EP3542118B1 - Wärmetauscher für den wärmetausch von flüssigkeiten mit unterschiedlichen temperaturen - Google Patents

Wärmetauscher für den wärmetausch von flüssigkeiten mit unterschiedlichen temperaturen Download PDF

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Publication number
EP3542118B1
EP3542118B1 EP17886878.2A EP17886878A EP3542118B1 EP 3542118 B1 EP3542118 B1 EP 3542118B1 EP 17886878 A EP17886878 A EP 17886878A EP 3542118 B1 EP3542118 B1 EP 3542118B1
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Prior art keywords
heat exchanger
low temperature
channel
high temperature
heat exchanging
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English (en)
French (fr)
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EP3542118A2 (de
EP3542118A4 (de
Inventor
Nattapong TARAPOOM
Treerat VACHARANUKRAUH
Kawisra SOMPECH
Wannawijit SRITHAMMARAT
Supawish KLANNARK
Nichaporn SIRIMUNGKALAKUL
Thana SORNCHAMNI
Rungroj CHUVAREE
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PTT Global Chemical PCL
PTT PCL
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PTT Global Chemical PCL
PTT PCL
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Priority claimed from TH1601007738A external-priority patent/TH175741A/th
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Publication of EP3542118A4 publication Critical patent/EP3542118A4/de
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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
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • F28D9/0068—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements with means for changing flow direction of one heat exchange medium, e.g. using deflecting zones
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/025—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being corrugated, plate-like elements
    • 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
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0031—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other
    • F28D9/0037—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by paired plates touching each other the conduits for the other heat-exchange medium also being formed by paired plates touching each 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
    • F28D9/00—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
    • F28D9/0062—Heat-exchange apparatus having stationary plate-like or laminated conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits for one heat-exchange medium being formed by spaced plates with inserted elements
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F3/00—Plate-like or laminated elements; Assemblies of plate-like or laminated elements
    • F28F3/02—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations
    • F28F3/04—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element
    • F28F3/042—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element
    • F28F3/046—Elements or assemblies thereof with means for increasing heat-transfer area, e.g. with fins, with recesses, with corrugations the means being integral with the element in the form of local deformations of the element the deformations being linear, e.g. corrugations
    • 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
    • F28D2021/0022—Other heat exchangers for particular applications; Heat exchange systems not otherwise provided for for chemical reactors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2260/00—Heat exchangers or heat exchange elements having special size, e.g. microstructures
    • F28F2260/02—Heat exchangers or heat exchange elements having special size, e.g. microstructures having microchannels

Definitions

  • Chemical engineering relates to a heat exchanger for exchanging heat of fluids having different temperatures.
  • the present invention relates to a heat exchanger having the features of the preamble of claim 1, as illustrated in US2010/314088 .
  • microchannel heat exchanger When compared to the normal size channels, the microchannels provide a higher heat transfer performance than normal heat exchanger, such as a shell and a tube heat exchanger and a plate and a frame heat exchanger. This is because the flow in microchannels can transfer heat from a channel wall into fluid faster, fluids in each channel have similar flow cross section temperatures, a heat transfer surface area is higher than normal channel at the same volume, and a pressure drop in the channel is relatively low.
  • the microchannels have some disadvantages that lead to limitation for application. For example, it is easily to be clogged because the channel is narrow. Especially, when being used for heat exchanging of fluids having highly different pressure, the permanent deforming can be happened.
  • the character of the channel of the heat exchanger is important to the heat transfer performance and the overall strength of the heat exchanger.
  • the character of the channel is a parameter to indicate the possibility in fabrication and the arrangement of the channel together. Therefore, there have been attempts continuously to develop the character of the channel in order to increase the performance of the heat exchanger and overcome the limitations previously said.
  • US20040031592 disclosed the heat exchanger comprising microchannel for the heat exchanging of three or more fluid streams, wherein the wall of said channel was flat with fins disposed in order to increase the heat changing surface area.
  • the installation of said fins increased a fouling rate inside the heat exchanger. Therefore, this reduced the heat transfer performance and increased the pressure drop of the heat exchanger.
  • said design might have a problem when using with high pressure fluid, leading to a limitation.
  • US4516632 disclosed the microchannel heat exchanger comprising the slotted heat exchanging sheets and unslotted heat exchanger sheets stacked in an alternating sequence, wherein the slotted heat exchanging sheet was placed in 90 degree with respect to one another in an alternating sequence in order to form a cross-flow configuration of fluids having different temperatures. Nevertheless, said flow configuration did not give a high heat exchanging performance.
  • EP1875959 disclosed the forming process of an emulsion with the installation of the heat exchanger comprising the microchannel heat exchanging plate stacked in an alternating sequence, wherein said channel was designed like a snake shape. This made two flowing patterns in said channel: a counter-current and a co-current. However, said channel design leads to easily clogging of the contaminants and was more difficult to clean comparing to the one flow direction path from one side to another side.
  • US8858159 disclosed a gas turbine comprising cooling channels for the low temperature air to flow pass and reduce heat of blades in the gas turbine, wherein said cooling channels were equipped with curved in and out ribs and the pedestals between each pair of ribs in order to increase the heat transfer performance.
  • said pedestals between each pair of ribs might increase the pressure drop of the heat exchanger which was the limitation when applying to the heat transfer between fluids with highly different pressure or fluids with high viscosity.
  • US20100314088 disclosed the heat exchanger comprising plates consisting of micrcochannels stacked in an alternating sequence. Said plates were designed to be curved and said microchannels were set into non-symmetric wavy form making parallel channel along the flow direction of fluids. The total length of direct portion and curve portion was set to be constant. However, said patent did not disclose the suitable parameters of said wavy channel such as width size, curve radius, etc.
  • this invention aims to provide the heat exchanger for exchanging heat of fluids having different temperatures, especially to increase the heat transfer performance of said fluids and decrease problems related to the heat exchanger for exchanging heat of fluids having highly different pressures.
  • This invention aims to provide the heat exchanger for exchanging heat of fluids having different temperatures, especially to increase the heat exchanging performance of said fluids having different temperatures and decrease problems related to the heat exchanger for exchanging heat of fluids having highly different pressures.
  • this invention discloses the heat exchanger for exchanging heat of fluids having different temperatures, comprising: at least one flat heat exchanging plate; at least one high temperature heat exchanging plate; and at least one low temperature heat exchanging plate stacked in an alternating sequence, wherein an inlet of high temperature fluid and an outlet of high temperature fluid are disposed in order to pass the high temperature fluid through each said high temperature heat exchanging plate , and an inlet of an low temperature fluid and an outlet of low temperature fluid are disposed in order to pass the low temperature fluid through each said low temperature heat exchanging plate, wherein said high temperature heat exchanging plate and said low temperature heat exchanging plate comprising the high temperature channel and the low temperature channel, wherein said channels have a length extending in a flow direction of said fluids and a side wall of each said channel has a symmetric wavy pattern with, a center line of each said channel.
  • the present invention relates to the heat exchanger for exchanging heat of fluids having different temperatures as described according to the following embodiments.
  • any tools, equipment, methods, or chemicals mentioned herein mean tools, equipment, methods, or chemicals commonly operated or use by those person skilled in the art unless explicated that they are tools, equipment, methods, or chemicals specific only in this invention.
  • This invention discloses the heat exchanger for exchanging heat of fluids having different temperatures, comprising: at least one flat heat exchanging plate; at least one high temperature heat exchanging plate; and at least one low temperature heat exchanging plate stacked in an alternating sequence, wherein an inlet of the high temperature fluid and an outlet of the high temperature fluid are disposed in order to pass the high temperature fluids through each said high temperature heat exchanging plate, and an inlet of low temperature fluid and an outlet of low temperature fluid are disposed in order to pass a low temperature fluid through each said low temperature heat exchanging plate, wherein said high temperature heat exchanging plate and low temperature heat exchanging plate comprising a high temperature channel and a low temperature channel, wherein said channels have a length extending in a flow direction of said fluids and a side wall of each said channel has symmetric wavy curve pattern with a center line of each said channel as a symmetric axis.
  • Figure 1 and 2 show one aspect of the heat exchanger according to the present invention.
  • the heat exchanger comprising at least one flat heat exchanging plate 12; at least one high temperature heat exchanging plate 14; and at least one low temperature heat exchanging plate 16 stacked in an alternating sequence, wherein an inlet of high temperature fluid 18a and an outlet of high temperature fluid 20a are disposed in order to pass a high temperature fluid through each said high temperature heat exchanging plate 14, and an inlet of low temperature fluid 18b and an outlet of low temperature fluid 20b are disposed in order to pass the-low temperature fluid through each said low temperature heat exchanging plate 16.
  • the said inlet and outlet parts assembly can be separated from the heat exchanger.
  • the said high temperature heat exchanging plate 14 comprising the high temperature channel 15 and said low temperature heat exchanging plate 16 comprising the low temperature channel 17, wherein said channels have a length extending the flow direction of said fluid and the side wall of each said channel has a symmetric wavy curve pattern with the center line of each said channel as a symmetric axis.
  • the high temperature channel 15 and the low temperature channel 17 have an average width (y) in a range of 100 to 5,000 ⁇ m and the curve length (x) and the curve radius (r) according to this equation: x ⁇ 2 r , wherein x is in a range of 100 to 100,000 ⁇ m.
  • said channel have the average width in the range of 100 to 3,000 ⁇ m, the curve length in the range of 1,000 to 3,000 ⁇ m, and the curve radius in the range of 2,000 to 5,000 ⁇ m.
  • the high temperature channel 15 and the low temperature channel 17 have the depth in the range of about 10 to 2,000 ⁇ m when comparing to the plane set by the top of each high temperature heat exchanging plate 14 and each low temperature heat exchanging plate 16.
  • the high temperature heat exchanging plate 14 and the low temperature heat exchanging plate 16 are arranged in order to place the high temperature channel 15 and the low temperature channel 17 oriented in alternate configuration as shown in figure 2 .
  • the flat heat exchanging plate 12, the high temperature heat exchanging plate 14, and the low temperature heat exchanging plate 16 have a thickness in a range of about 10 to 10,000 ⁇ m, preferably the thickness in the range of about 100 to 2,000 ⁇ m.
  • said heat exchanging plate may be made from carbon steel, stainless steel, aluminium, titanium, platinum, chromium, copper, or alloy of said materials, preferably made from stainless steel 316 grade (SS316).
  • the high temperature heat exchanging plate 14 and the low temperature heat exchanging plate 16 may be formed by stamping machine technique, photo chemical machine (PCM) technique, or computer numerical control milling machine technique.
  • the inlet of the high temperature fluid 18a and the inlet of low temperature fluid 18b are disposed in an opposite side of the heat exchanger in order to cause fluids having different temperatures to flow in the counter-current direction, wherein said fluids with different temperatures may have temperature difference at least 1 °C, preferably temperature difference at least 10 °C.
  • said flat heat exchanging plate 12, the high temperature heat exchanging plate 14, and the low temperature heat exchanging plate 16 can be stacked in an alternating sequence from three plates and more, they can be stacked in higher numbers in order to provide the heat exchanger with many channels for heat exchanging of fluids with high flow rate.
  • the heat exchanger according to this invention as the second embodiment comprising the high temperature channel 15 and the low temperature channel17 according to the appearance in figure 4 and the heat exchanger comprising the high temperature channel and the low temperature channel characterized in non-symmetric wavy pattern and straight channel (according to the appearance in figure 5 and 6 respectively) were build and tested with computational flow dynamics model using ANSYS Fluent Software, version 16.1 as being described below.
  • the heat exchanger 1 The heat exchanger 1
  • each flat heat exchanging plate 12, the high temperature heat exchanging plate 14, and the low temperature heat exchanging plate 16 was 0.5 mm.
  • the high temperature channel 15 and the low temperature channel 17 as shown in figure 4 had average width (y) about 2,000 ⁇ m, the curve length (x) about 2,000 ⁇ m, and the curve radius (r) about 3,000 ⁇ m.
  • the length of the channel was about 240 mm and the depth was about 1,000 ⁇ m.
  • the heat exchanger 2 The heat exchanger 2
  • each flat heat exchanging plate 12, the high temperature heat exchanging plate 14, and the low temperature heat exchanging plate 16 was 0.5 mm.
  • the high temperature channel 15 and the low temperature channel 17 as shown in figure 4 had the average width (y) about 2,000 ⁇ m, the curve length (x) about 2,000 ⁇ m, and the curve radius (r) about 4,000 ⁇ m.
  • the length of the channel was about 240 mm and the depth was about 1,000 ⁇ m.
  • each flat heat exchanging plate 12, the high temperature heat exchanging plate 14, and the low temperature heat exchanging plate 16 was 0.5 mm.
  • the high temperature channel 15 and the low temperature channel 17 as shown in figure 4 had average width (y) about 2,000 ⁇ m, the curve length (x) about 3,000 ⁇ m, and the curve radius (r) about 3,000 ⁇ m.
  • the length of the channel was about 240 mm and the depth was about 1,000 ⁇ m.
  • each flat heat exchanging plate 12, the high temperature heat exchanging plate 14, and the low temperature heat exchanging plate 16 was 0.5 mm.
  • the high temperature channel 15 and the low temperature channel 17 as shown in figure 4 had the average width (y) about 2,000 ⁇ m, the curve length (x) about 3,000 ⁇ m, and the curve radius (r) about 4,000 ⁇ m.
  • the length of the channel was about 240 mm and the depth was about 1,000 ⁇ m.
  • the heat exchanger A The heat exchanger A
  • the heat exchanger comprising the components as described in the heat exchanger 1 except that the characters of the high and the low temperature channel having a non-symmetric wavy pattern as shown in figure 5 was used.
  • the heat exchanger B The heat exchanger B
  • the heat exchanger comprising the components as described in the heat exchanger 2 except that the characters of the high and the low temperature channels having the non-symmetric pattern as shown in figure 5 was used.
  • the heat exchanger comprising the components as described in the heat exchanger 3 except that the characters of the high and the low temperature channel having the non-symmetric pattern as shown in figure 5 was used.
  • the heat exchanger D The heat exchanger D
  • the heat exchanger comprising the components as described in the heat exchanger 4 except that the characters of the high and the low temperature channel having the non-symmetric pattern as shown in figure 5 was used.
  • the heat exchanger comprising the components as described in the heat exchanger 1 except that the characters of the high and the low temperature channel having the straight path with about 2,000 ⁇ m width as shown in figure 6 was used.
  • the heat exchanger comprising different characters of the channel as described above was tested for heat exchanging performance using ANSYS Fluent software version 16.1 with the following parameters. Fluids used in the model were water at different temperatures, wherein the high temperature fluid was about 90 °C and the low temperature fluid was about 10 °C. The said fluids flowed in the counter-current direction with flow velocity in each path about 0.582 g/sec. The results were shown in table 1 and figure 7 . Table 1 shows temperature of the high temperature fluids outlet and the temperature of the low temperature fluids outlet from the outlet of the heat exchanger comprising different characters of the high temperature channel and the low temperature channel.
  • the performance of the heat exchanger can be considered from the temperature of the high temperature fluid outlets and the temperature of the low temperature fluid outlet as shown in table 1 and the heat transferred per fluid volume as shown in figure 7 .
  • the heat exchanger comprising different characters of the channel as described above was tested using ANSYS Fluent software version 16.1.
  • the parameters were set as the following.
  • the heat exchanging plates were made from 316 grade stainless steel (SS316).
  • the pressure of the high temperature fluid was about 1.5 MPa.
  • the pressure of the low temperature fluid was about 0.5 MPa.
  • the heat exchanging plates were fixed at the edges of the heat exchanging plates.
  • Table 2 shows the comparison of the strength of the heat exchanger according to present invention to the heat exchanger according to the prior art, which could be considered from the maximum equivalent stress and volumetric percentage of the heat exchanging plates in each stage of the equivalent stress happened to the heat exchanging plates of the heat exchanger during heat transferring of the fluids with different temperatures.
  • the channel of the heat exchanger according to the invention 3 had the symmetric wavy pattern with the average width about 2,000 ⁇ m, the curve length about 3 mm, and the curve radius about 3 mm, wherein the highest strength was considered from the lowest maximum equivalent stress, the high volumetric percentage of the heat exchanging plate in low equivalent stress stage (0 - 3 MPa), and the high volumetric percentage of the heat exchanging plate in high equivalent stress stage (6 - 9 MPa).
  • the maximum equivalent stress of the heat exchanger according to this present invention had a lower tensile yield strength than the 316 grade stainless steel (about 207 MPa), used as sample material in strength test. This showed that said heat exchanging plate of the heat exchanger did not permanently deformed when operated at the above conditions.
  • the heat exchanger according to present invention has high performance in heat transferring of the fluids with different temperatures, has high strength, and can be used for the heat exchanging of the fluids with highly different pressures as being said in the objectives of this invention.

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  • 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)

Claims (11)

  1. Wärmetauscher zum Austausch von Wärme von Fluiden, die unterschiedliche Temperaturen haben, umfassend:
    mindestens eine flache Wärmetauscherplatte (12); mindestens eine Hochtemperaturwärmetauscherplatte (14); und mindestens eine Niedertemperaturwärmetauscherplatte (16), die in alternierender Folge gestapelt sind,
    wobei ein Hochtemperaturfluideinlass (18a) und ein Hochtemperaturfluidauslass (20a) angeordnet sind, um ein Hochtemperaturfluid durch jede der besagten Hochtemperaturwärmetauscherplatten (14) durchzulassen, und ein Niedertemperaturfluideinlass (18b) und ein Niedertemperaturfluidauslass (20b) angeordnet sind, um ein Niedertemperaturfluid durch jede der besagten Niedertemperaturwärmetauscherplatte (16) zu durchzulassen, dadurch charakterisiert, dass
    besagte Hochtemperaturwärmetauscherplatte (14), die einen Hochtemperaturkanal (15) umfasst, und besagte Niedertemperaturwärmetauscherplatte (16), die einen Niedertemperaturkanal (17) umfasst,
    wobei der Wärmetauscher dadurch charakterisiert ist, dass
    besagte Kanäle eine Länge haben, die sich in einer Flussrichtung der besagten Fluide erstreckt, und eine Seitenwand jedes besagten Kanals eine symmetrische Wellenform mit einer Zentrumslinie des besagten Kanals als einer Symmetrieachse hat.
  2. Wärmetauscher nach Anspruch 1,
    wobei der Hochtemperaturkanal (15) und der Niedertemperaturkanal (17) eine durchschnittliche Breite (y) in einem Bereich von 100 bis 5.000 µm und eine Kurvenlänge (x) und einen Kurvenradius (r) gemäß der folgenden Gleichung haben: x ≤ 2 r ,
    Figure imgb0004
     wobei x in einem Bereich von 100 bis 100.000 µm ist.
  3. Wärmetauscher nach Anspruch 1 oder 2, wobei der Hochtemperaturkanal (15) und der Niedertemperaturkanal (17) die durchschnittliche Breite im Bereich von 100 bis 3.000 µm, die Kurvenlänge im Bereich von 1000 bis 3000 µm und den Kurvenradius im Bereich von 2000 bis 5000 µm haben.
  4. Wärmetauscher nach einem der vorhergehenden Ansprüche, wobei der Hochtemperaturkanal (15) und der Niedertemperaturkanal (17) eine Tiefe in einem Bereich von 10 bis 2000 µm gemäß der Fläche, die durch die Oberseite jeder Hochtemperaturwärmetauscherplatte (14) und jeder Niedertemperaturwärmetauscherplatte (16) definiert ist, haben.
  5. Wärmetauscher nach Anspruch 4, wobei der Hochtemperaturkanal (15) und der Niedertemperaturkanal (17) die Tiefe im Bereich von 500 bis 1.500 µm gemäß der Fläche, die durch die Oberseite jeder Hochtemperaturwärmetauscherplatte (14) und jeder Niedertemperaturwärmetauscherplatte (16) definiert ist, haben.
  6. Wärmetauscher nach Anspruch 4 oder 5, wobei die Hochtemperaturwärmetauscherplatte (14) und die Niedertemperaturwärmetauscherplatte (16) in der Richtung angeordnet sind, dass der Hochtemperaturkanal (15) und der Niedertemperaturkanal (17) in alternierender Konfiguration ausgerichtet sind.
  7. Wärmetauscher nach Anspruch 1, wobei die flache Wärmetauscherplatte (12), die Hochtemperaturwärmetauscherplatte (14), und die Niedertemperaturwärmetauscherplatte (16) eine Dicke in einem Bereich von 10 bis 10.000 µm haben.
  8. Wärmetauscher nach Anspruch 7, wobei die flache Wärmetauscherplatte (12), die Hochtemperaturwärmetauscherplatte (14) und die Niedertemperaturwärmetauscherplatte (12) eine Dicke im Bereich von 100 bis 2.000 µm haben.
  9. Wärmetauscher nach Anspruch 1, wobei der Hochtemperaturfluideinlass (18a) und der Niedertemperaturfluideinlass (18b) in der gegenüberliegenden Seite des Wärmetauschers angeordnet sind, um Gegenfluss von Fluiden, die unterschiedliche Temperaturen haben, zu bilden.
  10. Verwendung eines Wärmetauschers nach Anspruch 1 oder 9, wobei die Fluide einen Temperaturunterschied von mindestens 1 °C haben.
  11. Verwendung eines Wärmetauscher nach Anspruch 10, wobei die Fluide einen Temperaturunterschied von mindestens 10 °C haben.
EP17886878.2A 2016-12-26 2017-12-21 Wärmetauscher für den wärmetausch von flüssigkeiten mit unterschiedlichen temperaturen Active EP3542118B1 (de)

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Application Number Priority Date Filing Date Title
TH1601007738A TH175741A (th) 2016-12-26 เครื่องแลกเปลี่ยนความร้อนสำหรับแลกเปลี่ยนความร้อนของของไหล ที่มีอุณหภูมิต่างกัน
PCT/TH2017/000089 WO2018124980A2 (en) 2016-12-26 2017-12-21 A heat exchanger for exchanging heat of fluids having different temperatures

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EP3542118A2 EP3542118A2 (de) 2019-09-25
EP3542118A4 EP3542118A4 (de) 2020-09-02
EP3542118B1 true EP3542118B1 (de) 2021-09-29

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US (1) US20190339018A1 (de)
EP (1) EP3542118B1 (de)
JP (1) JP6942815B2 (de)
KR (1) KR102555230B1 (de)
CN (1) CN110268218A (de)
WO (1) WO2018124980A2 (de)

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WO2020013319A1 (ja) * 2018-07-13 2020-01-16 株式会社三井Ｅ＆Ｓマシナリー 気化器
JP1653096S (de) * 2018-11-26 2020-02-17
KR20210095673A (ko) * 2018-11-26 2021-08-02 피티티 글로벌 케미컬 퍼블릭 컴퍼니 리미티드 마이크로 채널 열 교환기
JP1653094S (de) * 2018-11-26 2020-02-17
JP1653095S (de) * 2018-11-26 2020-02-17
CN110006277A (zh) * 2019-05-06 2019-07-12 南通文鼎换热设备科技有限公司 一种板式换热器的波浪形流体通道换热片
US20210254904A1 (en) * 2020-02-19 2021-08-19 The Boeing Company Additively manufactured heat exchanger
JP7428538B2 (ja) * 2020-02-27 2024-02-06 三菱重工業株式会社 熱交換コア
CN111661888B (zh) * 2020-06-15 2022-07-05 方诺传热系统(江苏)有限公司 一种基于蒸发空冷技术的降膜式空冷器及废水处理流程
CN111680378B (zh) * 2020-07-17 2022-09-16 天华化工机械及自动化研究设计院有限公司 一种基于ansys的充液状态下换热器管束模态分析方法
CN111928688B (zh) * 2020-07-22 2021-10-29 武汉第二船舶设计研究所(中国船舶重工集团公司第七一九研究所) 印刷电路板换热器的流体通道结构及印刷电路板换热器
US11927402B2 (en) 2021-07-13 2024-03-12 The Boeing Company Heat transfer device with nested layers of helical fluid channels

Family Cites Families (16)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4815534A (en) * 1987-09-21 1989-03-28 Itt Standard, Itt Corporation Plate type heat exchanger
IL114613A (en) * 1995-07-16 1999-09-22 Tat Ind Ltd Parallel flow condenser heat exchanger
JP4072876B2 (ja) * 1998-05-22 2008-04-09 セキサーマル株式会社 積層型熱交換器
SE516537C2 (sv) * 2000-05-19 2002-01-29 Alfa Laval Ab Plattpaket och plattvärmeväxlare
US6867973B2 (en) * 2003-03-05 2005-03-15 Shyy-Woei Chang Heat dissipation device with liquid coolant
JP4756585B2 (ja) * 2005-09-09 2011-08-24 臼井国際産業株式会社 熱交換器用伝熱管
JP5082120B2 (ja) * 2007-03-23 2012-11-28 国立大学法人 東京大学 熱交換器
KR100990309B1 (ko) * 2008-06-03 2010-10-26 한국수력원자력 주식회사 열교환기
FR2938637B1 (fr) * 2008-11-18 2013-01-04 Cie Mediterraneenne Des Cafes Conduit de circulation d'un fluide
KR100938802B1 (ko) * 2009-06-11 2010-01-27 국방과학연구소 마이크로채널 열교환기
KR101303234B1 (ko) * 2011-08-08 2013-09-04 김태식 배기열 회수용 열교환기
US9878893B2 (en) * 2012-07-27 2018-01-30 Huang-Han Chen Water dispenser
ITPD20120365A1 (it) * 2012-12-05 2014-06-06 Blue Box Group S R L Scambiatore di calore
CN105329924A (zh) * 2015-10-14 2016-02-17 贵阳铝镁设计研究院有限公司 一种低速氧化铝管道化溶出换热装置
CN105651094A (zh) * 2016-03-17 2016-06-08 郑州大学 一种新型变截面相间螺旋扭曲换热管
CN105870081A (zh) * 2016-04-01 2016-08-17 西安交通大学 一种波形微通道式换热器

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CN110268218A (zh) 2019-09-20
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JP2020503492A (ja) 2020-01-30
WO2018124980A3 (en) 2018-10-25
KR102555230B1 (ko) 2023-07-13
EP3542118A2 (de) 2019-09-25
US20190339018A1 (en) 2019-11-07
WO2018124980A2 (en) 2018-07-05
EP3542118A4 (de) 2020-09-02

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