EP2409103A2 - Heat exchanger unit and thermotechnical system - Google Patents
Heat exchanger unit and thermotechnical systemInfo
- Publication number
- EP2409103A2 EP2409103A2 EP10719231A EP10719231A EP2409103A2 EP 2409103 A2 EP2409103 A2 EP 2409103A2 EP 10719231 A EP10719231 A EP 10719231A EP 10719231 A EP10719231 A EP 10719231A EP 2409103 A2 EP2409103 A2 EP 2409103A2
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat exchanger
- condenser
- exchanger unit
- evaporator
- evaporator device
- 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 claims description 13
- 238000013461 design Methods 0.000 claims description 9
- 238000009434 installation Methods 0.000 claims description 3
- 239000012530 fluid Substances 0.000 abstract description 6
- 238000001704 evaporation Methods 0.000 abstract 1
- 238000010276 construction Methods 0.000 description 5
- 239000006096 absorbing agent Substances 0.000 description 3
- 238000004378 air conditioning Methods 0.000 description 3
- 238000001816 cooling Methods 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 238000011161 development Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 241000699800 Cricetinae Species 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 238000010612 desalination reaction Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000010327 methods by industry Methods 0.000 description 1
- 239000003595 mist Substances 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000012549 training Methods 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 230000007704 transition Effects 0.000 description 1
- 239000002918 waste heat Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/0408—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids
- F28D1/0426—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids with units having particular arrangement relative to the large body of fluid, e.g. with interleaved units or with adjacent heat exchange units in common air flow or with units extending at an angle to each other or with units arranged around a central element
-
- 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
- F25B39/00—Evaporators; Condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/0408—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids
- F28D1/0426—Multi-circuit heat exchangers, e.g. integrating different heat exchange sections in the same unit or heat exchangers for more than two fluids with units having particular arrangement relative to the large body of fluid, e.g. with interleaved units or with adjacent heat exchange units in common air flow or with units extending at an angle to each other or with units arranged around a central element
- F28D1/0443—Combination of units extending one beside or one above the other
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D1/00—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators
- F28D1/02—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid
- F28D1/04—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits
- F28D1/047—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag
- F28D1/0477—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag
- F28D1/0478—Heat-exchange apparatus having stationary conduit assemblies for one heat-exchange medium only, the media being in contact with different sides of the conduit wall, in which the other heat-exchange medium is a large body of fluid, e.g. domestic or motor car radiators with heat-exchange conduits immersed in the body of fluid with tubular conduits the conduits being bent, e.g. in a serpentine or zig-zag the conduits being bent in a serpentine or zig-zag the conduits having a non-circular cross-section
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/007—Condensers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D21/00—Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
- F28D2021/0019—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for
- F28D2021/0068—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for refrigerant cycles
- F28D2021/0071—Evaporators
Definitions
- the invention relates to a heat exchanger unit and a heat engineering system, in particular a refrigeration system.
- the main components of refrigeration systems such as evaporator, absorber, expeller and condenser are heat exchangers, all of which transport between media heat. These heat exchangers are responsible for 50% of the costs and 75% of the volume of the refrigeration system.
- WO 2007/006289 A1 discloses a functional principle of a heat pump designed as an absorption refrigeration system. Based on a schematic diagram, the operation of the heat pump, which has a plurality of heat exchanger components, is explained in detail there. Heat exchanger components in the real construction of a plant are then also combined into heat exchanger units, which A steam generator configured to vaporize a heat exchanger operating or heat exchanger working fluid and having a condenser configured to fluidly liquefy the heat exchanger operating or heat exchanger working fluid.
- Known construction and construction types for heat exchanger units provide a pronounced spatial separation of the functional units, which are optionally arranged in a common shell or a common housing.
- the evaporator device and condenser device are arranged side by side.
- One embodiment of this is the so-called hamster baking construction, in which an evaporator device is arranged between two partial condenser devices and the overall structure is integrated in a tubular housing.
- Known units of heat exchanger components have a drip separator or steam jalousies to make it difficult for liquid splashes to make the transition to other heat exchanger units or to completely prevent this.
- the object of the invention is to provide a heat exchanger unit with an improved structural design, which supports the flexible use of the heat exchanger unit in applications with different requirements.
- a heat exchanger unit having an evaporator means configured to evaporate a heat exchange medium and a liquefaction means configured to liquefy the heat exchanger medium, the evaporator means and the condenser means for overflowing heat exchange means being in fluid communication and are arranged to each other in a frontal configuration.
- a heat pump in particular a refrigeration system, is provided with a plurality of heat exchanger units, which are assembled according to a modular structure.
- thermodynamic unit consists of one or more pairs of evaporator device and condenser, which form a thermodynamic and process engineering unit.
- This thermodynamic unit is characterized in particular in that both the length of the steam path and the specific steam mass flow are independent of the absolute power or capacity of the entire heat exchanger unit. The once optimized ratio of the capacities of the heat exchangers among themselves, which form a higher-level unit, is maintained even with scaling of the power.
- Modular heat exchanger units can be produced which can be assembled in an overall plant, thereby enabling improved scalability of thermal plants or heat pumps, in particular refrigerating plants and desalination plants.
- the frontal configuration allows a design with optimized space utilization and contributes significantly to the thermal separation of the different functional units, steam generator and condenser, which despite thermal optimization, the thermal losses are minimized.
- the evaporator device may be, for example, a generator or an evaporator.
- the condenser device is designed, for example, as an absorber or a condenser.
- the frontal arrangement of evaporator and condenser leads compared to known heat exchanger units to a changed vapor flow behavior between the devices, which implies a kind of wave formation, whereby an increased heat and mass transfer is achieved.
- the performance-related heat exchanger surface is reduced.
- the scalability achieved with the invention makes it possible to individually adapt thermal systems, in particular refrigeration systems, with regard to system size and performance for different applications.
- a compact design is possible, to advance into small power ranges that were unattractive to known designs of possible assembly of heat exchanger components due to poor power density and large footprint.
- a preferred embodiment of the invention provides that the evaporator device and the condenser are arranged opposite one another frontally.
- end surfaces of the evaporator device and the condenser device are arranged opposite one another, be it at a distance from each other or lying substantially one on top of the other.
- the evaporator device and the condenser are at least partially arranged end-to-end interlocking.
- line sections of evaporator device and condenser device engage in sections into one another, whereby an overlap formed thereby is preferably greater or smaller than half the longitudinal extension of the respective pipelines.
- An advantageous embodiment of the invention provides that piping of the evaporator device and pipes of the condenser device intermesh alternately. Alternately, a pipe of the evaporator and a pipe of the condenser are arranged.
- a development of the invention provides that an end face of the evaporator device facing the condenser device is arranged substantially completely overlapping with an end face of the condenser device facing the evaporator device and / or vice versa.
- the frontal surfaces are thus arranged substantially congruent.
- An advantageous embodiment of the invention provides a tropfabscheiderfill training. In contrast to known heat exchanger units, effort and precautions for a mist eliminator can be saved.
- a further development of the invention provides for a vapor barrier-free and / or a droplet barrier-free design. As a result, a further simplification is formed, which supports a material and cost-saving construction.
- a preferred embodiment of the invention provides a module structure.
- the design principle provided with regard to the arrangement of the evaporator device and condenser device makes it possible, in one embodiment, to form independent flow characteristics for the heat exchanger operating medium in the respective module, which essentially do not change when a plurality of heat exchanger units constructed as a module are assembled in one system.
- the evaporator device and the condenser device are formed in a thermal compressor.
- the thermal compressor is integrated in a refrigeration system.
- FIG. 1 is a perspective view of a thermal plant with four heat exchanger components
- FIG. 2 shows a schematic representation of a heat exchanger unit with a condenser device and evaporator device, in which end faces are arranged opposite one another
- FIG. 3 shows a schematic representation of a heat exchanger unit with condenser device and evaporator device, in which end faces are likewise arranged opposite one another
- FIG. 4 shows a schematic representation of a heat exchanger unit with a condenser device and evaporator device in an end-side configuration, wherein the evaporator device and the condenser device are partially arranged one inside the other.
- 1 shows a perspective view of a thermal installation with a heat exchanger unit 10, which is formed with a steam generator 11 and a condenser 12.
- the steam generator 11 and the condenser 12 each have associated pipes 13, 14.
- On the heat exchanger unit 10 a further heat exchanger unit 20 is arranged, which is formed with a condenser 21 and a steam generator 22.
- the two heat exchanger units 10, 20 form a refrigeration system.
- the steam generator 11 and the condenser 12 are positioned in a frontal configuration or arrangement with end faces disposed opposite one another.
- An identical structural design is provided for the further heat exchanger unit 20 with the condenser 21 and the steam generator 22.
- vaporized operating medium which is also referred to as working fluid, flows from the steam generator 11 to the condenser 12 in order to at least partially condense there.
- the liquid condensate is then transferred to the steam generator 22 to evaporate there and then flow as a vapor to the condenser 21, where condensation takes place again.
- the liquid produced in this case is then returned to the steam generator 11.
- FIG. 2 shows a schematic illustration of a heat exchanger unit with condenser device 30 and evaporator device 31 in which end faces 32, 33 are arranged opposite one another.
- FIG. 3 shows a schematic representation of a heat exchanger unit with condenser device 40 and evaporator device 41, in which end faces 42, 43 are likewise arranged opposite one another.
- FIG. 4 shows a schematic representation of a heat exchanger unit with condenser device 50 and evaporator device 51 in an end-side configuration, wherein the evaporator device 50 and the condenser device 51 are arranged partially interlocking, so that an overlap region 52 is created.
- the respective evaporator device steam generator
- the respective condenser device (condenser) is preferably designed as an absorber or a condenser.
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
Description
Claims
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102009013684A DE102009013684A1 (en) | 2009-03-20 | 2009-03-20 | Heat exchanger unit and thermal installation |
PCT/DE2010/000309 WO2010105613A2 (en) | 2009-03-20 | 2010-03-19 | Heat exchanger unit and thermotechnical system |
Publications (2)
Publication Number | Publication Date |
---|---|
EP2409103A2 true EP2409103A2 (en) | 2012-01-25 |
EP2409103B1 EP2409103B1 (en) | 2020-05-06 |
Family
ID=42674761
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP10719231.2A Active EP2409103B1 (en) | 2009-03-20 | 2010-03-19 | Heat exchanger unit and thermotechnical system |
Country Status (4)
Country | Link |
---|---|
US (1) | US10801782B2 (en) |
EP (1) | EP2409103B1 (en) |
DE (1) | DE102009013684A1 (en) |
WO (1) | WO2010105613A2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP3686714A1 (en) * | 2019-01-25 | 2020-07-29 | Asetek Danmark A/S | Cooling system including a heat exchanging unit |
Family Cites Families (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE1401713B2 (en) | 1958-10-14 | 1971-09-23 | HEAT EXCHANGER | |
DE1551523A1 (en) | 1967-01-05 | 1970-03-19 | Willy Scheller Maschb Kg Fa | Heat exchanger |
US3817708A (en) | 1970-02-25 | 1974-06-18 | Phillips Petroleum Co | Alkylation apparatus |
DE2343463A1 (en) | 1973-08-29 | 1975-03-13 | Ver Kesselwerke Ag | Pure distallate from contaminated feeds - by multi stage flash evaporation with interstage heating |
US5626102A (en) | 1996-03-14 | 1997-05-06 | Nir; Ari | Heat recovery system for a boiler and a boiler provided therewith |
US5916251A (en) * | 1997-10-29 | 1999-06-29 | Gas Research Institute | Steam flow regulation in an absorption chiller |
DE19902695B4 (en) * | 1998-01-21 | 2016-01-07 | Vaillant Gmbh | Sorption heat pump with an ad / desorber heat exchanger |
JP2000111212A (en) | 1998-10-09 | 2000-04-18 | Sanyo Electric Co Ltd | Absorption refrigerating machine interface activator circulating circuit |
DE19858686A1 (en) * | 1998-12-18 | 2000-06-21 | Linde Ag | Absorption machine for cooling with water or ambient air includes a generator and condenser exchanger unit and a damper and absorber exchanger unit |
CN1158499C (en) * | 1999-03-04 | 2004-07-21 | 株式会社荏原制作所 | Plate type heat exchanger |
US6529133B2 (en) * | 2000-03-31 | 2003-03-04 | Sanyo Electric Co., Ltd. | Repository and monitoring system therefor |
WO2003052338A1 (en) * | 2001-12-17 | 2003-06-26 | Showa Denko K.K. | Heat exchanger and process for fabricating same |
DE102005032266A1 (en) | 2005-07-11 | 2007-02-15 | Technische Universität Berlin | Process for removing a gas from a heat pump and heat pump |
JP2007113801A (en) * | 2005-10-18 | 2007-05-10 | Denso Corp | Heat exchanger |
US8506839B2 (en) * | 2005-12-14 | 2013-08-13 | E I Du Pont De Nemours And Company | Absorption cycle utilizing ionic liquids and water as working fluids |
CA2530621A1 (en) * | 2006-01-03 | 2007-07-03 | Free Energy Solutions Inc. | Thermal superconductor refrigeration system |
GB2451848A (en) | 2007-08-14 | 2009-02-18 | Arctic Circle Ltd | Multiple circuit heat exchanger comprising tube bundles |
-
2009
- 2009-03-20 DE DE102009013684A patent/DE102009013684A1/en not_active Withdrawn
-
2010
- 2010-03-19 EP EP10719231.2A patent/EP2409103B1/en active Active
- 2010-03-19 US US13/257,929 patent/US10801782B2/en active Active
- 2010-03-19 WO PCT/DE2010/000309 patent/WO2010105613A2/en active Application Filing
Non-Patent Citations (1)
Title |
---|
See references of WO2010105613A2 * |
Also Published As
Publication number | Publication date |
---|---|
DE102009013684A1 (en) | 2010-10-07 |
US10801782B2 (en) | 2020-10-13 |
WO2010105613A2 (en) | 2010-09-23 |
EP2409103B1 (en) | 2020-05-06 |
WO2010105613A3 (en) | 2011-03-10 |
US20120067713A1 (en) | 2012-03-22 |
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