EP2063201A2 - Procédé de fonctionnement d'un système frigorifique - Google Patents
Procédé de fonctionnement d'un système frigorifique Download PDFInfo
- Publication number
- EP2063201A2 EP2063201A2 EP09003503A EP09003503A EP2063201A2 EP 2063201 A2 EP2063201 A2 EP 2063201A2 EP 09003503 A EP09003503 A EP 09003503A EP 09003503 A EP09003503 A EP 09003503A EP 2063201 A2 EP2063201 A2 EP 2063201A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- measures
- operating
- refrigeration system
- temperature
- refrigerant
- 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 50
- 238000000034 method Methods 0.000 title claims abstract description 37
- 239000007788 liquid Substances 0.000 claims abstract description 62
- 238000002347 injection Methods 0.000 claims abstract description 49
- 239000007924 injection Substances 0.000 claims abstract description 49
- 238000001704 evaporation Methods 0.000 claims abstract description 25
- 230000008020 evaporation Effects 0.000 claims abstract description 25
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 24
- 239000003507 refrigerant Substances 0.000 claims description 88
- 230000008569 process Effects 0.000 claims description 13
- 230000001105 regulatory effect Effects 0.000 claims description 11
- 238000012423 maintenance Methods 0.000 claims description 9
- 238000003860 storage Methods 0.000 claims description 6
- 238000001816 cooling Methods 0.000 claims description 5
- 239000000203 mixture Substances 0.000 claims description 3
- 230000000087 stabilizing effect Effects 0.000 claims description 3
- 238000009833 condensation Methods 0.000 claims description 2
- 230000005494 condensation Effects 0.000 claims description 2
- 238000001514 detection method Methods 0.000 claims description 2
- 239000002826 coolant Substances 0.000 abstract 1
- 238000013021 overheating Methods 0.000 description 6
- 239000000243 solution Substances 0.000 description 6
- 230000001276 controlling effect Effects 0.000 description 4
- 230000002776 aggregation Effects 0.000 description 2
- 238000004220 aggregation Methods 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 238000005259 measurement Methods 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- 238000009530 blood pressure measurement Methods 0.000 description 1
- 238000009529 body temperature measurement Methods 0.000 description 1
- 239000012267 brine Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000005461 lubrication Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- HPALAKNZSZLMCH-UHFFFAOYSA-M sodium;chloride;hydrate Chemical compound O.[Na+].[Cl-] HPALAKNZSZLMCH-UHFFFAOYSA-M 0.000 description 1
- 238000004781 supercooling Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 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
- F25B5/00—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
-
- 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
- F25B5/00—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity
- F25B5/04—Compression machines, plants or systems, with several evaporator circuits, e.g. for varying refrigerating capacity arranged in series
-
- 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
- F25B2600/00—Control issues
- F25B2600/25—Control of valves
- F25B2600/2513—Expansion valves
-
- 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
- F25B2700/2103—Temperatures near a heat exchanger
-
- 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
- F25B2700/2115—Temperatures of a compressor or the drive means therefor
- F25B2700/21151—Temperatures of a compressor or the drive means therefor at the suction side of the compressor
Definitions
- the dry expansion operation in which the refrigerant undergoes a pressure reduction via an injection valve and the liquid state in a liquid / vapor mixture to completely evaporate in the evaporator, and then leave the evaporator with slightly superheated steam and so on Heat absorption a second medium cools down and secondly, the Thermosyphon ses in which the refrigerant is supplied via a balancing and separation vessel to the evaporator either by gravity or by means of a pump liquid and where at the evaporator outlet may still contain liquid fractions in the steam and so in the Usually there is no overheating of the refrigerant at the evaporator outlet.
- Dry expansion systems have the advantage of simple design and small refrigerant contents.
- the evaporator efficiency is essentially influenced by the smallest possible overheating of the evaporator.
- Our innovation relates first to the dry expansion system (6) (1), to the dry expansion system (6) (1) with downstream IWT (2) (internal heat exchanger, ie with a heat exchange between the refrigerant liquid line before the expansion valve on the one hand and the suction steam after the evaporator on the other hand), to the two-stage evaporation system (6) (1 + 2) (a combination of dry expansion system and thermosyphon system, evaporator with IWT) and other refrigerators constructed on this basis.
- IWT internal heat exchanger, ie with a heat exchange between the refrigerant liquid line before the expansion valve on the one hand and the suction steam after the evaporator on the other hand
- x value is the value which indicates the proportion of the already vaporized refrigerant at the beginning of the evaporation process) of the refrigerant state in the injection valve (6 ) and in the evaporator start (1), which has an impact on the injection valve (6) and evaporator performance (1) and the control behavior of the injection valve (6) and its performance, respectively, the delivered refrigerant mass flow and on the other hand the suction steam at the inlet to the compressor (5 ), where the changed temperature (B), because of the specific temperature associated with the respective temperature (and pressure), has an influence on the delivery volume of the compressor (5), ie in turn on the delivered mass flow.
- this temperature difference can be smaller than when the refrigerant leaves the evaporator (1) "overheated" (P8 / T22) during dry expansion operation.
- This constant can be achieved by various measures. For the sake of simplicity, we describe the constant maintenance by means of a heat exchanger (4) in the refrigerant liquid line in front of the injection valve, which keeps the outlet temperature of the liquid refrigerant constant by means of a second medium.
- the medium used for keeping the refrigerant liquid temperature constant can be arbitrary in nature (gaseous, liquid, etc.).
- One way of keeping constant the refrigerant liquid temperature before the injection valve (A) may be that the flow (D) of the medium to be cooled, for example water, brine, etc., is passed through a heat exchanger (4), in which on the second side the heat exchanger, the refrigerant is conducted either in cocurrent, cross or countercurrent, etc.
- the refrigerant liquid temperature upstream of the injection valve (A) can also be regulated by the IWT (2) by means of mass flow control of the refrigerant liquid (9) by the IWT (2) (depending on the conditions, in some cases only partial mass flows flow through the IWT (2)).
- New in the invention is that the refrigerant liquid temperature, especially in the two-stage evaporation process (1 + 2) in front of the injection valve (6) (A) at a very low value, near or on the left limit curve of the log (p), h diagram for refrigerant, (The refrigerant thus occurs liquid as in a thermosyphone system or with a minimum vapor content in the evaporator (1)) is kept constant.
- Measures may be appropriate, as in the constant maintenance of the refrigerant liquid before the injection valve (6) (A).
- heat exchangers or storage or inertial masses are used for keeping the suction steam temperature constant.
- Suction-plate temperature maintenance may also be performed by means such as external sub-coolers (3) which control the refrigerant liquid inlet temperature to the IWT (2) (8) and in this way control the suction vapor exit temperature from the IWT (2) (B).
- the Saugdampftemperaturkonstantaria can also be regulated by means of mass flow control of the refrigerant liquid (9) by the IWT (2) or the suction steam (12) by the IWT (2).
- Suction temperature maintenance can also be achieved by more or less "flooding" the IWT (2) (only in the two-stage evaporation process).
- the "flooding" of the IWT (2) can by means of a temperature control of the suction steam at the inlet of the compressor (two-stage evaporator control) (T23), level control (7) directly through the evaporator (1), IWT (2) individually or together or a reference variable For example, the collector or other or a pressure difference control (7) directly via the evaporator (1), IWT (2) individually or together.
- the invention is based on the fact that the refrigerant liquid temperature upstream of the injection valve (A) and the suction steam temperature upstream of the compressor (B) are at an arbitrary value by suitable measures (within the physically possible, however, as far as possible reaching the physical limits) is held.
- valves, heat exchangers, etc. can be used individually or in any possible combination. Further representations will be omitted and refer to the text!
- the invention is based on the fact that by means of suitable measures a stable operation of cooling systems is achieved with small temperature differences of the media to be cooled and thus higher efficiencies (and thereby highly efficient evaporation in refrigeration systems).
- the process of refrigeration is supplemented or changed to the effect that in addition to the controlled suction and high pressures in refrigeration systems, the temperature of the liquid refrigerant before the injector (A) and the suction steam in front of the compressor inlet (B) is controlled, controlled and kept constant.
- Controlling the refrigerant temperature upstream of the injection valve (A) results in defined states in the refrigerant mixture (liquid / vapor). These defined conditions in the refrigerant lead to stable conditions in the refrigeration cycle.
- the innovation is to control the two described refrigerant conditions (A + B), no matter which method this is used with, depending on the application, only one or the other measure (A or B or 7) must be taken. It is thus possible, only with the temperature control of the liquid refrigerant before the injection valve (A) or the temperature control of the suction steam before the compressor (B) or with the control of the liquid refrigerant before the injection valve and the temperature control of the suction steam (A + B) desired result to come.
- the temperature in front of the injection valve is kept constant by means of suitable measures (as described above).
- This temperature constant maintenance of the liquid refrigerant upstream of the injection valve can be done, for example, with a built-in between the liquid line and the medium flow heat exchanger (4).
- the medium can be passed through the exchanger at a regulated or uncontrolled temperature.
- the proportion of already evaporated refrigerant in the evaporator can be optimized and adjusted with a corresponding temperature of the liquid refrigerant upstream of the injection valve (A) to the Verdampferbauart (1) and thus the efficiency for starting the evaporation process.
- the refrigerant liquid inlet temperature in the second evaporator stage (IWT) (2) (F), for example by means of an external Subcooler (3) are limited at high condensation temperatures.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- General Engineering & Computer Science (AREA)
- Devices That Are Associated With Refrigeration Equipment (AREA)
- Air Conditioning Control Device (AREA)
- Compression-Type Refrigeration Machines With Reversible Cycles (AREA)
- Greenhouses (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
EP04705750A EP1709372B1 (fr) | 2004-01-28 | 2004-01-28 | Evaporation a haut rendement dans des dispositifs frigorifiques et procede correspondant d'obtention de conditions stables avec des differences de temperature minimales et/ou requises des produits a refroidir par rapport a la temperature d'evaporation |
PCT/CH2004/000046 WO2005073645A1 (fr) | 2004-01-28 | 2004-01-28 | Evaporation a haut rendement dans des dispositifs frigorifiques et procede correspondant d'obtention de conditions stables avec des differences de temperature minimales et/ou requises des produits a refroidir par rapport a la temperature d'evaporation |
Related Parent Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04705750.0 Division | 2004-01-28 | ||
EP04705750A Division EP1709372B1 (fr) | 2004-01-28 | 2004-01-28 | Evaporation a haut rendement dans des dispositifs frigorifiques et procede correspondant d'obtention de conditions stables avec des differences de temperature minimales et/ou requises des produits a refroidir par rapport a la temperature d'evaporation |
Publications (3)
Publication Number | Publication Date |
---|---|
EP2063201A2 true EP2063201A2 (fr) | 2009-05-27 |
EP2063201A3 EP2063201A3 (fr) | 2009-10-14 |
EP2063201B1 EP2063201B1 (fr) | 2013-02-27 |
Family
ID=34812843
Family Applications (2)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP09003503A Expired - Lifetime EP2063201B1 (fr) | 2004-01-28 | 2004-01-28 | Procédé de fonctionnement d'un système frigorifique |
EP04705750A Expired - Lifetime EP1709372B1 (fr) | 2004-01-28 | 2004-01-28 | Evaporation a haut rendement dans des dispositifs frigorifiques et procede correspondant d'obtention de conditions stables avec des differences de temperature minimales et/ou requises des produits a refroidir par rapport a la temperature d'evaporation |
Family Applications After (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP04705750A Expired - Lifetime EP1709372B1 (fr) | 2004-01-28 | 2004-01-28 | Evaporation a haut rendement dans des dispositifs frigorifiques et procede correspondant d'obtention de conditions stables avec des differences de temperature minimales et/ou requises des produits a refroidir par rapport a la temperature d'evaporation |
Country Status (6)
Country | Link |
---|---|
US (1) | US9010136B2 (fr) |
EP (2) | EP2063201B1 (fr) |
AT (1) | ATE426785T1 (fr) |
DE (1) | DE502004009247D1 (fr) |
ES (2) | ES2401946T3 (fr) |
WO (1) | WO2005073645A1 (fr) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US9010136B2 (en) | 2004-01-28 | 2015-04-21 | Bms-Energietechnik Ag | Method of obtaining stable conditions for the evaporation temperature of a media to be cooled through evaporation in a refrigerating installation |
DE202007017723U1 (de) * | 2007-11-21 | 2008-03-20 | Meister, Remo | Anlage für die Kälte-, Heiz- oder Klimatechnik, insbesondere Kälteanlage |
DE102008043823B4 (de) * | 2008-11-18 | 2011-05-12 | WESKA Kälteanlagen GmbH | Wärmepumpenanlage |
DE102012002593A1 (de) * | 2012-02-13 | 2013-08-14 | Eppendorf Ag | Zentrifuge mit Kompressorkühleinrichtung und Verfahren zur Steuerung einer Kompressorkühleinrichtung einer Zentrifuge |
Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3640086A (en) * | 1970-02-27 | 1972-02-08 | American Standard Inc | Refrigerant flow control employing plural valves |
DE2451361A1 (de) * | 1974-10-29 | 1976-05-06 | Jakob | Verfahren zum regeln einer kompressorkuehlanlage |
US4493193A (en) * | 1982-03-05 | 1985-01-15 | Rutherford C. Lake, Jr. | Reversible cycle heating and cooling system |
EP0325163A1 (fr) * | 1988-01-21 | 1989-07-26 | Linde Aktiengesellschaft | Procédé de fonctionnement d'une installation frigorifique et installation frigorifique pour la mise en oeuvre du procédé |
US5150584A (en) * | 1991-09-26 | 1992-09-29 | General Motors Corporation | Method and apparatus for detecting low refrigerant charge |
US5533352A (en) * | 1994-06-14 | 1996-07-09 | Copeland Corporation | Forced air heat exchanging system with variable fan speed control |
DE29800048U1 (de) * | 1998-01-03 | 1998-04-23 | Koenig Harald | Wärmepumpe mit Anordnung eines Wärmetauschers zur Leistungszahlverbesserung |
EP1043550A1 (fr) * | 1997-12-26 | 2000-10-11 | Zexel Corporation | Cycle de refrigeration |
US6164086A (en) * | 1996-08-14 | 2000-12-26 | Daikin Industries, Ltd. | Air conditioner |
US6293123B1 (en) * | 1999-07-30 | 2001-09-25 | Denso Corporation | Refrigeration cycle device |
US6330802B1 (en) * | 2000-02-22 | 2001-12-18 | Behr Climate Systems, Inc. | Refrigerant loss detection |
US6438978B1 (en) * | 1998-01-07 | 2002-08-27 | General Electric Company | Refrigeration system |
US6446450B1 (en) * | 1999-10-01 | 2002-09-10 | Firstenergy Facilities Services, Group, Llc | Refrigeration system with liquid temperature control |
WO2003051657A1 (fr) * | 2001-12-19 | 2003-06-26 | Sinvent As | Systeme de compression de la vapeur destine au chauffage et au refroidissement des vehicules |
WO2004053406A1 (fr) * | 2002-12-11 | 2004-06-24 | Bms-Energietechnik Ag | Systeme de commande de processus d'evaporation utilise dans la technique frigorifique |
Family Cites Families (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3952533A (en) * | 1974-09-03 | 1976-04-27 | Kysor Industrial Corporation | Multiple valve refrigeration system |
JP3598604B2 (ja) * | 1995-09-08 | 2004-12-08 | ダイキン工業株式会社 | 熱搬送装置 |
US5970732A (en) * | 1997-04-23 | 1999-10-26 | Menin; Boris | Beverage cooling system |
US5921092A (en) * | 1998-03-16 | 1999-07-13 | Hussmann Corporation | Fluid defrost system and method for secondary refrigeration systems |
FR2779994B1 (fr) * | 1998-06-23 | 2000-08-11 | Valeo Climatisation | Circuit de climatisation de vehicule muni d'un dispositif de predetente |
US6170270B1 (en) * | 1999-01-29 | 2001-01-09 | Delaware Capital Formation, Inc. | Refrigeration system using liquid-to-liquid heat transfer for warm liquid defrost |
US6216481B1 (en) * | 1999-09-15 | 2001-04-17 | Jordan Kantchev | Refrigeration system with heat reclaim and with floating condensing pressure |
NO318864B1 (no) * | 2002-12-23 | 2005-05-18 | Sinvent As | Forbedret varmepumpesystem |
US9010136B2 (en) | 2004-01-28 | 2015-04-21 | Bms-Energietechnik Ag | Method of obtaining stable conditions for the evaporation temperature of a media to be cooled through evaporation in a refrigerating installation |
-
2004
- 2004-01-28 US US10/587,741 patent/US9010136B2/en active Active
- 2004-01-28 AT AT04705750T patent/ATE426785T1/de active
- 2004-01-28 EP EP09003503A patent/EP2063201B1/fr not_active Expired - Lifetime
- 2004-01-28 DE DE502004009247T patent/DE502004009247D1/de not_active Expired - Lifetime
- 2004-01-28 ES ES09003503T patent/ES2401946T3/es not_active Expired - Lifetime
- 2004-01-28 EP EP04705750A patent/EP1709372B1/fr not_active Expired - Lifetime
- 2004-01-28 WO PCT/CH2004/000046 patent/WO2005073645A1/fr not_active Application Discontinuation
- 2004-01-28 ES ES04705750T patent/ES2322152T3/es not_active Expired - Lifetime
Patent Citations (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3640086A (en) * | 1970-02-27 | 1972-02-08 | American Standard Inc | Refrigerant flow control employing plural valves |
DE2451361A1 (de) * | 1974-10-29 | 1976-05-06 | Jakob | Verfahren zum regeln einer kompressorkuehlanlage |
US4493193A (en) * | 1982-03-05 | 1985-01-15 | Rutherford C. Lake, Jr. | Reversible cycle heating and cooling system |
EP0325163A1 (fr) * | 1988-01-21 | 1989-07-26 | Linde Aktiengesellschaft | Procédé de fonctionnement d'une installation frigorifique et installation frigorifique pour la mise en oeuvre du procédé |
US5150584A (en) * | 1991-09-26 | 1992-09-29 | General Motors Corporation | Method and apparatus for detecting low refrigerant charge |
US5533352A (en) * | 1994-06-14 | 1996-07-09 | Copeland Corporation | Forced air heat exchanging system with variable fan speed control |
US6164086A (en) * | 1996-08-14 | 2000-12-26 | Daikin Industries, Ltd. | Air conditioner |
EP1043550A1 (fr) * | 1997-12-26 | 2000-10-11 | Zexel Corporation | Cycle de refrigeration |
DE29800048U1 (de) * | 1998-01-03 | 1998-04-23 | Koenig Harald | Wärmepumpe mit Anordnung eines Wärmetauschers zur Leistungszahlverbesserung |
US6438978B1 (en) * | 1998-01-07 | 2002-08-27 | General Electric Company | Refrigeration system |
US6293123B1 (en) * | 1999-07-30 | 2001-09-25 | Denso Corporation | Refrigeration cycle device |
US6446450B1 (en) * | 1999-10-01 | 2002-09-10 | Firstenergy Facilities Services, Group, Llc | Refrigeration system with liquid temperature control |
US6330802B1 (en) * | 2000-02-22 | 2001-12-18 | Behr Climate Systems, Inc. | Refrigerant loss detection |
WO2003051657A1 (fr) * | 2001-12-19 | 2003-06-26 | Sinvent As | Systeme de compression de la vapeur destine au chauffage et au refroidissement des vehicules |
WO2004053406A1 (fr) * | 2002-12-11 | 2004-06-24 | Bms-Energietechnik Ag | Systeme de commande de processus d'evaporation utilise dans la technique frigorifique |
Also Published As
Publication number | Publication date |
---|---|
WO2005073645A1 (fr) | 2005-08-11 |
EP1709372A1 (fr) | 2006-10-11 |
US20070137229A1 (en) | 2007-06-21 |
ATE426785T1 (de) | 2009-04-15 |
DE502004009247D1 (de) | 2009-05-07 |
US9010136B2 (en) | 2015-04-21 |
ES2401946T3 (es) | 2013-04-25 |
ES2322152T3 (es) | 2009-06-17 |
EP1709372B1 (fr) | 2009-03-25 |
EP2063201A3 (fr) | 2009-10-14 |
EP2063201B1 (fr) | 2013-02-27 |
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