PLATE HEAT EXCHANGER AND HEAT PUMP APPARATUS
An upper heat transfer plate and a lower heat transfer plate adjacent to each other are corrugated in a wave pattern. Between these plates, intersection points are formed at intersections of a plurality of bottom edge lines representing bottoms of the wave pattern of the upper heat transfer plate, and the top edge lines representing tops of the wave pattern of the lower heat transfer plate. Each of the bottoms of the wave pattern represented by the bottom edge lines and each of the tops of the wave pattern represented by the top edge lines come into contact with each other at respective intersection points. The intersection point at an end closest to an outer periphery along the long side among the intersection points on one of the bottom edge lines is formed at a distance of 3 to 4.5 mm from the outer periphery along the long side.
This invention relates to a plate heat exchanger.
BACKGROUND ARTConventionally, there is a plate heat exchanger in which upper and lower plates are supported by providing a plurality of ridges on the plates in a longitudinal direction (for example, see Patent Document 1). There is also a plate heat exchanger in which upper and lower plates are joined at peaks of V-shaped wave portions of the respective plates (for example, see Patent Document 2).
CITATION LIST Patent LiteraturePatent Document 1: JP 10-103888 A
Patent Document 2: JP 2002-107074 A
DISCLOSURE OF INVENTION Technical ProblemConventionally, plate heat exchangers have the following problems. Firstly, when a flow rate is increased for enhancing heat transfer of a fluid, pressure loss is increased. Secondly, the increased pressure loss causes stagnation and clogging by dirt. Patent Document 1 provides a solution for solving these problems. However, the fluid is prompted to flow into flow paths formed by the ridges in a long axial direction, thereby being prevented from spreading in a short axial direction. There is also a general problem for plate heat exchangers. The problem is that when the peaks of V-shaped wave portions are joined between the upper and lower plates as discussed in Patent Document 2, ends of the wave portions are not aligned at an outer periphery, so that a brazing area at a joint portion between the upper and lower plates is enlarged, resulting in a narrower flow path and increased pressure loss.
It is an object of this invention to provide a plate heat exchanger that reduces pressure loss of a fluid and enhances heat exchange efficiency by a simple configuration.
Solution to ProblemA plate heat exchanger according to this invention is configured such that
a plurality of rectangular plates having a long side, a short side, and an outer periphery are stacked such that corresponding long sides, short sides, and outer peripheries are aligned, the outer peripheries defining a space in which a fluid is sealed;
each of the plates is corrugated in a wave pattern waving in a stacking direction;
the plates adjacent to each other have intersection points therebetween when seen in the stacking direction, the intersection points being formed at intersections of a plurality of virtual bottom edge lines and a plurality of virtual top edge lines, the bottom edge lines representing bottoms of the wave pattern of one of the plates adjacent to each other and extending in a direction different from a direction of the long side and the top edge lines representing tops of the wave pattern of another one of the plates adjacent to each other and extending in a direction different from the direction of the long side; and
each of the bottoms of the wave pattern represented by the bottom edge lines and each of the tops of the wave pattern represented by the top edge lines come into contact with each other at each of the intersection points, thereby forming a contact portion, and
the plate heat exchanger is characterized in that
the plates adjacent to each other are arranged such that the contact portion corresponding to one of the intersection points at an end closest to the outer periphery along the long side among the intersection points existing on one of the bottom edge lines is formed at a position at a predetermined distance in a direction of the short side from the outer periphery along the long side, depending on the direction in which the bottom edge lines extend and the direction in which the top edge lines extend; and
the contact portion corresponding to the one of the intersection points at the end closest to the outer periphery along the long side among the intersection points existing on the one of the bottom edge lines is formed at a distance of between 3 mm and 4.5 mm in a direction of the short side from the outer periphery along the long side when the direction of the bottom edge lines relative to the direction of the long side is between 60 degrees and 70 degrees.
Advantageous Effects of InventionAccording to a plate heat exchanger of this invention, pressure loss of a fluid can be reduced and heat exchange efficiency can be enhanced. Due to the reduced pressure loss and the enhanced heat efficiency, the size (capacity) of the plate heat exchanger can be reduced. The enhanced heat efficiency also reduces power consumption, so that CO2 emission can be reduced.
(1) In
(2) In
(3) In
(5) In
(6) In
(Description of Configuration)
As shown in
The joint point at the shortest distance in the short axial direction (direction Z) means the first joint point that is encountered when proceeding in the short axial direction from the outer periphery 2-3.
A more specific explanation will be provided. In
With the plate heat exchanger 100 of the first embodiment, the following effects can be obtained.
(1) Pressure loss: The plate heat exchanger 100 is effective in reducing the pressure loss of a fluid. The wave patterns are arranged such that the joint point of the upper and lower plates at the shortest distance in the short axial direction from the outer periphery along a long axial direction of the plates is positioned to substantially coincide with the outer periphery along the long axial direction. With this arrangement, the joint point of the upper and lower plates at the shortest distance in the short axial direction from the outer periphery is positioned closer to the outer periphery (the distance a is shortened). Thus, the accumulation of the brazing material at the outer periphery can be reduced and the flow path can be widened, thereby reducing the pressure loss.
(2) Efficiency: The effective heat transfer area is increased due to the enlarged flow path. As a result, the plate heat exchanger with enhanced heat exchange efficiency can be provided.
(3) Size reduction: When the heat transfer between the plates is enhanced and the pressure loss is reduced as described above, the plate heat exchanger can be configured with a reduced number of stacked plates. As a result, manufacturing costs such as material costs and processing costs can be substantially reduced.
(4) Reduction of CO2 emission: With an air conditioner incorporating this plate heat exchanger, not only costs but also power consumption and CO2 emission can be reduced. In addition, due to the reduced pressure loss, the accumulation of refrigeration oil, sludge, dirt, and so on can be prevented in the heat exchanger, thereby enhancing the reliability of the heat exchanger.
In the first embodiment, it has been described that in the plate heat exchanger configured by stacking a plurality of plates in which passage holes serving as fluid inlets and outlets are formed at four corners, the wave patterns are arranged such that the joint point of the upper and lower plates at the shortest distance in the short axial direction from the outer periphery along the long axial direction of the plates is positioned to substantially coincide with the outer periphery along the long axial direction.
Second EmbodimentIn the first embodiment, the interval between the outer periphery 2-3 of the plate and the joint point 11 of the upper and lower plates at the shortest distance in the short axial direction (direction Z) is minimized by arranging the end portion 9 at the valley of the wave pattern (an end of the bottom edge line) of the upper heat transfer plate 2 and the end portion 10 at the peak (an end of the top edge line) of the lower heat transfer plate 3 to coincide with each other. That is, the joint point 11 is positioned to substantially coincide with the outer periphery 2-3. With this arrangement, the pressure loss is reduced. In a second embodiment, it will be described that a specified interval (a specified distance b to be described later) is provided between the outer periphery along the long axial direction of the plates (the outer periphery along the long side) and the joint point of the upper and lower plates at the shortest distance in the short axial direction (direction Z).
In the following explanation, reference will again be made to
When the distance b between the outer periphery of the plates and the joint point 11 of the upper and lower plates at the shortest distance in the short axial direction (direction Z) is too short, that is, when the distance b is not as short as the distance a but is insufficiently short so that the effect of the distance a cannot be obtained, the following disadvantage is encountered. At the time of brazing, the brazing material at the outer periphery and the brazing material at the joint point converge and accumulate in the distance b, thereby narrowing the flow path. On the other hand, when the distance b is too long, the interval between the joint point 11 of the upper and lower plates and a joint point 13 next to the joint point 11 is shortened (the joint point 13 being the second closest to the outer periphery after the joint point 11 on the top edge line 22). As a result, the brazing material of the joint point 11 and the brazing material of the joint point 13 converge and accumulate between these points, thereby narrowing the flow path. In the plates of the second embodiment, the distance b is set to a predetermined length that will not cause the accumulation of the brazing material. With this arrangement, an area corresponding to the distance b also serves as the flow path of a fluid. With the plate heat exchanger thus configured, the pressure loss can be reduced while the heat transfer area can be enlarged.
For example, when the size of the plate in the short axial direction is 70 mm, the distance b should be 3 to 4.5 mm. The distance b may be adjusted depending on the size of the plate in the short axial direction, a wave angle θ, a wave pitch, properties of a fluid, and usage conditions. In
As described above, between the upper heat transfer plate 2 and the lower heat transfer plate 3, the joint point (contact portion) corresponding to the intersection point at the end closest to the outer periphery along the long side among the intersection points on one bottom edge line is formed at a position at a predetermined distance (3 to 4.5 mm) in a direction of the short side (direction Z) from the outer periphery along the long side, depending on a direction in which the bottom edge line extends (the direction of the bottom edge line determined by the wave angle θ1) and a direction in which the top edge line extends (the direction of the top edge line determined by the wave angle θ2).
Between the upper heat transfer plate 2 and the lower heat transfer plate 3, the closer the direction of the bottom edge line and the direction of the top edge line are to a direction perpendicular to the direction of the long side, the further away from the outer periphery along the long side the joint portion is formed. That is, the closer the wave angle θ1 and the wave angle θ2 are to 90 degrees, the wider than approximately “3 to 4.5 mm” the distance b should be.
In the second embodiment, it has been described that in the plate heat exchanger configured by stacking a plurality of plates in which passage holes serving as fluid inlets and outlets are formed at four corners, the joint point of the upper and lower plates at the shortest distance in the short axial direction from the outer periphery along the long axial direction of the plates is positioned at the predetermined distance b.
Third EmbodimentReferring to
By forming such a flow path c at the outer periphery, it is possible to avoid the narrowing of the flow path width due to the accumulation of the brazing material between the outer periphery and “the joint point of the upper and lower plates at the shortest distance in the short axial direction”. Further, the wave pattern is not shortened in one of the plates, so that the pressure loss can be reduced while the effect of facilitating heat transfer is maintained by agitating action caused by flow movement. Furthermore, when two or more types of fluid flow through the plates, the heat exchanger may be configured by arranging the plates such that a fluid with high pressure loss flows though the plates having the wave pattern with short edge lines and a fluid with low pressure loss flows through the plates having the wave pattern with long edge lines. In
In the third embodiment, it has been described that in the plate heat exchanger configured by stacking a plurality of plates in which passage holes serving as fluid inlets and outlets are formed at four corners, the edge lines of the wave pattern are shortened in either of the upper and lower plates.
Fourth EmbodimentReferring to
As discussed in the third and fourth embodiments, in at least either of the upper heat transfer plate 2 and the lower heat transfer plate 3 adjacent to each other, the area c or the area d where no wave pattern is formed is provided only to an extent of a predetermined width W (
In the fourth embodiment, it has been described that in the plate heat exchanger configured by stacking a plurality of plates in which passage holes serving as fluid inlets and outlets are formed at four corners, the flow path is formed by shortening the edge lines of the wave pattern in both of the upper and lower plates.
Fifth EmbodimentReferring to
Thus, in the fifth embodiment, in the upper heat transfer plate 2, for example, a plurality of the bottom edge lines are directed to the outer periphery 2-3 along the long side. Then, end portions of the plurality of the bottom edge lines corresponding to “the outer periphery 2-3 along the long side” are formed alternately at a position T and at a position S, the position T being immediately close to “the outer periphery 2-3 along the long side” and the position S being further away from the outer periphery 2-3 than the position T immediately close.
In the fifth embodiment, it has been described that in the plate heat exchanger configured by stacking a plurality of plates in which passage holes serving as fluid inlets and outlets are formed at four corners, the edge lines of alternate waves of the plates are shortened, the alternate waves being alternate in a direction in which the fluid flows.
Sixth EmbodimentReferring to
As described above, in the sixth embodiment, between the upper heat transfer plate 2 and the lower heat transfer plate 3 adjacent to each other, at the intersection point at the end closest to “the outer periphery along the long side” among the intersection points on one bottom edge line of the upper heat transfer plate 2, the gap is formed between the bottom of the wave pattern represented by the bottom edge line and the top of the wave pattern represented by the top edge line of the lower heat transfer plate 3. Then, at the intersection points other than the intersection point at the end, the bottoms of the wave pattern represented by the bottom edge lines are in contact with the tops of the wave pattern represented by the top edge lines.
In the sixth embodiment, it has been described that in the plate heat exchanger configured by stacking a plurality of plates in which passage holes serving as fluid inlets and outlets are formed at four corners, at the position corresponding to the joint point of the upper and lower plates at the shortest distance in the short axial direction from the outer periphery of the upper and lower plates, the gap of 0.2 mm or wider is provided between the bottom and the top of the wave patterns of the plates.
The heat transfer plates described in the first to sixth embodiments can be used in numerous industrial machines and home appliances, such as air conditioners, power generators, and heat sterilizers for foods. For example, in a heat pump apparatus in which a compressor, a radiator, an expansion mechanism, and an evaporator are connected by pipes, the heat transfer plates can be used in either or both of the radiator and the evaporator.
List of Reference Signs1: reinforcement side plate
2: upper heat transfer plate
2-1, 3-1: short sides
2-2, 3-2: long sides
2-3, 3-3: outer peripheries
3: lower heat transfer plate
4: reinforcement side plate
5: first fluid inlet pipe
6: second fluid inlet pipe
7: first fluid outlet pipe
8: second fluid outlet pipe
9: end point at the valley of the wave pattern of the upper heat transfer plate
10: end portion at the peak of the wave pattern of the lower heat transfer plate
11: joint portion of the upper and lower plates at the shortest distance in the short axial direction from the outer periphery
12: outer periphery of the plate
13: second joint point of the upper and lower plates in the short axial direction from the outer periphery
100: plate heat exchanger
Claims
1-9. (canceled)
10. A plate heat exchanger configured such that
- a plurality of rectangular plates having a long side, a short side, and an outer periphery are stacked such that corresponding long sides, short sides, and outer peripheries are aligned, the outer peripheries defining a space in which a fluid is sealed;
- each of the plates is corrugated in a wave pattern waving in a stacking direction;
- the plates adjacent to each other have intersection points therebetween when seen in the stacking direction, the intersection points being formed at intersections of a plurality of virtual bottom edge lines and a plurality of virtual top edge lines, the bottom edge lines representing bottoms of the wave pattern of one of the plates adjacent to each other and extending in a direction different from a direction of the long side and the top edge lines representing tops of the wave pattern of another one of the plates adjacent to each other and extending in a direction different from the direction of the long side; and
- each of the bottoms of the wave pattern represented by the bottom edge lines and each of the tops of the wave pattern represented by the top edge lines come into contact with each other at each of the intersection points, thereby forming a contact portion,
- wherein
- the plates adjacent to each other are arranged such that the contact portion corresponding to one of the intersection points at an end closest to the outer periphery along the long side among the intersection points existing on one of the bottom edge lines is formed at a position at a predetermined distance in a direction of the short side from the outer periphery along the long side, depending on the direction in which the bottom edge lines extend and the direction in which the top edge lines extend; and
- the contact portion corresponding to the one of the intersection points at the end closest to the outer periphery along the long side among the intersection points existing on the one of the bottom edge lines is formed at a distance of between 3 mm and 4.5 mm in a direction of the short side from the outer periphery along the long side when the direction of the bottom edge lines relative to the direction of the long side is between 60 degrees and 70 degrees.
11. The plate heat exchanger of claim 10, wherein
- the contact portion corresponding to the one of the intersection points at the end closest to the outer periphery along the long side among the intersection points existing on the one of the bottom edge lines is formed such that the direction of the top edge lines relative to the direction of the long side is between 60 degrees and 70 degrees.
12. The plate heat exchanger of claim 11, wherein
- the contact portion corresponding to the one of the intersection points at the end closest to the outer periphery along the long side among the intersection points existing on the one of the bottom edge lines is formed such that the direction of the bottom edge lines relative to the direction of the long side and the direction of the top edge lines relative to the direction of the long side are between 62.5 degrees and 67.5 degrees.
13. The plate heat exchanger of claim 10, wherein
- the plates adjacent to each other are arranged such that the closer the direction of the bottom edge lines and the direction of the top edge lines are to a direction perpendicular to the direction of the long side, the further away from the outer periphery along the long side the contact portion is formed.
14. The plate heat exchanger of claim 11, wherein
- the plates adjacent to each other are arranged such that the closer the direction of the bottom edge lines and the direction of the top edge lines are to a direction perpendicular to the direction of the long side, the further away from the outer periphery along the long side the contact portion is formed.
15. The plate heat exchanger of claim 12, wherein
- the plates adjacent to each other are arranged such that the closer the direction of the bottom edge lines and the direction of the top edge lines are to a direction perpendicular to the direction of the long side, the further away from the outer periphery along the long side the contact portion is formed.
16. A heat pump apparatus wherein a compressor, a first heat exchanger, an expansion mechanism, and a second heat exchanger are connected by pipes, the heat pump apparatus, comprising:
- the plate heat exchanger of claim 10, as at least either of the first heat exchanger and the second heat exchanger.
17. A heat pump apparatus wherein a compressor, a first heat exchanger, an expansion mechanism, and a second heat exchanger are connected by pipes, the heat pump apparatus, comprising:
- the plate heat exchanger of claim 11, as at least either of the first heat exchanger and the second heat exchanger.
18. A heat pump apparatus wherein a compressor, a first heat exchanger, an expansion mechanism, and a second heat exchanger are connected by pipes, the heat pump apparatus, comprising:
- the plate heat exchanger of claim 12, as at least either of the first heat exchanger and the second heat exchanger.
19. A heat pump apparatus wherein a compressor, a first heat exchanger, an expansion mechanism, and a second heat exchanger are connected by pipes, the heat pump apparatus, comprising:
- the plate heat exchanger of claim 13, as at least either of the first heat exchanger and the second heat exchanger.
20. A heat pump apparatus wherein a compressor, a first heat exchanger, an expansion mechanism, and a second heat exchanger are connected by pipes, the heat pump apparatus, comprising:
- the plate heat exchanger of claim 14, as at least either of the first heat exchanger and the second heat exchanger.
21. A heat pump apparatus wherein a compressor, a first heat exchanger, an expansion mechanism, and a second heat exchanger are connected by pipes, the heat pump apparatus, comprising:
- the plate heat exchanger of claim 15, as at least either of the first heat exchanger and the second heat exchanger.
Type: Application
Filed: Nov 12, 2010
Publication Date: Sep 13, 2012
Inventors: Daisuke Ito (Chiyoda-ku), Takehiro Hayashi (Chiyoda-ku)
Application Number: 13/510,633
International Classification: F28F 3/08 (20060101); F25B 1/00 (20060101);