[0001] The invention relates to a heat exchanger, manufactured from light metal by means
of casting technique, comprising at least a water duct, a burner space and elements
increasing the heat-transferring area. Such a heat exchanger is known from European
patent specification 0 547 641.
[0002] This known heat exchanger comprises two box-shaped parts attached to each other with
the open sides facing each other, with the inclusion of a burner space. Each part
comprises, at the side thereof facing the burner space, a number of series and columns
of projections that increase the heat-transferring area, which projections always
extend in the same direction, towards each other in the mounted condition of the heat
exchanger, and have their free ends approximately abutting against each other. At
the outside remote from the projections, each part comprises a water duct extending
zig-zag from the bottom upwards. The lateral sides of the heat exchanger are formed
by substantially closed, flat walls. During use, flue gases heated by means of a burner
are passed from the top side of the heat exchanger through the burner space along
the projections, while heat is transmitted to the projections. The projections transfer
the heat to water flowing through the water ducts. This known heat exchanger is easy
to manufacture, compact and practical in use, and has a favorable efficiency.
[0003] This known heat exchanger has as a drawback that the heat-transferring area is relatively
small compared with the dimensions of the heat exchanger. As a consequence, the efficiency
is not optimal. A water duct extends on two sides of the heat exchanger only, the
other sides are clear and act as radiation surface to the environment, so that heat
is lost, particularly when no or insufficient insulation measures are taken. The projections
are arranged so that They transfer the heat in a favorable manner to the or each water
duct, which means that they all connect to the parts of each heat exchanger part that
face the water duct. During use, as a consequence of the difference in heat transfer
of the different parts of the heat exchanger, stresses may occur in the material which
may cause damages or even breakage.
[0004] FR-A-694.311 discloses a heat exchanger comprising a closed, cylindrical inner wall
and a rib extending spiral-wise around said inner wall, formed integrally therewith.
From the inside of said inner wall elements increasing the heat transferring area
extend radially into the space enclosed within said inner wall, in which space also
a burner can be provided. A cylindrical outer sleeve is manufactured independently
and positioned over said inner sleeve and rib, for forming a spiral-wise extending
water duct. A water supply pipe extends through said rib, between the inner wall and
the outer wall, from the bottom part of said heat exchanger to the top part of said
water duct, for introduction of water into said water duct. A cap is connected to
the top side of said heat exchanger for at least partly closing said burner space.
This known heat exchanger has a number of parts which have to be assembled, wherein
at least the outer sleeve and the cap are made of plate metal.
[0005] The object of the invention is to provide a heat exchanger of the type described
in the preamble of the main claim, wherein the drawbacks mentioned are avoided, while
the advantages thereof are retained. To that end, a heat exchanger according to the
invention comprises the features of claim 1.
[0006] The substantially polygonal form of the heat exchanger provides a favorable ratio
between the contents and the wall surface of a heat exchanger. In this connection,
a polygonal section should be understood to mean a section which comprises as least
two, and in particular four or more angles and/or is partly built up of bent lines.
The angles can be sharp but can also have a bend radius. Moreover, the water duct
extends along at least almost the entire outside of the heat exchanger, so that the
heat of the flue gases is optimally used and heat radiation to the environment is
minimized. During use, the heat exchanger is as it were insulated by a water jacket.
Moreover, as the elements increasing the heat-transferring area extend from the inner
wall at least in a portion of the heat exchanger, distributed over the circumference
of the section thereof, the heat of the flue gases is optimally taken up and distributed
over the circumference of the inner wall and thus transferred to the water duct. Consequently,
substantial temperature differences over the inner wall are prevented in a simple
manner. A heat exchanger according to the invention can be manufactured and employed
in a simple manner and is economical in production, use and maintenance.
[0007] During production of the heat exchanger, the water duct, wound spiral-wise around
the inner wall, has the advantage that the casting core or casting core parts can
readily be removed therefrom, because no or at least few bends occur therein, which
bends, if present, are moreover only faint. The water duct extends in a flowing manner,
like a snake around the inner wall. This prevents core material, for instance sand,
wax or plastic, from staying behind in parts of the water duct and fouling and damaging
the apparatus. During use, such a spirally wound water duct has the advantage that
the water resistance of the heat exchanger is low, at least lower than in the case
of a water duct that extends zigzag. Thus, the advantage is for instance achieved
that a water pump of a lower capacity can be used, that there can be a more accurate
control, that a longer water duct or greater powers can be used and like advantages.
Moreover, the water duct can be cleaned more properly and foulings are more simply
prevented from adhering in the water duct during use.
[0008] A further advantage of arranging a spirally wound water duct is that a casting core
required therefor can be fitted and supported in a mold in a simpler manner, so that
the manufacture of such a heat exchanger is simpler, all the more because the number
of core holes in the water duct that are to be finished and sealed after casting is
smaller than in the case of the known heat exchangers. For instance, with one core
support, two windings of the water duct that lie side by side can in each case be
supported.
[0009] In this connection, spiral-wise should be understood to mean substantially continuous,
so that during use, water can flow, in a movement extending around the inner space,
from a position adjacent one end of the heat exchanger in the direction of the opposite
end without this involving the flow direction being strongly deflected. Any bends
in the water duct are faint, certainly less than 180°, and preferably less than 90°.
Particularly advantageous is an embodiment wherein no bends are included other than
those having a bend radius that is not smaller than the section of the water duct
at that location, or that are about 45° or less.
[0010] In a preferred embodiment, a heat exchanger according to the invention is further
characterized by the features of claim 4.
[0011] A heat exchanger constructed in one piece has the advantage that this requires fewer
assembling operations during the production of a heating apparatus designed therewith,
and that, moreover, sealing problems of parts of a heat exchanger are avoided. Accordingly,
such a heat exchanger is cheaper and more reliable in production and use.
[0012] In a first advantageous embodiment, a heat exchanger according to the invention is
further characterized by the features of claim 5.
[0013] An at least partly symmetrical embodiment of a heat exchanger according to the invention
inter alia offers the advantage that during the use thereof, a uniform heat distribution
is obtained, which is advantageous in terms of heat engineering and material. Moreover,
a casting core assembly for the manufacture thereof can be built up from equal parts,
which is advantageous in terms of manufacturing. This involves a reduction or even
an elimination of the chance of composition errors of the casting core assembly.
[0014] In a further advantageous embodiment, a heat exchanger according to the invention
is further characterized by the features of claim 7.
[0015] Such a heat exchanger can be manufactured as follows. By means of a mold, a casting
core for the water duct is formed by forming a cast of the water duct in, for instance,
molding sand or wax. This casting core is then removed in for instance one or more
parts from the or each mold, and next, if more than one, the parts are interconnected
to form a complete first casting core. If the walls of the water duct extended completely
spiral-wise and without the above-mentioned clearing spaces therebetween around the
inner wall, the core parts would be damaged during removing, because a part thereof
would be stuck behind a non-clearing part of each winding of this wall. By providing
the clearing spaces on a division seam of the first casting core mold, i.e. at the
level of the or each face that constitutes the contact face between the casting core
mold parts, so that each casting core mold part is withdrawable in an approximately
radial direction, the first casting core or each casting core part thereof can be
removed without damage. Thus, the advantage is achieved that an undamaged first casting
core can be obtained in a simple manner without this requiring, for instance, sliding
parts or parts that can be moved otherwise in the or each mold.
[0016] In a first further embodiment, such a heat exchanger according to the invention is
characterized by the features of claim 8.
[0017] In this embodiment, the water duct wall is wound substantially entirely spiral-wise,
and the clearing spaces are formed by profiles on the water duct wall. As a matter
of fact, it is of course also possible to provide the water duct so as to be alternately
inclined and right-angled relative to the longitudinal axis of the heat exchanger,
so that the right-angled part in each case forms a space that can be cleared in tangential
direction. This does create a slightly larger number of bends in the water duct, but
these bends can be relatively faint.
[0018] In a further advantageous embodiment, a heat exchanger according to the invention
is characterized by the features of claim 9.
[0019] In such an embodiment, a casting core for at least the burner space, the elements
increasing the heat-transferring area, and the inner wall can be formed in a particularly
simple manner without this requiring moving parts in the mold. Moreover, the elements
increasing the heat-transferring area can thus be readily and optimally distributed
over the surface of the inner wall.
[0020] In a further advantageous embodiment, a heat exchanger according to the invention
is characterized by the features of claim 12.
[0021] In this embodiment, the flow resistance of the heated gases through the heat exchanger
increases in the direction away from the burner. Accordingly, the heat transfer, at
least the intensity of the contact with the elements that increase the heat transfer,
increases in the same direction. The rate at which the gases are cooled down is thereby
reduced. This is advantageous from an energetic viewpoint.
[0022] In a further embodiment, a heat exchanger according to the invention is further characterized
by the features of claim 13.
[0023] A polygonal burner offers the advantage that it can optimally be adjusted to the
shape of the burner space of the heat exchanger. Moreover, such a burner may comprise
a series of flat or single-curved burner surfaces, as a result of which a burner having
a favorable burner pattern can be obtained in an economical manner.
[0024] Further advantageous elaborations of a heat exchanger according to the invention
are described in the subclaims.
[0025] The invention further relates to a casting core apparatus for manufacturing a heat
exchanger according to the invention, characterized by the features of claim 14 or
15.
[0026] The invention moreover relates to a method for manufacturing a heat exchanger according
to the invention, characterized by at least the features of claim 16.
[0027] The invention moreover relates to a heating apparatus comprising a heat exchanger
according to the invention.
[0028] To explain the invention, exemplary embodiments of a heat exchanger and a heating
apparatus will hereinafter be described, with reference to the accompanying drawings.
In these drawings:
Fig. 1 shows, in sectional side elevation, an embodiment of a heat exchanger according
to the invention;
Fig. 2 shows, in sectional top plan view, a heat exchanger taken on the line II-II
in Fig. 1;
Fig. 3 shows, in sectional top plan view, a heat exchanger taken on the line III-III
in Fig. 1;
Fig. 4 shows, in sectional top plan view, a casting core apparatus according to the
invention;
Fig. 5 shows a portion of a casting core for a water duct;
Fig. 5A shows a detail of a clearing space in a water duct in a first embodiment;
Fig. 5B shows, in cut-off perspective view, a portion of a mold for forming a casting
core part for a water duct of a heat exchanger according to the invention;
Fig. 6 shows, in side elevation, a portion of a heating apparatus according to the
invention; and
Figs. 7A-E show, in sectional top plan views taken on the line VII-VII in Fig. 6,
a number of alternative embodiments of a heat exchanger with a burner according to
the invention.
[0029] Figs. 1, 2 and 3 show, in sectional views, a heat exchanger 1 according to the invention.
The heat exchanger 1 comprises an inner wall 2 and an outer wall 3 arranged around
and aligned with the inner wall 2. Included between the inner wall 2 and the outer
wall 3 is a water duct wall 4, whereby a spiral-shaped water duct 5 is formed on the
outside of the inner wall 2. From the inside of the inner wall 2, elements 6 increasing
the heat-transferring area extend inwardly, approximately at right angles to the longitudinal
direction of the heat exchanger 1. In the top range of the heat exchanger, these elements
6 are formed by partitions 34, extending parallel to each other in the longitudinal
direction of the heat exchanger 1, i.e. vertically inwardly during normal use. In
the bottom range of the heat exchanger 1, these elements 6 are formed by projections
35, disposed in staggered rows and/or columns. The shape and positions of the elements
6 will be further discussed hereinafter. The heat exchanger 1 is formed in one piece
through casting and is manufactured from light metal. Light metal should be understood
to mean, at least, aluminum and aluminum alloys, brass and brass alloys.
[0030] The heat exchanger 1 has a substantially mirror-symmetrical, blocked shape with,
in the embodiment shown, an approximately rectangular top plan view, which means that
a highly favorable ratio is obtained between contents, heat-transferring area and
water duct contents. The heat exchanger 1 is formed by means of a casting core assembly
7 as shown in Fig. 4. In Fig. 4, a quarter of the casting core assembly 7 has been
left out. For clarity's sake, this quarter is schematically shown (in contour) in
broken lines. The casting core assembly 7 is of the type that is lost during or after
the casting of the heat exchanger 1 and is for instance formed from sand, wax or synthetic
material, such as polystyrene, or from combinations thereof. Moreover, parts such
as slides can of course be included, which can in fact be reused, if necessary.
[0031] The casting core assembly 7 comprises an outer box B wherein the shape of the outside
of the heat exchanger 1 is substantially fixed. The casting core assembly 7 further
comprises an inner core 8 and a water duct core 9. These cores are successively described.
[0032] The inner core 8 can be manufactured in portions and then be assembled from parts,
or can be of a one-piece construction. Manufacturing the inner core 8 in portions
has the advantage that the equipment required therefor is relatively cheap, at least
as far as cost price is concerned, yet the processing costs involved are relatively
high. For manufacturing the inner core in one part, relatively costly equipment is
necessary, yet an inner core 8 thus manufactured requires relatively little finishing.
[0033] In the embodiment shown in the drawing, the inner core 8 is composed of four sectors
I-IV, to be referred to as segments 10. Each segment 10 comprises about a quarter
of the section of the space 11 enclosed within the inner wall 2, the opposite sectors
I and III being substantially mirror-symmetrical, just as the opposite sectors II
and IV. As a matter of fact, the four sectors I-IV can also be equal to each other,
in which case, for manufacturing the sectors, only one mold may suffice and, moreover,
errors during the assembly of the inner core 8 are avoided. Each sector I-IV comprises
a large number of elements 6 which extend substantially parallel to each other, at
right angles to the longitudinal direction of the sector I-IV in question. The elements
6 extend so that they can be withdrawn, in such a manner that the sector in question,
after the formation thereof, can be drawn from a mold used for the formation in the
direction of the longitudinal edge C which, in a compound inner core 8, is directed
towards the other sectors. Hence, a thus formed segment 10 approximately has the shape
of a quarter of a square and has, in the outer face 12, a large number of parallel
recesses 13, each having the shape of the elements 6 to be formed.
[0034] The side faces 14 of the sectors I-IV, i.e. the faces which, in the compound inner
core 8, abut against each other, are irregularly shaped. A number of recesses 13'
extend beyond the (fictitious) boundary line 15 of the quarter enclosed by the relevant
sector 10. These recesses 13' extending therebeyond are provided so that in a compound
inner core 8, they lie between recesses 13 in the adjoining side face 14 of the adjacent
sector. This means that in the cast heat exchanger 1, a number of projections 35 cross
each other at the location where two sectors of the compound inner core 8 abutted
against each other during casting. Thus, a suitable density of projections 35 on the
different parts of the inner wall 2 is obtained, as a result of which, during use,
no substantial differences in heat transfer are created, which is advantageous in
terms of heat engineering and construction.
[0035] The sectors I-IV are glued together or joined otherwise with the side faces 14 against
one another, to obtain the compound inner core 8 shown in Fig. 4. In the embodiment
shown, four sectors I-IV are opted for, but of course, a different number can be chosen
as well, for instance two, three or more than four, which may be advantageous, in
particular in the case of relatively large dimensions of the heat exchanger. The direction
of the partitions 34 and the projections 35 will always have to be chosen depending
on the number of sectors.
[0036] When an inner core 8 is manufactured in one piece, a tool having different movable
parts (four in the embodiment shown) is used. In the starting situation, a tube with
the relevant inner section corresponding to the inside of the inner wall 2, wherein
elements 6 extend inwardly in the desired pattern, is filled with, for instance, molding
sand, which is allowed to harden. Then, the elements 6 are withdrawn outwards in segments
until they extend entirely outside the molding sand. For this purpose, the tube can
be divided into four quadrants, each comprising elements 6 fixedly connected thereto,
in accordance with the segments I-IV of the segmented inner core 8. When these four
quadrants are being drawn away, the entire inner core 8 is then directly clear. However,
the elements 6 can also be withdrawable through the wall of the tube, after which
the inner core 8 should subsequently be removed from the tube, which tube can, of
course, also be divisible for that purpose. This also permits the use of elements
6 that have such a position relative to each other that they are not jointly withdrawable,
for instance oblique projections. They can then be withdrawn simultaneously or individually
in the suitable direction if they are moveable independently of each other. As a result,
similar projections can be used, which is advantageous for the heat transfer and minimizes
stresses in the cast heat exchanger. In fact, the heat exchanger shown in the drawing
can of course also be manufactured in this manner.
[0037] Depending on the form of the burner that is inserted, during use (as will be further
discussed hereinafter), into the top side of the burner space 11 between the partitions
34, all elements 6 can approximately have the same length, for instance when a substantially
square or polygonal burner is inserted into a heat exchanger of a section having a
similar form, or changing lengths, for instance when a burner having a differently
shaped section is used in a heat exchanger of an approximately square section. Inter
alia the length, the section, the shape and the mutual distance and position of the
elements 6 relative to each other determine the heat transfer during use between the
flue gases and the water in the water duct.
[0038] In the embodiment shown, the water duct core 9 is manufactured in two parts in one
or more molds 16 and is schematically partly shown in Fig. 5B. In the embodiment shown,
the water duct core 9 is formed in two parts 9', 9", but a different number of parts
can of course be used as well. Two parts has the advantage that relatively few joints
are necessary, while the core parts 9', 9" can still be manufactured relatively simply.
Moreover, these core parts 9', 9" can readily be provided around the inner core 8.
Further, it is possible to construct the water duct core 9 in one piece, in particular
in the case of relatively short heat exchangers, wherein the mold 16 can for instance
be removed in portions from the water duct core 9.
[0039] As described, the water duct 5 is substantially spiral-shaped, wound around the outside
of the inner wall 2 of the heat exchanger 1. In this connection, spiral-wise should
be understood to mean substantially continuous, so that during use, water can flow,
in a movement extending around the inner space, from a position adjacent one end of
the heat exchanger in the direction of the opposite end without this involving the
flow direction being strongly deflected. Any bends in the water duct are faint, certainly
less than 180°, and preferably less than 90°. Particularly advantageous is an embodiment
wherein no bends are included other than those having a bend radius that is not smaller
than the section of the water duct at that location, or that are about 45° or less.
Of course, connection parts for a feed and discharge pipe can indeed include a relatively
sharp angle with the water duct, because they will be able to be cleared from the
outside. However, this is not advantageous. The water duct 5 being spiral-shaped,
the water duct core 9 can readily be removed after casting, if necessary, because
no bends of about 90° or even of 180° are included, as in the known heat exchangers.
This means that fewer or even no openings for cleaning the water duct need to be included,
which means that fewer finishing operations of the cast heat exchanger 1 are necessary.
[0040] In the embodiment shown in Figs. 1-3, the corners 40 of the heat exchanger 1 are
rounded, so that, in top plan view, each wall 2, 3 of the heat exchanger 1 comprises
four relatively long, flat first wall parts 41, at right angles to each other and
interconnected by bent second wall parts 42. The bend radius R of the second wall
parts 42 is preferably not less than the section D of the water duct 5.
[0041] By virtue of these features, the core 9 is readily removable and, moreover, the resistance
in the water duct 5, during use, is kept low. Further advantages will be further discussed
hereinafter.
[0042] To be able to remove the water duct core parts 9', 9" (Fig. 5) from or out of the
or each mold 16, these parts should be of a withdrawable construction. Figs. 5A and
5B give two possibilities for achieving such withdrawal.
[0043] Fig. 5A is an enlarged view of a clearing space 17 between two wall parts 4 of the
water duct 5, in a first embodiment. The clearing direction of the core parts 9',
9" of the mold 16 is at right angles to the plane of the drawing. The wall parts 4
are thickened so that the space therebetween has, in each case, no undercuts in at
least the clearing direction, i.e. when the heat exchanger 1 is held vertically and,
accordingly, the water duct 5 extends upwards/downwards spiral-wise, the relevant
wall parts are approximately parallel or receding in the clearing direction. This
permits the portion of the core parts 9 therebetween to be drawn away in approximately
horizontal direction without parts being left behind undercuts. This means that the
core parts 9', 9" can be removed and joined together to form the desired water duct
core 9 without damage.
[0044] Fig. 5B shows an alternative embodiment of a mold 16 for forming at least the wall
parts 4 of the water duct 5 for a heat exchanger of an octagonal section. In this
embodiment, the clearing direction of the water duct core part 9', 9" (not shown)
from the mold 16 is indicated by the arrow P. By way of illustration, three axes X,
Y and Z, at right angles to each other, are indicated by dash and dot lines. The upper
and lower parts of the mold 16 are broken away.
[0045] The water duct wall 4 comprises in each winding W
1-5 two first water duct wall parts 4A provided on opposite sides and extending in a
plane parallel to the X-axis and the Y-axis, parallel to the clearing direction P.
Each pair of first water duct wall parts 4A is interconnected by a second water duct
wall part 4B that is inclined relative to the Z-axis and that is parallel to the Y-axis.
This means that both the space 17A between two first water duct wall parts 4A lying
one above the other, and the space 17B between two second wall parts 4B lying one
above the other, can be cleared in the direction P.
[0046] Each water duct core part 9, 9" comprises (Fig. 5) a series of parallel parts 31.
These parts are interconnected by a transverse beam 18 on which the parts 31 are arranged,
via support pins 19. The parts 31 comprise a first part 50 that is slightly oblique
relative to the longitudinal direction of the beam 18, which is a representation of
the inclined portion of the water duct 5 (second space 17B). Further, each part 31
comprises two second parts 51, connecting to both ends of the first part 50 and extending
at right angles to the longitudinal direction of the beam 18, which parts form a representation
of parts of a flat portion of the water duct 5 (first space 17A). The first part 50
is in each case connected to a second part 51 via a third part 52 which is a representation
of the portion 17C of the water duct 5 forming the bevelled or rounded corner 40.
The parts 31 together form, when the core parts 9', 9" are joined together, a representation
in, for instance, molding sand of the water duct 5 (Fig. 5).
[0047] In fact, it is also possible to form the casting core 9 by means of a mold 16 provided
with slides or the like, or by means of a mold 16 of the lost type, which means that
it is lost during or after the formation of the casting core 9.
[0048] The casting core assembly 7 is rendered ready for use through the following steps.
In a first outer box part B', a cast is provided of a first half of the outside contour
of the heat exchanger, i.e. it is substantially determined by the outer wall 3. In
the hollow thus formed, a first part 9' of the water duct core 9 is placed, with the
beam 18 being received in the first outer box part so that only the support pins 19
and the parts 31 extend inside the hollow. The support pins 19 have such a length
that the parts are spaced from the inside of the hollow at a distance corresponding
to the desired wall thickness of the outer wall 3, for instance some millimeters.
Next, the inner core 8 is placed in the parts 31 and spaced therefrom at a distance
corresponding to the desired thickness of the inner wall 2. Then, the second part
9" of the water duct core 9 and the second outer box B" containing a cast of the second
half of the outside contour of the heat exchanger are provided over the inner core
in a similar manner, to obtain a substantially closed casting box B. Provided in one
or each outer box B', B" are a number of gates and risers (not shown in the drawing)
for feeding therein the casting melt, for instance aluminum or brass or alloys of
one or both metals.
[0049] After the heat exchanger has cooled down and hardened, the casting box is opened
and the casting cores are removed, i.e. in so far as they have not disappeared already
during casting. Because the water duct 5 is formed so as to be continuous, the removal
of at least the water duct core 9 is simple, while for removing the inner core, sufficient
space is present within the heat exchanger. After the removal of the casting cores,
the openings in the walls of the heat exchanger are closed, wherever this is necessary,
and the heat exchanger can be finished and incorporated into, for instance, a heating
apparatus.
[0050] Fig. 6 shows, in side elevation, a portion of a heating apparatus 20 comprising a
heat exchanger 1 according to the invention. In this heating apparatus 20, the heat
exchanger 1 is vertically arranged, i.e. the longitudinal axis thereof extends in
a vertical plane. However, it is also possible to arrange such a heat exchanger 1
differently, for instance in a horizontal or inclined position. At the top end thereof,
a burner 21 is inserted into the heat exchanger 1, which has for instance a jacket-shaped
burner deck 22. The burner has a relatively slight length compared with the heat exchanger
1. The top side of the heat exchanger is closed over the burner 21 by a cover cap
36, extending partly along the rear side of the heat exchanger and connected at that
location with a fan 24. The cover cap 36 thus forms a feed pipe 23 for the burner
21. By means of the fan 24, a combustible gas or gas-air mixture is fed under pressure
to the burner 21, wherein it is combusted. The hot flue gases are then forced between
the elements 6.
[0051] An impeller 25 (shown in broken lines in Fig. 1) is inserted between the elements
6 in the inner space of the heat exchanger, to a position adjacent the burner 1. This
impeller 25 largely fills up the space 11 below the burner 21 between the elements
6, whereby the flue gases are forced to flow between the partitions 34 and, next,
between the staggered projections 35 while transferring the heat to the partitions
34, the projections 35 and, directly or indirectly, to the inner wall 2. The partitions
34 have a radial height such that between the longitudinal edges thereof remote from
the inner wall 2 and the impeller 25, some space is left free. At the ends facing
the burner 25, the partitions 34 are bevelled in the direction of the inner wall 2.
The impeller 25 has a height such that the end thereof facing the burner 21 is approximately
flush with the beginning of the bevelled ends of the partitions 34, so that a free
space remains between the burner 21 and the impeller. As the partitions 34 are spaced
from the impeller and, moreover, create little flow resistance, the flue gases can,
during use, flow relatively freely along the partitions 34, with slight heat exchange.
Hence, the flue gases are cooled down slowly, which is advantageous for the emission
values of the heating apparatus.
[0052] Because the projections are disposed in staggered rows and/or columns, a labyrinth-shaped
flow path for the flue gases is formed in the lower range, so that the heat transfer
during use is improved. The impeller 25 is for instance a bush filled with fire-proof,
heat-resistant fibers or a ceramic bush. At least a number of the projections 6 almost
abut against the outside of the impeller 25. At its lower end, a flue gas discharge
26 connects to the inner space of the heat exchanger 1. The flue gases can condense
in the heat exchanger 1 and are discharged via the flue gas discharge 26. Adjacent
the bottom side, the flue gas discharge 26 connects to the heat exchanger in a sidewall
thereof, and can be provided with a condensate discharge opening, closable by a cap.
The flue gas discharge 26 can be cast together with the heat exchanger 1, as integral
part thereof, but can also be provided afterwards, with the interposition of a packing.
Thus, a greater freedom of choice is obtained in positioning the flue gas discharge
26 relative to the heat exchanger 1. In the embodiment shown, the flue gas discharge
duct 26 is rounded on the outside, and a particularly complete heating apparatus 20
is obtained having particularly favorable operating properties.
[0053] Adjacent the lower end, the water duct 5 is connected to a return pipe 29 and adjacent
the upper end, it is connected to a feed pipe 30 of, for instance, a heating circuit
(not shown). During use, water is passed through the water duct 5 and heated by means
of the heat emitted by the flue gases. As the water duct 5 encompasses almost the
entire heat exchanger 1, little heat is lost to the environment, while no specific
insulating measures are necessary. As the water duct 5 extends spiral-wise and has
no sharp angles, the water duct has a low water resistance, so that a pump of a relatively
small capacity and/or a relatively long water duct 5 can be used, which means that
relatively substantial powers are possible with a heating apparatus according to the
invention. This also enables the cleaning of the water duct 5 to be carried out in
a relatively simple manner.
[0054] The heating apparatus can further be designed in a known manner with, for instance,
radiators, a thermostat and a control device and like known attributes. A heating
apparatus according to the invention, in particular a heating boiler suitable therefor,
is compact and has a high efficiency, while it can be manufactured and employed in
a simple and relatively advantageous manner. The convenience time, i.e. the time between
the occurrence and the fulfilment of an established heat requirement, is relatively
short, which has a comfort-increasing effect.
[0055] In the exemplary embodiment shown, the burner has a burner deck 22 which extends
substantially transversely to the longitudinal direction of the heat exchanger 1,
parallel to the section II-II in Fig. 1. However, it is also possible to use a burner
wherein the burner 21 extends at least partly between the partitions 34 and, possibly,
the projections 35 and has its outwardly facing sides provided with burner faces 22.
Different embodiments thereof are shown in Figs. 7A-7E. Such an embodiment inter alia
offers the advantage that the entire burner surface 22 faces in the direction of the
elements 6 increasing the heat-transferring area. In that case, the impeller extends
less far and preferably has an end face thereof abutting against or lying adjacent
an end face of the burner 21.
[0056] Figs. 7A-E schematically show a series of sectional top plan views of a heat exchanger
1 with a burner 21. For clarity's sake, the elements 6 increasing the heat-transferring
area have been left out, the inner 3 and outer walls 3 are represented as single lines.
[0057] Fig. 7A shows an octagonal heat exchanger 101 with an octagonal burner 121. The burner
121 comprises a closed end face 129 and eight burner faces 122, arranged parallel
to the longitudinal axis of the burner 121, at right angles to the end face 129. The
burner faces 122 have their longitudinal edges slidably confined in link-shaped connection
parts 130. This allows the burner faces 122 to deform freely in a direction parallel
to their own planes, so that stresses are prevented. The burner faces 122 are flat,
which renders the manufacture of the burner 122 simple, and, accordingly, relatively
cheap, while the burner faces 122 are optimally positioned relative to the elements
6, which may all have an approximately equal length and heat-transfer capacity. This
heat exchanger has for instance eight planes of symmetry.
[0058] Fig. 7B shows a hexagonal heat exchanger 201 having six equally large side faces,
with a round, cylindrical burner. This burner 221 has a cylindrical burner face 222
and a closed end face 229. The burner face 222 is included in slide links, while behind
the burner face 222, a distributor plate 231 is included for distributing the gas
flow or gas-air flow over the burner plate 222, so that a better, calmer burner pattern
is obtained.
[0059] Fig. 7C shows a heat exchanger 301, comparable with the heat exchanger according
to Fig. 7B, but with rounder corners. Consequently, the water duct 5 exhibits an even
more flowing configuration. Two opposite sides 332 have a greater length than the
other sides, so that the heat exchanger is relatively flat in one direction. The burner
321 is designed as the burner 121 according to Fig. 7A, but with a hexagonal shape
and six burner faces 322.
[0060] Fig. 7D shows a substantially rectangular heat exchanger 401 having a likewise rectangular
burner 421. This heat exchanger and can readily be fitted against, for instance, a
wall so as to be relatively flat. The burner 421 has in each case one burner face
422A on the opposite short side and two burner faces 422B on the two long sides. Hence,
the burner faces 422A and B are relatively short, so that they will deform relatively
slightly during use.
[0061] Fig. 7E shows a heat exchanger 501 having one flat (rear) side 532 and a curved second
(front) side 533. The burner 521 has a similarly shaped section with five burner faces
522. This heat exchanger 501 has the advantage of a flat side for simple assembly
and an advantageous ratio between volume and heat-transferring area.
[0062] Of course, combinations of shapes and assemblies of heat exchangers and burners are
possible, which can be selected depending on the desired applications.
[0063] A heat exchanger according to the invention can of course also be assembled from
parts, but such embodiment has as a disadvantage that additional sealings, assembling
operations and/or assembling means are necessary.
[0064] The invention is by no means limited to the embodiments shown and described in the
drawings and specification. Many variations thereto are possible.
[0065] For instance, the water duct may be double-wound, i.e. consist of two or more water
ducts wound side by side or one over the other, while each water duct can be connected
to the same or to separate heating circuits. The length and the flow-through area
of the water ducts may differ, as well as the position thereof relative to the burner,
so that, during use, water of different temperatures can be obtained from the different
water ducts. Further, the projections may be formed differently or be designed as,
for instance, partitions or ribs. The projections may have the same length everywhere,
or may differ in length more substantially. The length and diameter of the heat exchanger
and the passage area, and the pitch of the water duct may be chosen differently, in
accordance with the desired capacities, while, also, a different type of burner may
be used. Moreover, the heat exchanger may have different sections at different levels,
for instance for constricting or widening the flow-through area for the flue gases
or for creating building-in space for, for instance, control and regulating means
and/or a pump within the describing circumferential face of the heat exchanger, so
that it can be used in an even more compact heating apparatus. Instead of the impeller,
other means may be included for the same purpose, for instance a water-filled vessel
that can act as boiler or a water duct that can act as tapping spiral. The feed pipe
for the fuel, the feed and discharge of water, and the flue gas discharge may be of
a different construction.
1. A heat exchanger (1), manufactured from light metal by means of casting technique,
comprising at least a water duct, a burner space (11) and elements (6) increasing
the heat-transferring area, characterized in that the heat exchanger (1) comprises a closed, polygonal or partly bent inner wall (2),
wherein the water duct (5) extends spiral-wise along the outside of the inner wall
(2) and the burner space (11) extends inside the inner wall (2), wherein at least
in a portion of the heat exchanger (1) on the inside, the elements (6) increasing
the heat-transferring area such as projections (35) and/or partitions (34) extend
from the inner wall (2).
2. A heat exchanger according to claim 1, characterized in that the water duct (5) extends spiral-wise around the entire inner wall (2).
3. A heat exchanger according to claim 1 or 2, characterized in that the elements (6) increasing the heat-transferring area extend in at least two directions
which include an angle relative to each other.
4. A heat exchanger according to any one of claims 1-3, characterized in that the heat exchanger (1) is of one piece.
5. A heat exchanger according to any one of claims 1-4, characterized in that the heat exchanger has at least one, and preferably a series of planes of symmetry.
6. A heat exchanger according to claim 5, characterized in that the heat exchanger has two planes of symmetry.
7. A heat exchanger according to any one of claims 1-6, characterized in that the water duct (5) comprises at least two windings, wherein each winding is at a
number of positions provided with a portion enclosed by two wall parts (4) extending
at right angles relative to the longitudinal direction of the heat exchanger, wherein
the space (17) between said wall parts (4) is designed so that it can be cleared in
tangential direction, the arrangement being such that at least one mold (16) can be
used for at least the formation of a first casting core (9) for the water duct (5),
which first casting core (9) is lost during or after the casting of the heat exchanger
(1).
8. A heat exchanger according to claim 7, characterized in that the water duct (5) is enclosed by the inner wall (2), an outer wall (3) and a water
duct wall (4) extending between the inner and outer walls, which water duct wall (4)
extends spiral-wise around the inner wall (2) and is in each winding, at at least
two positions, provided with such a thickening and/or profiling that, as a result,
two opposite water duct wall parts are formed that are at least parallel and preferably
slightly diverging outwardly in two opposite directions substantially transverse relative
to a section that is at right angles to the longitudinal direction of the heat exchanger
(1).
9. A heat exchanger according to any one of the preceding claims, characterized in that the elements (6) increasing the heat-transferring area are accommodated in sectors
(I-IV), wherein the elements (6) in each sector (I-IV) extend substantially parallel
to each other, the arrangement being such that each sector (I-IV) can be manufactured
by means of a withdrawable second casting core part (8), which second casting core
parts can be joined together to form a one-piece second casting core (8) which is
lost during or after the casting of the heat exchanger (1).
10. A heat exchanger according to any one of the preceding claims, characterized in that the elements increasing the heat-transferring area are projection-shaped (35) and
are provided in staggered rows and/or columns, wherein between the free ends of at
least a part of the projections (35) a polygonal free space (11) is defined.
11. A heat exchanger according to claims 9 and 10, characterized in that at least a number of the projections (35) of any two adjoining sectors (I-IV) lie
at least partly between each other and cross each other.
12. A heat exchanger according to any one of the preceding claims, characterized in that adjacent one end within the inner wall (2), there is provided an accommodation space
for a burner (21), preferably of the premix type, wherein in at least a part of the
heat exchanger (1), the elements (6) increasing the heat-transferring area have, in
the direction away from the accommodation space, an increasing surface and/or density
and/or length, the arrangement being such that during use, combustion gases flowing
along the elements (6) cool down relatively calmly.
13. A heat exchanger according to any one of the preceding claims, characterized in that an accommodation space is provided for a burner, preferably of the premix type, wherein
the burner has substantially a polygonal cross section.
14. A casting core apparatus for use in the manufacture of a heat exchanger according
to any one of the preceding claims, comprising at least a first casting core assembly
(9) having the form of at least a spiral-shaped water duct (5) and a second casting
core assembly (8) having at least the form of a burner space (11) with elements (6)
increasing the heat-transferring area, wherein the second casting core assembly (8)
is included within the first casting core assembly (9), wherein between the first
(9) and the second casting core assembly (8) a space is included for forming at least
the inner wall (2), wherein at least one of the casting core assemblies (8, 9) is
built up from parts and wherein the casting core apparatus (B, 8, 9) is at least substantially
of a type that is lost during or after the casting of the heat exchanger (1).
15. A casting core apparatus for use in the manufacture of a heat exchanger according
to any one of claims 1-13, comprising at least a first casting core assembly (9) having
the form of at least a spiral-shaped water duct (5) and a second casting core assembly
(8) having at least the form of a burner space (11) with elements (6) increasing the
heat-transferring area, wherein the second casting core assembly (8) is included within
the first casting core assembly (9), wherein between the first (9) and the second
casting core assembly (8) a space is included for forming at least the inner wall
(2), wherein the casting core assemblies (8, 9) are of a one-piece construction and
wherein the casting core apparatus (B, 8, 9) is at least substantially of a type that
is lost during or after the casting of the heat exchanger (1).
16. A method for manufacturing a heat exchanger suitable for a heat exchanger according
to any one of claims 1-13, comprising the following steps:
- manufacturing a first casting core assembly (9) of the lost type, in the form of
a spiral-shaped water duct (5);
- manufacturing a second casting core assembly (8) of the lost type, in the form of
a central burner space (11) with elements (6) increasing the heat-transferring area;
- positioning the two casting core assemblies (8, 9) within a casting box (B) so that
the first casting core assembly (9) substantially surrounds the second casting core
assembly (8) and is spaced therefrom;
- casting the heat exchanger (1) in the casting box (B) while substantially the first
(9) and the second casting core assembly (8) are simultaneously or contiguously lost;
and
- removing the one-piece heat exchanger (1) having a continuous, spiral-shaped water
duct (5).
17. A method according to claim 16, characterized in that the first (9) and/or the second casting core assembly (8) is manufactured in parts,
which parts are joined together.
18. A method according to claim 16 or 17, characterized in that the second casting core assembly (8) is manufactured in one piece by means of a mold
having moving parts, which, after formation of the casting core assembly (8) in the
mold, are pulled away in substantially radial, outward direction.
19. A method according to any one of claims 16-18, characterized in that the first casting core assembly (9) is manufactured in one piece by means of a mold.
20. A heating apparatus (20) comprising a heat exchanger (1) according to any one of claims
1-13.
1. Wärmetauscher (1), der durch Gießen aus einem Leichtmetall hergestellt ist, mit wenigstens
einer Wasserleitung, einem Brennerraum (11) und Elementen (6), welche die Wärmeübertragungsfläche
vergrößern, dadurch gekennzeichnet, daß der Wärmetauscher (1) eine geschlossene, polygonale oder teilweise gebogene Innenwand
(2) aufweist, wobei sich die Wasserleitung (5) spiralförmig entlang der Außenseite
der Innenwand (2) und der Brennerraum (11) sich innerhalb der Innenwand (2) erstreckt,
wobei wenigstens in einem Teil des Wärmetauschers (1) auf der Innenseite die die Wärmeübertragungsfläche
vergrößernden Elemente (6), wie Vorsprünge (35) und/oder Trennwände (34), sich von
der Innenwand (2) aus erstrecken.
2. Wärmetauscher nach Anspruch 1, dadurch gekennzeichnet, daß sich die Wasserleitung (5) spiralförmig um die gesamte Innenwand (2) erstreckt.
3. Wärmetauscher nach Anspruch 1 oder 2, dadurch gekennzeichnet, daß die die Wärmeübertragungsfläche vergrößernden Elemente (6) sich in wenigstens zwei
Richtungen erstrecken, die miteinander einen Winkel einschließen.
4. Wärmetauscher nach einem der Ansprüche 1-3, dadurch gekennzeichnet, daß der Wärmetauscher (1) einstückig ist.
5. Wärmetauscher nach einem der Ansprüche 1-4, dadurch gekennzeichnet, daß der Wärmetauscher wenigstens eine und vorzugsweise eine Reihe von Symmetrieebenen
aufweist.
6. Wärmetauscher nach Anspruch 5, dadurch gekennzeichnet, daß der Wärmetauscher zwei Symmetrieebenen hat.
7. Wärmetauscher nach einem der Ansprüche 1-6, dadurch gekennzeichnet, daß die Wasserleitung (5) wenigstens zwei Windungen aufweist, wobei jede Windung an einer
Anzahl von Positionen mit einem Bereich versehen ist, der von zwei Wandteilen ( 4)
in bezug zur Längsrichtung des wärme- tauschers rechtwinklig verlaufenden Wandteilen
umschlossen ist, wobei der Raum (17) zwischen den Wandteilen ( 4) derart ausgebildet
ist, daß er in tangentialer Richtung freigemacht werden kann, wobei die Anordnung
derart ausgeführt ist, daß wenigstens eine Form (16) zumindest zur Bildung eines ersten
Gußkerns (9) für die Wasserleitung (5) verwendet werden kann, wobei der erste Gußkern
(9) während oder nach dem Gießen des Wärmetauschers (1) verlorengeht.
8. Wärmetauscher nach Anspruch 7, dadurch gekennzeichnet, daß die Wasserleitung (5) von der Innenwand (2), einer Außenwand (3) und einer sich zwischen
der Innen- und der Außenwand erstreckenden Wasserleitungswand ( 4) umschlossen ist,
wobei die Wasserleitungswand ( 4) sich spiralförmig um die Innenwand (2) erstreckt
und in jeder Wicklung an mindestens zwei Positionen mit einer derartigen Verdickung
und/oder einem Profil versehen ist, daß infolgedessen zwei gegenüberliegende Wasserleitungswandteile
gebildet sind, die wenigstens parallel zueinander sind und vorzugsweise in zwei entgegengesetzte
Richtungen geringfügig nach außen und im wesentlichen transversal zu einem Abschnitt
divergieren, der rechtwinklig zur Längsrichtung des Wärmetauschers (1) verläuft.
9. Wärmetauscher nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß die die Wärmeübertragungsfläche vergrößernden Elemente (6) in Abschnitten (I-IV)
angeordnet sind, wobei die Elemente (6) in jedem Sektor (I-IV) sich im wesentlichen
parallel zueinander erstrecken, wobei die Anordnung derart ausgebildet ist, daß jeder
Abschnitt (I-IV) mittels eines herausziehbaren zweiten Gußkernteils (8) herstellbar
ist, wobei die zweiten Gußkernteile zur Bildung eines einstückigen zweiten Gußkernteils
(8) miteinander verbindbar sind, welches während oder nach dem Gießen des Wärmetauschers
(1) verlorengeht.
10. Wärmetauscher nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß die die Wärmeübertragungsfläche vergrößernden Elemente die Form von Vorsprüngen (35)
haben und in versetzten Reihen und/oder Spalten angeordnet sind, wobei zwischen den
freien Enden wenigstens eines Teils der Vorsprünge (35) ein polygonaler freier Raum
(11) gebildet ist.
11. Wärmetauscher nach den Ansprüchen 9 und 10, dadurch gekennzeichnet, daß wenigstens einige der Vorsprünge (35) zweier benachbarter Abschnitte (I-IV) zumindest
zum Teil zwischen einander liegen und einander kreuzen.
12. Wärmetauscher nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß nahe einem Ende innerhalb der Innenwand (2) ein Aufnahmeraum für einen Brenner (21),
vorzugsweise vom Vormisch-Typ, vorgesehen ist, wobei in wenigstens einem Teil des
Wärmetauschers (1) die die Wärmeübertragungsfläche vergrößernden Elemente (6) in vom
Aufnahmeraum weggerichteter Richtung eine zunehmende Fläche und/oder Dichte und/oder
Länge aufweisen, wobei, während des Gebrauchs, an den Elementen (6) vorbei strömende
Verbrennungsgase relativ ruhig abkühlen.
13. Wärmetauscher nach einem der vorhergehenden Ansprüche, dadurch gekennzeichnet, daß ein Aufnahmeraum für einen Brenner, vorzugsweise vom Vormisch-Typ, vorgesehen ist,
wobei der Brenner im wesentlichen einen polygonalen Querschnitt aufweist.
14. Gußkernvorrichtung zur Verwendung bei der Herstellung eines Wärmetauschers nach einem
der vorhergehenden Ansprüche, mit wenigstens einer ersten Gußkernanordnung (9) mit
der Form wenigstens einer spiralförmigen Wasserleitung (5) und einer zweiten Gußkernanordnung
(8) mit der Form wenigstens eines Brennerraums (11) mit die Wärmeübertragungsfläche
vergrößernden Elementen (6), wobei die zweite Gußkernanordnung (8) in der ersten Gußkernanordnung
(9) enthalten ist, wobei zwischen der ersten (9) und der zweiten Gußkernanordnung
(8) ein Raum zur Bildung wenigstens der Innenwand (2) eingeschlossen ist, wobei wenigstens
eine der Gußkernanordnungen (8, 9) aus Teilen aufgebaut ist, und wobei die Gußkernvorrichtung
(B, 8, 9) wenigstens im wesentlichen von dem Typ ist, der während oder nach dem Gießen
des Wärmetauschers (1) verlorengeht.
15. Gußkernvorrichtung zur Verwendung bei der Herstellung eines Wärmetauschers nach einem
der Ansprüche 1 - 13, mit wenigstens einer ersten Gußkernanordnung (9) mit der Form
wenigstens einer spiralförmigen Wasserleitung (5) und einer zweiten Gußkernanordnung
(8) mit der Form wenigstens eines Brennerraums (11) mit die Wärmeübertragungsfläche
vergrößernden Elementen (6), wobei die zweite Gußkernanordnung (8) in der ersten Gußkernanordnung
(9) enthalten ist, wobei zwischen der ersten (9) und der zweiten Gußkernanordnung
(8) ein Raum zur Bildung wenigstens der Innenwand (2) eingeschlossen ist, wobei die
Gußkernanordnungen (8, 9) einstückig sind, und wobei die Gußkernvorrichtung (B, 8,
9) wenigstens im wesentlichen von dem Typ ist, der während oder nach dem Gießen des
Wärmetauschers (1) verlorengeht.
16. Verfahren zur Herstellung eines Wärmetauschers, geeignet für einen Wärmetauscher nach
einem der Ansprüche 1 - 13, mit den folgenden Schritten:
- Herstellen einer ersten verlorenen Gußkernanordnung (9) mit der Form einer spiralförmigen
Wasserleitung (5);
- Herstellen einer zweiten verlorenen Gußkernanordnung (8) mit der Form eines Zentralbrennerraums
(11) mit die Wärmeübertragungsfläche vergrößernden Elementen (6);
- Positionieren der beiden Gußkernanordnungen (8, 9) in einem Gußkasten (B), so daß
die erste Gußkernanordnung (9) im wesentlichen die zweite Gußkernanordnung (8) um
gibt und von dieser beabstandet ist;
- Gießen des Wärmetauschers (1) in dem Gußkasten (B), wobei im wesentlichen die erste
(9) und die zweite Gußkernanordnung (8) gleichzeitig oder nacheinander verlorengehen;
und
- Entfernen des einstückigen Wärmetauschers (1), der eine durchgehende spiralförmige
Wasserleitung (5) aufweist.
17. Verfahren nach Anspruch 16, dadurch gekennzeichnet, daß die erste (9) und/oder die zweite Gußkernanordnung (8) in Teilen hergestellt wird,
die miteinander verbunden werden.
18. Verfahren nach Anspruch 16 oder 17, dadurch gekennzeichnet, daß die zweite Gußkernanordnung (8) mittels einer Form mit bewegbaren Teilen einstückig
hergestellt wird, welche nach dem Bilden der Gußkernanordnung (8) in der Form im wesentlichen
radial nach außen weggezogen werden.
19. Verfahren nach einem der Ansprüche 16 - 18, dadurch gekennzeichnet, daß die erste Gußkernanordnung (9) mittels einer Form einstückig hergestellt wird.
20. Heizvorrichtung (20) mit einem Wärmetauscher (1) nach einem der Ansprüche 1-13.
1. Echangeur de chaleur (1), fabriqué en métal léger par une technique de coulée, comprenant
au moins un conduit d'eau, un espace (11) de brûleur et des éléments (6) qui augmentent
la surface de transfert de chaleur, caractérisé en ce que l'échangeur de chaleur (1) comporte une paroi interne fermée polygonale ou partiellement
courbée (2), le conduit d'eau (5) s'étend sous forme spiralée le long de l'extérieur
de la paroi interne (2), et l'espace de brûleur (11) s'étend à l'intérieur de la paroi
interne (2), et en ce que, dans une partie au moins de l'échangeur de chaleur (1) du côté de l'intérieur, les
éléments (6) qui augmentent la surface de transfert de chaleur, tels que des saillies
(35) et/ou des cloisons (34), s'étendent depuis la paroi interne (2).
2. Echangeur de chaleur selon la revendication 1, caractérisé en ce que le conduit d'eau (5) s'étend en spirale tout autour de la paroi interne (2).
3. Echangeur de chaleur selon la revendication 1 ou 2, caractérisé en ce que les éléments (6) qui augmentent la surface de transfert de chaleur s'étendent dans
deux directions au moins qui forment un angle l'une avec l'autre.
4. Echangeur de chaleur selon l'une quelconque des revendications 1 à 3, caractérisé en ce que l'échangeur de chaleur (1) est en une seule pièce.
5. Echangeur de chaleur selon l'une quelconque des revendications 1 à 4, caractérisé en ce que l'échangeur de chaleur possède au moins un plan de symétrie et, de préférence, une
série de tels plans.
6. Echangeur de chaleur selon la revendication 5, caractérisé en ce que l'échangeur de chaleur a deux plans de symétrie.
7. Echangeur de chaleur selon l'une quelconque des revendications 1 à 6, caractérisé en ce que le conduit d'eau (5) comprend au moins deux enroulements, chaque enroulement comprend,
à un certain nombre de positions, une portion entourée par deux parties de paroi (4)
qui s'étendent perpendiculairement à la direction longitudinale de l'échangeur de
chaleur, et en ce que l'espace (17) compris entre les parties de paroi (4) est tel qu'il peut être dégagé
en direction tangentielle, la disposition étant telle qu'au moins un moule (16) peut
être utilisé au moins pour la formation d'un premier noyau de coulée (9) destiné au
conduit d'eau (5), ce premier noyau de coulée (9) étant perdu pendant ou après la
coulée de l'échangeur de chaleur (1).
8. Echangeur de chaleur selon la revendication 7, caractérisé en ce que le conduit d'eau (5) est enfermé par la paroi interne (2), une paroi externe (3)
et une paroi de conduit d'eau (4) qui s'étend entre les parois interne et externe,
la paroi (4) de conduit d'eau s'étendant en spirale autour de la paroi interne (2)
et comportant, dans chaque enroulement, à deux positions au moins, un épaississement
et/ou élément profilé tel que deux parties opposées de paroi de conduit d'eau sont
formées et sont au moins parallèles et de préférence légèrement divergentes vers l'extérieur
dans deux directions opposées pratiquement transversales à un tronçon qui est perpendiculaire
à la direction longitudinale de l'échangeur de chaleur (1).
9. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce que les éléments (6) qui augmentant la surface de transfert de chaleur sont logés dame
des secteurs (I-IV), les éléments (6) de chaque secteur (I-IV) s'étendent en directions
pratiquement parallèles les unes aux autres, la disposition étant telle que chaque
secteur (I-IV) peut être fabriqué par une seconde partie (8) de noyau de coulée qui
peut être retirée, les secondes parties de noyau de coulée pouvant être raccordées
pour former un second noyau de coulée en une seule pièce (8) qui est perdu pendant
ou après la coulée de l'échangeur de chaleur (1).
10. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce que les éléments qui augmentent la surface de transfert de chaleur ont une forme de saillie
(35) et sont disposés en lignes et/ou colonnes décalées, et un espace polygonal libre
(11) est délimité entre les extrémités libres d'une partie au moins des saillies (35).
11. Echangeur de chaleur selon les revendications 9 et 10, caractérisé en ce qu'un certain nombre au moins des saillies (35) de deux secteurs adjacents quelconques
(I-IV) sont disposées au moins partiellement les unes entre les autres et se recoupent.
12. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce que, près d'une extrémité placée dans la paroi interne (2), est disposé un espace de
logement d'un brûleur (21), de préférence du type à prémélange, et en ce que, dame une partie au moins de l'échangeur de chaleur (1), les éléments (6) qui augmentent
la surface de transfert de chaleur ont, dans la direction qui s'éloigne de l'espace
de logement, une surface et/ou une densité et/ou une longueur croissantes, la disposition
étant telle que, pendant l'utilisation, les gaz de combustion qui s'écoulent le long
des éléments (6) se refroidissent de manière relativement calme.
13. Echangeur de chaleur selon l'une quelconque des revendications précédentes, caractérisé en ce qu'un espace de logement est disposé pour un brûleur, de préférence du type à prémélange,
et en ce que le brûleur a une section pratiquement polygonale.
14. Appareil à noyau de coulée destiné à être utilisé pour la fabrication d'un échangeur
de chaleur selon l'une quelconque des revendications précédentes, comprenant au moins
un premier ensemble (9) de noyaux de coulée ayant la forme d'au moins un conduit d'eau
(5) de forme spiralée et un second ensemble (8) de noyaux de coulée ayant au moins
la forme d'un espace de brûleur (11) avec des éléments (6) qui augmentent la surface
de transfert de chaleur, en ce que le second ensemble de noyaux de coulée (8) est
incorporé dans le premier ensemble de noyaux de coulée (9), en ce que, entre le premier
(9) et le second (8) ensemble de noyaux de coulée est disposé un espace destiné à
former au moins la paroi interne (2), en ce que l'un au moins des ensembles (8, 9)
de noyaux de coulée est constitué de parties, et l'appareil à noyaux de coulée (B,
8, 9) est au moins pratiquement d'un type perdu pendant ou après la coulée de l'échangeur
de chaleur (1).
15. Appareil à noyau de coulée destiné à être utilisé pour la fabrication d'un échangeur
de chaleur selon l'une quelconque des revendications 1 à 13, comprenant au moins un
premier ensemble de noyaux coulée (9) ayant la forme d'au moins un conduit d'eau (5)
de forme spiralée et un second ensemble (8) de noyaux de coulée ayant au moins la
forme d'un espace de brûleur (11) possédant des éléments (6) qui augmentent la surface
de transfert de chaleur, et en ce que le second ensemble (8) de noyaux de coulée est
incorporé dans le premier ensemble (9) de noyaux de coulée, un espace est incorporé
entre le premier (9) et le second (8) ensemble de noyaux de coulée pour la formation
d'au moins la paroi interne (2), les ensembles (8, 9) de noyaux de coulée ont une
construction en une seule pièce, et l'appareil à noyaux de coulée (B, 8, 9) est au
moins pratiquement d'un type qui est perdu pendant ou après la coulée de l'échangeur
de chaleur (1).
16. Procédé de fabrication d'un échangeur de chaleur convenant à un échangeur de chaleur
selon l'une des revendications 1 à 13, comprenant les étapes suivantes :
la fabrication d'un premier ensemble (9) de noyaux de coulée du type perdu sous forme
d'un conduit d'eau spiralée (5),
la fabrication d'un ensemble (8) de noyaux de coulée de type perdu sous forme d'un
espace (11) de brûleur central ayant des éléments (6) qui augmentent la surface de
transfert de chaleur,
le positionnement des deux ensembles (8, 9) de noyaux de coulée dans une boîte (B)
de coulée afin que le premier ensemble (9) de noyaux de coulée entoure pratiquement
le second ensemble (8) de noyaux de coulée et en soit distant,
la coulée de l'échangeur de chaleur (1) dans la boîte de coulée (B) alors que le premier
(9) et le second (8) ensemble de noyaux de coulée sont perdue de manière pratiquement
simultanée ou contiguë4, et
l'extraction de l'échangeur de chaleur en une seule pièce (1) ayant un conduit continu
d'eau (5) de forme spiralée.
17. Procédé selon la revendication 16, caractérisé en ce que le premier (9) et/ou le second (8) ensemble à noyaux de coulée est réalisé en partie
et ces parties dont raccordées.
18. Procédé selon la revendication 16 ou 17, caractérisé en ce que le second ensemble (8) de noyaux de coulée est fabriqué en une seule pièce avec un
moule ayant des parties mobiles qui, après formation de l'ensemble (8) de noyaux de
coulée dans le moule, sont écartées en directions pratiquement radiales vers l'extérieur.
19. Procédé selon l'une quelconque des revendications 16 à 18, caractérisé en ce que le premier ensemble (9) de noyaux de coulée est fabriqué en une seule pièce à l'aide
d'un moule.
20. Appareil de chauffage (20) comprenant un échangeur de chaleur (1) selon l'une quelconque
des revendications 1 à 13.