Field of application
[0001] The present invention, in its most general aspect, refers to a heat exchanger for
the heat exchange between a first and a second fluid.
[0002] Particularly, but not exclusively, the invention concerns a heat exchanger for the
heat exchange between pressurized fluids, of the type comprising a plurality of casings,
of substantially flattened shape and of predetermined width, arranged in a pile, with
an air space defined between adjacent casings in the pile, and each formed from two
half-shells welded along a peripheral strip, which are in fluid communication with
each other through respective holes opening into said air space.
Prior art
[0003] Heat exchanger for the heat exchange between two fluids of the type comprising a
plurality of casings or flattened tubes are known.
[0004] Each casing is formed from two half-shells on which respective holes are open, in
corresponding positions, at which adjacent casings are joined through collectors.
[0005] In such an arrangement, each pair of adjacent casings defines an air space through
which a first flow of fluid is conveyed, whereas a second flow of fluid at a different
temperature crosses the plurality of casings.
[0006] In this way, such flows carry out a heat exchange, which is generally made more effective
by making their motion highly turbulent through the use of small corrugated plates,
or turbulators, arranged in the cavities and inside the casings, respectively.
[0007] The aforementioned joining collectors between adjacent casings are, according to
the prior art, pieces of tubes interfacing with the half-shells and forced, through
plastic deformation, around respective conical edges foreseen at the holes open on
the casings.
[0008] Heat exchangers thus realized, although advantageous, are not free from drawbacks,
including the main one represented by the low mechanical resistance that they possess
and that impairs its use, in particular in the case of heat exchange between flows
of fluids at high pressure values.
[0009] Such a low mechanical resistance is substantial both at the joints between adjacent
casings, where the plastic deformation does not ensure an adequate seal, and at the
half-shells which, for an effective heat exchange between the fluids, must be realized
with a small thickness.
[0010] It follows from this that heat exchangers thus realized cannot be used, or in any
case are of little industrial interest, in the case of heat exchange between flows
of fluids of which at least one is at a high pressure value; where by high pressure
value we mean a value greater than 10-13 bar.
Summary of the invention
[0011] The technical problem forming the basis of the present invention is that of devising
a heat exchanger for the heat exchange between a first fluid and a second fluid, of
the type comprising a plurality of casings, of substantially flattened shape and of
predetermined width, arranged in a pile, with an air space defined between adjacent
casings in the pile, and each formed from two half-shells welded along a peripheral
strip, in which the aforementioned casings are in fluid communication with each other
through respective holes opening into the aforementioned air space, having structural
and functional characteristics such as to overcome the aforementioned drawbacks, in
other words such as to ensure an unusual strength and mechanical resistance.
[0012] The aforementioned problem is solved according to the invention by a heat exchanger
of the type considered above, comprising, in the aforementioned air space, at least
one spacer, substantially of the sleeve type, abutting on at the top end and made
integral with said adjacent casings around the respective holes opening into said
air space.
[0013] Advantageously, the heat exchanger comprises irregularities associated with the aforementioned
at least one spacer, which extend in the air space to rigidify the half-shells.
[0014] Preferably, the aforementioned irregularities are radial spokes extending radially
from said at least one spacer.
[0015] Advantageously, the aforementioned radial spokes are practically equally angularly
spaced.
[0016] Again preferably, the aforementioned radial spokes are formed integrally with the
spacer, and more preferably radial spokes and spacer are a piece of an extruded profile.
[0017] Advantageously, the aforementioned extruded profile is made from metallic material
selected from the group comprising aluminium, aluminium alloys, copper, copper alloys
and similar metallic materials.
[0018] The characteristics and further advantages of a heat exchanger according to the present
invention shall become clearer from the description, made hereafter, with reference
to the attached drawings given for indicating and not limiting purposes.
Brief description of the drawings
[0019] In such drawings:
Figure 1 shows a schematic front section view of a heat exchanger in accordance with
the present invention, made along the line I-I;
Figure 2 shows a plan view of the heat exchanger of figure 1, made according to the
arrow II;
Figure 3 shows an enlarged view of a detail of the exchanger of figure 1;
Figure 4 shows a section view of a detail of the heat exchanger of figure 1, made
according to the line IV-IV of figure 3;
Figure 5 shows a perspective, exploded view of a portion of the exchanger of figure
1;
Figure 6 shows the portion of figure 5 of the heat exchanger in accordance with a
variant embodiment of the invention;
Figure 7 shows a detail of the portion of figure 5 in accordance with a further variant
embodiment of the invention;
Figure 8 shows the detail of figure 4 in accordance with a further variant embodiment
of the invention.
Detailed description
[0020] With reference to the aforementioned figures, a heat exchanger for the heat exchange
between a first fluid, for example oil, and a second fluid, for example air, realized
according to the present invention, is globally and schematically represented with
1.
[0021] The heat exchanger 1 essentially comprises a plurality of casings 2, of substantially
flattened shape, associated together in a predetermined distanced relationship in
a pile 2a, with respective cavities 3 defined between casings.
[0022] The casings 2, of predetermined width L, are clamped, in a known way, between a first
plate 4 and a second plate 5, the latter provided with joints 5a for the passage,
for example, of the first of the aforementioned fluids.
[0023] In the example, the described exchanger has joints 5a of 1" (one inch).
[0024] Each of the casings 2 is formed from two half-shells 6 welded along a peripheral
strip 6a each of which is equipped, in corresponding positions, with respective holes
7.
[0025] It should be noted that the aforementioned peripheral strip 6a has an outer edge
6b comprising a trim 6c bent square, and that the half-shells 6 are realized in aluminium
sheet of small thickness of between 0.1 and 0.4 mm, preferably 0.3 mm.
[0026] Such respective holes 7, which in the pile 2a are aligned, place the aforementioned
casings 2 in fluid communication with each other.
[0027] In such casings 2, a flow of the aforementioned first fluid is made to flow, whereas
the second fluid is made to flow in the aforementioned cavities 3, all in a
per se known way.
[0028] In accordance with a first characteristic of the invention, the heat exchanger 1
comprises, in each of said cavities 3, a spacer 8, substantially of the sleeve type,
abutting on at the top end and made integral with the aforementioned adjacent casings
around each of the respective holes 7 of the half-shells 6, realizing an inviolable
mechanical connection between adjacent casings.
[0029] Such spacers 8 made integral with the casings 2, for example through brazing or welding,
define, at the respective holes 7, passage collectors for the aforementioned first
fluid, communicating with the inside of the casings 2.
[0030] In accordance with a second characteristic of the invention, the heat exchanger 1
comprises irregularities 9 associated with each spacer 8, which extend in each air
space 3, constituting rigidifying elements of the half-shells 6.
[0031] With particular reference to the example of figures 4 and 5, it should be noted how
such irregularities are in the form of radial spokes 9, projecting radially towards
the outside of said spacer 8 and practically equally angularly spaced on such a spacer
8.
[0032] Advantageously and in accordance with a further characteristic of the invention,
a predetermined number of such radial spokes 9 extending outside of the spacer 8,
in the example a number equal to seven spokes indicated with 9a, extends up to the
aforementioned peripheral strip 6a.
[0033] In particular, such a predetermined number of radial spokes 9a extends up to, and
abuts upon, the aforementioned trim 6c bent square.
[0034] Again advantageously, the remaining radial spokes 9 of the same spacer 8, in the
example three spokes indicated with 9b, are sheared according to a transversal plane,
indicated with T, which constitutes the plane of reference and support for a corrugated
plate, globally indicated with 11, arranged in each of the cavities 3 and called "turbulator"
by the man skilled in the art.
[0035] Regarding this, it should also be stated that a second corrugated plate or turbulator
11a is arranged inside each casing 2.
[0036] The aforementioned corrugated plates 11, 11a have the purpose of increasing the efficiency
of the heat exchange of the heat exchanger 1, increasing the turbulence, by means
of their corrugated surfaces, of the flows of fluids intended for the heat exchange.
[0037] Preferably, the aforementioned radial spokes 9 are formed integrally with the spacer
8 from which they project, and more preferably radial spokes and spacer are a piece
of an extruded profile made from a metallic material selected from the group comprising
aluminium, copper, aluminium alloys, copper alloys and similar metallic materials.
[0038] It should be noted that the thickness s of the spacer 8 and the thicknesses of the
radial spokes 9 have values of between 2 and 4 mm, preferably 3.5 mm.
[0039] Again preferably, each of the aforementioned respective holes 7 of each half-shell
6 is foreseen equipped with a centring edge 12, projecting from the half-shell 6 in
the direction of the air space 3, for the alignment of the spacer 8.
[0040] The main advantage of the heat exchanger according to the present invention lies
in its unusual strength.
[0041] Indeed, thanks to the spacers welded and made integral at the top end on the casings,
a particularly strong structure is given to the pile of casings themselves.
[0042] In this way, an inviolable mechanical connection is realized between adjacent casings,
forming a seal and capable of withstanding violent stresses.
[0043] In particular, the portions of exchanger that according to the prior art were most
subject to explosion are reinforced, in the exchanger according to the invention,
both through the spacers made integral with the casings and through the radial spokes
projecting from each spacer which constitute rigidifying elements for each of the
half-shells.
[0044] The heat exchanger according to the invention, in this way, is particularly suitable
for the heat exchange between pressurized flows of fluids, also for pressures of up
to 35 bar and more.
[0045] Furthermore, the mechanical resistance of the exchanger is improved by the radial
spokes of the spacers, which constitute support elements for each corrugated plate
arranged in the cavities.
[0046] In this way, the corrugated plates are stably locked by the radial spokes in an optimal
position that allows an excellent increase in turbulence of the flow of fluid that
crosses the cavities, and an optimal heat exchange in particular at high pressure
values of such a flow.
[0047] In other words, the heat exchanger according to the present invention allows a heat
exchange to be carried out between a first fluid conveyed inside the casings, and
a second fluid conveyed into the cavities between adjacent casings, in particular
and at most when both of the respective flows of such fluids are at high pressure
values, thanks to the special structure described above.
[0048] Such an unusual strength of the heat exchanger according to the invention is achieved,
advantageously, simultaneously maintaining a compact structure of the exchanger, through
half-shells realized with a low thickness as required for an effective heat exchange.
[0049] A further advantage achieved by the heat exchanger according to the invention lies
in the minimal or negligible pressure drop that the fluids undergo during the heat
exchange, thanks to the aforementioned mechanical connection that ensures a better
seal than that which has been provided up to now by the prior art.
[0050] It should be stated, furthermore, that radial spokes extending up to the trim of
the peripheral strip, advantageously bent square, give the heat exchanger according
to the invention an effective mechanical resistance also against accidental knocks,
preserving the heat exchanger from dents and similar undesired damage that could derive
from such knocks.
[0051] Now, with particular reference to the example of figure 6, a variant embodiment of
the present invention is described for which details and cooperating parts having
the same structure and operation as the previous example embodiment shall be indicated
with the same reference numerals and symbols.
[0052] In such a variant embodiment, the heat exchanger comprises spacers 8, substantially
shaped like a sleeve, made integral at the top end on adjacent casings 2 and comprising
radial spokes 90 projecting towards the inside of the spacer 8.
[0053] The aforementioned radial spokes 90 projecting towards the inside of the spacer are
sheared, at their free ends, so as to surround the centring edge 12 of the respective
holes 7.
[0054] Again with reference to the example of figure 6, it should be noted that the spacer
8 comprises a first portion 80a with a curved profile, and a second portion 80b with
a squared profile constituting the reference plane for the turbulator 11.
[0055] In such a variant embodiment it should be noted that, advantageously, the pressure
that from the inside acts upon the spacer, due to the fluid that crosses the casings,
is completely counterbalanced by a pressure that acts from the outside on the spacer,
due to the fluid that crosses the cavities.
[0056] In the example of figure 7 a further variant embodiment of the heat exchanger in
accordance with the invention is represented.
[0057] In such a variant embodiment the heat exchanger comprises spacers 8, substantially
shaped like a sleeve, each equipped with radial spokes projecting towards the inside
of the spacer, indicated with 90a, and radial spokes projecting towards the outside
of the spacer and indicated with 90b.
[0058] It can be seen that the aforementioned radial spokes 90b extending towards the outside
of the spacer 8 are in prolongation of the radial spokes 90a extending towards the
inside of the spacer.
[0059] It is important to note that, in accordance with a further variant embodiment shown
with reference to the example of figure 8, the holes 7 open on the half-shells 6 of
the casings 2 are oblong.
[0060] Holes extending transversally are particularly advantageous in the case of large
widths of the exchanger, foreseen to withstand high flow rates of the fluid circulating
in the half-shells of the exchanger itself.
[0061] The man skilled in the art can bring numerous modifications to each of the four variant
embodiments of the heat exchanger described above in order to satisfy contingent and
specific requirements, all of these modifications in any case being covered by the
scope of protection of the invention, as defined by the claims listed hereafter.
1. Heat exchanger for the heat exchange between a first fluid and a second fluid, of
the type comprising a plurality of casings (2), of substantially flattened shape and
of predetermined width (L), arranged in a pile (2a), with an air space (3) defined
between adjacent casings in the pile, and each formed from two half-shells (6) welded
along a peripheral strip (6a), said casings (2) being in fluid communication with
each other through respective holes (7) opening into said air space (3), characterized in that it comprises, in said air space (3), at least one spacer (8), substantially of the
sleeve type, made integral at the top end with said adjacent casings (2) around the
respective holes (7) opening into said air space (3).
2. Heat exchanger according to claim 1, characterized in that it comprises irregularities (9) associated with said at least one spacer (8), said
irregularities (9) extending in said air space (3) to rigidify the half-shells (6).
3. Heat exchanger according to claim 2, characterized in that said irregularities (9) are radial spokes (9a, 9b, 90, 90a, 90b) extending radially
from said at least one spacer (8).
4. Heat exchanger according to claim 3, characterized in that said radial spokes (9a, 9b, 90b) extend outwards.
5. Heat exchanger according to claim 3, characterized in that said radial spokes (9o, 90a) extend inwards.
6. Heat exchanger according to claim 3, characterized in that said radial spokes are radial spokes extending outwards (90b) and radial spokes extending
inwards (90a).
7. Heat exchanger according to claim 6, characterized in that said radial spokes extending outwards (90b) are in prolongation of said radial spokes
extending inwards (90a).
8. Heat exchanger according to claim 4 or 6, characterized in that a predetermined number of said radial spokes (9a) extending towards the outside of
said at least one spacer (8) extends at least up to said peripheral strip (6a).
9. Heat exchanger according to claim 8, characterized in that each half-shell (6) comprises, at an outer edge (6b) of said peripheral strip (6a),
a trim (6c) bent square, and in that said predetermined number of radial spokes (9a) extending on the outside extends
up to said trim (6c).
10. Heat exchanger according to claim 2, characterized in that said irregularities (9) are formed integrally with said at least one spacer (8).
11. Heat exchanger according to any one of claims 2 to 10, characterized in that said at least one spacer (8) and said irregularities (9) are a piece of an extruded
profile.
12. Heat exchanger according to claim 11, characterized in that said piece of extruded profile is made from a metallic material selected from the
group comprising aluminium, aluminium alloys, copper, copper alloys and similar metallic
materials.
13. Heat exchanger according to claim 3, characterized in that said radial spokes (9a, 9b, 90, 90a, 90b) are practically equally angularly spaced.
14. Heat exchanger according to claim 3, characterized in that a predetermined number of said radial spokes (9b) are sheared according to a plane
(T) constituting the reference and support plane for a corrugated plate (11) arranged
in said air space (3).
15. Heat exchanger according to any one of the previous claims, characterized in that at least one of said respective holes (7) opening into said air space (3) is equipped
with a centring edge (12) for said at least one spacer (8).
16. Heat exchanger according to any one of the previous claims, characterized in that said respective holes (7) are oblong in a predetermined direction.
17. Heat exchanger according to claim 16, characterized in that said respective holes (7) are oblong in the direction of the width (L) of said casings
(2).
18. Heat exchanger according to any one of the previous claims, characterized in that said at least one spacer (8) has a predetermined thickness of between 2 and 4 mm,
preferably 3.5 mm.