Field of the Invention
[0001] The present invention relates to heat exchangers.
Background to the Invention
[0002] There are many heat exchanger applications where a hot gas inlet and a cooled gas
outlet need to be in close proximity to each other due to space constraints. Such
applications include automotive cooling systems, such as cars, trucks and rail locomotives,
and medical equipment applications, nuclear power industry applications and the like.
[0003] Typically, a known heat exchanger, used for example for cooling a gas flow, comprises
an external casing, a heat exchange plate or tube assembly comprising one or a plurality
of heat exchange plates or tubes, one or more coolant inlets for allowing a coolant
fluid to enter the casing and permeate around the heat exchange plate or tube assembly
,one or more coolant outlets for allowing the coolant fluid to drain from the casing,
one or more gas inlets for allowing gas to enter the heat exchange assembly, and one
or more gas outlets to allow gas to exhaust from the heat exchange plate or tube assembly.
[0004] The heat exchange plates or tubes are held rigidly in the casing by a bulkhead or
connecting plate which extends across an end of the casing.
[0005] In an "I" type heat exchanger, there is a first bulkhead at a first end of the cooling
plate assembly, and a second bulkhead at a second end of the heat exchange plate or
tube assembly, and fluid to be cooled or heated flows between the first and second
ends along a plurality of passages or conduits in the cooling plates.
[0006] In a known "U" shaped heat exchanger, a plurality of cooling plates are held in parallel
in a side by side relationship connected by a single connecting plate or bulkhead
at one end of the heat exchanger, so that both inlets and outlets of the fluid to
be cooled can be presented on a same face at a same end of the heat exchanger.
Summary of the Invention
[0007] A problem with known heat exchangers is that the boiling of a liquid coolant, for
example either water or a water and anti-freeze mixture, within a high temperature
heat exchanger can cause localized stress concentrations and failure of the heat exchanger.
[0008] A heat exchanger will exchange the greatest proportion of heat where the inlet gas
is at its hottest. Consequently, the highest proportion of heat exchange will occur
at and in close proximity to the inlet bulkhead.
[0009] Many prior art heat exchangers have a restriction to coolant flow near to the bulkhead
due to the need to interface the gas carrying conduits into the bulkhead. Even where
there is no restriction to coolant flow, then there is no defined path to increase
coolant flow at the bulkhead.
[0010] The relatively low coolant flow rate near the gas inlet end, combined with the increased
heat exchange can cause the coolant at or near the bulkhead to boil and lead to a
failure of the heat exchanger at or near the bulkhead.
[0011] Specific embodiments herein describe a plate cooler type heat exchanger having a
near inlet coolant channel at or near the interface between the hot fluid inlet header
and the start of the heat exchange section (often formed by a bulkhead) at which a
gas inlet is present. The inlet end coolant channel is aimed at increasing the coolant
flow across the interface between the inlet header and the heat exchanger and around
the bulkhead, and thereby reducing the likelihood of localised boiling. Reducing localised
boiling near the inlet to the heat exchange assembly may improve the reliability of
the cooler device.
[0012] According to a first aspect of the present invention, there is provided a heat exchanger
plate assembly for cooling a gas flow using a liquid coolant, said assembly comprising:
a plurality of heat exchange plates, each heat exchange plate comprising a plurality
of fluid conduits through which fluid can flow; and
said cooling plate assembly comprising a fluid inlet region, a fluid outlet region,
and a heat exchange region
characterised by,
a set of first fluid cooling channels arranged between said plurality of cooling plates
and positioned immediately adjacent to said fluid inlet region, each of said coolant
channels extending in a direction transverse to a main flow direction of said plurality
of fluid conduits, said set of first coolant channels allowing a relatively higher
coolant flow rate in a direction transverse to a main length of said coolant channels,
than occurs in a region of the cooling plates further away from said inlet region.
[0013] According to a second aspect there is provided a cooling plate for a heat exchanger,
said cooling plate comprising:
an upper plate;
a lower plate;
said upper plate and lower plate being connected together along first and second edges
in a fluid tight manner;
said upper and lower plates forming a plurality of gas conduits extending along a
length of said cooling plate;
said upper and lower plates comprising a plurality of protrusions and depressions
for allowing a fluid coolant to pass over an outer surface of said cooling plate in
a direction transverse to a fluid flow direction in said gas conduits;
characterised by
a region immediately adjacent one end of said heat exchange assembly, on at least
one of said upper or lower plates, for allowing a relatively higher coolant flow rate
across a width of said cooling plate immediately adjacent said end of said cooling
plate.
[0014] According to a third aspect there is provided a cooling plate assembly comprising:
a plurality of cooling plates, each cooling plate comprising a plurality of fluid
conduits through which gas can flow;
said plurality of cooling plates comprising a fluid inlet region, a fluid outlet region
and a heat exchange region;
characterised in that,
said fluid conduits are provided with a relatively extended smooth internal surface
immediately adjacent said at fluid inlet region, for minimising turbulence of fluid
flow in said fluid conduits adjacent to said fluid inlet region.
[0015] According to a fourth aspect there is provided a cooling plate comprising:
upper and lower plates joined together to form a plurality of fluid conduits through
which fluid can flow;
said plurality of cooling plate comprising a fluid inlet region, a fluid outlet region,
and a heat exchange region positioned between said fluid inlet region and said fluid
outlet region;
characterised in that,
said fluid conduits are provided with a relatively extended smooth internal surface
immediately adjacent said fluid inlet region, for minimising turbulence of fluid flow
in said fluid conduits adjacent to said fluid inlet region.
[0016] The embodiments encompass a heat exchanger gas conduit with a smoother gas side surface
at and near the bulkhead, which reduces the heat transfer co-efficient and thus reduces
the risk of localised boiling at or near the bulkhead.
[0017] Other aspects are as recited in the claims herein.
Brief Description of the Drawings
[0018] For a better understanding of the invention and to show how the same may be carried
into effect, there will now be described by way of example only, specific embodiments,
methods and processes according to the present invention with reference to the accompanying
drawings in which:
Referring to Figure 1 herein, there is illustrated schematically in external view,
a heat exchanger according to a first specific embodiment;
Referring to Figure 2 herein, there is illustrated schematically in view from above,
an individual cooling plate according to a first specific embodiment;
Referring to Figure 3 herein, there is illustrated schematically a cooling plate assembly
of the heat exchanger of Figure 1 herein;
Referring to Figure 4 herein, there is illustrated schematically in detail, a first
end of the cooling plate assembly of Figure 3 herein;
Referring to Figure 5A herein, there is illustrated schematically in view from one
side, the cooling plate assembly of Figure 3 herein;
Referring to Figure 5B herein, there is illustrated schematically a plot of coolant
temperature and gas temperature between first and second ends of the cooling plate
assembly as shown in Figure 5A herein;
Referring to Figure 6 herein, there is illustrated schematically in external view,
a "U" shaped heat exchanger according to a second specific embodiment having gas inlets
and gas outlets on one end of the cooler;
Referring to Figure 7 herein, there is illustrated schematically a cooling plate assembly
of the "U" shaped heat exchanger of Figure 6 herein;
Referring to Figure 8 herein, there is illustrated schematically in close up detail
a close up of a bulkhead and cooling plates at the first end of the "U" shaped heat
exchanger of Figures 6 and 7 herein;
Referring to Figure 9 herein, there is illustrated schematically in view from one
side a third embodiment heat exchanger comprising a plurality of individual cooling
plates;
Referring to Figure 10 herein, there is illustrated schematically in view from above
a fourth embodiment heat exchange plate; and
Referring to Figure 11 herein, there is illustrated schematically in view from one
side a heat exchange plate assembly according to a fourth specific embodiment.
Detailed Description
[0019] There will now be described by way of example a specific mode contemplated by the
inventors. In the following description numerous specific details are set forth in
order to provide a thorough understanding. It will be apparent however, to one skilled
in the art, that the present invention may be practiced without limitation to these
specific details. In other instances, well known methods and structures have not been
described in detail so as not to unnecessarily obscure the description.
[0020] In this specification there are described embodiments of heat exchangers for exchanging
heat between a first fluid, which in the general case can be a gas or a liquid and
a second fluid, which in the general case can be a gas or a fluid. In various places
for ease of description, the heat exchanger embodiments are referred to as coolers,
and the fluids are specified as gases or liquids, and embodiments are described where
a liquid, e.g. water and / or a water/ antifreeze mixture is used to cool a gas, e.g.
an engine exhaust gas. However although these are specific embodiments, in the general
case, the heat exchanger uses a liquid coolant and the fluid to be cooled may comprise
a gas or a gas/ liquid mixture, or even a liquid, and the invention is limited only
by the features of the claims
[0021] In this specification, for ease of terminology, the interface between the fluid inlets
of one or more heat exchange plates or heat exchange tubes will be referred to as
the "inlet header". In some embodiments a plurality of cooling plates are connected
together at their fluid inlet ends by a bulkhead plate, which extends in a direction
transverse to a main length direction of the heat exchange plates or tubes. In other
embodiments, the ends of a plurality of cooling plates may be connected together without
the use of a separate bulkhead plate. In either case, the region of the heat exchange
plates or tubes where the fluid flow enters the plates or tubes is referred to as
the "inlet header".
[0022] Specific embodiments described herein address the problem of localized boiling of
a coolant fluid near a gas inlet and bulkhead of a heat exchanger. Localized boiling
may lead to high component temperature and premature component failure. In the specific
embodiments, these problems are addressed by:
- 1. Directing a higher proportion of the coolant flow to the inlet header region of
the gas conduits, compared to the regions of the gas conduits in the center region
of the heat exchanger; and / or
- 2. Minimizing the turbulence in the gas near the inlet header, by reducing turbulence
inducing features in the gas flow, and thereby lowering the heat transfer co-efficient
on the gas side, in the region near the bulkhead.
[0023] In the embodiments described herein, the solution is addressed by implementing the
following improved features:
● The gas conduit or conduits is/ are shaped such that the gas cooling plate(s) narrow
at or near the inlet header.
● A relatively narrowed cooling plate at or near the inlet header results in a smoother
and larger flow path for the coolant to flow through, thus increasing coolant flow
at the inlet header; thus reducing the risk of localized boiling at or near the inlet
header.
● The conduit surface initially encountered by the gas flow (on the gas side of the
heat exchanger) and the section following the initial gas side surface is more planar
than the central section of the conduit, thus the gas side heat transfer co-efficient
is reduced; thus reducing the risk of localized boiling at or near the inlet header.
[0024] There is provided a heat exchanger gas conduit with a smoother gas side surface at
and near the bulkhead, which reduces the heat transfer co-efficient and thus reduces
the risk of localised boiling at or near the bulkhead.
[0025] Referring to figure 1 herein, there is illustrated schematically in perspective view,
an "I" type heat exchanger 100 comprising an external casing 101; a cooling plate
assembly; one or more coolant inlets 102 for allowing a coolant fluid to enter the
casing and permeate around the cooling plate assembly, and one or more coolant outlets
103 for allowing the coolant fluid to exit from the casing; one or more gas inlet
connectors 104 for allowing gas to enter the cooling plate assembly, and one or more
gas outlet connectors 105 to allow gas to exhaust from the cooling plate assembly.
[0026] The cooling plate assembly comprises a plurality of plates stacked side by side,
held rigid, and spaced apart from each other at their ends, between a first bulkhead
and a second bulkhead.
[0027] A fluid to be cooled, for example a hot gas, enters the heat exchanger at a first
end and exits the heat exchanger at a second end. The coolant surrounds one or a plurality
of cooling plates through which a fluid to be cooled (in this case a gas) passes,
and heat is transferred between the fluid to be cooled and the coolant. The gas flow
and coolant fluid flow are separated by metal walls of the cooling plate assembly.
Heat is transferred between the gas flow and the coolant fluid by conduction of heat
from the gas flow to the metal walls of the cooling plates, and from the metal cooling
plates to the coolant fluid.
[0028] A cooling plate assembly which fits in the outer casing will now be described with
reference to figures 2 to 5 herein.
[0029] Referring to Figure 2 herein, there is illustrated schematically in view from above,
one heat exchanger plate of the "I" type plate heat exchanger of figure 1 herein,
hereafter referred to as a cooling plate. The heat exchanger comprises one or a plurality
of such cooling plates.
[0030] Each cooling plate 200 comprises a pair of flat metal plates joined together at their
sides 201, 202, and forming a plurality of fluid conduits or passages 203 there between
(herein also referred to as gas conduits), each fluid conduit extending between first
and second ends 204, 205 respectively of the cooling plate.
[0031] The upper plate comprises a plurality of generally semi-cylindrical protrusions 206
extending along the lengths of the plate, which form gas passages or conduits. Along
each gas conduit, the plurality of protrusions 206 are alternated with a plurality
of indents 207. A main axial direction of the substantially semi-cylindrical protrusions
is arranged along a direction between the first and second ends.
[0032] Similarly, each lower plate of each cooling plate comprises a plurality of substantially
semi-cylindrical protrusions 206 and a plurality of indents 207 arranged in rows and
columns between a first end and a second end of the lower plate. The lower plate comprises
a plurality of generally semi-cylindrical indents and protrusions extending along
the length of the plate, which form the opposite walls of the gas passages or conduits
[0033] In each cooling plate, for each gas channel, the plurality of protrusions in the
upper plate line up opposite the plurality of indents in the lower plate, and the
plurality of protrusions on the lower plate line up opposite the corresponding respective
plurality of indents in the upper plate with the result that the protrusions and indents
along each gas conduit creates a serpentine tubular gas conduit in which the gas flow
follows a serpentine path along the conduit inside the cooling plate, between the
upper and lower plates, which causes continuous turbulence and mixing of the gas allowing
the gas to contact the interior surfaces of the gas conduits and thereby achieves
efficient heat transfer between the gas and the metal of the cooling plate. The edges
of the plates are sealed together in a gas tight manner.
[0034] On the upper plate, the plurality of indents or depressions are arranged in rows
and columns, and separating the plurality of raised protrusions, the arrangement being
that for each gas conduit between the first and second ends of the upper plate, each
conduit is periodically interrupted by a plurality of said indents / depressions.
[0035] Similarly, on the lower plate, there are a corresponding plurality of lines of protrusions
and depressions or indents, arranged in rows and columns over the lower plate, the
arrangement being that for each conduit extending between the first and second ends
of the lower plate, the internal bore of that conduit or passage are periodically
interspersed with a plurality of said indents /depressions, creating a substantially
serpentine gas flow path.
[0036] As the upper and lower plates are fixed together, the depressions of the upper plate
line up with the corresponding respective protrusions of the lower plate, and vice
versa the depressions of the lower plate line up adjacent to the corresponding respective
protrusions on the upper plate, the result being a plurality of tubular fluid or gas
conduits / passages channels extending between the first and second ends of the cooling
plate, each of which have a serpentine path. The gas passages cross a central plane
of the cooling plate, as the gas flow undulates passing between the semi-circular
protrusions of the upper and lower plates.
[0037] Providing the serpentine fluid conduits, causes the fluid to undulate, and generates
turbulence in the fluid flow and thereby enhances the heat transfer between the upper
and lower plates of each cooling plate and the gas flow.
[0038] In the cooling plate of Figure 2 herein, the depressions or indents on the external
surface of the cooling plate line up in a direction transverse to the main gas flow
direction, allowing coolant to penetrate between the cooling plates when the cooling
plates are stacked together, and allowing coolant flow over the outside surfaces of
the cooling plates.
[0039] There is also shown a substantially flat surface 212 on the upper plate of the cooling
plate at the first end, and a second substantially smooth flat planar surface 213
at the second end. Similarly, the lower plate at the first end has a flat smooth surface
extending across the width of the plate, and at the second end the lower plate has
a further flat smooth surface extending across a width of the plate. These surfaces
are provided to engage with a plurality of corresponding slots in the bulkheads 300,
301, so that during manufacture, the ends of the cooling plates can be inserted into
the slots, and brazed or soldered to the bulkhead.
[0040] At the ends of the cooling plate, there are also provided a set of protrusions 214
and indents 215 which are relatively longer than the other indents 207 and protrusions
206. These extended indents and protrusions provide relatively larger width coolant
channels extending across the width of the cooling plates at each end of the cooling
plate. This allows a relatively higher flow rate of coolant across the ends of the
cooling plates at the near inlet and near outlet ends of the cooling plates, than
in the more central heat exchange area between the ends, and allows enhanced access
of coolant to the joint between the cooling plates and the bulkheads. This helps to
provide more efficient cooling at the interface between the cooling plates and the
bulkhead at the inlet header.
[0041] The enhanced length protrusions and indents at the ends of the cooling plates also
provide a relatively straighter bore to the gas passages at the inlet end and the
outlet end compared to the more undulating bore of the gas passages in the central
heat exchange region. This results in slightly reduced heat transfer from gas to cooling
plate metal in the near inlet region, thereby assisting in reducing the temperature
at the inlet end of the cooling plate and at the joint between the cooling plate and
the bulkhead. Similarly, the extended length indents / protrusions at the other end
provide a region of slightly reduced heat exchange from gas to cooling plate, and
a slightly increased heat exchange from cooling plate to coolant, at the gas outlet
end. In this embodiment, the cooling plates and the cooling plate assembly are symmetrical,
and the assembly can be reversed so that the outlet can be used as the inlet end and
vice versa.
[0042] Referring to Figure 3 herein, there is illustrated schematically in view from one
side a cooling plate assembly of the heat exchanger of figure 1 herein.
[0043] The first ends of the plurality of cooling plates are connected to the first bulkhead
300, for example by brazing or soldering. Similarly, the plurality of second ends
of the plurality of cooling plates are connected to the second bulkhead 301 by brazing
or soldering.
[0044] The plurality of cooling plates are held by the first and second bulkheads, so that
the plates are stacked on top of each other, with a gap there between to allow passage
of coolant fluid between adjacent cooling plates.
[0045] The entire assembly shown in Figures 2 and 3 herein is encased in a rectangular box
section casing, having a coolant inlet and a coolant outlet. One or more gas inlets
and gas outlets are provided to the casing, and there is an inlet header region between
the main gas inlet connector on the casing between the main gas inlet connector 104,
and the inlet ends of the cooling plate assembly.
[0046] Each cooling plate has at least one gas inlet and at least one gas outlet, and in
the embodiment shown, there are a plurality of gas inlets 302 to the plurality of
cooling plates, protruding through the first bulkhead, and at the second end, there
are a plurality of gas outlets 303 of the individual cooling plates protruding from
the second bulkhead.
[0047] Referring to Figure 4 herein, there is illustrated schematically in close up, a view
of the first end of the "I" shaped cooling plate assembly. Each cooling plate has
a corresponding respective single gas inlet 400 - 406.
[0048] Since each cooling plate is substantially symmetrical, the gas flow can be reversed
in the opposite direction, from the second to the first end without any substantial
difference in performance.
[0049] In the side view of Figure 4 herein, there are shown viewed between and parallel
to the main planes of the cooling plates, a plurality of coolant cross channels 407
- 412 formed between a plurality of relatively longer substantially semi-cylindrical
protrusions 214 of the upper plates of the cooling plates, and the lower plates of
a neighboring cooling plates immediately adjacent. These channels near to the bulkhead
300 allow coolant to flow in a direction across the width of the cooling plate in
a region near to the bulkhead and allowing relatively high coolant flow rates and
direct coolant contact with an inner surface 413 of the bulkhead 300, thereby allowing
efficient heat transfer from the bulkhead 300 to the coolant, and heat transfer to
the coolant fluid from the portions of the cooling plate where the cooling plates
join the bulkhead.
[0050] As shown in Figures 3 and 4 herein, portions of the flat surfaces which protrude
from the bulkheads on the interior of the cooling plate assembly provide a plurality
of substantially straight through channels 407 - 412 for the coolant to flow across
the first bulkhead and parallel to the first bulkhead, in contact with the bulkhead
between the first and second sides of the cooling plate assembly. Similarly, the regions
of substantially flat plate immediately adjacent to the second bulkhead 301 at the
other (second) end of the cooling plate assembly form a plurality of substantially
straight coolant channels immediately adjacent the second bulkhead, allowing efficient
access of the cooling fluid to the bulkhead, and to the joints between the cooling
plates and the second bulkhead.
[0051] In Figures 3 and 4, since the cooling plates are substantially symmetrical, the cooling
plate assembly can be reversed so that gas can flow through in either direction, so
that either bulkhead can be used as the fluid inlet or the fluid outlet.
[0052] Referring to Figure 5A herein, there is illustrated schematically the "I" shaped
plate heat exchanger of Figure 1 herein, in view from one side.
[0053] In Figure 5B herein, there is shown schematically a comparison of gas temperature,
and coolant temperature along the length of the cooling plate assembly.
[0054] Referring to Figure 5A herein, an "I" plate heat exchanger is illustrated in view
from one side. At a first inlet end 500 (the inlet header end), there is provided
a plurality of coolant channels extending in a direction transverse to the overall
flow direction of fluid to be cooled, the coolant channels being of a relatively larger
cross sectional area, and allowing a relatively high coolant flow rate in a direction
parallel to a main plane of the inlet bulkhead of the plate cooler, compared to a
plurality of coolant fluid cross channels 501 nearer the centre of the heat exchanger.
[0055] Similarly, at a second end 502 of the "I" plate heat exchanger there is provided
a second set of cross channels 503 providing coolant flow in a direction transverse
to a main direction of gas flow, and parallel to a main plane of the second (outlet)
bulkhead plate, the second set of channels having relatively greater flow capacity
and relatively greater cross sectional area in a direction transverse to a direction
of coolant flow along the channels, than other coolant channels extending across the
cooler away from the bulkhead.
[0056] Referring to Figure 5B herein, there is illustrated a plot of coolant temperature
(round points) and gas temperature (diamond points) against the length along the cooling
plate assembly.
[0057] The inlet header end is at the left hand of the graph in Figure 5B and the outlet
end is at the right hand side of the graph in Figure 5B.
[0058] The coolant temperature, shown by circular dots is relatively reduced immediately
adjacent to the bulkhead, due to the presence of the near-inlet cooling channels extending
in a direction transverse to the direction of gas flow along the cooling plates. Similarly,
there is a corresponding slight reduction in coolant temperature immediately adjacent
to the gas outlet s and the second bulkhead.
[0059] The gas temperature, shown on the diamond shaped line in Figure 5B, which reduces
gradually as the gas passes along the cooling plates, from the inlet header end to
the outlet end.
[0060] The temperature of the coolant fluid near the inlet end is relatively reduced, whilst
the temperature profile of the gas / fluid along the length of the assembly shows
a gradual decline to an acceptable gas outlet temperature.
[0061] Referring to Figure 6 herein, there is illustrated schematically in perspective view,
a second heat exchanger 600 according to a second specific embodiment. The second
heat exchanger comprises a substantially "U" shaped canister type heat exchanger.
[0062] The "U" shaped heat exchanger 600 comprises a first section for cooling condensate
gas, and a second section for cooling an "anode off' gas, being a gas which is given
off an anode of a fuel cell, and which may be electrically charged.
[0063] The first and second heat exchange sections share a casing 601, and a liquid coolant
supply which flows into the casing via a coolant inlet pipe or tube 602, and leaves
the casing via a coolant outlet pipe or tube, 603. The first section comprises a gas
inlet 604 and a gas outlet 605, which feed gas into and out of the first heat exchange
section.
[0064] The second heat exchange section for cooling the anode gas comprises a a heat exchange
plate assembly, said heat exchange plate assembly comprising a plurality of heat exchange
plates stacked side by side and held rigid and spaced apart from each other by a bulkhead
plate. The heat exchange plate assembly comprises a plurality of gas inlets 606 -
608, accessible externally via the bulkhead; a plurality of gas outlets 609 - 611
accessible externally via the bulkhead; at least one fluid inlet connector 612, to
allow anode off gas to enter the casing; and at lease one fluid outlet connector 613
to allow cooled anode off gas to exit the casing. There is also provided a condensate
drain 614 to collect condensate from the cooling plates.
[0065] The anode off gas outlet 613 and condensate drain 614 each lead to a condensate tank
for collecting condensate. The anode off gas inlet 612, the anode off gas outlet 613,
and the condensate drain 614 may each comprise standard pipe connectors.
[0066] Referring to Figure 7 and 8 herein, there is illustrated schematically in view from
one side, the cooling plate assembly of the substantially "U" shaped heat exchanger
of Figure 6 herein. Figure 7 illustrates schematically, the cooling plate assembly,
absent of its external casing.
[0067] Figure 8 illustrates schematically in close up view, a detail of the connection between
the plurality of cooling plates and the bulkhead of the heat exchanger.
[0068] Referring to Figure 7 herein, shown in view from one side, a plurality of cooling
plates 700 - 704 are arranged side by side and spaced apart from each other to allow
coolant fluid to percolate between the cooling plates to cool the outer surfaces of
the cooling plates. At a first end 705, bulkhead 706 joins the plurality of cooling
plates together. The cooling plates may be inserted into a substantially "U" shaped
canister, such that the cooling plates are suspended inside the canister, held at
their first ends 707 by the bulkhead.
[0069] Each cooling plate comprises an upper plate and a lower plate connected together
around their perimeters, and forming at a first end, a gas inlet and a gas outlet,
so that the plurality of gas inlets and the plurality of gas outlets of the cooling
plates are all presented on a same face of the heat exchanger.
[0070] Each cooling plate comprises a plurality of gas passages or conduits formed as a
plurality of protrusions and indents or depressions, similarly as described herein
before with reference to the first embodiment. However, in the "U" shaped cooling
plates, the conduits extend in parallel from the first end to the second end 708,
arc around in a semi circle at the second end, and return from the second end to the
first end. Thus, gas enters on one side of the cooling plate, travels around a "U"
shaped gas conduit, and exits at the first end.
[0071] In this embodiment, the gas outlet of one cooling plate is arranged to locate on
a same side of the heat exchanger as a gas inlet of the adjacent cooling plate in
the stack, with the plurality of gas inlets and outlets all on the same face. Hence
each plate has a gas inlet region and a gas outlet region located side by side at
the first side of the cooling plate.
[0072] Gas enters the plurality of cooling plates at the respective inlet regions, and exhausts
from the plurality of cooling plates at the respective outlet regions. In this case,
since the channels are "U" shaped, the inlet header of one cooling plate lies adjacent
an outlet header of another cooling plate.
[0073] Gas travelling along each gas conduit experiences an alternating side to side serpentine
path, as it encounters alternate indents and protrusions along a length of the gas
conduit.
[0074] Fluid coolant flows across a width of the cooling plates in a direction transverse
to a length between the two ends of the cooling plates, via a plurality of fluid channels
formed by the plurality of indents or depressions in the otherwise substantially cylindrical
gas conduits.
[0075] Referring to figure 8 herein, immediately adjacent the bulkhead 706, there are provided
a plurality of fluid coolant channels 800, which are relatively increased in cross
sectional area in a direction transverse to a main direction of the gas flow. These
regions allow coolant fluid to contact the inner surface 801 of the bulkhead 706,
thereby allowing efficient cooling of the bulkhead.
[0076] The increased size coolant fluid channels 800 immediately adjacent to the bulkhead
and the joint between the bulkhead and the cooling plates reduces the occurrence of
overheating of the coolant fluid near to the joint, and allows the bulkhead and the
joint between the bulkhead and each cooling plate to be continuously in contact with
liquid coolant to dissipate heat.
[0077] Additionally, each gas conduit has a respective near inlet region 802 - 806 which
has a relatively straight and smooth bore, compared to the main heat exchange region
between the gas inlet and gas outlet of each conduit. This allows the gas to pass
relatively freely through this initial section of the gas passage, with low induction
of turbulence, which helps reduce the heat transfer between the gas and the metal
walls of the cooling plate in the immediate near inlet region of cooling plate. The
internal bore of the gas passage is relatively more undulating in the main heat exchange
region than at the gas inlet and gas outlet ends, and the fluid flow in through these
parts of the conduits is more turbulent.
[0078] Referring to Figure 9 herein, there is illustrated schematically in view from one
side a third embodiment heat exchanger comprising a plurality of individual cooling
plates 900-905.
[0079] Two separate arrangements are possible. In a first arrangement, similar to the "I"
plate arrangement of Figures 1-5, the plates are located adjacently, but without the
need for a bulkhead at either end. In this arrangement, all of the inlets are arranged
at one end of the heat exchanger plate assembly and all of the outlets are arranged
at the other (outlet) end.
[0080] In a second arrangement, where the cooling plates are "U" shaped cooling plates each
cooling plate having a gas inlet and a gas outlet at the same end, with the gas inlet
and gas outlet on opposite sides of the cooling plate, the gas outlet of a first cooling
plate for example 900 is co-located with a gas inlet of a second adjacent cooling
plate, for example 901. Similarly, the gas outlet of the second cooling plate 901
is co-located adjacent to a gas inlet of the third cooling plate 902 and so on, down
the stack of cooling plates.
[0081] In either case, adjacent to the inlet region of each cooling plate is provided an
indent, across the width of the cooling plate, so that when the cooling plates are
stacked one on top of the other as shown in Figure 9, a plurality of coolant channels
are formed 906-912 to allow coolant to flow across a width of the cooling plate and
in a direction transverse to a main gas flow direction. Since the coolant cross channels
906-912 are provided immediately adjacent to the inlet header of each cooling plate,
this allows coolant to flow across the width of the cooling plates in a direction
perpendicular to the main direction of gas flow, so that the inlets of the cooling
plates are cooled relatively more efficiently.
[0082] Similarly, as shown in the first and second embodiments herein, each cooling plate
has a plurality of gas conduits extending along the cooling plate, where each gas
conduit forms a serpentine gas path, there being enough space for coolant to flow
between the plates, so that heat exchange can occur between the fluid or gas flowing
through the conduits of the cooling plates, and the coolant which flows within the
casing and externally around the outside of the cooling plates.
[0083] In the embodiments of figure 9 herein, the cooling plates are held together at their
ends in contact with each other and without the need for a connecting bulkhead between
the individual plates. This means that the gas inlets and outlets of the cooling plates
can be relatively larger in cross sectional area than if a connecting bulkhead plate
were used. An outer connecting plate may surround the cooling plates to hold them
together in contact with each other within the outer casing. The ends of the cooling
plates may be brazed or dip soldered together at their inlet and outlet ends.
[0084] The increased fluid flow across the gas inlet ends of the cooling plates helps to
reduce the temperature of the inlet ends of the cooling plates, and reduce any stresses
where the cooling plates contact each other and / or the surrounding plate at the
inlet end.
[0085] Referring to Figures 10 and 11 herein, there is shown schematically a cooling plate
assembly of a "I" type heat exchanger unit according to a fourth specific embodiment.
[0086] The heat exchanger comprises one or a plurality of such cooling plates, held in an
outer casing, by first and second bulkhead plates, one at each end of the heat exchange
plate. The external casing comprises one or more coolant inlets for allowing a cooling
fluid to enter the casing and permeate around the cooling plate assembly and one or
more coolant outlets which allow the coolant fluid to exit the casing, one or more
gas inlet connectors to allow the gas to enter the cooling plate assembly and one
or more gas outlet connectors to allow the gas to exhaust from the heat exchange assembly.
In external view, the external casing may be similar to that shown in Figure 1 herein.
[0087] Referring to Figure 10 herein, there is illustrated schematically in view from above,
one cooling plate of an "I" type plate heat exchanger.
[0088] Each cooling plate 1000 comprises a pair of flat metal plates joined together at
their sides 1001, 1002, and forming a plurality of fluid conduits or passages 1003
there between (herein also referred to as gas conduits), each fluid conduit extending
between first and second ends 1004, 1005 respectively of the cooling plate.
[0089] The upper plate comprises a plurality of generally semi-cylindrical protrusions 1006
extending along the lengths of the plate, which form gas passages or conduits. Along
each gas conduit, the plurality of protrusions 1006 are alternated with a plurality
of scallop shaped indents 1007. A main axial direction of the substantially semi-cylindrical
protrusions is arranged along a direction between the first and second ends.
[0090] Similarly, each lower plate of each cooling plate comprises a plurality of substantially
semi-cylindrical protrusions 1006 and a plurality of scallop shaped indents 1007 arranged
in rows and columns between a first end and a second end of the lower plate. The plurality
of generally semi-cylindrical indents and protrusions extending along the lengths
of the lower plate form the opposite walls of the gas passages or conduits
[0091] In each cooling plate, for each gas channel, the plurality of protrusions in the
upper plate line up opposite the plurality of indents in the lower plate, and the
plurality of protrusions on the lower plate line up opposite the corresponding respective
plurality of indents in the upper plate with the result that the protrusions and indents
along each gas conduit creates a serpentine tubular gas conduit in which the gas flow
follows a serpentine path along the conduit inside the cooling plate, between the
upper and lower plates, which causes continuous turbulence and mixing of the gas within
the gas conduit, allowing the gas to contact the interior surfaces of the gas conduits
and thereby achieves efficient heat transfer between the gas and the metal of the
cooling plate. The edges of the plates are sealed together in a gas tight manner.
[0092] On the upper plate, the plurality of indents or depressions are arranged in rows
and columns, the arrangement being that for each gas conduit between the first and
second ends of the upper plate, each conduit is periodically interrupted by a plurality
of said indents / depressions.
[0093] Similarly, on the lower plate, there are a corresponding plurality of lines of protrusions
and depressions or indents, arranged in rows and columns over the lower plate, the
arrangement being that for each conduit extending between the first and second ends
of the lower plate, the internal bore of that conduit or passage is periodically interspersed
with a plurality of said indents /depressions, creating a substantially serpentine
gas flow path.
[0094] As the upper and lower plates are fixed together, the depressions of the upper plate
line up with the corresponding respective protrusions of the lower plate, and vice
versa the depressions of the lower plate line up adjacent to the corresponding respective
protrusions on the upper plate, the result being a plurality of tubular fluid or gas
conduits / passages channels extending between the first and second ends of the cooling
plate, each of which have a serpentine path. The gas passages cross a central plane
of the cooling plate, as the gas flow undulates passing between the semi-circular
protrusions of the upper and lower plates.
[0095] Providing the serpentine fluid conduits causes the fluid flow to undulate, and generates
turbulence in the fluid flow and thereby enhances the heat transfer between the upper
and lower plates of each cooling plate and the gas flow.
[0096] In the cooling plate of Figure 10 herein, the depressions or indents on the external
surface of the cooling plate line up in a direction transverse to the main gas flow
direction, allowing coolant to penetrate between the external surfaces of the adjacent
cooling plates when the cooling plates are stacked together, and allowing coolant
flow over the outside surfaces of the cooling plates.
[0097] There is also shown a substantially flat surface 1012 on the upper plate of the cooling
plate at the first end, and a second substantially smooth flat planar surface 1013
at the second end. Similarly, the lower plate at the first end has a flat smooth surface
extending across the width of the plate, and at the second end the lower plate has
a further flat smooth surface extending across a width of the plate. These surfaces
are provided to engage with a plurality of corresponding slots in the bulkheads 1100,
1101, so that during manufacture, the ends of the cooling plates can be inserted into
the slots, and brazed or soldered to the bulkhead.
[0098] At the ends of the cooling plate, the individual gas conduits have a near-bulkhead
region in which the internal bore of the gas passage is relatively smooth and uninterrupted
by protrusions or despressions. The length of the relatively smooth bore may extend
in the range 5% to 10% of the length of the whole cooling plate, and in this example,
approximately 7% of the length of the cooling plate. The individual near-bulkhead
regions of the gas conduits are slightly divergent in the direction of the inlets
1102 into the cooling plate, so as to provide a smooth gas passage, and to reduce
the amount of heat transfer between the gas and the insides of the gas passage at
the gas conduit immediate inlet region, compared to the central region of the cooling
plates, beyond the inlet region, where the gas passage follows a convoluted path.
[0099] Additionally, these extended smooth regions of the gas conduit shape the outside
of the cooling plates in the near bulkhead regions, to provide relatively larger width
coolant channels extending across the width of the cooling plates at each end of the
cooling plate. This allows a relatively higher flow rate of coolant across the ends
of the cooling plates at the near inlet and near outlet ends of the cooling plates,
than in the more central heat exchange area between the ends, and allows enhanced
access of coolant to the joints between the cooling plates and the bulkheads. This
helps to provide more efficient cooling at the interface between the cooling plates
and the bulkhead at the inlet header.
[0100] The enhanced length smooth bore portions at the end of the cooling plates provide
a relatively straighter bore to the gas passages at the inlet end and the outlet end
compared to the more undulating bore of the gas passages in the central heat exchange
region. This results in slightly reduced heat transfer from gas to cooling plate metal
in the near inlet region, thereby assisting in reducing the temperature at the inlet
end of the cooling plate and at the joint between the cooling plate and the bulkhead.
Similarly, the extended length smooth bore portions at the other end provide a region
of slightly reduced heat exchange from gas to cooling plate, and a slightly increased
heat exchange from cooling plate to coolant, at the gas outlet end. In this embodiment,
the cooling plates and the cooling plate assembly are symmetrical, and the assembly
can be reversed so that the outlet can be used as the inlet end and vice versa.
[0101] Referring to Figure 11 herein, there is illustrated schematically in view from one
side a cooling plate assembly of the heat exchanger of Figure 1 herein.
[0102] The first ends of the plurality of cooling plates are connected to the first bulkhead
1100, for example by brazing or soldering. Similarly, the plurality of second ends
of the plurality of cooling plates are connected to the second bulkhead 1101 by brazing
or soldering.
[0103] The plurality of cooling plates are held by the first and second bulkheads, so that
the plates are stacked on top of each other, with a gap there between to allow passage
of coolant fluid between adjacent cooling plates.
[0104] The entire assembly shown in Figures 10 and 11 herein is encased in a rectangular
box section casing, having a coolant inlet and a coolant outlet. One or more gas inlets
and gas outlets are provided to the casing, and there is an inlet header region between
the main gas inlet connector on the casing between the main gas inlet connector 104,
and the inlet ends of the cooling plate assembly.
[0105] Each cooling plate has at least one gas inlet and at least one gas outlet, and in
the embodiment shown, there are a plurality of gas inlets 1102 to the plurality of
cooling plates, protruding through the first bulkhead, and at the second end, there
are a plurality of gas outlets 1103 of the individual cooling plates protruding from
the second bulkhead.
1. A cooling plate assembly for cooling a fluid flow using a liquid coolant, said assembly
comprising:
a plurality of cooling plates, each cooling plate comprising a plurality of fluid
conduits through which fluid can flow; and
said cooling plate assembly comprising a fluid inlet region, a fluid outlet region
and a heat exchange region;
characterised by,
a set of first coolant channels arranged between said plurality of cooling plates
and positioned immediately adjacent to said fluid inlet region, each of said coolant
channels extending in a direction transverse to a main flow direction of said plurality
of fluid conduits, said set of first coolant channels allowing a relatively higher
coolant flow rate in a direction transverse to a main length of said coolant channels,
than occurs in a region of the cooling plates further away from said inlet region.
2. The cooling plate assembly as claimed in claim 1, wherein each said coolant channel
is formed between a lower section of one said cooling plate, and an upper section
of another said cooling plate.
3. The cooling plate assembly as claimed in claim 1, wherein each said coolant channel
is formed between a lower section of one cooling plate and an upper section of another
said cooling plate and the cooling plates are joined to form an interface between
said fluid conduits and a gas header.
4. The cooling plate assembly as claimed in any one of the preceding claims, comprising
a second set of coolant channels positioned further away from said inlet region than
said first coolant channels, wherein a flow path of a said first coolant channel enables
greater coolant flow rate in a direction transverse to the main fluid flow direction,
than occurs in said second coolant channel.
5. The cooling plate assembly as claimed in any one of the preceding claims, comprising
a second set of coolant channels positioned further away from said inlet region, than
said set of first coolant channels, wherein a cross sectional area of a said first
coolant channel in a direction transverse to a main fluid flow direction in said fluid
conduits, is in the range 1.2 to 5 times a cross sectional area of a said second coolant
channel in the same direction.
6. The cooling plate assembly as claimed any one of the preceding claims, comprising:
a first bulkhead plate at a first end of said assembly;
a second bulkhead plate at a second end of said assembly; and
said plurality of cooling plates extending between said first and second connecting
plates;
wherein there are provided a set of said first coolant channels immediately adjacent
to said first bulkhead, and a further set of said coolant channels positioned immediately
adjacent to said second bulkhead.
7. The cooling plate assembly as claimed in any one of claims 1 to 6, comprising a single
connecting plate connecting together aplurality of substantially "U" shaped cooling
plates.
8. The cooling plate assembly as claimed in claim 7, wherein there are provided a set
of said first coolant channels immediately adjacent a set of fluid inlets of said
substantially "U" shaped cooling plates.
9. The cooling plate assembly as claimed in claim 7, wherein there are provided a set
of said first coolant channels immediately adjacent a set of fluid inlets of said
substantially "U" shaped cooling plates and immediately adjacent a set of fluid outlets
of said plurality of substantially "U" shaped cooling plates.
10. A heat exchanger comprising:
a cooling plate assembly as claimed in any one of the preceding claims; and
an outer canister;
at least one coolant inlet for allowing coolant to flow into said canister; and
at least one coolant outlet for allowing coolant to flow out of said canister.
11. A cooling plate for a heat exchanger, said cooling plate comprising:
an upper plate;
a lower plate;
said upper plate and lower plate being connected together along first and second edges
in a fluid tight manner;
said upper and lower plates forming a plurality of fluid conduits extending along
a length of said cooling plate;
said upper and lower plates comprising a plurality of protrusions and depressions
for allowing a fluid coolant to pass over an outer surface of said cooling plate in
a direction transverse to a fluid flow direction in said fluid conduits;
characterised by
a region immediately adjacent one end of said cooling plate, on at least one of said
upper or lower plates, for allowing a relatively higher coolant flow rate across a
width of said cooling plate immediately adjacent said end of said cooling plate.
12. The cooling plate as claimed in claim 11, wherein
said fluid conduits extend between a first end and a second end of said cooling plate;
and
at least one end of said cooling plate is provided with a region immediately adjacent
to said end, which is clear of said protrusions on at least one of said upper or lower
plates, for allowing a relatively higher coolant flow rate across the width of said
cooling plate immediately adjacent to said end.
13. A cooling plate as claimed in claim 11 or 12, comprising a substantially "U" shaped
plate, having a plurality of fluid inlets and a plurality of fluid outlets at said
first end.
14. A cooling plate as claimed in claim 11 or 12, comprising:
a plurality of fluid inlets at a first end of said cooling plate; and
a plurality of fluid outlets at a second end of said cooling plate.
15. A cooling plate assembly comprising:
a plurality of cooling plates, each cooling plate comprising a plurality of fluid
conduits through which fluid can flow;
said plurality of cooling plates comprising a fluid inlet region, a fluid outlet region,
and a heat exchange region;
characterised in that,
said fluid conduits are each provided with a relatively extended smooth internal surface
immediately adjacent said at fluid inlet region, for minimising turbulence of fluid
flow in said fluid conduits adjacent to said fluid inlet region.
16. A cooling plate comprising:
upper and lower plates joined together to form a plurality of fluid conduits through
which fluid can flow;
said plurality of cooling plate comprising a fluid inlet region, a fluid outlet region,
and a heat exchange region positioned between said fluid inlet region and said fluid
outlet region;
characterised in that,
said fluid conduits are provided with a relatively extended smooth internal surface
immediately adjacent said fluid inlet region, for minimising turbulence of fluid flow
in said fluid conduits adjacent to said fluid inlet region .
17. A heat exchanger gas conduit with a smoother gas side surface at and near the bulkhead,
which reduces the heat transfer co-efficient and thus reduces the risk of localised
boiling at or near the bulkhead.
Amended claims in accordance with Rule 137(2) EPC.
1. A cooling plate assembly for cooling a fluid flow using a liquid coolant, said assembly
comprising:
a plurality of cooling plates (200), each cooling plate comprising a plurality of
fluid conduits (203) through which fluid can flow; and
said cooling plate assembly comprising a fluid inlet region, a fluid outlet region
and a heat exchange region;
characterised by,
a set of first coolant channels (407 - 412; 800) arranged between said plurality of
cooling plates and positioned immediately adjacent to said fluid inlet region, each
of said first coolant channels extending in a direction transverse to a main flow
direction of said plurality of fluid conduits, said fluid conduits being sealed from
said set of first coolant channels, and at least one of said first coolant channels
allowing a relatively higher coolant flow rate in a direction transverse to a main
length of said fluid conduits than occurs in a region further away from said inlet
region.
2. The cooling plate assembly as claimed in claim 1, wherein each said first coolant
channel (407 - 412; 800) is formed between a lower section of one said cooling plate,
and an upper section of another said cooling plate.
3. The cooling plate assembly as claimed in claim 1, wherein each said coolant channel
is formed between a lower section of one cooling plate and an upper section of another
said cooling plate and the cooling plates are joined to form an interface between
said fluid conduits and a gas header.
4. The cooling plate assembly as claimed in any one of the preceding claims, comprising
a second set of coolant channels (501) positioned further away from said inlet region
than said first coolant channels, wherein a flow path of a said first coolant channel
enables greater coolant flow rate in a direction transverse to the main fluid flow
direction, than occurs in said second coolant channel (501).
5. The cooling plate assembly as claimed in any one of the preceding claims, comprising
a second set of coolant channels 9501) positioned further away from said inlet region,
than said set of first coolant channels (407 - 412; 800), wherein a cross sectional
area of a said first coolant channel in a direction transverse to a main fluid flow
direction in said fluid conduits, is in the range 1.2 to 5 times a cross sectional
area of a said second coolant channel in the same direction.
6. The cooling plate assembly as claimed any one of the preceding claims, comprising:
a first bulkhead plate (300) at a first end of said assembly;
a second bulkhead plate (301) at a second end of said assembly; and
said plurality of cooling plates (200) extending between said first and second connecting
plates;
wherein there are provided a set of said first coolant channels (407 - 412; 800) immediately
adjacent to said first bulkhead, and a further set of said first coolant channels
positioned immediately adjacent to said second bulkhead.
7. The cooling plate assembly as claimed in any one of claims 1 to 5, comprising a single
bulkhead (706) connecting together a plurality of substantially "U" shaped said cooling
plates.
8. The cooling plate assembly as claimed in claim 7, wherein there are provided a set
of said first coolant channels immediately adjacent a set of fluid inlets of said
substantially "U" shaped cooling plates.
9. The cooling plate assembly as claimed in claim 7, wherein there are provided a set
of said first coolant channels (800) immediately adjacent a set of fluid inlets of
said substantially "U" shaped cooling plates and immediately adjacent a set of fluid
outlets of said plurality of substantially "U" shaped cooling plates.
10. A cooling plate assembly, as claimed in claim 1,wherein:
said fluid conduits are each provided with a relatively extended smooth internal)
surface (1105) immediately adjacent said at fluid inlet region, for minimising turbulence
of fluid flow in said fluid conduits adjacent to said fluid inlet region .
11. A heat exchanger comprising:
a cooling plate assembly as claimed in any one of the preceding claims; and
an outer canister (101; 601);
at least one coolant inlet (102; 602) for allowing coolant to flow into said canister;
and
at least one coolant outlet (103; 603) for allowing coolant to flow out of said canister.
12. A heat exchanger, comprising a cooling plate assembly as claimed in any one of claims
1 to 10, wherein the fluid conduit is a gas conduit with a smoother gas side surface
at and near the bulkhead, which reduces the heat transfer co-efficient and thus reduces
the risk of localised boiling at or near the bulkhead.
13. A cooling plate (200; 700 - 704) for a heat exchanger, said cooling plate comprising:
an upper plate;
a lower plate;
said upper plate and lower plates being connected together along first and second
edges (201; 202) in a fluid tight manner;
said upper and lower plates forming a plurality of fluid conduits (200) extending
along a length of said cooling plate, through which a first fluid can flow;
said upper and lower plates comprising a plurality of protrusions (206) and depressions
(207) for allowing a fluid coolant to pass over an outer surface of said cooling plate
in a direction transverse to a first fluid flow direction in said fluid conduits;
characterised by
said fluid conduits (203) being sealed from an outer surface of said cooling plate;
and
said protrusions (206) and depressions (207) are arranged such that a region immediately
adjacent one end (204; 205) of said cooling plate, on at least one of said upper or
lower plates, provides for allowing a relatively higher coolant flow rate across a
width of said cooling plate in a direction transverse to a main length of said fluid
conduits, in a region immediately adjacent said end of said cooling plate than occurs
in a region further away from said end.
14. The cooling plate as claimed in claim 13, wherein:
said fluid conduits extend between a first end (204) and a second end (205) of said
cooling plate; and
at least one end of said cooling plate is provided with a region immediately adjacent
to said end, which is clear of said protrusions (206) on at least one of said upper
or lower plates, for allowing a relatively higher coolant flow rate across the width
of said cooling plate immediately adjacent to said end.
15. A cooling plate as claimed in claim 13 or 14, comprising a substantially "U" shaped
plate, having a plurality of fluid inlets and a plurality of fluid outlets at a same
said end.
16. A cooling plate as claimed in claim 13 or 14, comprising:
a plurality of fluid inlets at a first end (204) of said cooling plate; and
a plurality of fluid outlets at a second end (205) of said cooling plate.
17. A cooling plate, as claimed in claim 13, wherein:
said fluid conduits are provided with a relatively extended smooth internal surface
(1105) immediately adjacent said fluid inlet region, for minimising turbulence of
fluid flow in said fluid conduits adjacent to said fluid inlet region.