BACKGROUND OF THE INVENTION
Field of the Invention
[0001] The present invention relates to a plate for heat exchange, which is formed from
a metallic thin plate and combined with the other plates in an aligned state into
a heat exchanger, and especially to the heat exchange plate, which enables, in use
in combination with the other plates, heat exchange fluids to slow smoothly along
the opposite surfaces of the heat exchange plate to make an effective heat exchange,
irrespective of a flowing system such as a parallel flowing system in which the heat
exchange fluids flow in parallel with each other, a counter-flowing system in which
the heat exchange fluids flow in the opposite directions to each other, and a cross
flowing system in which the heat exchange fluids flow in perpendicular directions
to each other, and relates to a heat exchange unit in which such a heat exchange plate
and the other plates are combined.
Description of the Related Art
[0002] If there is a request that heat transfer coefficient is increased to enhance heat
exchange effectiveness, utilizing a heat exchanger by which heat exchange is made
between a high temperature fluid and a low temperature fluid, a plate-type heat exchanger
has conventionally been used widely. The plate-type heat exchanger has a structure
in which a plurality of plates, i.e., heat transfer members having a plate-shape are
placed parallelly one upon another at prescribed intervals so as to form passages,
which are separated by means of the respective plates. A high temperature fluid and
a low temperature fluid flow alternately in the above-mentioned passages to make heat
exchange through the respective plates. Japanese Patent Provisional Publication No.
S53-56748 describes an example of such a conventional plate-type heat exchanger.
[0003] In the conventional plate-type heat exchanger, gasket members formed of elastic material
are placed between the adjacent two plates to make the distance between them constant
and define passages for fluid. However, a high pressure of the heat exchange fluid
flowing between the plates may cause deformation of the gasket member, thus disabling
an appropriate separation of the fluids from being ensured or leading to an unfavorable
variation in distance between the plates. In such a case, an effective heat exchange
may not be carried out, thus causing a problem. In view of these facts, the conventional
heat exchanger involves a problem that the heat exchange fluids can be utilized only
in a pressure range in which the gasket member withstands.
[0004] There has recently been proposed a heat exchanger having a structure in which metallic
thin plates, which are placed at predetermined intervals, are joined together at their
ends by welding to assemble the plates into a single unit so as to form gaps, which
serve as passages for heat exchange fluids, on the opposite sides of the respective
plates. Japanese Patent Provisional Publication No. 2003-194490 describes, as an example
of an invention made by the present inventor, a heat exchange unit in which metallic
thin plates are aligned in parallel with each other so as to be apart from each other,
these plates are welded at their periphery excepting one side into a united body having
an opening, and the opening is closed by an end plate.
[0005] The above-described conventional heat exchanger (i.e., the heat exchange unit) has
a structure, as described in the above-mentioned publication, that each of the plates
has a pattern of irregularity with a shape and arrangement, by which the most preferable
heat transfer performance in the flowing direction of the respective heat exchange
fluids. In most cases, fluids for heat exchange used in the heat exchanger utilizing
the plates have a relationship based on a parallel flowing system, a counter-flowing
system or a cross flowing system. The plate of the conventional heat exchanger has
an optimized pattern of irregularity exclusively for any one of the parallel flowing
system, the counter-flowing system and the cross flowing system. When the plates having
the pattern of irregularity, which has been optimized exclusively for the flowing
system to be applied originally, are applied to the different flowing system, variation
in flowing conditions may occur to deteriorate the heat transfer performance, thus
leading to a lower heat exchange efficiency and increase in pressure loss. Accordingly,
there is a need to use plates having a pattern of irregularity, which has been optimized
for the flowing system to be applied originally, exclusively for such a flowing system.
[0006] In addition, in the conventional plate-type heat exchanger, the heat exchange fluid
enters the heat exchanger from a narrow inlet, divergently extends over the wide plane
of the plate to flow and then converges into a narrow outlet. Each of the plates has
three kinds of patterns of irregularity, i.e., an inflow divergent area, a main heat
transfer area and an outflow condensation area, in order to introduce the fluid over
every area of the plate. However, the inflow divergent area and the outflow condensation
area having patterns of irregularity, in which importance is placed generally on the
guiding performance for the fluids, do not provide a sufficient heat transfer performance.
The excellent heat transfer performance cannot be provided by these areas, with the
result that an effective area utilized for heat transfer is relatively small to the
total area of the plate, thus causing waste in space of occupancy and cost.
SUMMARY OF THE INVENTION
[0007] An object of the present invention, which was made to solve the above-mentioned problems,
is therefore to provide a heat exchange plate, which is provided on it surface with
a pattern of irregularity properly formed, has flexibility in use in the flowing system,
and permits to ensure a sufficient heat transfer performance relative to fluids, thus
providing an excellent heat transfer property, as well as a heat exchange unit in
which such a heat exchange plate and the other plates are combined to provide a determined
heat transfer property.
[0008] In order to attain the aforementioned object, a plate for heat exchange of the first
aspect of the present invention comprises a metallic plate member having a predetermined
pattern of irregularity, said plate member being combined with at least one other
plate member so as to be in parallel with each other to constitute a heat exchanger,
which makes a heat exchange between a heat exchange fluid coming into contact with
a surface of said metallic plate member and another heat exchange fluid coming into
contact with another surface thereof, said metallic plate member comprising:
a plurality of main protrusions formed on one surface of said plate member, each of
said main protrusions having a shape of any one of a quadrangular pyramid and a quadrangular
truncated pyramid with a top, a first pair of opposite side surfaces and a second
pair of opposite side surfaces, said first pair of opposite side surfaces facing each
other in a first direction and said second pair of opposite side surfaces facing each
other in a second direction perpendicular to said first direction, said main protrusions
being aligned in the first direction and the second direction by a predetermined distance
so that the first pair of opposite surfaces and the second pair of opposite surfaces
of one of the main protrusions face corresponding opposite surfaces of adjacent protrusions;
and
a plurality of intermediate protrusions formed between adjacent two main protrusions
on said plate member, each of said intermediate protrusions having opposite foot portions
and a head ridge placed between said foot portions, each of said foot portions being
placed in a lowermost position at which ridgelines of the adjacent two main protrusions
intersect each other, and said head ridge being placed in a level that is higher than
said foot portions and lower than said top of each main protrusion, so as to provide
a bent roof shape, said intermediate protrusions and said main protrusions forming
said predetermined pattern of irregularity.
[0009] According to the first aspect of the present invention, the heat exchange plate is
formed of the metallic plate member having the pattern of irregularity that includes
the main protrusions and the intermediate protrusions provided on the plate member.
Combining such a heat exchange plate with the other heat exchange plates so that these
plates face each other at the same side and the tops of the main protrusions of the
plate come into contact with the corresponding tops of the main protrusions of the
other plate, or so that these plates face each other at the same other side and projections
between the adjacent two intermediate protrusions of the plate come into contact with
corresponding projections of the other plate, provides a gap between the adjacent
two plates. The above-mentioned gap has a dimension corresponding to the pattern of
irregularity of the plates, in which a unit of the similar pattern of irregularity
is repeated in two directions that are perpendicular to each other, thus providing
linear passages extending in the above-mentioned two directions so as to cross each
other at right angles. More specifically, each of the linear passages extending in
the direction includes expanded areas and throat areas that are placed alternately
in the same direction, on the one hand, and the linear passage extending in the perpendicular
direction to the above-mentioned direction includes expanded areas and throat areas
that are placed alternately in the same perpendicular direction, in the similar manner.
Using the thus assembled plates so that the flowing direction of the heat exchange
fluid coincides with the linear passage or is perpendicular thereto can impart substantially
the same behavior to the heat exchange fluid, irrespective the flowing system of the
heat exchange fluid, i.e., any one of the parallel flowing system, the counter-flowing
system and the cross flowing system. As a result, it is possible to perform a smooth
heat transfer at a low pressure loss to make an effective heat exchange, even when
the heat exchange fluids are combined in any manner in their flowing directions, thus
providing a high degree of freedom in design of the heat exchanger and becoming excellent
in general purpose use. In addition, the heat exchange fluid ca flow freely in the
above-mentioned two directions along the plate, and the constant heat transfer property
can be obtained, irrespective of the flowing direction of the heat exchange fluid.
It is therefore possible to cause the heat exchange fluid to spread over the entire
area of the plate so that such an entire area can serve as an effective heat transfer
section, thus increasing remarkably an amount of heat transfer per area and achieving
a high performance. Further, the strength of the assembled plates can be improved
remarkably by bringing the protrusions of the plate into contact with the corresponding
protrusions of the other plate, and it is therefore possible to keep the distance
between the adjacent two plates constant, even when there exists a large difference
in pressure between the heat exchange fluids, thus enhancing a pressure-resistant
property.
[0010] In the second aspect of the present invention, the plate member may have a shape
of any one of a rectangle and a square with side edges, along which said ridgelines
of said main protrusions extend in parallel with or perpendicular to said side edges
of said plate member.
[0011] According to the second aspect of the present invention, the plate member has the
pattern of irregularity in which the ridgelines of the main protrusions extend in
parallel with or perpendicular to the side edges of the plate member. Placing the
plates having such a pattern of irregularity so that the side edge of the plate coincides
with a horizontal direction or vertical direction provides areas between the intermediate
protrusions and the foot portions, each of which areas extends obliquely relative
to the horizontal or vertical direction. As a result, the heat exchange fluids introduced
into the combined plates flows in the oblique direction, and repeats divergence and
confluence to spread over every area of the plate. It is therefore possible to cause
the heat exchange fluid to spread over the entire area of the plate to facilitate
the heat transfer between the heat exchange fluids and improving the heat exchange
rate.
[0012] In order to attain the aforementioned object, a plate for heat exchange of the third
aspect of the present invention comprises a metallic plate member having a predetermined
pattern of irregularity, said plate member being combined with at least one other
plate member so as to be in parallel with each other to constitute a heat exchanger,
which makes a heat exchange between a heat exchange fluid coming into contact with
a surface of said metallic plate member and another heat exchange fluid coming into
contact with another surface thereof, said metallic plate member comprising:
a plurality of protrusions formed on one surface of said plate member, each of said
main protrusions having a shape of any one of a quadrangular pyramid and a quadrangular
truncated pyramid with ridgelines, said protrusion being aligned by a predetermined
distance so that parallel planes include said ridgelines of said protrusions; and
a plurality of recess portions formed between adjacent two protrusions on said plate
member, each of said recess portions having substantially the same shape as said protrusions
by deforming said plate member in an opposite direction to a protruding direction
of said protrusions, said protrusions and said recess portions on the surface of said
plate member forming said predetermined pattern of irregularity so that a similar
pattern of irregularity to said predetermined patter of irregularity is provided on
another surface of said plate member.
[0013] According to the third aspect of the present invention, the heat exchange plate is
formed of the metallic plate member having the pattern of irregularity that includes
the protrusions and the recess portions provided on the plate member. Combining such
a heat exchange plate with the other heat exchange plates so that these plates face
each other at the same side and the tops of the protrusions of the plate come into
contact with the corresponding tops of the protrusions of the other plate. The above-mentioned
gap has a dimension corresponding to the pattern of irregularity of the plates, in
which a unit of the similar pattern of irregularity is repeated in two directions
that are perpendicular to each other, thus providing linear passages extending in
the above-mentioned two directions so as to cross each other at right angles. More
specifically, each of the linear passages extending in the direction includes expanded
areas and throat areas that are placed alternately in the same direction, on the one
hand, and the linear passage extending in the perpendicular direction to the above-mentioned
direction includes expanded areas and throat areas that are placed alternately in
the same perpendicular direction, in the similar manner. Using the thus assembled
plates so that the flowing direction of the heat exchange fluid coincides with the
linear passage or is perpendicular thereto can impart substantially the same behavior
to the heat exchange fluid, irrespective the flowing system of the heat exchange fluid,
i.e., any one of the parallel flowing system, the counter-flowing system and the cross
flowing system. As a result, it is possible to perform a smooth heat transfer at a
low pressure loss to make an effective heat exchange, even when the heat exchange
fluids are combined in any manner in their flowing directions, thus providing a high
degree of freedom in design of the heat exchanger and becoming excellent in general
purpose use. In addition, the heat exchange fluid ca flow freely in the above-mentioned
two directions along the plate, and the constant heat transfer property can be obtained,
irrespective of the flowing direction of the heat exchange fluid. It is therefore
possible to cause the heat exchange fluid to spread over the entire area of the plate
so that such an entire area can serve as an effective heat transfer section, thus
increasing remarkably an amount of heat transfer per area and achieving a high performance.
Further, the strength of the assembled plates can be improved remarkably by bringing
the protrusions of the plate into contact with the corresponding protrusions of the
other plate, and it is therefore possible to keep the distance between the adjacent
two plates constant, even when there exists a large difference in pressure between
the heat exchange fluids, thus enhancing a pressure-resistant property.
[0014] In order to attain the aforementioned object, a heat exchange unit of the fourth
aspect of the present invention comprises a first set of plates for heat exchange
according to any one of the above-mentioned first to third aspects of the present
invention, the plate member of each of said plates having a shape of any one of a
rectangle and a square with side edges, along which the ridgelines of the main protrusions
or the protrusions extend in parallel with or perpendicular to the side edges of the
plate member, thus providing the predetermined pattern of irregularity; and a second
set of plates having a different predetermined pattern of irregularity, said different
predetermined pattern of irregularity being substantially same as said predetermined
pattern of irregularity of said first set of plates, but turning at an angle of about
45 degrees relative thereto, said first set of plates and said second set of plates
being assembled in variation in combination into a unit.
[0015] According to the fourth aspect of the present invention, two kinds of plates, i.e.,
the first set of plates and the second set of plates having the ridgelines extending
in the different direction from the extending direction of the ridgelines of the first
set of plates are assembled in an appropriate combination into a unit, so as to provide
combined properties of the different heat exchange properties of the two kinds of
plates, for a general structure of the unit. It is therefore possible to adjust the
heat exchange properties for the general structure of the unit by combining the two
kinds of plates in a different manner, thus providing relatively easily the desired
heat exchange properties. Consequently, there can be provided a heat exchanger, which
has optimum properties and an excellent heat exchange efficiency in accordance with
a kind, state and amount of the heat exchange fluid, as well as an actual use of the
heat exchanger.
BRIEF DESCRIPTION OF THE DRAWINGS
[0016]
FIG. 1 is a schematic structural view of a heat exchange plate according to the first
embodiment of the present invention;
FIG. 2 is an enlarged plan view of an essential structure of the heat exchange plate
according to the first embodiment of the present invention;
FIG. 3(A) is a cross-sectional view cut along the line A-A in FIG. 2, FIG. 3(B) is
a cross-sectional view cut along the line B-B in FIG. 2 and FIG. 3(C) is a cross-sectional
view cut along the line C-C in FIG. 2;
FIG. 4(A) is a cross-sectional view cut along the line D-D in FIG. 2 and FIG. 4(B)
is a cross-sectional view cut along the line E-E in FIG. 2;
FIGS. 5(A) and 5(B) are descriptive views illustrating gaps formed between a pair
of combined heat exchange plates according to the first embodiment of the present
invention and the other gaps formed between the other pair of combined heat exchange
plates according to the first embodiment of the present invention;
FIG. 6 is a schematic structural view of a heat exchange plate according to the second
embodiment of the present invention;
FIG. 7 is a descriptive view illustrating a flow of a heat exchange fluid in the combined
heat exchange plates according to the second embodiment of the present invention;
FIG. 8 is an enlarged plan view of an essential structure of the heat exchange plate
according to the other embodiment of the present invention;
FIG. 9(A) is a cross-sectional view cut along the line F-F in FIG. 8 and FIG. 9(B)
is a cross-sectional view cut along the line G-G in FIG. 8;
FIG. 10(A) is a cross-sectional view cut along the line H-H in FIG. 8, FIG. 10(B)
is a cross-sectional view cut along the line I-I in FIG. 8 and FIG. 10(C) is a descriptive
view illustrating a state in which the heat exchange plates according to the other
embodiment of the present invention are combined with each other; and
FIG. 11 is a schematic structural view of a heat exchange unit according to the third
embodiment of the present invention.
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS
[First Embodiment of the Present Invention]
[0017] Now, the first embodiment of the present invention will be described in detail below
with reference to FIGS. 1 to 5(B). FIG. 1 is a schematic structural view of a heat
exchange plate according to the first embodiment of the present invention. FIG. 2
is an enlarged plan view of an essential structure of the heat exchange plate according
to the first embodiment of the present invention. FIG. 3(A) is a cross-sectional view
cut along the line A-A in FIG. 2, FIG. 3(B) is a cross-sectional view cut along the
line B-B in FIG. 2 and FIG. 3(C) is a cross-sectional view cut along the line C-C
in FIG. 2. FIG. 4(A) is a cross-sectional view cut along the line D-D in FIG. 2 and
FIG. 4(B) is a cross-sectional view cut along the line E-E in FIG. 2. FIGS. 5(A) and
5(B) are descriptive views illustrating gaps formed between a pair of combined heat
exchange plates according to the first embodiment of the present invention and the
other gaps formed between the other pair of combined heat exchange plates according
to the first embodiment of the present invention.
[0018] As shown in FIGS.1 to 5(B), the heat exchange plate 1 according to the first embodiment
of the present invention includes a metallic plate member having a rectangular shape.
The plate member, which has a pattern of irregularity formed through a press forming,
includes a plurality of main protrusions 2 formed on one surface of the plate member
and a plurality of intermediate protrusions 3 formed between adjacent two main protrusions
2 on the plate member. Each of the main protrusions 2 has a shape of a quadrangular
pyramid with a top, the first pair of opposite side surfaces and the second pair of
opposite side surfaces. The first pair of opposite side surfaces faces each other
in the first direction. The second pair of opposite side surfaces faces each other
in the second direction perpendicular to the first direction. The main protrusions
are aligned in the first direction and the second direction by a predetermined distance
so that the first pair of opposite surfaces and the second pair of opposite surfaces
of one of the main protrusions face corresponding opposite surfaces of adjacent protrusions.
Each of the intermediate protrusions 3 has opposite foot portions 3a and a head ridge
3b placed between the foot portions 3a. Each of the foot portions 3a is placed in
a lowermost position at which ridgelines 2b of the adjacent two main protrusions 2b
intersect each other. The head ridge 3b is placed in a level that is higher than the
foot portions 3a and lower than the top 2a of each main protrusion 2, so as to provide
a bent roof shape. The main protrusions 2 and the intermediate protrusions 3 form
the predetermined pattern of irregularity.
[0019] The above-mentioned heat exchange plate 1 has a structure in which the direction
along which any one of the ridgelines 2b of the main protrusion 2 having the quadrangular
pyramid extends, intersects any one of the sides of the plate having the rectangular
shape at an angle of 45 degrees. The present invention is not limited only to such
a structure, but the direction along which the ridgeline 2b of the main protrusion
2 may intersect the side of the plate at a desired angle to provide a desired pattern
of irregularity.
[0020] The above-mentioned heat exchange plate 1 is combined with the other plate having
the same structure so that these plates face each other at the same side and the tops
2a of the main protrusions 2 of the plate 1 come into contact with the corresponding
tops 2a of the main protrusions 2 of the other plate, or so that these plates face
each other at the same other side and projections between the adjacent two intermediate
protrusions 3 of the plate come into contact with corresponding projections of the
other plate. Such a combination forms a gap 4, in which a heat exchange fluid can
flow, between the adjacent two plates 1, excepting contacting portions thereof, thus
providing a heat exchanger in which a heat exchange can be made between the heat exchange
fluid coming into contact with the upper surface of the plate 1 and the other heat
exchange fluid coming into contact with the lower surface of the plate 1.
[0021] When the plates are combined with each other as described above, the main protrusions
2 and the intermediate protrusions 3 project in the gap, the intermediate protrusions
3 of the plate 1, which have the lower height than the main protrusions 2, face the
corresponding intermediate protrusions 3 of the other plate 1 so as to apart from
each other by a predetermined distance, and the foot portions 3a of the plate 1, which
are placed the lowest level, face the corresponding foot portions 3a of the other
plate 1 so as to apart from each other by a predetermined larger distance. Areas formed
between the intermediate protrusions 3 and areas formed between the foot portions
3a alternately communicate with each other to form linear passages in a reticulation
shape. In such linear passages, the areas between the foot portions 3a provide orifices,
which are larger than orifices provided by the areas between the intermediate protrusions
3, with the result that the respective passage includes expansion zones and reduction
zones, which are repeated alternately, to extend linearly, and intersects the other
passages so as to communicate therewith (see FIG. 5(A)).
[0022] On the opposite side to the projecting direction of the protrusions 2, 3 of the plate,
spatial areas are provided between the opposing intermediate protrusions 3, which
are the smaller height than the main protrusions 2, so as to communicate the adjacent
areas formed between the opposing main protrusions 3 with each other, thus forming
linear passages. In such linear passages, the areas between the main protrusions 3
provide orifices, which are larger than orifices provided by the areas between the
intermediate protrusions 3, with the result that the respective passage includes expansion
zones and reduction zones, which are repeated alternately, to extend linearly in the
alignment direction of the main protrusions 2, and intersects the other passages so
as to communicate therewith (see FIG. 5(B)).
[0023] Now, description will be given below of operation of the heat exchanger to which
the heat exchange plates according to the first embodiment of the present invention
are applied. In the assembled state in which the heat exchange plates 1 are combined
in parallel with each other, a heat exchange fluid is introduced into and discharged
from the gap 4 in which the respective protrusions 2, 3 project, while the other heat
exchange fluid is introduced through the gap 5, which is placed on the opposite side
to the projecting side of the protrusions 2, 3, through the heat exchange plate 1
separating the gap 5 from the gap 4, so as to make heat exchange between the two kinds
of heat exchange fluids.
[0024] The gaps 4, 5, which are formed between the plates, extend linearly in the aligning
directions of the protrusions 2, 3 in correspondence with the respective shapes of
the protrusions 2, 3. Even when the two kinds of heat exchange fluids are introduced
into the gaps 4, 5, respectively, in accordance with any one of the flowing systems
of the parallel flowing system, the counter-flowing system and the cross flowing system,
the heat exchange fluids can be subjected to substantially the same conditions. Accordingly,
it is possible to cause the heat exchange fluids to pass smoothly through the gaps
4, 5, respectively, to make an effective heat exchange. In addition, the heat exchange
fluids pass through the passages having the specific shape in which expanded areas
and throat areas are placed alternately to make an effective heat exchange relative
to the plates, thus improving the heat exchange efficiency between the fluids and
eliminating pressure loss in the passages.
[0025] Further, the strength of the assembled plates can be improved remarkably by bringing
the protrusions of the plate into contact with the corresponding protrusions of the
other plate, and it is therefore possible to keep the distance between the adjacent
two plates constant, thus coping with a case where there exists a large difference
in pressure between the heat exchange fluids.
[0026] According to the heat exchange plate according to the first embodiment of the present
invention, the heat exchange plate 1 is formed of the metallic rectangular plate member
having the pattern of irregularity that includes the main protrusions 2 and the intermediate
protrusions 3 provided on the plate member. Combining such a heat exchange plate 1
with the other heat exchange plates so that these plates face each other at the same
side and the tops 2a of the main protrusions 2 of the plate come into contact with
the corresponding tops of the main protrusions of the other plate, or so that these
plates face each other at the same other side and projections between the adjacent
two intermediate protrusions of the plate come into contact with corresponding projections
of the other plate, provides a gap 4 between the adjacent two plates. A further additional
plate is combined with one of these plates in the same manner to provide the other
gap 5 between them. Each of the above-mentioned gaps 4, 5 has a dimension corresponding
to the pattern of irregularity of the plates, in which a unit of the similar pattern
of irregularity is repeated in two directions that are perpendicular to each other,
thus providing linear passages extending in the above-mentioned two directions so
as to cross each other at right angles. More specifically, each of the linear passages
extending in the direction includes expanded areas and throat areas that are placed
alternately in the same direction, on the one hand, and the linear passage extending
in the perpendicular direction to the above-mentioned direction includes expanded
areas and throat areas that are placed alternately in the same perpendicular direction,
in the similar manner. Using the thus assembled plates can impart substantially the
same behavior to the heat exchange fluid, irrespective the flowing system of the heat
exchange fluid, i.e., any one of the parallel flowing system, the counter-flowing
system and the cross flowing system. As a result, it is possible to perform a smooth
heat transfer at a low pressure loss to make an effective heat exchange, even when
the heat exchange fluids are combined in any manner in their flowing directions, thus
providing a high degree of freedom in design of the heat exchanger and becoming excellent
in general purpose use.
[0027] The present invention is not limited only to the above-described first embodiment
of the present invention in which the heat exchange plates are connected directly
to each other by welding, to constitute the heat exchanger. The present invention
may be applied to the conventional plate-type heat exchanger in which the plates are
assembled into a unit in a state that gasket members formed of elastic material are
placed between the plates.
[Second Embodiment of the Present Invention]
[0028] Now, the second embodiment of the present invention will be described in detail below
with reference to FIGS. 6 and 7. FIG. 6 is a schematic structural view of a heat exchange
plate according to the second embodiment of the present invention. FIG. 7 is a descriptive
view illustrating a flow of a heat exchange fluid in the combined heat exchange plates
according to the second embodiment of the present invention.
[0029] As shown in FIGS. 6 and 7, the heat exchange plate 10 according to the second embodiment
of the present invention has the pattern of irregularities with the main protrusions
11 and the intermediate protrusions 12 in the same manner as the above-described first
embodiment of the present invention. However, the heat exchange plate 10 according
to the second embodiment differs from the first embodiment in that the ridgelines
14 of the main protrusions 11 extend in parallel with or perpendicular to the side
edges of the heat exchange plate 10.
[0030] Concerning the pattern of irregularities of the heat exchange plate, the main protrusions
11 and the intermediate protrusions 12 project in the gap, the intermediate protrusions
12 of the plate, which have the lower height than the main protrusions 11, face the
corresponding intermediate protrusions 12 of the other plate 1 so as to apart from
each other by a predetermined distance, and the foot portions 15 of the plate, which
are placed the lowest level, face the corresponding foot portions 15 of the other
plate so as to apart from each other by a predetermined larger distance, in the same
manner as the above-described first embodiment of the present invention.
[0031] Now, description will be given below of behavior of the heat exchange fluids flowing
on the respective surfaces of the heat exchange plate according to the second embodiment
of the present invention. In a state in which the heat exchange plates 10 are assembled
into a unit so as to be placed in parallel with each other, the different kinds of
heat exchange fluids flows on the opposite surfaces of the heat exchange plate 10,
respectively, so as to provide the counter-flowing system in the same manner as the
first embodiment of the present invention. However, on the side of the upper surface
of the plate, from which the protrusions 11, 12 project, fluid passages are provided
to extend obliquely in two directions along which the main protrusions 11 and the
intermediate protrusions 12 are aligned alternately. In each of the fluid passages,
the intermediate protrusions 12 having the intermediate height and the foot portions
15 having the lowest level are repeated alternately. The heat exchange fluid flows
downward in the above-mentioned fluid passages (as shown in FIG. 7 by hollow arrows
in solid lines). On the side of the lower surface of the plate, which is opposite
to the projecting direction of the protrusions 11, 12, other fluid passages extending
obliquely are provided by recess portions, which are formed directly below the main
protrusions 11, and other recess portions, which are formed directly below the intermediate
protrusions 12, in combination. The other heat exchange fluid flows upward in these
fluid passages (as shown in FIG. 7 by hollow arrows in dotted lines. Each of the heat
exchange fluids flows obliquely, while repeating divergence and confluence, to spread
smoothly over every area of the heat exchange plate 10. As a result, an effective
heat transfer can be made between the different kinds of heat exchange fluids through
the heat exchange plates 10.
[0032] According to the heat exchange plate according to the second aspect of the present
invention, the plate member has the pattern of irregularity in which the ridgelines
of the main protrusions 11 extend in parallel with or perpendicular to the side edges
of the plate 10. Placing the plates 10 having such a pattern of irregularity so that
the side edge of the plate coincides with the horizontal direction or vertical direction
provides areas between the intermediate protrusions 12 and the foot portions 15, each
of which areas extends obliquely relative to the horizontal or vertical direction.
As a result, the heat exchange fluids introduced into the combined plates flows in
the oblique direction, and repeats divergence and confluence to spread over every
area of the plate 10. It is therefore possible to cause the heat exchange fluid to
spread over the entire area of the heat exchange plate 10 to facilitate the heat transfer
between the heat exchange fluids and improving the heat exchange rate.
[0033] The heat exchange plate according to the first and second embodiments of the present
invention has a structure in which there is used the pattern of irregularities having
the combination of the main protrusions 2, 11, which have the quadrangular pyramid,
and the intermediate protrusions 3, 12, which have the bent roof shape having the
lower height than the main protrusions 2, 11. The present invention is not limited
only to such a structure, but there may be adopted a structure as shown in FIGS. 8
to 10(C), in which the pattern of irregularities is formed by a plurality of protrusions
6 and a plurality of recess portions 7. The protrusions 6, each of which projects
in the form of a quadrangular pyramid or a quadrangular truncated pyramid having four
ridgelines, are aligned in the two directions, which are perpendicular to each other,
so that the protrusions 6 are apart from each other by a predetermined distance and
the ridgelines of the protrusions 6 are placed on straight lines corresponding to
the above-mentioned two directions. Each of the recess portions 7 is formed, in the
form of a quadrangular pyramid or a quadrangular truncated pyramid, between four protrusions
so as to be surrounded by the four protrusions 6. Consequently, the plate is provided
on the opposite surfaces with the patterns of irregularities having the inverse projection
relationship, in which the plate is provided, on respective areas of its upper surface,
with the protrusions 6, and on the corresponding areas of its lower surface, with
the recess portions 7. When the heat exchange plate is combined with the other plate
having the same structure so that the protrusions 6 of the former come into contact
with the protrusions of the latter, the ridgelines 6a of the protrusions of the plate
face those of the corresponding protrusions of the other plate by a predetermined
distance, and the recess portions 7 of the plate face the corresponding portions of
the other plate by a predetermined distance within the gap 8. Spaces formed between
the adjacent protrusions 6 communicate alternatively with spaces defined by the recess
portions 7 to form linear passages. Accordingly, each of the linear passages extending
in the direction includes expanded areas and throat areas that are placed alternately
in the same direction, on the one hand, and the linear passage extending in the perpendicular
direction to the above-mentioned direction includes expanded areas and throat areas
that are placed alternately in the same perpendicular direction, in the similar manner
(see FIG. 10(c)). Even when the two kinds of heat exchange fluids are introduced into
the gaps 8, respectively, in accordance with any one of the flowing systems of the
parallel flowing system, the counter-flowing system and the cross flowing system,
the heat exchange fluids can be subjected to substantially the same conditions in
the same manner as the first embodiment of the present invention. Accordingly, it
is possible to cause the heat exchange fluids to pass smoothly through the gaps 8,
respectively, to make an effective heat exchange.
[0034] In the heat exchange plate according to the first and second embodiments of the present
invention, there is no limitations in the introducing and discharging directions of
the two kinds of heat exchange fluids, which flow on the opposite surfaces of the
heat exchange plate, respectively, to make heat exchange between these fluids, and
in the flowing system for them. These limitations may be given in accordance with
the use of the heat exchanger. More specifically, there may be adopted a structure
in which inlet and outlet for the first fluid are provided on the opposite edges of
the heat exchange plate in its longitudinal direction, respectively, inlet and outlet
for the second fluid are provided on the opposite edges of the heat exchange plate
in its transverse direction, respectively, and the first fluid flows in the longitudinal
direction and the second fluid flows in the transverse direction in accordance with
the cross flowing system. Alternatively, there may be adopted a structure in which
inlet and outlet for the first fluid are provided on the opposite edges of the longitudinal
side of the heat exchange plate, respectively, inlet and outlet for the second fluid
are provided on the opposite edges of the remaining longitudinal side of the heat
exchange plate, respectively, and the first fluid flows in the longitudinal direction
and the second fluid flows in the longitudinal direction in accordance with the parallel
flowing system or the counter-flowing system. Further, there may be adopted a structure
in which inlet and outlet for the first fluid are provided on the opposite edges of
the longitudinal side of the heat exchange plate, respectively, inlet and outlet for
the second fluid are provided on the same opposite edges, respectively, and the first
fluid flows in the longitudinal direction and the second fluid flows in the opposite
longitudinal direction in accordance with the counter-flowing system.
[Third Embodiment of the Present Invention]
[0035] Now, the third embodiment of the present invention will be described in detail below
with reference to FIG. 11. The third embodiment describes a heat exchange unit into
which the above-described heat exchange plates of the present invention are assembled
so as to be placed in parallel with each other. FIG. 11 is a schematic structural
view of the heat exchange unit according to the third embodiment of the present invention.
[0036] As shown in FIG. 11, the heat exchange unit 50 has a structure in which a predetermined
number of the first heat exchange plates according to the first embodiment and a predetermined
number of the second heat exchange plates according to the second embodiment are combined
with each other. More specifically, the first heat exchange plates each having the
pattern of irregularities in which the ridgelines 2b of the main protrusions 2 intersects
any one of the sides of the plate having the rectangular shape at an angle of 45 degrees,
and the second heat exchange plates each having the pattern of irregularities in which
the ridgelines 14 of the main protrusions 11 are in parallel with or perpendicular
to any one of the sides of the plate having the rectangular shape are assembled in
the unit in an appropriate combination.
[0037] The heat exchange plates used in the heat exchange unit 50 are classified into the
first group of the heat exchange plates 1, which have the same pattern of irregularities
and are placed one upon another, and the second group of the heat exchange plates
10, which have the pattern of irregularities that are the same as each other but different
from the first series of the heat exchange plates 1, and are placed one upon another
in the same manner. Using the two groups of the heat exchange plates having the different
heat exchanging properties due to the different pattern of irregularities, so as to
be placed in parallel with each other provides an intermediate property between the
first property according to the unit in which only the first group of heat exchange
plates is utilized and the second property according to the unit in which only the
second group of heat exchange plates is utilized. When such a unit is applied to the
heat exchange fluids, which are suitable to such an intermediate property, heat exchange
can be made in an appropriate manner, thus improving the heat exchange efficiency.
[0038] According to the heat exchange unit according to the third embodiment of the present
invention, two kinds of plates, i.e., the first set of plates 1 and the second set
of plates 10 having the ridgelines extending in the different direction from the extending
direction of the ridgelines of the first set of plates are assembled in an appropriate
combination into a unit, so as to provide combined properties of the different heat
exchange properties of the two kinds of plates. It is therefore possible to provide
the heat exchanger having the effective heat exchanging properties as desired, which
cannot be obtained by combination of the single kind of plates.
[0039] In the heat exchange unit according to third embodiment of the present invention,
the two kinds of heat exchange plates 1, 10 are assembled into the unit so that the
first group of plates having the same pattern of irregularities and the second group
of plates having the same pattern of irregularities are combined in parallel with
each other. The present invention is not limited only to such a structure. A plurality
of kinds of plates having the different pattern of irregularities, for example, two
kinds of plates, i.e., the heat exchange plates 1 having the pattern of irregularities
as shown in FIG. 1 and the heat exchange plates 10 having the pattern of irregularities
as shown in FIG. 6 may be placed alternately one upon another. Alternatively, there
may be placed, between a plurality of groups of plate having the same pattern of irregularities,
one or more plate having the different pattern of irregularities. Combination of the
plates can be varied strictly in number of the plates in the respective group in this
manner. It is therefore possible to adjust appropriately the arrangement of the various
kinds of plates having the different heat exchanging properties due to the different
pattern of irregularities, to obtain a desired heat exchange properties for the general
structure of the unit, thus providing a heat exchanger, which has optimum properties
and an excellent heat exchange efficiency in accordance with a kind, state and amount
of the heat exchange fluid, as well as an actual use of the heat exchanger.