EP0058259B1 - Echangeur de chaleur conservant de l'énergie pour des machines frigorifiques, et machine frigorifique pourvue d'un tel échangeur de chaleur - Google Patents
Echangeur de chaleur conservant de l'énergie pour des machines frigorifiques, et machine frigorifique pourvue d'un tel échangeur de chaleur Download PDFInfo
- Publication number
- EP0058259B1 EP0058259B1 EP19810300602 EP81300602A EP0058259B1 EP 0058259 B1 EP0058259 B1 EP 0058259B1 EP 19810300602 EP19810300602 EP 19810300602 EP 81300602 A EP81300602 A EP 81300602A EP 0058259 B1 EP0058259 B1 EP 0058259B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- refrigerant
- water
- heat
- exchanger
- refrigerating machine
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 88
- 239000003507 refrigerant Substances 0.000 claims description 45
- 238000005057 refrigeration Methods 0.000 claims description 17
- 239000000498 cooling water Substances 0.000 claims 1
- 238000010438 heat treatment Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000012530 fluid Substances 0.000 description 3
- 238000009434 installation Methods 0.000 description 3
- 238000004134 energy conservation Methods 0.000 description 2
- 239000011159 matrix material Substances 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000002826 coolant Substances 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000009977 dual effect Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F24—HEATING; RANGES; VENTILATING
- F24D—DOMESTIC- OR SPACE-HEATING SYSTEMS, e.g. CENTRAL HEATING SYSTEMS; DOMESTIC HOT-WATER SUPPLY SYSTEMS; ELEMENTS OR COMPONENTS THEREFOR
- F24D17/00—Domestic hot-water supply systems
- F24D17/02—Domestic hot-water supply systems using heat pumps
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B29/00—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously
- F25B29/003—Combined heating and refrigeration systems, e.g. operating alternately or simultaneously of the compression type system
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
- F25B40/00—Subcoolers, desuperheaters or superheaters
- F25B40/04—Desuperheaters
Definitions
- the present invention relates generally to heat exchangers for utilizing heat from the refrigerant of refrigerating machines, especially of a commercial cube/crushed ice-making machine, and to refrigerating machines equipped with such an exchanger.
- CA ⁇ A ⁇ 1048802 shows a pressure sensitive valve system on the output side of a refrigerating machine, without combining it with a heat exchanger
- US-A-4089667 shows a valved by-pass round a waterrefrigerant heat-exchanger
- the control system is adapted to be responsive to refrigerant pressure at the outlet of the exchanger so as to maintain it at an optimum efficiency for the refrigeration system, as well as to the output water temperature from the condenser.
- the heat exchanger may be combined with a refrigerating machine such as a refrigerator or ice-making machine having a closed loop refrigeration system of which the refrigerant side of the exchanger forms part; and the system may include in series therein: a compressor, a refrigerant-to-water condenser whereby heat rejected from the closed loop system is transferred to the heat reclamation means through the condenser, an expansion valve, and an evaporator.
- a refrigerating machine such as a refrigerator or ice-making machine having a closed loop refrigeration system of which the refrigerant side of the exchanger forms part
- the system may include in series therein: a compressor, a refrigerant-to-water condenser whereby heat rejected from the closed loop system is transferred to the heat reclamation means through the condenser, an expansion valve, and an evaporator.
- an ice-maker and heat reclamation system constructed in accordance with the present invention, and generally indicated at 10, includes a commercial ice-maker 11 such as sold under the trademark ROSS-TEMP, and an indirect heat reclamation device which is a refrigerant-to-water condenser 12 which is conventional in itself and which, in this embodiment, is positioned externally of the ice-maker.
- the condenser 12 is preferably connected to a conventional external water supply which, in this embodiment, is shown to include a water pump 13 and a hot water storage tank 14 connected in series with the coolant side of the condenser 12.
- any commercial ice-maker may be utilized in the system of the present invention
- two commercial ice-making systems are ideally suited for use with the heat reclamation system of the present invention.
- a layer of ice is formed on the bottom of a working sheet or plate.
- the second type of commercial ice-maker utilizes a hollow cylinder with ice being formed on an exterior surface thereof.
- An auger or the like is sleeved over the evaporator and includes a helical working edge which sweeps across the hollow cylindrical surface to shave ice therefrom in order to create "crushed" ice.
- the refrigeration system of the ice-maker 11 includes a conventional refrigerant compressor 15 having a high pressure exhaust port 15a which is connected by conduit 16a to refrigerant inlet port 12 of the heat reclamation condenser 12.
- the refrigerant outlet port 12b is connected by conduit 16b to a secondary air-cooled condenser 17 having a cooling fan 18 and a fan control switch 18a associated therewith.
- a refrigerant receiver or accumulator 19 is operatively positioned between the secondary condenser and a thermal expansion valve 20 by conduits 16c and 16d.
- a conventional evaporator 21 and conduit 16e are downstream of the valve and operatively connected via conduit 16f to a low pressure inlet port 15b of the compressor.
- the air-cooled secondary condenser 17 may be the original equipment condenser for the separate ice-maker. If the refrigerant-to-water condenser 12 is mounted within the physical confines of the ice-maker 11, it is understood that it could be sized to completely replace the secondary air-cooled condenser 17. The purpose of the secondary condenser will be discussed in connection with the operation of the system.
- the water supply includes a pump 13 which receives water from an inlet conduit 22 and pumps same through outlet conduit 23 to the water inlet port 12c of the refrigerant-to-water condenser 12 where the water is positioned in heat exchange relation with the high pressure refrigerant and passes out water outlet port 12d, through temperature actuated sensor 30, and conduit 24 to the hot water storage tank 14 where the water may be discharged through conduit 25.
- a pump 13 which receives water from an inlet conduit 22 and pumps same through outlet conduit 23 to the water inlet port 12c of the refrigerant-to-water condenser 12 where the water is positioned in heat exchange relation with the high pressure refrigerant and passes out water outlet port 12d, through temperature actuated sensor 30, and conduit 24 to the hot water storage tank 14 where the water may be discharged through conduit 25.
- the condenser 12 may act as a primary or secondary heating source for the water supply.
- the control system does not provide for operation of the compressor if the ice machine is filled to capacity, it is assumed that in most installations the condenser 12 will act as only a secondary heat source for the water supply.
- the flow of water from pump 13 into the refrigerant-to-water condenser 12 is regulated by a valve 26 which acts in response to the pressure of the refrigerant at outlet 12b of the condenser.
- the operational pressure of the refrigerant proximately ranges from about 6,9 bar (100 psig) to about 11 bar (160 psig) as discussed in more detail hereafter.
- a condenser bypass conduit 27 which bridges between the refrigerant inlet and outlet ports 12a, 12b, respectively, of the condenser 12 includes a solenoid operated valve 28 therein which is actuated by temperature actuated sensor 30 positioned adjacent the water discharge port 12d of condenser 12.
- Valve 28 is a fail- safe valve which, in this embodiment, shuts off the heat exchanging condenser if water usage is so minimal that the water temperature reaches a severely high level.
- the pressure regulation valve 26 controls the flow of water through the condenser 12 to maintain a preset pressure, in this embodiment approximately 6,9-8,3 bar (100-120 psig) in the refrigerant at the outlet port 12b of condenser 12. If the initial temperature of the water is about 15.5°C, water flow through the condenser will be minimized such that the water exit temperature therefrom approximates 38°C. The refrigerant temperature at outlet port 12b may then approximate 27°C.
- valve 26 gradually opens to allow greater water flow through the condenser 12 in order to maintain the pre-determined refrigerant pressure at the condenser outlet 12b.
- the water flow through the condenser will be at its maximum when the inlet water temperature is approximately 38°C or above.
- the refrigerant may be maintained at approximately 49°C and 8,3 bar (120 psig), and all of the heat rejected from the ice machine is absorbed into the water system.
- This heat includes the sensible heat from superheating the refrigerant vapor, the latent heat from condensing the refrigerant, and the sensible heat from subcooling the refrigerant liquid. Also since a water-cooled condenser has been utilized, the refrigerant discharge pressure has been lower than the usual discharge pressure achieved when solely using an air-cooled condenser. With the high pressure refrigerant being an optimal value, which is lower than achievable with an air-cooled condenser, the machine has been operating more efficiently than heretofore-known ice machines of comparable size.
- the temperature or pressure of the refrigerant will be sufficiently high (approximating 49°C and 7,3 bar (106 psig) to actuate the switch 18a and turn on the motor of the cooling fan 18 of the air-cooled secondary condenser 17.
- the switch 18a cycles the fan on and off at approximately two-minute intervals.
- the additional condenser capacity in this embodiment acts to lower the refrigerant pressure to a satisfactory level approximating 8,3 bar (120 psig), but nevertheless, to a level which is higher than the discharged pressure when the refrigerant-to-water condenser 12 was the sole heat rejection means in the system.
- the refrigerant-to-water condenser since the refrigerant-to-water condenser is still in the system, the refrigerant high side pressure is still lower and closer to optimum than if an air-cooled condenser alone were present in the system; thus, the system is still more efficient than a system solely using an air-cooled condenser.
- the dual condensers can no longer lower the refrigerant pressure to 8,3 bar (120 psig) and the fan motor the air-cooled condenser 17 begins to run constantly rather than cyclicly. With the air-cooled condenser fan on constantly, the heat transferred to the water in the condenser 12 through desuperheating will be added at a lower rate than previously described.
- the sensor 30 actuates the solenoid 28 to open the bypass line 27 allowing most of the hot refrigerant vapor to pass directly to the air-cooled condenser 17.
- An additional safety sensor 32 at the hot water storage tank 14 is capable of stopping the operation of the compressor 15 if the water temperature in the tank reaches an unsafe temperature, approximating 93°C. It should be noted that during normal operation both hot water usage and actual ice usage will, to some extent, determine the operation of the heat reclaiming device.
- the condenser 12 During normal operating hours, when both the ice machine and hot water system would be in use, the condenser 12 would be of sufficient size to handle all heat rejected by the ice machine. If the use of the external water supply should drop substantially or stop, in connection with an embodiment having a secondary air-cooled condenser, it may be expected that the secondary condenser would run in its cyclic phase during such extreme circumstances.
- the hot water storage tank 14 in accordance with another aspect of the invention, serves as a pre-heater which is positioned in the hot water system in parallel with a conventional hot water heater 44 such that the water supply inlet.
- conduit 45 directs water into the storage tank where that water is mixed with heated water already in the tank.
- a modification of the system shown in connection with Figure 3 may include a second independent water-to-water condenser 40 or a second stage of condenser 12 may be positioned in the refrigeration unit to replace the air-cooled condenser 17.
- the water-cooled secondary condenser 40 would operate in a manner similar to air-cooled condenser 17 in that the pressure regulating valve 41 would not turn on a separate water cooling system, indicated by inlet conduit 42 and outlet conduit 43, until the primary refrigerant-to-water condenser 12 was operating at full heat reclaiming capacity.
- the commercial ice-maker and heat reclamation device combination of the present invention provides an efficient means of reclaiming the heat rejected from the refrigeration cycle of a commercial ice-making machine and transferring same to an external hot water supply.
- the system of the present invention provide an additional refrigeration device from which heat may be reclaimed, but the use of a refrigerant-to-water condenser in a commercial ice-maker coupled with a control system which is responsive to refrigerant condenser outlet pressure rather than temperature provides added efficiency to the commercial ice-making device while, at the same time, reclaiming the heat rejected from the refrigerant cycle.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Production, Working, Storing, Or Distribution Of Ice (AREA)
Claims (11)
Priority Applications (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP19810300602 EP0058259B1 (fr) | 1981-02-13 | 1981-02-13 | Echangeur de chaleur conservant de l'énergie pour des machines frigorifiques, et machine frigorifique pourvue d'un tel échangeur de chaleur |
DE8181300602T DE3171763D1 (en) | 1981-02-13 | 1981-02-13 | Energy conserving heat exchange apparatus for refrigerating machines, and refrigerating machine equipped therewith |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP19810300602 EP0058259B1 (fr) | 1981-02-13 | 1981-02-13 | Echangeur de chaleur conservant de l'énergie pour des machines frigorifiques, et machine frigorifique pourvue d'un tel échangeur de chaleur |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0058259A1 EP0058259A1 (fr) | 1982-08-25 |
EP0058259B1 true EP0058259B1 (fr) | 1985-08-14 |
Family
ID=8188211
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP19810300602 Expired EP0058259B1 (fr) | 1981-02-13 | 1981-02-13 | Echangeur de chaleur conservant de l'énergie pour des machines frigorifiques, et machine frigorifique pourvue d'un tel échangeur de chaleur |
Country Status (2)
Country | Link |
---|---|
EP (1) | EP0058259B1 (fr) |
DE (1) | DE3171763D1 (fr) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP3737381B2 (ja) * | 2000-06-05 | 2006-01-18 | 株式会社デンソー | 給湯装置 |
US20120151946A1 (en) * | 2009-07-27 | 2012-06-21 | Ecolactis | Method and device for heat recovery on a vapour refrigeration system |
CN102353175A (zh) * | 2011-08-12 | 2012-02-15 | 侯全舵 | 单压机多功能热泵装置 |
CN114294784B (zh) * | 2021-12-28 | 2023-08-01 | 中山市爱美泰电器有限公司 | 一种热泵机组除霜控制方法及热泵机组 |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US1854402A (en) * | 1928-07-05 | 1932-04-19 | Justus C Goosmann | Refrigerating apparatus and control valve therefor |
US1874803A (en) * | 1931-01-12 | 1932-08-30 | Reed Frank Maynard | Heat exchange mechanism |
US2356261A (en) * | 1938-06-25 | 1944-08-22 | Honeywell Regulator Co | Refrigeration |
US2181354A (en) * | 1939-07-28 | 1939-11-28 | Winters John | Condenser for refrigerators |
US2702671A (en) * | 1951-03-13 | 1955-02-22 | Detroit Controls Corp | Differential temperature valve with pressure override |
US2700279A (en) * | 1952-06-12 | 1955-01-25 | Gen Motors Corp | Refrigerating apparatus and water heater |
US2807145A (en) * | 1953-12-10 | 1957-09-24 | Ray M Henderson | Apparatus for supplying heat for hot gas defrosting systems |
US2952991A (en) * | 1959-02-20 | 1960-09-20 | Carrier Corp | High side pressure control for refrigeration systems |
DE1476954A1 (de) * | 1965-03-18 | 1969-09-04 | Walter Andreas | Milchkuehlgeraet |
US4089667A (en) * | 1976-10-27 | 1978-05-16 | Sun-Econ, Inc. | Heat extraction or reclamation apparatus for refrigerating and air conditioning systems |
FR2370424A1 (fr) * | 1976-11-10 | 1978-06-09 | Vironneau Pierre | Procede et dispositif pour economiser l'energie dans les installations laitieres de traite |
CA1048802A (fr) * | 1976-12-06 | 1979-02-20 | Eds-Way Manufacturing Supply Limited | Recuperateur de chaleur |
DE2712110C2 (de) * | 1977-03-19 | 1985-02-07 | Brown Boveri - York Kälte- und Klimatechnik GmbH, 6800 Mannheim | Anlage zum Heizen und/oder Kühlen |
US4134274A (en) * | 1978-01-26 | 1979-01-16 | The Trane Company | System for producing refrigeration and a heated liquid and control therefor |
DE2842841A1 (de) * | 1978-10-02 | 1980-04-17 | Eckerfeld Geb Maurer Erika | Anordnung zur warmwasserbereitung |
US4226606A (en) * | 1978-10-06 | 1980-10-07 | Air & Refrigeration Corp. | Waste heat recovery system |
US4238931A (en) * | 1979-01-25 | 1980-12-16 | Energy Conservation Unlimited, Inc. | Waste heat recovery system controller |
-
1981
- 1981-02-13 EP EP19810300602 patent/EP0058259B1/fr not_active Expired
- 1981-02-13 DE DE8181300602T patent/DE3171763D1/de not_active Expired
Also Published As
Publication number | Publication date |
---|---|
DE3171763D1 (en) | 1985-09-19 |
EP0058259A1 (fr) | 1982-08-25 |
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