[0001] The present invention relates to a heat exchanger, particularly to an electrical
heater for a vehicle.
[0002] A vehicle generally includes a heater for heating air to be supplied to a passenger
compartment. Alternatively, the heater is used to supply heated air to demist or defrost
the windscreen. In some cases, the heater is used to supply hot air or hot coolant
for cold starting the engine. With the emergence of the electric vehicles, the heater
is also applicable for battery thermal management. The heaters can be used for efficient
thermal management of the batteries used for powering the electric motor, thereby
drastically enhancing the service life of the batteries. The air to be heated is generally
passed through a heat exchanger, which includes a heating element such as for example,
heat exchange flow pipes through which a heated fluid circulates in case of thermal
heater or an electrical resistive heater supplied with current. Particularly, the
air to be heated circulates across the heat exchanger and extracts heat from the heating
element.
[0003] The electrical heater includes a plurality of heating elements arranged with respect
to fluid flow passes configured adjacent the heating elements for heat exchange between
the fluid flowing through the fluid flow passes and the heating elements. Each heating
element includes a tube that receives electrical core therein. Specifically, the tube
together with the electrical core forms the heating element. The electrical core is
for example, PTC (Positive Temperature Coefficient) resistors. Each tube may have
several electrical cores, which may be arranged one after the other in a direction
of the tube. Each heating element includes electrodes on both sides for power supply
through the heating element. Further, the heating elements include electrically insulating
and thermally conductive material layers. The layers being located between one of
the electrodes and walls of the tube. In this way, the tube is electrically insulated
from the electrodes and the electrical core but thermally in contact with them.
[0004] The fluid flow passes are either defined by a housing enclosing the heating elements
or by a plurality of modular elements assembled to define the fluid flow passes adjacent
to the heating elements. The fluid flow passes are in fluid communication with an
inlet and an outlet. The fluid entering the electrical heater through the inlet flows
through the fluid flow passes disposed adjacent to the heating elements and in the
process extracts heat from the heating elements. The fluid after extracting heat from
the heating elements egresses through the outlet. Different flow diverting means,
such as for example, deflectors and openings formed on alternative opposite longer
walls of the plates configure multiple flow passes between the inlet and the outlet.
The flow diverting means are configured with an intension of increasing the fluid
flow path between the inlet and the outlet and retaining the fluid adjacent to the
heating elements to improve the contact and prolong the time of contact between the
fluid and heating elements. Further, in some cases, it is required that the inlet
and the outlet be configured on the same side of the electrical heater, in such cases
the baffles become inevitable. Although, the arrangement of baffles configuring multiple
passes is intended to increase the fluid flow path, retain the fluid adjacent the
heating elements, build pressure for homogenous filling of the fluid flow passes with
fluid and prevent escape of the fluid from the outlet without undergoing sufficient
heat exchange with the heating elements. However, such baffles cause fluid to follow
an arch trajectory as the fluid passes the baffle, thereby creating dead zone, i.e.
no fluid zone, downstream of the baffle in the fluid flow direction. Further, the
electrical heater configured with multiple fluid flow passes fluidly coupled to each
other fails to achieve homogeneous fluid filling in all the fluid flow passes. The
problem of nonhomogeneous fluid filling in the fluid flow passages is because the
subsequent fluid flow passes downstream of the baffle in the fluid flow direction
depend on homogenous fluid filling in the previous passes upstream of the baffle in
the fluid flow direction. More specifically, in case of electrical heater with multiple
fluid flow passes to increase the fluid flow path it is difficult to maintain sufficient
pressure for the fluid to fill all the fluid flow passes.
[0005] For efficient performance of the electrical heater, for example, a high voltage coolant
heater, the heat exchange fluid, for example, the coolant is required to be homogeneously
distributed in the fluid flow passages. Specifically, the fluid is required to be
filled in all the fluid flow passes to achieve sufficient contact between the fluid
and the heating elements for efficient heat extraction therefrom. However, conventional
electrical heater fails to achieve homogenous distribution of the fluid in the fluid
flow passages and fail to achieve filling of all the fluid flow passes, accordingly,
the efficiency and performance of the electrical heater is detrimentally impacted.
[0006] Accordingly, there is a need for an electrical fluid heater configured with multiple
fluidly coupled fluid passes that not only increases the fluid flow path but also
includes an arrangement to achieve homogeneous fluid distribution and fluid filling
in all the fluid flow passes to efficient heat exchange between the fluid and the
heating elements. Further, there is a need for an electrical fluid heater that is
configured with arrangement for preventing formation of the dead zones inside the
electrical heater. Furthermore, there is a need for an electrical fluid heater that
exhibits comparatively improved efficiency and performance than the conventional electrical
fluid heaters. Further, there is a need for an electrical fluid heater that addresses
packaging issues by configuring the inlet and the outlet on same side thereof, while
still preventing the problems faced due to use of baffle to achieve U-flow trajectory
of the fluid flow.
[0007] An object of the present invention is to provide an electrical fluid heater that
obviates the problems faced by conventional electrical fluid heaters due to formation
of dead zones and inefficiency and low performance caused thereby.
[0008] Still another object of the present invention is to provide an electrical fluid heater
that ensures homogeneous fluid distribution and fluid filling in all the fluid flow
passes to achieve improved efficiency and performance.
[0009] Still another object of the present invention is to provide an electrical fluid heater
configured with an arrangement to uniformly distribute coolant in the fluid flow passes
adjacent to the electric heating elements and configured with features for improving
scavenging of the coolant from inside the electrical fluid heater.
[0010] In the present description, some elements or parameters may be indexed, such as a
first element and a second element. In this case, unless stated otherwise, this indexation
is only meant to differentiate and name elements which are similar but not identical.
No idea of priority should be inferred from such indexation, as these terms may be
switched without betraying the invention. Additionally, this indexation does not imply
any order in mounting or use of the elements of the invention.
[0011] An electrical fluid heater includes a pair of end plates, a plurality of heating
elements and a plurality of intermediate plates. The pair of end plates include a
first end plate and a second end plate. The first end plate includes an inlet for
ingress of fluid into and an outlet for egress of fluid out of the electrical fluid
heater from same side of the electrical fluid heater to cause the fluid to follow
a U-turn trajectory between the inlet and the outlet. The second end plate formed
with different portions that are in fluid communication with each other. The plurality
of intermediate plates are stacked and arranged between the first and the second end
plates respectively. The heating elements are sandwiched between the intermediate
plates. The adjacent intermediate plates define fluid flow passes adjacent the at
least one corresponding heating element to permit heat exchange between the fluid
and the at least one corresponding heating element. Each intermediate plate is formed
into different sections corresponding to the different portions of the second end
plate. The first sections of the intermediate plates defines fluidly coupled first
fluid flow passes to receive fluid from the inlet for heat exchange with the heating
elements and second sections of the intermediate plates define fluidly coupled second
fluid flow passes to deliver fluid to the outlet after heat exchange with the heating
elements. The second end plate includes multiple fluid deflecting walls formed on
its surface to promote a homogeneous distribution of fluid received in a first portion
of the second end plate and homogeneous distribution of the fluid from the first portion
to a second portion of the second end plate in the U-turn trajectory between the inlet
and the outlet.
[0012] Generally, the first end plate includes a first portion corresponding to the first
sections of the intermediate plates, and formed with the inlet at the center of the
first portion and proximal to a longer wall of the first end plate and a second portion
corresponding to the second sections of the intermediate plates and formed with outlet
at the center of the second portion and proximal to the longer walls of the first
end plate.
[0013] Each intermediate plate includes a pair of opposite longer walls, a pair of opposite
shorter side portions, at least one of guiding pins and corresponding guiding holes
and at least one rib. The pair of opposite longer walls is formed with portions corresponding
to the first and second sections of the intermediate plate. The portion of the intermediate
plate proximal to either one of the opposite longer walls is formed with openings
for either one of ingress and egress of fluid from the fluid flow pass defined by
the intermediate plate in conjunction with the adjacent intermediate plate. The pair
of opposite shorter side portions in conjunction with the pair of opposite longer
walls define the periphery of the intermediate plate that defines at least a portion
of the fluid flow pass corresponding to the intermediate plate. The at least one rib
defines the different sections of the intermediate plate.
[0014] Specifically, the guiding pins formed on the intermediate plate engages with corresponding
guiding holes of the adjacent intermediate plates to position and assemble the intermediate
plate with respect to the adjacent intermediate plate.
[0015] Particularly, the openings are formed alternately on the opposite longer walls of
each pair of the adjacent intermediate plates to define zig-zag fluid flow path between
the inlet and the outlet and permit fluid communication between the fluid flow passes
defined by the adjacent intermediate plates.
[0016] Specifically, the first portion of the second end plate is configured to collect
fluid that has entered the electrical fluid heater through the inlet on the first
end plate and percolated through the first fluid flow passes defined by the first
sections of the intermediate plates after heat exchange with the corresponding heating
elements. The second portion of the second end plate distributes the fluid accumulated
there above to the second fluid flow passes defined by the second sections of the
intermediate plates.
[0017] Particularly, the second end plate includes a first longer wall and a second longer
wall respectively disposed opposite to each other and a first shorter side wall and
a second shorter side walls disposed opposite to each other, together defining periphery
of the second end plate and at least a portion of the fluid flow pass corresponding
to the second end plate. The first longer wall of the second end plate is disposed
aligned with a corresponding first longer wall of the first end plate proximal to
the inlet and the outlet.
[0018] Generally, the multiple fluid deflecting walls configured on the second end plate
homogeneously distributes the fluid from the first fluid flow passes over the first
portion of the second end plate and subsequently the fluid received in the first portion
of the second end plate is distributed over the second portion of the second end plate.
[0019] Specifically, the fluid deflecting walls include a baffle disposed at the interface
between the first portion and the second portion of the second end plate that extends
along an axis (A) and orthogonally from the first longer wall.
[0020] More specifically, the fluid deflecting walls include a plurality of first curved
walls configured on the first portion of the second end plate and extending in a fluid
flow direction from a first extreme end thereof to a second extreme end thereof. At
least one of the first curved walls extends from the first extreme end in a region
proximal to the first longer wall to the second extreme end in a region proximal to
an axis (A) of the baffle.
[0021] Further, the fluid deflecting walls include a plurality of second curved walls configured
on the second portion and extending in a fluid flow direction from a first extreme
end thereof to a second extreme end thereof. The first extreme end of at least one
of the second curved walls is offset from a first extreme end of the previous second
curved wall along the first longer wall. At least one of the second curved walls is
having its second extreme end disposed in a region proximal to the first longer wall.
[0022] Particularly, at least one pair of adjacent first curved walls directs the fluid
received there-between towards at least one gap defined between at least one pair
of the adjacent second curved walls.
[0023] Further, the first extreme ends of the plurality of first curved walls are disposed
on the planes symmetrically to the second extreme ends of the plurality of second
curved walls with respect to the axis (A). Furthermore, at least one of the plurality
of first curved walls is longer than the second curved walls whose second extreme
ends are disposed symmetrically to the first extreme ends of the at least one of the
plurality of first curved walls.
[0024] In accordance with an embodiment of the present invention, at least one of the plurality
of first curved walls has its second extreme end disposed closer from the axis (A)
than the first extreme end of the corresponding one of the second curved walls whose
second extreme end is disposed symmetrically to the first end of the at least one
of the plurality of first curved walls.
[0025] Generally, inside corners of the second end plate defined by the second longer wall
and the respective shorter sidewalls of the second end plate is a curved profile that
directs fluid towards the first curved walls and the second curved walls and from
the first curved walls towards the second curved walls.
[0026] Other characteristics, details and advantages of the invention can be inferred from
the description of the invention hereunder. A more complete appreciation of the invention
and many of the attendant advantages thereof will be readily obtained as the same
becomes better understood by reference to the following detailed description when
considered in connection with the accompanying figures, wherein:
FIG. 1 illustrates an isometric view of an electrical fluid heater in accordance with
an embodiment of the present invention;
FIG. 2 illustrates an exploded view of the electrical fluid heater of FIG. 1;
FIG. 3 illustrates an isometric view of a first end plate of the electrical fluid
heater of FIG. 1;
FIG. 4 illustrates an isometric view of the heating element in accordance with an
embodiment of the present invention;
FIG. 5 illustrates an isometric view of an intermediate plate of a pair of adjacent
intermediate plates defining at least a portion of a fluid flow pass;
FIG. 6 illustrates an isometric view of the adjacent intermediate plate of the pair
of adjacent intermediate plates, wherein the adjacent intermediate plate in conjunction
with the intermediate plate of FIG. 4 defines at least a portion of the fluid flow
pass; and
FIG. 7 illustrates a top view of a second end plate configured with multiple fluid
deflecting walls formed on its surface.
[0027] The present invention envisages an electrical fluid heater, particularly, a high
temperature coolant heater, hereinafter, simply referred to as a fluid heater. The
fluid heater includes a pair of end plates, a plurality of heating elements and a
plurality of intermediate plates. The pair of end plates include a first end plate
and a second end plate. The first end plate includes a first portion and a second
portion formed with an inlet for ingress of fluid into and an outlet for egress of
fluid out of the fluid heater from same side of the fluid heater. The second end plate
is formed with different portions that are in fluid communication with each other
unlike different portions of the first end plate that are in fluid isolation with
each other. Such configuration of the fluid heater causes the fluid to follow a U-turn
trajectory between the inlet and the outlet. The plurality of intermediate plates
are stacked and arranged between the first and the second end plates respectively.
The heating elements are sandwiched between the adjacent intermediate plates. The
adjacent intermediate plates define fluid flow passes adjacent the at least one corresponding
heating element to permit heat exchange between the fluid and the at least one corresponding
heating element. Each intermediate plate is formed into different sections corresponding
to the different portions of the second end plate. The first sections of the intermediate
plates defines fluidly coupled first fluid flow passes to receive fluid from the inlet
for heat exchange with the heating elements and second sections of the intermediate
plates define fluidly coupled second fluid flow passes to deliver fluid to the outlet
after heat exchange with the heating elements. The second end plate is limited by
peripheral walls that define limits of the second end plate and at least a portion
of the fluid flow pass corresponding thereto. The second end plate further includes
multiple fluid deflecting walls formed on its surface. The fluid deflecting walls
promote a homogeneous distribution of fluid received in a first portion of the second
end plate and homogeneous distribution of the fluid from the first portion to a second
portion of the second end plate to define U-turn trajectory between the inlet and
the outlet.
[0028] Although, the present invention is described in the forthcoming description and the
accompanying drawings with an example of an electrical fluid heater for a vehicle.
However, the present invention is also applicable for any heat exchanger for use in
vehicular and non-vehicular applications, wherein the heat exchanger includes inlet
and outlet on the same side thereof to cause the fluid to follow a U-turn trajectory
between the inlet and the outlet. More specifically, the present invention is also
applicable for tubular fluid heat exchanger apart from the electrical fluid heaters.
The tubular heat exchanger includes tubular elements configuring flow of first heat
exchange fluid there through and a second heat exchange fluid flows through fluidly
coupled first and second fluid flow passes adjacent the tubular elements carrying
the first fluid to undergo heat exchange with the first fluid. Particularly, the present
invention is applicable where it is required that fluid is homogeneously filled in
the first and second fluid passes and formation of dead zones in either of the first
pass and the second pass is to be avoided to achieve improved heat exchange for enhancing
efficiency and performance of the tubular heat exchanger.
[0029] FIG. 1 illustrates an isometric view of an electric fluid heater 100, hereinafter
referred to as fluid heater 100, in accordance with an embodiment of the present invention.
The fluid heater 100 includes a pair of end plates 10 and 20, a plurality of heating
elements 30 and a plurality of intermediate plates 40, wherein each intermediate plate
40 is formed of different sections 40a and 40b. FIG. 2 illustrates an exploded view
of the fluid heater 100 and the sequence in which the different elements of the fluid
heater 100 are arranged and assembled with respect to each other.
[0030] The pair of end plates 10 and 20 include a first end plate 10 and a second end plate
20. Referring to the FIG. 3, the first end plate 10 is defined by the opposite longer
walls 12 and 14 and the pair of opposite shorter walls 16 and 18. The opposite longer
walls 12 and 14 are also referred to as first and second longer walls 12 and 14. The
opposite shorter walls 16 and 18 are also referred to as first and second shorter
walls 16 and 18. The opposite longer walls 12 and 14 and the opposite shorter walls
16 and 18 define the periphery of the first end plate 10 and at least a portion of
the fluid flow passes corresponding to the first end plate 10. The first end plate
10 includes an inlet 12a for ingress of fluid into and an outlet 12b for egress of
fluid out of the fluid heater 100 from same side of the fluid heater 100 to achieve
certain advantages. For example, configuring the inlet 12a and the outlet 12b on the
same side of the fluid heater 100 provides compact configuration to the fluid heater
100 and addresses packaging issues. Further, such configuration also addresses routing
issues associated with routing of inlet and outlet conduits connected to the inlet
12a and the outlet 12b for supplying and delivering out fluid from the fluid heater
100. The second end plate 20 fluidly couples the first and the second fluid flow passes
formed adjacent the heating elements 30 and in fluid communication with the inlet
12a and the outlet 12b respectively. Such configuration of the fluid heater 100 with
end plates 10 and 20, the end plate 20 formed with fluidly coupled first and second
portions 20a and 20b, the inlet 12a and the outlet 12b on same side causes the fluid
to follow a U-turn trajectory between the inlet 12a and the outlet 12b. Specifically,
the first end plate includes a first portion 10a and a second portion 10b, wherein
a groove 19 separates the first portion 10a from the second portion 10b. The first
portion 10a and the second portion 10b are raised portion that inherently form the
groove at the interface between first portion 10a and the second portion 10b. The
cross section of the first portion 10a is increasing from the inlet 12a towards the
first fluid flow passes defined by the first sections 40a. Further as illustrated
in FIG. 1 - FIG. 3, the inlet 12a is disposed at the center of the first portion 10a
and proximal to the longer walls 12 of the first end plate 10. Such strategic placement
of the inlet ensures even distribution of the coolant to the portion of the fluid
flow passes defined by the first sections 40a. Similarly, the second portion 10b corresponding
to the second sections 40b of the intermediate plates 40 and is converging from the
second sections 40b to the outlet 12b in the fluid flow direction. Specifically, the
cross section of the second portion 10b is decreasing from the second fluid flow passes
defined by the second sections 40b towards the outlet 12b. Further, again referring
to the FIG. 1 - FIG. 3, the outlet 12b is also disposed at the center of the second
portion 10b and proximal to the longer walls 12 of the first end plate 10. In accordance
with another embodiment of the present invention, the outlet 12b is disposed at the
corner of the first end plate 10 defined at the intersection of the first longer wall
12 and the first shorter wall 16. Specifically, the outlet 12b is farthest from the
groove 19. Such strategic placement of the outlet 12b ensures that the portion of
the fluid flow passes defined by the second sections 40b of the intermediate plates
is filled before the fluid egresses through the outlet 12b. More specifically, such
strategic placement of the outlet 12b ensures even distribution of the coolant in
the fluid flow passes defined by the second sections 40b before egressing through
the outlet 12b. Such configuration of the outlet avoids trapping air in the area beneath
the second portion and the fluid flow passes defined by the second sections 40b by
scavenging the fluid evenly underneath the second portion 10b of the first end plate
10. In another embodiment, the outlet 12b can be disposed horizontally instead of
being disposed vertically the to reduce back-pressure and improve flow path. However,
the present invention is not limited to any particular configuration of the first
end plate 10 with the inlet 12a and the outlet 12b in any particular position. The
inlet and the outlet can be positioned on the first and the second potions so as to
avoid air trapping by scavenging the fluid evenly underneath the first and second
portions 10a and 10b respectively based on multiple fluid deflecting walls 50 formed
on surface of the second end plate 20. Similar to the first end plate 10, the second
end plate 20 is formed with different portions 20a and 20b, refer FIG. 7 for details.
The first portion 20a and the second portion 20b of the second end plate 20 is corresponding
to the first sections 40a and the second sections 40b of the intermediate plates 40
and the first portion 10a and the second portion 10b of the first end plate 10. However,
the first and the second portions 20a and 20b of the second end plates 20 are in fluid
communication with each other unlike the first and second portions 10a and 10b of
the first end plate 10.
[0031] The heating elements 30 are sandwiched between the intermediate plates 40. Referring
to FIG. 4, each heating element 30 includes a tube 32 that receives electrical core
34 therein. The tube 32 together with the electrical core 34 forms the heating element
30. The electrical core 34, is for example, PTC (Positive Temperature Coefficient)
resistors. Each tube 32 may have several electrical cores 34, which may be arranged
one after the other in a direction of the tube 32. Each heating element 30 includes
electrodes 36 on both sides for power supply through the heating element 30. Further,
the heating elements 30 includes electrically insulating and thermally conductive
material layers 38. The layers 38 being located between one of the electrodes 36 and
walls 32a and 32b of the tube 32. In this way, the tube 32 is electrically insulated
from the electrodes 36 and the electrical core 34 but thermally in contact with them.
[0032] The plurality of intermediate plates 40 are stacked and arranged between the first
and the second end plates 10 and 20 respectively. The adjacent intermediate plates
40 define fluid flow passes adjacent the at least one corresponding heating element
30 to permit heat exchange between the at least one heating element 30 and the fluid
flowing through the corresponding fluid flow passages defined by the adjacent intermediate
plates 40. Referring to FIG. 5 and FIG. 6, each intermediate plate 40 is formed into
different sections 40a and 40b corresponding to the different portions 20a and 20b
of the second end plate 20 and the different portions 10a and 10b of the first end
plate 10. The first sections 40a of the intermediate plates 40 defines fluidly coupled
first fluid flow passes. In the assembled configuration of the intermediate plates
40, the first fluid flow passes receive fluid distributed thereto by the first portion
10a of the first end plate 10 from the inlet 12a for heat exchange with at least a
portion of the heating elements 30 sandwiched between the intermediate plates 40.
Also, the second sections 40b of the intermediate plates 40 define fluidly coupled
second fluid flow passes. The second flow passes deliver fluid to the second portion
10b of the first end plate 10 for egress through the outlet 12b after heat exchange
with the heating elements 30 in the assembled configuration of the intermediate plates.
The intermediate plates 40 are positioned and assembled to each other by using first
positioning elements 42b, 44b and corresponding second positioning elements 42c, 44c
formed on the adjacent intermediate plates 40. More specifically, the guiding
[0033] FIG. 5 and FIG. 6 illustrates isometric views of the intermediate plates 40. FIG.
4 illustrates an isometric view of the intermediate plate 40 of a pair of adjacent
intermediate plates defining at least a portion of a fluid flow pass. FIG. 5 illustrates
an isometric view of the adjacent intermediate plate of the pair of adjacent intermediate
plates, wherein the adjacent intermediate plate in conjunction with the other intermediate
plate of the pair of adjacent intermediate plates arranged in axial direction with
respect to each other defines at least a portion of the fluid flow pass. Each intermediate
plate 40 includes a pair of opposite longer walls 42 and 44, hereinafter referred
to as the first and the second longer walls 42 and 44 respectively, a pair of opposite
shorter side portions 46 and 48, hereinafter, referred to as first and second shorter
side portions 46 and 48 respectively. The pair of opposite shorter side portions 46
and 48 in conjunction with the pair of opposite longer walls 42 and 44 define the
periphery of the intermediate plate 40 that defines at least a portion of the fluid
flow pass defined by the adjacent intermediate plates 40. Each longer wall 42, 44
of the pair of opposite longer walls 42 and 44 is formed with separate portions corresponding
to the first and second sections 40a and 40b of the intermediate plate 40.
[0034] The portion of the intermediate plate 40 proximal to either one of the opposite longer
walls 42 and 44 is formed with openings or slots 42a, 44a for either one of ingress
and egress of fluid from the fluid flow pass defined by the intermediate plate in
conjunction with the adjacent intermediate plate. The openings or slots 42a, 44a are
formed alternately on the opposite longer walls 42, 44 of each pair of the adjacent
intermediate plates to define zig-zag fluid flow path between the inlet 12a and the
outlet 12b and permit fluid communication between the fluid flow passes defined by
the adjacent intermediate plates. The zig-zag fluid flow path between the inlet 12a
and the outlet 12b increases the length of the fluid flow path and accordingly enhances
the contact area and contact time between the fluid flowing through the fluid flow
passes and the heating element 30, thereby improving the efficiency and performance
of the fluid heater 100. In accordance with an embodiment, if the openings or slots
44a are formed on the adjacent intermediate plates 40 at portions thereof proximal
to second longer side wall 44, then, the corresponding openings or slots 42a are formed
on the subsequent adjacent intermediate plates 40 at portions thereof proximal to
first longer side wall 42 that is opposite to the second longer side 44. In a preferred
embodiment of the present invention, each pair of the adjacent intermediate plates
40 include slots 42a, 44a instead of the openings formed alternately on the opposite
longer walls 42, 44 thereof. However, the present invention is not limited to any
particular number, placement and configuration of the openings / slots formed on the
portions of the adjacent intermediate plates 40 proximal to either one of the opposite
longer walls 42 and 44 as far as the slots / openings define zig-zag fluid flow path
between the inlet 12a and the outlet 12b and permit fluid communication between the
fluid flow passes defined by the adjacent intermediate plates
[0035] Each intermediate plate 40 includes at least one of first positioning elements 42b
and 44b in the form of guiding pins 42b and 44b and corresponding second positioning
elements 42a and 44c in the form of guiding holes 42c and 44c. The guiding pins 42b
and 44b formed on the intermediate plate 40 engages with the corresponding guiding
holes 42c and 44c of the adjacent intermediate plate 40 to position and assemble the
intermediate plate with respect to the adjacent intermediate plate. Referring to the
FIG. 5, there are two guiding pins 42b along the portion of the intermediate plate
40 proximal to the first longer side wall 42, each guiding pin 42b disposed on the
respective portions of the intermediate plate corresponding to the two sections 40a
and 40b of the intermediate plate 40. Further, there are two guiding pins 44b along
the portion of the intermediate plate 40 proximal to the second longer side wall 44,
each guiding pin 44b disposed on the respective portions of the intermediate plate
40 corresponding to the two sections 40a and 40b of the intermediate plate 40. Referring
to the FIG. 6, there are two guiding holes 42c along the portion of the adjacent intermediate
plate 40 proximal to the first longer side wall 42, each guiding hole 42c disposed
on the respective portions of the adjacent intermediate plate 40 corresponding to
the two sections 40a and 40b of the intermediate plate 40. Further, there are two
guiding holes 44c along the portion of the intermediate plate 40 proximal to the second
longer side wall 44 each guiding hole 44c disposed on the respective portions of the
adjacent intermediate plate 40 corresponding to the two sections 40a and 40b of the
adjacent intermediate plate 40. However, the present invention is not limited to any
particular number, placement and configuration of the positioning and assembling means
for assembling together the intermediate plates in aligned manner such that the opening
or slots 42a, 44a formed on the adjacent pair of intermediate plates 40 are aligned
with respect to each other to define zig-zag fluid flow path between the inlet 12a
and the outlet 12b and permit fluid communication between the fluid flow passes defined
by the adjacent intermediate plates.
[0036] Further, each intermediate plate 40 includes at least one rib 49. The at least one
rib 49 defines the different sections of the intermediate plate 40. The ribs 49 of
the adjacent intermediate plates 40 acts as poke - yoke feature and facilitates in
correct assembly between the adjacent intermediate plates 40.
[0037] Referring to the FIG. 7 of the accompanying drawings, the second end plate 20 includes
multiple fluid deflecting walls 50 formed on the surface thereof. Particularly, the
multiple deflecting walls 50 configured on the second end plate 20 homogeneously distributes
the fluid from the first fluid flow passes over the first portion 20a of the second
end plate 20 and subsequently the fluid from the first portion 20a over the second
portion 20b of the second end plate. More particularly, the first portion 20a of the
second end plate 20 is configured with fluid deflecting walls 50 to collect fluid
that has percolated through the first fluid flow passes defined by the first sections
40a of the intermediate plates 40 after heat exchange with the corresponding heating
elements 30 sandwiched between the adjacent intermediate plates 40. The second portion
20b of the second end plate 20 distributes the fluid accumulated there above to the
second fluid flow passes defined by the second sections 40b of the intermediate plates
40. The second end plate 20 includes a first longer wall 22 and a second longer wall
24 respectively disposed opposite to each other and a first shorter side wall 26 and
a second shorter side wall 28 disposed opposite to each other. The pair of opposite
first and second longer walls 22 and 24 along with the pair of opposite shorter side
walls 26 and 28 together define periphery of the second end plate 20 and at least
a portion of the fluid flow pass corresponding to the second end plate 20. The first
longer wall 22 of the second end plate 20 is disposed aligned with a corresponding
first longer wall 12 of the first end plate 10 proximal to the inlet 12a and the outlet
12b and opposite to a second longer wall 14 of the first end plate 10. The inside
corners of the second end plate 20 defined by the second longer wall 24 and the respective
first and second shorter side walls 26 and 28 of the second end plate 20 is a curved
profile that directs fluid towards first curved walls 54 and second curved walls 56
formed on surface of first and second portions 20a and 20b of the second end wall
20 and from the first curved walls 54 towards the second curved walls 56.
[0038] Referring to the FIG. 7, the fluid deflecting walls 50 includes a baffle 52 disposed
at the interface between the first portion 20a and the second portion 20b of the second
end plate 20. The baffle 52 extends along an axis (A) and orthogonally from the first
longer wall 22. Further, the fluid deflecting walls 50 includes the first curved walls
54 configured on the first portion 20a of the second end plate 20 and extending in
a fluid flow direction from a first extreme end 54a thereof to a second extreme end
54b thereof. More specifically, at least one of the first curved walls 54 extends
from the first extreme end 54a disposed in a region proximal to the first longer wall
22 to the second extreme end 54b disposed in a region proximal to an axis 'A" of the
baffle 52. The first extreme ends 54a of the first curved walls 54 are so disposed
with respect to the first longer wall 22 to receive and direct the fluid received
from the first fluid flow passes defined by the first sections 40a of the intermediate
plates 40 to the gaps between the adjacent first curved walls 54. At least one of
the first curved walls 54 follows a curved profile with the vertex of the curved profile
being complementary to and aligned with but spaced from the curved profile formed
at the first inside corner of the second end plate 20 defined by the second longer
wall 24 and the second shorter sidewall 28. Further, the fluid deflecting walls 50
includes a plurality of second curved walls 56 configured on the second portion 20b
of the second end plate 20 and extending in a fluid flow direction from a first extreme
end 56a thereof to a second extreme end 56b thereof. The first extreme end 56a of
at least one of the second curved walls 56 is offset from a first extreme end 56a
of the previous second curved wall 56 along the first longer wall 22. The first extreme
ends 56a of the second curved walls 56 receive and direct the fluid directed thereto
by the first curved walls 54 towards the gaps between the adjacent second curved walls
56. At least one of the second curved walls 56 is having its second extreme end 56b
disposed in a region proximal to the first longer wall 22. At least one of the second
curved walls 56 follows a curved profile with the vertex of the curved profile being
complementary to and aligned with but spaced from the curved profile formed at the
second inside corner of the second end plate 20 defined by the second longer wall
24 and the first shorter side wall 26.
[0039] Particularly, at least one pair of adjacent first curved walls 54 directs the fluid
received there-between towards at least one gap defined between at least one pair
of the adjacent second curved walls 56. Further, the first extreme ends 54a of the
plurality of first curved walls 54 are disposed on the planes symmetrically to the
second extreme end 56b of the plurality of second curved walls 56 with respect to
the axis "A". Furthermore, at least one of the plurality of first curved walls 54
is longer than the second curved walls 56 whose second extreme end 56b is disposed
symmetrically to the first end 54a of the at least one of the plurality of first curved
walls 54. In accordance with an embodiment of the present invention, at least one
of the plurality of first curved walls 54 has its second end thereof 54b disposed
closer to the axis (A) than the first end 56a of the corresponding one of the second
curved walls 56 whose second extreme ends 56b are disposed symmetrically to the first
ends 54a of the at least one of the plurality of first curved walls 54.
[0040] The baffle 52 terminates at before the first extreme ends 54a of the first curved
walls 54 and the second extreme end 56b of the second curved walls 56.
[0041] In any case, the invention cannot and should not be limited to the embodiments specifically
described in this document, as other embodiments might exist. The invention shall
spread to any equivalent means and any technically operating combination of means.
1. An electrical fluid heater (100) comprising:
• a pair of end plates (10, 20), wherein
∘ a first end plate (10) comprises an inlet (12a) for ingress of fluid into and an
outlet (12b) for egress of fluid out of the electrical fluid heater (100) from same
side of the electrical fluid heater (100) and is adapted to cause the fluid to follow
a U-turn trajectory between the inlet (12a) and the outlet (12b);
∘ a second end plate (20) formed with different portions (20a, 20b) that are in fluid
communication with each other;
• a plurality of heating elements (30);
• a plurality of intermediate plates (40) stacked and arranged between the first and
the second end plates (10) and (20) respectively, the heating elements (30) being
sandwiched there between, adjacent intermediate plates (40) defining fluid flow passes
adjacent the at least one corresponding heating element (30) to permit heat exchange
between the fluid and the at least one corresponding heating element (30), each intermediate
plate (40) being divided into different sections (40a, 40b) respectively corresponding
to the different portions (20a, 20b) of the second end plate (20), wherein the first
sections (40a) of the intermediate plates (40) define fluidly coupled first fluid
flow passes adapted to receive fluid from the inlet (12a) for heat exchange with the
heating elements (30) and the second sections (40b) of the intermediate plates (40)
define fluidly coupled second fluid flow passes adapted to deliver fluid to the outlet
(12b) after heat exchange with the heating elements (30);
characterized in that the second end plate (20) comprising multiple fluid deflecting walls (50) on its
surface adapted to promote an homogeneous distribution of fluid received in a first
portion (20a) of the second end plate (20) and homogeneous distribution of the fluid
from the first portion (20a) to a second portion (20b) of the second end plate (20)
in the U-turn trajectory between the inlet (12a) and the outlet (12b).
2. The electrical fluid heater (100) as claimed in the previous claim, wherein the first
end plate (10) comprises a first portion (10a) corresponding to the first sections
(40a) of the intermediate plates (40) and formed with the inlet (12a) at the center
of the first portion (10a) and proximal to a longer wall (12) of the first end plate
(10) and a second portion (10b) corresponding to the second sections (40b) of the
intermediate plates (40) formed with outlet (12b) at the center of the second portion
(10a) and proximal to a longer wall (12) of the first end plate (10).
3. The electrical fluid heater (100) as claimed in any of the preceding claims, wherein
each intermediate plate (40) comprises:
• a pair of opposite longer walls (42, 44) formed with portions corresponding to the
first and the second sections (40a, 40b) of the intermediate plate (40), either one
of the portions of the intermediate plate (40) proximal to opposite longer walls (42,
44) formed with openings (42a, 44a) for either one of ingress and egress of fluid
from the fluid flow pass defined by the intermediate plate (40) in conjunction with
the adjacent intermediate plate (40);
• a pair of opposite shorter side portions (46, 48) in conjunction with the pair of
opposite longer walls (42, 44) define the periphery of the intermediate plate (40)
that define at least a portion of the fluid flow pass corresponding to the intermediate
plate (40);
• at least one rib (49) defining the different sections (40a, 40b) of the intermediate
plate (40).
4. The electrical fluid heater (100) as claimed in the previous claim, wherein first
positioning elements (42b, 44b) formed on the intermediate plate (40) are adapted
to engage with corresponding second positioning elements (42c, 44c) of the adjacent
intermediate plates (40) to position and assemble the intermediate plate (40) with
respect to the adjacent intermediate plate (40).
5. The electrical fluid heater (100) as claimed in the claim 3, wherein the openings
(42a, 44a) are formed alternately on the opposite longer walls (42, 44) of each pair
of the adjacent intermediate plates (40) to define zig-zag fluid flow path between
the inlet (12a) and the outlet (12b) and permit fluid communication between the fluid
flow passes defined by the adjacent intermediate plates (40).
6. The electrical fluid heater (100) as claimed in any of the preceding claims, wherein
the first portion (20a) of the second end plate (20) is configured to collect fluid
that has entered the entered the electrical fluid heater (100) through the inlet (12a)
on the first end plate (10) and percolated through the first fluid flow passes defined
by the first sections (40a) of the intermediate plates (40) after heat exchange with
the corresponding heating elements (40) and the second portion (20b) of the second
end plate (20) distributes the fluid accumulated there above to the second fluid flow
passes defined by the second sections (40b) of the intermediate plates (40).
7. The electrical fluid heater (100) as claimed in any of the preceding claims, wherein
the second end plate (20) comprises a first longer wall (22) and a second longer wall
(24) respectively disposed opposite to each other and a first shorter side wall (26)
and a second shorter side wall (28) disposed opposite to each other, together defining
periphery of the second end plate (20) and at least a portion of the fluid flow pass
corresponding to the second end plate (20), the first longer wall (22) of the second
end plate (20) is disposed aligned with a corresponding first longer wall (12) of
the first end plate (10) proximal to the inlet (12a) and the outlet (12b).
8. The electrical fluid heater (100) as claimed in any of the preceding claims, wherein
the multiple fluid deflecting walls (50) configured on the second end plate (20) are
adapted to homogeneously distribute the fluid from the first fluid flow passes over
the first portion (20a) of the second end plate (20) and subsequently the fluid received
in the first portion (20a) of the second end plate (20) is distributed over the second
portion (20b) of the second end plate (20).
9. The electrical fluid heater (100) as claimed in claim 7 or claim 8 combined with claim
7, wherein the fluid deflecting walls (50) comprises a baffle (52) at the interface
between the first portion (20a) and the second portion (20b) of the second end plate
(20) that extends along an axis (A) and orthogonally from the first longer wall (22).
10. The electrical fluid heater (100) according to the previous claim, wherein the fluid
deflecting walls (50) comprises a plurality of first curved walls (54) configured
on the first portion (20a) of the second end plate (20) and extending in a fluid flow
direction from a first extreme end (54a) thereof to a second extreme end (54b) thereof,
at least one of the first curved walls (54) extending from the first extreme end (54a)
in a region proximal to the first longer wall (22) to the second extreme end (54b)
in a region proximal to an axis (A) of the baffle (52).
11. The electrical fluid heater (100) as claimed in any of the claim 7, claim 8 combined
with claim 7, claim 9 or 10, wherein the fluid deflecting walls (50) comprises a plurality
of second curved walls (56) configured on the second portion (20b) and extending in
a fluid flow direction from a first extreme end (56a) thereof to a second extreme
end (56b) thereof, the first extreme end (56a) of at least one of the second curved
walls (56) is offset from a first extreme end (56a) of the previous second curved
wall (56) along the first longer wall (22), at least one of the second curved walls
(56) having its second extreme end (56b) disposed in a region proximal to the first
longer wall (22).
12. The electrical fluid heater (100) as claimed in claims 10 and 11, wherein at least
one pair of adjacent first curved walls (54) directs the fluid received there-between
towards at least one gap between at least one pair of the adjacent second curved walls
(56).
13. The electrical fluid heater (100) as claimed in claims 10 and 11 or as claimed in
claim 12, wherein:
- the first extreme ends (54a) of the plurality of first curved walls (54) are disposed
on the second end plate (20) symmetrically to the second extreme ends (56b) of the
plurality of second curved walls (56) with respect to the axis (A),
- at least one of the plurality of first curved walls (54) is longer than the second
curved walls (56) whose second extreme ends (56b) are disposed symmetrically to the
first extreme ends (54a) of the at least one of the plurality of first curved walls
(54).
14. The electrical fluid heater (100) as claimed in claims 10 and 11 or as claimed in
claim 12 or 13, wherein at least one of the plurality of first curved walls (54) has
its second end (54b) disposed closer from the axis (A) than the first end (56a) of
the corresponding one of the second curved walls (56b) whose second extreme end (56b)
is disposed symmetrically to the first end (54a) of the at least one of the plurality
of first curved walls (54).
15. The electrical fluid heater (100) as claimed in claims 10 and 11 or as claimed in
one of claims 12 to 14, wherein the inside corners of the second end plate (20) defined
by the second longer wall (24) and the respective first and second shorter side walls
(26, 28) of the second end plate (20) is a curved profile adapted to direct fluid
towards the first curved walls (54) and the second curved walls (56) and from the
first curved walls (54) towards the second curved walls (56).