JP2016061542A - Exhaust gas heat exchanger - Google Patents

Exhaust gas heat exchanger Download PDF

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JP2016061542A
JP2016061542A JP2014192369A JP2014192369A JP2016061542A JP 2016061542 A JP2016061542 A JP 2016061542A JP 2014192369 A JP2014192369 A JP 2014192369A JP 2014192369 A JP2014192369 A JP 2014192369A JP 2016061542 A JP2016061542 A JP 2016061542A
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exhaust gas
heat exchanger
heat transfer
header
tube
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JP6114726B2 (en
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圭佐 福本
Yoshisuke Fukumoto
圭佐 福本
中島 竜一
Ryuichi Nakajima
竜一 中島
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NISSHIN CORP KK
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Abstract

PROBLEM TO BE SOLVED: To provide an exhaust gas heat exchanger having a superior acid corrosion resistance, capable of quite easily and efficiently performing inspection, repairing and replacement of a heat transfer pipe and having a simple structure.SOLUTION: A heat exchanger shell 1 has a fixable or removable lid plate 11, its inner side is partitioned into an upstream side sub-chamber 13 and a downstream side sub-chamber 14 and a water conduction pipe passage 4 is connected between both sub-chambers 13, 14 through each of connection headers. Many heat transfer pipes 2 suspended from the heat exchanger shell show double-pipes by an outer pipe having lower end closed and coated with fluorine resin and an inner pipe of fluorine resin having its lower end opened, every plurality of pipes constitute a group of pipes corresponding to each of the headers, each of the outer pipes is inserted, fitted and fixed to bottom walls 15 of both sub-chambers at its opened upper end part, upper sides of the inner pipes are extended into the sub-chambers, collected at their corresponding headers and communicated therewith, cold water W1 fed into the inlet header 31 is heat exchanged with combustion exhaust gas G1 of high temperature at a process reaching the outlet header 32 while being reciprocated in each of the heat transfer pipes and then the water is fed out as hot water W2.SELECTED DRAWING: Figure 1

Description

本発明は、ボイラー排ガス等の燃焼排ガスの排ガスダクト内に設置され、該燃焼排ガスとの熱交換によって導入した冷水を温水化して熱回収すると共に、該燃焼排ガスを低温化するのに用いる排ガス用熱交換器に関する。   The present invention is installed in an exhaust gas duct of combustion exhaust gas such as boiler exhaust gas, and heat recovery is performed by warming and recovering cold water introduced by heat exchange with the combustion exhaust gas, and for exhaust gas used for lowering the temperature of the combustion exhaust gas. It relates to a heat exchanger.

一般的に、ボイラー排ガス等の高温の燃焼排ガスより熱回収する手段として、該燃焼排ガスが流れる排ガスダクト内に伝熱管を配設し、該伝熱管に供給した冷水(水道水)を燃焼排ガスとの熱交換で昇温させて温水として取り出す方法が広く採用されている(例えば、特許文献1,2)。   Generally, as means for recovering heat from high-temperature combustion exhaust gas such as boiler exhaust gas, a heat transfer pipe is disposed in an exhaust gas duct through which the combustion exhaust gas flows, and cold water (tap water) supplied to the heat transfer pipe is used as combustion exhaust gas. The method of raising the temperature by heat exchange and taking it out as hot water is widely adopted (for example, Patent Documents 1 and 2).

しかるに、燃焼排ガスは、概して燃料中の硫黄分に由来する亜硫酸ガス(SO2)や硫酸ガス(SO3)を含んでおり、これらによる強い腐食性(特に露点以下の低温部での結露による酸露点腐食性)があるため、排ガス用熱交換器の伝熱管やその配管支持部等の排ガスに接する金属部分が早期に腐食劣化するという問題があった。そこで、従来より、排ガス用熱交換器の耐酸腐食対策として、接ガス部にステンレス鋼や低合金鋼等の耐蝕性の高い金属材料を用いたり、接ガス部の金属表面にフッ素系樹脂によるライニングやコーティングを施す試みがなされているが、現状では優れた耐酸腐食性を備えるものとして次のような排ガス用熱交換器が唯一実用化されている(非特許文献1)。 However, combustion exhaust gas generally contains sulfurous acid gas (SO 2 ) and sulfuric acid gas (SO 3 ) derived from sulfur in the fuel, and strong corrosiveness due to these (especially acid due to condensation in a low temperature part below the dew point). Since there is dew point corrosion), there is a problem that metal parts in contact with the exhaust gas such as the heat transfer pipe of the heat exchanger for exhaust gas and its pipe support part corrode quickly. Therefore, conventionally, as a countermeasure against acid corrosion of heat exchangers for exhaust gas, a metal material with high corrosion resistance such as stainless steel or low alloy steel is used for the gas contact part, or a fluorine resin lining is used for the metal surface of the gas contact part. At present, the following exhaust gas heat exchangers have been put into practical use only as those having excellent acid corrosion resistance (Non-patent Document 1).

この実用化されている排ガス用熱交換器は、図6に示すように、排ガスダクト10の天井部に配置する炭素鋼からなる熱交換器シェル100から多数本(数百本)の伝熱管200が垂下している。その熱交換器シェル100は、内側が水平仕切板101によって上下に仕切られており、仕切られた上側空間が縦仕切壁110によって入口側分室111と出口側分室112及び中間分室113に区画されると共に、下側空間も縦仕切壁120によって上流側室121と下流側室122とに区画されている。そして、入口側分室111には冷水W1を導入する入口ヘッダー131が、出口側分室112には熱交換後の温水W2を導出する出口ヘッダー132が、それぞれ設けてある。一方、各伝熱管200は、上端側を熱交換器シェル100の底壁をなすシールプレート102に止着した外管201と、この外管201内に挿通されて上端を水平仕切板101に止着した図示一点鎖線で示す内管202とからなる二重管になっている。なお、排ガスダクト10内の上流側には、伝熱管200に向けて洗浄水W3を噴射して付着ダストを洗い流すための洗浄水ノズル300が配設されており、その洗浄後の洗浄水W4を下方のドレン400より排出するようになっている。   As shown in FIG. 6, the exhaust gas heat exchanger in practical use includes a large number (several hundreds) of heat transfer tubes 200 from a heat exchanger shell 100 made of carbon steel disposed on the ceiling of the exhaust gas duct 10. Is drooping. The heat exchanger shell 100 is divided into upper and lower parts by a horizontal partition plate 101, and the partitioned upper space is partitioned into an inlet side compartment 111, an outlet side compartment 112 and an intermediate compartment 113 by a vertical partition wall 110. In addition, the lower space is also divided into an upstream chamber 121 and a downstream chamber 122 by the vertical partition wall 120. The inlet-side compartment 111 is provided with an inlet header 131 for introducing the cold water W1, and the outlet-side compartment 112 is provided with an outlet header 132 for extracting the hot water W2 after heat exchange. On the other hand, each heat transfer tube 200 has an outer tube 201 whose upper end is fixed to a seal plate 102 that forms the bottom wall of the heat exchanger shell 100 and an upper end that is inserted into the outer tube 201 and is fixed to the horizontal partition plate 101. It is a double tube made up of an inner tube 202 shown by a dashed dotted line in the figure. A cleaning water nozzle 300 is provided upstream of the exhaust gas duct 10 to inject cleaning water W3 toward the heat transfer tube 200 to wash away the adhering dust. It is discharged from the lower drain 400.

図7で詳細に示すように、各伝熱管200の外管201は、ステンレス鋼管211の外面にフッ素系樹脂PFA(テトラフルオロエチレン・パーフルオロアルキルビニルエーテル共重合体)の被覆層212が設けてあり、下端を栓体(図示省略)で閉塞し、開放した上端側をシールプレート102の係止孔102aに挿通して、その挿通部の上中下三カ所を拡径213することによって該シールプレート102に止着されている。また、内管202は、フッ素系樹脂FEP(テトラフルオロエチレン・ヘキサフルオロプロピレン共重合体)製チューブからなり、上下両端が開放し、その上端側を水平仕切板101の取付孔101aに貫通して、内側にステンレス鋼製の短管221を圧入することにより、該水平仕切板101に止着されている。そして、シールプレート102の底面を含む熱交換器シェル100の接ガス部表面にはフッ素系樹脂PFAのルーズライニング150が施されている。   As shown in detail in FIG. 7, the outer tube 201 of each heat transfer tube 200 is provided with a coating layer 212 of fluororesin PFA (tetrafluoroethylene / perfluoroalkyl vinyl ether copolymer) on the outer surface of the stainless steel tube 211. The lower end is closed with a plug (not shown), the opened upper end is inserted into the locking hole 102a of the seal plate 102, and the upper, middle, lower and upper three portions of the insertion portion are expanded in diameter 213. It is fixed to 102. The inner tube 202 is made of a fluororesin FEP (tetrafluoroethylene / hexafluoropropylene copolymer) tube, and both upper and lower ends are open, and the upper end side penetrates through the mounting hole 101a of the horizontal partition plate 101. The stainless steel short pipe 221 is press-fitted on the inner side, thereby being fixed to the horizontal partition plate 101. A loose lining 150 of fluororesin PFA is applied to the surface of the gas contact portion of the heat exchanger shell 100 including the bottom surface of the seal plate 102.

この排ガス用熱交換器では、上記構成によって熱交換部が図6の如く入口側から出口側へ4つの領域Z1〜Z4に分かれる形になり、入口ヘッダー131から入口側分室111へ導入された冷水W1は、該入口側分室111直下の領域Z1において、各伝熱管200の内管202内に分配流入し、その下端から流出して外管201の内側を上昇して上流側室121内へ流出する。次いで、該上流側室121が中間分室113に臨む領域Z2において、各伝熱管200の外管201内に分配流入し、その下端内部から内管202内へ流入して上昇し、中間分室113内へ流出する。続いて、該中間分室113が下流側室122に臨む領域Z3において、各伝熱管200の内管202内に分配流入し、その下端から流出して外管201の内側を上昇し、下流側室122内へ流出する。更に、出口側分室112直下の領域Z4において、各伝熱管200の外管201内に分配流入し、その下端内部から内管202内へ流入して上昇し、出口側分室112へ流出し、この過程での排ガスとの熱交換によって昇温した温水W2として出口ヘッダー132から導出される。なお、図7は、熱交換の操作線を示しており、導入された冷水W1が各領域Z1〜Z4を順次経る過程で段階的に昇温して温水W2として導出する一方、高温排ガスG1は逆に領域Z4→Z1を通過することで連続的に降温して低温排ガスG2として下流側へ移行する。   In this heat exchanger for exhaust gas, the heat exchange part is divided into four regions Z1 to Z4 from the inlet side to the outlet side as shown in FIG. 6 by the above configuration, and the cold water introduced from the inlet header 131 to the inlet side compartment 111. W1 distributes and flows into the inner tube 202 of each heat transfer tube 200 in the region Z1 directly below the inlet-side compartment 111, flows out from the lower end thereof, rises inside the outer tube 201, and flows into the upstream chamber 121. . Next, in the region Z2 where the upstream chamber 121 faces the intermediate compartment 113, it flows into the outer tube 201 of each heat transfer tube 200, flows into the inner tube 202 from its lower end, rises, and enters the intermediate compartment 113. leak. Subsequently, in the region Z3 where the intermediate compartment 113 faces the downstream chamber 122, it flows into the inner tube 202 of each heat transfer tube 200, flows out from its lower end, rises inside the outer tube 201, and flows into the downstream chamber 122. Spill to Further, in the region Z4 immediately below the outlet side compartment 112, it flows into the outer pipe 201 of each heat transfer pipe 200, flows into the inner pipe 202 from the lower end inside, rises, and flows out into the outlet side compartment 112. The hot water W2 heated by heat exchange with the exhaust gas in the process is led out from the outlet header 132. In addition, FIG. 7 has shown the operating line of heat exchange, and while the introduced cold water W1 goes through each area | region Z1-Z4 sequentially, it heats up in steps and derives as hot water W2, while high temperature exhaust gas G1 is On the other hand, the temperature is continuously lowered by passing through the region Z4 → Z1, and moves to the downstream side as the low temperature exhaust gas G2.

特開2010−255925号公報JP 2010-255925 A 特開2014−126330号公報JP 2014-126330 A

インターネット・ウエブ・エアーフローリッヒ/耐酸熱交換器/伊藤忠マシンテクノス株式会社、検索日:2014年7月7日、http://www.itcmt.co.jp/products/industrial/plant/airflow.htmlInternet Web Airflow Rich / Acid Resistance Heat Exchanger / ITOCHU Machine Technos Co., Ltd. Search Date: July 7, 2014, http://www.itcmt.co.jp/products/industrial/plant/airflow.html

しかしながら、前記従来の排ガス用熱交換器の場合、図7に示すように、熱交換器シェル100の上壁部は周辺部をパッキン104を介してボルト止めする着脱可能な蓋板103にて構成されるが、伝熱管200の異常の有無を点検する際、蓋板103を取り外しても水平仕切板101が存在するから、そのままでは各伝熱管200の状態を目視で確認することができず、点検するためには該水平仕切板101を止着した多数本の内管202ごと引き上げて熱交換器シェル100外へ持ち出す必要があり、その作業に多大な労力及び時間を要する上、補修・交換にも非常に手間がかかるという難点があった。また、水平仕切板101は、熱交換器シェル100に対して周縁部でパッキン104を介してねじ止めする構造であるが、熱交換器シェル100の略内側全体を覆う広面積で且つ比較的に薄肉の板体であるため、撓みや歪みによる封止不良を生じ易く、特に上記点検時の着脱操作に伴って周辺部が変形して封止不良に繋がる懸念が多分にあった。   However, in the case of the conventional exhaust gas heat exchanger, as shown in FIG. 7, the upper wall portion of the heat exchanger shell 100 is constituted by a detachable lid plate 103 that is bolted to the periphery via a packing 104. However, when checking whether there is an abnormality in the heat transfer tube 200, even if the cover plate 103 is removed, the horizontal partition plate 101 is present, so the state of each heat transfer tube 200 cannot be visually confirmed as it is, In order to inspect, it is necessary to pull up a large number of inner pipes 202 to which the horizontal partition plate 101 is fixed, and take them out of the heat exchanger shell 100. This work requires a great deal of labor and time, and repair and replacement. However, there was a problem that it was very time-consuming. Further, the horizontal partition plate 101 has a structure in which the heat exchanger shell 100 is screwed to the heat exchanger shell 100 through the packing 104 at the peripheral edge, but has a large area that covers substantially the entire inner side of the heat exchanger shell 100 and is relatively Since it is a thin plate body, sealing failure due to bending or distortion is likely to occur, and there are many concerns that the peripheral portion may be deformed due to the attachment / detachment operation at the time of inspection, leading to sealing failure.

本発明は、上述の事情に鑑み、優れた耐酸腐食性を具備し、亜硫酸ガス及び硫酸ガスを含む高温の燃焼排ガスを熱交換対象として、長期にわたって高い熱交換効率が得られる上、伝熱管の点検及び補修・交換を極めて容易に能率よく行え、構造的にも簡素な排ガス用熱交換器を提供することを目的としている。   In view of the above-described circumstances, the present invention has excellent acid corrosion resistance, and high-temperature combustion exhaust gas containing sulfurous acid gas and sulfuric acid gas is used as a heat exchange target, and high heat exchange efficiency is obtained over a long period of time. The object is to provide a heat exchanger for exhaust gas that can be inspected, repaired, and replaced very easily and efficiently and that is structurally simple.

上記目的を達成するための手段を図面の参照符号を付して示せば、請求項1の発明に係る排ガス用熱交換器は、燃焼排ガスが横方向に流れる排ガスダクト10の天井部に配置する熱交換器シェル1と、該熱交換器シェル1から垂下する多数本の伝熱管2とを備え、熱交換器シェル1は、天井部が着脱可能な蓋板11にて構成され、内部が仕切壁12によって複数の分室13,14に区割され、最上流側の分室13に臨む入口ヘッダー31と最下流側の分室14に臨む出口ヘッダー32とを備えると共に、隣接する上流側の分室13と下流側の分室14との間に各々接続ヘッダー33,34を介して通水管路4が接続され、伝熱管2は、外面にフッ素系樹脂のコーティング51が施されて下端を閉塞した金属パイプ(ステンレス鋼パイプ20)からなる外管21と、この外管21内に挿入されて下端が開放したフッ素系樹脂の可撓性チューブからなる内管22とで二重管状をなし、その複数本ずつが入口ヘッダー31及び出口ヘッダー32と各接続ヘッダー33,34に各々対応する群を構成し、各伝熱管2の外管21は、上端部が分室13,14の底壁15に設けた取付孔15aに気密に挿嵌固定されて、内部が該分室13,14内に連通し、該伝熱管2における内管22の上部側が前記分室13,14内に延出されて前記群毎に集合して対応するヘッダー31〜34に連通し、入口ヘッダー31より導入された冷水W1が、二重管状の各伝熱管2内を往復しつつ熱交換器シェル1の各分室13,14を経て出口ヘッダー32に至る過程で、排ガスダクト10内を流れる高温の燃焼排ガスと熱交換して該出口ヘッダー32より温水W2として導出すると共に、該熱交換によって燃焼排ガスを低温化するように構成されてなる。   If the means for achieving the above object is shown with reference numerals in the drawings, the heat exchanger for exhaust gas according to the invention of claim 1 is arranged on the ceiling portion of the exhaust gas duct 10 in which the combustion exhaust gas flows in the lateral direction. A heat exchanger shell 1 and a large number of heat transfer tubes 2 hanging from the heat exchanger shell 1 are provided. The heat exchanger shell 1 is composed of a lid plate 11 with a detachable ceiling, and the interior is partitioned. The wall 12 is divided into a plurality of compartments 13 and 14 and includes an inlet header 31 facing the upstreammost compartment 13 and an outlet header 32 facing the downstreammost compartment 14, and an adjacent upstream compartment 13. A water pipe 4 is connected to each of the downstream compartments 14 via connection headers 33 and 34, and the heat transfer pipe 2 is a metal pipe whose outer surface is coated with a fluororesin 51 and whose lower end is closed ( Stainless steel pipe 20) The outer tube 21 and the inner tube 22 made of a fluororesin flexible tube that is inserted into the outer tube 21 and has an open lower end form a double tube. A group corresponding to each of the outlet header 32 and the connection headers 33 and 34 is configured, and the outer tube 21 of each heat transfer tube 2 is hermetically inserted into the mounting hole 15a provided in the bottom wall 15 of the compartments 13 and 14 at the upper end. The header 31 is fitted and fixed so that the inside communicates with the compartments 13 and 14, and the upper side of the inner tube 22 of the heat transfer tube 2 extends into the compartments 13 and 14 to be assembled for each group. To the outlet header 32 through the respective compartments 13 and 14 of the heat exchanger shell 1 while reciprocating in the double tubular heat transfer tubes 2. , High-temperature combustion flowing in the exhaust gas duct 10 With gas and exchanges heat derived as hot W2 from the outlet header 32, it is configured to low temperature flue gas by heat exchange.

請求項2の発明は、上記請求項1の排ガス用熱交換器において、各ヘッダー31〜34の内空間30と分室13,14との間に仕切板6が介在し、該仕切板6に設けた取付孔6aに伝熱管2における各内管22の上端部が挿嵌され、この挿嵌部分が熱可塑性フッ素系樹脂によって溶接53されてなるものとしている。   According to a second aspect of the present invention, in the exhaust gas heat exchanger of the first aspect, the partition plate 6 is interposed between the inner space 30 of each of the headers 31 to 34 and the compartments 13 and 14, and is provided on the partition plate 6. The upper end portion of each inner tube 22 in the heat transfer tube 2 is inserted into the mounting hole 6a, and this inserted portion is welded 53 with a thermoplastic fluororesin.

請求項3の発明は、上記請求項1又は2の排ガス用熱交換器において、熱交換器シェル1内が上流側分室13と下流側分室14とに2区割され、上流側分室13の側壁部13aに入口ヘッダー31と通水管路4の一端側の接続ヘッダー33が設けられると共に、下流側分室14の側壁部14aに出口ヘッダー32と通水管路4の他端側の接続ヘッダー34が設けられてなるものとしている。   According to a third aspect of the present invention, in the heat exchanger for exhaust gas according to the first or second aspect, the inside of the heat exchanger shell 1 is divided into two sections, an upstream compartment 13 and a downstream compartment 14, and the side wall of the upstream compartment 13 An inlet header 31 and a connection header 33 on one end side of the water conduit 4 are provided in the portion 13a, and an outlet header 32 and a connection header 34 on the other end side of the water conduit 4 are provided on the side wall portion 14a of the downstream compartment 14. It is supposed to be made.

請求項4の発明は、上記請求項1〜3のいずれかの排ガス用熱交換器において、排ガスダクト10内における伝熱管2の配置部よりも上流側に、該伝熱管2に対して洗浄水W3を噴射する洗浄水ノズル8が配設されると共に、該伝熱管2の配置部の下方に水溜まり部10aが設けられ、この水溜まり部10aに溜まった洗浄水W4中に各伝熱管2の下端部が浸漬されてなるものとしている。   According to a fourth aspect of the present invention, in the exhaust gas heat exchanger according to any one of the first to third aspects of the present invention, the cleaning water is washed with respect to the heat transfer tube 2 upstream of the arrangement portion of the heat transfer tube 2 in the exhaust gas duct 10. A cleaning water nozzle 8 for injecting W3 is provided, and a water reservoir 10a is provided below the arrangement portion of the heat transfer tube 2, and the lower ends of the heat transfer tubes 2 are contained in the cleaning water W4 collected in the water reservoir 10a. It is assumed that the part is immersed.

次に、本発明の効果について、図面の参照符号を付して説明する。まず、請求項1の発明に係る排ガス用熱交換器では、熱交換器シェル1より排ガスダクト10内へ垂下する二重管状の各伝熱管2は、外管21が外面にフッ素系樹脂のコーティング51を施した金属パイプ20からなり、内管22がフッ素系樹脂の可撓性チューブからなるため、優れた耐酸腐食性を具備し、亜硫酸ガス及び硫酸ガスを含む高温の燃焼排ガスを熱交換対象として、長期にわたって高い熱交換効率が得られる。しかも、該伝熱管2は、入口ヘッダー31及び出口ヘッダー32と接続ヘッダー33,34に対し、内管22が複数本ずつの群として集合して連通する一方、各伝熱管2の外管21が上端部で分室13,14の底壁15に挿嵌固定されて内部を該分室13,14内に連通しているから、伝熱管2を点検する際、熱交換器シェル1の天井部をなす蓋板11を取り外すだけで、外管21及び内管22の止着部分が露呈する。従って、各内管22を外管21から抜出することにより、内外管22,21の状態を目視によって簡単に確認できると共に、内外管22,21に破損や劣化等の欠陥が発見された場合の補修や交換の作業も容易に能率よく行える。また、熱交換器シェル1自体は、内部が仕切壁12によって複数の分室13,14に区割されているだけであるから、構造的に簡素であって安価に製作できるという利点がある。   Next, effects of the present invention will be described with reference numerals in the drawings. First, in the exhaust gas heat exchanger according to the first aspect of the present invention, each of the double tubular heat transfer tubes 2 hanging from the heat exchanger shell 1 into the exhaust gas duct 10 has an outer tube 21 coated with a fluorine resin on the outer surface. 51, and the inner tube 22 is made of a fluororesin flexible tube. Therefore, it has excellent acid corrosion resistance, and heat exchange is performed on high-temperature combustion exhaust gas containing sulfurous acid gas and sulfuric acid gas. As a result, high heat exchange efficiency can be obtained over a long period of time. In addition, the heat transfer tubes 2 communicate with the inlet header 31 and the outlet header 32 and the connection headers 33 and 34 in a group of a plurality of inner tubes 22, while the outer tubes 21 of the heat transfer tubes 2 are connected to each other. At the upper end, it is inserted and fixed to the bottom wall 15 of the compartments 13 and 14, and the interior communicates with the compartments 13 and 14, so that when inspecting the heat transfer tube 2, it forms the ceiling part of the heat exchanger shell 1. By simply removing the cover plate 11, the fastening portions of the outer tube 21 and the inner tube 22 are exposed. Accordingly, by pulling out each inner tube 22 from the outer tube 21, the state of the inner and outer tubes 22, 21 can be easily confirmed visually, and defects such as breakage and deterioration are found in the inner and outer tubes 22, 21. Repair and replacement work can be done easily and efficiently. Further, the heat exchanger shell 1 itself has an advantage that it is structurally simple and can be manufactured at low cost because the inside is only divided into the plurality of compartments 13 and 14 by the partition wall 12.

請求項2の発明によれば、各ヘッダー31〜34の内空間30と分室13,14との間に介在する仕切板6に、各ヘッダー31〜34毎に対応する内管22群が一体化しているから、前記点検に際し、該仕切板6を引くことで内管22群を各々の外管21から一挙に抜出でき、それだけ作業性が向上すると共に、各内管22の上端部が該仕切板6に対して熱可塑性フッ素系樹脂によって溶接53されているから、その溶接部の加熱溶融によって該内管22の交換を容易に行える。   According to the invention of claim 2, the inner pipe 22 group corresponding to each header 31 to 34 is integrated with the partition plate 6 interposed between the inner space 30 of each header 31 to 34 and the compartments 13 and 14. Therefore, at the time of the inspection, by pulling the partition plate 6, the inner tube 22 group can be pulled out from each outer tube 21 at a stroke, so that the workability is improved and the upper end of each inner tube 22 is Since the partition plate 6 is welded 53 with thermoplastic fluororesin, the inner tube 22 can be easily replaced by heating and melting the welded portion.

請求項3の発明によれば、熱交換器シェル1内が上流側分室13と下流側分室14とに2区割され、入口ヘッダー31及び出口ヘッダーと通水管路4の両側の接続ヘッダー33,34が両分室13,14の側壁部13a,14aに設けられ、入口ヘッダー31に導入された冷水W1が各ヘッダー31〜34に対応する領域Z1〜Z4の各々で伝熱管2を往復し、排ガスダクト10内を計4往復して出口ヘッダー32より温水W2として導出する構成であるから、排ガス用熱交換器として簡素で且つ機能的である上に高い熱交換効率が得られる。   According to the invention of claim 3, the inside of the heat exchanger shell 1 is divided into the upstream compartment 13 and the downstream compartment 14, and the inlet header 31, the outlet header, and the connection headers 33 on both sides of the water conduit 4, 34 is provided in the side wall portions 13a and 14a of both the compartments 13 and 14, and the cold water W1 introduced into the inlet header 31 reciprocates in the heat transfer pipe 2 in each of the regions Z1 to Z4 corresponding to the headers 31 to 34, and the exhaust gas. Since the inside of the duct 10 is reciprocated four times and led out as the hot water W2 from the outlet header 32, it is simple and functional as an exhaust gas heat exchanger, and high heat exchange efficiency is obtained.

請求項4の発明によれば、洗浄水ノズル8から噴射された洗浄水W3によって伝熱管2の表面に付着したダストが洗い流され、もって熱交換効率の低下が防止されると共に、該伝熱管2の配置部の下方の水溜まり部10aに溜まった洗浄水W4中に各伝熱管2の下端部が浸漬されるから、該伝熱管2内での沸騰が防止され、その沸騰に伴う伝熱管2の膨張で表面のフッ素系樹脂のコーティング層51が破壊されるのを回避できる。   According to the fourth aspect of the present invention, the dust adhering to the surface of the heat transfer tube 2 is washed away by the cleaning water W3 sprayed from the cleaning water nozzle 8, thereby preventing the heat exchange efficiency from being lowered, and the heat transfer tube 2 Since the lower end of each heat transfer tube 2 is immersed in the wash water W4 accumulated in the water reservoir 10a below the arrangement portion, boiling in the heat transfer tube 2 is prevented, and the heat transfer tube 2 accompanying the boiling of the heat transfer tube 2 is prevented. It is possible to avoid the destruction of the coating layer 51 of the fluororesin on the surface due to expansion.

本発明の一実施形態に係る排ガス用熱交換器の設置状態を模式的に示す概略縦断側面図である。It is a schematic longitudinal cross-sectional side view which shows typically the installation state of the heat exchanger for waste gas which concerns on one Embodiment of this invention. 同排ガス用熱交換器の熱交換器シェルの横断平面図である。It is a cross-sectional plan view of the heat exchanger shell of the exhaust gas heat exchanger. 同排ガス用熱交換器の温度操作線図である。It is a temperature operation diagram of the heat exchanger for exhaust gas. 同排ガス用熱交換器の熱交換器シェルにおける伝熱管の外管の止着部分を示す縦断面図である。It is a longitudinal cross-sectional view which shows the fixation part of the outer tube | pipe of the heat exchanger tube in the heat exchanger shell of the heat exchanger for exhaust gas. 同排ガス用熱交換器の熱交換器シェルにおける伝熱管の内管の止着部分を示す横断平面図である。It is a cross-sectional top view which shows the fixation part of the inner tube | pipe of the heat exchanger tube in the heat exchanger shell of the heat exchanger for exhaust gas. 従来の排ガス用熱交換器の設置状態を模式的に示す概略縦断側面図である。It is a general | schematic longitudinal cross-sectional side view which shows typically the installation state of the conventional heat exchanger for waste gas. 同排ガス用熱交換器の熱交換器シェルにおける伝熱管の止着部分を示す縦断面図である。It is a longitudinal cross-sectional view which shows the fixation part of the heat exchanger tube in the heat exchanger shell of the heat exchanger for exhaust gas. 同排ガス用熱交換器の温度操作線図である。It is a temperature operation diagram of the heat exchanger for exhaust gas.

以下に、本発明の一実施形態に係る排ガス用熱交換器について、図面を参照して具体的に説明する。   Hereinafter, an exhaust gas heat exchanger according to an embodiment of the present invention will be specifically described with reference to the drawings.

この排ガス用熱交換器は、図1に示すように、燃焼排ガスが横方向に流れる排ガスダクト10の天井部に、炭素鋼からなる熱交換器シェル1が配置し、この熱交換器シェル1から多数本(数百本)の伝熱管2が排ガスダクト10内に垂下している。その熱交換器シェル1は、天井部が着脱可能な蓋板11にて構成され、内部が仕切壁12によって上流側分室13と下流側分室14とに区割されている。そして、上流側分室13には水道水等の冷水W1を導入する入口ヘッダー31が設けられ、下流側分室14には熱交換後の温水W2を導出する出口ヘッダー32が設けられる共に、両分室13,14間には熱交換器シェル1の外側に配置した通水管路4が接続されている。また、各伝熱管2は、熱交換器シェル1のシールプレートをなす底壁15に上端部を止着した外管21と、この外管21内に挿通した可撓性チューブからなる内管22とで二重管構成になっている。   As shown in FIG. 1, the exhaust gas heat exchanger has a heat exchanger shell 1 made of carbon steel disposed on a ceiling portion of an exhaust gas duct 10 in which combustion exhaust gas flows in a lateral direction. A large number (several hundreds) of the heat transfer tubes 2 are suspended in the exhaust gas duct 10. The heat exchanger shell 1 is composed of a lid plate 11 with a detachable ceiling portion, and the interior is divided into an upstream compartment 13 and a downstream compartment 14 by a partition wall 12. The upstream side compartment 13 is provided with an inlet header 31 for introducing cold water W1 such as tap water, and the downstream side compartment 14 is provided with an outlet header 32 for deriving hot water W2 after heat exchange. , 14 is connected to a water conduit 4 arranged outside the heat exchanger shell 1. Each heat transfer tube 2 includes an outer tube 21 having an upper end fixed to a bottom wall 15 that forms a seal plate of the heat exchanger shell 1, and an inner tube 22 made of a flexible tube inserted into the outer tube 21. It has a double tube configuration.

なお、排ガスダクト10内における伝熱管2の配置部よりも上流側に、該伝熱管2に対して洗浄水W3を噴射する洗浄水ノズル8が配設されると共に、該伝熱管2の配置部の下方に、底を平坦にした水溜まり部10aが設けられ、この水溜まり部10aに溜まった洗浄水W4中に各伝熱管2の下端部が浸漬された状態になっている。   A cleaning water nozzle 8 for injecting the cleaning water W3 to the heat transfer tube 2 is disposed upstream of the heat transfer tube 2 arrangement portion in the exhaust gas duct 10, and the heat transfer tube 2 arrangement portion. A water reservoir 10a having a flat bottom is provided below the lower end of the heat transfer tube 2. The lower end of each heat transfer tube 2 is immersed in the cleaning water W4 accumulated in the water reservoir 10a.

図2に示すように、入口ヘッダー31及び出口ヘッダー32は両分室13,14の各側壁部13a,14aに設けられ、通水管路4の両端部は両分室13,14の側壁部13a,14aに対して各々接続ヘッダー33,34を介して取り付けられている。そして、多数本の伝熱管2は、その複数本ずつが入口ヘッダー31及び出口ヘッダー32と各接続ヘッダー33,34に各々対応する四つの群を構成しており、各群の内管22の上部側が外管21から両分室13,14内へ延出して対応するヘッダー31〜34の各々に集合して連通接続している。なお、図2では、伝熱管2の配置と内管22の集合状態が判り易いように、多数本の伝熱管2の内の一部を図示し、他の伝熱管2は位置のみを(+)記号で示している。また、伝熱管2の実際の本数は図2による図示の数倍になっている。   As shown in FIG. 2, the inlet header 31 and the outlet header 32 are provided in the side wall portions 13 a and 14 a of both the branch chambers 13 and 14, and both end portions of the water conduit 4 are the side wall portions 13 a and 14 a of both the branch chambers 13 and 14. Are attached via connection headers 33 and 34, respectively. The plurality of heat transfer tubes 2 constitute four groups, each of which corresponds to the inlet header 31, the outlet header 32, and the connection headers 33 and 34, and the upper portion of the inner tube 22 of each group. The side extends from the outer tube 21 into the two compartments 13 and 14 and is gathered and connected to each of the corresponding headers 31 to 34. In FIG. 2, a part of the multiple heat transfer tubes 2 is illustrated so that the arrangement of the heat transfer tubes 2 and the assembled state of the inner tubes 22 can be easily understood, and the other heat transfer tubes 2 are only positioned (+ ) Symbol. Further, the actual number of the heat transfer tubes 2 is several times as shown in FIG.

図4及び図5で詳細に示すように、各伝熱管2の外管21は、ステンレス鋼パイプ20の外面にフッ素系樹脂PFAのコーティング51を施したものであり、図示を省略した下端がフッ素系樹脂PFAの栓体の融着やステンレス鋼製端板の溶接等で閉塞され、開放した上端側を熱交換器シェル1の底壁15の係止孔15aに挿通して、その挿通部の中間と下部を拡径21aすると共に、ステンレス鋼パイプ20の上端周縁を溶接7することにより、該底壁15に止着されている。なお、底壁15の係止孔15aの内周には、外管21の拡径21aを許容する環状凹部15bが形成されている。   As shown in detail in FIGS. 4 and 5, the outer tube 21 of each heat transfer tube 2 is obtained by coating the outer surface of the stainless steel pipe 20 with a coating 51 of a fluorine-based resin PFA, and the lower end of which is not illustrated is fluorine. It is closed by fusing the stopper of the resin PFA, welding the stainless steel end plate, etc., and the open upper end side is inserted into the locking hole 15a of the bottom wall 15 of the heat exchanger shell 1, and the insertion portion The middle and lower portions are enlarged in diameter 21 a and the upper peripheral edge of the stainless steel pipe 20 is welded 7 to be fixed to the bottom wall 15. In addition, an annular recess 15 b that allows an enlarged diameter 21 a of the outer tube 21 is formed on the inner periphery of the locking hole 15 a of the bottom wall 15.

一方、各伝熱管2の内管22は、フッ素系樹脂FEP製の可撓性チューブからなり、上下両端が開放しており、分室13,14内に延出した各上端部がヘッダー31〜34の内空間30と分室13,14内とを遮断する仕切板6の取付孔6aに挿通され、その先端外周部をフッ素系樹脂PFAによる樹脂溶接53によって該仕切板6に固着している。また、底壁15の底面を含む熱交換器シェル1の接ガス部表面には、フッ素系樹脂PFAのコーティング52が施されている。   On the other hand, the inner tube 22 of each heat transfer tube 2 is made of a flexible tube made of fluororesin FEP, and both upper and lower ends are open, and each upper end portion extending into the compartments 13 and 14 has headers 31 to 34. The inner space 30 and the compartments 13 and 14 are inserted into the mounting holes 6a of the partition plate 6, and the outer peripheral portion of the tip is fixed to the partition plate 6 by resin welding 53 using a fluororesin PFA. The surface of the gas contact portion of the heat exchanger shell 1 including the bottom surface of the bottom wall 15 is coated with a fluorine resin PFA coating 52.

なお、図5に示すように、仕切板6は、ステンレス鋼板の表面にフッ素系樹脂PFAのコーティング54を施したものからなり、熱交換器シェル1の側壁部13a,14aに設けた開口部1aの外側周縁に固着された環状補強板17と、各ヘッダー31〜34のカップ部材35の周縁フランジ部35aとの間で周辺部を挟着され、その挟着部分をボルト止めすることで該開口部1aに着脱可能に取り付けられている。   As shown in FIG. 5, the partition plate 6 is made of a stainless steel plate having a fluorine resin PFA coating 54 on the surface thereof, and an opening 1 a provided in the side wall portions 13 a and 14 a of the heat exchanger shell 1. The peripheral portion is clamped between the annular reinforcing plate 17 fixed to the outer peripheral edge of the plate and the peripheral flange portion 35a of the cup member 35 of each header 31 to 34, and the opening is secured by bolting the clamped portion. The unit 1a is detachably attached.

上記構成の排ガス用熱交換器にあっては、図2で示すように、熱交換部が入口側から出口側へ4つの領域Z1〜Z4に分かれる形になり、入口ヘッダー31に導入された冷水W1は、上流側分室13における入口ヘッダー31側半部の領域Z1において、該入口ヘッダー31に接続した各伝熱管2の内管22内に分配流入し、その下端から流出して外管21の内側を上昇して該上流側分室13内へ流出する。次いで、該上流側分室13の接続ヘッダー33側半部の領域Z2において、各伝熱管2の外管21内に分配流入し、その下端内部から内管22内へ流入して上昇し、これら内管22を通して接続ヘッダー33内へ流入して通水管路4へ導出される。続いて、下流側分室14における接続ヘッダー34側半部の領域Z3において、通水管路4を通って接続ヘッダー34から接続した各伝熱管2の内管22内に分配流入し、その下端から流出して外管21の内側を上昇して該下流側分室14内へ流出する。更に、該下流側分室14の出口ヘッダー32側半部の領域Z4において、各伝熱管2の外管21内に分配流入し、その下端内部から内管22内へ流入して上昇し、これら内管22を通して出口ヘッダー32内へ流入する。   In the exhaust gas heat exchanger configured as described above, as shown in FIG. 2, the heat exchange part is divided into four regions Z1 to Z4 from the inlet side to the outlet side, and cold water introduced into the inlet header 31 is formed. W1 distributes and flows into the inner pipe 22 of each heat transfer pipe 2 connected to the inlet header 31 in the region Z1 on the inlet header 31 side half in the upstream side compartment 13 and flows out from the lower end of the outer pipe 21. The inside rises and flows into the upstream compartment 13. Next, in the region Z2 on the connection header 33 side half of the upstream side chamber 13, it flows into the outer tube 21 of each heat transfer tube 2, flows into the inner tube 22 from the lower end inside, and rises. It flows into the connection header 33 through the pipe 22 and is led out to the water conduit 4. Subsequently, in the area Z3 on the side of the connection header 34 in the downstream side compartment 14, it flows into the inner pipe 22 of each heat transfer pipe 2 connected from the connection header 34 through the water conduit 4, and flows out from its lower end. As a result, the inside of the outer tube 21 rises and flows into the downstream compartment 14. Further, in the region Z4 on the outlet header 32 side half portion of the downstream side compartment 14, it distributes and flows into the outer pipe 21 of each heat transfer pipe 2, flows into the inner pipe 22 from the lower end inside thereof, rises, It flows into the outlet header 32 through the tube 22.

すなわち、入口ヘッダー31に導入された冷水W1は、4つの領域Z1〜Z4の各々で伝熱管2内を1往復し、排ガスダクト10内を計4往復する過程での高温排ガスG1との熱交換により、昇温した温水W2として該出口ヘッダー32から導出される。なお、図3は、熱交換の操作線を示しており、導入された冷水W1が各領域Z1〜Z4を順次経る過程で段階的に昇温して温水W2として導出する一方、高温排ガスG1は逆に領域Z4→Z1を通過することで連続的に降温して低温排ガスG2として下流側へ移行する。   In other words, the cold water W1 introduced into the inlet header 31 reciprocates once in the heat transfer tube 2 in each of the four regions Z1 to Z4 and exchanges heat with the high-temperature exhaust gas G1 in the process of reciprocating four times in the exhaust gas duct 10 in total. Thus, the heated water W2 having been heated is led out from the outlet header 32. In addition, FIG. 3 has shown the operating line of heat exchange, and while the introduced cold water W1 goes through each area | region Z1-Z4 sequentially, it heats up in steps and derives as hot water W2, while high temperature exhaust gas G1 is On the other hand, the temperature is continuously lowered by passing through the region Z4 → Z1, and moves to the downstream side as the low temperature exhaust gas G2.

なお、図1に示すように、排ガスダクト10内に配設された洗浄水ノズル8は、洗浄水W3の噴射によって伝熱管2の表面に付着したダストを洗い流し、もって付着ダストに起因した熱交換効率の低下を防止するものである。しかして、この洗浄後のダストを含む洗浄水W4は該伝熱管2の配置部の下方の水溜まり部10aに溜まり、その溜まり量を超える分がオーバーフロー管9を通して排出されるが、その溜まった洗浄水W4中に各伝熱管2の下端部が浸漬しているから、該伝熱管2内での沸騰が防止され、その沸騰に伴う伝熱管2の膨張で表面のフッ素系樹脂のコーティング層51が破壊されるのを回避できる。   In addition, as shown in FIG. 1, the washing water nozzle 8 disposed in the exhaust gas duct 10 flushes the dust adhering to the surface of the heat transfer tube 2 by the jetting of the washing water W3, and thereby heat exchange caused by the adhering dust. This prevents a decrease in efficiency. Accordingly, the cleaning water W4 containing the dust after the cleaning is accumulated in the water reservoir 10a below the arrangement portion of the heat transfer tube 2, and the excess amount is discharged through the overflow pipe 9, but the accumulated cleaning is performed. Since the lower ends of the heat transfer tubes 2 are immersed in the water W4, boiling in the heat transfer tubes 2 is prevented, and the coating layer 51 of the fluororesin on the surface is formed by expansion of the heat transfer tubes 2 accompanying the boiling. You can avoid being destroyed.

このような排ガス用熱交換器によれば、二重管状の各伝熱管2は、外管21の外面にフッ素系樹脂のコーティング51が施され、内管22がフッ素系樹脂の可撓性チューブからなり、また熱交換器シェル1の接ガス表面にもフッ素系樹脂のコーティング51が施されているため、優れた耐酸腐食性を具備し、亜硫酸ガス及び硫酸ガスを含む高温の燃焼排ガスG1を熱交換対象として、長期にわたって高い熱交換効率が得られる。しかも、伝熱管2を点検する際、熱交換器シェル1の天井部をなす蓋板11を取り外すだけで、外管21及び内管22の止着部分が露呈するから、各内管22を外管21から抜出することにより、内外管22,21の状態を目視によって簡単に確認できると共に、内外管22,21に破損や劣化等の欠陥が発見された場合の補修や交換の作業も容易に能率よく行える。また、熱交換器シェル1自体は、内部が仕切壁12によって上流側分室13と下流側分室14とに区割されているだけであるから、構造的に簡素であって安価に製作できるという利点がある。   According to such a heat exchanger for exhaust gas, each double-tubular heat transfer tube 2 is coated with a fluororesin coating 51 on the outer surface of the outer tube 21, and the inner tube 22 is a flexible tube made of a fluororesin. In addition, since the gas contact surface of the heat exchanger shell 1 is also coated with a fluorine-based resin coating 51, it has excellent acid corrosion resistance, and a high-temperature combustion exhaust gas G1 containing sulfurous acid gas and sulfuric acid gas is provided. As a heat exchange target, high heat exchange efficiency can be obtained over a long period of time. In addition, when the heat transfer tubes 2 are inspected, the fixing portions of the outer tube 21 and the inner tube 22 are exposed only by removing the cover plate 11 that forms the ceiling of the heat exchanger shell 1. By pulling out from the tube 21, the state of the inner and outer tubes 22, 21 can be easily confirmed visually, and repair and replacement work is easily performed when defects such as breakage or deterioration are found in the inner and outer tubes 22, 21. Can be done efficiently. Further, since the heat exchanger shell 1 itself is only divided into the upstream compartment 13 and the downstream compartment 14 by the partition wall 12, it is structurally simple and can be manufactured at low cost. There is.

また、実施形態の構成では、各ヘッダー31〜34の内空間30と分室13,14との間に介在する仕切板6に、各ヘッダー31〜34毎に対応する内管22群が一体化しているから、前記点検に際し、該仕切板6を引くことで内管22群を各々の外管21から一挙に抜出でき、それだけ作業性が向上すると共に、各内管22の上端部が該仕切板6に対して熱可塑性フッ素系樹脂によって溶接53されているから、その溶接部の加熱溶融によって該内管22の交換を容易に行える。   In the configuration of the embodiment, the inner pipe 22 group corresponding to each header 31 to 34 is integrated with the partition plate 6 interposed between the inner space 30 of each header 31 to 34 and the compartments 13 and 14. Therefore, at the time of the inspection, the inner pipe 22 group can be pulled out from each outer pipe 21 at a stroke by pulling the partition plate 6, and the workability is improved accordingly, and the upper end portion of each inner pipe 22 is connected to the partition. Since the plate 6 is welded 53 with thermoplastic fluororesin, the inner tube 22 can be easily replaced by heating and melting the welded portion.

本発明の排ガス用熱交換器では、熱交換器シェル1内を実施形態の如く上流側分室13と下流側分室14とに2区割する構成に限らず、3区割以上として、その隣接する上流側の分室と下流側の分室との間を接続ヘッダーを介して通水管路4で連結した構成としてもよい。ただし、実施形態のように2区割する構成では、排ガス用熱交換器として簡素で且つ機能的である上、高い熱交換効率が得られるという利点がある。また、本発明では、熱交換器シェル1とこれより垂下する多数本の伝熱管2とを熱交換ユニットとして、その複数のユニットを排ガスダクト10の大きさや通過ガス量に応じて並設してもよい。   The exhaust gas heat exchanger of the present invention is not limited to the configuration in which the heat exchanger shell 1 is divided into two sections, that is, the upstream compartment 13 and the downstream compartment 14 as in the embodiment. The upstream compartment and the downstream compartment may be connected by a water conduit 4 via a connection header. However, the configuration divided into two sections as in the embodiment has an advantage that it is simple and functional as a heat exchanger for exhaust gas, and high heat exchange efficiency can be obtained. In the present invention, the heat exchanger shell 1 and the multiple heat transfer tubes 2 depending from the heat exchanger shell 1 are used as a heat exchange unit, and the plurality of units are arranged in parallel according to the size of the exhaust gas duct 10 and the amount of passing gas. Also good.

その他、本発明の排ガス用熱交換器では、熱交換器シェル1の形状、該熱交換器シェル1に対する入口及び出口ヘッダー31,32と接続ヘッダー33,34の取付位置、これらヘッダー31〜34の構造、伝熱管2の本数と配列、該伝熱管2の外管21及び内管22の止着構造、コーティング51,52に用いる熱可塑性フッ素系樹脂の種類等、細部構成については実施形態以外に種々設計変更可能である。   In addition, in the heat exchanger for exhaust gas of the present invention, the shape of the heat exchanger shell 1, the mounting positions of the inlet and outlet headers 31 and 32 and the connection headers 33 and 34 with respect to the heat exchanger shell 1, The structure, the number and arrangement of the heat transfer tubes 2, the fastening structure of the outer tube 21 and the inner tube 22 of the heat transfer tube 2, the type of thermoplastic fluororesin used for the coatings 51 and 52, etc. Various design changes are possible.

1 熱交換器シェル
11 蓋板
12 仕切壁
13 上流側分室
13a 側壁部
14 下流側分室
14a 側壁部
15 底壁
15a 取付孔
2 伝熱管
20 ステンレス鋼パイプ(金属パイプ)
21 外管
22 内管
31 入口ヘッダー
32 出口ヘッダー
33,34 接続ヘッダー
4 通水管路
51 コーティング
53 溶接
6 仕切板
6a 取付孔
10 排ガスダクト
10a 水溜まり部
G1 高温排ガス
G2 低温排ガス
W1 冷水
W2 温水
W3,W4 洗浄水
DESCRIPTION OF SYMBOLS 1 Heat exchanger shell 11 Cover plate 12 Partition wall 13 Upstream side compartment 13a Side wall part 14 Downstream side compartment 14a Side wall part 15 Bottom wall 15a Mounting hole 2 Heat transfer tube 20 Stainless steel pipe (metal pipe)
21 Outer pipe 22 Inner pipe 31 Inlet header 32 Outlet header 33, 34 Connection header 4 Water conduit 51 Coating 53 Welding 6 Partition plate 6a Mounting hole 10 Exhaust gas duct 10a Water reservoir G1 High temperature exhaust gas G2 Low temperature exhaust gas W1 Cold water W2 Hot water W3, W4 Wash water

Claims (4)

燃焼排ガスが横方向に流れる排ガスダクトの天井部に配置する熱交換器シェルと、該熱交換器シェルから垂下する多数本の伝熱管とを備え、
前記熱交換器シェルは、天井部が着脱可能な蓋板にて構成され、内部が仕切壁によって複数の分室に区割され、最上流側の分室に臨む入口ヘッダーと最下流側の分室に臨む出口ヘッダーとを備えると共に、隣接する上流側の分室と下流側の分室との間に各々接続ヘッダーを介して通水管路が接続され、
前記伝熱管は、外面にフッ素系樹脂のコーティングが施されて下端を閉塞した金属パイプからなる外管と、この外管内に挿入されて下端が開放したフッ素系樹脂の可撓性チューブからなる内管とで二重管状をなし、その複数本ずつが前記入口ヘッダー及び出口ヘッダーと各接続ヘッダーに各々対応する群を構成し、
各伝熱管の前記外管は、上端部が前記分室の底壁に設けた取付孔に気密に挿嵌固定されて、その内部が該分室内に連通し、
該伝熱管における前記内管は、上部側が前記分室内に延出されて前記群毎に集合して対応するヘッダーに連通し、
入口ヘッダーより導入された冷水が、二重管状の各伝熱管内を往復しつつ前記熱交換器シェルの各分室を経て出口ヘッダーに至る過程で、排ガスダクト内を流れる高温の燃焼排ガスと熱交換して該出口ヘッダーより温水として導出すると共に、該熱交換によって燃焼排ガスを低温化するように構成されてなる排ガス用熱交換器。
A heat exchanger shell disposed on a ceiling portion of an exhaust gas duct in which combustion exhaust gas flows laterally, and a plurality of heat transfer tubes hanging from the heat exchanger shell,
The heat exchanger shell is composed of a cover plate with a detachable ceiling, and the interior is divided into a plurality of compartments by a partition wall, and faces an inlet header facing the most upstream compartment and a most downstream compartment. An outlet header, and a water conduit is connected between each of the adjacent upstream and downstream compartments via a connection header,
The heat transfer tube is composed of an outer tube made of a metal pipe whose outer surface is coated with a fluorine resin and closed at the lower end, and an inner tube made of a fluorine resin flexible tube inserted into the outer tube and having the lower end opened. A pipe and a double tube, each of which constitutes a group corresponding to each of the inlet header and outlet header and each connection header;
The outer tube of each heat transfer tube is hermetically inserted and fixed in a mounting hole provided in the bottom wall of the compartment, and the inside communicates with the compartment.
The inner pipe of the heat transfer pipe has an upper side extending into the branch chamber and is assembled for each group and communicates with a corresponding header,
The cold water introduced from the inlet header exchanges heat with the high-temperature combustion exhaust gas flowing in the exhaust gas duct in the process of reciprocating in each double-tube heat transfer tube and passing through each compartment of the heat exchanger shell to the outlet header. Then, the exhaust gas heat exchanger is configured to be led out as hot water from the outlet header and to reduce the temperature of the combustion exhaust gas by the heat exchange.
前記各ヘッダーの内空間と前記分室との間に仕切板が介在し、該仕切板に設けた取付孔に前記伝熱管における各内管の上端部が挿嵌され、この挿嵌部分が熱可塑性フッ素系樹脂によって溶接されてなる請求項1に記載の排ガス用熱交換器。   A partition plate is interposed between the inner space of each header and the compartment, and an upper end portion of each inner tube in the heat transfer tube is inserted into a mounting hole provided in the partition plate, and this insertion portion is thermoplastic. The heat exchanger for exhaust gas according to claim 1, which is welded with a fluorine-based resin. 前記熱交換器シェル内が上流側分室と下流側分室とに2区割され、上流側分室の側壁部に前記入口ヘッダーと前記通水管路の一端側の接続ヘッダーが設けられると共に、下流側分室の側壁部に前記出口ヘッダーと前記通水管路の他端側の接続ヘッダーが設けられてなる請求項1又は2に記載の排ガス用熱交換器。   The inside of the heat exchanger shell is divided into an upstream compartment and a downstream compartment, and the inlet header and a connection header on one end side of the water conduit are provided on the side wall of the upstream compartment, and the downstream compartment The heat exchanger for exhaust gas according to claim 1 or 2, wherein a connection header on the other end side of the outlet header and the water conduit is provided on a side wall portion of the exhaust gas. 前記排ガスダクト内における前記伝熱管の配置部よりも上流側に、該伝熱管に対して洗浄水を噴射する洗浄水ノズルが配設されると共に、該伝熱管の配置部の下方に水溜まり部が設けられ、この水溜まり部に溜まった洗浄水中に各伝熱管の下端部が浸漬されてなる請求項1〜3のいずれかに記載の排ガス用熱交換器。   A cleaning water nozzle for injecting cleaning water to the heat transfer tube is disposed upstream of the heat transfer tube arrangement portion in the exhaust gas duct, and a water reservoir is provided below the heat transfer tube arrangement portion. The exhaust gas heat exchanger according to any one of claims 1 to 3, wherein a lower end portion of each heat transfer tube is immersed in the wash water provided and stored in the water reservoir.
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KR20200088610A (en) * 2019-01-15 2020-07-23 비에이치아이 주식회사 Bundle Header for Gas Preheater

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