JP2012042069A - Heat exchanger for waste heat recovery - Google Patents

Heat exchanger for waste heat recovery Download PDF

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JP2012042069A
JP2012042069A JP2010181679A JP2010181679A JP2012042069A JP 2012042069 A JP2012042069 A JP 2012042069A JP 2010181679 A JP2010181679 A JP 2010181679A JP 2010181679 A JP2010181679 A JP 2010181679A JP 2012042069 A JP2012042069 A JP 2012042069A
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combustion exhaust
heat exchanger
heat
flow path
corrugated plate
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Noboru Otomo
昇 大友
Takeshi Kashiwase
毅 柏瀬
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Atago Seisakusho Co Ltd
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Atago Seisakusho Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a heat exchanger for waste heat recovery prevented from retention of condensed water in the heat exchanger by collecting condensed water produced by lowering of temperature of combustion exhaust in a process of heat exchange and promptly leading the condensed water to the outside.SOLUTION: Both sides of a corrugated plate 10 formed in corrugated shape are held by side plates 20, 30 to form fluid flow passages partitioned by sidewalls 15 of the corrugated plate 10 so that water and combustion exhaust to be heat-exchanged alternately flow through the fluid flow passages in mutually reverse flow directions. Swelling sections are formed at both side ends of both side plates 20, 30 to form inlet headers 22, 32 at one end and to form outlet headers 23, 33 at the other end. The heat exchanger is installed so that the fluid flow passages extend along a vertical direction and that the outlet header 33 of combustion exhaust is located in a lower position. The bottom of the outlet header 33 of combustion exhaust is provided with a drain pipe 37 for leading the condensed water to the outside.

Description

この発明は、各種の熱関連装置やシステムにおいて、燃焼排気に含まれる潜熱を回収するための廃熱回収用熱交換器に関するものである。   The present invention relates to a waste heat recovery heat exchanger for recovering latent heat contained in combustion exhaust in various heat-related devices and systems.

各種の熱関連装置やシステムにおいて、燃焼排気をそのまま廃棄することなく、これに含まれる潜熱を回収する廃熱回収用熱交換器を設け、熱エネルギーの二次利用、熱効率の向上、燃焼排気の低温下等が図られている。従来、こうした廃熱回収用熱交換器として、プレートフィンアンドチューブタイプの熱交換器(特許文献1参照)やシェルアンドチューブタイプの熱交換器が用いられている。廃熱回収用熱交換器では、水と燃焼排気との間で熱交換が行われ、熱交換の過程で燃焼排気が低温下して結露による凝縮水を生じ、熱交換器の性能低下や故障の原因となっている。前者の場合、凝縮水の対応手段として、捕集タンクとして外部容器を別途設ける必要があり、装置の構造が複雑化する。後者の場合、構造は簡単であるが、伝熱面積が比較的小さいので熱効率に劣り、熱交換器自体が大型化する。   In various heat-related devices and systems, a waste heat recovery heat exchanger that recovers the latent heat contained in the exhaust gas is disposed without discarding the combustion exhaust as it is, and secondary use of heat energy, improvement of thermal efficiency, A low temperature etc. are aimed at. Conventionally, as such a heat exchanger for waste heat recovery, a plate fin and tube type heat exchanger (see Patent Document 1) and a shell and tube type heat exchanger have been used. In the heat exchanger for waste heat recovery, heat is exchanged between water and combustion exhaust, and during the heat exchange process, the combustion exhaust falls to a low temperature to produce condensed water due to condensation. Cause. In the former case, it is necessary to separately provide an external container as a collecting tank as a means for handling condensed water, which complicates the structure of the apparatus. In the latter case, the structure is simple, but since the heat transfer area is relatively small, the heat efficiency is inferior, and the heat exchanger itself is enlarged.

特許第3868644号公報Japanese Patent No. 3868644

この発明は、所定形状に形成した金属板で流体の流通路を形成する熱交換器であり、熱交換の過程で生じる凝縮水を捕集して速やかに外部に導出し、凝縮水が器内に滞留することがない廃熱回収用熱交換器を提案することを目的とするものである。また、小型、薄型に製作され、組立作業性、生産性に優れるとともに、熱交換する流体の圧力損失を低減し、熱効率に優れた廃熱回収用熱交換器を提案することを目的とするものである。   The present invention is a heat exchanger in which a fluid flow path is formed by a metal plate formed in a predetermined shape. Condensed water generated in the process of heat exchange is collected and quickly led out to the outside. The purpose of the present invention is to propose a heat exchanger for waste heat recovery that does not stay in the heat exchanger. In addition, the purpose is to propose a heat exchanger for waste heat recovery that is small and thin, has excellent assembly workability and productivity, reduces the pressure loss of the fluid that exchanges heat, and has excellent thermal efficiency. It is.

こうした目的を達成するため、この発明の廃熱回収用熱交換器は、波形成形したコルゲート板10の両側を側板20、30で挟持し、コルゲート板10の側壁15で区画された流体の流通路を形成し、熱交換する水と燃焼排気とが、その流通方向が逆方向で流体の流通路を交互に流通する。そして、両側板20、30の両側端部に膨出部を形成して一端に入口ヘッダー22、32、他端に出口ヘッダー23、33を形成し、流体の流通路が垂直方向に沿うととともに、燃焼排気の出口ヘッダー33が下位置となるように設置し、燃焼排気の出口ヘッダー33の底部に、熱交換の過程で燃焼排気が低温下して生じる凝縮水を外部に導出する排水管37を設けるものである。   In order to achieve such an object, the heat exchanger for waste heat recovery according to the present invention sandwiches both sides of the corrugated corrugated plate 10 with the side plates 20 and 30 and is a fluid flow path defined by the side walls 15 of the corrugated plate 10. The water for exchanging heat and the combustion exhaust gas alternately flow through the fluid flow passages with the flow directions being opposite to each other. And the bulging part is formed in the both-sides edge part of the both-sides plates 20 and 30, the inlet headers 22 and 32 are formed in one end, the outlet headers 23 and 33 are formed in the other end, and the fluid flow path is along the vertical direction The exhaust pipe 37 is installed so that the outlet header 33 of the combustion exhaust is at the lower position, and the condensed water generated by the combustion exhaust at a low temperature in the process of heat exchange is led to the bottom of the outlet header 33 of the combustion exhaust. Is provided.

また、燃焼排気の流通路の幅Aが水の流通路の幅Bより大きくなるようにコルゲート板10を形成するものである。   Further, the corrugated plate 10 is formed so that the width A of the flow path of combustion exhaust is larger than the width B of the flow path of water.

この発明の廃熱回収用熱交換器は、コルゲート板10の側壁15で区画された流体の流通路を、熱交換する水と燃焼排気とが、その流通方向が逆方向で交互に流通し、コルゲート板10の側壁15を介して両流体の熱交換が行われる。そして、流体の流通路が垂直方向に沿うととともに、燃焼排気の出口ヘッダー33が下位置となるように設置するので、熱交換の過程で燃焼排気が低温下して生じる凝縮水は出口ヘッダー33に捕集され、捕集された凝縮水を、出口ヘッダー33の底部に設けた排水管37から速やかに外部に導出することができる。したがって、凝縮水が器内に滞留することがなく、熱交換器の性能低下や故障の原因を取り除くことができる。   In the heat exchanger for waste heat recovery according to the present invention, water and combustion exhaust for heat exchange are alternately circulated in opposite directions in the flow direction of the fluid partitioned by the side wall 15 of the corrugated plate 10, Heat exchange between the two fluids is performed via the side wall 15 of the corrugated plate 10. And since the flow path of the fluid is along the vertical direction, and the outlet header 33 of the combustion exhaust is installed at the lower position, the condensed water produced when the combustion exhaust is lowered in the process of heat exchange becomes the outlet header 33. The condensed water collected and collected can be quickly led out from the drain pipe 37 provided at the bottom of the outlet header 33. Therefore, the condensed water does not stay in the vessel, and the cause of the performance deterioration or failure of the heat exchanger can be removed.

また、熱交換する燃焼排気と水が、極めて狭間隔の流通路を交互に流通し、流体の流通路が単純であるから、流体の圧力損失が大幅に低減されるとともに、伝熱面積の増大により熱効率に優れるものである。また、コルゲート板10を2枚の側板20、30で挟持して簡単に組み立てられ、コルゲート板10の折り返し面が側板20、30に当接するので接合性に優れ、組立作業性、生産性に優れ、製作コストが安価であるとともに、小型、薄型に製作され、設置の省スペース化が図られる。   In addition, combustion exhaust and water that exchange heat alternately flow through extremely narrow flow paths, and the fluid flow path is simple, so the pressure loss of the fluid is greatly reduced and the heat transfer area is increased. Therefore, it is excellent in thermal efficiency. Further, the corrugated plate 10 is easily assembled by sandwiching it between the two side plates 20 and 30, and since the folded surface of the corrugated plate 10 abuts the side plates 20 and 30, the bonding property is excellent, and the assembling workability and the productivity are excellent. The manufacturing cost is low, and the device is manufactured in a small size and a thin shape, so that the installation space can be saved.

また、燃焼排気の流通路の幅Aが水の流通路の幅Bより大きくなるようにコルゲート板10を形成することで、大流量の燃焼排気に対応し、効率的な熱交換の促進を図ることができる。   Further, by forming the corrugated plate 10 so that the width A of the flow path of the combustion exhaust is larger than the width B of the flow path of the water, it is possible to cope with a large flow of combustion exhaust and promote efficient heat exchange. be able to.

この発明の実施例の正面図。The front view of the Example of this invention. 側面図。Side view. 図2中A−A線で切断した拡大断面図。The expanded sectional view cut | disconnected by the AA line in FIG. コルゲート板の平面図。The top view of a corrugated board. コルゲート板の拡大断面図。The expanded sectional view of a corrugated board. コルゲート板の他の実施例の平面図。The top view of the other Example of a corrugated board. コルゲート板の拡大断面図。The expanded sectional view of a corrugated board.

以下に、この発明の実施形態を図面の実施例に基づいて具体的に説明する。   Embodiments of the present invention will be specifically described below based on examples of the drawings.

図1から5は、この発明の最初の実施例である。図において、金属板(例えばアルミの薄板)を波形成形したコルゲート板10が形成され、コルゲート板10は、折り返し面12、14が平坦状で断面が矩形波形状に形成されている。コルゲート板10の両側を側板20、30で挟持し、折り返し面12、14に側板20、30が当接し、コルゲート板10の側壁15で区画された流体の流通路が形成されている。コルゲート板10の前後端面は端板11で閉塞され、図3に示すように、水の流通路Wと燃焼排気の流通路Gとが交互に形成されている。コルゲート板10は、図5に示すように、燃焼排気の流通路Gの幅Aと水の流通路Wの幅Bが同一寸法となるように、折り返し面12、14の幅寸法が設定されている。   1 to 5 show the first embodiment of the present invention. In the figure, a corrugated plate 10 formed by corrugating a metal plate (for example, a thin aluminum plate) is formed. The corrugated plate 10 has folded surfaces 12 and 14 that are flat and a rectangular cross section. Both sides of the corrugated plate 10 are sandwiched between the side plates 20 and 30, the side plates 20 and 30 are in contact with the folded surfaces 12 and 14, and a fluid flow path defined by the side wall 15 of the corrugated plate 10 is formed. The front and rear end faces of the corrugated plate 10 are closed by the end plate 11, and as shown in FIG. 3, water flow passages W and combustion exhaust flow passages G are alternately formed. As shown in FIG. 5, the corrugated plate 10 has the width dimensions of the folded surfaces 12 and 14 so that the width A of the combustion exhaust flow path G and the width B of the water flow path W have the same dimensions. Yes.

一方の側板20の両側端部に膨出部が形成され、膨出部は流体の流通路の両端位置に位置している。この膨出部によって形成される膨出空間に水の流通路Wが開口し、一端に入口ヘッダー22を形成して入口管25を設け、他端に出口ヘッダー23を形成して出口管26を設けている。   The bulging portions are formed at both end portions of one side plate 20, and the bulging portions are positioned at both end positions of the fluid flow passage. A water flow passage W is opened in the bulging space formed by the bulging portion, an inlet header 22 is formed at one end, an inlet pipe 25 is provided, an outlet header 23 is formed at the other end, and an outlet pipe 26 is provided. Provided.

同様に、他方の側板30の両側端部に膨出部が形成され、この膨出部によって形成される膨出空間に燃焼排気の流通路Gが開口し、一端に入口ヘッダー32を形成して入口管35を設け、他端に出口ヘッダー33を形成して出口管36を設け、出口ヘッダー33の底部に排水管37を設けている。なお、水と燃焼排気とがそれぞれの流通路W、Gを逆方向へ流通するように、入口ヘッダーと出口ヘッダーの位置関係は両側板20、30で反対である。   Similarly, a bulging portion is formed at both end portions of the other side plate 30, a combustion exhaust flow passage G is opened in the bulging space formed by this bulging portion, and an inlet header 32 is formed at one end. An inlet pipe 35 is provided, an outlet header 33 is formed at the other end, an outlet pipe 36 is provided, and a drain pipe 37 is provided at the bottom of the outlet header 33. The positional relationship between the inlet header and the outlet header is opposite between the side plates 20 and 30 so that water and combustion exhaust gas flow through the respective flow passages W and G in opposite directions.

この熱交換器は、図1に示すように、流体の流通路W、Gが垂直方向に沿うととともに、燃焼排気の出口ヘッダー33が下位置となるように設置する。熱交換する一方の流体である水は、入口ヘッダー22から流通路Wを流通して出口ヘッダー23へ至り(図1中、白抜き矢印)、熱交換する他方の流体である燃焼排気は、入口ヘッダー32から流通路Gを流通し、出口ヘッダー33へ至り(図1中、実線矢印)、水と燃焼排気は逆方向(クロス方向)へ流通し、極めて狭間隔の流通路W、Gを交互に流通し、コルゲート板10の側壁15を介して熱交換が行われる。この熱交換の過程で燃焼排気が低温下して生じる凝縮水は出口ヘッダー33に捕集され、捕集された凝縮水は、出口ヘッダー33の底部に設けた排水管37から速やかに外部に導出される。なお、排水管37には凝縮水を貯留するタンクや排水路を開閉操作するバルブ等を設けてもよい。   As shown in FIG. 1, this heat exchanger is installed so that the fluid flow paths W and G are along the vertical direction and the outlet header 33 of the combustion exhaust is at the lower position. Water, which is one fluid for heat exchange, flows from the inlet header 22 through the flow path W to the outlet header 23 (indicated by white arrows in FIG. 1), and the combustion exhaust, which is the other fluid for heat exchange, Flowing from the header 32 through the flow passage G to the outlet header 33 (solid arrow in FIG. 1), water and combustion exhaust flow in the opposite direction (cross direction), and the flow passages W and G with extremely narrow intervals are alternately arranged. The heat exchange is performed through the side wall 15 of the corrugated plate 10. Condensed water generated when the combustion exhaust gas is lowered in the heat exchange process is collected in the outlet header 33, and the collected condensed water is quickly led out to the outside from a drain pipe 37 provided at the bottom of the outlet header 33. Is done. The drain pipe 37 may be provided with a tank for storing condensed water, a valve for opening and closing the drain path, or the like.

図6及び7は、コルゲート板の他の実施例である。この実施例のコルゲート板10は、燃焼排気の流通路の幅Aが水の流通路の幅Bより大きくなるように、折り返し面12、14の幅寸法を設定したものである。このようにコルゲート板10を形成することで、大流量の燃焼排気に対応し、効率的な熱交換の促進を図ったものである。   6 and 7 show another embodiment of the corrugated plate. In the corrugated plate 10 of this embodiment, the width dimensions of the folded surfaces 12 and 14 are set so that the width A of the flow path of combustion exhaust is larger than the width B of the flow path of water. By forming the corrugated plate 10 in this way, it is possible to cope with a large flow rate of combustion exhaust and promote efficient heat exchange.

10 コルゲート板
15 側壁
20 側板
22 入口ヘッダー
23 出口ヘッダー
30 側板
32 入口ヘッダー
33 出口ヘッダー
10 Corrugated plate 15 Side wall 20 Side plate 22 Inlet header 23 Outlet header 30 Side plate 32 Inlet header 33 Outlet header

Claims (2)

波形成形したコルゲート板10の両側を側板20、30で挟持し、コルゲート板10の側壁15で区画された流体の流通路を形成し、熱交換する水と燃焼排気とが、その流通方向が逆方向で流体の流通路を交互に流通し、
両側板20、30の両側端部に膨出部を形成して一端に入口ヘッダー22、32、他端に出口ヘッダー23、33を形成し、
流体の流通路が垂直方向に沿うととともに、燃焼排気の出口ヘッダー33が下位置となるように設置し、燃焼排気の出口ヘッダー33の底部に、熱交換の過程で燃焼排気が低温下して生じる凝縮水を外部に導出する排水管37を設けた廃熱回収用熱交換器。
Both sides of the corrugated plate 10 having the corrugated shape are sandwiched between the side plates 20 and 30 to form a fluid flow path partitioned by the side wall 15 of the corrugated plate 10, and the flow direction of water for heat exchange and combustion exhaust gas is reversed. The fluid flow path alternately in the direction,
Forming bulges on both side ends of both side plates 20, 30 to form inlet headers 22, 32 at one end and outlet headers 23, 33 at the other end,
It is installed so that the flow path of the fluid is along the vertical direction and the outlet header 33 of the combustion exhaust is at the lower position, and the combustion exhaust is lowered to the bottom of the outlet header 33 of the combustion exhaust in the process of heat exchange. A heat exchanger for recovering waste heat provided with a drain pipe 37 for leading the condensed water generated to the outside.
燃焼排気の流通路の幅Aが水の流通路の幅Bより大きくなるようにコルゲート板10を形成した請求項1に記載の廃熱回収用熱交換器。   The heat exchanger for waste heat recovery according to claim 1, wherein the corrugated plate 10 is formed so that the width A of the flow path of the combustion exhaust is larger than the width B of the flow path of the water.
JP2010181679A 2010-08-16 2010-08-16 Heat exchanger for waste heat recovery Pending JP2012042069A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013113512A (en) * 2011-11-29 2013-06-10 Atago Seisakusho:Kk Heat exchanger for waste heat recovery

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004197664A (en) * 2002-12-19 2004-07-15 Sanyo Electric Co Ltd Exhaust gas heat exchanger and refrigerating plant
JP2010121925A (en) * 2008-10-21 2010-06-03 Atago Seisakusho:Kk Heat exchanger

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004197664A (en) * 2002-12-19 2004-07-15 Sanyo Electric Co Ltd Exhaust gas heat exchanger and refrigerating plant
JP2010121925A (en) * 2008-10-21 2010-06-03 Atago Seisakusho:Kk Heat exchanger

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2013113512A (en) * 2011-11-29 2013-06-10 Atago Seisakusho:Kk Heat exchanger for waste heat recovery

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