TECHNICAL FIELD
[0001] The present invention relates to a heat exchanger assembly, in particular a heat
exchanger assembly such as a water chiller or water gas cooler operating with R744
as a refrigerant. A heat exchanger according to the preamble of claim 1 is known from
document
JP 2001 050681.
PRIOR ART
[0002] A heat exchanger assembly known from the prior art generally comprises two fluid
circuits. A first fluid circuit for a fluid to be cooled down comprises two manifolds
and a plurality of flow ducts connecting two manifolds together. A second fluid circuit
for a coolant includes a plurality of stacked plates arranged in pairs. Each pair
of the stacked plates defines a channel therebetween. The channels defined by different
pairs of the stacked plates are in fluid communication with each other so that a coolant
flow path is created. One flow duct of the first fluid circuit is arranged between
two adjacent pairs of the stacked plates. Heat exchanger takes place at the interface
between two pairs of the stacked plates and one flow duct situated between two pairs
of the stacked plates.
[0003] In the prior art solution described above the heat exchange efficiency is significantly
reduced due to the fact that the heat exchange surface is not used efficiently. The
coolant is not in direct contact with the flow ducts traversed by the fluid to be
cooled down. In fact, heat is exchanged between both fluid circuits only at the surface
where the pairs of the stacked plates and the flow ducts contact each other. It means
that there are two layers of material, which transfer heat between both fluids. Moreover,
in the heat exchanger assembly known from the prior art the stacked plates are provided
with dimpled areas to guide the flow of the coolant. The dimpled areas are situated
at a wall of the plates, which is in contact with the flow duct. This additionally
reduces the heat exchange surface between both fluid circuits.
AIMS OF INVENTION
[0004] One aim of the present invention is to provide a heat exchanger assembly with increased
heat exchange efficiency.
[0005] Another aim of the present invention is to provide a heat exchanger assembly, which
is easier to manufacture, has fewer types of components and is more robust.
[0006] The above and other aims of the present invention are achieved by a heat exchanger
assembly as defined in the annexed claims.
SUMMARY OF INVENTION
[0007] A heat exchanger assembly comprises a first fluid circuit for a first working fluid.
The first fluid circuit including two manifolds and a plurality of flow ducts connecting
the manifolds. The heat exchanger assembly further comprises a second fluid circuit
for a second working fluid. The second fluid circuit including a plurality of shaped
plates. The flow ducts and the shaped plates are arranged alternatively one above
the other so that one flow duct is arranged between two successive shaped plates.
The shaped plates comprise a circumferential wall, which includes two opposite cavities
to receive the flow ducts. Each two successive shaped plates and one flow duct arranged
therebetween define together a channel for the second working fluid. The channels
defined by the shaped plates and the flow ducts being in fluid communication with
each other.
[0008] Further advantageous embodiments of the present invention are defined in dependent
claims.
[0009] In the present invention a coolant flows through the channels defined by the shaped
plates and is in direct contact with the flow ducts traversed by a fluid to be cooled
down. In this way the heat exchange surface is maximized. Moreover, the amount of
material separating both fluids is limited to the material constituting the flow ducts
only.
[0010] Additionally, the manufacturing process of the heat exchanger assembly of the present
invention is considerably simplified because the second fluid circuit may consist
of only one type of the shaped plates. Moreover, as the shaped plates are stacked
alternatively with the flow ducts, namely one shaped plate, one flow duct, one shaped
plate, etc., the number of components used is greatly reduced compared to the prior
art. It in turn reduces the overall size of the heat exchanger assembly, simultaneously
leaving the heat exchange efficiency unaffected.
BRIEF DESCRIPTION OF DRAWINGS
[0011] The present invention is described in more detail below, with reference to the accompanying
drawings, which show non-limiting embodiments of the present invention, wherein:
Fig. 1 shows a perspective view of a heat exchanger assembly,
Fig. 2 shows a perspective view of the heat exchanger assembly, with some parts removed
for clarity,
Fig. 3 shows an exploded perspective view of two successive shaped plates and one
flow duct placed therebetween,
Fig. 4 shows a cross-section view of two successive shaped plates and one flow duct,
once assembled,
Fig. 5 shows a perspective view of another embodiment of the heat exchanger assembly,
with some parts removed for clarity,
Fig. 6 shows a view similar to that of figure 3, but for the embodiment of figure
5, and
Fig. 7 shows a view similar to that of figure 4, but for the embodiment of figure
5.
EMBODIMENTS OF INVENTION
[0012] A heat exchanger assembly 1 according to the present invention comprises two manifolds,
namely a first manifold 21 and a second manifold 22, and a plurality of flat hollow
parallel flow ducts 3 arranged in one column between the manifolds 21, 22. Ends of
the flow ducts 3 are received in the manifolds 21, 22, namely in corresponding slots
provided in the manifolds 21, 22. In other words, the flow ducts 3 connect the manifolds
21, 22 to each other. In the embodiment shown in the figures the first manifold 21
operates as an inlet/outlet manifold, whereas the second manifold 22 is an intermediate
manifold. The first manifold 21 includes two series of narrow longitudinal channels
defined therein. A first series of the narrow longitudinal channels is in fluid communication
with a first half of the flow ducts 3, while a second series of the narrow longitudinal
channels is in fluid communication with a second half of the flow ducts 3. The second
manifold 22 includes one wide longitudinal channel defined therein, which is in fluid
communication with all flow ducts 3.
[0013] The flow ducts 3 include a plurality of through channels, which are in fluid communication
with the longitudinal channels of the manifolds 21, 22. The heat exchanger assembly
1 comprises a connection block 4 connected to the first manifold 21. The connection
block 4 in turn comprises an inlet port 5 and an outlet port 6. The inlet and outlet
ports 5, 6 are in fluid communication with both series of the narrow longitudinal
channels of the first manifold 21, respectively.
[0014] A fluid to be cooled down flows into the heat exchanger assembly 1 through the inlet
port 5. Next, the fluid to be cooled down flows along the first series of the narrow
longitudinal channels of the first manifold 21 and through the first half of the flow
ducts 3, enters the wide longitudinal channel of the second manifold 22, then flows
into the second half of the flow ducts 3 and the second series of the narrow longitudinal
channels of the first manifold 21 and finally flows out of the heat exchanger assembly
1 through the outlet port 6.
[0015] However, the invention is not limited to the embodiment described above. In another
embodiment of the invention, not shown in the figures, each series of the narrow longitudinal
channels in the first manifold 21 can be replaced by one wide longitudinal channel
and the wide longitudinal channel in the second manifold 22 can be replaced by a series
of narrow longitudinal channels. Moreover, the first manifold 21 can be an inlet manifold,
while the second manifold 22 can be an outlet manifold. In such a case, the manifolds
21, 22 each need be provided with only one wide longitudinal channel or one series
of the narrow longitudinal channels, which are in fluid communication with all flow
ducts 3. Moreover, each of the first and second manifolds 21, 22 is provided with
its own connection block 4, which comprises only one port connected to the longitudinal
channel(s) of the respective manifold 21, 22.
[0016] In figures it is shown that the connection block 4 is a part separate from one or
both manifolds 21, 22. However, in still another embodiment of the invention the connection
block 4 can be integral to one of the manifolds 21, 22, while the other can be devoid
of the connection block 4, or both manifolds 21, 22 can comprise the integral connection
block 4. The integral connection block 4 is in fact an opening in any of the manifolds
21, 22 and is in fluid communication with the longitudinal channel(s) of the manifold
21, 22 concerned.
[0017] Moreover, instead of having a plurality of through channels, the flow ducts 3 each
can include only one wide through channel.
[0018] The manifolds 21, 22, the flow ducts 3 and, if used, the connection block(s) 4, either
separate or integral, define together a first fluid circuit for a first working fluid,
especially the fluid to be cooled down.
[0019] The heat exchanger assembly 1 further comprises a plurality of shaped plates 7. One
flow duct 3 is inserted between two successive adjacent shaped plates 7. In other
words, the flow ducts 3 and the shaped plates 7 are arranged alternatively one above
the other so that a pile of the flow ducts 3 and the shaped plates 7 is created. For
this purpose, each of the shaped plates 7 is provided with a circumferential wall.
The circumferential wall includes a first pair of two opposite side walls 71 at two
opposite sides 7a of the shaped plate 7 and a second pair of two opposite side walls
79 at two other opposite sides 7b of the shaped plate 7. The side walls 71 are higher
than the side walls 79. This way two opposite cavities 73 are formed at two opposite
sides 7b of the shaped plates 7. In other words the side walls 71 and the lower side
walls 79 define and delimit the cavities 73. Two opposite cavities 73 at two opposite
sides 7b of the shaped plate 7 receive one flow duct 3, which rests on the side walls
79.
[0020] When the heat exchanger assembly 1 is assembled one flow duct 3 is closed and/or
enclosed between two successive adjacent shaped plates 7 in such a way that only ends
of the flow ducts 3 extend beyond a body defined by a stacked pile of the shaped plates
7 and the flow ducts 3. The ends of the flow ducts 3 are received in the manifolds
21, 22. It means that a channel 8 is defined between two successive adjacent shaped
plates 7 and a major part of the flow duct 3 fits inside the channel 8. The coolant
flows through the channels 8 and is in direct contact with the flow ducts 3. In fact,
the channels 8 are closed or sealed not only by two successive adjacent shaped plates
7 but also by the flow ducts 3, which are arranged between these two successive adjacent
shaped plates 7 and fill the cavities 73.
[0021] The shaped plate 7 can be provided with two openings 75, preferably at the opposite
sides 7a with the side walls 71. When the shaped plates 7 are stacked the openings
75 define two coolant channels, namely an inlet coolant channel 76 and an outlet coolant
channel 77. Thus, the channels 8 defined between the shaped plates 7 are in fluid
communication with both the coolant channels 76, 77 and each other. In the embodiment
shown in the figures, the channels 8 are in fact fluidly connected parallel to each
other. In other words, the coolant leaves the inlet coolant channel 76 and flows simultaneously
into all channels 8. Moreover, the coolant flows out of all channels 8 at the same
time and enters the outlet coolant channel 77.
[0022] The topmost shaped plate 7 is provided with two coolant ports 9, 10. Each of the
coolant ports 9, 10 is connected to one of the openings 75 of the topmost shaped plate
7 and extends at the extension of the inlet and outlet coolant channels 76, 77. The
openings 75 of the bottommost shaped plate 7 are sealed and/or closed. In fact, the
bottommost shaped plate 7 can be made without openings 75. The shaped plates 7 stacked
in a pile define a second fluid circuit for a second working fluid, especially the
coolant. In fact, the second fluid circuit consists of the channels 8, the inlet and
outlet coolant channels 76, 77 and the coolant ports 9, 10. Of course, if necessary,
the topmost shaped plate 7 can comprise only one of the coolant ports 9, 10, while
the bottommost shaped plate 7 comprises the other of the coolant ports 9, 10, and
the openings 75 of the topmost and bottommost shaped plates, which are not connected
to the coolant ports 9, 10, are closed.
[0023] The shaped plate 7 can comprise flow guiding protrusions 74, arranged at a bottom
78 of the shaped plate 7 and extending from one opening 75 to the other. The flow
guiding protrusions 74 can extend in different configurations. The function of the
flow guiding protrusions 74 is to guide the flow of the coolant along the flow ducts
3 as long as possible, which greatly increases the heat exchange efficiency. Moreover,
the flow guiding protrusions 74 are very easy to manufacture as no machining is required.
The flow guiding protrusions 74 can simply be embossed or dimpled in the shaped plates
7. In addition, the flow guiding protrusions 74 can extend at both sides of the shaped
plate 7 and into both channels 8 adjacent to the shaped plate 7 concerned, as shown
in figure 4. The flow guiding protrusions 74 can be in contact with the flow ducts
3 so that the coolant must follow only the path defined by the flow guiding protrusions
74 and is prevented from choosing the shortest path between the openings 75.
[0024] As mentioned above, the shaped plates 7 can be stacked on top of each other, thus
creating sufficient cavities 73 for the flow ducts 3 to fit in. This is achieved by
the fact that each shaped plate 7 is provided with the side walls 71, which the shaped
plate 7 situated above can rest on. This higher situated shaped plate 7 rests also
on the flow duct 3, situated below it, at the edges of the shaped plate 7, which are
present at two opposite sides 7b. It is particularly beneficial because the heat exchanger
assembly 1 can be made of only one type of shaped plates 7, which can be easily stacked
on top of each other.
[0025] As shown in the figures, the side walls 71 are not exactly perpendicular to the bottom
of the shaped plate 7 but are slightly inclined towards the outside the shaped plate
7. It means that an angle between the side wall 71 and the bottom of the shaped plate
7 is greater than 90°. This way, the shaped plates 7 can easily be stacked one on
the top of the other, namely an external surface of the side wall 71 of one shaped
plate 7 is in contact with an internal surface of the side wall 71 of the shaped plate
7 located below.
[0026] In the embodiment described above and shown in the figures, the channels 8 are fluidly
connected parallel to each other. However, in another embodiment of the present invention,
not shown in the figures, the channels 8 are fluidly connected to each other in series.
In this embodiment, each shaped plate 7 has only one opening 75 and the openings 75
in the successive shaped plates 7 in a pile are positioned alternately. It means that
a first shaped plate 7 has one opening 75 at a first side, a second shaped plate 7
has one opening 75 at a second side, opposite to the first side, a third shaped plate
7 has one opening 75 at its first side, etc. This way, a long S-shaped coolant flow
path is defined. In such a case each of the topmost shaped plate 7 and the bottom
most shaped plate 7 is provided with only one of the inlet and outlet coolant ports
9, 10. This also means that the heat exchanger assembly 1 utilizes two types of the
shaped plates 7, but they differ only in the position of the opening 75, while the
general configuration of the shaped plates 7 remains unchanged. Nevertheless, only
one type of the shaped plates 7 can also be employed. In such a case, the shaped plates
7 with two openings 75, as discussed above and shown in the figures, are stacked in
a pile and each shaped plate 7 has its one opening 75 closed by an additional plug.
[0027] All components of the heat exchanger assembly 1 are brazed to each other to ensure
the proper fluid-tightness of the assembly. This way flow paths of the first fluid
circuit and the second fluid circuit are sealed and separated from each other. The
ends of the flow ducts 3 are brazed to the manifolds 21, 22. Two successive adjacent
shaped plates 7 are brazed to each other and to the flow ducts 3 arranged therebetween
so that the channels 8 are fluid-tight and separated from the outside environment.
[0028] In another embodiment of the present invention shown in figures 5 - 7 each shaped
plate 7 is provided with two projecting tongues 72 at its two opposite sides 7b. The
projecting tongues 72 projects from the side walls 79. Each projecting tongue 72 divides
each cavity 73 into two separate cavities 73a, 73b. In other words, the separate cavities
73a, 73b form together one common cavity 73 described above. Similarly, each flow
duct 3 is divided into two separate flow ducts 3a, 3b. Two separate flow ducts 3a,
3b are received in pairs of the separate cavities 73a, 73b, respectively. If necessary,
more than one projecting tongue 72 can be provided at each of two opposite sides 7b
of the shaped plate 7. For example, two projecting tongues 72 at each of two opposite
sides 7b of the shaped plate 7 divide each cavity 73 into three separate cavities,
etc. In this embodiment of the present invention two successive shaped plates 7 enclose
two or more separate flow ducts 3a, 3b, depending on the number of the projecting
tongues 72 used.
[0029] Moreover, in the embodiments of the present invention described above and shown in
the figures, the shaped plate 7 is rectangular and, therefore, is provided with the
circumferential wall, which in turn can be divided into four sections, namely four
side walls 71, 79. However, in another embodiments the shaped plate 7 can have other
configurations. For example, the shaped plate 7 can be oval. It means that the circumferential
wall of the shaped plate 7 cannot any longer be divided into separate distinctive
sections. In this embodiment it is important to note that the cavities 73, 73a, 73b
should be arranged opposite to each other so that the flow ducts 3 could be received
in respective pairs of the cavities 73, 73a, 73b. This oval circumferential wall can
be perpendicular to the bottom or can be slightly inclined towards the outside of
the shaped plate 7.
1. A heat exchanger assembly (1) comprising:
a first fluid circuit for a first working fluid, said first fluid circuit including
two manifolds (21, 22) and a plurality of flow ducts (3) connecting said manifolds
(21, 22);
a second fluid circuit for a second working fluid, said second fluid circuit including
a plurality of shaped plates (7);
wherein
said flow ducts (3) and said shaped plates (7) are arranged alternatively one above
the other so that one flow duct (3) is arranged between two successive shaped plates
(7);
said shaped plates (7) comprise a circumferential wall, said shaped plates (7) include
two opposite cavities (73) to receive said flow ducts (3); and
each two successive shaped plates (7) and said one flow duct (3) arranged therebetween
define together a channel (8) for said second working fluid, said channels (8) defined
by said shaped plates (7) and said flow ducts (3) being in fluid communication with
each other; and characterized in that the circumferential wall of the shaped plates is inclined towards the outside of
the shaped plates.
2. The heat exchanger assembly (1) according to claim 1, characterized in that said circumferential wall includes a first pair of opposite side walls (71) and a
second pair of opposite side walls (79), said first pair of said opposite side walls
(71) being higher that said second pair of said opposite side walls (79) so that said
cavities (73) are defined at said second pair of said opposite side walls (79).
3. The heat exchanger assembly (1) according to any of claims 1 and 2, characterized in that at least one projecting tongue (72) is provided at each of said opposite side walls
(79) of said second pair so that each of said at least one projecting tongue (72)
divides each of said cavities (73) into at least two separate cavities (73a, 73b),
said flow ducts (3) each being divided into at least two separate flow ducts (3a,
3b), said at least two separate flow ducts (3a, 3b) being received in said at least
two separate cavities (73a, 73b), respectively.
4. The heat exchanger assembly (1) according to any of the preceding claims, characterized in that said shaped plates (7) include flow guiding protrusions (74) at their bottom (78).
5. The heat exchanger assembly (1) according to any of the preceding claims, characterized in that said channels (8) are fluidly connected parallel to each other.
6. The heat exchanger assembly (1) according to any of claims 1-4, characterized in that said channels (8) are fluidly connected to each other in series.
1. Wärmetauscheranordnung (1), die umfasst:
einen erste Fluidkreis für ein erstes Arbeitsfluid, wobei der erste Fluidkreis zwei
Verteiler (21, 22) und mehrere die Verteiler (21, 22) verbindende Strömungskanäle
(3) aufweist;
einen zweiten Fluidkreis für ein zweites Arbeitsfluid, wobei der zweite Fluidkreis
mehrere Formplatten (7) aufweist;
wobei
die Strömungskanäle (3) und die Formplatten (7) abwechselnd übereinander derart angeordnet
sind, dass ein Strömungskanal (3) zwischen zwei aufeinanderfolgenden Formplatten (7)
angeordnet ist;
wobei die Formplatten (7) eine Umfangswand umfassen,
wobei die Formplatten (7) zwei gegenüberliegende Aussparungen (73) zum Aufnehmen der
Strömungskanäle (3) aufweisen; und
wobei jeweils zwei aufeinanderfolgende Formplatten (7) und der eine dazwischen angeordnete
Strömungskanal (3) zusammen einen Durchgang (8) für das zweite Arbeitsfluid definieren,
wobei die Durchgänge (8) definiert sind, indem die Formplatten (7) und die Strömungskanäle
(3) in Fluidverbindung miteinander stehen; und
dadurch gekennzeichnet, dass die Umfangswand der Formplatten hin zu der Außenseite der Formplatten geneigt ist.
2. Wärmetauscheranordnung (1) nach Anspruch 1, dadurch gekennzeichnet, dass die Umfangswand ein erstes Paar von gegenüberliegenden Seitenwänden (71) und ein
zweites Paar von gegenüberliegenden Seitenwänden (79) aufweist, wobei das erste Paar
von gegenüberliegenden Seitenwänden (71) höher als das zweite Paar von gegenüberliegenden
Seitenwänden (79) ist, so dass die Aussparungen (73) an dem zweiten Paar von gegenüberliegenden
Seitenwänden (79) definiert sind.
3. Wärmetauscheranordnung (1) nach einem der Ansprüche 1 und 2, dadurch gekennzeichnet, dass mindestens eine hervorstehende Zunge (72) an jeder der gegenüberliegenden Seitenwände
(79) des zweiten Paars derart bereitgestellt sind, dass jede der mindestens einen
hervorstehenden Zunge (72) jede der Aussparungen (73) in mindestens zwei separate
Aussparungen (73a, 73b) teilt, wobei die Strömungskanäle (3) jeweils in mindestens
zwei separate Strömungskanäle (3a, 3b) geteilt sind, wobei die mindestens zwei separaten
Strömungskanäle (3a, 3b) jeweils in den mindestens zwei separaten Aussparungen (73a,
73b) aufgenommen sind.
4. Wärmetauscheranordnung (1) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass die Formplatten (7) Strömungsleitüberstände (74) an ihrer Unterseite (78) aufweisen.
5. Wärmetauscheranordnung (1) nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, dass die Durchgänge (8) parallel miteinander fluidisch verbunden sind.
6. Wärmetauscheranordnung (1) nach einem der Ansprüche 1-4, dadurch gekennzeichnet, dass die Durchgänge (8) in Reihe miteinander fluidisch verbunden sind.
1. Ensemble échangeur thermique (1) comprenant :
un premier circuit de fluide pour un premier fluide de travail, ledit premier circuit
de fluide comprenant deux collecteurs (21, 22) et une pluralité de conduits d'écoulement
(3) reliant lesdits collecteurs (21, 22) ;
un second circuit de fluide pour un second fluide de travail, ledit second circuit
de fluide comprenant une pluralité de plaques façonnées (7) ;
lesdits conduits d'écoulement (3) et lesdites plaques façonnées (7) étant disposés
alternativement l'un au-dessus de l'autre de sorte qu'un conduit d'écoulement (3)
soit disposé entre deux plaques façonnées (7) successives ;
lesdites plaques façonnées (7) comprenant une paroi circonférentielle,
lesdites plaques façonnées (7) comprenant deux cavités (73) opposées pour recevoir
lesdits conduits d'écoulement (3) ; et
chacune des deux plaques façonnées (7) successives et ledit un conduit d'écoulement
(3) disposé entre elles définissant ensemble un canal (8) pour ledit second fluide
de travail, lesdits canaux (8) définis par lesdites plaques façonnées (7) et lesdits
conduits d'écoulement (3) étant en communication fluidique entre eux ; et
caractérisé en ce que la paroi circonférentielle des plaques façonnées est inclinée vers l'extérieur des
plaques façonnées.
2. Ensemble échangeur thermique (1) selon la revendication 1, caractérisé en ce que ladite paroi circonférentielle comprend une première paire de parois latérales opposées
(71) et une seconde paire de parois latérales opposées (79), ladite première paire
desdites parois latérales opposées (71) étant plus élevée que ladite seconde paire
desdites parois latérales opposées (79) de sorte que lesdites cavités (73) soient
définies au niveau de ladite seconde paire desdites parois latérales opposées (79).
3. Ensemble échangeur thermique (1) selon l'une quelconque des revendications 1 et 2,
caractérisé en ce qu'au moins une languette saillante (72) est disposée au niveau de chacune desdites parois
latérales opposées (79) de ladite seconde paire de sorte que chacune desdites au moins
une languette saillante (72) divise chacune desdites cavités (73) en au moins deux
cavités séparées (73a, 73b), lesdits conduits d'écoulement (3) étant chacun divisés
en au moins deux conduits d'écoulement séparés (3a, 3b), lesdits au moins deux conduits
d'écoulement séparés (3a, 3b) étant reçus dans lesdites au moins deux cavités séparées
(73a, 73b), respectivement.
4. Ensemble échangeur thermique (1) selon l'une quelconque des revendications précédentes,
caractérisé en ce que lesdites plaques façonnées (7) comprennent des saillies de guidage d'écoulement (74)
au niveau de leur base (78).
5. Ensemble échangeur thermique (1) selon l'une quelconque des revendications précédentes,
caractérisé en ce que lesdits canaux (8) sont en communication fluidique en parallèle les uns aux autres.
6. Ensemble échangeur thermique (1) selon l'une quelconque des revendications 1 à 4,
caractérisé en ce que lesdits canaux (8) sont en communication fluidique les uns avec les autres en série.