EP2309208A1 - Cycle de réfrigération - Google Patents
Cycle de réfrigération Download PDFInfo
- Publication number
- EP2309208A1 EP2309208A1 EP09750463A EP09750463A EP2309208A1 EP 2309208 A1 EP2309208 A1 EP 2309208A1 EP 09750463 A EP09750463 A EP 09750463A EP 09750463 A EP09750463 A EP 09750463A EP 2309208 A1 EP2309208 A1 EP 2309208A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- refrigerant
- refrigeration cycle
- heat exchanger
- internal heat
- refrigeration
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Granted
Links
- 238000005057 refrigeration Methods 0.000 title claims abstract description 86
- 239000003507 refrigerant Substances 0.000 claims abstract description 70
- 238000004088 simulation Methods 0.000 claims abstract description 6
- 238000002474 experimental method Methods 0.000 claims abstract description 5
- 238000001704 evaporation Methods 0.000 claims description 9
- 238000004378 air conditioning Methods 0.000 claims description 5
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 abstract description 8
- 238000010586 diagram Methods 0.000 description 11
- 230000005494 condensation Effects 0.000 description 8
- 238000009833 condensation Methods 0.000 description 8
- 238000004364 calculation method Methods 0.000 description 5
- 230000008020 evaporation Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 3
- 230000012447 hatching Effects 0.000 description 2
- 238000010792 warming Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
Images
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
- F25B40/00—Subcoolers, desuperheaters or superheaters
-
- 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
-
- 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
- F25B2400/12—Inflammable refrigerants
- F25B2400/121—Inflammable refrigerants using R1234
-
- 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
- F25B2400/18—Refrigerant conversion
Definitions
- the present invention relates to a refrigeration cycle, and specifically relates to a refrigeration cycle which can be operated in a high refrigeration ability when a new-type refrigerant is used.
- refrigeration cycle 1 has compressor 2 for compressing refrigerant, condenser 3 for condensing compressed refrigerant, expansion valve 4 as a pressure reduction and expansion means for reducing in pressure and expanding condensed refrigerant, evaporator 5 for evaporating pressure-reduced and expanded refrigerant and internal heat exchanger 6 for exchanging heat between refrigerant at the exit side of the condenser and refrigerant at the exit side of the evaporator, where the refrigerant is circulated in the arrow direction as changing in state in refrigerant cycle 1.
- internal heat exchanger 6 provided in refrigeration cycle 1 can generally improve its refrigeration ability.
- internal heat exchanger 6 has not been used actually because the advantage thereby is relatively low when using typical refrigerant R134a.
- R134a can be quoted as a typical refrigerant at present, and new type refrigerants have been researched and developed aiming further improvement of global warming potential (GWP), etc., as disclosed in Non-patent document 1.
- GWP global warming potential
- R1234yf has been announced recently as a new refrigerant aiming at such an improvement, and it is becoming possible that it is examined and studied for applying to refrigeration cycle as used for an automotive air conditioning system.
- Non-patent document 1 Refrigeration, Vol. 83, No. 965, March issue, 2008
- an object of the present invention is to provide a refrigeration cycle, which can be operated in a high refrigeration ability greater than or equal to a refrigeration cycle using the conventional refrigerant R134a even when refrigerant is changed to the new-type refrigerant R1234yf.
- a refrigeration cycle according to the present invention is a refrigeration cycle comprising a compressor for compressing refrigerant, a condenser for condensing compressed refrigerant, a pressure reduction and expansion means for reducing in pressure and expanding condensed refrigerant, an evaporator for evaporating pressure-reduced and expanded refrigerant, and an internal heat exchanger for exchanging heat between refrigerant at an exit side of the condenser and refrigerant at an exit side of the evaporator, characterized in that R1234yf is used as refrigerant for the refrigeration cycle, and an amount of heat exchange by the internal heat exchanger is greater than or equal to a specific value that has been determined beforehand by a simulation or an experiment.
- Fig. 2 shows how the refrigeration ability can be improved by using the internal heat exchanger when the new-type refrigerant R1234yf is used in the refrigeration cycle having the same basic configuration as shown in Fig. 1 , in comparison between one case where the conventional refrigerant R134a is used without using an internal heat exchanger and the other case where the new-type refrigerant R1234yf is used as using an internal heat exchanger, under the same calculational condition such as condensation temperature, evaporation temperature, superheating degree and subcooling degree.
- the horizontal axis of Fig. 2 shows quantity of heat exchange by the internal heat exchanger (the ability of the internal heat exchanger), and the vertical axis thereof shows the refrigeration ability as a whole refrigeration cycle.
- the refrigeration ability changes as shown in Fig. 2 by providing the internal heat exchanger.
- the quantity of heat exchange by internal heat exchanger is shown as constant because the internal heat exchanger is not used. In other words, if the quantity of heat exchange by the internal heat exchanger is greater than or equal to a specific value, such as 0.7kW in the comparative characteristic diagram shown in Fig. 2 , the improvement of refrigeration ability by providing the internal heat exchanger can be achieved surely in a case where the new-type refrigerant R1234yf is used.
- the refrigeration ability with R1234yf is less than that with R134a, which means that the advantage of providing the internal heat exchanger as seen in the R134a case cannot be obtained. Therefore, it can be found that only if the quantity of heat exchange by the internal heat exchanger is set greater than or equal to a specific value, or a predetermined value, the case with R1234yf can achieve refrigeration ability greater than or equal to the case with R134a, so as to actually improve the refrigeration ability.
- the present invention is based on this technical idea and characterized in that , when R1234yf is used as refrigerant for the refrigeration cycle an amount of heat exchange by the internal heat exchanger is greater than or equal to a specific value that has been determined beforehand by a simulation or an experiment. Namely, used is the region identified by hatching, which is the right side region of the point of intersection with a characteristic line in the R134a case and another characteristic line in the R1234yf case, in Fig. 2 .
- the specific value of the amount of heat exchange by the internal heat exchanger is set so that a total refrigeration ability of the refrigeration cycle using R1234yf as refrigerant is greater than or equal to a total refrigeration ability of a refrigeration cycle using R134a as refrigerant under the same conditions.
- the size or thermal efficiency of the internal heat exchanger can be set arbitrarily if specification of the evaporator or the condenser used in each refrigeration cycle is preliminarily known.
- a refrigeration cycle which is configured based on this concept, because the approximate ability of the internal heat exchanger is known, refrigeration ability as a whole refrigeration cycle can be obtained stably, where the refrigeration ability is kept greater than or equal to the refrigeration ability in the R134a case by properly controlling the opening degree of the decompression-expansion means according to the superheating degree of refrigerant at the outlet side connecting to the compressor side of the internal heat exchanger.
- Such a refrigeration cycle according to the present invention is basically applicable to any refrigeration cycle which aims to use the new-type refrigerant R1234yf, and is specifically suitable to a refrigeration cycle used in an automotive air conditioning system which is required to achieve efficient operation for a long term.
- the refrigeration cycle according to the present invention makes it possible that when the refrigerant is replaced to the new-type refrigerant R1234yf, the improvement of coefficient of performance (COP) can be greatly achieved, and superior characteristics, such as improvement of the global warming potential (GWP), etc., which the new-type refrigerant R1234yf has in itself can be performed.
- COP coefficient of performance
- GWP global warming potential
- FIG. 1 A basic configuration of equipments of a refrigeration cycle according to the present invention can be the same one as shown in Fig. 1 .
- refrigeration cycle 1 has compressor 2 for compressing refrigerant, condenser 3 for condensing compressed refrigerant, expansion valve 4 as a pressure reduction and expansion means for reducing in pressure and expanding condensed refrigerant, evaporator 5 for evaporating pressure-reduced and expanded refrigerant and internal heat exchanger 6 for exchanging heat between refrigerant at the exit side of the condenser and refrigerant at the exit side of the evaporator, where the refrigerant is circulated in the arrow direction as changing in state in refrigerant cycle 1, as described above.
- the present invention basically uses the region identified by hatching, which is the right side region of the point of intersection with a characteristic line in the R134a case and another characteristic line in the R1234yf case, in Fig. 2 , as described above.
- an internal heat exchanger is provided as using the new-type refrigerant R1234yf, so that the refrigeration ability can be improved from the conventional case using refrigerant R134a.
- ability rate of internal heat exchanger which means an improvement effect of an ability by an internal heat exchanger to a refrigeration ability as a whole refrigeration cycle, will change when the condition of the amount of heat exchange by the internal heat exchanger at the point of intersection with a characteristic line in the R134a case and another characteristic line in the R1234yf case in Fig. 2 is changed to another condition thereof, such as different condensation temperature of the refrigerant.
- Characteristic B in Fig. 3 shows a relation of "ABILITY RATE OF INTERNAL HEAT EXCHANGER TO REFRIGERATION ABILITY" as a whole refrigeration cycle to "CONDENSATION TEMPERATURE" if the efficiency of the internal heat exchanger is assumed to be 100%.
- the intersectional point of the characteristic lines A and B in the calculation result shown in Fig. 3 is positioned at where the ability rate of the internal heat exchanger to refrigeration ability is 6.6%, if the ability rate is no less than 7% the refrigeration ability is to be surely improved by providing the internal heat exchanger, according to the relational characteristics shown in Fig. 3 .
- the upper limit value of the ability rate is not specifically limited, and the refrigeration ability has been confirmed to be improved, even in a condition around 30%, according to the calculation result shown in Fig. 3 .
- the refrigeration ability per unit volume can be kept no less than the level with the conventional refrigerant R134a by increasing the amount of heat exchange of the internal heat exchanger as shown in the region surrounded by a bold border in Table 1. Therefore, the compressor does not have to be operated rapidly any more.
- the density of compressor suction refrigerant becomes low the circulating volume of refrigerant decreases, and a pressure loss can be reduced.
- the compressor suction side refrigerant superheating degree becomes greater and the compressor discharge temperature becomes higher than R134a, so that the efficiency can be improved.
- the coefficient of performance (COP) can be kept no less than the same level with R134a because the increase of the compressor power (consumption power) is comparatively small.
- Fig. 4 - Fig. 6 show an example of comparative result between R1234yf and R134a on the Mollier diagram.
- Fig. 4 - Fig. 6 show respective cases which have varied thermal efficiencies of the internal heat exchanger in the R1234yf case.
- the conditions in each Fig. are as follows.
- the refrigeration cycle according to the present invention is applicable for every refrigeration cycle where the new-type refrigerant R1234yf will be used, and specifically suitable as a refrigeration cycle used for an automotive air conditioning system.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Air-Conditioning For Vehicles (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2008131981A JP5180680B2 (ja) | 2008-05-20 | 2008-05-20 | 冷凍サイクル |
PCT/JP2009/058336 WO2009142101A1 (fr) | 2008-05-20 | 2009-04-28 | Cycle de réfrigération |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2309208A1 true EP2309208A1 (fr) | 2011-04-13 |
EP2309208A4 EP2309208A4 (fr) | 2011-07-06 |
EP2309208B1 EP2309208B1 (fr) | 2014-04-16 |
Family
ID=41340033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09750463.3A Active EP2309208B1 (fr) | 2008-05-20 | 2009-04-28 | Cycle de réfrigération |
Country Status (5)
Country | Link |
---|---|
US (1) | US20110067435A1 (fr) |
EP (1) | EP2309208B1 (fr) |
JP (1) | JP5180680B2 (fr) |
CN (1) | CN102037292A (fr) |
WO (1) | WO2009142101A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4170262A1 (fr) * | 2021-10-20 | 2023-04-26 | Thermo King Corporation | Pompe à chaleur, procédés de fonctionnement et de simulation |
Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2010032157A (ja) * | 2008-07-30 | 2010-02-12 | Denso Corp | 冷凍サイクル装置 |
JP2011179689A (ja) * | 2010-02-26 | 2011-09-15 | Hitachi Appliances Inc | 冷凍サイクル装置 |
JP2011247482A (ja) * | 2010-05-27 | 2011-12-08 | Panasonic Corp | 冷凍装置および冷暖房装置 |
DE102010033518A1 (de) * | 2010-08-05 | 2012-02-09 | Gm Global Technology Operations Llc (N.D.Ges.D. Staates Delaware) | Klimaanlage und Verfahren zum Betreiben einer Klimaanlage |
WO2012101672A1 (fr) * | 2011-01-26 | 2012-08-02 | 三菱電機株式会社 | Dispositif de conditionnement d'air |
JP5792585B2 (ja) * | 2011-10-18 | 2015-10-14 | サンデンホールディングス株式会社 | 冷凍機、冷蔵ショーケース及び自動販売機 |
JP6911527B2 (ja) * | 2017-05-23 | 2021-07-28 | 株式会社デンソー | 冷凍サイクル装置 |
JP7473198B2 (ja) | 2020-10-16 | 2024-04-23 | 京都電子工業株式会社 | 振動式密度計、及び振動式密度計における気泡混入判定方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050233934A1 (en) * | 2004-04-16 | 2005-10-20 | Honeywell International, Inc. | Azeotrope-like compositions of tetrafluoropropene and trifluoroiodomethane |
EP1632733A2 (fr) * | 2004-09-07 | 2006-03-08 | Matsushita Electric Industrial Co., Ltd. | Appareil à cycle de réfrigération et procédé de régulation |
EP1862749A2 (fr) * | 2006-05-30 | 2007-12-05 | Sanden Corporation | Cycle frigorifique à compression de vapeur |
FR2905633A1 (fr) * | 2006-09-08 | 2008-03-14 | Valeo Systemes Thermiques | Boucle de climatisation d'un vehicule automobile dont le fluide refrigerant est a base de 1,1,1,2-tetrafluoroproprene et de trifluoroiodomethane |
Family Cites Families (13)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5392612A (en) * | 1984-08-08 | 1995-02-28 | Richard H. Alsenz | Refrigeration system having a self adjusting control range |
JPH0754207B2 (ja) * | 1986-11-25 | 1995-06-07 | 日本電装株式会社 | 冷凍サイクル装置 |
US4948525A (en) * | 1988-04-06 | 1990-08-14 | Nippon Oil Co., Ltd. | Lubricating oil compositions for refrigerators |
JP2000179960A (ja) * | 1998-12-18 | 2000-06-30 | Sanden Corp | 蒸気圧縮式冷凍サイクル |
US7076964B2 (en) * | 2001-10-03 | 2006-07-18 | Denso Corporation | Super-critical refrigerant cycle system and water heater using the same |
US7279451B2 (en) * | 2002-10-25 | 2007-10-09 | Honeywell International Inc. | Compositions containing fluorine substituted olefins |
CN1732365A (zh) * | 2002-11-11 | 2006-02-08 | 沃特克斯·埃尔康公司 | 具有过冷旁路和部件体积全优化的制冷系统 |
JP2005337700A (ja) * | 2004-04-28 | 2005-12-08 | Fuji Electric Retail Systems Co Ltd | 冷媒冷却回路 |
JP2006071174A (ja) * | 2004-09-01 | 2006-03-16 | Daikin Ind Ltd | 冷凍装置 |
JP4626531B2 (ja) * | 2005-04-01 | 2011-02-09 | 株式会社デンソー | エジェクタ式冷凍サイクル |
JP4246189B2 (ja) * | 2005-09-07 | 2009-04-02 | 株式会社デンソー | 冷凍サイクル装置 |
JP2007155229A (ja) * | 2005-12-06 | 2007-06-21 | Sanden Corp | 蒸気圧縮式冷凍サイクル |
JP4826759B2 (ja) * | 2006-05-11 | 2011-11-30 | 三菱電機株式会社 | 圧縮機 |
-
2008
- 2008-05-20 JP JP2008131981A patent/JP5180680B2/ja not_active Expired - Fee Related
-
2009
- 2009-04-28 CN CN2009801189126A patent/CN102037292A/zh active Pending
- 2009-04-28 WO PCT/JP2009/058336 patent/WO2009142101A1/fr active Application Filing
- 2009-04-28 US US12/993,458 patent/US20110067435A1/en not_active Abandoned
- 2009-04-28 EP EP09750463.3A patent/EP2309208B1/fr active Active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20050233934A1 (en) * | 2004-04-16 | 2005-10-20 | Honeywell International, Inc. | Azeotrope-like compositions of tetrafluoropropene and trifluoroiodomethane |
EP1632733A2 (fr) * | 2004-09-07 | 2006-03-08 | Matsushita Electric Industrial Co., Ltd. | Appareil à cycle de réfrigération et procédé de régulation |
EP1862749A2 (fr) * | 2006-05-30 | 2007-12-05 | Sanden Corporation | Cycle frigorifique à compression de vapeur |
FR2905633A1 (fr) * | 2006-09-08 | 2008-03-14 | Valeo Systemes Thermiques | Boucle de climatisation d'un vehicule automobile dont le fluide refrigerant est a base de 1,1,1,2-tetrafluoroproprene et de trifluoroiodomethane |
Non-Patent Citations (1)
Title |
---|
See also references of WO2009142101A1 * |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP4170262A1 (fr) * | 2021-10-20 | 2023-04-26 | Thermo King Corporation | Pompe à chaleur, procédés de fonctionnement et de simulation |
EP4170263A1 (fr) * | 2021-10-20 | 2023-04-26 | Thermo King LLC | Pompe à chaleur, procédés de fonctionnement et de simulation |
US12123634B2 (en) | 2021-10-20 | 2024-10-22 | Thermo King Llc | Heat pump, methods of operation and simulation |
Also Published As
Publication number | Publication date |
---|---|
CN102037292A (zh) | 2011-04-27 |
EP2309208A4 (fr) | 2011-07-06 |
EP2309208B1 (fr) | 2014-04-16 |
WO2009142101A1 (fr) | 2009-11-26 |
JP5180680B2 (ja) | 2013-04-10 |
US20110067435A1 (en) | 2011-03-24 |
JP2009281610A (ja) | 2009-12-03 |
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