WO2008018373A1 - Climatiseur et procédé pour le nettoyer - Google Patents
Climatiseur et procédé pour le nettoyer Download PDFInfo
- Publication number
- WO2008018373A1 WO2008018373A1 PCT/JP2007/065234 JP2007065234W WO2008018373A1 WO 2008018373 A1 WO2008018373 A1 WO 2008018373A1 JP 2007065234 W JP2007065234 W JP 2007065234W WO 2008018373 A1 WO2008018373 A1 WO 2008018373A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- filling
- refrigeration cycle
- air conditioner
- pressure
- cleaning
- Prior art date
Links
- 238000004140 cleaning Methods 0.000 title claims abstract description 136
- 238000000034 method Methods 0.000 title claims abstract description 98
- 238000005057 refrigeration Methods 0.000 claims abstract description 210
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims abstract description 163
- 229910002092 carbon dioxide Inorganic materials 0.000 claims abstract description 81
- 239000001569 carbon dioxide Substances 0.000 claims abstract description 81
- 238000010977 unit operation Methods 0.000 claims abstract description 44
- 239000003507 refrigerant Substances 0.000 claims description 134
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 127
- 239000012530 fluid Substances 0.000 claims description 73
- 229910052757 nitrogen Inorganic materials 0.000 claims description 58
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 32
- 238000007599 discharging Methods 0.000 claims description 26
- 238000001514 detection method Methods 0.000 claims description 10
- 238000009835 boiling Methods 0.000 claims description 9
- 238000010438 heat treatment Methods 0.000 claims description 8
- 239000012535 impurity Substances 0.000 abstract description 70
- 239000000463 material Substances 0.000 abstract description 2
- 239000002826 coolant Substances 0.000 abstract 2
- 239000007789 gas Substances 0.000 description 59
- 239000007788 liquid Substances 0.000 description 43
- 230000000694 effects Effects 0.000 description 33
- 230000008569 process Effects 0.000 description 32
- 238000004378 air conditioning Methods 0.000 description 22
- 229910001873 dinitrogen Inorganic materials 0.000 description 12
- 238000012360 testing method Methods 0.000 description 9
- 238000001816 cooling Methods 0.000 description 8
- 230000001965 increasing effect Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 230000006870 function Effects 0.000 description 4
- 238000012545 processing Methods 0.000 description 4
- 230000003252 repetitive effect Effects 0.000 description 4
- KYKAJFCTULSVSH-UHFFFAOYSA-N chloro(fluoro)methane Chemical compound F[C]Cl KYKAJFCTULSVSH-UHFFFAOYSA-N 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
- 238000005187 foaming Methods 0.000 description 3
- 239000011261 inert gas Substances 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 230000004044 response Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 238000010792 warming Methods 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 description 2
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000004891 communication Methods 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 238000005429 filling process Methods 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- FBAFATDZDUQKNH-UHFFFAOYSA-M iron chloride Chemical compound [Cl-].[Fe] FBAFATDZDUQKNH-UHFFFAOYSA-M 0.000 description 2
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 description 2
- 230000009257 reactivity Effects 0.000 description 2
- 238000004904 shortening Methods 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 230000002159 abnormal effect Effects 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000000274 adsorptive effect Effects 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 239000012459 cleaning agent Substances 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- NBVXSUQYWXRMNV-UHFFFAOYSA-N fluoromethane Chemical compound FC NBVXSUQYWXRMNV-UHFFFAOYSA-N 0.000 description 1
- 235000011187 glycerol Nutrition 0.000 description 1
- 239000001282 iso-butane Substances 0.000 description 1
- 231100001231 less toxic Toxicity 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000012806 monitoring device Methods 0.000 description 1
- 150000002829 nitrogen Chemical class 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
- 230000032258 transport Effects 0.000 description 1
- 238000013022 venting Methods 0.000 description 1
Classifications
-
- 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
-
- 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
- F25B1/00—Compression machines, plants or systems with non-reversible cycle
-
- 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
- F25B43/00—Arrangements for separating or purifying gases or liquids; Arrangements for vaporising the residuum of liquid refrigerant, e.g. by heat
-
- 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
- F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
- F25B9/002—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant
- F25B9/008—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the refrigerant the refrigerant being carbon dioxide
-
- 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
- F25B13/00—Compression machines, plants or systems, with reversible cycle
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/0318—Processes
- Y10T137/0402—Cleaning, repairing, or assembling
- Y10T137/0419—Fluid cleaning or flushing
Definitions
- the present invention relates to an air conditioner and a cleaning method thereof, and more particularly to an air conditioner using carbon dioxide as a working refrigerant and a cleaning method thereof.
- chlorofluorocarbon which is a fluid that efficiently transports heat energy
- Patent Document 1 shown below proposes a method for removing iron chloride mixed as an impurity in a refrigerant as a method for replacing conventional air-conditioning equipment by using alternative chlorofluorocarbon.
- the conventional CFC refrigerant is recovered by evacuation of the HCFC refrigerant, and the relatively environmentally friendly HFC refrigerant is once introduced into the refrigeration cycle, and then recovered to adsorb and remove iron chloride and passed through activated carbon. Later, a method of re-introducing has been proposed.
- this alternative chlorofluorocarbon which has a relatively high global warming factor, is also being restricted.
- the Fluorocarbon Recovery and Destruction Law which obligates proper collection, has been promulgated, and attention has been focused on the development of new alternative refrigerants and their utilization technologies.
- this alternative refrigerant there are natural refrigerants such as carbon dioxide, ammonia, hydrocarbons (isobutane, filling pan, etc.), water, air and the like. These natural refrigerants have a very low GWP (Global Warming Potential) value compared to the above-mentioned CFCs and alternative CFCs.
- GWP Global Warming Potential
- carbon dioxide has an ozone depletion potential of zero, a global warming potential that is significantly less toxic than conventional refrigerants, and is nonflammable.
- ozone depletion potential of zero
- a global warming potential that is significantly less toxic than conventional refrigerants, and is nonflammable.
- Patent Document 1 JP 2004-218972 A
- the present invention has been made in view of the above-described points, and an object of the present invention is to use existing equipment that does not perform evacuation when carbon dioxide is used as a working refrigerant.
- An object of the present invention is to provide an air conditioner capable of reducing the amount of impurities remaining in the refrigeration cycle and a cleaning method therefor.
- a method for cleaning an air conditioner according to a first invention is a method for cleaning an air conditioner that uses carbon dioxide as a working refrigerant, and includes the following steps.
- the filling step the refrigeration cycle is filled with working fluid.
- the release step the filling object filled in the refrigeration cycle is released after the filling step.
- the repetitive step if the filling step and the discharging step are unit operations, the unit operation is performed at least once.
- the working fluid for cleaning here includes carbon dioxide, nitrogen, etc., which do not need to have a function as a refrigerant during air conditioning.
- the working fluid is filled into the refrigeration cycle in the filling step, so that the relative concentration of impurities in the refrigeration cycle can be reduced.
- the object to be filled which is filled in the refrigeration cycle without evacuating the conventional refrigeration cycle, is discharged out of the refrigeration cycle. At this time, some of the impurities present in the refrigeration cycle are also released out of the refrigeration cycle, and the absolute amount of impurities in the refrigeration cycle is reduced.
- the unit operation by the filling step and the discharging step is repeated at least once.
- the air monitoring device is a method for cleaning an air conditioner according to the first invention, and in the filling step, the working fluid is used until the pressure in the refrigeration cycle reaches at least a pressure exceeding the atmospheric pressure. Fill in. In the release step, the object to be filled is released until the pressure in the refrigeration cycle is approximately atmospheric pressure.
- the pressure above atmospheric pressure in the filling step here is preferably 5 atmospheres or more, more preferably 7 atmospheres or more.
- the concentration of impurities remaining in the refrigeration cycle can be further reduced. Then, after the filling step for reducing the relative concentration of impurities is completed in this way, in the discharging step, the filling object is discharged until the pressure in the refrigeration cycle becomes substantially atmospheric pressure, and a large amount of working fluid is discharged. As a result, many impurities can be released out of the refrigeration cycle.
- the unit is connected to the plurality of indoor units.
- a higher cleaning effect can be obtained than the conventional vacuuming. That is, in the conventional evacuation, there is a possibility that the cleaning effect may be improved only in the portion where the fluid easily flows in the piping, and there is a case where it is desired to improve the cleaning effect in the branching portion of the piping.
- the working fluid is filled until the pressure in the refrigeration cycle becomes equal to or higher than the atmospheric pressure. Therefore, impurities existing in parts where flow of fluid is difficult to flow, such as pipe branch parts, are also mixed with the working fluid. Together In other words, it can be efficiently discharged by being dissolved in the working fluid.
- a method for cleaning an air conditioner according to a third invention is the method for cleaning an air conditioner according to the first or second invention, wherein the working fluid is carbon dioxide having the same component as the working refrigerant.
- carbon dioxide which is the same component as the working refrigerant, is used as the working fluid used for cleaning the inside of the refrigeration cycle. For this reason, even if it remains after the working fluid force release step filled in the refrigeration cycle in the filling step, it will be used as a working refrigerant in the end, so there will be no problem.
- the unit is connected to the plurality of indoor units.
- a higher cleaning effect can be obtained than the conventional vacuuming. That is, in the conventional evacuation, there is a possibility that the cleaning effect may be improved only in the portion where the fluid easily flows in the piping, and there is a case where it is desired to improve the cleaning effect in the branching portion of the piping.
- the working fluid is filled until the pressure in the refrigeration cycle becomes equal to or higher than the atmospheric pressure. Therefore, impurities existing in parts where flow of fluid is difficult to flow, such as pipe branch parts, are also mixed with the working fluid. In other words, it can be discharged efficiently by being dissolved in the working fluid.
- a method for cleaning an air conditioner according to a fourth invention is the method for cleaning an air conditioner according to the first invention or the second invention, wherein the working fluid is nitrogen.
- nitrogen which is different from the working fluid used during the air-conditioning operation, is used as the working fluid for cleaning. Since this nitrogen has poor chemical reactivity with impurities in the piping, it is possible to obtain a cleaning effect corresponding to the amount of nitrogen filled. Then, carbon dioxide used as a working refrigerant may be filled while recovering the filling target from the refrigeration cycle filled with nitrogen.
- An air-conditioning apparatus cleaning method is the air-conditioning apparatus cleaning method according to any one of the first to fourth aspects of the present invention, wherein the filling step is! /
- the temperature of the fluid and / or the pressure in the refrigeration cycle when stopping filling in the filling step and the number of repetitions of the unit operation in the repeating step are approximately inversely proportional to each other.
- the pressure of the working fluid is increased and / or the pressure in the refrigeration cycle when stopping filling at the filling step is increased, the number of repetitions of the unit operation in the repetition step is reduced.
- the temperature of the working fluid to be filled in the filling step and / or the filling step when stopping the filling! The degree of increasing the pressure in the refrigeration cycle can be reduced.
- An air conditioner cleaning method is the air conditioner cleaning method according to the fifth invention, wherein the unit operation is repeated a predetermined number of times in a repetitive step.
- the working fluid is filled at a temperature corresponding to the predetermined number of times and / or in accordance with a pressure condition in the refrigeration cycle corresponding to the predetermined number of times.
- the filling step is performed at a temperature corresponding to the predetermined number of times and / or a pressure condition in the refrigeration cycle corresponding to the predetermined number of times. Is filled with a working fluid.
- An air conditioner cleaning method is the air conditioner cleaning method according to the fifth aspect of the present invention, wherein, in the filling step, a predetermined temperature and / or working fluid at the time of filling the working fluid The predetermined pressure in the refrigeration cycle when filling #2. In the repetition step, the unit operation is repeated by the number of times corresponding to the predetermined temperature and / or the predetermined pressure.
- the process is repeated.
- the unit operation is repeated by the number of times corresponding to the predetermined temperature and / or the predetermined pressure.
- An air conditioner cleaning method is the air conditioner cleaning method according to any one of the first to seventh inventions, wherein the filling step is included in the discharged filling medium.
- the concentration of a predetermined component that is a component other than the working refrigerant and other than the working fluid is detected, and the temperature of the working fluid to be filled in the next filling step is detected according to the detected value. And / or adjust the pressure.
- the concentration of a predetermined component contained in the discharged filling medium is detected, and this value is used to adjust the temperature and / or pressure of the working fluid in the next filling step! /
- An air conditioner cleaning method is the air conditioner cleaning method according to the eighth aspect of the present invention, wherein the predetermined component contains moisture. Then, in the filling step, heating is performed so that the temperature exceeds the boiling point of moisture corresponding to the pressure in the refrigeration cycle and the pressure in the refrigeration cycle.
- the pressure in the refrigeration cycle may be a partial pressure of moisture in the refrigeration cycle.
- the object to be heated may be a working fluid to be filled or a part of a refrigeration cycle! /.
- a method for cleaning an air conditioner according to a tenth aspect of the invention is a method for cleaning an air conditioner according to any of the first to ninth aspects, wherein the refrigeration cycle includes a single heat source unit, There are several usage units, and a connecting pipe provided with a branch portion for connecting a plurality of usage units in parallel to one heat source unit. Then, the filling step, the discharging step, and the repeating step are performed for at least the branch portion.
- An air conditioner according to an eleventh aspect of the invention is an air conditioner that uses carbon dioxide as a working refrigerant, and includes a refrigeration cycle and a counter.
- the refrigeration cycle can be performed by repeating the unit operation of discharging the filling target after filling the working fluid at least once.
- the counter counts and outputs the number of unit operations. Note that the output by the counter here includes a case where count data is transmitted to another device other than just outputting count data to a display device such as a display.
- the cleaning working fluid here is not particularly required to have a function as a refrigerant during air conditioning, and includes carbon dioxide, nitrogen, and the like.
- the working fluid is filled in the refrigeration cycle, so that The relative concentration of impurities can be reduced. Then, by releasing the filling target containing impurities filled in the refrigeration cycle without evacuating the conventional refrigeration cycle, the impurities existing in the refrigeration cycle are discharged. Part of it is released outside the refrigeration cycle, and the absolute amount of impurities in the refrigeration cycle can be reduced. It is possible to further reduce the amount of impurities in the refrigeration cycle by repeating the unit operation of discharging the filling target after filling such a working fluid at least once. Here, since the number of unit operations can be grasped by the counter, the amount of impurities remaining in the refrigeration cycle can be predicted.
- An air conditioner according to a twelfth aspect of the present invention is the air conditioner according to the eleventh aspect of the present invention, wherein the judgment is made as to whether or not to repeat the unit operation based on the number of times obtained by the output of the counter.
- the unit is further provided.
- An air conditioner according to a thirteenth aspect of the present invention is the air conditioner according to the twelfth aspect of the present invention, wherein the determination unit includes the temperature of the working fluid to be filled and / or the pressure in the refrigeration cycle after filling of the working fluid. It is determined that the unit operation is repeated by the number of times corresponding to the above.
- the determination unit since the number of repetitions according to the temperature / pressure situation is determined by the determination unit, the reliability of the cleaning effect can be improved.
- An air conditioner according to a fourteenth aspect of the present invention is the air conditioner according to the twelfth aspect of the present invention or the thirteenth aspect of the present invention, wherein the component contained in the discharged filling medium is other than the working refrigerant.
- a detection unit that detects the concentration of a predetermined component that is a component other than the working fluid is further provided.
- the judgment part is unit by the number of times according to the density
- the determination unit determines to repeat the unit operation according to the concentration of the predetermined component detected by the detection unit, the reliability of the cleaning effect can be further improved.
- An air conditioner according to a fifteenth aspect of the present invention is the air conditioner according to any of the twelfth to fourteenth aspects of the present invention, wherein the working fluid is charged into the refrigeration cycle, and the discharge of the filling object from the refrigeration cycle thereafter.
- the control unit further includes a control unit that performs the charge / discharge control to stop the charge / discharge when the determination unit determines that the unit operation is to be repeated.
- the control unit can stop the filling / releasing control to automate the completion of the filling / releasing process.
- An air conditioner according to a sixteenth aspect of the present invention is the air conditioner according to any of the tenth to fifteenth aspects of the present invention, wherein the refrigeration cycle includes one heat source unit, a plurality of utilization units, And a connecting pipe provided with a branching section to connect a plurality of utilization units in parallel to one heat source unit. Then, the unit operation of discharging the filling target after filling the working fluid is performed at least once for at least the branch portion.
- the amount of carbon dioxide released during cleaning of the refrigeration cycle can be reduced.
- the temperature at the time of filling the working fluid is fixed in advance to a predetermined temperature, and / or the pressure in the refrigeration cycle at the time of filling the working fluid is set to a predetermined pressure in advance.
- the working fluid is repeated in the repetition step V, and the unit operation is repeated by the number of times corresponding to the predetermined temperature and / or the predetermined pressure. It is possible to specify the filling conditions and the number of repetitions for recovering impurities more efficiently in consideration of the state of filling and the effect of removing impurities.
- the air conditioner according to the twelfth aspect of the present invention it is possible to automate the determination as to whether or not to finish the repetitive process as long as the number of times the unit operation is repeated can be grasped by the counter.
- the reliability of the cleaning effect can be further improved.
- the control unit stops the filling / releasing control, whereby the completion of the filling / releasing process can be automated.
- the cleaning effect can be improved even at a branch portion with a large flow resistance.
- FIG. 1 is a diagram showing a refrigerant circuit of an air conditioner according to an embodiment of the present invention.
- FIG. 2 is a block diagram of a control device of the air conditioner.
- FIG. 3 is a flowchart of a refrigeration cycle cleaning process.
- FIG. 4 is a flowchart of a refrigeration cycle cleaning process according to Modification (A).
- FIG. 5 is a diagram showing the number of times charging / discharging is repeated for each condition in the refrigeration cycle cleaning method according to modification (G).
- FIG. 1 is a schematic diagram of a refrigerant circuit of the air conditioner 1.
- the air conditioner 1 is a multi-type device that is used for air conditioning such as cooling and heating in buildings, etc., and uses one heat source unit 2 and carbon dioxide as a working refrigerant, which are connected in parallel.
- a plurality of use units 5 (in this embodiment), a liquid refrigerant pipe 6 and a gas refrigerant pipe 7, a service port S and a control device 70 for connecting the heat source unit 2 and the use nut 5 are provided. I have.
- the heat source unit 2 is installed on the roof of a building, etc., and mainly includes a compressor 21, a four-way switching valve 22, a heat source side heat exchanger 23, a heat source side expansion valve 24, a liquid side closing valve 25, The gas side shut-off valve 26 and the refrigerant pipe connecting them are configured.
- the compressor 21 is a device for sucking and compressing a gas refrigerant.
- the four-way switching valve 22 is a valve for switching the direction of refrigerant flow in the refrigerant circuit when switching between cooling operation and heating operation. This four-way switching valve connects the discharge side of the compressor 21 and the gas side of the heat source side heat exchanger 23 and also connects the suction side of the compressor 21 and the gas side shut-off valve 26 during the cooling operation. Sometimes it is possible to connect the discharge side of the compressor 21 and the gas side shut-off valve 26 and also connect the discharge side of the compressor 21 and the gas side of the heat source side heat exchanger 23 It is.
- the heat source side heat exchanger 23 is a heat exchanger for evaporating or condensing the refrigerant using air or water as a heat source.
- the heat source side expansion valve 24 is a valve for adjusting refrigerant flow rate and refrigerant pressure provided on the liquid side of the heat source side heat exchanger 23.
- the liquid side shutoff valve 25 and the gas side shutoff valve 26 are connected to the liquid refrigerant pipe 6 and the gas refrigerant pipe 7, respectively.
- the usage unit 5 is installed at various locations in the building, and is mainly composed of a usage-side expansion valve 51, a usage-side heat exchanger 52, and a refrigerant pipe connecting them.
- the use side heat exchanger 52 is a heat exchanger for cooling or heating indoor air by evaporating or condensing the refrigerant.
- the use side expansion valve 51 is a valve for adjusting the refrigerant flow rate and the refrigerant flow rate provided on the liquid side of the use side heat exchanger 52.
- the liquid refrigerant pipe 6 and the gas refrigerant pipe 7 are refrigerant pipes that connect the heat source mute 2 and the utilization mute 5, and most of them are arranged in the wall of the building or behind the ceiling.
- a branch portion B is provided in the refrigerant pipe.
- the service port S is a connection port for charging and discharging the working refrigerant to and from the refrigeration cycle.
- the service port S is a liquid port provided adjacent to the use side heat exchanger 52 side of the liquid side shut-off valve 25.
- a pipe-side service port S6, and a gas-side service port S7 provided on the suction side of the compressor 21 adjacent to the use-side heat exchanger 52 side of the gas-side shut-off valve 26 during cooling operation. ing.
- the liquid pipe side service port S6 is provided with a discharge side pipe 34 that is attached to and detached from the liquid pipe when it is filled with refrigerant and communicates with the liquid refrigerant pipe 6 in the attached state! /
- the discharge side pipe 34 is formed with a discharge end 36 at the end opposite to the end on the liquid pipe side service port S6 side, and the end of the liquid pipe side service port S6 side and the discharge end 36 are connected to each other.
- a discharge-side electromagnetic valve 35 is provided between them, and the discharge can be controlled by a control device 70 described later.
- the discharge side pipe 34 includes a temperature sensor T for detecting the refrigerant temperature and a pressure for detecting the refrigerant pressure. Each sensor P is provided.
- the discharge side pipe 34 is provided with a concentration sensor C for detecting the concentration of nitrogen contained in the discharge target when the charge target in the refrigeration cycle is discharged in a discharge step S30 described later.
- the gas pipe side service port S7 is provided with a filling side pipe 32 that is attached to and detached from itself when the refrigerant is filled, and communicates with the gas refrigerant pipe 7 in the attached state. Being! /
- the other end of the filling side pipe 32 opposite to the end on the gas pipe side service port S 7 side is connected to a cylinder body 31 filled with carbon dioxide in a carbon dioxide cylinder 30 described later.
- a filling-side electromagnetic valve 33 is provided between the gas pipe-side service port S7 side end and the cylinder body 31 so that filling can be controlled by a control device 70 described later.
- the control device 70 is a device that performs air conditioning operation and cleaning control, which will be described later.
- the control device 70 mainly includes a control unit 71, a memory 72, a display 73, a counter 74, a temperature detection unit 75, and a pressure detection unit 76. , A density acquisition unit 77, a setting input unit 78, and the like.
- the control unit 71 controls the air conditioning operation or the cleaning process for the refrigeration cycle.
- the memory 72 stores data input from the setting input unit 78 and the like, count data from the counter 74, and the like.
- the counter 74 counts using three processes, which will be described later, a filling step S10, a waiting step S20, and a discharging step S30 as unit operations.
- the display 73 displays the count data by the counter 74 according to the stored contents of the memory 72.
- the temperature detection unit 75 acquires data obtained from the temperature sensor T.
- the pressure detection unit 76 acquires data obtained from the pressure sensor P.
- the density acquisition unit 78 acquires data obtained from the density sensor C.
- the compressor 21 When the liquid side shut-off valve 25 and the gas side shut-off valve 26 are fully opened and an operation command for cooling operation is issued from the control unit 71, the compressor 21 is started. Then, the low-pressure refrigerant is absorbed by the compressor 21. It becomes a high-pressure refrigerant that is compressed to a pressure exceeding the critical pressure. Thereafter, the high-pressure refrigerant is sent to the outdoor heat exchanger 23, where it is cooled by exchanging heat with the outdoor air V in the outdoor heat exchanger 23 functioning as a cooler.
- the high-pressure refrigerant cooled in the outdoor heat exchanger 23 passes through the liquid refrigerant pipe 6 and the liquid side shut-off valve 25 and is sent to the utilization unit 5.
- the high-pressure refrigerant sent to the use unit 5 is sent to the use-side expansion valve 51, and the use-side expansion valve 51 reduces the pressure to a pressure lower than the critical pressure (that is, a pressure close to the suction pressure of the compressor 21).
- the indoor heat exchanger 52 After being reduced in pressure to become a low-pressure gas-liquid two-phase refrigerant, it is sent to the indoor heat exchanger 52 where it evaporates by exchanging heat with indoor air in the indoor heat exchanger 52 that functions as an evaporator. It becomes a low-pressure refrigerant.
- the low-pressure refrigerant evaporated in the indoor heat exchanger 52 is sent to the heat source unit 2, passes through the gas refrigerant pipe 7 and the gas-side shutoff valve 26, and is sucked into the compressor 21 again. In this way, the air conditioning operation of the air conditioner 1 is performed.
- the air conditioner 1 that performs the air conditioning operation as described above is configured by connecting mainly four elements of a heat source unit 2, a utilization unit 5, a liquid refrigerant pipe 6, and a gas refrigerant pipe 7. And installed in the building. First, each of the three elements of the utilization unit 5, the liquid refrigerant pipe 6 and the gas refrigerant pipe 7 is checked for airtightness.
- FIG. 1 all the piping parts from the liquid side shutoff valve 25 to the gas side shutoff valve 26 in the state where the use unit 5, the liquid refrigerant pipe 6 and the gas refrigerant pipe 7 are connected to each other are targeted. Check for airtightness.
- the airtightness test is performed by filling the piping with nitrogen gas for the utilization unit 5, the liquid refrigerant pipe 6 and the gas refrigerant pipe 7 connected to each other.
- the presence or absence of leakage at this time is expected to be due to foaming liquid such as stone water (and a few drops of glycerin mixed with it) at an appropriate concentration. Make sure that it is thoroughly distributed to all locations and check for foaming by the foaming liquid. If airtightness is confirmed by the above airtightness test, it can be recognized that the air conditioning apparatus 1 is free from the possibility of leakage of the working refrigerant even when the operation refrigerant is charged and operated.
- the use unit 5 the liquid refrigerant pipe 6 and the gas refrigerant pipe 7 have been subjected to an airtight test, and it has been confirmed that airtightness has been secured for these three elements constituting the refrigeration cycle.
- air and other non-condensable gases mainly nitrogen gas used in the airtightness test remain.
- the air conditioner 1 of the present embodiment constitutes a refrigeration cycle using carbon dioxide as a working refrigerant
- such residual air mainly nitrogen
- carbon dioxide of the working refrigerant It is positioned as an impurity for If such impurities are present in the refrigeration cycle and carbon dioxide is charged as a working refrigerant and air conditioning operation is performed, the high pressure will rise abnormally, power consumption will increase, and air conditioning capacity will decline. Etc., a defect in each element occurs.
- the gas pipe side service port S7 is connected to the carbon dioxide cylinder 30 via the filling side pipe 32, and the discharge side is the liquid pipe side. It is executed by connecting service port S6 to the discharge side pipe.
- the discharge side pipe 34 is connected to the liquid pipe side service port S6.
- the discharge side solenoid valve 33 is closed by the control unit 71 in order to stop the discharge of the refrigerant from the discharge end 36. Opening and closing is controlled so as to be in a closed state.
- the carbon dioxide cylinder 30 includes a cylinder body 31, a filling side pipe 32, and a filling side solenoid valve 33.
- Carbon dioxide is sealed in the cylinder body 31 in a high pressure state.
- the filling side pipe 32 has the same component as the working refrigerant of the air conditioner 1.
- the filling-side electromagnetic valve 33 is controlled to be opened and closed by the control unit 71, whereby the filling amount of carbon dioxide is adjusted and the pressure in the refrigeration cycle is also adjusted.
- the temperature acquisition unit 75 of the control device 70 is connected to the temperature sensor T, the pressure acquisition unit 76 is connected to the pressure sensor S, and the concentration acquisition unit 77 is connected to the concentration sensor C. It has been done. Then, the control unit 71 controls the cleaning process of the refrigeration cycle based on each data acquired by the temperature sensor T, the pressure sensor S, and the concentration sensor C. Specifically, the control unit 71 controls the opening degree of the charging side electromagnetic valve 33 based on the pressure data acquired by the pressure acquisition unit 76, and based on the nitrogen concentration acquired by the concentration acquisition unit 77! /, By controlling the opening of the discharge side solenoid valve, the filling and discharging control in the cleaning process is performed. This allows the pressure in the refrigeration cycle to be adjusted automatically during the cleaning process and the number of repetitions of the cleaning process to be adjusted.
- FIG. 3 shows a flowchart of the cleaning process performed by the control device 70.
- control flow performed by the control device 70 starting from a state in which the carbon dioxide cylinder 30 is connected to the filling-side service port S7 will be described.
- cleaning process here is performed when the residual nitrogen concentration in the refrigeration cycle is targeted to be less than lOOppm! /,
- the setting input unit 78 of the control device 70 A case where the predetermined pressure for filling is set to 10 atm by operating and inputting will be explained.
- step S10 the controller 70 controls all the valves provided in the refrigeration cycle (specifically, the heat source side expansion valve 24, the liquid side closing valve 25, the gas side closing valve 26, and the usage side expansion valve). 51, etc.) are fully opened, and the charging side solenoid valve 33 is set to the “open” state in order to start filling the carbon dioxide gas in such a fully opened refrigeration cycle, so that the discharge side solenoid valve 35 Controls automatic filling so that is closed. Since each valve is in the “open” state, carbon dioxide gas is used in the refrigeration cycle utilization unit 5 and liquid refrigerant distribution. Spread throughout pipe 6 and gas refrigerant pipe 7.
- the carbon dioxide gas which is the same component as the working refrigerant of the air conditioner 1, is pressurized and filled in the refrigeration cycle.
- the control unit 71 performs control to keep the filling side electromagnetic valve 33 in the “open” state until the pressure value acquired by the pressure acquisition unit 76 reaches 10 atmospheric pressure set as the predetermined pressure, and continues the filling at the predetermined pressure.
- the filling-side solenoid valve 33 When a certain 10 atmospheres is reached, the filling-side solenoid valve 33 is set to the “closed” state, and the filling is terminated (again, the discharge-side solenoid valve 35 is maintained in the “closed” state).
- the counter 74 stores the count data as “once” in the memory 72, and the control unit 71 determines that the unit operation is the first time according to the count data stored in the memory 72. To show, “Once” is displayed on the display 73.
- step S20 the control device 70 maintains a state in which carbon dioxide gas is charged at a predetermined pressure (10 atm) during the refrigeration cycle for a predetermined time (for example, 10 minutes). Thereby, the carbon dioxide gas filled in the refrigeration cycle and the nitrogen remaining in the refrigeration cycle are sufficiently mixed.
- the waiting time here may be adjusted according to the pressure and temperature state of the carbon dioxide gas to be filled, for example, shortening to an appropriate time in the case of high pressure and high temperature. Good.
- step S30 when the control unit 71 of the control device 70 determines that the standby time has exceeded the predetermined time, the discharge-side solenoid valve 35 is set to the “open” state, and the refrigeration cycle utilization unit 5 and liquid Carbon dioxide gas filled in the refrigerant pipe 6 and the gas refrigerant pipe 7 and nitrogen as an impurity are released from the discharge end 36.
- the release is performed until the control unit 71 determines that the pressure S has been reduced to the atmospheric pressure based on the value of the pressure sensor P acquired by the pressure acquisition unit 76.
- the nitrogen partial pressure as an impurity is 0.5 atm, which corresponds to the total pressure of the impurity.
- the partial pressure ratio is getting smaller.
- the discharge of the filling object by the discharge step S30 When the refrigeration cycle is returned to atmospheric pressure at, the nitrogen partial pressure in the refrigeration cycle with a total pressure of 1 atm is reduced to about 0.05 atm. In this way, the refrigeration cycle is cleaned.
- step S40 the concentration acquisition unit 77 acquires from the concentration sensor C the nitrogen concentration in the component released in the release step S30. Then, the control unit 71 of the control device 70 determines whether or not the nitrogen concentration power acquired by the concentration acquisition unit 77 is less than lOOppm which is the residual nitrogen concentration within the target allowable range. Here, if it is not less than lOOppm, the process returns to step S10, and the cleaning process by filling the carbon dioxide gas and releasing the filling object is repeated. In this case, the counter 74 increments the count data and stores it in the memory 72 as “twice”, and the control unit 71 determines that the unit operation is the second time according to the count data stored in the memory 72. To show, “2 times” is displayed on the display 73. On the other hand, if it is less than lOOppm, it is determined that nitrogen has been sufficiently removed from the refrigeration cycle, and the cleaning process is terminated.
- the optimum refrigerant charge amount is adjusted due to various pipe lengths etc. There is a need to. For this reason, the refrigerant that is insufficient with only the amount of carbon dioxide refrigerant as the working refrigerant provided in advance in the heat source unit 2 is additionally charged into the refrigeration cycle by opening the liquid side shutoff valve 25 and the gas side shutoff valve 26. .
- the additional filling amount of carbon dioxide here is the amount that maximizes the refrigerating capacity in the refrigeration cycle and does not cause problems such as abnormal pressure.
- step S40 the nitrogen concentration remaining in the refrigeration cycle can be reduced to the target concentration.
- the force S can effectively reduce the residual nitrogen concentration in the refrigeration cycle without evacuation.
- the air conditioner 1 of the present embodiment Since the working refrigerant is carbon dioxide of the same component, it does not become an impurity in the refrigeration cycle, and the relative concentration of impurities in the refrigeration cycle does not cause a problem! / Power S can be.
- carbon dioxide having a water solubility higher than that of nitrogen is used as a component to be filled in the refrigeration cycle (for example, the solubility in 1 liter of water at 1 atm is normal temperature). Nitrogen is 0.00007 mol, whereas carbon dioxide is 0.053 mol).
- the refrigeration cycle it is preferable to remove moisture as an impurity, but moisture remaining in such a refrigeration cycle can be effectively discharged together with the carbon dioxide gas to be filled. it can. Thereby, in the cleaning method of the present embodiment in which carbon dioxide is filled and released, water remaining in the refrigeration cycle can also be effectively discharged, so that the cleaning effect of the refrigeration cycle can be improved.
- the refrigeration cycle is performed during normal air-conditioning operation.
- the remaining moisture may be absorbed immediately and become carbonic acid, which may corrode the refrigerant piping from the inside.
- the water in the refrigeration cycle is sufficiently removed before filling the carbon dioxide as the working refrigerant and performing normal air conditioning operation, and corrosion of the pipes, etc. The problem is less likely to occur.
- the cleaning method for the air conditioner 1 of the present embodiment pressurizes and fills the refrigeration cycle with carbon dioxide gas, and reaches every corner of the refrigeration cycle. Carbon dioxide gas is distributed. For this reason, even if there is a complicated part in the refrigerant piping of the refrigeration cycle, such as branch part B, where the fluid cannot flow straight, the carbon dioxide gas and nitrogen as an impurity are sufficiently mixed. It can be discharged together. As a result, the branch portion B of the refrigerant pipe can be sufficiently cleaned.
- the number of cleaning unit operations is counted by the counter 74 and displayed on the display, so that the person performing the cleaning process can easily set the number of cleanings. You can see how much it has been cleaned
- the power to offer is S.
- the carbon dioxide which is the same component as the working refrigerant, is pressurized and filled into the refrigeration cycle, and nitrogen that is an impurity in the refrigeration cycle is reduced by releasing the filling target. I gave it as an explanation.
- the present invention is not limited to this.
- the nitrogen in the refrigeration cycle before the treatment for reducing the nitrogen concentration in the refrigeration cycle, the nitrogen in the refrigeration cycle is used.
- nitrogen which is an inert gas (a gas having poor chemical reactivity with respect to impurities in the refrigerant piping)
- inert gas a gas having poor chemical reactivity with respect to impurities in the refrigerant piping
- step S1 the controller 70 controls all the valves provided in the refrigeration cycle (specifically, the heat source side expansion valve 24, the liquid side closing valve 25, the gas side closing valve 26, and the use side expansion valve). 51) is fully opened, and in order to start charging nitrogen gas for such a fully opened refrigeration cycle, the charging side solenoid valve 33 is in the “open” state, and the discharge side solenoid valve 35 is Automatic filling control is performed so that it is in the “closed” state. Since each valve of the refrigeration cycle is in the “open” state, nitrogen gas is distributed throughout every part of the refrigeration cycle. As a result, the nitrogen gas and moisture as impurities are sufficiently mixed even in the branch portion B where the refrigerant pipe is branched and has a complicated structure.
- the controller 70 controls all the valves provided in the refrigeration cycle (specifically, the heat source side expansion valve 24, the liquid side closing valve 25, the gas side closing valve 26, and the use side expansion valve). 51) is fully opened, and in order to start charging nitrogen gas for such a fully opened refrigeration cycle, the charging side solenoi
- control unit 71 performs control to keep the filling side electromagnetic valve 33 in the “open” state until the pressure value acquired by the pressure acquisition unit 76 reaches 10 atmospheric pressure set as the predetermined pressure, and the predetermined pressure is reached. Filled when 10 atm is reached The side solenoid valve 33 is set to the “closed” state, and control for terminating the filling is performed (again, the discharge side solenoid valve 35 is maintained in the “closed” state).
- the counter 74 stores the count data as “one time” in the memory 72, and the control unit 71 determines that the unit operation is the first time according to the count data stored in the memory 72. In order to show, “once” is displayed on the display 73.
- step S2 the control device 70 maintains a state in which nitrogen gas is charged at a predetermined pressure (10 atm) during the refrigeration cycle for a predetermined time (for example, 10 minutes).
- a predetermined pressure 10 atm
- the nitrogen gas filled in the refrigeration cycle is sufficiently mixed with the water remaining in the refrigeration cycle.
- the waiting time here may be adjusted according to the pressure and temperature state of the nitrogen gas to be filled, for example, shortening to an appropriate time in the case of high pressure and high temperature. .
- step S3 when the control unit 71 of the control device 70 determines that the standby time has exceeded the predetermined time, the release-side solenoid valve 35 is set to the “open” state, and the refrigeration cycle utilization unit 5 and liquid Nitrogen gas filled in the refrigerant pipe 6 and the gas refrigerant pipe 7 and moisture as impurities are discharged from the discharge end 36.
- the release here is performed until the control unit 71 determines that the pressure has decreased to atmospheric pressure based on the value of the pressure sensor P acquired by the pressure acquisition unit 76.
- the filling step S1 for example, when the total pressure of the refrigeration cycle is 10 atmospheric pressure, the partial pressure of water, which is an impurity, becomes 0.5 atm. The ratio of partial pressure to is decreasing.
- the inside of the refrigeration cycle is returned to the atmospheric pressure in the discharge of the filling object in the release step S3, for example, the partial pressure of water in the refrigeration cycle at the total pressure and the atmospheric pressure is reduced to about 0.05 atmosphere. In this way, the refrigeration cycle is cleaned.
- step S4 the concentration acquisition unit 77 acquires from the concentration sensor C the nitrogen concentration in the component released in the release step S3. Then, the control unit 71 of the control device 70 Determine whether the nitrogen concentration acquired by acquisition unit 77 is less than or equal to lOOppm, which is the residual nitrogen concentration within the target allowable range. Here, if it is not less than lOOppm, the process returns to step S1, and the cleaning process by filling the nitrogen gas and releasing the filling object is repeated. In this case, the counter 74 increments the count data and stores it in the memory 72 as “twice”, and the control unit 71 determines that the unit operation is the second time according to the count data stored in the memory 72. To show, “2 times” is displayed on the display 73.
- step S10 the control unit 71 resets the count data by the counter 74 and returns the count data in the memory 72 to zero.
- a component having moisture adsorptivity other than nitrogen may be used as a filling material for removing moisture.
- the refrigeration cycle may be washed.
- a cleaning method for the air conditioner 1 according to the modified example (B) of the present invention for example, moisture present as an impurity in the refrigeration cycle is changed from a liquid state to a gaseous state by heating to be released. It may be included so that water removal in the refrigeration cycle is effective.
- the carbon dioxide charged in the filling step S10 described above is set to a temperature higher than the boiling point of water corresponding to the pressure state of the charged carbon dioxide. Is filled into the refrigeration cycle. That is, in the filling step S 10, the force that pressurizes the inside of the refrigeration cycle to a pressure exceeding the atmospheric pressure, and accordingly, the boiling point of water also increases. For this reason, the above-described filling step S10 is completed, the boiling point of water corresponding to the refrigerant pressure in the refrigeration cycle in the standby step S20 is specified, and the refrigerant is heated and filled above the boiling point of water corresponding to this pressure state. . Therefore, the water present in the refrigeration cycle is more likely to exist in a gaseous state than in the liquid state, and can be sufficiently mixed with the carbon dioxide refrigerant that is filled!
- the release target in the release step S30 can contain a large amount of moisture other than nitrogen alone as an impurity.
- water that is composed solely of nitrogen can be effectively discharged to the outside from the utilization unit 5, the liquid refrigerant pipe 6, and the gas refrigerant pipe 7 of the refrigeration cycle.
- control device 70 is provided in the air conditioner 1 and has been described as an example.
- control device 70 may be configured to be provided for the carbon dioxide cylinder 30, for example.
- the same effect as that of the above-described embodiment can be obtained only by preparing the carbon dioxide cylinder 30 for performing pipe cleaning without providing such a control device in the air conditioner 1.
- the nitrogen concentration in the filling object to be released is measured repeatedly in step S40, and the filling step S10, the standby step S20, and the releasing step S30 are performed until the measured value satisfies the allowable range.
- the case of repeating was explained as an example.
- the present invention is not limited to this.
- the pressure value in the refrigeration cycle set as the pressure filling in the filling step S10 without performing processing such as measurement of the concentration of the filling target is set.
- the control unit 71 may determine the number of times to repeat the unit operations of the filling step S10, the standby step S20, and the discharging step S30.
- the pressure in the refrigeration cycle in the filling process may be different each time.
- the filling process may be performed so that the pressure in the refrigeration cycle gradually increases each time the number of repetitions is repeated.
- control unit 71 may determine the pressure condition and temperature condition of the next filling step S 10 according to the impurity concentration to be filled detected by the concentration sensor C in each discharge step S30. Good. In this case, if the nitrogen concentration in the refrigeration cycle is high, the amount of carbon dioxide required for cleaning can be reduced. In addition, if the nitrogen concentration in the refrigeration cycle has been reduced by repeating the cleaning process, the discharge of nitrogen as an impurity can be more effectively performed by further increasing the pressure of carbon dioxide gas in the refrigeration cycle. Can be urged.
- the number of repetitions is fixed in advance by setting input, and the filling pressure in the filling step S10 is set so that the concentration of impurities can be equal to or less than the target concentration by only the number of repetitions set and input.
- the control unit 71 may determine the value and temperature.
- the multi-type air conditioner 1 in which a plurality of use units 5 are connected to one heat source unit 2 has been described as an example.
- the present invention is not limited thereto.
- the cleaning method of the above embodiment may be applied to a pair-type air conditioner in which one use unit 5 is connected to one heat source unit.
- the cleaning process when nitrogen is used as an impurity is described as an example.
- the present invention is not limited to this, and the impurity may be air containing nitrogen.
- the concentration of impurities present in the release target released in the release step S30 is detected by the concentration sensor C, and the target residual concentration is repeatedly determined in step S40.
- the case where the filling step S10, the waiting step S20 and the discharging step S30 are repeated until the condition is satisfied has been described as an example.
- the present invention is not limited to this.
- the number of repetitions of filling (charging) and discharging (venting) as shown in FIG. A database showing the relationship between the remaining amount of nitrogen in the refrigeration cycle may be stored.
- the control unit 71 refers to the table in FIG.
- the number of repetitions required in S40 may be automatically specified.
- the number of repetitions required to bring the impurity concentration below a predetermined target is inversely proportional to the value of the filling pressure in the filling step S10.
- the control unit 71 may automatically repeat the filling step S10, the waiting step S20, and the discharging step S30 a specified number of times.
- the present invention is not limited to this, and the refrigeration cycle is filled with carbon dioxide via the liquid side service port S6, and the filling object is discharged via the gas pipe side service port S7. May be.
- both filling and discharging may be performed only by the liquid pipe side service port S6, or both filling and discharging may be performed only by the gas pipe side service port S7. This also provides a cleaning effect as in the above embodiment.
- the present invention is used, the amount of impurities remaining in the refrigeration cycle can be reduced while using existing equipment that does not perform evacuation. It is useful as a method for cleaning an air conditioner using
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Description
Claims
Priority Applications (4)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP07791908.2A EP2056044A4 (en) | 2006-08-08 | 2007-08-03 | AIR CONDITIONING AND METHOD FOR CLEANING THEREOF |
CN200780029380XA CN101501422B (zh) | 2006-08-08 | 2007-08-03 | 空调装置及其清洗方法 |
AU2007282574A AU2007282574B2 (en) | 2006-08-08 | 2007-08-03 | Air conditioner and air conditioner cleaning method |
US12/376,172 US8230691B2 (en) | 2006-08-08 | 2007-08-03 | Air conditioner and air conditioner cleaning method |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JP2006215238A JP4187020B2 (ja) | 2006-08-08 | 2006-08-08 | 空気調和装置およびその洗浄方法 |
JP2006-215238 | 2006-08-08 |
Publications (1)
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WO2008018373A1 true WO2008018373A1 (fr) | 2008-02-14 |
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PCT/JP2007/065234 WO2008018373A1 (fr) | 2006-08-08 | 2007-08-03 | Climatiseur et procédé pour le nettoyer |
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US (1) | US8230691B2 (ja) |
EP (1) | EP2056044A4 (ja) |
JP (1) | JP4187020B2 (ja) |
KR (1) | KR20090041406A (ja) |
CN (2) | CN101881532B (ja) |
AU (1) | AU2007282574B2 (ja) |
WO (1) | WO2008018373A1 (ja) |
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WO2010109221A3 (en) * | 2009-03-23 | 2010-12-23 | Joseph George Poole | Compressed-gas regulator apparatus |
JP2021011960A (ja) * | 2019-07-04 | 2021-02-04 | 三星電子株式会社Samsung Electronics Co.,Ltd. | 冷媒充填装置 |
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BRPI0903956A2 (pt) * | 2009-01-09 | 2010-11-23 | Aurelio Mayorca | processo e equipamento para melhorar eficiência de compressores e refrigeradores |
JP2011085360A (ja) * | 2009-10-19 | 2011-04-28 | Panasonic Corp | 空気調和機及び空気調和機の設置方法 |
GB2477997B (en) * | 2010-02-23 | 2015-01-14 | Artemis Intelligent Power Ltd | Fluid working machine and method for operating fluid working machine |
JP5573296B2 (ja) * | 2010-03-31 | 2014-08-20 | ダイキン工業株式会社 | 空気調和装置 |
WO2011141959A1 (ja) * | 2010-05-12 | 2011-11-17 | 三菱電機株式会社 | 切換装置及び空気調和装置 |
US8701432B1 (en) * | 2011-03-21 | 2014-04-22 | Gaylord Olson | System and method of operation and control for a multi-source heat pump |
US9773014B2 (en) | 2014-06-03 | 2017-09-26 | Samsung Electronics Co., Ltd. | Heterogeneous distributed file system using different types of storage mediums |
CN107250785B (zh) * | 2015-02-02 | 2020-06-05 | 开利公司 | 制冷剂分析仪及其使用方法 |
CN106839487B (zh) * | 2017-03-16 | 2019-02-22 | 华北电力大学(保定) | 一种带反冲洗功能的跨临界二氧化碳空气源热泵系统 |
JP2020071002A (ja) * | 2018-11-01 | 2020-05-07 | 株式会社長府製作所 | ヒートポンプ装置 |
WO2024080213A1 (ja) * | 2022-10-11 | 2024-04-18 | 株式会社島津製作所 | 熱輸送装置への冷媒の充填方法および熱輸送装置用の冷媒充填制御装置 |
CN116202250A (zh) * | 2023-03-14 | 2023-06-02 | 中国船舶集团有限公司第七一一研究所 | 气体传热系统及气体充注方法 |
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2006
- 2006-08-08 JP JP2006215238A patent/JP4187020B2/ja not_active Expired - Fee Related
-
2007
- 2007-08-03 KR KR1020097003435A patent/KR20090041406A/ko not_active Application Discontinuation
- 2007-08-03 EP EP07791908.2A patent/EP2056044A4/en not_active Withdrawn
- 2007-08-03 CN CN2010102227399A patent/CN101881532B/zh not_active Expired - Fee Related
- 2007-08-03 US US12/376,172 patent/US8230691B2/en not_active Expired - Fee Related
- 2007-08-03 AU AU2007282574A patent/AU2007282574B2/en not_active Ceased
- 2007-08-03 WO PCT/JP2007/065234 patent/WO2008018373A1/ja active Application Filing
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JPH04198676A (ja) * | 1990-11-29 | 1992-07-20 | Yoshinori Satomura | 冷媒システム洗浄装置 |
JPH0783545A (ja) * | 1993-09-17 | 1995-03-28 | Hitachi Ltd | 空気調和機の冷媒変更方法 |
JP2001041613A (ja) * | 1999-08-03 | 2001-02-16 | Mitsubishi Electric Corp | 冷凍サイクル装置 |
JP2001165535A (ja) * | 1999-12-07 | 2001-06-22 | Matsushita Electric Ind Co Ltd | 空気調和機の製造方法 |
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JP2004270974A (ja) * | 2003-03-06 | 2004-09-30 | Mitsubishi Electric Corp | 冷凍冷蔵装置用冷媒回路の冷媒変更方法 |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2010109221A3 (en) * | 2009-03-23 | 2010-12-23 | Joseph George Poole | Compressed-gas regulator apparatus |
JP2021011960A (ja) * | 2019-07-04 | 2021-02-04 | 三星電子株式会社Samsung Electronics Co.,Ltd. | 冷媒充填装置 |
Also Published As
Publication number | Publication date |
---|---|
JP2008039308A (ja) | 2008-02-21 |
CN101881532A (zh) | 2010-11-10 |
US20090320502A1 (en) | 2009-12-31 |
AU2007282574B2 (en) | 2010-10-07 |
AU2007282574A1 (en) | 2008-02-14 |
CN101501422B (zh) | 2011-01-19 |
CN101501422A (zh) | 2009-08-05 |
KR20090041406A (ko) | 2009-04-28 |
EP2056044A1 (en) | 2009-05-06 |
CN101881532B (zh) | 2012-06-13 |
EP2056044A4 (en) | 2014-04-23 |
JP4187020B2 (ja) | 2008-11-26 |
US8230691B2 (en) | 2012-07-31 |
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