[0001] The present invention relates to a heat exchanger system, particularly, the present
invention relates to a multi-circuit heat exchanger system for vehicles.
[0002] With evolution of vehicles toward hybrid and pure electric vehicles, there is need
for cooling of power electronics and battery packs powering such vehicles along with
a Heating Ventilation and Air Conditioning (HVAC) system for such vehicles. Accordingly,
there is need for complex heat exchangers, particularly, multi-circuit heat exchangers
that can operate either as water cooled condenser using R1234yf refrigerant or as
a gas cooler using R744 refrigerant or as a water chiller depending on the requirements.
The water cooled condenser / gas cooler can be generally used in Heating Ventilation
and Air Conditioning (HVAC) system and the water chiller can be used for at least
one of battery cooling, facilitating cabin cooling or cooling of power electronic
based elements depending on the requirements. The multi-circuit heat exchanger involves
at least three heat exchange media, two coolants and one refrigerant, and configures
refrigerant circuit disposed between the coolant circuits. The coolant circuits facilitate
cooling of coolants flowing there-through and the refrigerant circuit facilitates
in condensing of a refrigerant fluid such as for example R1234yf or cooling of another
refrigerant fluid such as for example R744, particularly, high pressure refrigerant
fluid flowing through the refrigerant circuit. More specifically, depending upon whether
the refrigerant flowing through the refrigerant circuit is R744 or R1234yf, the refrigerant
is either cooled without phase change or condensed with phase change respectively.
For, example, in case R744 refrigerant is flowing through the refrigerant circuit,
the R744 refrigerant is cooled without undergoing phase change, i.e. the R744 refrigerant
remains in gas phase and the refrigerant circuit acts as a gas cooler, whereas in
case the R1234yf is flowing through the refrigerant circuit, the R1234yf undergoes
condensation, phase change of R1234yf from gas to liquid phase occurs and the refrigerant
circuit acts as the condenser of the air conditioning system.
[0003] Specifically, when the multi-circuit heat exchanger operates as the water chiller,
the coolants in liquid state at relatively low operating pressures of 0.5 to 3 bars
and flowing through the independent coolant circuits respectively reject heat to the
high pressure refrigerant fluid flowing through the refrigerant circuit configured
between the coolant circuits for achieving cooling of the two coolants either one
at a time or simultaneously. With such configuration, cold refrigerant flowing through
the refrigerant circuit can be used for simultaneously cooling two different coolants
flowing through the two different coolant circuits. The cooled coolants received from
the two different coolant circuits can be used differently. For example, one coolant
can be used for battery cooling. In this way, the coolants after extracting heat from
the battery pack are cooled by the refrigerant from the refrigerant circuit for ensuring
a regular supply of cool coolant to the battery pack. The regular cooling of the battery
pack prevents damage thereof due to over-heating and also ensures efficient operation
thereof. The other coolant can be used for other applications such as facilitating
cooling of the air supplied to vehicle cabin or for cooling power electronics based
elements such as controllers.
[0004] Further, when the multi-circuit heat exchanger operates as the condenser using R1234yf
as the refrigerant and gas cooler using R744 refrigerant, the high pressure refrigerant
operating at high pressures up to 170 bars reject heat to the coolants flowing through
the coolant circuits for achieving condensation /gas cooling of the high pressure
refrigerant. In this way, the high pressure refrigerant loses heat energy by heat
exchange with the coolants and either gets condensed into liquid phase for R1234yf
or gets cooled while still remaining in gas phase (for R744). Thereafter, the high
pressure, treated refrigerant passes through an expansion valve, which further cools
the liquid refrigerant / cooled gas due to lowering of the refrigerant pressure. For
R1234yf - the low pressure refrigerant liquid and flash gas leaving the expansion
valve flows at proper rate through the evaporator and the compressor to complete the
air conditioning cycle. The operating pressure of the refrigerant circuit depends
on the refrigerant flowing through the refrigerant circuit in both liquid and gaseous
state. For example, in case, the refrigerant flowing through the refrigerant circuit
is R1234yf, the condenser operates at an operating pressure of up to 25 bars. For
example, in case, the refrigerant flowing through the refrigerant circuit is a high
pressure refrigerant, is particularly, R744, the refrigerant circuit operates as the
gas cooler (instead of the condenser) and operates at a substantially higher operating
pressure as high as up to 170 bars.
[0005] Referring to
FIGURE 1 of the accompanying drawings, a conventional multi-circuit heat exchanger
10 is depicted. The conventional multi-circuit heat exchanger
10 is generally formed of plurality of corrugated plates
12a and
12b that are stacked over each other in a pre-defined configuration as illustrated in
FIGURE 1, to define a refrigerant circuit
20a and coolant circuits
20b and
20c. More specifically, the refrigerant flows though passages configured between the
first and second corrugated plates
12a and
12b by joining the first and second corrugated plates
12a and
12b at specific points to define the refrigerant circuit
20a. In case the multi-circuit heat exchanger
10 is operating as the condenser (R1234yf) / gas cooler (R744), as the refrigerant flows
through the refrigerant circuit
20a, the refrigerant loses heat energy by heat exchange with the first and second coolants
flowing above and below the corrugated plates
12a and
12b respectively defining the coolant circuits
20b and
20c, and as such the refrigerant gets condensed to liquid phase (R1234yf) or gets cooled
while still remaining in gas state (R744). In case the multi-circuit heat exchanger
10 is operating as the water chiller, the first and the second coolants flowing over
and below the first and second corrugated plates
12a and
12b respectively are cooled by the refrigerant flowing between the first and the second
corrugated plates
12a and
12b. Although such configuration of the conventional multi-circuit heat exchanger 10
configures circulation paths for the first and second coolants and the refrigerant
for facilitating heat exchange between the coolants and the refrigerant. However,
the heat exchange between the refrigerant and the coolants for condensation / cooling
of the refrigerant or cooling of the coolant is not effective. Also, as the refrigerant
flowing through the passages configured by joining the first and second corrugated
plates
12a and
12b at specific points is high pressure refrigerant, particularly, in case the refrigerant
is R744 (CO
2) having operating pressures as high as up to 170 bars there are chances of bursting
and separation of the first and second corrugated plates
12a and
12b. Such bursting may cause pressure drop in the condenser / gas cooler circuit
20a and may render the conventional multi-circuit heat exchanger
10 in-effective. Also, such bursting may cause irreversible damage to the multi-circuit
heat exchanger
10 and render the same useless. Such bursting may also cause mixing of the refrigerant
with the coolant, thereby rendering both the coolants and the refrigerant useless.
Such bursting may also be cause of accidents and may render the multi-circuit heat
exchanger
10 unsafe, requiring frequent maintenance and unreliable.
[0006] Accordingly, there is a need for a multi-circuit heat exchanger system that configures
separate and independent one refrigerant circuit and two coolant circuits for facilitating
effective heat exchange between the refrigerant and the coolant. Specifically, there
is a need for a multi-circuit heat exchanger system that configures separate and independent
circulation paths for flow of a first coolant, a second coolant and a high pressure
refrigerant there through such that elements of the multi-circuit heat exchanger configuring
a refrigerant circuit sandwiched between independent coolant circuits are able to
withstand high operating pressures of the high pressure refrigerant flowing there
through. Further, there is a need for a multi-circuit heat exchanger system that achieves
effective direct heat exchange between the high pressure refrigerant flowing through
a refrigerant circuit and a first and a second coolant flowing through respective
separate coolant circuits for achieving cooling of the first and second coolants.
Also, there is a need for a multi-circuit heat exchanger system that configures separate
and independent refrigerant circuit sandwiched between independent coolant circuits
so that mixing of high pressure refrigerant flowing through the refrigerant circuit
with a first and a second coolant flowing through the respective coolant circuits
is eliminated. Also there is a need for a multi-circuit heat exchanger system that
is safe, requires less maintenance and exhibits extended service life and reliability.
[0007] An object of the present invention is to provide a multi-circuit heat exchanger system
that configures separate and independent one refrigerant circuit and two coolant circuits
for facilitating effective heat exchange between the refrigerant and the coolants
for functioning either as Water Cooled Gas Cooler or Gas Cooled Water Chiller.
[0008] Another object of the present invention is to provide a multi-circuit heat exchanger
system that obviates the drawbacks associated with conventional multi-circuit heat
exchanger that use only corrugated plates for configuring heat exchange passages irrespective
of whether heat exchange medium is high pressure medium.
[0009] Still another object of the present invention is to provide such a multi-circuit
heat exchanger system that elements of the multi-circuit heat exchanger system configuring
a refrigerant circuit are sandwiched between and in contact with plates configuring
the separate coolant or chiller-circuits and are able to withstand high operating
pressures of the high pressure refrigerant flowing there through.
[0010] Yet another object of the present invention is to provide a multi-circuit heat exchanger
system that configures separate and independent circulation paths for a first coolant,
a second coolant and a refrigerant so that mixing of high pressure refrigerant flowing
through a refrigerant circuit with a first and a second coolant flowing through the
respective coolant circuits is eliminated.
[0011] Another object of the present invention is to provide a multi-circuit heat exchanger
system that configures heat exchange between refrigerant and first coolant, refrigerant
and second coolant and between the first coolant and the second coolant.
[0012] Yet another object of the present invention is to provide a multi-circuit heat exchanger
system that exhibits enhanced heat exchange efficiency and performance.
[0013] Still another object of the present invention is to provide a multi-circuit heat
exchanger system that is robust in construction, reliable and ensures safe operation.
[0014] Another object of the present invention is to provide a multi-circuit heat exchanger
system that is less prone to failures and requires less maintenance.
[0015] Yet another object of the present invention is to provide a multi-circuit heat exchanger
system that exhibits better flow control of heat exchange fluids flowing there-through.
[0016] 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.
[0017] A multi-circuit heat exchanger system, hereinafter referred to as a "system" is disclosed
in accordance with an embodiment of the present invention. The "system" includes a
plurality of sets of tubular elements to configure fluid flow passages for a refrigerant
and a plurality of first cooling panels and second cooling panels to configure independent
fluid flow passages for a first coolant and a second coolant respectively, wherein
the first cooling panels and the second cooling panels are so arranged with respect
to the sets of tubular elements that at least one set of tubular elements is sandwiched
between each of the adjacent first cooling panels and second cooling panels.
[0018] Further, the multi-circuit heat exchanger system includes an inlet manifold and an
outlet manifold of a first manifold that are connected by at least one set of tubular
elements configuring fluid flow passages for the refrigerant.
[0019] In accordance with an embodiment of the present invention, the tubular elements of
each set of tubular elements are divided into inlet tubular elements and the corresponding
outlet tubular elements that are interconnected to each other by an intermediate manifold.
[0020] Generally, each tubular element of the set of tubular elements withstands high operating
pressures of a high pressure refrigerant flowing there through.
[0021] Specifically, each tubular element of the set of tubular elements receives R744 as
refrigerant and withstands operating pressures in range of 150 to 190 bars.
[0022] Further, the multi-circuit heat exchanger system includes a first pair of inlet and
outlet columns connected by at least one fluid flow passage configured by at least
one of the first cooling panels.
[0023] Still further, the multi-circuit heat exchanger system includes a second pair of
inlet and outlet columns connected by at least one fluid flow passage configured by
at least one of the second cooling panels, the fluid flow passages configured by the
second cooling panels are independent from fluid flow passages configured by the first
cooling panels.
[0024] Generally, the inlet and outlet columns of the first pair of inlet and outlet columns
are configured at opposite front corners of the multi-circuit heat exchanger system
near the first manifold and interconnect all of the first cooling panels configuring
the multi-circuit heat exchanger system.
[0025] Similarly, the inlet and outlet columns of the second pair of inlet and outlet columns
are configured at opposite rear corners of the multi-circuit heat exchanger system
near the intermediate manifold and interconnect all of the second cooling panels configuring
the multi-circuit heat exchanger system.
[0026] In accordance with an embodiment of the present invention, the inlet manifold further
includes at least one inlet and the outlet manifold further includes at least one
outlet, the at least one inlet receives refrigerant to be treated to facilitate distribution
of the refrigerant to the inlet tubular elements via the inlet manifold, whereas the
at least one outlet delivers out the treated refrigerant received by the outlet manifold
from the outlet tubular elements.
[0027] Specifically, the first manifold includes at least one plate with a first set of
slots and a second set of slots configured thereon, at least one distribution column
and at least one collection column. The first set of slots in conjunction with the
at least one distribution column facilitates distribution of refrigerant received
by the inlet manifold to the inlet tubular elements and the second set of slots in
conjunction with the at least one collection column facilitates collection of refrigerant
from the outlet tubular elements into the outlet manifold.
[0028] Specifically, the intermediate manifold includes a cover, at least one plate with
a first set of slots and a second set of slots configured thereon. The first set of
slots facilitates receiving refrigerant from the inlet tubular elements and the second
set of slots facilitates delivering the refrigerant received from said first set of
slots to the outlet tubular elements.
[0029] Generally, each of the first and second cooling panels respectively withstands low
operating pressures (0.5 to 3 bars) of the first and second coolants flowing there-through.
[0030] Specifically, each of the first and second cooling panels receives water glycol mixture
as the first coolant and the second coolant respectively and withstands operating
pressures in range of 0.5 to 3 bars.
[0031] In accordance with an embodiment of the present invention, each of the first cooling
panels is formed by joining preferably identical half plates with an array of flow
restrictors disposed between the half plates.
[0032] Similarly, each of the second cooling panels is formed by joining preferably identical
half plates with the flow restrictors disposed between the half plates.
[0033] In accordance with an embodiment of the present invention, each column of the first
pair of inlet and outlet columns is configured by assembling and joining connector
elements configured on adjacent first cooling panels by brazing. Each connector element
includes a male collar and a female collar, wherein the male collar is received in
a female collar of a first adjacent connector element and the female collar receives
a male collar of a second adjacent connector element.
[0034] Similarly, each column of the second pair of inlet and outlet columns is configured
by assembling and joining connector elements configured on adjacent second cooling
panels by brazing. Each connector element includes a male collar and a female collar,
wherein the female collar receives a male collar of a first adjacent connector element
and the male collar is received in a female collar of a second adjacent connector
element.
[0035] 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:
FIGURE 1 illustrates a schematic representation depicting a multi-circuit heat exchanger system
in accordance with a prior art, wherein the multi-circuit heat exchanger is configured
by arranging and joining corrugated plates in a pre-defined configuration;
FIGURE 2 illustrates an isometric view of a multi-circuit heat exchanger system in accordance
with an embodiment of the present invention;
FIGURE 3 illustrates an isometric view of the multi-circuit heat exchanger system of FIGURE 2 without a first manifold and an intermediate manifold for depicting arrangement of
inlet and outlet tubular elements with respect to cooling panels;
FIGURE 4a illustrates an assembled view depicting arrangement of adjacent sets of tubular elements
with respect to the adjacent first and second cooling panels in accordance with an
embodiment of the present invention;
FIGURE 4b illustrates an exploded view depicting the arrangement of FIGURE 4a, wherein one set of tubular elements including inlet and outlet tubular elements
is depicted sandwiched between adjacent first and second cooling panels;
FIGURE 5a illustrates an isometric view of the inlet and outlet tubular elements of FIGURE 4b;
FIGURE 5b illustrates an isometric sectional view of the first and second cooling panels of
FIGURE 4a and FIGURE 4b depicting internal details thereof, wherein an array of flow restrictors is disposed
within each one of the first and second cooling panels;
FIGURE 6 illustrates a sectional view of the multi-circuit heat exchanger system along a sectional
plane passing through centre of each column of a first pair of inlet and outlet columns
of Figure 2 and Figure 3, also is depicted an enlarged view depicting connection between connector elements
of adjacent first cooling panels for configuring the first pair of inlet and outlet
columns;
FIGURE 7 illustrates a sectional view of the multi-circuit heat exchanger system along a sectional
plane passing through centre of each column of a second pair of inlet and outlet columns
of Figure 2 and Figure 3, also is depicted an enlarged view depicting connection between connector elements
of adjacent second cooling panels for configuring the second pair of inlet and outlet
columns;
FIGURE 8a illustrates an isometric view of a first manifold in accordance with an embodiment
of the present invention, wherein the first manifold is configured with at least one
inlet for receiving refrigerant, particularly high pressure refrigerant to be treated
and at least one outlet for delivering the treated high pressure refrigerant;
FIGURE 8b illustrates an isometric view of the first manifold of FIGURE 8a with a distribution arrangement for distributing high pressure refrigerant to be
treated to inlet tubular elements and a collection arrangement for collecting treated
high pressure refrigerant from corresponding outlet tubular elements;
FIGURE 9a illustrates an isometric view of an intermediate manifold in accordance with an embodiment
of the present invention configured with a first and a second set of slots to facilitate
receiving and delivering of high pressure refrigerant from and to the inlet tubular
elements and the outlet tubular elements respectively;
FIGURE 9b illustrates another isometric view of the intermediate manifold of FIGURE 9a; and
FIGURE 10a and FIGURE 10b illustrate isometric views of an adaptor element connected to the first manifold
of FIGURE 8a and FIGURE 8b for facilitating receiving of high pressure refrigerant in the multi-circuit heat
exchanger system and delivering of treated high pressure refrigerant out of the multi-circuit
heat exchanger.
[0036] 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.
[0037] Although, as per the disclosures made in the present specification, a multi-circuit
heat exchanger system that configures separate and independent coolant circuits and
a refrigerant circuit for operating either as a water chiller for a battery cooling
system or as a water cooled gas cooler for a Heating Ventilation and Air Conditioning
(HVAC) system of a vehicle respectively is disclosed. More specifically, as per the
disclosure made in the current specification, the multi-circuit heat exchanger system
configures separate independent heat exchange circuits for facilitating efficient
heat exchange between a refrigerant, particularly a high pressure refrigerant and
two coolants. However, the multi-circuit heat exchanger system of the present invention
is also applicable for use in other systems and applications not limited for use in
vehicle only. Particularly, such multi-circuit heat exchanger system are also applicable
in any other systems or applications in which the multi-circuit heat exchanger system
is required to configure separate independent heat exchange circuits for facilitating
efficient heat exchange between different media, and wherein one of the heat exchange
media is a high pressure medium and the heat exchange element configuring heat exchange
circuit for such high pressure medium is required to withstand high operating pressures.
[0038] Referring to
FIGURE 2 of the accompanying drawings, a multi-circuit heat exchanger system
100 also simply referred to as "system" in accordance with an embodiment of the present
invention is illustrated. The "system"
100 includes a plurality of sets of tubular elements
102a,
102b, first and second cooling panels
104 and
106 respectively, a first manifold
130, an intermediate manifold
140 and an adaptor element
150.
[0039] The plurality of sets of tubular elements
102a,
102b configure fluid flow passages for a refrigerant, particularly, a high pressure refrigerant
to facilitate heat exchange and also connect an inlet manifold
130a and an outlet manifold
130b of the first manifold
130 that in turn facilitate ingress and egress of high pressure refrigerant in and out
of the "system"
100. The inlet manifold
130a and the outlet manifold
130b of the first manifold
130 are connected by at least one set of tubular elements
102a,
102b configuring fluid flow passages for the high pressure refrigerant. Particularly,
the tubular elements of each set of tubular elements are divided into the inlet tubular
elements
102a and the corresponding outlet tubular elements
102b that are interconnected to each other either directly or indirectly by the intermediate
manifold
140. The inlet tubular elements
102a receive high pressure refrigerant-from the inlet manifold
130a and the outlet tubular elements
102b deliver high pressure refrigerant to the outlet manifold
130b. Further, in one example, the inlet tubular elements
102a configure a portion of fluid flow passage for high pressure refrigerant from the
inlet manifold
130a to the intermediate manifold
140 and the outlet tubular elements
102b configure a reverse flow passage for high pressure refrigerant from the intermediate
manifold
140 to the outlet manifold
130b. Such configuration of the inlet and outlet tubular elements
102a and
102b of each set of tubular elements configure a fluid flow path connecting the inlet
manifold
130a to the outlet manifold
130b. Similar sets of tubular elements configure numerous fluid flow paths connecting the
inlet manifold
130a to the outlet manifold
130b. In accordance with an embodiment of the present invention, the inlet manifold
130a and the outlet manifold
130b are connected by at least one tubular element configuring a continuous fluid flow
path connecting the inlet manifold
130a and the outlet manifold
130b. More specifically, instead of the separate inlet tubular elements
102a and the outlet tubular elements
102b connected by the intermediate manifold
140 forming connection between the inlet manifold
130a to the outlet manifold
130b, a plurality of continuous tubular elements configures continuous fluid flow paths
connecting the inlet manifold
130a to the outlet manifold
130b.
[0040] FIGURE 3 illustrates an isometric view of the "system"
100 without the first manifold
130 and the intermediate manifold
140 for the purpose of clearly depicting the arrangement of inlet and outlet tubular
elements
102a and
102b with respect to the first and the second cooling panels
104 and
106 respectively.
[0041] Specifically,
FIGURE 4a of the accompanying drawings depicts arrangement of adjacent sets of tubular elements
102a,
102b, for example in form of multi-port panels with respect to the adjacent first and
second cooling panels
104 and
106. Generally, the tubular elements
102a, 102b are multi-port panels formed by either one of extrusion and folding. The adjacent
sets of tubular elements
102a, 102b in the form of multi port panels are depicted converging at both the extreme ends
thereof while one of the adjacent sets of the of tubular elements
102a,
102b is depicted sandwiched between adjacent first and second cooling panels
104 and
106. In the sandwiched configuration of one of the adjacent sets of the of tubular elements
102a,
102b between adjacent first and second cooling panels
104 and
106, the tubular elements
102a,
102b of the set are in contact with the first and second cooling panels
104 and
106. Such arrangement of the tubular elements
102a and
102b with respect to the adjacent first and second cooling panels
104 and
106 facilitates better heat exchange between the high pressure refrigerant flowing through
the tubular elements
102a,
102b and the first and second coolants flowing through the first and second cooling panels
104 and
106 respectively. The converging extreme ends of the adjacent sets of tubular elements
102a,
102b are received in slots configured on at least one plate
134 of the first manifold
130. Such arrangement facilitates in packaging of the various elements of the "system"
100 in limited space, thereby achieving a compact configuration of the "system"
100.
[0042] FIGURE 4b of the accompanying drawings illustrate an exploded view depicting the arrangement,
wherein one set of tubular elements including inlet and outlet tubular elements
102a,
102b is depicted sandwiched between the adjacent first and the second cooling panels
104 and
106 respectively. However, more than one set of the tubular elements
102a,
102b can also be disposed between or sandwiched between each of the adjacent first and
second cooling panels
104 and
106, such that the tubular elements
102a,
102b are in direct contact with the adjacent first and second cooling panels
104 and
106 for facilitating direct heat exchange between a first coolant flowing in the first
cooling panels
104 and high pressure refrigerant flowing through the tubular elements
102a,
102b, separate direct heat exchange between a second coolant flowing in the second cooling
panels
106 and high pressure refrigerant flowing through the tubular elements
102a,
102b and indirect heat exchange between the first coolant and the second coolant flowing
in the adjacent first and second cooling panels
104 and
106 respectively via the high pressure refrigerant flowing through the tubular elements
102a,
102b disposed between adjacent first and second cooling panels
104 and
106. The flow of the high pressure refrigerant through the inlet tubular elements
102a and flow of first coolant flowing in the first cooling panels
104 is either parallel flow or counter flow. The flow of the high pressure refrigerant
through the inlet tubular elements
102a and flow of second coolant flowing in the second cooling panels
106 is either parallel flow or counter flow. Such configuration results in cooling of
the first and second coolants when the multi-circuit heat exchanger system
100 is operating as chiller and condensation (R1234yf) / cooling (R744) of the high pressure
refrigerant when the multi-circuit heat exchanger system
100 is operating as condenser / gas cooler. More specifically, depending upon whether
the refrigerant flowing through the refrigerant circuit is R744 or R1234yf, the refrigerant
is either cooled without phase change or condensed with phase change respectively.
For, example, in case R744 refrigerant is flowing through the refrigerant circuit,
the R744 refrigerant is cooled without undergoing phase change, i.e. the R744 refrigerant
remains in gas phase and the refrigerant circuit acts as a gas cooler, whereas in
case the R1234yf is flowing through the refrigerant circuit, the R1234yf undergoes
condensation and the refrigerant circuit acts as the condenser of the air conditioning
system. However, counter flow between high pressure refrigerant with respect to the
first coolant and the second coolant is preferred for better performance and efficiency.
Further, the present invention is not limited to the configuration of the flow between
the refrigerant and the two coolants as far as there is efficient heat transfer between
the refrigerant and the two coolants.
[0043] The inlet tubular elements
102a and the outlet tubular elements
102b are receives and facilitates fluid flow there through of a high pressure refrigerant
such as for example, R744 (CO2) refrigerant that has an operating pressure up to 170
bars. Accordingly, the inlet tubular elements
102a and the outlet tubular elements
102b should be capable of withstanding such high pressures and as such the inlet tubular
elements
102a and the outlet tubular elements
102b are for example configured of micro multiport panels or extruded tubes as depicted
in
FIGURE 5a of the accompanying drawings that in turn are configured by either one of extrusion
and folding. Also, with such configuration, the inlet and outlet tubular elements
102a and
102b respectively are able to withstand high operating pressures of the high pressure
refrigerant such as for example, R744 (CO
2) flowing there through without any danger of bursting. Specifically, the inlet and
outlet tubular elements
102a and
102b configured of micro multiport panels that are capable of receiving R744 as refrigerant
and withstanding high operating pressures in range of 150 to 190 bars. Such a configuration
of the inlet and outlet tubular elements
102a and
102b configured of micro multiport panels, renders the inlet and outlet tubular elements
102a and
102b lighter in weight, safe and compact. Further, the inlet and outlet tubular elements
102a and
102b of such configuration exhibits enhanced heat transfer efficiency, energy and material
saving potential and service life over regular tube counterparts. As the inlet and
outlet tubular elements
102a and
102b configured of micro multiport panels are compact, these can be conveniently packaged
in limited space between adjacent first and second cooling panels
104 and
106. However, the operating pressure of the tubular elements
102a and
102b defining the refrigerant circuit is based on the refrigerant selected. For example,
in case the refrigerant is R134a / R1234yf, the operating pressure of the tubular
elements
102a and
102b defining the refrigerant circuit is in the range of 3-25 bars (absolute), whereas
in case the refrigerant is R744 - CO
2, the operating pressure of the tubular elements
102a and
102b defining the refrigerant circuit is up to 170 bars (absolute). However, present invention
is not limited to use of any particular refrigerant in the tubular elements
102a and
102b of the multi-circuit heat exchanger system
100 of the present invention and any high pressure refrigerant can be used.
[0044] The first and second cooling panels
104 and
106 configure independent fluid flow passages for first and second coolants respectively,
wherein the first and the second cooling panels
104 and
106 are so arranged with respect to the sets of tubular elements
102a and
102b that at least one set of the inlet and the outlet tubular elements
102a,
102b is sandwiched between each of the adjacent first and second cooling panels
104 and
106 as illustrated in the
FIGURE 4b. In accordance with an embodiment, the first and second coolants are water glycol
mixtures of same or different concentrations or composition, for example water-glycol
mixture having different percentage of water and glycol. With use of water glycol
mixture, the operating pressure of the first and the second cooling panels
104 and
106 is up to 3 bars (absolute). However, present invention is not limited to use of any
particular coolants. With such configuration, cold refrigerant flowing through the
refrigerant circuit can be used for cooling the different coolants flowing through
the two different coolant circuits either one at a time or simultaneously. The cooled
coolants received from the two different coolant circuits can be used differently,
for example, one coolant can be used for battery cooling while the other coolant can
be used for other applications such as at least one of battery cooling, facilitating
cooling the air supplied to vehicle cabin and cooling power electronics based elements
such as controllers. Further, the coolants in the first and second cooling panels
104 and
106 can be of same or different compositions.
[0045] Each of the first cooling panels
104 is formed by joining identical half plates
104a and
104b with an array of flow restrictors
120 disposed between the half plates
104a and
104b.
FIGURE 5b of the accompanying drawings depicts an isometric sectional view of the first cooling
panel
104, wherein internal details thereof with the array of flow restrictors
120 disposed within the first cooling panel
104 are also depicted. Further, each one of the first cooling panels
104 is configured with at least one fluid flow passage to facilitate flow of the first
coolant there through and heat exchange between the first coolant flowing there through
and high pressure refrigerant flowing through the tubular elements
102a,
102b disposed adjacent thereto. Further, the first cooling panels
104 also connect a first pair of inlet and outlet columns
108a and
108b that facilitate ingress and egress of first coolant in and out of the "system"
100. As illustrated in
FIGURE 3, as an example, the first coolant enters inside the "system"
100 from the first inlet column
108a, the first coolant's entry inside the "system" is referred to by arrow C1
in and leaves the "system"
100 from the outlet column
108b, referred to arrow C1
out. In between the first set of inlet and outlet columns
108a and
108b, the first coolant is distributed among and flows through the heat exchange passages
configured by the first cooling panels
104 connecting the first pair of inlet and outlet columns
108a and
108b. The flow restrictors
120 retard fluid flow through the at least one fluid flow passage configured within each
of the first cooling panels
104 to enhance heat transfer.
[0046] Similarly, each of the second cooling panels
106 is formed by joining identical half plates
106a and
106b with the flow restrictors
120 disposed between the half plates
106a and
106b. FIGURE 5b of the accompanying drawings also depicts an isometric sectional view of the second
cooling panel
106, wherein internal details thereof with the array of flow restrictors
120 disposed within the second cooling panel
106 are also depicted. Further, each of the second cooling panels
106 is configured with at least one fluid flow passage independent from fluid flow passages
associated with and configured by the first cooling panels
104. The fluid flow passages associated with the second cooling panels
106 facilitate heat exchange between the second coolant flowing there through and high
pressure refrigerant flowing through the tubular elements
102a, 102b disposed adjacent to the second cooling panels
106. The second cooling panels
106 also connect a second pair of inlet and outlet columns
110a and
110b that facilitate ingress and egress of the second coolant in and out of the "system"
100. As illustrated in
FIGURE 3, as an example, the second coolant enters inside the "system"
100 from the second inlet column
110a, the second coolant's entry in the "system"
100 is referred to by arrow C2
in and leaves the "system"
100 from the outlet column
110b, referred to by arrow C2
out. In between the second set of inlet and outlet columns
110a and
110b, the second coolant is distributed among and flows through the heat exchange passages
configured by the second cooling panels
106 connecting the second pair of inlet and outlet columns
110a and
110b. The flow restrictors
120 retard fluid flow through the at least one fluid flow passage configured within each
of the second cooling panels
106 and enhance heat transfer. Each of the first and second cooling panels
104 and
106 is capable of withstanding low pressures in range of 0.5 to 3 bars.
[0047] FIGURE 6 of the accompanying drawings illustrates a sectional view of the "system"
100 along a sectional plane passing through center of each column of the first pair of
inlet and outlet columns
108a and
108b. Also, is depicted first set of fluid flow passages configured by the first cooling
panels
104 for facilitating flow of first coolant there-through. Further is depicted the first
pair of inlet and outlet columns
108a and
108b connected with the first set of fluid flow passages configured by at least one of
the first cooling panels
104 for facilitating ingress and egress of first coolant in and out of the first cooling
panels
104 of the "system"
100. As depicted in
FIGURE 2 and
FIGURE 3, the inlet and outlet columns
108a and
108b of the first pair of inlet and outlet columns are configured at opposite front corners
of the multi-circuit heat exchanger system
100 near the first manifold
130 and interconnect all of the first cooling panels
104 configuring the multi-circuit heat exchanger system
100. Again referring to the
FIGURE 6, connection between adjacent connector elements
105,
105a and
105b configured on adjacent first cooling panels
104 for configuring the first pair of inlet and outlet columns
108a and
108b is depicted in an enlarged view. More specifically, each column of the first pair
of inlet and outlet columns
108a and
108b is configured by assembling and joining connector elements configured on adjacent
first cooling panels of all of the first cooling panels
104 by brazing. More specifically, each connector element
105 includes a male collar
105m and a female collar
105f, wherein the male collar
105m is received in a female collar
105fa of a first connector element
105a configured on an adjacent first cooling panel
104 and the female collar
105f receives male collar
105mb of a second connector element
105b configured on another adjacent first cooling panel
104. Similarly, the connector elements configured on the subsequent adjacent first cooling
panels are also assembled to facilitate configuring of the first pair of inlet and
outlet columns
108a and
108b. Once all the adjacent connector elements configured on all of the first cooling
panels
104 are assembled together, the connector elements can be joined by a single step brazing
process to configure the first pair of inlet and outlet columns
108a and
108b, thereby making the manufacturing of the "system"
100 both convenient and quick.
[0048] FIGURE 7 of the accompanying drawings illustrates a sectional view of the "system"
100 along a sectional plane passing through centre of each column of the second pair
of inlet and outlet columns
110a and
110b. Also is depicted a second set of fluid flow passages configured by at least one
of the second cooling panels
106 for facilitating flow of second coolant there through. Further, is depicted the second
pair of inlet and outlet columns
110a and
110b connected with the second set of fluid flow passages configured by at least one of
the second cooling panels
106 to facilitate ingress and egress of second coolant in and out of the second cooling
panels
106. As depicted in
FIGURE 2 and
FIGURE 3, the second pair of inlet and outlet columns
110a and
110b are configured at opposite rear corners of the multi-circuit heat exchanger system
100 near the intermediate manifold
140 and interconnects all of the second cooling panels
106 configuring the multi-circuit heat exchanger system
100. Again referring to the
FIGURE 7, connection between connector elements of adjacent second cooling panels
106 for configuring the second pair of inlet and outlet columns
110a and
110b is depicted in an enlarged view. More specifically, each column of the second pair
of inlet and outlet columns
110a and
110b is configured by assembling and joining connector elements configured on all of the
second cooling panels
106 by brazing. More specifically, each connector element
111 includes a male collar
111m and a female collar
111f. The female collar
111f receives a male collar
111ma of a first connector element
111a configured on an adjacent second cooling panel
106 and the male collar
111m is received in a female collar
111fb of a second connector element
111b configured on another adjacent second cooling panel
106. Similarly, the connector elements configured on the subsequent adjacent second cooling
panels are also assembled to facilitate configuring of the second pair of inlet and
outlet columns
110a and
110b. Once all the adjacent connector elements configured on all of the second cooling
panels
106 are assembled together, the connector elements can be joined by a single step brazing
process to configure the second pair of inlet and outlet columns
110a and
110b, thereby making the manufacturing of the "system"
100 both convenient and quick.
[0049] Referring to
FIGURE 8a and
FIGURE 8b of the accompanying drawings, isometric views of the first manifold
130 that in turn includes the inlet manifold
130a and the outlet manifold
130a is depicted. The inlet manifold
130a of the first manifold
130 includes at least one inlet
132a that receives high pressure refrigerant to be treated, particularly, high pressure
refrigerant to be condensed and facilitates distribution of the high pressure refrigerant
to be treated to the inlet tubular elements
102a via the inlet manifold
130a and a distribution arrangement. The outlet manifold
130b includes at least one outlet
132b that delivers out the treated high pressure refrigerant received by the outlet manifold
130b from the outlet tubular elements
102b via a collection arrangement. Specifically, the manifold
130 includes at least one plate
134 with a first set of slots
134a and a second set of slots
134b configured thereon, at least one distribution column
136a and at least one collection column
136b. The first set of slots
134a in conjunction with the at least one distribution column
136a facilitate distribution of high pressure refrigerant received by the inlet manifold
130a to the inlet tubular elements
102a. The second set of slots
134b in conjunction with the at least one collection column
136b facilitates collection of high pressure refrigerant received from the outlet tubular
elements
102b into the outlet manifold
130b. More specifically, each of the first set of slots
134a configured on the at least one plate
134 receives the inlet tubular elements
102a in the form of multi port panels to facilitate fluid communication between the inlet
manifold
130a and the inlet tubular elements
102a received in the first set of slots
134a. In one example, converging ends of adjacent multi port panels configuring adjacent
inlet tubular elements
102a are received in one of the slots of the first set of slots
134a configured on the at least one plate
134 of the first manifold
130. Further, the remaining slots of the first set of slots
134a also receive converging ends of adjacent multi port panels configuring adjacent inlet
tubular elements
102a to facilitate fluid communication between the inlet manifold
130a and the remaining inlet tubular elements
102a. Such configuration of the inlet manifold
130a enables uniform distribution of the high pressure refrigerant received by the inlet
manifold
130a to all of the inlet tubular elements
102a.
[0050] Similarly, each of the second set of slots
134b configured on the at least one plate
134 receives the outlet tubular elements
102b in the form of multi port panels to facilitate fluid communication between the outlet
manifold
130b and the outlet tubular elements
102b received in the second set of slots
134b. In one example, converging ends of adjacent multi port panels configuring adjacent
outlet tubular elements
102b are received in one of the slots of the second set of
134b configured on the at least one plate
134 of the first manifold
130. Further, the remaining slots of the second set of slots
134a also receive converging ends of adjacent multi port panels configuring adjacent outlet
tubular elements
102b to facilitate fluid communication between the outlet manifold
130b and the remaining outlet tubular elements
102b. Such configuration of the outlet manifold
130b enables the outlet manifold
130b to effectively collect the high pressure refrigerant from the outlet tubular elements
102b. With such configuration, the sets of inlet and outlet tubular elements
102a and
102b configure connection between the inlet manifold
130a and the outlet manifold
130b
[0051] Referring to
FIGURE 9a and
FIGURE 9b of the accompanying drawings, isometric views of the intermediate manifold
140 are depicted. The intermediate manifold
140 interconnects and facilitates fluid communication between the inlet tubular elements
102a and corresponding outlet tubular elements
102b. In an example, the intermediate manifold
140 includes a cover
142, at least one plate
144 with a first set of slots
144a and a second set of slots
144b configured thereon. The plate
144 with the first set of slots
144a and the second set of slots
144b configured thereon is similar to the plate
134 with the first set of slots
134a and the second set of slots
134b configured thereon. The first set of slots
144a facilitate receiving high pressure refrigerant from the inlet tubular elements
102a and the second set of slots
144b facilitate delivering the high pressure refrigerant to the outlet tubular elements
102b. More specifically, each of the first set of slots
144a configured on the at least one plate
144 receives the inlet tubular elements
102a in the form of multi port panels to facilitate fluid communication between the inlet
tubular elements
102a received in the first set of slots
144a and the intermediate manifold
140. In one example, converging ends of adjacent multi port panels configuring adjacent
inlet tubular elements
102a are received in one of the slots of the first set of slots
144a configured on the at least one plate
144 of the intermediate manifold
140. Further, the remaining slots of the first set of slots
144a also receive converging ends of adjacent multi port panels configuring adjacent inlet
tubular elements
102a to facilitate fluid communication between the remaining inlet tubular elements
102a and the intermediate manifold
140a. Similarly, each of the second set of slots
144b configured on the at least one plate
144 receives the outlet tubular elements
102b in the form of multi port panels to facilitate fluid communication between the intermediate
manifold
140 and the outlet tubular elements
102b received in the second set of slots
144b. In one example, converging ends of adjacent multi port panels configuring adjacent
outlet tubular elements
102b are received in one of the slots
144b configured on the at least one plate
144 of the intermediate manifold
140. Further, the remaining slots of the second set of slots
144b also receive converging ends of adjacent multi port panels configuring adjacent outlet
tubular elements
102b to facilitate fluid communication between the intermediate manifold
140 and the remaining outlet tubular elements
102b. With such configuration, the intermediate manifold
140 configures fluid communication between the sets of inlet and outlet tubular elements
102a and
102b.
[0052] Referring to
FIGURE 10a and
FIGURE 10b, an adaptor element
150 connected to the first manifold
130 for facilitating receiving of high pressure refrigerant in the "system"
100 and delivering the condensed high pressure refrigerant out of the "system"
100 is illustrated. The adaptor element
150 is configured with snap fit engagement elements
154a and
154b for configuring snap fit engagement with the corresponding engagement elements
138a and
138b configured on the first manifold
130 that facilitate engagement between the adaptor element
150 over the first manifold
130 such that at least one inlet and outlet
152a and
152b configured on the adaptor element
150 are aligned with the corresponding inlet and outlet
132a and
132b configured on the first manifold
130. Further, the inlet
152a configured on the adaptor element
150 is connected to inlet hoses supplying high pressure refrigerant to the "system"
100 and the outlet
152b is connected to the outlet hoses for receiving high pressure refrigerant from the
"system"
100.
[0053] Several modifications and improvement might be applied by the person skilled in the
art to a multi-circuit heat exchanger system as defined above, as long as the multi-circuit
heat exchanger system include sets of tubular elements that configure fluid flow passages
for a refrigerant and plurality of first and second cooling panels to configure independent
fluid flow passages for first and second coolants respectively, wherein the first
and second cooling panels are so arranged with respect to the sets of tubular elements
that at least one set of tubular elements is sandwiched between each of the adjacent
first and second cooling panels.
[0054] Obviously, numerous modifications and variations of the present invention are possible
in light of the above teachings. It is therefore to be understood that the invention
may be practiced otherwise than as specifically described herein.
[0055] 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.