WO2010138526A1 - Echangeur de chaleur à plaque à double paroi amélioré - Google Patents

Echangeur de chaleur à plaque à double paroi amélioré Download PDF

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Publication number
WO2010138526A1
WO2010138526A1 PCT/US2010/036106 US2010036106W WO2010138526A1 WO 2010138526 A1 WO2010138526 A1 WO 2010138526A1 US 2010036106 W US2010036106 W US 2010036106W WO 2010138526 A1 WO2010138526 A1 WO 2010138526A1
Authority
WO
WIPO (PCT)
Prior art keywords
heat exchanger
double
plate heat
leakage
skin
Prior art date
Application number
PCT/US2010/036106
Other languages
English (en)
Inventor
Hemant Kumar
Jonathan G. Shaw
Gary A. Crawford
Jes H. Petersen
Original Assignee
Apv North America, Inc.
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 Apv North America, Inc. filed Critical Apv North America, Inc.
Priority to EP10781104.4A priority Critical patent/EP2435774B1/fr
Priority to DK10781104.4T priority patent/DK2435774T3/en
Priority to CN201080023585.9A priority patent/CN102449420B/zh
Publication of WO2010138526A1 publication Critical patent/WO2010138526A1/fr

Links

Classifications

    • 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
    • F28F3/08—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning
    • F28F3/10—Arrangements for sealing the margins
    • 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
    • F28D9/0043—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 plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another
    • F28D9/005—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 plates having openings therein for circulation of at least one heat-exchange medium from one conduit to another the plates having openings therein for both heat-exchange media
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2265/00—Safety or protection arrangements; Arrangements for preventing malfunction
    • F28F2265/16—Safety or protection arrangements; Arrangements for preventing malfunction for preventing leakage

Definitions

  • the present invention relates to double-walled plate heat exchangers.
  • Plate heat exchangers are used in many process fields where a fluid in a liquid or gas form is heated or cooled to a suitable temperature during continuous flow through the plate heat exchanger.
  • a fluid When a fluid is to be heated, it is caused to flow through a small passage in the plate heat exchanger, the passage having a large thermal contact face exposed to a heat-emitting fluid which preferably passes through the plate heat exchanger in counterfiow to the fluid for heating.
  • the other fluid in the heat exchanger is heat-absorbing.
  • FIG. 1 is a schematic of a conventional single-walled plate heat exchanger 1.
  • FIG. 1 shows five rectangular plates 10a- 1Oe, generally referred to as plate 10, which is typically just a small part of the total number of plates of the plate heat exchanger 1.
  • Each of the plates 10 has four port holes 12a-12d, collectively referred to as port hole 12, as well as a heat transfer area 14.
  • a first fluid flows between two adjacent plates 10 from a first distribution channel 15 at a fluid inlet, e.g., port hole 12a, to a second distribution channel 16 at a fluid outlet, e.g., port hole 12c.
  • FIG. 2 is a schematic of a plate 10 in a conventional plate heat exchanger 1.
  • the plate 10 e.g., any one of plates 1Oa-IOe, is provided with a gasket 20 which is secured to the plate 10.
  • the gasket 20 has a gasket part 22 which substantially follows the periphery of the individual plate 10 and thus seals the cavity formed between two plates 10 upon assembly of the plate heat exchanger 1.
  • the gasket part 22 permits fluid flow over the plate 10 from an inlet, e.g., port holes 12a, 12c, of a distribution channel 15-18 to its outlet, e.g., 12b, 12d, respectively.
  • the gasket part 22 also prevents fluid passage from the other port holes 12 to the cavity between the two plates.
  • the first fluid passing through port holes 12a and 12c has no contact with the second fluid passing through port holes 12b and 12d.
  • the gasket 20 additionally has two ring-shaped gasket parts 24 surrounding and sealing off the other port holes 12b, 12d which do not communicate with the cavity between the plates.
  • the ring-shaped gasket parts 24, as depicted, are an integral part of the gasket 20, since they are connected to the gasket part 22 through connectors 26.
  • the plate 10 has a notch 30 which can accommodate a guide rail (not shown) upon assembly of the plate heat exchanger 1, thereby ensuring correct assembly.
  • the heat transfer area 14 of the plate 10 across which the fluid flows is divided into a central area 34 molded in a pattern, e.g. washboard-shaped, while end areas 32 around the port holes 12a-12d are provided with diagonal channels.
  • the molding of the plates 10 serves several functions, including reduction of the flow rate of the fluid to ensure good heat transfer between the fluids, while distributing the pressure from the compression of the plate heat exchanger 1 to the entire cross-section of the plate.
  • lOb-lOd can develop an unintended perforation, e.g., a hole or a crack, in the zone transferring heat from the hot medium to the cold medium.
  • the aforementioned perforation may allow the higher-pressure medium to pass through the perforation into the lower-pressure medium, which is not desirable.
  • the higher pressure medium may be glycol and the lower pressure medium may be potable water, resulting in the contamination of the potable water with the toxic glycol.
  • a proposed solution to the above-described drawback uses double-walled plates replacing single-walled plates as described above. It is known to replace each of the inner plates lOb-d with double-walled elements. Such elements are made from two metal skins which have undergone stretch forming together. The two metal skins are typically tightly and permanently joined in the corner port holes 12.
  • a proposed solution to this drawback uses port holes 12 that are not permanently joined, but by making different-sized holes in the two skins, and providing a suitable sealing member, such as peripheral sealing gasket-carrying grooves, at these port holes 12, the permanent joining is avoided altogether. Thus, the space between the plates 10 is able to be inspected. [0013] However, because the two skins are in close contact, any leakage into the space between the skins does not easily reach the external edge of the plate heat exchanger 1 for easy observation by the process operator, which means the process operator may not be properly alerted to a problem.
  • the gasket compression through the plate stack hinders leakage to the external edge.
  • One known solution to this is placing metal tapes between the skins in line with the gasket sealing members or by creating a small channel. In either case, the net result is one or more leak paths in the space between the plates 10 in line with the gasket sealing members on each side.
  • the sealing portion extends around the heat exchange portion as well as the flow openings, (e.g., port holes 12).
  • vent space For external leakage, virtually all conventional plate heat exchangers 1 have a leakage groove in a so-called vent space. This vent space is in free communication with the atmosphere around the plate heat exchanger 1. This communication is achieved by locally removing the sealing portion of the surrounding gasket 20. Often, the plate 10 is weakened at the same time to ensure that there is no impediment to leakage. The purpose of this design is to make sure that, in a conventional plate heat exchanger 1, there is a double-gasket barrier between hot and cold media, the space between the barriers being open to atmosphere.
  • this space is not in between the two skins of the double- walled plate 10 but on the front face of a front plate, e.g., plate 1Oa-IOd, where the gasket 20 is on only one side of the plate 10a- 1Od.
  • Embodiments of the present invention advantageously provide a plate heat exchanger with multi-layered plates which provides drainage of fluid that accumulates between plates, prevents cross-contamination of fluids, and allows inspection of the heat exchanger for leaks.
  • Another embodiment of the invention includes a method of managing a leak in a double-walled plate heat exchanger, the method including allowing fluid leaked between first and second skins of a first plate in a double-walled plate heat exchanger to exit the double-walled plate heat exchanger via a leakage escape path, the leakage escape path including a leakage orifice, the first plate further including first and second port holes.
  • Another embodiment of the invention includes a double- walled plate heat exchanger includes leakage escape means for allowing fluid leaked between first and second skins of a first plate in a double-walled plate heat exchanger to exit the double-walled plate heat exchanger, the leakage escape means including at least one leakage orifice means for allowing the leaked fluid to exit via first skin.
  • Another embodiment of the invention includes a double-walled plate heat exchanger which includes leakage escape means for allowing fluid leaked between first and second skins of a first plate in a double-walled plate heat exchanger to exit the double- walled plate heat exchanger, the leakage escape means including leakage orifice means for allowing the leaked fluid to exit from between the first and second skins, the first plate having at least two port holes.
  • FIG. 1 is a schematic view of a conventional single-walled plate heat exchanger.
  • FIG. 2 is a schematic view of a plate in a conventional plate heat exchanger.
  • FIG. 3 is a schematic view of a portion of a plate in a double-walled plate heat exchanger in accordance with an embodiment of the present invention.
  • FIG.4 is a schematic view of another portion of the plate in a double-walled plate heat exchanger shown in FIG. 3.
  • FIG. 5 is a flow chart of a method of forming a plate heat exchanger in accordance with an embodiment of the present invention.
  • FIG. 6 is a flow chart of another method of forming a plate heat exchanger in accordance with an embodiment of the present invention.
  • FIG. 7 is a flow chart of a method of managing a leak in a double-walled plate heat exchanger.
  • FIG. 8 is a schematic view of a portion of a double- walled plate heat exchanger in accordance with an embodiment of the present invention.
  • FIG. 9 is a schematic view of a portion of a double-walled plate heat exchanger in accordance with an embodiment of the present invention.
  • FIG. 3 is a schematic view of a portion of a plate utilized in a double-walled plate heat exchanger in accordance with an embodiment of the present invention.
  • a double-walled plate heat exchanger 100 includes a plate 110 which is provided with a gasket 120 that is secured to a front side 300 of the plate 110.
  • a first plate is referenced as 110a.
  • Each plate made in accordance with the invention may be the same as plate 110a, although a second plate described below will be referenced as 110b for ease of description.
  • plate 110 e.g., first plate 110a
  • the gasket 120 has a gasket part 122 which substantially follows the periphery of the individual plate 110 and thus seals the heat transfer area 114 formed between two plates 110 upon assembly of the plate heat exchanger 100.
  • the gasket part 122 permits fluid flow over the plate 110 from an inlet, e.g., port hole 112 as depicted in FIG. 3.
  • the gasket part 122 also prevents fluid passage from the other port holes to the heat transfer area 114 between the two plates 110a, HOb.
  • the gasket 120 has a ring-shaped gasket part 124 surrounding and sealing off the port holes 112 which does not communicate with the heat transfer area 114 between the plates.
  • the ring-shaped gasket part 124 is an integral part of the gasket 120, since it is connected to the gasket part 122 through connector 126.
  • the plate 110 has a notch 130 which can accommodate a guide rail (not shown) upon assembly of the plate heat exchanger 100, thereby ensuring correct assembly.
  • the plate 110 also has additional port holes 112, each of which may be formed and surrounded by a ring- shaped gasket part 124 as depicted for the port hole 112 shown in FIG. 3. It should be appreciated that, in a preferred embodiment, four port holes 112 would be utilized, such that fluid flow for non-leaked fluid will be similar to that shown in the FIG. 1 distribution channels 15-18.
  • a leakage escape path 311 is provided between the first and second skins 301, 302 for allowing leaked fluid to exit the double-walled plate heat exchanger 100, the leakage escape path 311 is in contact with at least one leakage orifice 315 and an outer edge 306 of the double-walled plate heat exchanger 100.
  • the leakage orifice 315 is provided in a vent area 350 of the front plate 300.
  • the first skin 301 is provided with the gasket 120.
  • the second skin 302 may be viewed through the leakage orifice 315.
  • a leakage groove 305 is provided across the gasket connector 126, so fluid may escape to the atmosphere at the outer edge 306 of the double-walled plate heat exchanger 100.
  • the gasket may be recessed, or even completely removed or eliminated, to allow passage of fluid across the leakage groove 305.
  • an optional groove extension 316 may be provided to further guide fluid from the leakage orifice 315 to the leakage groove 305.
  • FIG. 4 is a schematic view of another portion of the plate in a double-walled plate heat exchanger shown in FIG. 3.
  • the feature illustrated in FIG. 4 is the second skin 302 of the double- walled plate heat exchanger 100.
  • the second skin 302 includes a vent area 450 which includes an indentation 420 that connects a leak guide 421.
  • the leak guide 421 may include ribs 425, 430, 435 that aid in keeping the skins 301, 302 apart when pressed together, so that leaked fluid may pass along the leak guide 421.
  • the two fluids are kept completely separate by the gasket 120.
  • a leak occurs between the skins of the plate 110, for example, via a defect in, crack in, or corrosion of one of the skins 301, 302
  • internal pressure will tend to push the fluid toward the leak guide 421 or directly to the indentation 420, and leakage orifice 315, depending on the location of the defect causing the leak.
  • the fluid will them flow through the leakage orifice 315 to the leakage groove 305, and out to the atmosphere where it will either dissipate or be collected for analysis and/or disposal.
  • the location of the expected leak will thus be known in advance, so an operator will know where to look, in general, for leaks.
  • Another embodiment of the present invention involves providing one or more leakage orifices 315 in the front plate 300 in the vent area 350, 450, such that the space between the double-walled plates 110a and 110b is in communication with this vent area 350, 450.
  • the vent area 350, 450 is open to the atmosphere via the break in the sealing at the periphery, e.g., gasket area 310.
  • any fluid which has reached the space between the skins 301, 302 of the plate 110 e.g., via a perforation, is able to leak out into the vent space 350, 450 and then out of the vent space 350, 450 to the edge 306 of the double-walled plate heat exchanger 100.
  • the leakage orifice 315 is positioned on a surface which is in a relatively close contact with the second skin 302.
  • the second skin 302 is modified by a depression or depressions, i.e., indentation 420, which align with the leakage orifice 315 in the front skin 301 to reduce flow resistance.
  • the leak guide 421 may be provided at an edge of the heat exchange portion of the second skin 302 which is not in contact with a sealing member. This positioning is preferred to reduce the hydraulic resistance to the leakage path out of the heat exchange zone. Substantial design changes can be made in this area since these surfaces do not have to seal against a gasket 120. Various shapes and inclinations, longitudinal or transverse or intermediate, or attachments of various thicknesses and numbers can be made to allow leakage to reach the leakage orifices and depressions (e.g., leakage orifice 315, indentation 420) made in the first and second skins 301, 302 in the vent space 350, 450 as described above.
  • the leakage orifices and depressions e.g., leakage orifice 315, indentation 420
  • distribution areas are positioned. These distribution areas may have large flat portions. When the skins 301, 302 touch flat-on-flat, oftentimes it is more difficult for leakage to overcome the flow resistance. Accordingly, a rib or ribs, e.g., ribs 425, 430, 435, may be formed in one or both skins which create a local separation to carry leakage from the heat transfer area 114 to the vent space 350, 450. Alternatively, small width and small thickness attachments can be made to provide the same effect. The attachments may be permanently attached or removable. The shape and length of ribs or attachments can vary depending on the application.
  • Such separator ribs and attachments e.g., ribs 425, 430, 435, may be formed at any point where there is large flat-to-flat contact.
  • a method 500 of forming a double-walled plate heat exchanger 100 includes forming a first plate (step 510), e.g., plate 110a, including forming a first skin 301, including forming a gasket 120, and forming at least one leakage orifice 315 (step 520).
  • the method 500 further includes forming a second skin 302 (step 530).
  • the leakage orifice 315 is provided as a partial an escape path for leakage between the first and second skins 301, 302.
  • the method 500 further includes forming a second plate in contact with the first skin of the first plate (step 540).
  • the second plate may be similar to the first plate 110a, and will be similarly denoted below as second plate 110.
  • the method 500 further includes forming at least one depression, e.g., indentation 420, in the second skin 302 of the first plate 110a.
  • Said indentation 420 at least partially surrounds the at least one leakage orifice 315 in the first plate 110a such that the first and second skins 301, 302 are separated near the at least one depression (e.g., indentation 420) and the leakage orifice 315 (step 550).
  • Forming the second plate 110b may further include forming a first skin, e.g., first skin 301 and forming a second skin, e.g., second skin 302.
  • Forming the second plate 110b may also include forming at least one separator, e.g., ribs 425, 430, 435, configured to provide separation between the first and second plates 110a, 110b near the at least one separator (step 560).
  • Step 560 may further include providing the at least one separator as part of the escape path for leakage between the first and second skins 301, 302 of the first plate HOa.
  • a method 600 of forming a double-walled plate heat exchanger includes forming a first plate (step 610), e.g., plate 110a, including forming a first skin 301, including forming a gasket 120 (step 620), and forming a second skin 302 (step 630).
  • the method 600 further includes forming a second plate, e.g., plate 110a, in contact with the first skin 301 of the first plate (step 640).
  • Forming the second plate 110b includes forming a first skin, e.g., first skin 301 (step 650), and forming a second skin, e.g., skin 302, which includes forming at least one separator, e.g., ribs 425, 430, 435, configured to provide separation between the first and second plates 110a, 110b near the at least one separator (step 660).
  • the step 660 of forming the at least one separator may include providing at least part of an escape path for leakage between the first and second skins 301 , 302 in the first plate 11 Oa (step 670).
  • FIG. 7 depicts a flow chart of a method of managing a leak in a double- walled plate heat exchanger.
  • the method 700 includes allowing fluid leaked between first and second skins of a first plate in a double-walled plate heat exchanger to exit the double-walled plate heat exchanger via a leakage escape path, the leakage escape path including at least one leakage orifice in the first skin, the first skin further including first and second port holes (step 710).
  • An optional step 720 includes collecting the leaked fluid for analysis and/or disposal, which may be done at a predetermined location on the double-walled plate heat exchanger.
  • the leakage escape path contacts an outer edge of the double-walled plate heat exchanger.
  • the leakage escape path further includes at least one depression in the second skin at least partially surrounding the at least one leakage orifice such that the first and second skins are separated near the at least one depression and the leakage orifice.
  • the leakage escape path further comprises at least one separator in a skin of a second plate configured to provide separation between the first and second plates near the at least one separator.
  • FIG. 8 Another embodiment shown in FIG. 8 includes a double-walled plate heat exchanger 800 having a front plate 805 having a front skin 810 and a back skin 815.
  • the front skin 810 has a small hole 820 above a bridge gasket 825 in a bridge gasket groove 826 near a first port 835.
  • a flow bridge 830 may have no gasket.
  • the front plate 805 may have four ports 835-838 and may be a diagonal flow plate. Fluid may enter through one port, e.g., port 836, flow through a center section 839, and exit via a diagonally-opposite port, e.g., port 838.
  • the back skin 815 may have supporting separators 840 ridges pressed into it.
  • the separators 840 may be ridges pressed upwards toward where the bridge gasket groove 826 of the front skin 810 will be when the double-walled plate heat exchanger 800 is assembled.
  • the separators 840 may also be formed by attaching another object to the front skin 810. These separators 840 maintain a gap between the two skins 810, 815 when the skins 810, 815 are pressed together upon assembly. If any puncture occurs through either the first skin 810 or the second skin 815, fluid passes between the skins 810, 815. It can flow upwards, through a small inherent internal space between the skins 810, 815, until it reaches the bridge gasket groove 826.
  • the gap forms a channel between the skins 810, 815, and collects fluid from a backside 870 of the front skin 810 behind the center section 839 over the entire distance of a flow width of the front plate 805, and conducts that fluid all the way through to a depression 845 in the second skin 815.
  • the depression 845 may be located directly underneath the hole 820 in the first skin 810.
  • the backside 870 of the front skin 810 and front center 871 of the back skin 815 will be in contact upon assembly. Unless there is a leak, there will be no fluid in the space between the backside 870 of the front skin 810 and front center 871 of the back skin 815
  • the fluid can rise up through the hole 820 of the first skin 805, and then pass out through a leakage cutaway groove 848 of the gasket 850 and exit externally at an outer edge 855 of the front plate 805.
  • the front plate 805 may also have a groove depression 860 an outer side wall of the groove 848, so there is a clear leakage slot allowing fluid to pass through to the outside.
  • Each item applied to the area near the first port 835, e.g., the hole 820, and the separators 840, is also applied to the third port 837. Fluid can emerge from the front plate 805, either from the first leakage groove 845 near the first port 835 or a second hole 846 and second leakage groove 847 from the third port 837.
  • Each item described as being on the front plate 805 may be included in a back plate 880 having four ports 885-888, except each is applied to the diagonally opposite ports, e.g., instead of to the first and third ports, they are applied to the second and fourth ports, e.g., ports 886, 888.
  • the double-walled plate heat exchanger 900 includes a front plate 905 having front and back skins 910, 915 and four ports 916-919.
  • the features applied in FIG. 8 to the areas near the first and third ports 835, 837 are applied instead to areas near the second and fourth ports 917, 919 of the plate 905.
  • the front skin 910 may have at least one separator 920 formed on the flow port side of the plate in a flow bridge 925.
  • the separators 920 may be made by pressing into the front skin 910 or by attaching another object to the front skin 910 to maintain separation of the flow bridge 925 from its mating back skin bridge gasket 930.
  • Fluid may collect from a backside 970 of the front skin 910 behind a center section 939 over the entire distance of a flow width of the front plate 905, and be conducted all the way through to a hole 935 in the second skin 915.
  • the backside 970 of the front skin 910 and front center 971 of the back skin915 will be in contact upon assembly. Unless there is a leak, there will be no fluid in the space between the backside 970 of the front skin 910 and front center 971 of the back skin 915
  • the back skin 915 has a leakage hole 935. This permits liquid to flow out from between the skins 910, 915. Liquid may emerge and instead flow back from the back skin 915, and leak toward the next plate 950.
  • the next plate 950 may have a leakage groove 955 in a gasket 960. So again, the liquid leaks out externally. Fluid from the front plate 905 would emerge from a gasket leakage grove 955 in the next plate 950.
  • the back skin may have its own separators 980, similarly to the front skin separators 920.

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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)

Abstract

La présente invention concerne un échangeur de chaleur à plaque à double paroi et un procédé de gestion associé, l'échangeur comprenant : une première plaque, comprenant une première peau ; une seconde peau ; au moins deux orifices ; et une voie d'échappement de fuite, entre les première et deuxième peaux, pour permettre au liquide fuyant de sortir de l'échangeur de chaleur à plaque à double paroi, la voie d'échappement de fuite étant en contact avec un orifice de fuite dans l'une des peaux, et un bord externe de l'échangeur de chaleur à plaque à double paroi. La première plaque comprend en outre une seconde plaque en contact avec la seconde peau.
PCT/US2010/036106 2009-05-28 2010-05-26 Echangeur de chaleur à plaque à double paroi amélioré WO2010138526A1 (fr)

Priority Applications (3)

Application Number Priority Date Filing Date Title
EP10781104.4A EP2435774B1 (fr) 2009-05-28 2010-05-26 Echangeur de chaleur à plaque à double paroi
DK10781104.4T DK2435774T3 (en) 2009-05-28 2010-05-26 DOUBLE WALLED PLATE HEAT EXCHANGERS
CN201080023585.9A CN102449420B (zh) 2009-05-28 2010-05-26 改进的双壁板式热交换器

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US12/473,945 US20100300651A1 (en) 2009-05-28 2009-05-28 Double-walled plate heat exchanger
US12/473,945 2009-05-28

Publications (1)

Publication Number Publication Date
WO2010138526A1 true WO2010138526A1 (fr) 2010-12-02

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PCT/US2010/036106 WO2010138526A1 (fr) 2009-05-28 2010-05-26 Echangeur de chaleur à plaque à double paroi amélioré

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US (1) US20100300651A1 (fr)
EP (1) EP2435774B1 (fr)
CN (1) CN102449420B (fr)
DK (1) DK2435774T3 (fr)
WO (1) WO2010138526A1 (fr)

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US9163882B2 (en) 2011-04-25 2015-10-20 Itt Manufacturing Enterprises, Inc. Plate heat exchanger with channels for ‘leaking fluid’
WO2013061966A1 (fr) * 2011-10-24 2013-05-02 株式会社日阪製作所 Échangeur de chaleur à plaques
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CN106052432B (zh) * 2016-04-27 2017-12-19 中石化石油机械股份有限公司研究院 具有交叉流道的微通道换热器
CN107917629B (zh) * 2016-10-11 2020-12-18 恒丰工程（香港）有限公司 双壁板板壳式换热器及其专用双壁换热板
JP6862773B2 (ja) * 2016-11-07 2021-04-21 株式会社デンソー 熱交換器
JP6911469B2 (ja) * 2017-03-31 2021-07-28 株式会社Ihi 熱処理装置
EP3489606A1 (fr) * 2017-11-22 2019-05-29 Danfoss A/S Plaque de transfert de chaleur pour échangeur de chaleur à plaque et échangeur de chaleur à plaque la comportant
CN110186300B (zh) * 2019-06-27 2024-10-15 浙江银轮机械股份有限公司 板片、板片组件及热交换器

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Publication number Publication date
EP2435774B1 (fr) 2018-11-28
US20100300651A1 (en) 2010-12-02
EP2435774A1 (fr) 2012-04-04
EP2435774A4 (fr) 2014-12-31
CN102449420B (zh) 2016-03-30
DK2435774T3 (en) 2019-03-11
CN102449420A (zh) 2012-05-09

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