with the suction inlet of the pumping tank to said evaporator, Tand independently operable valve means controlling the flow o f liquid refrigerant from said receiver to said accumulator tankand to said pumping tank. V-
6.`In a refrigerating system, in combination, an evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator while permitting gaseous refrigerant to return to the compressor, a condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, a receiver connected to receive and store refrigerant liquefied in said condenser, said receiver being connected todeliver liquid refrigerant to said accumulator tank, a pair of pumping tanks connected to said accumulator tank for receiving liquid refrigerant therefrom by gravity ow, conduit means connecting said pumping tanks with the inlet side of said evaporator, conduit means connecting said pumping tanks to receive pressurized refrigerant from said receiver, and valve means operable to direct the flow of pressurized refrigerant to said pumping tanks alternately.
7. In a refrigerating system, in combination, an evaporator, a compressor, a suction line for returning spent gaseous refrigerant from the loutlet side of the evaporator to the suction side of the compressor, an accumulator tank interposed in said suction line operative to separate the liquid from the gaseous refrigerant received from said evaporator, a condenser connected to receive and liquefy compressed gaseous refrigerant received from said compressor, a receiver connectedvto receive and store the refrigerant liquefied in said condenser, a feed line connecting said receiver with said accumulator tank,
t valve means in said feed line, liquid level responsive said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator while permitting gaseous refrigerant vto return to the compressor, av condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, a receiver connected to receive and store refrigerant liquefied in said condenser, said receiver being connected to deliver liquid refrigerant to said accumulator tank, a pair of pumping tanks connected to said accumulator tank for receiving liquid refrigerant therefrom by gravity ow, conduit means connecting said Y pumping tanks with the inlet side of said evaporator, and means for introducing pressurized refrigerant from said receiver into saidv pumping tanks alternately to force the liquid refrigerant therein to said evaporator.
5. In a refrigerating system, in combination, an evaporator, a compressor, a suction line connecting the discharge side of said evaporator with the suction inlet of said compressor, an accumulator tank interposed in said suction line operative to collect liquid refrigerant passing through the evaporator While permitting gaseous refrigerant to return to the compressor, a condenser connected to the outlet of said compressor operative to cool and liquefy compressed refrigerant gas received from the compressor, a receiver connected to receive and store refrigerant liquefied in said condenser, said receiver being connected to deliver liquid refrigerant to said accumulator tank, a pumping tank connected to receive liquid refrigerant from said accumulator tank by gravity flow, conduit means connecting said pumping tank with the inlet side of said evaportor, conduit means connecting said pumping tank to receive flashed liquid refrigerant from said receiver for forcing the liquid refrigerant in means operative to open said valve and admit liquid refrigerant Ifrom said receiver to said accumulator tank when the liquid in the tank falls below a predetermined level, the pressure of the admitted liquid being reduced to suction line pressure with la consequent removal of flash gas and supercooling of the liquid refrigerant, means for drawing off the supercooled liquid refrigerant at suction line pressure, and means for repressurizing the drained off liquid refrigerant and delivering it to the inlet side of said evaporator.
8. In a refrigerating system, in combination, an evaporator, a compressor, a suction line for returning spent gaseous refrigerant from the outlet side of the evaporator to the suction side of the compressor, an accumulator tank interposed in said suction line operative to separate the liquid from the gaseous refrigerant received from said evaporator, a condenser connected to receive and liquefy compressed gaseous refrigerant received from said compressor, a receiver connected to receive and store the refrigerant liquefied in said condenser, a feed line con-` necting said receiver with said accumulator tank, valve means in said feed line, liquid level responsive means operative to open said valve and admit liquid refrigerant from said receiver to said accumulator tank when the liquid in the tank falls below a predetermined level, the pressure of the admitted liquid being reduced to suction line pressure with a consequent removal of Hash gas and supercooling of the liquid refrigerant, means for drawing off the supercooled liquid refrigerant at suction line pressure including a pair of auxiliary tanks having connections vwith said accumulator tank and with said receiver, and valve means operative to control said connections so that one tank receives liquid refrigerant from the accumulator tank While the other is pressurized by refrigerant from the receiver to force the liquid refrigerant therein to said evaporator.
9. In a refrigerating system, in combination, an evaporator, a compressor, a suction line for returning spent gaseous refrigerant from the outlet side of the evaporator to the suction side of the compressor, an accumulator tank interposed in said suction line operative to separate the liquid from the gaseous refrigerant received from said evaporator, a condenser connected to receive and liquefy compressed gaseous refrigerant received from said compressor, a receiver connected to receive and store the refrigerant liquefied in said condenser, a feed line connecting said receiver with said accumulator tank, valve means in said feed line, control means operative to open said valve and admit liquid refrigerant to said accumulator tank as it collects in the condenser or receiver, the pressure of the admitted liquid being reduced to suction line pressure with'a consequent removal of flash gas and supercooling of the liquid refrigerant, means for drawing ot the supercooled liquid refrigerant at suction line pressure, and means for repressurizing the drained 0E liq'uid refrigerant and delivering it to the inlet side of said evaporator.
References'Cited in the le of this patent Y' UNITED l'STATES PATENTS 2,159,251 'Brizzolara e May 23, 19,39 2,512,869 McBroom June 27, 1950 2,570,979 Phillips Oct. 9, 1951 2,589,859 Phillips Mar. 18, 1952 2,590,741 Watkins Mar. 25,` 1952 2,617,264 McGovern Nov. 11, 1952 2,617,265 Ru? Nov. 11, 1952 2,655,794 Ruif Oct. 20, 1953 2,778,195 Christensen Jan. 22, 1957 2,871,673 Richards Feb. 3, 1959
US784683A 1959-01-02 1959-01-02 Low pressure refrigerating systems Expired - Lifetime US2952137A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
US784683A US2952137A (en) 1959-01-02 1959-01-02 Low pressure refrigerating systems

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
US784683A US2952137A (en) 1959-01-02 1959-01-02 Low pressure refrigerating systems

Publications (1)

Publication Number Publication Date
US2952137A true US2952137A (en) 1960-09-13

Family

ID=25133208

Family Applications (1)

Application Number Title Priority Date Filing Date
US784683A Expired - Lifetime US2952137A (en) 1959-01-02 1959-01-02 Low pressure refrigerating systems

Country Status (1)

Country Link
US (1) US2952137A (en)

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3164973A (en) * 1963-03-28 1965-01-12 John E Watkins Refrigerating systems
US3352124A (en) * 1966-02-11 1967-11-14 John E Watkins Liquid refrigerant recirculating system
US3643460A (en) * 1970-09-11 1972-02-22 Frick Co Gravity refrigerant recirculation
US3797265A (en) * 1970-09-11 1974-03-19 Frick Co Pressurized refrigerant feed with recirculation
US3827249A (en) * 1973-03-12 1974-08-06 Frick Co Pressurized refrigerant recirculation system with control means
US3945219A (en) * 1970-08-25 1976-03-23 Kabushiki Kaisha Maekawa Seisakusho Method of and apparatus for preventing overheating of electrical motors for compressors
US4027496A (en) * 1976-06-22 1977-06-07 Frick Company Dual liquid delivery and separation apparatus and process
EP0033560A3 (en) * 1980-02-04 1982-05-26 Engineering Management Services Limited Method of refrigeration and a refrigeration system
US5189885A (en) * 1991-11-08 1993-03-02 H. A. Phillips & Co. Recirculating refrigeration system
US5365748A (en) * 1991-10-23 1994-11-22 Guangjing Li Screw compressor ice making packaged unit
US20120204583A1 (en) * 2009-10-14 2012-08-16 Carrier Corporation Receiver with flow metering device

Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2159251A (en) * 1936-11-14 1939-05-23 Robert T Brizzolara Refrigeration method and apparatus
US2512869A (en) * 1948-04-24 1950-06-27 James C Mcbroom Method and apparatus for circulating refrigerants
US2570979A (en) * 1949-06-23 1951-10-09 Harry A Phillips Compound system for liquid refrigerant return
US2589859A (en) * 1948-11-12 1952-03-18 Harry A Phillips Suction line liquid return trap
US2590741A (en) * 1949-01-24 1952-03-25 John E Watkins Liquid return trap in refrigerating systems
US2617265A (en) * 1951-01-16 1952-11-11 V C Patterson & Associates Inc Oil removal system for refrigeration apparatus
US2617264A (en) * 1950-03-20 1952-11-11 Mojonnier Bros Co Evaporator structure in refrigerating apparatus
US2655794A (en) * 1952-12-09 1953-10-20 V C Patterson & Associates Inc Oil removal system for refrigeration apparatus
US2778195A (en) * 1953-10-20 1957-01-22 Creamery Package Mfg Co Refrigerant liquid return means
US2871673A (en) * 1956-10-08 1959-02-03 H A Phillips Company Liquid return system

Patent Citations (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2159251A (en) * 1936-11-14 1939-05-23 Robert T Brizzolara Refrigeration method and apparatus
US2512869A (en) * 1948-04-24 1950-06-27 James C Mcbroom Method and apparatus for circulating refrigerants
US2589859A (en) * 1948-11-12 1952-03-18 Harry A Phillips Suction line liquid return trap
US2590741A (en) * 1949-01-24 1952-03-25 John E Watkins Liquid return trap in refrigerating systems
US2570979A (en) * 1949-06-23 1951-10-09 Harry A Phillips Compound system for liquid refrigerant return
US2617264A (en) * 1950-03-20 1952-11-11 Mojonnier Bros Co Evaporator structure in refrigerating apparatus
US2617265A (en) * 1951-01-16 1952-11-11 V C Patterson & Associates Inc Oil removal system for refrigeration apparatus
US2655794A (en) * 1952-12-09 1953-10-20 V C Patterson & Associates Inc Oil removal system for refrigeration apparatus
US2778195A (en) * 1953-10-20 1957-01-22 Creamery Package Mfg Co Refrigerant liquid return means
US2871673A (en) * 1956-10-08 1959-02-03 H A Phillips Company Liquid return system

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3164973A (en) * 1963-03-28 1965-01-12 John E Watkins Refrigerating systems
US3352124A (en) * 1966-02-11 1967-11-14 John E Watkins Liquid refrigerant recirculating system
US3945219A (en) * 1970-08-25 1976-03-23 Kabushiki Kaisha Maekawa Seisakusho Method of and apparatus for preventing overheating of electrical motors for compressors
US3643460A (en) * 1970-09-11 1972-02-22 Frick Co Gravity refrigerant recirculation
US3797265A (en) * 1970-09-11 1974-03-19 Frick Co Pressurized refrigerant feed with recirculation
US3827249A (en) * 1973-03-12 1974-08-06 Frick Co Pressurized refrigerant recirculation system with control means
US4027496A (en) * 1976-06-22 1977-06-07 Frick Company Dual liquid delivery and separation apparatus and process
EP0033560A3 (en) * 1980-02-04 1982-05-26 Engineering Management Services Limited Method of refrigeration and a refrigeration system
US5365748A (en) * 1991-10-23 1994-11-22 Guangjing Li Screw compressor ice making packaged unit
US5189885A (en) * 1991-11-08 1993-03-02 H. A. Phillips & Co. Recirculating refrigeration system
US20120204583A1 (en) * 2009-10-14 2012-08-16 Carrier Corporation Receiver with flow metering device
US9057548B2 (en) * 2009-10-14 2015-06-16 Carrier Corporation Receiver with flow metering device

Similar Documents

Publication Publication Date Title
US2952137A (en) Low pressure refrigerating systems
US2589859A (en) Suction line liquid return trap
US2715317A (en) Automatic load control for a reversible heat pump and air conditioner
US3360958A (en) Multiple compressor lubrication apparatus
US2949750A (en) Heat exchange system of the evaporative type with means for maintaining liquid supply line pressure
US2375157A (en) Heat pump system
TW293079B (en)
US2841962A (en) Return apparatus for a two-stage refrigeration system
US2966043A (en) Balanced circulating system for refrigeration
US2133962A (en) Refrigerating apparatus
US3621670A (en) Lubricating oil equalizing system
US3234753A (en) Hot gas refrigeration defrosting system
US2720084A (en) Energy storage for air conditioning systems
US2590741A (en) Liquid return trap in refrigerating systems
US3744264A (en) Refrigeration apparatus and method of operating for powered and non-powered cooling modes
US3848425A (en) Low pressure refrigeration system
US3487656A (en) Refrigeration system with refrigerant return means
US2253623A (en) Refrigerating apparatus
US2722108A (en) Refrigeration control service
US3643460A (en) Gravity refrigerant recirculation
US1907885A (en) Refrigeration system and method
US3352124A (en) Liquid refrigerant recirculating system
US2466863A (en) Refrigerant injector and surge drum arrangement
US3003332A (en) Control means for refrigerating system
US2282878A (en) Air conditioning system