US20020026807A1 - Refrigeration systems - Google Patents

Refrigeration systems Download PDF

Info

Publication number
US20020026807A1
US20020026807A1 US09/943,534 US94353401A US2002026807A1 US 20020026807 A1 US20020026807 A1 US 20020026807A1 US 94353401 A US94353401 A US 94353401A US 2002026807 A1 US2002026807 A1 US 2002026807A1
Authority
US
United States
Prior art keywords
accumulator
refrigeration system
refrigerant
compressor
evaporator
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.)
Granted
Application number
US09/943,534
Other versions
US6449980B1 (en
Inventor
David Minister
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.)
NBS Cryo Research Ltd
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
Assigned to NBS CRYO RESEARCH LIMITED reassignment NBS CRYO RESEARCH LIMITED ASSIGNMENT OF ASSIGNORS INTEREST (SEE DOCUMENT FOR DETAILS). Assignors: MINISTER, DAVID JOHN
Publication of US20020026807A1 publication Critical patent/US20020026807A1/en
Application granted granted Critical
Publication of US6449980B1 publication Critical patent/US6449980B1/en
Anticipated expiration legal-status Critical
Expired - Fee Related 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
    • F25B7/00Compression machines, plants or systems, with cascade operation, i.e. with two or more circuits, the heat from the condenser of one circuit being absorbed by the evaporator of the next circuit
    • 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
    • F25B43/00Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
    • F25B43/006Accumulators
    • 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
    • F25B2400/01Heaters
    • 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
    • F25B2500/26Problems to be solved characterised by the startup of the refrigeration cycle

Definitions

  • the present invention relates to refrigeration systems, and particularly (but not exclusively) to refrigeration systems for ultra-low temperature storage compartments.
  • a basic refrigeration system comprises a compressor which compresses gaseous refrigerant and supplies it to a heat exchanger where the refrigerant is condensed to a liquid, giving out heat energy.
  • This liquid refrigerant then passes through a flow restrictor into an evaporator whereat the low pressure and the expansion of the refrigerant causes the refrigerant to vaporise thereby absorbing heat.
  • the gaseous refrigerant then passes out of the evaporator back to the compressor to begin the cycle again.
  • An accumulator is usually provided in the return path between the evaporator and the compressor, and the accumulator collects any liquid vapour passing through the evaporator so as to prevent its entry into the compressor.
  • Refrigeration systems including dual stage systems, seldom operate continuously, but instead switch as appropriate between an on-time and an off-time so as to maintain the desired temperature.
  • This on/off switching aims to make the operation of the refrigeration system as efficient as possible, and is usually controlled thermostatically.
  • an accumulator is effectively to protect the compressor by preventing liquid refrigerant from entering it at the start of an on-time, the accumulator needs to be able to hold all of the charge of refrigerant that passes through the evaporator in the off-time.
  • the system starts an on-time, it takes a while for the liquid refrigerant in the accumulator to vaporise and return to the compressor.
  • the slow rate of evaporation causes the pressure at the input to the compressor to drop to a low level until a sufficient amount of vapour is available for compression, to be passed round the system. This low pressure at the start of a period of operation drastically reduces the volumetric efficiency of the compressor and prolongs the on-time.
  • the compressor which consumes the most energy in the cycle, operates at the beginning of an on-time at a lower efficiency.
  • the efficiency i.e. the amount of cooling achieved per unit of energy input
  • a refrigeration system comprising a compressor, an evaporator to which refrigerant compressed by the compressor is supplied through a flow restrictor, and return means to direct back to the compressor refrigerant expanded in the evaporator, in which system the return means includes an accumulator in which may collect any liquid refrigerant leaving the evaporator, the accumulator being provided with heating means to evaporate liquid refrigerant collected by the accumulator.
  • the heating means provides sufficient heat to the liquid refrigerant in the accumulator to cause at least partial vaporisation thereof. Heating the accumulator causes the liquid refrigerant to vaporise more rapidly and at a higher pressure. This gaseous refrigerant then can return to the compressor to pass round the cycle.
  • the time taken for the compressor to achieve optimum efficiency is dramatically reduced, and in consequence the length of any on-time may be significantly shortened. Tests have shown a 40%-50% reduction in the average duration of on-times.
  • a controller for the heating means which controller is arranged to cause the heating means to operate for an interval at the commencement of a period of refrigeration following a period of inactivity of the system.
  • the duration of the heating interval may preferably be between 2 and 6 minutes, with 3-4 minutes being even more preferred.
  • the control of the duration of the heating interval is dependent on a number of factors, such as the temperature of the refrigerant.
  • the heating means may be electrically powered.
  • the heating means may be integrally formed with the accumulator, or may be a separate unit applied to the outside thereof. If applied separately, the heating means may be in the form of a flexible electric heating pad placed against a portion, preferably at least a lower portion, of the accumulator. Alternatively the heating means could utilise hot gas from other parts of the high or low side, flow of which could be controlled by a solenoid valve.
  • the controller may comprise or include a microprocessor adapted to operate the heating means.
  • the controller may operate in response to data pre-stored therein.
  • the controller may operate in response to data received from external sources such as a pressure sensor, temperature sensors or other control equipment.
  • the present invention is applicable to various refrigeration systems, but will find a particular application to low temperature dual-stage systems.
  • the heating means could be applied to both an accumulator on the low-side and an accumulator on the high-side.
  • the present invention offers at least two further advantages. Firstly if the heater should fail, the system can still continued to operate as an existing system thereby not increasing the risk of damage to the goods stored in a freezer using such a refrigeration system. In effect it is fail-safe. Secondly, use of the present invention simplifies the task of charging the system with refrigerant during manufacture. In existing systems, the amount of refrigerant introduced into the system has to be carefully controlled. Too little refrigerant causes poor performance, but if too much is contained, not only can performance suffer, but more importantly refrigerant condensing during the off-time can overflow the condenser and flood the compressor. In systems according to the present invention larger capacity accumulators may be used without sacrificing performance, as would be the case in existing systems. Therefore, a greater degree of variation in the amount of refrigerant introduced can be tolerated and the process of manufacture simplified.
  • a low-temperature storage compartment such as a freezer, incorporating a refrigeration system as hereinbefore described.
  • FIG. 1 shows a schematic diagram of one embodiment of a dual stage refrigeration system according to the present invention.
  • the refrigeration system shown in FIG. 1 has two discrete cycles; one generally termed the high-side (labelled A), and the other generally termed the low-side (labelled B).
  • the low-side draws heat from the area to be cooled
  • the high-side is adapted to cool the refrigerant of the low-side and dissipate that heat to the external environment.
  • Separate refrigerants flow around the two cycles and whilst they thermally interact they do not come into direct contact.
  • the types of refrigerant used are well know in the prior art so will not be discussed in detail.
  • the direction of flow is indicated by arrows.
  • the high-side cycle comprises a compressor 10 which receives gaseous refrigerant from a return pipe 12 .
  • the compressor pressurises the gaseous refrigerant and pumps it out through a discharge pipe 14 into the condenser 16 .
  • heat energy is dissipated from the condensing refrigerant to the external atmosphere.
  • the thus liquefied refrigerant passes out of the condenser 16 into a flow-restricting capillary pipe 18 .
  • liquid high-side refrigerant exits the capillary tube 18 and is allowed to expand. This expansion cause the absorption of heat thereby cooling refrigerant passing round the low-side (herein after termed low-side refrigerant). Gaseous high-side refrigerant then passes back to condenser 10 through a return pipe 12 .
  • the high-side and low-side refrigerants are allowed to thermally interact, but do not come into physical contact.
  • the low-side cycle operates in a broadly similar way.
  • Gaseous refrigerant enter the compressor 30 from a low-side return pipe 32 and is pressurised.
  • Pressurised refrigerant passes out of the compressor 30 to a de-super-heating coil 34 , and then to an oil separator 36 .
  • oil separator 36 any oil picked up during passage of the refrigerant through the compressor is separated and returned to the compressor 30 through oil return pipe 38 .
  • the refrigerant subsequently passes along feeder pipe 40 to the heat exchanger assembly 20 .
  • low-side refrigerant is cooled by the high-side refrigerant.
  • the cooled low-side refrigerant then passes out of heat exchanger unit 20 through a low-side discharge pipe 42 .
  • the refrigerant then passes through a flow restrictor, which in this embodiment is low-side capillary tube 46 .
  • the low-side refrigerant passes from the capillary tube 46 into an evaporator 48 .
  • the evaporator 48 At least a major portion of the low-side refrigerant changes state from liquid to gas and absorbs heat from the surrounding area, thereby effecting cooling.
  • Gaseous refrigerant passing out of the evaporator 48 returns to the compressor 30 through the low-side return pipe 32 .
  • an accumulator 50 Arranged between the discharge end of the evaporator 46 and the return pipe 32 there is provided an accumulator 50 .
  • the accumulator is adapted to prevent any liquid refrigerant passing through the evaporator from entering the low-side return pipe 32 and thereby gaining access to the compressor 30 . If liquid refrigerant were able to enter the compressor 30 , it could cause serious damage.
  • low-side refrigerant will tend to condense within the evaporator 48 and will collect in the accumulator 50 .
  • the low-side refrigerant will vaporise and return to the compressor to start the cycle. As mentioned above the slow rate of vaporisation in prior art systems reduces the efficiency of the system.
  • the accumulator 50 is provided with a heater 52 disposed therearound.
  • the heater 52 is operated at the beginning of an on-time to increase the rate of vaporisation of the low-side refrigerant in the accumulator 50 .
  • a controller 54 possibly including a microprocessor chip, is operatively connected to the heater 52 by a lead 56 .
  • the duration of heating is controlled by the controller 54 which may be integrated into an overall system control mechanism (not shown).
  • Filter dryers 58 are provided both in the high-side capillary tube 18 and the low-side capillary tube 46 , and the function of these will be well understood in the art.

Abstract

A refrigeration system which comprises a compressor, an evaporator to which liquid refrigerant compressed by the compressor is supplied through a flow restrictor, and return means which direct refrigerant expanded in the evaporator back to the compressor. The return means include an accumulator in which liquid refrigerant leaving said evaporator may collect, and heating means either integral with or attached to the accumulator. The heating means are adapted to supply heat energy to the liquid refrigerant collected by said accumulator in order to promote its evaporation, thereby increasing the overall efficiency of the refrigeration system. The heating. means may be controlled by a microprocessor.

Description

    FIELD OF INVENTION
  • The present invention relates to refrigeration systems, and particularly (but not exclusively) to refrigeration systems for ultra-low temperature storage compartments. [0001]
  • BACKGROUND OF INVENTION
  • The operation of conventional low temperature refrigeration systems is well known in the art, so will not be described in detail here. However to appreciate the benefits provided by the present invention it is necessary briefly to explain how such conventional systems work. [0002]
  • A basic refrigeration system comprises a compressor which compresses gaseous refrigerant and supplies it to a heat exchanger where the refrigerant is condensed to a liquid, giving out heat energy. This liquid refrigerant then passes through a flow restrictor into an evaporator whereat the low pressure and the expansion of the refrigerant causes the refrigerant to vaporise thereby absorbing heat. The gaseous refrigerant then passes out of the evaporator back to the compressor to begin the cycle again. An accumulator is usually provided in the return path between the evaporator and the compressor, and the accumulator collects any liquid vapour passing through the evaporator so as to prevent its entry into the compressor. [0003]
  • Systems intended to cool to lower temperatures often employ a dual-stage cascade system which essentially comprises two separate but cooperating refrigeration systems. One of these stages draws heat from the location to be cooled; this stage is generally termed the low-side because it operates at a lower average temperature. The other stage is adapted to cool the compressed low-side refrigerant and release the heat to the external environment. As this second stage operates at a higher average temperature it is generally termed the high-side. [0004]
  • Refrigeration systems, including dual stage systems, seldom operate continuously, but instead switch as appropriate between an on-time and an off-time so as to maintain the desired temperature. This on/off switching aims to make the operation of the refrigeration system as efficient as possible, and is usually controlled thermostatically. [0005]
  • Many refrigeration systems, and particularly low temperature dual-stage ones, use a capillary tube as the flow restrictor (also called a metering device), and whilst such systems have many advantages, they are still far from totally efficient. The main cause of this lack of efficiency is the unnecessary time of operation when in an on-condition. [0006]
  • When a refrigeration system shuts off, gaseous refrigerant will condense within the evaporator, and this refrigerant will collect in the accumulator. During normal operation liquid refrigerant that has not been fully vaporized is stored in the accumulator, particularly at the end of the cycle as the load on the evaporator decreases. When a capillary tube is employed as a metering device liquid refrigerant continues to flow through the evaporator during the off cycle until the system pressure balances. If an accumulator is effectively to protect the compressor by preventing liquid refrigerant from entering it at the start of an on-time, the accumulator needs to be able to hold all of the charge of refrigerant that passes through the evaporator in the off-time. Unfortunately, when the system starts an on-time, it takes a while for the liquid refrigerant in the accumulator to vaporise and return to the compressor. When the compressor starts, the slow rate of evaporation causes the pressure at the input to the compressor to drop to a low level until a sufficient amount of vapour is available for compression, to be passed round the system. This low pressure at the start of a period of operation drastically reduces the volumetric efficiency of the compressor and prolongs the on-time. [0007]
  • In essence the compressor, which consumes the most energy in the cycle, operates at the beginning of an on-time at a lower efficiency. The efficiency (i.e. the amount of cooling achieved per unit of energy input) of the compressor increases up to an optimum as the on-time continues, but the delay in reaching this optimum efficiency can cause the on-time to be unnecessarily prolonged. [0008]
  • SUMMARY OF INVENTION
  • Therefore, according to the present invention there is provided a refrigeration system comprising a compressor, an evaporator to which refrigerant compressed by the compressor is supplied through a flow restrictor, and return means to direct back to the compressor refrigerant expanded in the evaporator, in which system the return means includes an accumulator in which may collect any liquid refrigerant leaving the evaporator, the accumulator being provided with heating means to evaporate liquid refrigerant collected by the accumulator. [0009]
  • In use the heating means provides sufficient heat to the liquid refrigerant in the accumulator to cause at least partial vaporisation thereof. Heating the accumulator causes the liquid refrigerant to vaporise more rapidly and at a higher pressure. This gaseous refrigerant then can return to the compressor to pass round the cycle. By encouraging the liquid refrigerant in the accumulator to vaporise, the time taken for the compressor to achieve optimum efficiency is dramatically reduced, and in consequence the length of any on-time may be significantly shortened. Tests have shown a 40%-50% reduction in the average duration of on-times. [0010]
  • If the accumulator were to be heated continuously the pressure would remain high, thus inhibiting the operation of the evaporator. Therefore it is highly preferred that there is provided a controller for the heating means, which controller is arranged to cause the heating means to operate for an interval at the commencement of a period of refrigeration following a period of inactivity of the system. [0011]
  • The duration of the heating interval may preferably be between 2 and 6 minutes, with 3-4 minutes being even more preferred. The control of the duration of the heating interval is dependent on a number of factors, such as the temperature of the refrigerant. [0012]
  • This system is primarily intended for use in an electrically powered refrigeration system. As such the heating means may be electrically powered. The heating means may be integrally formed with the accumulator, or may be a separate unit applied to the outside thereof. If applied separately, the heating means may be in the form of a flexible electric heating pad placed against a portion, preferably at least a lower portion, of the accumulator. Alternatively the heating means could utilise hot gas from other parts of the high or low side, flow of which could be controlled by a solenoid valve. [0013]
  • To ensure accurate and reliable control of the refrigeration system, the controller may comprise or include a microprocessor adapted to operate the heating means. The controller may operate in response to data pre-stored therein. In addition, or instead, the controller may operate in response to data received from external sources such as a pressure sensor, temperature sensors or other control equipment. [0014]
  • The present invention is applicable to various refrigeration systems, but will find a particular application to low temperature dual-stage systems. In such systems the heating means could be applied to both an accumulator on the low-side and an accumulator on the high-side. In practice, testing so far has shown that application of heating means to a high-side accumulator provides little if any increase in efficiency; thus, for reasons of economy, the heater may be provided on the low-side accumulator only. [0015]
  • It is normal for a conventional refrigeration system to include some form of control means, even if it is as simple as a thermostatic switch linked to the power supply. For reasons of simplicity and overall efficiency, the controller may be integrated in, or part of, an overall system controller. [0016]
  • In addition to the advantages discussed above, the present invention offers at least two further advantages. Firstly if the heater should fail, the system can still continued to operate as an existing system thereby not increasing the risk of damage to the goods stored in a freezer using such a refrigeration system. In effect it is fail-safe. Secondly, use of the present invention simplifies the task of charging the system with refrigerant during manufacture. In existing systems, the amount of refrigerant introduced into the system has to be carefully controlled. Too little refrigerant causes poor performance, but if too much is contained, not only can performance suffer, but more importantly refrigerant condensing during the off-time can overflow the condenser and flood the compressor. In systems according to the present invention larger capacity accumulators may be used without sacrificing performance, as would be the case in existing systems. Therefore, a greater degree of variation in the amount of refrigerant introduced can be tolerated and the process of manufacture simplified. [0017]
  • According to the present invention, there is also provided a low-temperature storage compartment, such as a freezer, incorporating a refrigeration system as hereinbefore described.[0018]
  • BRIEF DESCRIPTION OF DRAWING
  • By way of example only and in order that the present invention may be better understood one embodiment thereof will now be described in detail, with reference to the accompanying drawings in which: [0019]
  • FIG. 1 shows a schematic diagram of one embodiment of a dual stage refrigeration system according to the present invention.[0020]
  • DESCRIPTION OF PREFERRED EMBODIMENTS
  • The refrigeration system shown in FIG. 1 has two discrete cycles; one generally termed the high-side (labelled A), and the other generally termed the low-side (labelled B). During periods of on-time in normal operation, the low-side draws heat from the area to be cooled, and the high-side is adapted to cool the refrigerant of the low-side and dissipate that heat to the external environment. Separate refrigerants flow around the two cycles and whilst they thermally interact they do not come into direct contact. The types of refrigerant used are well know in the prior art so will not be discussed in detail. In FIG. 1 the direction of flow is indicated by arrows. [0021]
  • The high-side cycle comprises a [0022] compressor 10 which receives gaseous refrigerant from a return pipe 12. The compressor pressurises the gaseous refrigerant and pumps it out through a discharge pipe 14 into the condenser 16. In the condenser, heat energy is dissipated from the condensing refrigerant to the external atmosphere. The thus liquefied refrigerant passes out of the condenser 16 into a flow-restricting capillary pipe 18.
  • At the [0023] heat exchanger assembly 20, liquid high-side refrigerant exits the capillary tube 18 and is allowed to expand. This expansion cause the absorption of heat thereby cooling refrigerant passing round the low-side (herein after termed low-side refrigerant). Gaseous high-side refrigerant then passes back to condenser 10 through a return pipe 12. The high-side and low-side refrigerants are allowed to thermally interact, but do not come into physical contact.
  • The low-side cycle operates in a broadly similar way. Gaseous refrigerant enter the [0024] compressor 30 from a low-side return pipe 32 and is pressurised. Pressurised refrigerant passes out of the compressor 30 to a de-super-heating coil 34, and then to an oil separator 36. In the oil separator 36, any oil picked up during passage of the refrigerant through the compressor is separated and returned to the compressor 30 through oil return pipe 38. The refrigerant subsequently passes along feeder pipe 40 to the heat exchanger assembly 20. In the heat exchanger 20 low-side refrigerant is cooled by the high-side refrigerant. The cooled low-side refrigerant then passes out of heat exchanger unit 20 through a low-side discharge pipe 42.
  • The refrigerant then passes through a flow restrictor, which in this embodiment is low-[0025] side capillary tube 46. The low-side refrigerant passes from the capillary tube 46 into an evaporator 48. In the evaporator 48, at least a major portion of the low-side refrigerant changes state from liquid to gas and absorbs heat from the surrounding area, thereby effecting cooling. Gaseous refrigerant passing out of the evaporator 48 returns to the compressor 30 through the low-side return pipe 32.
  • Arranged between the discharge end of the [0026] evaporator 46 and the return pipe 32 there is provided an accumulator 50. The accumulator is adapted to prevent any liquid refrigerant passing through the evaporator from entering the low-side return pipe 32 and thereby gaining access to the compressor 30. If liquid refrigerant were able to enter the compressor 30, it could cause serious damage. During an off-time, low-side refrigerant will tend to condense within the evaporator 48 and will collect in the accumulator 50. At the beginning of an on-time the low-side refrigerant will vaporise and return to the compressor to start the cycle. As mentioned above the slow rate of vaporisation in prior art systems reduces the efficiency of the system. Therefore in this system the accumulator 50 is provided with a heater 52 disposed therearound. The heater 52 is operated at the beginning of an on-time to increase the rate of vaporisation of the low-side refrigerant in the accumulator 50. A controller 54, possibly including a microprocessor chip, is operatively connected to the heater 52 by a lead 56. The duration of heating is controlled by the controller 54 which may be integrated into an overall system control mechanism (not shown).
  • [0027] Filter dryers 58 are provided both in the high-side capillary tube 18 and the low-side capillary tube 46, and the function of these will be well understood in the art.

Claims (15)

I claim:
1. A refrigeration system comprising a compressor, an evaporator to which refrigerant compressed by the compressor is supplied through a flow restrictor, and return means to direct back to the compressor refrigerant expanded in the evaporator, in which system said return means include an accumulator in which may collect liquid refrigerant leaving said evaporator, and heating means associated with said accumulator to evaporate liquid refrigerant collected by said accumulator.
2. A refrigeration system as claimed in claim 1, wherein the heating means is electrically powered.
3. A refrigeration system as claimed in claim 1, wherein the heating means receives heat energy from refrigerant in other parts of the refrigeration system and at an elevated temperature.
4. A refrigeration system as claimed in claim 1, wherein the heating means comprises a separate unit mounted externally on the accumulator.
5. A refrigeration system as claimed in claim 1, wherein the heating means comprises a flexible electric heating pad mounted externally on the accumulator and thermally associated therewith.
6. A refrigeration system as claimed in claim 1, wherein the heating means is a silicone rubber mat heater.
7. A refrigeration system as claimed in any of claims 1, wherein the heating means is integrally formed with the accumulator.
8. A refrigeration system as claimed in claim 1, wherein a controller for the heating means is provided, said controller being arranged to cause the heating means to operate for a time interval at the commencement of a period of refrigeration following a period of inactivity of the refrigeration system.
9. A refrigeration system as claimed in claim 8, wherein the controller controls the duration of the interval dependent on at least one of the amount of liquid refrigerant in the accumulator at the commencement of a period of refrigeration, the vapour pressure within the accumulator and the temperature of the refrigerant within the accumulator.
10. A refrigeration system as claimed in claim 8, wherein said time interval is between 2 and 6 minutes.
11. A refrigeration system as claimed in claim 8, wherein the controller includes a microprocessor adapted to operate the heating means in response to at least one of data stored in the controller and data received by the controller.
12. A refrigeration system as claimed in claim 8, wherein the controller is part of a system controller which controls the overall refrigeration system.
13. A refrigeration system as claimed in claim 1, wherein the refrigeration system comprises a low-temperature stage of a dual-stage refrigeration system.
14. A dual-stage refrigeration system having a low-temperature stage and a high temperature stage, wherein the low-temperature stage comprises, an evaporator to which refrigerant compressed by the compressor is supplied through a flow restrictor, and return means to direct back to the compressor refrigerant expanded in the evaporator, in which system said return means include an accumulator in which may collect liquid refrigerant leaving said evaporator, and heating means associated with said accumulator to evaporate liquid refrigerant collected by said accumulator.
15. A low-temperature storage compartment incorporating a refrigeration system comprising a compressor, an evaporator to which refrigerant compressed by the compressor is supplied through a flow restrictor, and return means to direct back to the compressor refrigerant expanded in the evaporator, in which system said return means include an accumulator in which may collect liquid refrigerant leaving said evaporator, and heating means associated with said accumulator to evaporate liquid refrigerant collected by said accumulator.
US09/943,534 2000-08-31 2001-08-30 Refrigeration systems Expired - Fee Related US6449980B1 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
GB0021335 2000-08-31
GB0021335.5 2000-08-31
GB0021335A GB2370874B (en) 2000-08-31 2000-08-31 Refrigeration systems

Publications (2)

Publication Number Publication Date
US20020026807A1 true US20020026807A1 (en) 2002-03-07
US6449980B1 US6449980B1 (en) 2002-09-17

Family

ID=9898555

Family Applications (1)

Application Number Title Priority Date Filing Date
US09/943,534 Expired - Fee Related US6449980B1 (en) 2000-08-31 2001-08-30 Refrigeration systems

Country Status (2)

Country Link
US (1) US6449980B1 (en)
GB (1) GB2370874B (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060053831A1 (en) * 2004-09-10 2006-03-16 Serge Dube Evaporation circuit for alternative refrigerant in a refrigeration system
EP1655554A2 (en) * 2004-11-03 2006-05-10 LG Electronics, Inc. Multi-type air conditioner
US20070261434A1 (en) * 2006-05-11 2007-11-15 Denso Corporation Refrigerating cycle and component assembly for the same
US20200025396A1 (en) * 2018-07-17 2020-01-23 United Electric Company. L.P. Regrigerant charge control system for heat pump systems

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP3815302B2 (en) * 2001-11-12 2006-08-30 株式会社デンソー Air conditioner for vehicles
KR100499486B1 (en) * 2002-11-23 2005-07-05 엘지전자 주식회사 accumulator of heat pump system with at least two compressors
KR100499485B1 (en) * 2002-11-23 2005-07-07 엘지전자 주식회사 accumulator of heat pump system with at least two compressors
EP1642695B1 (en) * 2003-07-04 2013-08-21 Bridgestone Corporation Apparatus and method for vulcanizing tire
US7152415B2 (en) * 2004-03-18 2006-12-26 Carrier Commercial Refrigeration, Inc. Refrigerated compartment with controller to place refrigeration system in sleep-mode
CN100432562C (en) * 2004-09-30 2008-11-12 乐金电子(天津)电器有限公司 Central air-conditioner and its control method
JP4326445B2 (en) * 2004-10-20 2009-09-09 三洋電機株式会社 Washing and drying machine
US20070283716A1 (en) * 2006-06-08 2007-12-13 Joseph Marsala Pumped refrigerant loop cooling system for cooling High thermal density heat loads
JP5551882B2 (en) * 2009-02-24 2014-07-16 ダイキン工業株式会社 Heat pump system

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3792594A (en) * 1969-09-17 1974-02-19 Kramer Trenton Co Suction line accumulator
US3779035A (en) * 1971-12-17 1973-12-18 D Kramer Suction accumulators for refrigeration systems
AT325644B (en) * 1973-10-11 1975-10-27 Bosch Hausgeraete Gmbh REFRIGERATED UNITS, IN PARTICULAR SECOND TEMPERATURE REFRIGERATOR
US4068493A (en) * 1976-03-04 1978-01-17 Kramer Trenton Company Suction accumulator for refrigeration systems
US5245833A (en) * 1992-05-19 1993-09-21 Martin Marietta Energy Systems, Inc. Liquid over-feeding air conditioning system and method
US5233842A (en) * 1992-07-01 1993-08-10 Thermo King Corporation Accumulator for refrigeration system
JP3160097B2 (en) * 1992-11-20 2001-04-23 マツダ株式会社 Automotive heating system
JPH07234027A (en) * 1994-02-22 1995-09-05 Sanyo Electric Co Ltd Cascade refrigerator
US5714738A (en) * 1995-07-10 1998-02-03 Watlow Electric Manufacturing Co. Apparatus and methods of making and using heater apparatus for heating an object having two-dimensional or three-dimensional curvature

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060053831A1 (en) * 2004-09-10 2006-03-16 Serge Dube Evaporation circuit for alternative refrigerant in a refrigeration system
EP1655554A2 (en) * 2004-11-03 2006-05-10 LG Electronics, Inc. Multi-type air conditioner
EP1655554A3 (en) * 2004-11-03 2011-08-24 LG Electronics, Inc. Multi-type air conditioner
US20070261434A1 (en) * 2006-05-11 2007-11-15 Denso Corporation Refrigerating cycle and component assembly for the same
US20200025396A1 (en) * 2018-07-17 2020-01-23 United Electric Company. L.P. Regrigerant charge control system for heat pump systems
US11879673B2 (en) * 2018-07-17 2024-01-23 United Electric Company. L.P. Refrigerant charge control system for heat pump systems

Also Published As

Publication number Publication date
US6449980B1 (en) 2002-09-17
GB2370874B (en) 2004-11-24
GB2370874A (en) 2002-07-10
GB0021335D0 (en) 2000-10-18

Similar Documents

Publication Publication Date Title
US6393851B1 (en) Vapor compression system
US6449980B1 (en) Refrigeration systems
US6237359B1 (en) Utilization of harvest and/or melt water from an ice machine for a refrigerant subcool/precool system and method therefor
US6351950B1 (en) Refrigeration system with variable sub-cooling
US4833893A (en) Refrigerating system incorporating a heat accumulator and method of operating the same
US7210303B2 (en) Transcritical heat pump water heating system using auxiliary electric heater
US20020157416A1 (en) Vapor compression system and method
US6581398B2 (en) Vapor compression system and method
EP2837901B1 (en) Cooling system
US7225627B2 (en) Vapor compression system and method for controlling conditions in ambient surroundings
US4774815A (en) Harvest pressure regulator valve system
US6314747B1 (en) Vapor compression system and method
US4907422A (en) Harvest cycle refrigerant control system
US5916254A (en) Method of circulating refridgerant for defrosting and refrigerator employing the same
US2928256A (en) Refrigerating system including auxiliary hot gas defrosting circuit
US4878361A (en) Harvest cycle refrigerant control system
CN106091192A (en) Air conditioning system and control method thereof
WO2005001345A1 (en) Improved cooling system
US6250090B1 (en) Apparatus and method for evaporator defrosting
US2961848A (en) Refrigerating system including hot gas defrost means
US4918931A (en) Compressor slugging prevention method for a refrigeration system
JPH09318205A (en) Refrigerating device
JPH07190534A (en) Heat storage type air conditioning equipment
US2895307A (en) Refrigerating system including a hot gas defrosting circuit
EP1616136B1 (en) Refrigeration system and a method for operating such system

Legal Events

Date Code Title Description
AS Assignment

Owner name: NBS CRYO RESEARCH LIMITED, ENGLAND

Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNOR:MINISTER, DAVID JOHN;REEL/FRAME:012141/0438

Effective date: 20010807

FPAY Fee payment

Year of fee payment: 4

REMI Maintenance fee reminder mailed
LAPS Lapse for failure to pay maintenance fees
STCH Information on status: patent discontinuation

Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362

FP Lapsed due to failure to pay maintenance fee

Effective date: 20100917