WO2015111222A1 - Refrigeration device - Google Patents
Refrigeration device Download PDFInfo
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- WO2015111222A1 WO2015111222A1 PCT/JP2014/051690 JP2014051690W WO2015111222A1 WO 2015111222 A1 WO2015111222 A1 WO 2015111222A1 JP 2014051690 W JP2014051690 W JP 2014051690W WO 2015111222 A1 WO2015111222 A1 WO 2015111222A1
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- WIPO (PCT)
- Prior art keywords
- refrigerant
- heat exchanger
- liquid
- temperature
- refrigeration apparatus
- Prior art date
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Classifications
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- 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
- F25B49/00—Arrangement or mounting of control or safety devices
- F25B49/02—Arrangement or mounting of control or safety devices for compression type machines, plants or systems
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- 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
- F25B41/00—Fluid-circulation arrangements
- F25B41/006—Fluid-circulation arrangements optical fluid control arrangements
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- 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
- F25B45/00—Arrangements for charging or discharging refrigerant
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- 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
- F25B2400/00—General 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
- F25B2400/13—Economisers
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- 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
- F25B2400/00—General 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
- F25B2400/16—Receivers
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- 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
- F25B2500/00—Problems to be solved
- F25B2500/01—Geometry problems, e.g. for reducing size
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- 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
- F25B2500/00—Problems to be solved
- F25B2500/23—High amount of refrigerant in the system
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- 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
- F25B2500/00—Problems to be solved
- F25B2500/24—Low amount of refrigerant in the system
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- 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
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2106—Temperatures of fresh outdoor air
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- 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
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2116—Temperatures of a condenser
- F25B2700/21162—Temperatures of a condenser of the refrigerant at the inlet of the condenser
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- 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
- F25B2700/00—Sensing or detecting of parameters; Sensors therefor
- F25B2700/21—Temperatures
- F25B2700/2116—Temperatures of a condenser
- F25B2700/21163—Temperatures of a condenser of the refrigerant at the outlet of the condenser
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- 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
- F25B40/02—Subcoolers
Definitions
- the present invention relates to a refrigeration apparatus.
- showcases are mainly installed in food departments, but the number, size, type, arrangement, etc., vary depending on the store.
- the internal volume of the evaporator arranged in the showcase differs accordingly.
- the unit cooler has the same evaporator volume depending on the type.
- the installation place of the refrigerator which accommodates the compressor, the condenser, and the liquid receiver also differs depending on the structure of the store, and may be installed on the back of the food department or on the roof, for example. Therefore, the distance between the evaporator, the compressor, the condenser, and the liquid receiver varies depending on the installation location of the refrigerator, and the lengths of the extension pipes such as the gas extension pipe and the liquid extension pipe also differ.
- the refrigerant of the refrigerator is filled (enclosed) after configuring the refrigeration cycle on site.
- the amount of refrigerant required for the refrigeration cycle varies depending on the state of the refrigeration cycle, and the state of the refrigeration cycle also varies depending on the outside air temperature, the operating state of the load-side equipment of the showcase, and the like. For this reason, normally, a large amount of refrigerant is charged so that the amount of refrigerant necessary for each component device such as a condenser and an evaporator is always distributed regardless of the operating state.
- FIG. 7 is a diagram illustrating an example of a refrigerant circuit of a conventional refrigeration apparatus.
- a sight glass 17 is provided in the liquid piping downstream of the receiver 4 as shown in FIG. 7, and the internal temperature (the temperature of the target space cooled by the evaporator) is set to the set temperature during the test operation.
- the flash gas bubbles
- the time is the amount of refrigerant with no surplus, so a method of charging a certain amount of refrigerant with respect to the amount of refrigerant has been proposed.
- this filling amount becomes the surplus refrigerant amount corresponding to the fluctuation of the necessary refrigerant amount due to the state change of the refrigeration cycle.
- This percentage is 5 to 10% of the amount of refrigerant sealed up to the point when the flash disappears according to the manufacturer's instructions, but it is the know-how of each supplier. Therefore, a large amount of refrigerant is often added.
- a method of detecting the refrigerant liquid level in the receiver by using a capacitance sensor, determining that the refrigerant amount is excessive, appropriate, and insufficient, and calculating the insufficient refrigerant amount, and a sight glass on the side of the receiver A method has been proposed in which a human detects the liquid level visually and compares the relationship between the amount of refrigerant given as data and the liquid level position (height) to determine surplus, appropriateness, and shortage. And the amount of refrigerant
- Japanese Patent No. 2997487 see, for example, pages 2 to 3 and FIG. 4.
- the current situation is that the method for calculating the amount of refrigerant that is insufficient, determined by the capacitance sensor shown in Patent Document 1 as surplus, appropriate, and insufficient, is almost unpractical due to high costs.
- the method of providing sight glass that can judge appropriate, surplus, and deficiency on the side of the receiver, it is appropriate for each refrigeration system in refrigerators with greatly different operating conditions such as the internal volume of the evaporator, the length of the extension pipe, and the internal temperature.
- the surplus and deficient refrigerant amounts differ greatly. Therefore, a large sight glass is required to cope with the change in the refrigerant amount, but this is unrealistic, and even if implemented, the cost is high.
- the present invention has been made to solve at least one of the above-described problems, and can easily and properly carry out refrigerant filling at the time of trial operation or service of a refrigeration apparatus, thereby suppressing overfilling.
- An object of the present invention is to provide a refrigeration apparatus that can perform the above.
- the refrigeration apparatus includes a compressor, a heat source side heat exchanger, a supercooling heat exchanger, a heat source side unit having at least a liquid receiver, and a load side unit having at least a load side expansion means and a load side heat exchanger.
- a compressor a heat source side heat exchanger, a supercooling heat exchanger, a heat source side unit having at least a liquid receiver, and a load side unit having at least a load side expansion means and a load side heat exchanger.
- the compressor the heat source side heat exchanger, the supercooling heat exchanger, the liquid receiver, the load side expansion means, and the load side heat exchanger.
- a sight glass is provided on a side surface of the receiver, and the sight glass has a maximum refrigerant liquid level position throughout the year of the receiver during operation. It is provided at a position where it can be confirmed.
- the sight glass that can confirm the refrigerant liquid level position of the receiver is installed, and the liquid level position indicates the maximum refrigerant liquid level position during operation.
- the refrigerant filling at the time of service of the refrigeration apparatus can be carried out easily, quickly and accurately, and overfilling can be suppressed.
- FIG. 1 is a diagram illustrating an example of a refrigerant circuit of a refrigeration apparatus according to Embodiment 1 of the present invention.
- the refrigeration apparatus according to Embodiment 1 includes an outdoor unit 100 and an indoor unit 200.
- the outdoor unit 100 includes a compressor 1, a condenser 3, a liquid receiver 4, and a supercooling heat exchanger 5. Further, downstream of the supercooling heat exchanger 5, the main unit 22 branches to a main flow path 22 toward the evaporator 7 of the indoor unit 200 and an injection flow path 23 toward the injection port 1 a of the compressor 1.
- the liquid operation valve 10 is provided, and the expansion valve 8 is provided on the injection flow path 23 side.
- the indoor unit 200 uses a showcase, a unit cooler, or the like.
- the indoor unit 200 includes a liquid electromagnetic valve 9, an expansion valve 6, and an evaporator 7.
- the indoor unit 200 is connected to the outdoor unit 100 by the liquid extension pipe 18 and the gas extension pipe 19.
- the refrigerant circuit which circulates a refrigerant
- the amount of refrigerant distributed to the condenser 3, the liquid receiver 4, the supercooling heat exchanger 5, the evaporator 7, the liquid extension pipe 18, and the gas extension pipe 19 is determined by the respective internal volume, performance, and operation state.
- surplus refrigerant after each component device of the refrigeration cycle has an appropriate amount of refrigerant is stored in the liquid receiver 4.
- the compressor 1 sucks refrigerant and compresses the refrigerant to a high temperature and high pressure state.
- the injection port 1 a is an intermediate pressure port that allows the refrigerant to flow into the compression chamber in the middle of compression of the compressor 1.
- the condenser 3 performs heat exchange between air supplied from a blower (not shown) and the refrigerant, and condenses the refrigerant into a liquid refrigerant.
- the liquid receiver 4 is disposed between the condenser 3 and the evaporator 7 and stores excess refrigerant.
- the liquid receiver 4 should just be a container which can store an excess refrigerant
- the supercooling heat exchanger 5 performs heat exchange between air and refrigerant in the same manner as the condenser 3 to supercool the liquid refrigerant.
- the expansion valves 6 and 8 expand the refrigerant by decompressing it.
- the expansion valves 6 and 8 may be configured by a valve whose opening degree can be variably controlled, for example, a precise flow rate control means using an electronic expansion valve, an inexpensive refrigerant flow rate control means such as a capillary tube, or the like.
- the evaporator 7 exchanges heat between air supplied from a blower (not shown) and the refrigerant to evaporate the refrigerant into a gas refrigerant. This evaporator 7 cools the target space such as a showcase.
- the liquid electromagnetic valve 9 controls whether the refrigerant flows into the evaporator 7 by electronic opening and closing.
- the liquid operation valve 10 is configured to allow the refrigerant to flow into the liquid extension pipe 18 or not by manual opening and closing.
- the refrigeration apparatus includes refrigerant amount determination means 20 that determines whether or not the minimum amount of refrigerant charged in the refrigerant circuit is filled.
- the refrigerant amount determination means 20 can be configured by a microcomputer or the like provided on the control board of the refrigeration apparatus, for example. Temperature information detected by the first temperature sensor (TH5), the second temperature sensor (TH8), and the third temperature sensor (TH6) is input to the refrigerant amount determination means 20.
- the first temperature sensor (TH5) is located at any position on the outlet side of the condenser 3 or the flow path from the portion where the refrigerant is in a two-phase state in the condenser 3 to the inlet side of the supercooling heat exchanger 5. It is provided and detects the temperature of the refrigerant.
- the second temperature sensor (TH8) is provided at any position in the flow path from the outlet side of the supercooling heat exchanger 5 to the inlet side of the expansion valve 6, and detects the temperature of the refrigerant.
- the third temperature sensor (TH6) detects the temperature of the air before the condenser 3 exchanges heat with the refrigerant.
- the refrigerant amount determination means 20 is provided with a display unit 21 that displays the determination result and various types of information.
- the display unit 21 includes, for example, a 7-segment LED. Note that a cylinder (not shown) is used when the refrigerant circuit is filled with the refrigerant.
- the refrigerant circulating in the refrigerant circuit is mainly present in the condenser 3, the liquid receiver 4, the liquid extension pipe 18, the evaporator 7, and the gas extension pipe 19.
- the refrigerant is in the gas phase, the higher the temperature, the higher the density. Therefore, in the condenser 3 having a larger gas phase, the refrigerant is stored in the condenser 3 as the condensation temperature is higher.
- the gas phase is dominant, and the higher the condensation temperature, the more the refrigerant is stored in the liquid receiver 4.
- the density increases as the temperature decreases. Therefore, the refrigerant accumulates in the liquid extension pipe 18 as the liquid temperature decreases.
- FIG. 2 is a Mollier diagram corresponding to different condensation temperatures of the refrigeration apparatus according to Embodiment 1 of the present invention.
- Tc represents the condensation temperature
- Te represents the evaporation temperature.
- the two-phase refrigerant throttled by the expansion valve 6 evaporates into a gas phase.
- the lower the condensation temperature the higher the wetness immediately after the expansion valve 6. Will store a lot of refrigerant. Therefore, the seasonal variation in the amount of refrigerant required to operate the refrigeration apparatus is a relative relationship between the volume of the condenser 3 and the volume of the liquid receiver 4 and the liquid extension pipe + evaporator volume if the evaporation temperature is constant.
- the required refrigerant amount increases as the condensation temperature increases.
- the required refrigerant amount decreases as the condensation temperature decreases. Become more.
- the required volume of the liquid receiver 4 is required to enable the recovery of the refrigerant in the liquid receiver 4 by closing the liquid operation valve 10 downstream of the liquid receiver 4, so that the volume of the condenser 3 And the volume of the liquid extension pipe 18 are almost determined by the volume, and the following values are obtained.
- Receiver volume (condenser volume + liquid extension pipe volume) x (125% ⁇ 25%)
- FIG. 3 is a diagram showing a ratio of the liquid in the liquid receiver 4 with respect to the outside air temperature of the refrigeration apparatus according to Embodiment 1 of the present invention.
- FIG. 4 is a diagram illustrating an example of the sight glass 14 of the refrigeration apparatus according to Embodiment 1 of the present invention.
- the use range of the outside air temperature around the outdoor unit 100 is -15 to 43 ° C.
- the graph shows how the amount of refrigerant in the liquid receiver 4 changes due to a change in the outside air temperature.
- the volume of the showcase is larger than the volume of the unit cooler.
- the graph of the condition of the pipe length of 100 m when the load in FIG. 3 is a showcase shows that the volume of the load is large, the extension pipe is long, the volume of the condenser 3 and the liquid receiver 4 is small, and the liquid in the liquid receiver 4 This is an example in which the rate of change of the ratio is maximized.
- the maximum value of the rate of change in the liquid ratio in the receiver 4 is 22.7% of the volume of the receiver 4 when the refrigerant amount is 43 ° C., and 0.0% when the ambient temperature is ⁇ 15 ° C.
- the change width is 22.7%. That is, since the required refrigerant is low at the outside air temperature of 43 ° C., a large amount of surplus refrigerant is stored in the liquid reservoir, and at the outside air temperature of ⁇ 15 ° C., the necessary refrigerant is large and the surplus refrigerant is eliminated and there is no refrigerant stored in the liquid reservoir. The required amount of refrigerant tends to increase as the outside air temperature decreases.
- the sight glass 14 is placed on the side surface of the liquid receiver 4 so that the position of the refrigerant liquid surface 11 of the liquid receiver 4 can be confirmed, and the maximum amount of refrigerant in the liquid reservoir (22 above). 7%), a margin of about 10% is provided at a maximum position of 33.0%, and this position is set as the position of the refrigerant liquid surface 11 that becomes the maximum throughout the year.
- the sight glass 14 is attached to a copper pipe 16 from the end plate and barrel of the liquid receiver 4.
- the sight glass 14 has a function of determining the presence or absence of moisture, and has a size equal to or smaller than the size of the liquid extension pipe 18. Alternatively, it may be installed directly on the shell of the liquid receiver 4, but the refrigerant flow tends to disturb the refrigerant liquid level 11 in the liquid receiver 4, making it difficult to check the refrigerant liquid level 11.
- FIG. 5 is a diagram illustrating another example of the refrigerant circuit of the refrigeration apparatus according to Embodiment 1 of the present invention.
- the indoor unit 100A includes a compressor 1, a condenser 3, a liquid receiver 4, and a supercooling heat exchanger 5A as in FIG. 1, but the supercooling heat exchanger 5A includes a plate heat exchanger and a copper Heat exchange between the refrigerant and the refrigerant is possible with the double pipe of the pipe.
- the main flow path 22 heading toward the evaporator 7 downstream of the supercooling heat exchanger 5A and the injection flow path 23 to the injection port 1a of the compressor 1 are branched.
- the cooling heat exchanger 5A is connected in this order.
- the “outdoor unit 100” corresponds to a “heat source side unit” in the present invention.
- the “indoor unit 200” corresponds to the “load unit” in the present invention.
- the “condenser 3” corresponds to the “heat source side heat exchanger” in the present invention.
- the “expansion valve 6” corresponds to “load-side expansion means” in the present invention.
- the “evaporator 7” corresponds to the “load side heat exchanger” in the present invention.
- the “liquid extension pipe 18” corresponds to the “liquid pipe” in the present invention.
- the “gas extension pipe 19” corresponds to the “gas pipe” in the present invention.
- the high-temperature and high-pressure gas refrigerant discharged from the compressor 1 flows into the condenser 3.
- the high-temperature and high-pressure gas refrigerant that has flowed into the condenser 3 is condensed by exchanging heat with air in the condenser 3, becomes high-pressure liquid refrigerant (liquid or two-phase state), and is stored in the liquid receiver 4.
- the high-pressure liquid refrigerant stored in the liquid receiver 4 further exchanges heat with air in the supercooling heat exchanger 5 to become supercooled liquid refrigerant.
- the liquid refrigerant is stored in the liquid receiver 4 only when the refrigerant amount of each component device other than the liquid receiver 4 of the refrigeration cycle becomes an appropriate amount and surplus refrigerant is generated.
- the refrigerant amount of each component device other than 4 is insufficient, only the gas refrigerant is stored in the liquid receiver 4.
- the high-temperature and high-pressure refrigerant branched to the injection flow path 23 downstream of the supercooling heat exchanger 5 is reduced to an intermediate pressure by the expansion valve 8 and then connected to a compression chamber in the middle of compression of the compressor 1.
- the discharge temperature of the compressor 1 is reduced by directly flowing into the pressure injection port 1a.
- the high-temperature and high-pressure refrigerant branched to the injection flow path 23 side is decompressed to an intermediate pressure by the expansion valve 8 and then exchanges heat with the high-temperature and high-pressure refrigerant by the supercooling heat exchanger 5. It flows into the injection port 1a of the compressor 1.
- the refrigerant quantity determination means 20 in the first embodiment uses the temperature efficiency ⁇ of the supercooling heat exchanger 5 to check whether the refrigerant is filled with the minimum necessary quantity (the liquid refrigerant is stored in the receiver 4 and the refrigeration is performed). It is determined whether or not the refrigerant of each component device other than the liquid receiver 4 of the cycle is filled with an appropriate amount).
- the temperature efficiency ⁇ of the supercooling heat exchanger 5 is determined by determining the degree of supercooling of the refrigerant at the outlet of the supercooling heat exchanger 5 (condenser 3 outlet temperature TH5—supercooling heat exchanger 5 outlet temperature TH8) by the maximum temperature difference ( It is a value divided by the condenser 3 outlet temperature TH5-the outside air temperature TH6) and is expressed by the following (Formula 1). For example, it is determined that the minimum necessary refrigerant amount is filled when ⁇ reaches 0.6.
- N is displayed on the LED.
- the operator performs refrigerant filling while confirming this display, and records the amount of refrigerant filled when the LED display changes from N to O (Oh) with a memo or the like.
- the calculation of the amount of refrigerant filled is normally performed by measuring the mass of the cylinder before and after filling. Then, from the time when the display of the LED changes from N to O (O), the amount of refrigerant filled after that becomes the surplus refrigerant amount stored as liquid refrigerant in the liquid receiver 4.
- the operator can check the coolant level 11 with the sight glass 14 while checking the sight glass 14 on the side of the liquid receiver 4. Add refrigerant in small increments until When the coolant level 11 can be confirmed with the sight glass 14, the amount of the coolant is 32.0% of the volume of the receiver 4 and therefore the amount of the coolant is insufficient even if conditions such as the outside air temperature change thereafter. There is no state.
- the amount of refrigerant added from the time when the LED display changes from N to O (O) until the refrigerant liquid level 11 can be confirmed with the sight glass 14 on the side surface of the liquid receiver 4 becomes the surplus refrigerant. Since the outside air temperature, the evaporation temperature, and the operation frequency differ depending on the season, the necessary amount of refrigerant changes, but the amount of refrigerant that has changed can be filled. In addition, since the refrigerant
- each sensor such as the outside air temperature TH6 when the LED display changes from N to O described above, the temperature inside the refrigerator or showcase, the length of the extension pipe, and the load are shown. If the controller in the refrigerator can recognize the local information such as the case or unit cooler from the graph in FIG. 3 or Japanese Patent Application Laid-Open No. 2012-132039, etc. Can be calculated. If the amount is displayed on the LED and can be sealed, it is not necessary to fill the coolant up to the position of the sight glass 14. For example, when the refrigerant is sealed at a value of the outside air temperature TH6 of ⁇ 15 ° C., the amount of additional refrigerant may be 10% of the capacity of the receiver 4 for the margin, and the amount is displayed.
- the additional refrigerant amount is 12.1% of the volume of the receiver 4 + margin
- the minute 10% 22.1% is sufficient, and the amount is displayed.
- the refrigerant amount determination mode is set with a switch or the like on the control board of the refrigeration apparatus, and the LED is confirmed.
- the display is N, it is understood that the amount of refrigerant is less than the minimum necessary amount of refrigerant, and a large amount of additional refrigerant is required.
- O O
- the minimum required refrigerant amount has been reached, so adding a small amount of refrigerant changes the outside air temperature, evaporation temperature, and operating frequency depending on the season, and the required refrigerant amount changes. It can be seen that there is a high possibility that a sufficient amount of refrigerant can be filled.
- the sight glass 14 that can confirm the position of the refrigerant liquid 11 of the liquid receiver 4 is installed, and the liquid level indicates the maximum refrigerant liquid level 11 during operation.
- Refrigerant charging at the time of service of the refrigeration apparatus can be carried out easily, quickly and accurately, and overfilling can be prevented. Therefore, by suppressing the increase in high pressure, it is possible to save energy and reduce the amount of refrigerant charged, so that the cost, environmental impact and damage can be reduced.
- the liquid receiver 4, the accumulator (not shown), and the sight glass 14 can be made small, so that the product cost can be reduced and the product can be made compact.
- the sight glass 14 on the side of the liquid receiver 4 is the same as or smaller than the size of the main liquid extension pipe 18 and has a moisture indicator (moisture detector), so that the product cost can be reduced and the refrigerant can be reduced. The presence or absence of moisture can be confirmed. Therefore, it is possible to prevent problems such as corrosion of the refrigerant circuit components, rust, and the oil return hole of the accumulator caused by the ice stack caused by the moisture mixed in the refrigerant circuit, and the reliability can be improved.
- a moisture indicator moisture detector
- the sight glass 14 is taken out from the end plate and barrel of the liquid receiver 4 with a copper pipe 16, and when not installed directly on the liquid receiver 4, the refrigerant liquid surface 11 is stabilized and the presence / absence of the refrigerant liquid surface 11 can be easily confirmed. can do.
- FIG. FIG. 6 is a diagram illustrating an example of the sight glasses 14 and 15 of the refrigeration apparatus according to Embodiment 2 of the present invention.
- the same parts as those in the first embodiment will be denoted by the same reference numerals and the description thereof will be omitted.
- a description will be given of a case where the refrigerant filling amount is confirmed by changing the position of the refrigerant liquid surface 11 that is maximum throughout the year depending on the season, the outside air temperature, high pressure, and the like.
- the refrigerant is charged until the coolant level 11 can be confirmed with the sight glass 14 after the LED on the control board changes from N to O (O), the refrigerant is more than necessary. May be filled. Therefore, the amount of refrigerant to be additionally charged may be changed according to the outside air temperature or the high pressure during operation of the refrigerator.
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- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
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- General Engineering & Computer Science (AREA)
- Air Conditioning Control Device (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
Abstract
Description
冷媒量を判定する方法として、図7に示すようにサイトグラス17を受液器4下流の液配管に設け、試運転中に庫内温度(蒸発器により冷却される対象空間の温度)が設定温度まで低下し、運転が安定した時点で冷媒中のフラッシュガス(気泡)を目視により確認する。そして、フラッシュガスが消えたらその時が余剰なしの冷媒量であるため、その冷媒量に対し、ある割合の冷媒を充填する方法が提案されている。なお、この充填量が冷凍サイクルの状態変化による必要冷媒量の変動に対応する余剰冷媒量となる。この割合は、あるメーカの説明書ではフラッシュが消えた時点までに封入した冷媒量に対し5~10%としているが、各業者のノウハウとなっており、少なすぎると冷媒不足となり、冷却不良となるため、冷媒を多めに追加する場合が多い。 FIG. 7 is a diagram illustrating an example of a refrigerant circuit of a conventional refrigeration apparatus.
As a method of determining the amount of refrigerant, a sight glass 17 is provided in the liquid piping downstream of the
また、万が一、機器の不具合などで冷媒が漏洩した場合、環境に与える被害がより大きくなっていた。 Further, in order to check the flash gas, it is necessary to install the sight glass 17 in the liquid pipe downstream of the
Also, in the unlikely event that the refrigerant leaks due to equipment malfunctions, the damage to the environment was greater.
図1は、本発明の実施の形態1に係る冷凍装置の冷媒回路の一例を示す図である。
本実施の形態1に係る冷凍装置は、室外ユニット100及び室内ユニット200を備えている。
室外ユニット100は、圧縮機1、凝縮器3、受液器4、及び過冷却熱交換器5を備えている。
また、過冷却熱交換器5の下流で、室内ユニット200の蒸発器7へ向かうメイン流路22と、圧縮機1のインジェクションポート1aへ向かうインジェクション流路23とに分岐され、メイン流路22側には液操作弁10が、インジェクション流路23側には膨張弁8が、それぞれ設けられている。なお、室内ユニット200は、ショーケース、ユニットクーラなどが利用される。
1 is a diagram illustrating an example of a refrigerant circuit of a refrigeration apparatus according to
The refrigeration apparatus according to Embodiment 1 includes an
The
Further, downstream of the
第2温度センサ(TH8)は、過冷却熱交換器5の出口側から膨張弁6の入口側に至る流路のいずれかの位置に設けられ、冷媒の温度を検知する。
第3温度センサ(TH6)は、凝縮器3が冷媒と熱交換する前の空気の温度を検知する。 The first temperature sensor (TH5) is located at any position on the outlet side of the
The second temperature sensor (TH8) is provided at any position in the flow path from the outlet side of the
The third temperature sensor (TH6) detects the temperature of the air before the
なお、冷媒回路には冷媒を充填する際には、図示省略のボンベが用いられる。 In addition, the refrigerant amount determination means 20 is provided with a
Note that a cylinder (not shown) is used when the refrigerant circuit is filled with the refrigerant.
蒸発器7では膨張弁6で絞られた2相冷媒が蒸発し気相となるが、図2に示すとおり、凝縮温度が低いほど膨張弁6直後の湿り度が大きくなるため蒸発器7内には多くの冷媒が貯留することになる。
よって、冷凍装置を運転するのに必要な冷媒量の季節による変動は、蒸発温度が一定であれば、凝縮器3容積、受液器4容積と液延長配管+蒸発器容積の相対的な関係により決まり、凝縮器3、受液器4容積の割合が多くなると凝縮温度が高いほど必要冷媒量が多くなり、液延長配管+蒸発器容積の割合が多くなると凝縮温度が低いほど必要冷媒量は多くなる。 FIG. 2 is a Mollier diagram corresponding to different condensation temperatures of the refrigeration apparatus according to
In the
Therefore, the seasonal variation in the amount of refrigerant required to operate the refrigeration apparatus is a relative relationship between the volume of the
受液器容積 = (凝縮器容積+液延長配管容積)×(125%±25%) [Formula 1]
Receiver volume = (condenser volume + liquid extension pipe volume) x (125% ± 25%)
図3は、外気温度が変化することで、受液器4内液比率(=受液器4内の液冷媒が存在する部分の容積÷受液器4容積)がどのように変化するかを条件別に示している。 FIG. 3 is a diagram showing a ratio of the liquid in the
FIG. 3 shows how the liquid ratio in the liquid receiver 4 (= the volume of the liquid refrigerant in the
つまり、外気温度43℃は必要冷媒が少ないため余剰冷媒が液だめ内に多く貯留し、外気温度-15℃では必要冷媒が多いため余剰冷媒がなくなり液だめ内に貯留する冷媒はなくなる。外気温度が低くなるほど必要冷媒量が増える傾向にあり、これは凝縮器3、受液器4内冷媒量の変化量よりも液延長配管+蒸発器容積内冷媒量の変化量が多いためである。外気温度5℃以下で受液器内液比率の変化がないのは凝縮器3のファン風量をコントロールして凝縮温度を一定に保つ制御を実施しているためである。 The use range of the outside air temperature around the
That is, since the required refrigerant is low at the outside air temperature of 43 ° C., a large amount of surplus refrigerant is stored in the liquid reservoir, and at the outside air temperature of −15 ° C., the necessary refrigerant is large and the surplus refrigerant is eliminated and there is no refrigerant stored in the liquid reservoir. The required amount of refrigerant tends to increase as the outside air temperature decreases. This is because the amount of change in the amount of refrigerant in the liquid extension pipe + evaporator volume is greater than the amount of change in the amount of refrigerant in the
室内ユニット100Aは、図1と同様に圧縮機1、凝縮器3、受液器4、及び過冷却熱交換器5Aを備えているが、過冷却熱交換器5Aは、プレート熱交換器や銅管の2重管で冷媒と冷媒との熱交換が可能となっている。過冷却熱交換器5Aの下流で蒸発器7へ向かうメイン流路22と、圧縮機1のインジェクションポート1aへのインジェクション流路23とに分岐され、インジェクション流路23側では、膨張弁8、過冷却熱交換器5Aの順に接続されている。 FIG. 5 is a diagram illustrating another example of the refrigerant circuit of the refrigeration apparatus according to
The
なお、「室内ユニット200」は、本発明における「負荷側ユニット」に相当する。
なお、「凝縮器3」は、本発明における「熱源側熱交換器」に相当する。
なお、「膨張弁6」は、本発明における「負荷側膨張手段」に相当する。
なお、「蒸発器7」は、本発明における「負荷側熱交換器」に相当する。
なお、「液延長配管18」は、本発明における「液配管」に相当する。
なお、「ガス延長配管19」は、本発明における「ガス配管」に相当する。 The “
The “
The “
The “
The “
The “
The “
圧縮機1から吐出された高温高圧のガス冷媒は、凝縮器3へ流入する。凝縮器3へ流入した高温高圧のガス冷媒は、凝縮器3において空気と熱交換して凝縮され、高圧液冷媒(液または二相状態)となり、受液器4に貯留される。受液器4に貯留された高圧液冷媒は、さらに過冷却熱交換器5で空気と熱交換して、過冷却された液冷媒となる。
ここで、受液器4に液冷媒が貯留されるのは、冷凍サイクルの受液器4以外の各構成機器の冷媒量が適正量になって余剰冷媒が生じた場合のみで、受液器4以外の各構成機器の冷媒量が不足している場合は、受液器4に貯留されるのはガス冷媒のみとなる。 Next, the flow of the refrigerant in the refrigeration apparatus according to
The high-temperature and high-pressure gas refrigerant discharged from the
Here, the liquid refrigerant is stored in the
また、図5の場合において、インジェクション流路23側に分岐された高温高圧の冷媒は、膨張弁8で中間圧に減圧された後、過冷却熱交換器5で高温高圧冷媒と熱交換し、圧縮機1のインジェクションポート1aに流入する。 Further, the high-temperature and high-pressure refrigerant branched to the
Further, in the case of FIG. 5, the high-temperature and high-pressure refrigerant branched to the
ε = (TH5-TH8)÷(TH5-TH6) [Formula 2]
ε = (TH5-TH8) ÷ (TH5-TH6)
次に、このような温度効率εと、図4に示す受液器4のサイトグラス14を用いた試運転時の冷媒充填の具体的な方法について説明する。
まず、冷凍装置の回路内の真空引きを実施した後、冷凍装置を停止した状態で冷媒を充填する。その後、冷凍装置を運転しながら冷媒を少しずつ充填する。このとき、冷凍装置の制御基板上のスイッチなどで冷媒量判定モードとすることで、基板のLED上に冷媒が最低必要な量充填されているかを上記εに基づいて表示する。例えば、εの値が0.6以上となり、冷媒が最低必要な量に達している場合、LEDにO(オー)を表示する。 (Refrigerant charging method during trial operation)
Next, a specific method for charging the refrigerant during the trial operation using the temperature efficiency ε and the
First, after evacuating the circuit of the refrigeration apparatus, the refrigerant is charged in a state where the refrigeration apparatus is stopped. Thereafter, the refrigerant is filled little by little while operating the refrigeration apparatus. At this time, by setting the refrigerant amount determination mode with a switch or the like on the control board of the refrigeration apparatus, whether or not the minimum amount of refrigerant is filled on the LED of the board is displayed based on the above ε. For example, when the value of ε is 0.6 or more and the refrigerant reaches the minimum required amount, O (O) is displayed on the LED.
なお、冷媒液面11がサイトグラス14で確認できた時点で充填した冷媒量は十分であるため、それ以上冷媒を充填しないようにする。 That is, the amount of refrigerant added from the time when the LED display changes from N to O (O) until the
In addition, since the refrigerant | coolant amount with which the refrigerant |
次に、製品をサービスする場合など、ある程度冷媒回路内に冷媒が残っている状態での冷媒充填方法について説明する。
作業者は冷凍装置を運転しながら、受液器4側面のサイトグラス14を確認する。液冷媒が確認できる場合は、季節によって、外気温度、蒸発温度、運転周波数が異なり、必要な冷媒量が変化する分も含めて十分な冷媒量が充填されているため、特に冷媒を追加する必要がない。逆に、冷媒を多く充填しすぎている可能性がある場合は、冷媒液面11が確認できるまで冷媒を回収する。 (Method of charging refrigerant at the time of service)
Next, a refrigerant charging method in a state where the refrigerant remains in the refrigerant circuit to some extent, such as when servicing a product, will be described.
The operator checks the
なお、サービス時も冷媒液面11がサイトグラス14で確認できた時点で充填した冷媒量は十分であるため、それ以上冷媒を充填しないようにする。 When the
In addition, since the refrigerant | coolant amount with which the refrigerant |
冷凍装置運転中に液電磁弁9または液操作弁10を閉じることで、受液器4内に冷媒を回収するポンプダウンを実施する。これにより、受液器4側面のサイトグラス14が満液状態となり、サイトグラス14に付属の図示省略のモイスチャインジケータ(水分検知器)により、冷媒回路内の水分有無を確認できる。 Next, a method for confirming the presence or absence of moisture in the refrigerant circuit using the
By closing the liquid
また、サイトグラス14は受液器4の鏡板、胴から銅配管16で取り出し、受液器4に直接設置しない場合は冷媒液面11を安定化させ、冷媒液面11有無の確認を容易とすることができる。 Further, the
Further, the
図6は、本発明の実施の形態2に係る冷凍装置のサイトグラス14、15の一例を示す図である。
なお、本実施の形態2では本実施の形態1との相違点を中心に説明し、本実施の形態1と同一部分には、同一符号を付して説明を省略するものとしている。
実施の形態2では、季節、外気温度、高圧などにより、年間を通して最大となる冷媒液面11位置を変化させて冷媒充填量を確認する場合について説明する。 Embodiment 2. FIG.
FIG. 6 is a diagram illustrating an example of the
In the second embodiment, differences from the first embodiment will be mainly described, and the same parts as those in the first embodiment will be denoted by the same reference numerals and the description thereof will be omitted.
In the second embodiment, a description will be given of a case where the refrigerant filling amount is confirmed by changing the position of the
Claims (9)
- 圧縮機、熱源側熱交換器、過冷却熱交換器、受液器を少なくとも有する熱源側ユニットと、負荷側膨張手段および負荷側熱交換器を少なくとも有する負荷側ユニットとが、液配管およびガス配管を介して接続され、
前記圧縮機、前記熱源側熱交換器、前記過冷却熱交換器、前記受液器、前記負荷側膨張手段、および前記負荷側熱交換器に冷媒を循環させる冷媒回路が形成される冷凍装置において、
前記受液器の側面にサイトグラスを備え、
前記サイトグラスは、運転中における前記受液器の年間を通して最大となる冷媒液面位置を確認できる位置に設けられた
ことを特徴とする冷凍装置。 A heat source side unit having at least a compressor, a heat source side heat exchanger, a supercooling heat exchanger, and a liquid receiver, and a load side unit having at least a load side expansion means and a load side heat exchanger include a liquid pipe and a gas pipe. Connected through
In the compressor, the heat source side heat exchanger, the supercooling heat exchanger, the liquid receiver, the load side expansion means, and a refrigeration apparatus in which a refrigerant circuit for circulating a refrigerant in the load side heat exchanger is formed. ,
A sight glass is provided on the side of the receiver,
The said sight glass was provided in the position which can confirm the refrigerant | coolant liquid level position which becomes the maximum through the year of the said receiver during a driving | operation. The refrigeration apparatus characterized by the above-mentioned. - 前記受液器の容積は、
前記熱源側熱交換器の容積と前記液配管の容積との和の、125%±25%の範囲内に決定される
ことを特徴とする請求項1に記載の冷凍装置。 The volume of the receiver is
2. The refrigeration apparatus according to claim 1, wherein the refrigeration apparatus is determined within a range of 125% ± 25% of a sum of a volume of the heat source side heat exchanger and a volume of the liquid pipe. - 前記サイトグラスは、冷媒が前記受液器の容積の33%以下であるときの冷媒液面位置を確認できる位置に設けられた
ことを特徴とする請求項1または2に記載の冷凍装置。 3. The refrigeration apparatus according to claim 1, wherein the sight glass is provided at a position where a refrigerant liquid level position can be confirmed when the refrigerant is 33% or less of the volume of the liquid receiver. - 外気温度を限定した場合の最高液面位置を確認できる位置に、前記サイトグラスを少なくともさらに1つ設けた
ことを特徴とする請求項1~3のいずれか一項に記載の冷凍装置。 The refrigeration apparatus according to any one of claims 1 to 3, wherein at least one sight glass is provided at a position where the highest liquid level position when the outside air temperature is limited can be confirmed. - 前記冷媒回路に充填された冷媒が、冷媒不足でない量充填されているかを判定する冷媒量判定手段を備えた
ことを特徴とする請求項1~4のいずれか一項に記載の冷凍装置。 The refrigeration apparatus according to any one of claims 1 to 4, further comprising a refrigerant amount determination unit that determines whether or not the refrigerant charged in the refrigerant circuit is charged in an amount that is not insufficient for the refrigerant. - 前記熱源側熱交換器の出口側から前記過冷却熱交換器の入口側に至る流路のいずれかの位置に設けられ、前記冷媒の温度を検出する第1温度センサと、
前記過冷却熱交換器の出口側から前記負荷側膨張手段の入口側に至る流路のいずれかの位置に設けられ、前記冷媒の温度を検出する第2温度センサと、
前記熱源側熱交換器が前記冷媒と熱交換する空気の温度を検出する外気温度センサと、を備え、
前記冷媒量判定手段は、
前記第1温度センサの検出温度と、前記第2温度センサの検出温度との温度差により、過冷却度を求め、
前記第1温度センサの検出温度と、前記外気温度センサの検出温度との温度差により、前記過冷却熱交換器の最大温度差を求める
ことを特徴とする請求項5に記載の冷凍装置。 A first temperature sensor that is provided at any position in the flow path from the outlet side of the heat source side heat exchanger to the inlet side of the subcooling heat exchanger, and detects the temperature of the refrigerant;
A second temperature sensor that is provided at any position in the flow path from the outlet side of the supercooling heat exchanger to the inlet side of the load side expansion means, and detects the temperature of the refrigerant;
An outside air temperature sensor that detects the temperature of the air with which the heat source side heat exchanger exchanges heat with the refrigerant, and
The refrigerant amount determination means includes
The degree of supercooling is obtained from the temperature difference between the detected temperature of the first temperature sensor and the detected temperature of the second temperature sensor,
The refrigeration apparatus according to claim 5, wherein a maximum temperature difference of the supercooling heat exchanger is obtained from a temperature difference between a temperature detected by the first temperature sensor and a temperature detected by the outside air temperature sensor. - 前記冷媒量判定手段は表示部を備え、
前記冷媒回路に充填された冷媒が、冷媒不足でない量充填されているかの判定結果を前記表示部に表示する
ことを特徴とする請求項5または6に記載の冷凍装置。 The refrigerant amount determination means includes a display unit,
The refrigeration apparatus according to claim 5 or 6, wherein the display unit displays a determination result as to whether or not the refrigerant charged in the refrigerant circuit is filled in an amount that is not insufficient for the refrigerant. - 前記表示部は7セグメントLEDにより構成された
ことを特徴とする請求項7に記載の冷凍装置。 The refrigeration apparatus according to claim 7, wherein the display unit includes a 7-segment LED. - 前記サイトグラスは、水分検知機能付きである
ことを特徴とする請求項1~8のいずれか一項に記載の冷凍装置。 The refrigeration apparatus according to any one of claims 1 to 8, wherein the sight glass has a moisture detection function.
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Also Published As
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JPWO2015111222A1 (en) | 2017-03-23 |
CN105408704B (en) | 2017-10-24 |
CN105408704A (en) | 2016-03-16 |
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