WO1987001795A1 - Plate heat exchanger - Google Patents

Plate heat exchanger Download PDF

Info

Publication number
WO1987001795A1
WO1987001795A1 PCT/SE1986/000410 SE8600410W WO8701795A1 WO 1987001795 A1 WO1987001795 A1 WO 1987001795A1 SE 8600410 W SE8600410 W SE 8600410W WO 8701795 A1 WO8701795 A1 WO 8701795A1
Authority
WO
WIPO (PCT)
Prior art keywords
plate
heat exchanger
distance means
plates
channel
Prior art date
Application number
PCT/SE1986/000410
Other languages
French (fr)
Inventor
Jarl Andersson
Jan-Ove Bergqvist
Original Assignee
Alfa-Laval Thermal Ab
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 Alfa-Laval Thermal Ab filed Critical Alfa-Laval Thermal Ab
Priority to BR8607187A priority Critical patent/BR8607187A/en
Priority to AT86905973T priority patent/ATE59466T1/en
Priority to DE8686905973T priority patent/DE3676709D1/en
Publication of WO1987001795A1 publication Critical patent/WO1987001795A1/en

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
    • F28F3/083—Elements constructed for building-up into stacks, e.g. capable of being taken apart for cleaning capable of being taken apart

Definitions

  • This invention relates to a plate heat exchanger comprising heat exchange plates mounted between a frame plate and a pressure plate in a frame, the heat exchange plates between themselves forming channels for heat exchange media which are introduced into and taken out of the channels via ports in the corner portions of the plates, and each heat exchange plate having two distributing areas and an intermediate heating area and a plate pattern of turbulence generating and distance-giving means, pressed out of the plate.
  • Such a heat exchanger is common today for heat exchange between two media of different temperatures.
  • a plate heat exchanger which is preferably intended for a high-viscous medium and/or a medium mixed with fibers.
  • the channels of the heat exchanger have to be designed in a special way.
  • the inlet of the channels at the plate ports must have such a design that a free inflow of the medium into the channel is allowed.
  • Plates in known plate heat exchangers in a known way, have a plate pattern comprising turbulence generating and distance giving means also at the area of the ports.
  • the plate has been so designed at the ports that when these ones have been cut out of the plate through the turbulence generating and distance giving means, the inlet of each channel, when two plates have been put together, has been comp ' osed of a number of cell-like openings.
  • These cell-like openings have formed sharp edges for the inflowing medium, the consequence of which should be that, if a medium containing fibers is used, these fibers should fasten in the cell walls and shut off the inlet of the channels.
  • the cell-like openings into the channel would be too narrow for a high-viscous medium.
  • the object of this invention is to design the plates forming the channel ⁇ in that way that the media can stream relatively freely through respective channels.
  • the object is achieved in a plate heat exchanger of the kind mentioned by way of introduc ⁇ tion, which is characterized in that the two ports delimiting the inlet to each channel at least for one of the media are so designed in the two adjacent plates delimiting the mentioned channel that the one port is positioned in the bottom plane of the one plate and the other port is positioned in the top plane of the other plate.
  • Fig. 1 shows a heat exchange plate according to the invention
  • Fig. 2 shows a section along the line II-II in Fig. 1 with the presumption that several plates are placed under that plate and
  • Fig. 3 shows a section along the line III-III in Fig. 1 with the presumption that several plates are placed under that plate.
  • the plate 1 in Fig. 1 is in a known way provided with four ports 2a-d for the media that shall be heat exchanged. Furthermore, the plate is provided with two distributing areas 3, 4 and a heating area 5. This heating area 5 is provided with particular distance means in the form of several ridges 6a-d which are parallel in relation to each other and symmetrically placed in relation to the longitudinal center line of the plate and extend in the longitudinal direction of the plate along essentially the whole heating area.
  • this distance means has a height exceeding the height of the distance means in the ordinary plate pattern, there is formed, when putting this plate and a conven ⁇ tional one without the particular distance means together, on the former one's upper side a channel having a sufficient width for a high-viscous medium and/or a medium mixed with fibers.
  • the ridges 6a-d are preferably positioned on only one side of the plate 1 and can be composed of folds which have been pressed out of the plate material.
  • the ridges can be composed of loose parts which are welded or soldered to the plate.
  • the press pattern is so designed that a part of the distance means is given a height corresponding to the height of the distance means 6a-d. Further ⁇ more, at least a part of the distance means 7 in the inlet portions and outlet portions of the channels, i.e. in the area close to the plate ports, has also a height corresponding to the height of the distance means 6a-d. Due to that fact the distance between the plates can be guaranteed also in the passage of the distributing surfaces and at the area close to the plate ports.
  • the distance means 7, 10 are placed a short distance from the port edge 8, 9.
  • This fact and the placing of the ports in bottom plane and top plane, respectively, have the consequence that there is formed a soft transfer passage without sharp edges for the viscous medium from the port channel and into the channel between the plates 8, 9. Due to that fact the inflow of the viscous medium into the channel is still more facilitated.
  • the distance means 7 of the press pattern of the one plate rests against the distance means 10 of the press pattern of the other plate, whereby the distance means form contact points between the plates In the area close to the plate ports.
  • the invention is, of course, not limited to the mentioned embo ⁇ diment.
  • the inlets to the channels for both media shall be as wide as possible.
  • the port of the one plate shall be placed in its bottom plane and the port of the adjacent plate in its top plane, that the distance means of the press pattern of the plates being opposite to each other shall have essentially the same height.
  • the distance means 6 can also be unsymmetrically placed in relation to the longitudinal center line of the plate, whereby the plate becomes mixable with itself.
  • a heat exchanger built up by such plates should be particularly suitable to use when the two media are high-viscous.
  • the special design of the plates at the area of the ports makes the heat exchanger particularly suitable to be used for media which are contaminated in different ways, for instance by fibers.

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)
  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

Plate heat exchanger comprising heat exchange plates mounted between a frame plate and a pressure plate in a frame, the heat exchange plates between themselves forming channels for heat exchange media which are introduced into and taken out of the channels via ports in the corner portions of the plates, and each heat exchange plate having two distributing areas and an intermediate heating area and a plate pattern of turbulence generating and distance giving means, pressed out of the plate. According to the invention the two ports (8, 9) delimiting the inlet to each channel at least for one of the media are so designed in the two adjacent plates delimiting the mentioned channel that the one port (8) is positioned in the bottom plane of the one plate and the other port (9) is positioned in the top plane of the other plate.

Description

Plate heat exchanger
This invention relates to a plate heat exchanger comprising heat exchange plates mounted between a frame plate and a pressure plate in a frame, the heat exchange plates between themselves forming channels for heat exchange media which are introduced into and taken out of the channels via ports in the corner portions of the plates, and each heat exchange plate having two distributing areas and an intermediate heating area and a plate pattern of turbulence generating and distance-giving means, pressed out of the plate.
Such a heat exchanger is common today for heat exchange between two media of different temperatures.
However, there is a need in the market for a plate heat exchanger, which is preferably intended for a high-viscous medium and/or a medium mixed with fibers. In order to manage a heat exchange where at least one of the media is high-viscous and/or mixed with fibers, the channels of the heat exchanger have to be designed in a special way. Thus, particularly the inlet of the channels at the plate ports must have such a design that a free inflow of the medium into the channel is allowed.
Plates in known plate heat exchangers, in a known way, have a plate pattern comprising turbulence generating and distance giving means also at the area of the ports. In this connectio the plate has been so designed at the ports that when these ones have been cut out of the plate through the turbulence generating and distance giving means, the inlet of each channel, when two plates have been put together, has been comp'osed of a number of cell-like openings. These cell-like openings have formed sharp edges for the inflowing medium, the consequence of which should be that, if a medium containing fibers is used, these fibers should fasten in the cell walls and shut off the inlet of the channels. Moreover, the cell-like openings into the channel would be too narrow for a high-viscous medium.
The object of this invention is to design the plates forming the channelβ in that way that the media can stream relatively freely through respective channels. The object is achieved in a plate heat exchanger of the kind mentioned by way of introduc¬ tion, which is characterized in that the two ports delimiting the inlet to each channel at least for one of the media are so designed in the two adjacent plates delimiting the mentioned channel that the one port is positioned in the bottom plane of the one plate and the other port is positioned in the top plane of the other plate.
A preferred embodiment of the invention usable for heat exchange of media of which one is high-viscous shall be described more closely in connection with the accompanying drawings, in which
Fig. 1 shows a heat exchange plate according to the invention,
Fig. 2 shows a section along the line II-II in Fig. 1 with the presumption that several plates are placed under that plate and
Fig. 3 shows a section along the line III-III in Fig. 1 with the presumption that several plates are placed under that plate.
The plate 1 in Fig. 1 is in a known way provided with four ports 2a-d for the media that shall be heat exchanged. Furthermore, the plate is provided with two distributing areas 3, 4 and a heating area 5. This heating area 5 is provided with particular distance means in the form of several ridges 6a-d which are parallel in relation to each other and symmetrically placed in relation to the longitudinal center line of the plate and extend in the longitudinal direction of the plate along essentially the whole heating area. Since this distance means has a height exceeding the height of the distance means in the ordinary plate pattern, there is formed, when putting this plate and a conven¬ tional one without the particular distance means together, on the former one's upper side a channel having a sufficient width for a high-viscous medium and/or a medium mixed with fibers.
The ridges 6a-d are preferably positioned on only one side of the plate 1 and can be composed of folds which have been pressed out of the plate material.
Instead of being an integral part of the plate, the ridges can be composed of loose parts which are welded or soldered to the plate.
In the distributing surfaces 3, 4 the press pattern is so designed that a part of the distance means is given a height corresponding to the height of the distance means 6a-d. Further¬ more, at least a part of the distance means 7 in the inlet portions and outlet portions of the channels, i.e. in the area close to the plate ports, has also a height corresponding to the height of the distance means 6a-d. Due to that fact the distance between the plates can be guaranteed also in the passage of the distributing surfaces and at the area close to the plate ports.
As has been previously mentioned the plates in previously known plate heat exchangers have been so designed at the area of the ports that the inlet of the channels has been composed of a cell pattern with sharp edges. There have been at least two drawbacks connected therewith. Firstly, these sharp edges results in that a medium containing fibers easily closes up the inlet of the channels. Secondly, these cells bring about a very limited inlet area, wherefore a high-viscous medium should meet a great resistance when flowing into the channels via these cells. These problems are solved according to the invention, the inlet getting the greatest possible width. This is brought about, as appears from Fig. 3, by giving the plates a special design at the area of the ports. Thus, the port of one of the plates (8 shows the inner edge of the port), in this case the plate provided with the particular distance ridges, is placed in the bottom plane of the plate,^ while the port of the adjacent plate (9 shows the inner edge of the port) is placed in its top plane. Due to that fact the distance between the ports of the two plates, during co-operation of the distance means 7, 10 of the two plates, will be as great as possible. This has the conse¬ quence that the inlet to the channel for the viscous medium becomes as great as possible, whereby the inflow into the channel is facilitated. In Fig. 3 the viscous medium has been indicated by two arrows 11, 12.
The mentioned placing of the ports in the two plates delimiting a channel for the viscous medium results in that the plates 9, 8 rest against each other at the port area between two inlets to the channels for the viscous medium.
As has been shown in Fig. 3 the distance means 7, 10 are placed a short distance from the port edge 8, 9. This fact and the placing of the ports in bottom plane and top plane, respectively, have the consequence that there is formed a soft transfer passage without sharp edges for the viscous medium from the port channel and into the channel between the plates 8, 9. Due to that fact the inflow of the viscous medium into the channel is still more facilitated.
Furthermore, from Fig. 3 is apparent that the distance means 7 of the press pattern of the one plate rests against the distance means 10 of the press pattern of the other plate, whereby the distance means form contact points between the plates In the area close to the plate ports. The invention is, of course, not limited to the mentioned embo¬ diment. Thus, it is possible to have two high-viscous media of essentially the same viscosity which shall be heat exchanged. In this case the inlets to the channels for both media shall be as wide as possible. This means, besides the fact that the port of the one plate shall be placed in its bottom plane and the port of the adjacent plate in its top plane, that the distance means of the press pattern of the plates being opposite to each other shall have essentially the same height.
The distance means 6 can also be unsymmetrically placed in relation to the longitudinal center line of the plate, whereby the plate becomes mixable with itself. A heat exchanger built up by such plates should be particularly suitable to use when the two media are high-viscous.
,_•
The special design of the plates at the area of the ports makes the heat exchanger particularly suitable to be used for media which are contaminated in different ways, for instance by fibers.

Claims

Claims
1. A plate heat exchanger comprising heat exchange plates mounted between a frame plate and a pressure plate in a frame, the heat exchange plates between themselves forming channels for heat exchange media which are introduced into and taken out of the channels via ports in the corner portions of the plates, and each heat exchange plate having two distributing areas and an intermediate heating area and a plate pattern of turbulence generating and distance giving means, pressed out of the plate, c h a r a c t e r i z e d I n that the two ports (8, 9) delimiting the inlet to each channel at least for one of the media are so designed in the two adjacent plates delimiting the mentioned channel that the one port (8) is positioned in the bottom plane of the one plate and the other port (9) is posi¬ tioned in the top plane of the other plate.
2. A plate heat exchanger according to claim 1, c h a r a c ¬ t e r i z e d i n that at least the one plate (1) in a channel has distance means (6a-d) comprising ridges extending in the longitudinal direction of the plate along essentially the whole length of the heating area, and that the distance means (6a-d) is pressed out of the plate material.
3. A plate heat exchanger according to claim 1, c h a r a c ¬ t e r i z e d i n that at least the one plate (1) in a channel has distance means (6a-d) comprising ridges extending in the longitudinal direction of the plate along essentially the whole length of the heating area, and that the distance means is composed of loose parts welded or soldered to the plate.
4. A plate heat exchanger according to claim 2 or 3, c h a r a c t e r i z e d i n that a part of the ridges in the distributing areas (3, 4) has a height corresponding to the height of the distance means (6a-d).
5. A plate heat exchanger according to any one of the claims 2-4, c h a r a c t e r i z e d i n that the press pattern in the area close to the plate ports has distance means (7) with a height corresponding to the height of the distance means in the heating area.
6. A plate heat exchanger according to any one of the claims 2-5, c h a r a c t e r i z e d i n that the distance means (6a-d; 7) has a height exceeding the height of the distance means (10) in the ordinary plate pattern.
7. A plate heat exchanger according to claim 2 or 3, c h a r a c t e r i z e d i n that the distance means (6a-d) in the heating area is symmetrically placed in relation to the longitudinal center line of the plate.
8. A plate heat exchanger according to claim 2 or 3, c h a r a c t e r i z e d i n that the distance means (6a-d) in the heating surface is unsymmetrically placed in relation to the longitudinal center line of the plate.
9. A plate heat exchanger according to claim 6, c h a r a c ¬ t e r i z e d i n that the distance means (7, 10) closest to the port area in the two plates forming a channel for a viscous medium is placed a distance from the port edge (8, 9), whereby a soft transfer passage is formed for the medium from the port channel and into the channel between the plates.
PCT/SE1986/000410 1985-09-23 1986-09-12 Plate heat exchanger WO1987001795A1 (en)

Priority Applications (3)

Application Number Priority Date Filing Date Title
BR8607187A BR8607187A (en) 1985-09-23 1986-09-12 PLATE HEAT EXCHANGER
AT86905973T ATE59466T1 (en) 1985-09-23 1986-09-12 PLATE HEAT EXCHANGER.
DE8686905973T DE3676709D1 (en) 1985-09-23 1986-09-12 HEAT EXCHANGER.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
SE8504379-2 1985-09-23
SE8504379A SE8504379D0 (en) 1985-09-23 1985-09-23 PLATTVEMEVEXLARE

Publications (1)

Publication Number Publication Date
WO1987001795A1 true WO1987001795A1 (en) 1987-03-26

Family

ID=20361475

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/SE1986/000410 WO1987001795A1 (en) 1985-09-23 1986-09-12 Plate heat exchanger

Country Status (7)

Country Link
US (1) US4911235A (en)
EP (1) EP0272266B1 (en)
JP (1) JP2634046B2 (en)
BR (1) BR8607187A (en)
DE (1) DE3676709D1 (en)
SE (1) SE8504379D0 (en)
WO (1) WO1987001795A1 (en)

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WO1993006426A1 (en) * 1991-09-16 1993-04-01 Apv Corporation Limited Plate heat exchanger
WO1997039301A1 (en) * 1996-04-16 1997-10-23 Alfa Laval Ab A plate heat exchanger
WO2002053998A1 (en) * 2001-01-04 2002-07-11 Alfa Laval Corporate Ab Heat transfer plate, plate pack and plate heat exchanger
WO2009154543A1 (en) * 2008-06-17 2009-12-23 Alfa Laval Corporate Ab Heat exchanger
US8272430B2 (en) 2007-07-23 2012-09-25 Tokyo Roki Co., Ltd. Plate laminate type heat exchanger
CN103759474A (en) * 2014-01-28 2014-04-30 丹佛斯微通道换热器（嘉兴）有限公司 Plate heat exchanger
US8794303B2 (en) 2007-07-23 2014-08-05 Tokyo Roki Co., Ltd. Plate laminate type heat exchanger

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US5179999A (en) * 1989-11-17 1993-01-19 Long Manufacturing Ltd. Circumferential flow heat exchanger
DE4142177C2 (en) * 1991-12-20 1994-04-28 Balcke Duerr Ag Plate heat exchanger
SE470339B (en) * 1992-06-12 1994-01-24 Alfa Laval Thermal Flat heat exchangers for liquids with different flows
SE505225C2 (en) * 1993-02-19 1997-07-21 Alfa Laval Thermal Ab Plate heat exchanger and plate for this
US5555933A (en) * 1994-07-14 1996-09-17 Solar Turbines Incorporated Primary surface heat exchanger for use with a high pressure ratio gas turbine engine
SE518276C2 (en) * 1997-12-19 2002-09-17 Swep Int Ab plate heat exchangers
DK174409B1 (en) * 1998-01-12 2003-02-17 Apv Heat Exchanger As Heat exchanger plate with reinforced edge design
JP3292128B2 (en) * 1998-02-27 2002-06-17 ダイキン工業株式会社 Plate heat exchanger
AUPP410598A0 (en) 1998-06-15 1998-07-09 Aos Pty Ltd Heat exchangers
US6244333B1 (en) 1998-08-27 2001-06-12 Zeks Air Drier Corporation Corrugated folded plate heat exchanger
US6186223B1 (en) 1998-08-27 2001-02-13 Zeks Air Drier Corporation Corrugated folded plate heat exchanger
US6357113B1 (en) 1999-11-04 2002-03-19 Williams International Co., L.L.C. Method of manufacture of a gas turbine engine recuperator
DE10035939A1 (en) * 2000-07-21 2002-02-07 Bosch Gmbh Robert Heat transfer device
SE519306C2 (en) * 2001-07-09 2003-02-11 Alfa Laval Corp Ab Heat transfer plate, plate package and plate heat exchanger
GB0210434D0 (en) * 2002-05-08 2002-06-12 Smiths Group Plc Apparatus
DE10228263A1 (en) * 2002-06-25 2004-01-22 Behr Gmbh & Co. Plate heat exchanger in stack construction
KR100581843B1 (en) * 2005-05-09 2006-05-22 대원열판(주) Structure for combining heat plate with gasket of a plate type heat exchanger
GB2429054A (en) * 2005-07-29 2007-02-14 Howden Power Ltd A heating surface element
JP2007178010A (en) * 2005-12-27 2007-07-12 Calsonic Kansei Corp Inner fin for heat exchanger
US20070261833A1 (en) * 2006-05-09 2007-11-15 Kaori Heat Treatment Co., Ltd. Heat exchanger having different flowing paths
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US9389028B2 (en) * 2010-07-08 2016-07-12 Swep International Ab Plate heat exchanger
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US20140076527A1 (en) * 2012-09-20 2014-03-20 Airia Leasing Inc. Planar plate core and method of assembly
CN107449310B (en) 2013-09-19 2020-03-24 豪顿英国有限公司 Heat exchange element profile with enhanced cleanability features
EP3306253B1 (en) * 2016-10-07 2019-04-10 Alfa Laval Corporate AB Heat exchanging plate and heat exchanger
ES2966217T3 (en) * 2017-03-10 2024-04-19 Alfa Laval Corp Ab Plate for a heat exchanger device
US10876794B2 (en) * 2017-06-12 2020-12-29 Ingersoll-Rand Industrial U.S., Inc. Gasketed plate and shell heat exchanger
US11486657B2 (en) 2018-07-17 2022-11-01 Tranter, Inc. Heat exchanger heat transfer plate
CN110545646B (en) * 2019-08-26 2020-06-19 江苏宝得换热设备股份有限公司 Condenser
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Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1993006426A1 (en) * 1991-09-16 1993-04-01 Apv Corporation Limited Plate heat exchanger
US5522462A (en) * 1991-09-16 1996-06-04 Apv Corporation Limited Plate heat exchanger
WO1997039301A1 (en) * 1996-04-16 1997-10-23 Alfa Laval Ab A plate heat exchanger
WO2002053998A1 (en) * 2001-01-04 2002-07-11 Alfa Laval Corporate Ab Heat transfer plate, plate pack and plate heat exchanger
US7168483B2 (en) 2001-01-04 2007-01-30 Alfa Laval Corporate Ab Heat transfer plate, plate pack and plate heat exchanger
CN1299091C (en) * 2001-01-04 2007-02-07 阿尔法·拉瓦尔股份公司 Heat transfer plate, plate pack and plate heat exchanger
US8272430B2 (en) 2007-07-23 2012-09-25 Tokyo Roki Co., Ltd. Plate laminate type heat exchanger
US8794303B2 (en) 2007-07-23 2014-08-05 Tokyo Roki Co., Ltd. Plate laminate type heat exchanger
WO2009154543A1 (en) * 2008-06-17 2009-12-23 Alfa Laval Corporate Ab Heat exchanger
US9518782B2 (en) 2008-06-17 2016-12-13 Alfa Laval Corporated Ab Heat exchanger
EP2304369B1 (en) * 2008-06-17 2018-11-14 Alfa Laval Corporate AB Heat exchanger
CN103759474A (en) * 2014-01-28 2014-04-30 丹佛斯微通道换热器（嘉兴）有限公司 Plate heat exchanger

Also Published As

Publication number Publication date
JPS63501030A (en) 1988-04-14
BR8607187A (en) 1988-09-13
JP2634046B2 (en) 1997-07-23
SE8504379D0 (en) 1985-09-23
US4911235A (en) 1990-03-27
EP0272266A1 (en) 1988-06-29
EP0272266B1 (en) 1990-12-27
DE3676709D1 (en) 1991-02-07

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