[0001] The present invention relates to a plate heat exchanger of cross-flow type for heat
exchange between different media of which at least one is a gas, wherein the plate
heat exchanger comprises plates with elongated and in various alternating directions
protruding corrugating ridges, wherein the plate heat exchanger has through-flow gaps
for a first medium and through-flow gaps for a second medium, wherein the through-flow
gaps extend cross-wise relative to each other through the plate heat exchanger such
that said first and second medium flow cross-wise relative to each other through said
plate heat exchanger, wherein each plate defines a partition wall between two different
through-flow gaps for different media such that heat transfer between said media occurs
through said plate, wherein the corrugating ridges are situated between two planes,
wherein each plate has two edge portions which are provided in one plane and two other
opposing edge portions which are provided in the other plane, wherein the corrugating
ridges are located inclined or obliquely relative to said edge portions, wherein two
adjacent plates are mounted relative to each other such that two edge portions of
one of the plates and provided in one plane are joined together with two edge portions
of the other plate located in the same plane, while two edge portions of said one
plate and provided in another plane are situated at a distance from two edge portions
of said other plate provided in said another plane, said two edge portions located
at a distance from each other defining outlet and inlet gaps into and from a through--flow
gap defined between the plates, said outlet and inlet gaps having substantially the
same height as said through-flow gap, and wherein two adjacent plates are also mounted
such that the corrugating ridges inclined relative to the edge portions, cross each
other in said through-flow gap.
[0002] Plate heat exchangers of the abovementioned cross-flow type are previously known
from e.g. US, A, 4 099 928. At these prior art plate heat exchangers, separate sealing
means are required to provide sufficient sealing in the corners of said plate heat
exchanger. Such separate sealing means must be exactly adapted to the plate heat exchanger
to obtain the required sealing in its corners, assembly work is required to apply
them and they must be held in position by means of corner rails in a frame structure.
[0003] The object of the present invention has been to provide, at a plate heat exchanger
of the type defined above, a construction at which said separate sealing means can
be deleted. This is arrived at according to the invention by providing the plate heat
exchanger substantially with the characterizing features of subsequent claim 1.
[0004] The plate heat exchanger according to the invention has, inter alia, the following
advantages:
1) since the corrugating ridges cross each other and are inclined relative to the
edge portions, a strong turbulence is generated in the through-flow gaps, which is
advantageous,
2) since the inlet and outlet gaps, when the plates are assembled, have substantially
the same height as the through-flow gaps, restriction of the flow at the inlets and
outlets of the through-flow gaps is avoided,
3) since the plates have corner portions which are joined close to each other, the
plate heat exchanger does not need to be provided with separate sealing means, but
may instead only consist of plates of the same type and located at 90° relative to
each other,
4) since the corner portions, the edge portions and the corrugating ridges are designed
such that the plates simply can be stacked on top of each other and since they are
joined together through soldering, the plate heat exchanger can be manufactured in
a quick and effective soldering process such that it will be gas-tight, and
5) since the corrugating ridges are also joined together through soldering, the plate
heat exchanger is very rigid and durable and separate framworks for obtaining the
required tightness and stability can be completely dispensed with.
[0005] The invention will be further described below with reference to the accompanying
drawings, in which
fig. 1 is a perspective view of a plate heat exchanger according to the invention;
fig. 2 is a perspective view of two plates forming part of the plate heat exchanger
of fig. 1 and facing each other in such first positions in which they can be attached
to each other;
fig. 2a is a front view, partly in section, with the plates facing each other as in
fig. 2;
fig. 2b shows the plates facing each other as in fig. 2a and attached to each other;
fig. 3 is a perspective view of two plates forming part of the plate heat exchanger
of fig. 1 and facing each other in such other positions in which they also can be
attached to each other;
fig. 3a is a front view, partly in section, of the plates facing each other as in
fig. 3;
fig. 3b shows the plates facing each other as in fig. 3a and attached to each other;
fig. 3c is a plan view of a corner portion of a plate before it is bent;
fig. 3d is a plan view of the same corner portion of the plate after bending thereof;
fig. 3e is a view 3e of the corner portion of fig. 3d;
fig. 4 is a section along the line IV-IV through one of the plates of fig. 2;
fig. 5 illustrates schematically flows of medium through through-flow passages between
two adjacent plates in the plate heat exchanger of fig. 1; and
fig. 6 is a plan view of a plate heat exchanger according to the invention wherein
the plates have another shape than at the plate heat exchanger of figs. 1 and 5.
[0006] The plate heat exchanger illustrated in the drawings is of the cross-flow type for
heat exchange between different media of which at least one is a gas. This plate heat
exchanger comprises a stack 1 of plates under which there may be located a bottom
plate 2 and on top of which there may be located a top plate 3. The stack 1 of plates
includes plates 8a, 8b which in the drawings are square, but which alternatively can
be rectangular. The plates are preferably made of a sheet material which is folded
to form elongated, substantially in wave shape extending corrugating ridges 15.
[0007] Plates 8a, 8b define together through-flow gaps 9 and 10 of which every second through-flow
gap 9 extends through the plate heat exchanger and is adapted to let through a first
medium V, e.g. hot air. The remaining through-flow gaps 10 extend crosswise relative
to the through-flow gaps 9 extending through the plate heat exchanger and are adapted
to permit passage of a second medium K, e.g. cold air.
[0008] Each plate 8a and 8b respectively, defines a partition wall between the two different
through-flow gaps 9, 10 so that heat transfer can occur from one medium, e.g. the
hot air V, to the other medium, e.g. the cold air K, through said plate 8a and 8b
respectively.
[0009] Adjacent plates 8a, 8b are provided such that their corrugating ridges 15 cross each
other in a through-flow gap 9 or 10 defined between the plates 8a, 8b.
[0010] Of two adjacent plates 8a, 8b are the corrugating ridges 15 of one plate 8a in a
through-flow gap 9 or 10 defined between the adjacent plates 8a, 8b directed preferably
in a lateral direction relative to an inlet direction of a medium V or K flowing into
the through-flow gap 9 or 10.
[0011] The corrugating ridges 15 of the other plate 8b of said adjacent plates 8a, 8b are
in said through-flow gap 9 or 10 directed in another lateral direction relative to
said inlet direction.
[0012] The plates 8a, 8b have opposing edge portions 11, 12 and 13, 14 respectively. These
edge portions 11, 12 and 13, 14 respectively, are preferably straight or substantially
straight and the corrugating ridges 15 are preferably inclined relative thereto. The
corrugating ridges 15 extend e.g. at an angle of about 45° relative to said edge portions.
[0013] The corrugating ridges 15 of adjacent plates 8a, 8b engage each other pointwise in
the through-flow gap 9 or 10 defined between said plates 8a, 8b and are joined together
in the points of engagement.
[0014] A through-flow gap 9 or 10 defined by the adjacent plates 8a, 8b and inlet and outlet
gaps 17, 18 defined by opposing edge portions 11, 12 or 13, 14 of the plates 8a, 8b
for inlet and outlet flow of said media V, K into and from said through-flow gap 9
or 10, preferably have the same or substantially the same height H.
[0015] The plates 8a, 8b in the stack 1 thereof are also provided or mounted such that two
opposing edge portions 13, 14 or 11, 12 of first and second plates 8a, 8b are joined
closely together for closing through-flow gaps 9 or 10 defined between said plates
8a, 8b at two opposite sides, while two other opposing edge portions 11, 12 or 13,
14 of first and second plates 8a, 8b define between them inlet and outlet gaps 17,
18 into and from said through-flow gaps 9 or 10.
[0016] The two opposing edge portions 11 and 12 of each plate 8a and 8b respectively, lie
preferably in the same first plane P1 and its two other opposing edge portions 13
and 14 preferably in the same second plane P2.
[0017] The corrugating ridges 15 of each plate 8a and 8b respectively, extend back and forth
between said first and second planes P1 and P2 so that outer portions 15a of every
second corrugating ridge 15 lie in the first plane P1 and outer portions 15a of corrugating
ridges 15 there-between lie in the second plane P2.
[0018] Adjacent plates 8a, 8b in the stack 1 thereof may be located in two different positions
relative to each other, namely either the positions according to figs. 2 2a and 2b
or the positions according to figs. 3, 3a and 3b. Common to these two different mutual
positions is that the adjacent plates 8a, 8b are located relative to each other such
that their corrugating ridges 15 extend crosswise relative to each other. Additionally,
the two adjacent plates 8a, 8b are facing each other such that corrugating ridges
15 on one plate 8a are facing corrugating ridges 15 on the other plate 8b. The outer
portions 15a of the corrugating ridges 15 facing each other of the two adjacent plates
8a, 8b engage each other.
[0019] The two adjacent plates 8a, 8b define between them a through-flow gap 9 or 10 the
height H of which is some-what less than the distance A1 between the two planes P1
and P2 of one plate 8a plus the distance A2 between the two planes P1 and P2 of the
other plate 8b. Particularly, the height H is similar to the distances A1 + A2 minus
the wall thickness of two plates 8a, 8b.
[0020] The plates 8a, 8b can be designed such that the distance A1 and A2 respectively,
between the planes P1 and P2 of the respective plate 8a, 8b, is always the same, which
means that the through-flow gap 9 or 10 is twice as high as the distance between the
planes P1 and P2 of one plate. However, the plates 8a, 8b may alternatively be designed
such that the distance between the planes P1, P2 of one plate 8a is less than the
distance between corresponding planes P1, P2 of the other plate 8b. In this case,
the height H of the through-flow gap 9 or 10 is less than the sum of the distances
between the planes P1, P2 of said plates 8a, 8b.
[0021] Said two adjacent plates 8a, 8b may also have such mutual positions that two opposing
edge portions 13, 14 and 11, 12 respectively, of one plate 8a engage and are joined
together with two opposing edge portions 13, 14 of the other plate 8b. Two other opposing
edge portions 11, 12 of one plate 8a and two other opposing edge portions 11, 12 of
the other plate 8b define between them an inlet gap 17 into and an outlet gap 18 from
the through-flow gap 9 or 10, the heights H of which correspond with or substantially
correspond with the height H of the through-flow gap 9 or 10.
[0022] As mentioned above, the adjacent plates 8a, 8b may be located in two different positions
relative to each other. When the plates are in the relative positions illustrated
in figs. 2, 2a and 2b, opposing edge portions 13, 14 which on the plate 8a lie in
the same second plane P2, engage and are joined together with opposing edge portions
13, 14 which on the other plate 8b also lie in said second plane P2.
[0023] The other opposing edge portions 11, 12 of the first plate 8a, lying in the same
first plane P1, and the other opposing edge portions 11, 12 of said other or second
plate 8b, define between them said inlet gap 17 and said outlet gap 18.
[0024] When the plates 8a, 8b instead are located in the positions relative to each other
shown in figs. 3, 3a and 3b, opposing edge portions 11, 12 which on one plate 8b lie
in the same first plane P1, engage and are joined together with opposing edge portions
13, 14 which on an adjacent plate 8a lie in said second plane P2.
[0025] The other opposing edge portions 13, 14 of the plate 8b which lie in said second
plane P2 and other opposing edge portions 11, 12 of the plate 8a, define between them
said inlet gap 17 and said outlet gap 18.
[0026] In order to seal the through-flow gaps 9, 10 at the corners of the stack 1 of plates
and/or to hold the plates 8a, 8b together and/or to stiffen the stack 1 of plates,
each plate 8a, 8b has four corner portions 20. When the plates 8a, 8b are placed in
said stack 1 thereof, the inside of the corner portions 20 of a plate is joined together
with the outside of corresponding corner portions 20 of an adjacent plate 8b or 8a.
[0027] In order to provide such a corner portion 20 at e.g. the plate 8b (see figs. 3c,
3d), a corner portion 20 of said plate extends obliquely from the edge portion 14
lying in the plane P1 to the edge portion 12 lying in the plane P2 of the plate. The
corner portion 20 is bent downwards (or upwards) along a bending line 20b which, seen
from above (fig. 3c), extends from the edge portion 14 to the edge portion 12. By
bending the plate 8a and 8b respectively, downwards (or upwards) along this bending
line 20b, the outer part of the edge portion 14 is bent downwards, the corner part
20a downwards along a part of the bending line 20b extending obliquely between the
planes P1, P2 and the outer part of the edge portion 12 downwards. In order to hereby
ensure that the corner portion 20 is directed straight or almost straight downwards
although it partly emanates from a bending line 20a which extends obliquely between
the planes P1, P2, the corner portion 20 is formed, preferably in connection with
the bending, such that one side 20c thereof becomes longer than its other side 20d
and this difference in length depends on the distance between the planes P1 and P2.
The corner portion 20 of the plate 8a is provided in the same way.
[0028] The corner portions 20 are provided so close and/or durable to each other by soldering
and/or have such rigidity that they replace separate sealing and/or holding and/or
stiffening means at the corners of the stack 1 of plates.
[0029] When the plates 8a, 8b are joined together in said positions, through-flow gaps 9,
10 are defined which form a "through-flow labyrinth" for the media flows passing through
said gaps. By forming this "through-flow labyrinth", undesired temperature zoning
or layering at the outlet gaps 18 can be prevented or at least obstructed.
[0030] The angles α of the corrugating ridges relative to the inlet gaps 17 for hot medium
V may e.g. be less than the angles β of the corrugating ridges 15 relative to inlet
gaps 17 for cold medium K. In this example it is achieved that a greater flow resistance
is generated for hot medium V in the plate heat exchanger than for cold medium K.
[0031] The angles α may be about 30° and the angles β consequently about 60°, but said angles
α, β may vary in view of the desired flow resistance for each medium V and K.
[0032] The corrugating ridges 15 or a part thereof may form spaces 16 in one of two adjacent
plates 8b, 8b, said spaces being directed from a first inlet gap 17 of the plate heat
exchanger for a medium, preferably cold medium K, obliquely towards an inlet gap 17
of the plate heat excbanger for a second medium, preferably hot medium V. Hereby,
said cold medium K can quickly cool such a part of the plate heat exchanger which
is heated most by said hot medium V.
[0033] In order to further cool those parts of the plate heat exchanger which are heated
most be hot medium V, a separate through-flow passage 19 may be provided close to
and extend along the inlet gap 17 for hot medium V. This separate through-flow passage
19 may lack corrugating ridges 15 such that cold medium K can flow therethrough with
substantially less turbulence than the turbulence generated in cold medium K in the
other through-flow gaps 10.
[0034] Said separate through-flow gap 19 can be rectilinear and it can be located immediately
within the inlet gap 17 for hot medium V.
[0035] The plates 8a, 8b may have identical shape or substantially identical shape. As an
example it can be noted that all plates 8a, 8b may have corner portions 20 bent in
the same direction. Alternatively, every second plate 8a, 8b may have corner portions
20 bent in the opposite direction, but otherwise, the plates 8a, 8b may be identical.
[0036] The plates 8a, 8b are manufactured of a metallic material and they are mounted or
attached to each other by soldering, e.g. vacuum soldering. The soldering can be carried
through by applying a material suitable for soldering between the plates 8a, 8b (and
eventually also between the members of the frame structure 4 and the plates), and
then place the plate heat exchanger in a heating device in which the soldering material
is melted. When the plate heat exchanger is removed from the heating device and the
melted soldering material has cooled down, the solder is finished and the plate heat
exchanger tight or leakproof.
[0037] By means of said soldering, the edge portions 11-14, the corrugating ridges 15 and
the corner portions 20 are joined together in a stable and durable manner and it is
possible to do without all types of frame structures located outside the stack 1 of
plates for holding the plates together and/or provide sufficient stability to said
stack 1 of plates.
[0038] Finally, it should be mentioned that the embodiments of the plate heat exchanger
described above may vary within the scope of the following claims and that the plate
heat exchanger can be used for two gaseous media or for one gaseous medium and one
liquid medium.
1. Plate heat exchanger of cross-flow type for heat exchange between different media
of which at least one is a gas,
wherein the plate heat exchanger comprises plates (8a, 8b) with elongated and in various
alternating directions protruding corrugating ridges (15),
wherein the plate heat exchanger has through-flow gaps (9) for a first medium (V)
and through-flow gaps (10) for a second medium (K),
wherein the through-flow gaps (9, 10) extend crosswise relative to each other through
the plate heat exchanger such that said first and second medium (V, K) flow cross-wise
relative to each other through said plate heat exchanger,
wherein each plate (8a and 8b respectively) defines a partition wall between two different
through-flow gaps (9, 10) for different media (V and K respectively) such that heat
transfer between said media (V and K respectively) occurs through said plate (8a and
8b respectively),
wherein the corrugating ridges (15) are situated between two planes (P1, P2),
wherein each plate (8a, 8b) has two edge portions (11, 12) which are provided in one
plane (P1) and two other opposing edge portions (13, 14) which are provided in the
other plane (P2),
wherein the corrugating ridges (15) are located inclined or obliquely relative to
said edge portions (11-14),
wherein two adjacent plates (8a, 8b) are mounted relative to each other such that
two edge portions (13, 14) of one of the plates (8a) and provided in one plane (P2)
are joined together with two edge portions (13, 14) of the other plate (8b) located
in the same plane (P2), while two edge portions (11, 12) of said one plate (8a) and
provided in another plane (P1) are situated at a distance from two edge portions (11,
12) of said other plate (8b) provided in said another plane (P1), said two edge portions
(11, 12) located at a distance from each other defining outlet and inlet gaps (17,
18) into and from a through-flow gap (9, 10) defined between the plates (8a, 8b),
said outlet and inlet gaps (17, 18) having substantially the same height (H) as said
through-flow gap (9 or 10), and
wherein two adjacent plates (8a, 8b) are also mounted such that the corrugating ridges
(15) inclined relative to the edge portions (11-14), cross each other in said through-flow
gap (9 or 10),
characterized in
that each plate (8a, 8b) has four corner portions (20) for sealing between the through-flow
gaps (9, 10) at the corners of said plates (8a, 8b),
that each corner portion (20) of a plate (8a or 8b) is by means of soldering joined
closely together with a corresponding corner portion (20) of an adjacent plate (8b
or 8a), and
that the edge portions (11-14) and corrugating ridges (15) of two adjacent plates
(8a, 8b) are joined together by means of soldering.
2. Plate heat exchanger according to claim 1, characterized in that the corner portions (20) of each plate (8a, 8b) replace separate sealing members
in the corners of a stack (1) of plates formed by said plates (8a, 8b).
3. Plate heat exchanger according to claim 1 or 2, characterized in that each corner portion (20) is formed by bending of the plate (8a and 8b respectively)
along a bending line (20b) such that said plate has outer parts of two edge portions
(14, 12) located in different planes (P1, P2) and corner parts (20a) of the plate
(8a and 8b respectively) located between said outer parts, said corner parts extending
at said bending line (20b) obliquely between said planes (P1, P2) and that each corner
portion (20) has two sides (20c, 20d) of different length such that the corner portion
(20) is directed perpendicular or substantially perpendicular to the plate (8a and
8b respectively).
4. Plate heat exchanger according to any preceding claim, characterized in that the plates (8a, 8b) are identical except for corner portions (20) which on every
second plate (8a and 8b respectively) in the stack (1) thereof are turned relative
to corner portions (20) of the other plates.
5. Plate heat exchanger according to any of claims 1-3, characterized in that the plates (8a, 8b) are identical and have corner portions (20) turned in the
same direction.
6. Plate heat exchanger according to any preceding claim, characterized in that the angles (α) of the corrugating ridges (15) relative to edge portions at inlet
gaps (17) for the medium (V) for which the heat transfer in the plate heat exchanger
shall be maximized, are less than the angles (β) of the corrugating ridges (15) relative
to edge portions at inlet gaps (17) for the medium (K) for which the resistance in
the plate heat exchanger shall be minimized.
7. Plate heat exchanger according to any preceding claim, characterized in that the corrugating ridges (15) engaging each other pointwise, are joined together
by soldering at the engagement or contact points.
8. Plate heat exchanger according to any preceding claim, characterized in that adjacent plates (8a, 8b) define a separate through-flow passage (19) for cold
medium (K) without corrugating ridges (15), said separate through-flow passage (19)
being provided close to and extending along an inlet gap (17) for hot medium (V) such
that cold medium (K) flowing through said separate through-flow passage (19) cools
the plate heat exchanger near said inlet gap (17) for hot medium (V).
9. Plate heat exchanger according to claim 8, characterized in that said separate through-flow passage (19) extends rectilinearly through the plate
heat exchanger.
10. Plate heat exchanger according to claim 8 or 9, characterized in that said separate through-flow passage (19) is located immediately within an inlet
gap (17) through which hot medium (V) flows into the plate heat exchanger.