[0001] The present invention generally relates to a heat exchanger, and in particularly,
to a condenser provided with a connector having a diverging cross-section to enable
uniform distribution of a refrigerant in a core of the condenser.
[0002] Generally, heat exchangers, preferably condensers, are provided in Heating Ventilation
Air-Conditioning (HVAC) system to reduce heat of the refrigerant flowing in the condenser.
The condenser generally receives high pressure refrigerant in form gas from the compressor
and condensate said high pressure refrigerant into liquid by reducing heat from the
refrigerant. The condensers enable heat exchange between the refrigerant flowing into
a core of the condenser and ambient air or coolant flowing around the core of the
condenser, thereby reducing heat from the refrigerant. Further, the heat exchanger
is provided with an inlet connector and an outlet connector to supply refrigerant
to and from the core of the heat exchanger. The core having a plurality of heat exchanger
tubes extended between a pair of manifolds. The pair of manifolds may include an inlet
opening to receive the inlet connector, and an outlet opening to receive the outlet
connector. Further, a baffle/blocking member is provided in a manifold to divide the
heat exchanger tubes into a first portion of tubes and a second portion of tubes in
a fluid communication with each other. Conventionally, the inlet connector having
uniform cross-section is connected to the inlet opening of the heat exchanger, which
may cause non-uniform distribution of refrigerant in the heat exchanger tubes due
to not uniform positioning of said inlet connector in relation to geometrical center
of the first and second portion of tubes. Such non-uniformly distributed refrigerant
may create dead zones in the heat exchanger tubes, in which heat exchange between
the refrigerant and the ambient air is sub-optimal, thereby, efficiency of the heat
exchanger is reduced. In case, the inlet opening is provided in an end of the manifold
corresponding the first portion of tubes, refrigerant flow in the tubes in the top
portion of the first portion of tubes is low as comparted to rest of the tubes in
the first portion of tubes, thereby dead zones are created in the first portion of
tubes. To overcome such situation, the manifold is provided with more than inlet openings
and a jumper line is connected to the inlet connector. In other words, the inlet connector
is connected to one inlet opening and the jumper line connected with the inlet connector
is connected to another inlet opening, thereby enabling uniform distribution of refrigerant.
However, such configuration of having a jumper line with the inlet connector increases
weight of the heat exchanger, is more problematic in terms of packaging and performance
may be negatively affected.
[0003] Accordingly, there is a need for a simple connector for a heat exchanger that enable
uniform distribution of refrigerant across the heat exchanger. Further, there is a
need for a heat exchanger with a connector that improves performance of the heat exchanger
without modifying core structure of the heat exchanger such as fin density, heat exchange
tubes geometry and number of channels in the heat exchange tubes.
[0004] 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.
[0005] In view of the foregoing, an embodiment of the invention herein provides a heat exchanger
provided with at least one first block and a second block to enable flow of heat exchange
fluid in the heat exchanger. The heat exchanger includes a first manifold and a second
manifold spaced apart from the first manifold. Further, a plurality of heat exchange
elements is fluidically connected between the first manifold and the second manifold.
The at least one first block is adapted to be coupled to the first manifold. The at
least one first block further comprising a first passage. Further, at least a part
of the first passage is having a progressively diverging cross-section and is adapted
to be fluidically coupled to the first manifold.
[0006] Further, the heat exchange includes a second passage fluidically connected to the
first passage.
[0007] Further, the heat exchanger includes a second block adapted to be coupled to any
one of the first manifold and the second manifold to receive the heat exchange fluid
from the plurality of heat exchange elements.
[0008] In one embodiment, the first manifold comprises a first opening adapted to be in
a fluid communication with the at least one first block, and a second opening adapted
to be in a fluid communication with the second block.
[0009] In another embodiment, the second manifold comprises a second opening adapted to
be in a fluid communication with the second block.
[0010] Further, the first opening of the first manifold is provided with a collar to receive
a perpendicular thrilling from the first passage of the at least one first block and
comprising a brazing area for brazing the at least one first block with the collar
of the first manifold.
[0011] In one embodiment, the first passage of the at least one first block is any one of
cylindrical, ellipse and oblong shape.
[0012] Further, geometry of the first passage may be constant from one end of the first
passage to another end of the first passage.
[0013] In another embodiment, geometry of the first passage is progressively diverging from
one end of the first passage to another end of the first passage.
[0014] In another embodiment, the at least one first block is an inlet connector adapted
to introduce the heat exchange fluid to the plurality of heat exchange elements, and
the second block is an outlet connector adapted to receive the heat exchanger fluid
from the plurality of heat exchange elements.
[0015] Further, the second passage of the at least one first block is of a cylindrical shape
having uniform cross-section throughout the second passage.
[0016] In yet another embodiment, the second passage formed in the at least one first block
is perpendicular to the first passage formed in the at least one first block.
[0017] Further, the part of the first passage is having larger cross-section than of rest
of the first passage.
[0018] In one embodiment, the first passage having an end proximate to a second side is
inclined at angle to form the progressively diverging cross-section of the first passage.
[0019] 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 a schematic view of a heat exchanger, in accordance with an embodiment
of the present invention; and
Fig. 2A is a perspective view of a first block of the heat exchanger, in accordance
with an embodiment of the present invention;
Fig. 2B is a cross-sectional view of the first block of the heat exchanger of Fig,
2A;
Fig. 2C is a schematic view of the first block with a first manifold of the heat exchanger
of Fig. 1; and
Fig. 3 illustrates a cross-section view of the first block of Fig. 1, in accordance
with an embodiment of the present invention.
[0020] It must be noted that the figures disclose the invention in a detailed enough way
to be implemented, the figures helping to better define the invention if needs be.
The invention should however not be limited to the embodiment disclosed in the description.
[0021] The present invention relates to a heat exchanger, preferably a condenser, provided
with a pair of connectors to supply a heat exchange fluid to and from the heat exchanger.
As the inlet connector connected to a manifold of the heat exchanger provides constant
pressure of the heat exchange fluid, the heat exchange fluid may distributed non-uniformly
in heat exchanger tubes of the heat exchanger, which negatively impacts performance
of the heat exchanger. In order to attain uniform distribution of the heat exchange
fluid in the heat exchanger tubes, internal pressure drop of the heat exchanger fluid
at an inlet opening of the manifold can be decreased, thereby increasing the heat
exchange fluid flow in the heat exchanger tubes of the heat exchanger. The internal
pressure drop at the inlet opening can be achieved by modifying a section of an inlet
connector connected at the inlet opening. Further, cross-section of at least a portion
of the inlet connector is modified to be non-uniform to increase the heat exchange
fluid flow in the heat exchanger. In one embodiment, at least a portion of the inlet
connector is modified to have larger cross-section than of rest of the inlet connector.
Therefore, internal pressure drop of the heat exchange fluid at the inlet opening
is reduced, so that heat exchange fluid can be uniformly distributed throughout the
heat exchanger tubes.
[0022] While aspects relating to modifying cross-section of an inlet connector to reduce
pressure drop of heat exchange fluid at a first section of heat exchange tubes as
described above and henceforth can be implemented in an outlet connector to reduce
pressure drop of the heat exchange fluid at a second section of heat exchange tubes,
the embodiments are described in the context of the following system(s).
[0023] Fig. 1 illustrates a schematic view of a heat exchanger 100, in accordance with an
embodiment of the present invention. The heat exchanger 100 is provided with at least
one first block 108 and a second block 110 to enable heat exchange fluid flow in the
heat exchanger 100. The heat exchanger 100 includes a first manifold 102 and a second
manifold 104 spaced apart from the first manifold 102. The heat exchanger 100 further
includes a plurality of heat exchange elements 106 extended between the first manifold
102 and the second manifold 104. The plurality of heat exchange elements 106 is fluidically
connected to the first manifold 102 and the second manifold 104. In one embodiment,
the heat exchange fluid can be refrigerant and the plurality of heat exchange elements
106 can be heat exchanger tubes/plates. The first manifold 102 includes at least one
baffle 105 provided in the first manifold 102 to divide the plurality of heat exchange
elements 106 into a first section of heat exchange elements 106A, hereinafter referred
to as first section of tubes, and a second section of heat exchange elements 106B,
hereinafter referred to as second section of tubes. Further, the at least one first
block 108 is fluidically connected to the first manifold 102, corresponding to the
first section of tubes 106A, to introduce the heat exchange fluid, hereinafter referred
to as refrigerant, into the first section of tubes 106A.
[0024] The second block 110 is fluidically connected to the first manifold 102, corresponding
to the second section of tubes 106B, to receive the refrigerant from the second section
of tubes 106B. Generally, the refrigerant flows from the at least one first block
108 to the first section of tubes 106A and flows to the second section of tubes 106B
through the second manifold 104. The refrigerant flowing in the heat exchange elements
106 release heat to the air flowing across the heat exchanger 100. In one embodiment,
the at least one first block 108 and the second block 110 is a part of an inlet connector
and an outlet connector respectively. In case the heat exchanger 100 includes more
than one first blocks 108, the first blocks 108 may be connected at both ends of the
first manifold 102, corresponding to the first section of tubes 106A. Further, the
first manifold 102 further includes a first opening 112 adapted to be in fluid communication
with the at least one first block 108 and a second opening 114 adapted to be in fluid
communication with the second block 110. The first opening 112 can be formed at an
end of the first manifold 102 or can be formed in between both ends of the first manifold
102.
[0025] In another aspect of the invention, the at least one first block 108 is connected
to the first manifold 102 and the second block 110 is connected to the second manifold
104. In such cases, the first opening 112 is provided in the first manifold 102 corresponding
to the at least one first block 108 and the second opening 114 is provided in the
second manifold 104 corresponding to the second block 110. In this aspect of the invention,
the heat exchanger 100 has single section of the plurality of heat exchange elements
106. Further, the first opening 112 and the second opening 114 are formed in a such
way the first opening 112 and the second opening 114 are fluidically coupled to the
at least one first block 108 and the second block 110. For the sake of brevity and
clarity, the present invention is described with one first block 108 and the second
block 110. Further, the internal pressure drop of the refrigerant at the plurality
of heat exchange elements 106, hereinafter referred to as heat exchange elements,
is reduced by increasing cross-section of at least a part of the first block 108,
so the amount of refrigerant flow in the heat exchange elements 108 is increased,
thereby increasing performance of the heat exchanger.
[0026] Figs. 2A and 2B illustrate simplified views of the first block 108 of Fig. 1, in
accordance with an embodiment of the present invention. In an example, Fig. 2A is
a perspective view of the first block 108 of the heat exchanger 100 and Fig. 2B is
a cross-sectional view of the first block 108 of the heat exchanger 100. The first
block 108 includes 204 a first passage 202 and a second passage 204 fluidically connected
to the first passage 202. Further, the second passage 204 and the first passage 202
are formed in the first block 108 to enable refrigerant circulation to the first opening
112 formed in the first manifold 102. The second passage 204 of the first block 108
may be in a fluid communication with the inlet connector or conduits carrying the
refrigerant and the first passage 202 of the first block 108 may be in a fluid communication
with the first opening 112 of the heat exchanger 100. The second passage 204 may have
uniform cross-section throughout the second passage 204, whereas the first passage
202 may have non-uniform and progressively diverging cross-section at a part of the
first passage 202. In one embodiment, at least a part 206 of the first passage 202
has bigger cross-section than of the rest of the first passage 202. As the cross-section
of the first passage 202 proximate to the first opening 112 is more than of rest of
the first passage 202, pressure drop of the refrigerant at the first opening 112 is
reduced, thereby increasing refrigerant flow in the heat exchange elements 106. In
one aspect, geometry of the first passage 202 of the first block 108 is constant from
one end to another end of the first passage 202, while the cross-section of the first
passage 202 is progressively diverging from the one end to another end of the first
passage 202. In another aspect, geometry and cross-section of the first passage 202
of the first block 108 is progressively diverging from the one end to another end
of the first passage 202. In one embodiment, the geometry of the first passage 202
can be any shape such as, for example, cylindrical, oblong, ellipse, rectangular etc.
[0027] Further, the first block 108 may include a first side 208A that is adapted to be
in-contact with the inlet connector when the second passage 204 of the first block
108 is in fluid communication with the inlet connector. The first block 108 may further
include a second side 208B that is in adapted to be in-contact to the first manifold
102 when the first passage 202 is in fluid communication with the first manifold 102.
In one embodiment, the first passage 202 having an end proximate to the second side
208B of the first block 108 is inclined at angle to achieve non-uniform cross-section
of the first passage 202. Further, the inclination may be formed, an end proximate
to the second side 208B, in upper portion of the first passage 202 or throughout the
first passage 202 depends on coupling position of the first block 108 with the first
manifold 102. In one embodiment, the second passage 204 is perpendicularly formed
with respect to the first passage 202 formed in the first block 108. In another embodiment,
the second passage 204 is parallel formed with respect to the first passage 202. In
yet another embodiment, the second passage 204 is oblong to the first passage 202
of the first block 108. Further, the second passage 204 may be formed from the first
side 208A of the first block 108 and the first passage 202 may be formed from the
second side 208B of the first block 108. The second side 208B may be in-contact with
the first manifold 102 in such a way that the first passage 202 is in a fluid communication
with the first opening 112 formed in the first manifold 102. The second passage 204
formed in the first side 208A in such a way that the second passage 204 is in a fluid
communication with the inlet connecter or conduits carrying the refrigerant to the
heat exchanger 100.
[0028] Fig. 3 illustrates a cross-section view of the first block 108 of Fig. 1, in accordance
with an embodiment of the present invention. In this embodiment, the cross-section
of the first passage 202 is progressively diverging throughout the first passage 202.
In other words, the first passage 202 is progressively diverging from an end to another
end of the first passage 202, which is proximate to the second side 208B of the first
passage 202. In simple words, cross-section of the first passage 202 at one end, which
is proximate to the second side 208B of the first passage 202, is more than of another
end of the first passage 202. In one embodiment, the second passage 204 and the first
passage 202 can be any one of cylindrical or oblong in shape. Further, the first block
108 and the second block 110 can be brazed to any one of the first manifold 102 and
the second manifold 104. Further, the first opening 112 of the first manifold 102
is provided with a collar 210 to receive a perpendicular thrilling 214 from the first
passage 202 of the first block 108 and provide brazing area 216 for brazing the at
least one first block 108 with the collar 210 of the first manifold 102. As shown
in the schematic view of the first block 108 with the first manifold 102, the collar
210 is provided in the first opening 112 of the first manifold 102. In one example,
the first block 108 can be the inlet connector to introduce the refrigerant to the
heat exchanger 100 and the second block 110 can be the outlet connector to receive
the refrigerant from the heat exchanger 100. As the first passage having non-uniform
cross-section, pressure drop of the refrigerant at the heat exchange elements 106
is reduced and refrigerant is uniformly distributed in the heat exchanger elements
106, thereby performance of the heat exchanger 100 is optimum. Although the present
invention is described with the first block 108 having non-uniform cross-section,
it can be applied to the second block 108.
[0029] 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. A heat exchanger (100), comprising:
a first manifold (102);
a second manifold (104) spaced apart from the first manifold (102);
a plurality of heat exchange elements (106) fluidically connected between the first
manifold (102) and the second manifold (104);
at least one first block (108) adapted to be coupled to the first manifold (102),
wherein the at least one first block (108) further comprising:
a first passage (202), wherein at least a part (206) of the first passage (202) is
having a progressively diverging cross-section and is adapted to be fluidically coupled
to the first manifold (102).
2. The heat exchanger (100) as claimed in claim 1, further includes a second passage
(204) fluidically connected to the first passage (202).
3. The heat exchanger (100) as claimed any of the preceding claims, further includes
a second block (110) adapted to be coupled to any one of the first manifold (102)
and the second manifold (104) to receive the heat exchange fluid from the plurality
of heat exchange elements (106).
4. The heat exchanger (100) as claimed in claim 3, wherein the first manifold (102) comprises
a first opening (112) adapted to be in a fluid communication with the at least one
first block (108).
5. The heat exchanger (100) as claimed in claim 4, wherein the first manifold (102) further
comprises a second opening (114) adapted to be in a fluid communication with the second
block (110).
6. The heat exchanger (100) as claimed in claim 4, wherein the second manifold (104)
comprises a second opening (114) adapted to be in a fluid communication with the second
block (110).
7. The heat exchanger (100) as claimed in any of claims 4 to 6, wherein the first opening
(112) of the first manifold (102) is provided with a collar (210) to receive a perpendicular
thrilling (214) from the first passage (202) of the at least one first block (108)
and comprising a brazing area (216) for brazing the at least one first block (108)
with the collar (210) of the first manifold (102).
8. The heat exchanger (100) as claimed in any of preceding claims, wherein the first
passage (202) of the at least one first block (108) is any one of cylindrical, ellipse,
and oblong shape.
9. The heat exchanger (100) as claimed in any of claims 1 to 8, wherein geometry of the
first passage (202) is constant from one end of the first passage (202) to another
end of the first passage (202).
10. The heat exchanger (100) as claimed in any of claims 1 to 8, wherein geometry of the
first passage (202) is progressively diverging from one end of the first passage (202)
to another end of the first passage (202).
11. The heat exchanger (100) as claimed in any of preceding claims, wherein the at least
one first block (108) is an inlet connector adapted to introduce the heat exchange
fluid to the plurality of heat exchange elements (106), and the second block (110)
is an outlet connector adapted to receive the heat exchanger fluid from the plurality
of heat exchange elements (106).
12. The heat exchanger (100) as claimed in claim 2, wherein the second passage (204) of
the at least one first block (108) is of a cylindrical shape having uniform cross-section
throughout the second passage (204).
13. The heat exchanger (100) as claimed in any of preceding claims, wherein the second
passage (204) formed in the at least one first block (108) is perpendicular to the
first passage (202) formed in the at least one first block (108).
14. The heat exchanger as claimed in any of preceding claims, wherein the part (206) of
the first passage (202) is having larger cross-section than of rest of the first passage
(202).
15. The heat exchanger as claimed in any of preceding claims, wherein the first passage
(202) having an end proximate to a second side (208B) is inclined at angle to form
the progressively diverging cross-section of the first passage (202).