Title of Invention

A METHOD OF MANUFACTURING A PLATE HEAT EXCHANGER

Abstract

The present invention relates to a manufacturing brazed, double wall plate heat exchangers the double walls (5, 6) should comprise areas (5a, 5b) connected and sealed to each other around the port holes of the exchanger. This is obtained thereby that the said areas (5a, 5b) are shaped such as to comprise areas not covering each other. The brazing is thus established by capillary suction of brazing material from other plate areas.

Full Text

A Method of Manufacturing a Plate Heat Exchanger Technical Field of the Invention This invention relates to a method of manufacturing a plate heat exchanger in which each heat exchanging plate is designed as a double wall. In many applications this is specified by regulations in order to avoid that a leakage of a plate may cause one fluid medium to enter into the path of another fluid with which it should exchange heat and which might be used for human consumption. Any leakage through one of the two walls of a double walled heat exchanger plate may be detected by draining the leakage between the two walls towards the periphery of the double walled heat exchanger plate. The Prior Art In most compact plate heat exchangers a number of stacked plates separating the flows exchanging heat are made of stainless steel and interconnected by brazing using copper or nickel as brazing material. The brazing is commonly performed by providing all plates to be sealed and connected to another plate with a thin sheet of brazing material on one side of the plate. The plates are subsequently stacked and heated in a vacuum oven to a temperature sufficient to cause brazing. A plate heat exchanger of the type equipped with plates having double walls has been shown as Figs. 1 and 2 in the attached drawings, and as an example of a prior art patent specification reference could be made to WO Oil 165 44 Al. A problem presently found in the manufacture of brazed, double wall, compact plate heat exchangers is to provide a reliable sealing around port holes in the plates preventing the flow passing the port hole from entering into the path of one or more other flows of medium passing the exchanger as well as into the small space between the double walls. The prior use of brazing material may cause unintended brazing connections between the two walls of a double wall at locations making it possible that leakage through the double wall may follow a path not leading to the space between the two walls for draining the leaking fluid to the periphery of the exchanger and - therefore - being impossible to detect. SUBSTITUTE SHEET (RULE 26) Object of the Invention The object of the present invention is to provide a method of manufacturing a brazed, double wall heat exchanger in which the brazing material will be prevented from entering into the spaces between the two walls of any of the heat exchanger plates to such extent that it will prevent leakage of fluid through one of the double walls from entering the outwardly drained space between the two walls. Brief Description of the Invention The above object is achieved by a method in which a plate heat exchanger comprising a plurality of stacked plates limiting two ore more separate fluids exchanging heat across the said plates, and in which the said plates are of double wall design so as to prevent a fluid which might leak through a wall of the plates from entering into the path of another fluid, the double walls of each of the said plates being sealingly interconnected around borders of port holes in the plates - and which method according to the present invention is characterized in that each of the double walled plates of the exchanger prior to a brazing operation is provided with brazing material on a surface engaging another double walled plate, and that the areas of the mutually contacting wall surfaces of the two plates forming a double wall plate around borders of a port hole are designed so as to only partly cover each other. The invention will be described below reference being made to the accompanying drawings. Contents of the Drawings Fig. 1 is a schematic, exploded, perspective view of a plate heat exchanger of known design in which the heat exchanging plates have double walls and in which all parts of the exchanger are adapted to be interconnected by brazing. SUBSTITUTE SHEET (RULE 26) Fig. 2 at a greater scale is a section of an exchanger of the type shown in Fig. 1, the section being taken in the direction of the arrows A-A in Fig. 1. Fig. 3 at a larger scale is a plan view in the direction of the arrows B-B in Fig. 2 of a part of a stack of heat exchanging plates of an exchanger manufactured according to the invention, the part surrounding a port hole. Fig. 4 at a still larger scale is a vertical section indicated by the arrows Bl-Bl of Fig. 3 prior to heating for brazing. Fig. 5 is a vertical section indicated by the arrows B2-B2 of Fig.3 prior to heating for brazing Fig. 6 corresponds to Fig. 4, but shows the condition after brazing. Fig.7 corresponds to Fig. 5, but shows the condition after brazing. Fig. 8 shows an alternative to the exchanger shown in Fig, 3 Fig. 9 is a vertical section indicated by the arrows Cl-Cl of Fig. 8 prior to heating for brazing. Fig. 10 is a vertical section indicated by the arrows C2-C2 of Fig.8 prior to heating for brazing. Fig. 11 corresponds to Fig. 9, but shows the condition after brazing. Fig. 12 corresponds to Fig. 10, but shows the condition after brazing. Fig. 13 shows a further embodiment of an alternative to the one shown in Fig.3. Fig 14 is a section indicated by the arrows D-D in Fig. 13 prior to heating for brazing. SUBSTITUTE SHEET (RULE 26) Fig 15 is a section indicated by the arrows D-D in Fig. 13 after heating for brazing. Fig. 16 shows a still further embodiment of an alternative to the one shown in Fig.3. Fig 17 is a section indicated by the arrows El-El in Fig. 16 prior to heating for brazing. Fig 18 is a section indicated by the arrows E2-E2 in Fig. 16 prior to heating for brazing. Fig 19 is a section indicated by the arrows El-El in Fig. 16 after heating for brazing. Fig 20 is a section indicated by the arrows E2-E2 in Fig. 16 after heating for brazing. Detailed Description of the Drawings The basic design of a two circuit plate heat exchanger is schematically shown in Fig.l. The exchanger comprises two end plates 1 and 2, two flow guiding plates 3 and 4, and four heat exchanging plates 5-8. The plates 3-8 are provided with pressed patterns of ridges and depressions forming herring bone designs. In order to explain the two circuits of the exchanger the plates 1-8 are shown separated as an exploded view in Fig.l. The end plate 1 is provided with an inlet opening 9 and an outlet opening 10 for a heating fluid as well as an inlet opening 11 and an outlet opening 12 for a fluid to be heated. The heating fluid is separately passed through the end plate 1 and the flow guiding plate 3 via port holes - which because of the exploded view are illustrated as a tube. A part of this heating fluid may now pass upwards between the plates 3 and 5 and subsequently to the outlet opening 10 at the end plate 1. The rest of the heating fluid is passed to the spaces between the plates 6 and 7 or between the plates 8 and 4 and is subsequently passed to the outlet opening 10. The flow to be heated is in a similar way supplied via the inlet opening 11 and passed through the space between the plates 5 and 6, or through the space between the plates 7 and 8 and is subsequently passed to the outlet opening 12. It will be understood that heat may be exchanged between the two flows of fluid via the plates 5-8. As explained above regulations may often require use of double walls SUBSTITUTE SHEET (RULE 26) (not shown in Fig. 1) in the exchanger plates 5-8 in case one of the two flows is used for consumption. Fig. 2 is a section indicated by the arrows A-A in Fig.l. Fig. 2 shows the inlet opening 9 for the heating fluid and the outlet opening 12 for the heated fluid and how the plates 3-8 guiding the two flows of fluid are contacting each other to form a stack of plates of equal size and shape, but in which each other plate in the stack is turned 180 degrees in its plane relative to the neighboring plates. The double walls of the plates 5-8 are shown with thick lines. In Fig. 3 - which at a larger scale in the direction of the arrows B-B in Fig. 2 is a plan view of a part of a stack of heat exchanger plates in a heat exchanger according to the invention, said part surrounding a port hole - the reference numeral 13 indicates the border of the port opening in the plate 5 connecting the space between the plates 3 and 5 with the space between the plates 6 and 7. The plates 5 and 6 should be sealed and brazed together along a ring shaped contact area around the border 13 of the port opening. In Figs. 4 and 5, which are sections indicated by the arrows Bl-Bl, resp. the arrows B2-B2 of Fig. 3, the plate 5 is shown as composed of two walls 5a and 5b contacting each other except for areas of the wall 5a being provided with four indentations 14 and areas of the wall 5b provided with four indentations 15. As shown in Figs. 4 and 5 the lower sides of the plates 5-8 are provided with a thin foil of brazing material - e.g. copper or nickel - illustrated as thick lines. It should be noted that no foil of brazing material is placed between the adjacent surfaces of two walls -e.g. 5a and 5b - forming a heat exchanger plate. The Figs. 4 and 5 show the stacked plates 5-8 prior to heating in a vacuum oven to effect brazing. The Figs. 6 and 7 correspond to the Figs. 4 and 5 and show how the brazing material has become displaced after conventional treatment in a vacuum oven. The brazing material has almost disappeared from the lower sides of the heat exchanger plates except for the parts thereof contacting an adjacent plate. However, due to capillary suction arising SUBSTITUTE SHEET (RULE 26) where a free surface area continues into a narrow gap between two surfaces, brazing material will enter and provide a seal between the two walls 5a, 5b forming a double wall heat exchanger plate. Such free surface areas are provided by the indentations 14 and 15. The sealing brazing material has been shown by thicker lines also in Figs. 6 and 7. The number of indentations 14 and 15 is a matter of choice and experience. The peripheral distance between them may preferably be less than 5 mm. If desired, small ring shaped foils of brazing material may be placed between the surfaces of the double wall plates contacting each other around port openings, but not to such extent that brazing material could enter into areas in which the double walls have heat exchanging function. In most cases this use of foils of brazing material will not be needed. Fig. 8 is a plan view of a part of a heat exchanger plate corresponding to that of Fig.3 i.e. as shown by the arrows B-B in Fig. 2, but showing an alternative way of providing capillary suction. Figs. 9 and 10 are sections indicated by the arrows Cl-Cl respectively C2-C2 in Fig. 8. The free areas continuing in narrow gaps between two surfaces are provided by four holes 16 in the wall 5a and by four holes 17 in the wall 5b. The Figs. 11 and 12 illustrate how brazing material by capillary suction has entered between the two walls of each heat exchanger plate after melting the brazing material in a vacuum oven according to the traditional way of connecting stacked plates in the manufacture of plate heat exchangers. The brazing material has been shown by thick lines A further example of providing sealing by capillary suction of brazing material has been illustrated in the Figures 13-15. Here it is shown how a port hole border 18 in the wall 5a and a port hole border 19 in the wall 5b are relatively displaced and thus forming the free areas providing the capillary suction. Figs. 14 and 15 are both sections indicated by the arrows D-D i Fig. 13 and they show the location of brazing material prior to respectively after the heating for brazing. A still further example is shown in the Figs. 16-20. Port hole borders 20, 21 in the two walls 5a and 5b forming the exchanger plate 5 are elliptic and placed so as to establish SUBSTITUTE SHEET (RULE 26) free wall areas adjacent to the areas of the walls contacting each other. Figs. 17 and 19 show the distribution of the brazing material prior to respectively after the heating in the brazing oven along the section indicated by the arrows El-El in Fig. 16. Figs. 18 and 20 are corresponding illustrations regarding a section indicated by arrows E2-E2 in Fig. 16. SUBSTITUTE SHEET (RULE 26) Claims 1. A method of manufacturing a plate heat exchanger comprising a plurality of stacked plates (5-8) limiting two ore more separate fluids exchanging heat across the said plates, and in which the said plates (5-8) are of double wall design so as to prevent a fluid which might leak through a wall of the plates (5-8) from entering into the path of another fluid, the double walls of each of the said plates being sealingly interconnected around borders of port holes in the plates (5-8), characterized in that each of the double walled plates (5-8) of the exchanger prior to a brazing operation is provided with brazing material on a surface engaging another double walled plate (5-8), and that the areas of the mutually contacting wall surfaces of the two plates forming a double wall plate around borders (13 Figs. 3 and 8; 18,19 Fig. 13; 20, 21 Fig. 16) of a port hole are designed so as to only partly cover each other. 2. A method according to claim 1, characterized in that the borders (13, Figs. 3-7) of the port holes in walls (5a, 5b) engaging each other in a plate (5) of a plate heat exchanger have equal diameters and are provided with relatively displaced indentations (14, 15). 3. A method according to claim 1, characterised in that the areas around the borders (13; Figs.8-12) of the port holes of two walls (5a, 5b) in a heat exchanger plate (5) are provided with holes (16, 17) said holes (17) in one wall (5a) being angularly displaced relative to said holes (16) in the other wall (5b). 4. A method according to claim 1, characterised in that the two walls (5a, 5b) of a heat exchanger plate are provided with relatively displaced port holes leaving free areas adjacent to contacting surface areas around a port hole opening (Figs. 13-15). SUBSTITUTE SHEET (RULE 26) 5. A method according to claim 1, characterised in that the two holes in a pair of walls forming a port hole in a heat exchanger plate are of elliptic shape and angularly displaced (Figs. 16-20). 6. A plate heat exchange made according to the method defined in any of the proceeding claims Reference List 1 end plate 2 end plate 3-4 flow guiding plate 5a wall of plate 5b wall of plate 5-8 heat exchanging plates 9 inlet opening for heating fluid 10 outlet opening for heating fluid 11 inlet opening for heated fluid 12 outlet opening for heated fluid 13 border of port opening 14-15 indentations 16-17 holes in wall plates 18-21 port hole borders

Documents:

0646-che-2006 abstract-duplicate.pdf

0646-che-2006 claims-duplicate.pdf

0646-che-2006 description (complete)-duplicate.pdf

646-CHENP-2006 ABSTRACT.pdf

646-CHENP-2006 CORRESPONDENCE OTHERS.pdf

646-CHENP-2006 CORRESPONDENCE PO.pdf

646-CHENP-2006 FORM-18.pdf

646-CHENP-2006 POWER OF ATTORNEY.pdf

646-chenp-2006-abstract.pdf

646-chenp-2006-claims.pdf

646-chenp-2006-correspondence-others.pdf

646-chenp-2006-description(complete).pdf

646-chenp-2006-drawings.pdf

646-chenp-2006-form 1.pdf

646-chenp-2006-form 3.pdf

646-chenp-2006-form 5.pdf

646-chenp-2006-pct.pdf