US20050167089A1 - Multi-tube heat exchanger - Google Patents
Multi-tube heat exchanger Download PDFInfo
- Publication number
- US20050167089A1 US20050167089A1 US11/048,896 US4889605A US2005167089A1 US 20050167089 A1 US20050167089 A1 US 20050167089A1 US 4889605 A US4889605 A US 4889605A US 2005167089 A1 US2005167089 A1 US 2005167089A1
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- Prior art keywords
- tubes
- tube
- fluid
- peripheral face
- heat exchanging
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Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/24—Arrangements for promoting turbulent flow of heat-exchange media, e.g. by plates
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D7/00—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall
- F28D7/16—Heat-exchange apparatus having stationary tubular conduit assemblies for both heat-exchange media, the media being in contact with different sides of a conduit wall the conduits being arranged in parallel spaced relation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F9/00—Casings; Header boxes; Auxiliary supports for elements; Auxiliary members within casings
- F28F9/22—Arrangements for directing heat-exchange media into successive compartments, e.g. arrangements of guide plates
Definitions
- the present invention relates to a multi-tube heat exchanger for saving energy in plants of various types, architectures and so on, or for conducting chemical reactions, and more particularly to a structure of a baffle plate which is employed in the multi-tube heat exchanger.
- a multi-tube heat exchanger As a type of heat exchanger structure, there has been known a multi-tube heat exchanger.
- This type of heat exchanger includes a number of tubes bundled into a tube bundle which are arranged inside an outer shell, and heat exchanging fluids having respectively different temperatures are supplied into the multi-tubes and inside the outer shell, thereby to conduct heat exchange between the heat exchanging fluids through walls of the multi-tubes.
- a baffle plate is provided at the right angle with respect to an axial direction of the tubes for the purpose of supporting the tube bundle, and at the same time, for the purpose of preventing drift of the heat exchanging fluid which flows inside the outer shell so as to change a state of flow thereby to enhance heat exchanging efficiency.
- the baffle plate is provided with through holes corresponding to an outer shape of the tubes so that the multi-tubes may be passed therethrough (For example, Japanese Patent Publication No. JP-A-05-106993 and Japanese Patent Publication No. JP-A-06-185891).
- FIGS. 3A and 3B show a baffle plate 30 which is provided with a number of through holes 31 through which tubes 40 are adapted to pass, and additionally provided with small pass holes 32 around the through holes 31 .
- metal plates 35 in a strip shape are assembled like a latticework, as shown in FIGS. 4A and 4B , by alternately engaging slits formed therein with each other or by welding.
- the tubes 40 are passed through the latticework to be supported, and the heat exchanging fluid is supplied through gaps 41 around the tubes 40 .
- waves are formed in the metal plates in correspondence with the outer shape of the tubes.
- the invention has been made in view of the above described circumstances as the background, and it is an object of the invention to provide a multi-tube heat exchanger in which tubes can be stably fixed with sufficient stability in strength and dimension, and at the same time, a flow of heat exchanging fluid can be favorably made, whereby fluid resistance can be decreased without lowering heat exchanging efficiency.
- a multi-tube heat exchanger comprising a bundle of tubes which form fluid passages of first heat exchanging fluid, an outer shell which covers the bundle of tubes and form a fluid passage of second heat exchanging fluid, and a baffle plate which is arranged inside the outer shell in a direction intersecting an axial direction of the bundle of tubes and provided with a plurality of through holes through which respective tubes of the bundle are passed, characterized in that a part or all of the through holes have such a shape that a portion of an outer peripheral face of the tube comes into contact with a portion of an inner peripheral face of the through hole, and a gap for passing the second heat exchanging fluid is formed between the other portion of the inner peripheral face and the outer peripheral face of the tube.
- the through hole has a shape symmetrical with respect to a point. In this manner, support of the tubes and a flow of the heat exchanging fluid can be made maintaining a good balance.
- the through hole has a substantially rhombic shape, wherein a pair of rounded opposed corner portions to be internally contacted with the outer peripheral face of the tube, and the other pair of opposed corner portions have a shape to be separated from the outer peripheral face of the tube.
- the outer peripheral face of the tube is internally contacted with a pair of the opposed corner portions respectively, whereby the tube can be stably held.
- the other pair of the opposed corner portions have the shape to be separated from the outer peripheral face of the tube, whereby the flow of the heat exchanging fluid can be ensured.
- the other pair of the opposed corner portions may be formed either in an angled shape or in a rounded shape. In case of forming them in a rounded shape, the above described gap can be reliably obtained, by making their curvature smaller than a curvature of the tube.
- the aforesaid through holes are regularly arranged, for example in a plurality, according to the arrangement of the tubes. Moreover, a plurality of the aforesaid baffle plates may be arranged in a spaced relation in an axial direction of the tubes.
- the through holes can be formed by piercing the baffle plate by laser work or mechanical work.
- a method of forming the through holes is not particularly limited, but it is possible to form the through holes by appropriate known means.
- the number of the tubes, manner of arranging the tubes and so on are not particularly limited, and it is possible to appropriately select the tubes out of straight tubes, U-shaped tubes, corrugated tubes, etc.
- the shape of the outer shell is not particularly limited, and an appropriate shape can be selected according to necessity, as far as its essential function is fulfilled.
- each the tube can be supported by a portion of the inner peripheral face of the through hole which is formed in the baffle plate, and therefore, the tube can be stably fixed with high positional accuracy.
- the gap is formed between the through hole and the outer peripheral face of the tube so that the heat exchanging fluid can pass it through, and the heat exchanging fluid can be smoothly passed. Further, contact between the heat exchanging fluid and the tube will not be interrupted by the through hole, but the heat exchanging fluid will be directly brought into contact with the tube while it passes the aforesaid gap. As the results, the heat exchanging efficiency will be further enhanced.
- the multi-tube heat exchanger according to the invention includes a bundle of tubes which form the fluid passages of the first heat exchanging fluid, the outer shell which covers the bundle of the tubes and form the fluid passage of the second heat exchanging fluid, and the baffle plate which is arranged inside the outer shell in a direction intersecting the axial direction of the bundle of the tubes and provided with a plurality of the through holes through which respective tubes of the bundle are passed, and a part or all of the through holes have such a shape that a portion of the outer peripheral face of the tube comes into contact with a portion of the inner peripheral face of the through hole, and the gap for passing the second heat exchanging fluid is formed between the other portion of the inner peripheral face and the outer peripheral face of the tube. Therefore, the multi-tube heat exchanger according to the invention has the following advantages;
- FIG. 1 is a sectional view showing an entirety of a heat exchanger in an embodiment of the invention
- FIGS. 2A and 2B show a part of a baffle plate in the same embodiment in an enlarged scale, in which FIG. 2A is a front view showing arrangement of through holes, and FIG. 2B is a perspective view showing a tube in a state passed through the through hole;
- FIGS. 3A and 3B show a baffle plate as one example of background art, in which FIG. 3A is front view showing arrangement of through holes, and FIG. 3B is a plan view showing tubes in a state passed through the through holes; and
- FIGS. 4A and 4B show metal plates assembled like a latticework as another example of the background art, in which FIG. 4A is a front view showing the latticework and arrangement of tubes, and FIG. 4B is a plan view showing the tubes in a state passed through the latticework.
- FIGS. 1 and 2 A and 2 B Now, an embodiment of the invention will be described referring to FIGS. 1 and 2 A and 2 B.
- An outer shell 1 mainly includes a body part 1 a in a cylindrical shape, and head parts 1 b , 1 c in a semicircular shape which are continued from both ends of the body part la.
- partition walls 2 b , 2 c for separating a space inside the body part 1 a from spaces inside the head parts 1 b , 1 c .
- the head parts 1 b , 1 c are respectively provided with fluid ports 3 b , 3 c which are open to the exterior and communicated with the spaces defined by the partition walls 2 b , 2 c .
- the body part 1 a is provided with fluid ports 4 a , 5 a which are open to the exterior and communicated with the spaces defined by the partition walls 2 b , 2 c.
- a number of tubes 6 bundled into a tube bundle are bridged between the partition walls 2 b , 2 c . Both ends of the tubes are respectively communicated with the spaces inside the head parts 1 b , 1 c which are defined by the partition walls 2 b , 2 c.
- baffle plates 7 , 7 for regularly disturbing a flow of the fluid are arranged in a spaced relation in an axial direction of the tubes 6 , and the fluid can move across the baffle plates 7 , 7 through openings (not shown) which are provided in a part thereof.
- Each of the baffle plates 7 , 7 is provided with through holes 8 , 8 in regular arrangement, through which the tubes 6 are adapted to pass.
- the though holes 8 are formed by piercing the baffle plate 7 by laser work or so, and has a substantially rhombic shape which is symmetrical with respect to a point, as shown in FIGS. 2A and 2B .
- Inner faces of a pair of opposed corner portions 8 a at a larger opening degree are in a rounded shape having a larger curvature than a curvature of an outer peripheral shape of the tube 6 .
- the other pair of opposed corner portions 8 b at a smaller opening degree are in a rounded shape having a smaller curvature than the curvature of the outer peripheral shape of the tube 6 .
- a distance between the pair of the opposed corner portions 8 a , 8 a which have the larger opening degree is substantially equal to an outer diameter of the tube 6 at the largest position, and slightly larger than the tube 6 .
- gaps between the opposed corner portions 8 b , 8 b and the outer wall of the tube 6 become gradually larger at both sides of the opposed corner portions 8 a , 8 a toward the opposed corner portions 8 b , 8 b , and thus, gaps 9 which will be the largest at the opposed corner portions 8 b , 8 b can be obtained.
- the multi-tube heat exchanger in the embodiment of the invention is constructed in the above described manner.
- a first heat exchanging fluid to be subjected to heat exchange (for example, cold water) is introduced from one of the fluid ports in the head parts 1 b , 1 c , for example the fluid port 3 b , into the head part 1 b . Then, the first heat exchanging fluid moves from the space inside the head part 1 b through the tubes 6 into the space inside the other head part 1 c , and discharged from the fluid port 3 c to the exterior.
- the second heat exchanging fluid (for example, hot water) is introduced from the fluid port 4 a into the space inside the body part 1 a .
- the second heat exchanging fluid moves while it is guided by surfaces of the baffle plates 7 and the openings which are not shown, and comes into contact with the outer walls of the tubes 6 thereby to conduct the heat exchange with the first heat exchanging fluid which flows inside the tubes 6 .
- a portion of the second heat exchanging fluid will pass the baffle plates 7 through the gaps 9 of the through holes 8 through which the tubes 6 are passed. Because the second fluid moves along the outer walls of the tubes 6 on this occasion, the heat exchange between the second fluid and the tubes 6 will be further promoted.
- the second fluid passes the baffle plates 7 through the gaps 9 , it is possible to decrease the fluid resistance of the second heat exchanging fluid, and a drop of flow rate of the second heat exchanging fluid can be prevented generally. As the results, heat exchanging efficiency by the second heat exchanging fluid will be improved.
- the tubes 6 can be reliably held by the through holes 8 with high stability and high dimensional accuracy, and therefore, regularity of arranging the tube bundle can be maintained even though pitch between the through holes are minimized. As the results, the heat exchanger can be made compact.
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- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Fluid Mechanics (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Details Of Heat-Exchange And Heat-Transfer (AREA)
Abstract
The multi-tube heat exchanger includes a bundle of tubes which form fluid passages of first heat exchanging fluid, an outer shell which covers the bundle of tubes and form a fluid passage of second heat exchanging fluid, and a baffle plate which is arranged inside the outer shell in a direction intersecting an axial direction of the bundle of tubes and provided with a plurality of through holes through which respective tubes of the bundle are passed. Each of the through holes has such a shape that a portion of an outer peripheral face of the tube comes into contact with a portion of an inner peripheral face of the through hole, and a gap for passing the second heat exchanging fluid is formed between the other portion of the inner peripheral face and the outer peripheral face of the tube. It is possible to support the tubes with high dimensional accuracy, and to enhance heat exchanging efficiency by decreasing fluid resistance. It is also possible to make pitch of the through holes smaller and to make the heat exchanger compact.
Description
- 1. Field of the Invention
- The present invention relates to a multi-tube heat exchanger for saving energy in plants of various types, architectures and so on, or for conducting chemical reactions, and more particularly to a structure of a baffle plate which is employed in the multi-tube heat exchanger.
- 2. Related Art
- As a type of heat exchanger structure, there has been known a multi-tube heat exchanger. This type of heat exchanger includes a number of tubes bundled into a tube bundle which are arranged inside an outer shell, and heat exchanging fluids having respectively different temperatures are supplied into the multi-tubes and inside the outer shell, thereby to conduct heat exchange between the heat exchanging fluids through walls of the multi-tubes. There have been known some types of this heat exchanger in which a baffle plate is provided at the right angle with respect to an axial direction of the tubes for the purpose of supporting the tube bundle, and at the same time, for the purpose of preventing drift of the heat exchanging fluid which flows inside the outer shell so as to change a state of flow thereby to enhance heat exchanging efficiency. The baffle plate is provided with through holes corresponding to an outer shape of the tubes so that the multi-tubes may be passed therethrough (For example, Japanese Patent Publication No. JP-A-05-106993 and Japanese Patent Publication No. JP-A-06-185891).
- It has been also proposed to provide the baffle plate with pass holes for passing the fluid, for the purpose of reducing fluid resistance while the heat exchanging fluid moves.
FIGS. 3A and 3B show abaffle plate 30 which is provided with a number of throughholes 31 through whichtubes 40 are adapted to pass, and additionally provided withsmall pass holes 32 around the throughholes 31. - Moreover, it has been proposed that instead of the above described baffle plate,
metal plates 35 in a strip shape are assembled like a latticework, as shown inFIGS. 4A and 4B , by alternately engaging slits formed therein with each other or by welding. Thetubes 40 are passed through the latticework to be supported, and the heat exchanging fluid is supplied throughgaps 41 around thetubes 40. Further, an improvement of this art in which waves are formed in the metal plates in correspondence with the outer shape of the tubes has been proposed. - However, in the heat exchanger in which the small pass holes are formed in the baffle plate, there has been a problem that the fluid cannot favorably pass through the small pass holes due to their insufficient opening rate, and a request for lowering the fluid resistance cannot be fully satisfied.
- Moreover, in the heat exchanger in which the metal plates are assembled like a latticework, although the fluid can relatively favorably flow, supporting strength for the tubes is insufficient, and therefore, it is necessary to employ the metal plates having a larger width (in the axial direction of the tube). As the results, there has been a problem that a heat transfer area between the heat exchanging fluid and outer walls of the tubes has been decreased. There has been another problem that because stability in strength and dimension is insufficient, it is difficult to fix positions of the holes, and consequently, arrangement of the tubes is liable to be confused. Specifically, in the conventional structure, it has been impossible to satisfy all the requirements such as compact arrangement of the tubes, dimensional stability, and the opening rate.
- The invention has been made in view of the above described circumstances as the background, and it is an object of the invention to provide a multi-tube heat exchanger in which tubes can be stably fixed with sufficient stability in strength and dimension, and at the same time, a flow of heat exchanging fluid can be favorably made, whereby fluid resistance can be decreased without lowering heat exchanging efficiency.
- Specifically, according to the invention, there is provided a multi-tube heat exchanger comprising a bundle of tubes which form fluid passages of first heat exchanging fluid, an outer shell which covers the bundle of tubes and form a fluid passage of second heat exchanging fluid, and a baffle plate which is arranged inside the outer shell in a direction intersecting an axial direction of the bundle of tubes and provided with a plurality of through holes through which respective tubes of the bundle are passed, characterized in that a part or all of the through holes have such a shape that a portion of an outer peripheral face of the tube comes into contact with a portion of an inner peripheral face of the through hole, and a gap for passing the second heat exchanging fluid is formed between the other portion of the inner peripheral face and the outer peripheral face of the tube.
- It is desirable that the through hole has a shape symmetrical with respect to a point. In this manner, support of the tubes and a flow of the heat exchanging fluid can be made maintaining a good balance.
- Moreover, it is further desirable that the through hole has a substantially rhombic shape, wherein a pair of rounded opposed corner portions to be internally contacted with the outer peripheral face of the tube, and the other pair of opposed corner portions have a shape to be separated from the outer peripheral face of the tube. As described above, the outer peripheral face of the tube is internally contacted with a pair of the opposed corner portions respectively, whereby the tube can be stably held. Moreover, the other pair of the opposed corner portions have the shape to be separated from the outer peripheral face of the tube, whereby the flow of the heat exchanging fluid can be ensured. Further, the other pair of the opposed corner portions may be formed either in an angled shape or in a rounded shape. In case of forming them in a rounded shape, the above described gap can be reliably obtained, by making their curvature smaller than a curvature of the tube.
- The aforesaid through holes are regularly arranged, for example in a plurality, according to the arrangement of the tubes. Moreover, a plurality of the aforesaid baffle plates may be arranged in a spaced relation in an axial direction of the tubes. The through holes can be formed by piercing the baffle plate by laser work or mechanical work. However, in this invention, a method of forming the through holes is not particularly limited, but it is possible to form the through holes by appropriate known means.
- Further, the number of the tubes, manner of arranging the tubes and so on are not particularly limited, and it is possible to appropriately select the tubes out of straight tubes, U-shaped tubes, corrugated tubes, etc. Also, the shape of the outer shell is not particularly limited, and an appropriate shape can be selected according to necessity, as far as its essential function is fulfilled.
- More specifically, according to the invention, each the tube can be supported by a portion of the inner peripheral face of the through hole which is formed in the baffle plate, and therefore, the tube can be stably fixed with high positional accuracy. Moreover, the gap is formed between the through hole and the outer peripheral face of the tube so that the heat exchanging fluid can pass it through, and the heat exchanging fluid can be smoothly passed. Further, contact between the heat exchanging fluid and the tube will not be interrupted by the through hole, but the heat exchanging fluid will be directly brought into contact with the tube while it passes the aforesaid gap. As the results, the heat exchanging efficiency will be further enhanced.
- As described herein above, the multi-tube heat exchanger according to the invention includes a bundle of tubes which form the fluid passages of the first heat exchanging fluid, the outer shell which covers the bundle of the tubes and form the fluid passage of the second heat exchanging fluid, and the baffle plate which is arranged inside the outer shell in a direction intersecting the axial direction of the bundle of the tubes and provided with a plurality of the through holes through which respective tubes of the bundle are passed, and a part or all of the through holes have such a shape that a portion of the outer peripheral face of the tube comes into contact with a portion of the inner peripheral face of the through hole, and the gap for passing the second heat exchanging fluid is formed between the other portion of the inner peripheral face and the outer peripheral face of the tube. Therefore, the multi-tube heat exchanger according to the invention has the following advantages;
-
- (1) Because of good dimensional accuracy, sufficient fixation of the tubes can be performed, and a sufficient wall thickness of the baffle plate can be selected, whereby the strength will be ensured.
- (2) Due to an increased opening area and decrease of the fluid resistance, a drop of flow rate of the heat exchanging fluid inside the outer shell can be prevented, whereby heat transfer efficiency will be improved.
- (3) Because pitch of the through holes can be minimized and the arrangement of the tube bundle can be made compact, an inner diameter of the outer shell can be made smaller, thus enabling production cost of the heat exchanger to be decreased.
-
FIG. 1 is a sectional view showing an entirety of a heat exchanger in an embodiment of the invention; -
FIGS. 2A and 2B show a part of a baffle plate in the same embodiment in an enlarged scale, in whichFIG. 2A is a front view showing arrangement of through holes, andFIG. 2B is a perspective view showing a tube in a state passed through the through hole; -
FIGS. 3A and 3B show a baffle plate as one example of background art, in whichFIG. 3A is front view showing arrangement of through holes, andFIG. 3B is a plan view showing tubes in a state passed through the through holes; and -
FIGS. 4A and 4B show metal plates assembled like a latticework as another example of the background art, in whichFIG. 4A is a front view showing the latticework and arrangement of tubes, andFIG. 4B is a plan view showing the tubes in a state passed through the latticework. - Now, an embodiment of the invention will be described referring to
FIGS. 1 and 2 A and 2B. - An
outer shell 1 mainly includes abody part 1 a in a cylindrical shape, andhead parts outer shell 1, there are providedpartition walls body part 1 a from spaces inside thehead parts head parts fluid ports partition walls body part 1 a is provided withfluid ports partition walls - Further, a number of
tubes 6 bundled into a tube bundle are bridged between thepartition walls head parts partition walls - In the space inside the
body part 1 a, a plurality ofbaffle plates tubes 6, and the fluid can move across thebaffle plates baffle plates holes tubes 6 are adapted to pass. The though holes 8 are formed by piercing thebaffle plate 7 by laser work or so, and has a substantially rhombic shape which is symmetrical with respect to a point, as shown inFIGS. 2A and 2B . Inner faces of a pair ofopposed corner portions 8 a at a larger opening degree are in a rounded shape having a larger curvature than a curvature of an outer peripheral shape of thetube 6. On the other hand, the other pair ofopposed corner portions 8 b at a smaller opening degree are in a rounded shape having a smaller curvature than the curvature of the outer peripheral shape of thetube 6. A distance between the pair of theopposed corner portions tube 6 at the largest position, and slightly larger than thetube 6. In case where the largest distance between theopposed corner portions tube 6, it will be difficult to insert thetube 6, and on the contrary, in case where the distance is too large, supporting performance for thetube 6 will be deteriorated. Therefore, the above described distance may be determined taking these factors into consideration. - In a state where the
tubes 6 are respectively passed through the throughholes 8, outer walls of thetubes 6 come into contact with theopposed corner portions tubes 6 will be supported. On this occasion, the distance between theopposed corner portions tube 6, and as the distance between theopposed corner portions tube 6 will be held in a stabilized position. On the other hand, gaps between theopposed corner portions tube 6 become gradually larger at both sides of theopposed corner portions opposed corner portions opposed corner portions - Then, operation of the above described multi-tube heat exchanger will be explained.
- A first heat exchanging fluid to be subjected to heat exchange (for example, cold water) is introduced from one of the fluid ports in the
head parts fluid port 3 b, into thehead part 1 b. Then, the first heat exchanging fluid moves from the space inside thehead part 1 b through thetubes 6 into the space inside theother head part 1 c, and discharged from thefluid port 3 c to the exterior. On the other hand, the second heat exchanging fluid (for example, hot water) is introduced from thefluid port 4 a into the space inside thebody part 1 a. Then, the second heat exchanging fluid moves while it is guided by surfaces of thebaffle plates 7 and the openings which are not shown, and comes into contact with the outer walls of thetubes 6 thereby to conduct the heat exchange with the first heat exchanging fluid which flows inside thetubes 6. A portion of the second heat exchanging fluid will pass thebaffle plates 7 through the gaps 9 of the throughholes 8 through which thetubes 6 are passed. Because the second fluid moves along the outer walls of thetubes 6 on this occasion, the heat exchange between the second fluid and thetubes 6 will be further promoted. - As described above, because the second fluid passes the
baffle plates 7 through the gaps 9, it is possible to decrease the fluid resistance of the second heat exchanging fluid, and a drop of flow rate of the second heat exchanging fluid can be prevented generally. As the results, heat exchanging efficiency by the second heat exchanging fluid will be improved. - Moreover, as described above, the
tubes 6 can be reliably held by the throughholes 8 with high stability and high dimensional accuracy, and therefore, regularity of arranging the tube bundle can be maintained even though pitch between the through holes are minimized. As the results, the heat exchanger can be made compact. - Although the invention has been described referring to the above described embodiment, the invention is not limited to the description of the embodiment. It is apparent that appropriate modifications can be made within a scope of the invention.
Claims (4)
1. A multi-tube heat exchanger comprising:
a plurality of tubes which form a first fluid passage of a first heat exchanging fluid,
an outer shell which covers said tubes and forms a second fluid passage of a second heat exchanging fluid, and
a baffle plate arranged inside said outer shell, intersecting an axial direction of said tubes and provided with a plurality of through holes through which said tubes are passed,
wherein at least one of said through holes has a shape such that a portion of an outer peripheral face of said tube is brought into contact with a portion of an inner peripheral face of the through hole, and a gap for passing said second heat exchanging fluid is formed between another portion of said inner peripheral face and the outer peripheral face of said tube.
2. A multi-tube heat exchanger according to claim 1 , wherein said through hole has a shape symmetrical with respect to a point.
3. A multi-tube heat exchanger according to claim 1 , wherein said through hole has a substantially rhombic shape which has a pair of rounded opposite corner portions to be internally contacted with the outer peripheral face of said tube, and another pair of opposed corner portions are separated from the outer peripheral face of said tube.
4. A multi-tube heat exchanger according to claim 1 , wherein a plurality of said through holes are regularly arranged.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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JPP2004-27861 | 2004-02-04 | ||
JP2004027861A JP2005221118A (en) | 2004-02-04 | 2004-02-04 | Shell-and-tube exchanger |
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US20050167089A1 true US20050167089A1 (en) | 2005-08-04 |
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Family Applications (1)
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US11/048,896 Abandoned US20050167089A1 (en) | 2004-02-04 | 2005-02-03 | Multi-tube heat exchanger |
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US (1) | US20050167089A1 (en) |
EP (1) | EP1562016A3 (en) |
JP (1) | JP2005221118A (en) |
KR (1) | KR100640301B1 (en) |
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CN104567519A (en) * | 2015-01-04 | 2015-04-29 | 沈阳化工大学 | Heat exchanger baffle plate capable of removing heat transfer dead area |
CN105716448A (en) * | 2016-04-06 | 2016-06-29 | 太原理工大学 | Shutter-shaped baffle plate fixed tube-sheet heat exchanger and machining and installing method |
CN106989631A (en) * | 2017-03-21 | 2017-07-28 | 茂名重力石化装备股份公司 | A kind of moon shape deflection plate and shell-and-tube heat exchanger |
CN108895864A (en) * | 2018-04-11 | 2018-11-27 | 南京师范大学 | Baffle plate component and shell-and-tube heat exchanger including this component |
CN110849180A (en) * | 2018-08-21 | 2020-02-28 | 洛阳超蓝节能技术有限公司 | Heat exchanger with non-circular cross section of heat exchange tube and heat exchange method thereof |
CN110849181A (en) * | 2018-08-21 | 2020-02-28 | 洛阳超蓝节能技术有限公司 | Gas-gas heat exchanger and heat exchange method thereof |
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Also Published As
Publication number | Publication date |
---|---|
JP2005221118A (en) | 2005-08-18 |
KR20050079222A (en) | 2005-08-09 |
KR100640301B1 (en) | 2006-10-31 |
EP1562016A3 (en) | 2010-09-15 |
EP1562016A2 (en) | 2005-08-10 |
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