EP2156110A1 - Thermoelektrischer kühler zur leistungsverstärkung eines kältemittelkreislaufs mit economiser - Google Patents

Thermoelektrischer kühler zur leistungsverstärkung eines kältemittelkreislaufs mit economiser

Info

Publication number
EP2156110A1
EP2156110A1 EP07784476A EP07784476A EP2156110A1 EP 2156110 A1 EP2156110 A1 EP 2156110A1 EP 07784476 A EP07784476 A EP 07784476A EP 07784476 A EP07784476 A EP 07784476A EP 2156110 A1 EP2156110 A1 EP 2156110A1
Authority
EP
European Patent Office
Prior art keywords
economizer
refrigerant
set forth
thermoelectric cooler
heat exchanger
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.)
Withdrawn
Application number
EP07784476A
Other languages
English (en)
French (fr)
Inventor
Michael F. Taras
Alexander Lifson
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Carrier Corp
Original Assignee
Carrier Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Carrier Corp filed Critical Carrier Corp
Publication of EP2156110A1 publication Critical patent/EP2156110A1/de
Withdrawn legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B25/00Machines, plants or systems, using a combination of modes of operation covered by two or more of the groups F25B1/00 - F25B23/00
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B1/00Compression machines, plants or systems with non-reversible cycle
    • F25B1/10Compression machines, plants or systems with non-reversible cycle with multi-stage compression
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B21/00Machines, plants or systems, using electric or magnetic effects
    • F25B21/02Machines, plants or systems, using electric or magnetic effects using Peltier effect; using Nernst-Ettinghausen effect
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2309/00Gas cycle refrigeration machines
    • F25B2309/06Compression machines, plants or systems characterised by the refrigerant being carbon dioxide
    • F25B2309/061Compression machines, plants or systems characterised by the refrigerant being carbon dioxide with cycle highest pressure above the supercritical pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/13Economisers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25BREFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B2400/00General 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
    • F25B2400/23Separators

Definitions

  • thermoelectric cooler provides additional cooling and a performance boost to assist the conventional economizer circuit.
  • Refrigerant compressors circulate a refrigerant through a refrigerant system to condition a secondary fluid.
  • a compressor compresses a refrigerant and delivers it to a heat rejection heat exchanger.
  • Refrigerant from the heat rejection heat exchanger passes through an expansion device, in which its pressure and temperature are reduced. Downstream of the expansion device, the refrigerant passes through a heat accepting heat exchanger, and then back to the compressor.
  • the heat accepting heat exchanger is typically an evaporator.
  • the heat rejecting heat exchanger is a condenser, in subcritical applications, and a gas cooler, in transcritical applications.
  • a portion of refrigerant is tapped from a main refrigerant stream downstream of the heat rejection heat exchanger.
  • this tapped refrigerant is passed through an auxiliary expansion device, to be expanded to an intermediate pressure and temperature, and then this partially expanded tapped refrigerant passes in heat exchange relationship with a main refrigerant flow in an economizer heat exchanger. In this manner, the main refrigerant is cooled such that it will have a greater thermodynamic potential when it reaches the heat accepting heat exchanger.
  • thermoelectric cooler essentially takes advantage of specific thermoelectric properties of dissimilar semiconductor materials and is based on two phenomena - the Peltier effect and Seebeck effect concurrently taking place during operation of the thermoelectric device.
  • the Peltier effect is associated to the release or absorption of a finite heat flux at the junction of two electrical conductors, made from different materials and kept at constant temperature, at the presence of electric current.
  • the Seebeck effect is related to the same arrangement, where the two junctions are maintained at different temperatures, which would create a finite potential difference, and an electromotive force that would drive an electric current in the closed-loop electric circuit.
  • the Peltier and Seebeck effects are presented simultaneously in the thermoelectric cooler that is preferably made from the materials that have dissimilar absolute thermoelectric powers.
  • the finite electric current passing through the two junctions triggers two heat transfer interactions with two cold and hot reservoirs kept at different temperatures.
  • heat fluxes associated with the two junctions should have opposite signs. If the external system maintains potential difference and drives electric current against this difference, the two-junction system becomes a thermoelectric cooling device.
  • a typical thermoelectric cooler consists of an array of P-type and N-type semiconductor elements that act as the two dissimilar conductors.
  • the P-type material has an insufficient number of electrons and the N-type material has extra electrons.
  • These electrons in the N-type material and so-called "holes" in the P-type material in addition to carrying an electric current, become a transport media to move the heat from the cold junction to the hot junction.
  • the heat transport rate depends on the current passing through the circuit and the number of moving electron-hole couples. As an electric current is passed through one or more pairs of P-N elements, there is a decrease in temperature at the cold junction resulting in the absorption of heat from the object to be cooled.
  • thermoelectric cooler The heat is carried through the thermoelectric cooler by electron transport and released at the hot junction as the electrons move from a high to a low energy state.
  • thermoelectric devices are inherently irreversible, since heat and electric current must flow through the circuit during their operation, they do not have moving parts that makes them extremely reliable.
  • the refrigerant of the conventional vapor compression system is replaced by electrons carrying energy from a cold junction to a hot junction, created by two conductors with dissimilar absolute thermoelectric powers and connected electrically in series and thermally in parallel.
  • thermoelectric coolers has only been proposed to be positioned downstream of a heat rejection heat exchanger in a conventional refrigerant cycle. Such thermoelectric coolers have never been proposed for providing an additional performance boost to an economizer cycle.
  • Performance enhancement of economized refrigerant systems becomes especially crucial in a view of a limited capability of the economizer cycle in the air conditioning application range and continuously raising efficiency standards.
  • alternate refrigerants such as carbon dioxide operating in a transcritical regime, require extra means, in addition to the economizer function, to achieve the performance levels comparable to the performance levels of refrigerant systems charged with conventional refrigerants.
  • thermoelectric cooler is operable to provide an additional performance boost to the economized refrigerant system by providing extra cooling either to an economized refrigerant flow or directly to a main refrigerant flow or both.
  • a thermoelectric cooler can be positioned upstream or downstream of an economizer, in relation to a respective refrigerant flow.
  • the thermoelectric cooler allows for additional cooling of the main refrigerant flow and its temperature reduction upstream of the main expansion device. Therefore, the thermodynamic cooling potential of the refrigerant flow entering an evaporator and the overall performance of the refrigerant system are increased.
  • Figure IA shows a first schematic.
  • Figure IB shows a second schematic.
  • Figure 2A shows a third embodiment.
  • Figure 2B shows a fourth schematic.
  • Figure 3A shows a fifth schematic.
  • Figure 3 B shows a sixth schematic.
  • Figure 4A is a P-h diagram for Figures IA, IB, 2A and 2B.
  • Figure 4B is a P-h diagram for Figures 3 A and 3B.
  • FIG. IA An economized refrigerant system 20 is illustrated in Figure IA.
  • a compressor 22 compresses a refrigerant and delivers it downstream to a heat rejection heat exchanger 24.
  • the heat rejection heat exchanger 24 is a gas cooler for a transcritical cycle and a condenser for a subcritical cycle.
  • the refrigerant passes through an economizer heat exchanger 26.
  • a main refrigerant flow passes through the economizer heat exchanger 26, and a tap refrigerant line 30 taps a portion of the refrigerant from a main refrigerant line 28 downstream of the economizer heat exchanger.
  • the tap line 30 passes through an economizer expansion device 32, and then once again through the economizer heat exchanger 26.
  • the expansion device 32 the tapped refrigerant is expanded to an intermediate pressure and temperature, and therefore can cool the refrigerant in the main refrigerant line 28 during heat transfer interaction in the economizer heat exchanger 26.
  • the refrigerant from the tap refrigerant line 30 passes through an injection refrigerant line 34 back to an intermediate compression point at the compressor 22.
  • Refrigerant in the main refrigerant line 28 downstream of the economizer heat exchanger 26 passes through a main expansion device 40, and then through a heat accepting heat exchanger (evaporator) 42. From the heat accepting heat exchanger 42, the refrigerant passes back to the compressor 22.
  • the economized refrigerant system described above is generally known in the art.
  • the present invention enhances performance of this known economized refrigerant system by including a thermoelectric cooler 38 downstream of the economizer heat exchanger 26.
  • Thermoelectric cooler 38 provides further cooling to the refrigerant in the main refrigerant line 28 by providing a thermal contact between a cold junction of the thermoelectric cooler 38 and a refrigerant in the main refrigerant line 28.
  • thermoelectric cooler 38 also cools the refrigerant which is tapped into the tap refrigerant line 30, and thus provides even greater thermodynamic cooling potential for the tapped refrigerant and a higher heat transfer rate between the main refrigerant in the main refrigerant line 28 and tapped refrigerant in the tap refrigerant line 30, in the economizer heat exchanger 26.
  • the thermoelectric cooler 38 may be of any type or configuration known in the art. For instance, the hot junction of the thermoelectric cooler 38 may be cooled by an air stream. In embodiments, the components may be positioned such that a single air moving device moves air over both the gas cooler 24 and the thermoelectric cooler 38 to reject heat from both components. Alternatively, separate air moving devices can be utilized.
  • thermoelectric cooler 38 Obviously, other heat rejection means from the hot junction of the thermoelectric cooler 38 are also feasible.
  • the attachment of the cold junction of the thermoelectric cooler 38 to the main refrigerant line to provide sufficient thermal contact can be, for instance, by a mechanical contact, brazing, soldering, welding, gluing, or any other means.
  • the tap refrigerant line 30 for the economizer circuit can be positioned upstream of the thermoelectric cooler 38. Similar benefits can be achieved in this configuration as well.
  • Figure IB shows an embodiment 50, which is similar to the embodiment 20 depicted in Figure IA, other than in the location of the thermoelectric cooler 52.
  • the thermoelectric cooler 52 is positioned intermediate the economizer expansion device 32, and the economizer heat exchanger 26. In this case, the thermoelectric cooler can be made more compact, since it has to cool only a portion of refrigerant tapped into the tap refrigerant line 30.
  • thermoelectric cooler can also be positioned between the tap point 33 and the economizer expansion device 32.
  • FIG. 2A shows yet another embodiment 60.
  • a portion of refrigerant is tapped into the refrigerant line 30 upstream of the economizer heat exchanger 26, and passed through a thermoelectric cooler 62 prior to reaching the economizer expansion device 32.
  • refrigerant in the tap refrigerant line 30 will be colder, and thus will be able to cool the refrigerant in the main refrigerant line 28 to an even greater extent, in the economizer heat exchanger 26.
  • Figure 2B shows an embodiment 70 that is similar to the embodiment 60 of
  • thermoelectric cooler 72 downstream of the economizer expansion device 32.
  • FIG. 3A shows still another embodiment 80 where the economizer heat exchanger 26 of previous embodiments is replaced by a flash tank 44.
  • Economized systems with a flash tank are known in the art.
  • the flash tank separates liquid and vapor refrigerant phases, with the liquid phase flowing through the main circuit and the vapor phase delivered to an intermediate compression point in the compressor 22.
  • a thermoelectric cooler 46 is placed between the economizer expansion device 32 and the flash tank 44 to provide extra liquid content in the refrigerant mixture flowing into the flash tank 44 and an additional performance boost to the refrigerant system 80.
  • FIG 3B shows another embodiment 90, which is similar to the embodiment 80 of Figure 3A, with the exception that a thermoelectric cooler 48 is positioned between the flash tank 44 and the main expansion device 40. In this case, rather than increasing the liquid content in the two-phase mixture flowing into the flash tank 44, the thermoelectric cooler 48 further cools the liquid exiting the flash tank 44, thus enhancing performance of the refrigerant system 90.
  • thermoelectric cooler at the locations as shown in this application can be seen from the P-h diagrams of Figures 4 A and 4B.
  • the P-h diagram depicted in Figure 4A shows additional capacity provided by a thermoelectric cooler for the refrigerant systems having an economizer circuit containing an economizer heat exchanger, as shown in figures IA, IB, 2A and 2B.
  • Figure 4B shows benefits provided by a thermoelectric cooler for the refrigerant systems including a flash tank, as exhibited in Figure 3B.
  • thermoelectric coolers disclosed in this invention can be used in both conventional subcritical applications, as shown in Figure 4 A, and transcritical applications, as exhibited in Figure 4B. Since transcritical applications, such as those employing carbon dioxide as a refrigerant, are inherently less efficient, the thermoelectric cooler would be the most advantageous in those applications. Also, since the augmentation provided by an economizer cycle for air conditioning applications is limited by a reduced pressure ratio, the thermoelectric cooler integration would provide additional benefits for air conditioning applications, especially in a view of continuously raising efficiency standards and diminishing returns of standard performance enhancement methods.
  • thermoelectric cooler can provide additional flexibility in unloading economized refrigerant systems. Turning the thermoelectric device on will supply additional capacity to compensate for thermal load demand in the conditioned space. On the other hand, switching the thermoelectric device off will allow for unloading of the refrigerant system when only part-load capacity is required to meet the space demand.
  • compressors could be used in this invention.
  • scroll, screw, rotary, or reciprocating compressors can be employed.
  • the refrigerant systems that utilize this invention may have various options and enhancement features, such as, for instance, tandem components, reheat circuits, intercooler heat exchangers, etc., and can be used in many different applications, including, but not limited to, air conditioning systems, heat pump systems, marine container units, refrigeration truck-trailer units, and supermarket refrigeration systems.

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  • 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)
EP07784476A 2007-06-19 2007-06-19 Thermoelektrischer kühler zur leistungsverstärkung eines kältemittelkreislaufs mit economiser Withdrawn EP2156110A1 (de)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
PCT/US2007/071537 WO2008156482A1 (en) 2007-06-19 2007-06-19 Thermoelectric cooler for economized refrigerant cycle performance boost

Publications (1)

Publication Number Publication Date
EP2156110A1 true EP2156110A1 (de) 2010-02-24

Family

ID=40156488

Family Applications (1)

Application Number Title Priority Date Filing Date
EP07784476A Withdrawn EP2156110A1 (de) 2007-06-19 2007-06-19 Thermoelektrischer kühler zur leistungsverstärkung eines kältemittelkreislaufs mit economiser

Country Status (5)

Country Link
US (1) US20100122540A1 (de)
EP (1) EP2156110A1 (de)
CN (1) CN101688706B (de)
HK (1) HK1142387A1 (de)
WO (1) WO2008156482A1 (de)

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Publication number Priority date Publication date Assignee Title
JP5636871B2 (ja) * 2010-03-01 2014-12-10 ダイキン工業株式会社 冷凍装置
US20120180512A1 (en) * 2011-01-13 2012-07-19 General Electric Company Water recovery system for a cooling tower
EP2799343B1 (de) 2013-04-03 2017-02-15 Airbus Operations GmbH Flugzeugklimaanlagensystem
DE102013211177A1 (de) * 2013-06-14 2014-12-18 Airbus Operations Gmbh Flugzeugkühlsystem und Verfahren zum Betreiben eines Flugzeugkühlsystems
US10054994B2 (en) 2015-04-04 2018-08-21 Indian Institute Of Technology Bombay Non-uniform intensity mapping using high performance enterprise computing system
US10605469B2 (en) * 2016-07-27 2020-03-31 Johnson Controls Technology Company System and method for capture of waste heat in an HVAC unit

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WO1998021531A1 (fr) * 1996-11-08 1998-05-22 Matsushita Refrigeration Company Systeme de refroidissement thermoelectrique
US6479445B1 (en) * 1997-05-23 2002-11-12 Huntsman Petrochemical Corporation Paint stripping compositions
US6351950B1 (en) * 1997-09-05 2002-03-05 Fisher & Paykel Limited Refrigeration system with variable sub-cooling
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US6374631B1 (en) * 2000-03-27 2002-04-23 Carrier Corporation Economizer circuit enhancement
US6883341B1 (en) * 2003-11-10 2005-04-26 Carrier Corporation Compressor with unloader valve between economizer line and evaporator inlet
US6941770B1 (en) * 2004-07-15 2005-09-13 Carrier Corporation Hybrid reheat system with performance enhancement
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Also Published As

Publication number Publication date
US20100122540A1 (en) 2010-05-20
CN101688706A (zh) 2010-03-31
HK1142387A1 (en) 2010-12-03
CN101688706B (zh) 2013-04-10
WO2008156482A1 (en) 2008-12-24

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