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JP7183035B2 - air heater - Google Patents
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JP7183035B2 - air heater - Google Patents

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JP7183035B2
JP7183035B2 JP2018245143A JP2018245143A JP7183035B2 JP 7183035 B2 JP7183035 B2 JP 7183035B2 JP 2018245143 A JP2018245143 A JP 2018245143A JP 2018245143 A JP2018245143 A JP 2018245143A JP 7183035 B2 JP7183035 B2 JP 7183035B2
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tube sheet
upstream tube
heat
air heater
upstream
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JP2020106202A (en
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哲也 近藤
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Kawasaki Motors Ltd
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Kawasaki Jukogyo KK
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

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  • Details Of Heat-Exchange And Heat-Transfer (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Description

本発明は、腐食性ガスによって空気を加熱する空気加熱器に関する。 The present invention relates to an air heater that heats air with corrosive gas.

従来から、ごみ焼却炉やボイラなどの設備から排出される比較的に高温の排ガスを利用して空気を加熱する空気加熱器が知られている。例えば、特許文献1には、排ガスが流れる流路を挟んで対向する上流管板および下流管板と、それらの上流管板と下流管板とに跨って延びる複数の伝熱管を含む空気加熱器(特許文献1では空気予熱器と称呼)が開示されている。 2. Description of the Related Art Conventionally, there has been known an air heater that heats air using relatively high-temperature exhaust gas discharged from equipment such as a waste incinerator and a boiler. For example, Patent Document 1 discloses an air heater that includes an upstream tube sheet and a downstream tube sheet that face each other across a flow path through which exhaust gas flows, and a plurality of heat transfer tubes that extend across the upstream tube sheet and the downstream tube sheet. (referred to as an air preheater in Patent Document 1) is disclosed.

特許文献1に開示された空気加熱器では、上流管板に面する空間が入口ダクトで覆われ、下流管板に面する空間が出口ダクトで覆われている。入口ダクト内には空気が導入され、その空気は上述した伝熱管内を通って出口ダクトまで流れる。 In the air heater disclosed in Patent Document 1, the space facing the upstream tube sheet is covered with an inlet duct, and the space facing the downstream tube sheet is covered with an outlet duct. Air is introduced into the inlet duct and flows through the above-described heat transfer tubes to the outlet duct.

特開2007-285606号公報Japanese Patent Application Laid-Open No. 2007-285606

しかしながら、上述したような構造の空気加熱器では、入口ダクト内に導入される空気が比較的に低温であるため、上流管板と下流管板との間の流路を流れる排ガスが腐食性ガスである場合には、上流管板および伝熱管の上流管板側の端部が低温腐食を起こす。 However, in the air heater having the structure described above, since the air introduced into the inlet duct is relatively low temperature, the exhaust gas flowing through the passage between the upstream tube sheet and the downstream tube sheet is a corrosive gas. , cold corrosion occurs in the upstream tube sheet and the ends of the heat transfer tubes on the upstream tube sheet side.

そこで、本発明は、上流管板および伝熱管の上流管板側の端部が低温腐食を起こすことを抑制することができる空気加熱器を提供することを目的とする。 SUMMARY OF THE INVENTION Accordingly, it is an object of the present invention to provide an air heater capable of suppressing low-temperature corrosion of the upstream tube sheet and the ends of the heat transfer tubes on the upstream tube sheet side.

前記課題を解決するために、本発明の空気加熱器は、腐食性ガスによって空気を加熱する空気加熱器であって、腐食性ガスが流れる流路を挟んで互いに対向する上流管板および下流管板と、前記上流管板と前記下流管板とに跨って延びる複数の伝熱管と、前記上流管板に面する空間を覆う入口ダクトと、前記複数の伝熱管の間で前記上流管板に取り付けられた吸熱板と、を備える、ことを特徴とする。 In order to solve the above-described problems, an air heater of the present invention is an air heater that heats air with a corrosive gas, and includes an upstream tube sheet and a downstream tube facing each other across a flow path through which the corrosive gas flows. a plate, a plurality of heat transfer tubes extending across the upstream tube sheet and the downstream tube sheet, an inlet duct covering a space facing the upstream tube sheet, and between the plurality of heat transfer tubes to the upstream tube sheet. and an attached heat absorbing plate.

上記の構成によれば、伝熱管の間で上流管板に吸熱板が取り付けられているので、腐食性ガスの熱を吸熱板を介して上流管板に伝達することができる。これにより、入口ダクト内に導入された空気を積極的に加熱することができる。従って、上流管板および伝熱管の上流管板側の端部が低温腐食を起こすことを抑制することができる。 According to the above configuration, since the heat absorbing plate is attached to the upstream tube sheet between the heat transfer tubes, the heat of the corrosive gas can be transferred to the upstream tube sheet via the heat absorbing plate. Thereby, the air introduced into the inlet duct can be actively heated. Therefore, it is possible to suppress the occurrence of low-temperature corrosion in the upstream tube sheet and the ends of the heat transfer tubes on the upstream tube sheet side.

前記入口ダクト内には、当該入口ダクト内に導入された空気を、前記上流管板における前記吸熱板が取り付けられた部分へ吹き付けるノズルを形成するノズル構造体が設けられていてもよい。この構成によれば、入口ダクト内に導入された空気をより効果的に加熱することができる。 A nozzle structure may be provided in the inlet duct that forms a nozzle for blowing the air introduced into the inlet duct onto a portion of the upstream tube sheet to which the heat absorption plate is attached. According to this configuration, the air introduced into the inlet duct can be heated more effectively.

前記吸熱板は、前記上流管板に着脱可能に取り付けられていてもよい。この構成によれば、吸熱板が低温腐食を起こしたときには、吸熱板を交換することができる。特に、入口ダクト内に上記のノズル構造体が設けられている場合には、吸熱板の温度が低くなって吸熱板に低温腐食が起きやすい。従って、吸熱板が上流管板に対して着脱可能であることは、入口ダクト内に上記のノズル構造体が設けられている場合に特に有効である。 The heat absorption plate may be detachably attached to the upstream tube sheet. According to this configuration, the heat absorbing plate can be replaced when low-temperature corrosion occurs in the heat absorbing plate. In particular, when the above-mentioned nozzle structure is provided in the inlet duct, the temperature of the heat absorbing plate becomes low and low temperature corrosion tends to occur in the heat absorbing plate. Therefore, the detachability of the heat absorbing plate from the upstream tube sheet is particularly effective when the nozzle structure is provided in the inlet duct.

前記吸熱板の前記上流管板側の端部には、当該吸熱板の厚さ方向の両側に突出する一対の突起が設けられており、前記上流管板には、当該上流管板との間に前記一対の突起が挿入される溝を形成する一対の押え部材が設けられていてもよい。この構成によれば、吸熱板の上流管板への取り付けおよび上流管板からの取り外しを容易に行うことができる。 A pair of protrusions protruding to both sides in the thickness direction of the heat absorption plate is provided at the end of the heat absorption plate on the upstream tube sheet side, and the upstream tube sheet has a gap between the upstream tube sheet and the upstream tube sheet. may be provided with a pair of pressing members forming grooves into which the pair of projections are inserted. According to this configuration, the heat absorbing plate can be easily attached to and removed from the upstream tube sheet.

本発明によれば、上流管板および伝熱管の上流管板側の端部が低温腐食を起こすことを抑制することができる。 ADVANTAGE OF THE INVENTION According to this invention, it can suppress that the edge part by the side of an upstream tube sheet and a heat exchanger tube causes low-temperature corrosion.

本発明の一実施形態に係る空気加熱器の横断面図である。1 is a cross-sectional view of an air heater according to one embodiment of the present invention; FIG. 図1のII-II線に沿った縦断面図である。FIG. 2 is a longitudinal sectional view taken along line II-II of FIG. 1; 上流管板に対する吸熱板の取り付け部分の拡大図である。FIG. 4 is an enlarged view of a portion where the heat absorption plate is attached to the upstream tube sheet;

図1および図2に、本発明の一実施形態に係る空気加熱器1を示す。この空気加熱器1は、腐食性ガスと空気との間で熱交換を行い、腐食性ガスによって空気を加熱するものである。 1 and 2 show an air heater 1 according to one embodiment of the present invention. This air heater 1 performs heat exchange between corrosive gas and air, and heats the air with the corrosive gas.

具体的に、空気加熱器1は、腐食性ガスが流れる流路10を形成する筒状の本体2と、本体2に接続された空気用の入口ダクト4および出口ダクト6を含む。 Specifically, the air heater 1 comprises a tubular body 2 forming a flow path 10 for the corrosive gas, and an inlet duct 4 and an outlet duct 6 for air connected to the body 2 .

本体2は、流路10を挟んで互いに対向する上流管板21および下流管板22と、上流管板21と下流管板22の端部同士を連結する一対の側板23を含む。本実施形態では、腐食性ガスの流れ方向(すなわち筒状の本体2の軸方向)が鉛直方向である。ただし、腐食性ガスの流れ方向は水平方向や斜め方向であってもよい。 The main body 2 includes an upstream tube sheet 21 and a downstream tube sheet 22 facing each other across the flow path 10 and a pair of side plates 23 connecting the ends of the upstream tube sheet 21 and the downstream tube sheet 22 . In this embodiment, the direction of flow of the corrosive gas (that is, the axial direction of the tubular main body 2) is the vertical direction. However, the direction of flow of the corrosive gas may be horizontal or oblique.

以下では、説明の便宜上、上流管板21と下流管板22とが対向する方向を前後方向、側板23同士が対向する方向を左右方向という。 Hereinafter, for convenience of explanation, the direction in which the upstream tube sheet 21 and the downstream tube sheet 22 face each other is called the front-rear direction, and the direction in which the side plates 23 face each other is called the left-right direction.

本体2は、前後方向に延びる複数の伝熱管3によって貫通されている。つまり、伝熱管3は、上流管板21と下流管板22とに跨って延びていてそれらに溶接されている。伝熱管3の熱伸びに対応するために、各側板23の両端部には段差部が形成されている。 The main body 2 is penetrated by a plurality of heat transfer tubes 3 extending in the front-rear direction. That is, the heat transfer tubes 3 extend across the upstream tube sheet 21 and the downstream tube sheet 22 and are welded to them. Stepped portions are formed at both ends of each side plate 23 in order to accommodate thermal expansion of the heat transfer tubes 3 .

本実施形態では、伝熱管3が前後方向から見てマトリクス状に配置されている。図例では、伝熱管3が左右方向に8列、上下方向に8列で配置されているが、伝熱管3の左右方向および上下方向の列数は適宜変更可能である。ただし、伝熱管3は千鳥状に配置されてもよい。 In this embodiment, the heat transfer tubes 3 are arranged in a matrix when viewed from the front-rear direction. In the illustrated example, the heat transfer tubes 3 are arranged in 8 rows in the horizontal direction and 8 rows in the vertical direction, but the number of rows of the heat transfer tubes 3 in the horizontal direction and the vertical direction can be changed as appropriate. However, the heat transfer tubes 3 may be arranged in a zigzag pattern.

上述した入口ダクト4は、上流管板21に面する空間を覆っており、出口ダクト6は、下流管板22に面する空間を覆っている。入口ダクト4内には空気が導入され、その空気は伝熱管3内を通って出口ダクト6まで流れる。 The inlet duct 4 described above covers the space facing the upstream tube sheet 21 , and the outlet duct 6 covers the space facing the downstream tube sheet 22 . Air is introduced into the inlet duct 4 and flows through the heat transfer tubes 3 to the outlet duct 6 .

本実施形態では、入口ダクト4の流入口および出口ダクト6の流出口が左右方向に沿って開口している。ただし、入口ダクト4の流入口および出口ダクト6の流出口は、前後方向に沿って開口してもよい。 In this embodiment, the inlet of the inlet duct 4 and the outlet of the outlet duct 6 are opened along the horizontal direction. However, the inlet of the inlet duct 4 and the outlet of the outlet duct 6 may be opened along the front-rear direction.

本体2内には、複数の吸熱板7が設けられている。本実施形態では、吸熱板7が腐食性ガスの流れ方向(本実施形態では鉛直方向)と平行となるように配置されている。ただし、吸熱板7は、腐食性ガスの流れ方向と直交するように配置されてもよい。そして、吸熱板7は、伝熱管3の間で上流管板21に取り付けられている。 A plurality of heat absorbing plates 7 are provided inside the main body 2 . In this embodiment, the heat absorption plate 7 is arranged so as to be parallel to the flow direction of the corrosive gas (the vertical direction in this embodiment). However, the heat absorbing plate 7 may be arranged so as to be perpendicular to the flow direction of the corrosive gas. The heat absorption plate 7 is attached to the upstream tube sheet 21 between the heat transfer tubes 3 .

本実施形態では、隣り合う伝熱管3の間に1つおきに吸熱板7が存在するように、合計4つの吸熱板7が設けられている。ただし、吸熱板7の数は適宜変更可能である。例えば、左右方向における伝熱管3のピッチの3倍のピッチで吸熱板7が設けられてもよい。あるいは、吸熱板7の数は1つであってもよい。 In the present embodiment, a total of four heat absorption plates 7 are provided such that heat absorption plates 7 are provided alternately between adjacent heat transfer tubes 3 . However, the number of heat absorbing plates 7 can be changed as appropriate. For example, the heat absorption plates 7 may be provided at a pitch three times the pitch of the heat transfer tubes 3 in the left-right direction. Alternatively, the number of heat absorbing plates 7 may be one.

前後方向における吸熱板7の長さは適宜決定可能であるが、例えば、上流管板21と下流管板22との間の距離の半分程度であってもよい。また、上下方向における吸熱板7の長さも適宜決定可能であるが、例えば、全ての伝熱管3の配置範囲よりも長く設定されてもよい。 The length of the heat absorption plate 7 in the front-rear direction can be determined as appropriate, but may be, for example, approximately half the distance between the upstream tube sheet 21 and the downstream tube sheet 22 . Also, the length of the heat absorbing plate 7 in the vertical direction can be determined as appropriate.

本実施形態では、各吸熱板7が、上流管板21に着脱可能に取り付けられる。ただし、各吸熱板7は、必ずしも上流管板21に対して着脱可能である必要はなく、上流管板21に溶接で固定されてもよい。 In this embodiment, each heat absorption plate 7 is detachably attached to the upstream tube sheet 21 . However, each heat absorption plate 7 does not necessarily have to be detachable from the upstream tube sheet 21 and may be fixed to the upstream tube sheet 21 by welding.

具体的には、図3に示すように、各吸熱板7の上流管板21側の端部には、当該吸熱板7の厚さ方向の両側に突出する一対の突起71が設けられている。一方、上流管板21には、各吸熱板7に対して、当該上流管板21との間に突起71が挿入される溝を形成する一対の押え部材8が設けられている。 Specifically, as shown in FIG. 3, a pair of projections 71 projecting to both sides in the thickness direction of the heat absorbing plate 7 is provided at the end of each heat absorbing plate 7 on the upstream tube sheet 21 side. . On the other hand, the upstream tube sheet 21 is provided with a pair of pressing members 8 forming grooves into which the projections 71 are inserted between the respective heat absorbing plates 7 and the upstream tube sheet 21 .

このような構成であれば、各吸熱板7を上流管板21へ取り付ける際および上流管板21から取り外す際には、吸熱板7を上方向または下方向へスライドさせるだけでよい。従って、各吸熱板7の上流管板21への取り付けおよび上流管板21からの取り外しを容易に行うことができる。 With such a configuration, when attaching each heat absorbing plate 7 to the upstream tube sheet 21 or removing it from the upstream tube sheet 21 , it is only necessary to slide the heat absorbing plate 7 upward or downward. Therefore, each heat absorption plate 7 can be easily attached to and removed from the upstream tube sheet 21 .

なお、各吸熱板7から上流管板21へ熱を良好に伝達するという観点からは、突起71は上流管板21に押し付けられることが望ましい。例えば、押え部材8の先端と上流管板21との間の距離を突起71の厚さよりも少しだけ小さく設定し、押え部材8の弾性変形によって突起71を上流管板21に押し付けてもよい。あるいは、押え部材8に、突起71を押圧する切り起こし片を形成してもよい。 From the viewpoint of good heat transfer from each heat absorbing plate 7 to the upstream tube sheet 21 , it is desirable that the projections 71 are pressed against the upstream tube sheet 21 . For example, the distance between the tip of the pressing member 8 and the upstream tube sheet 21 may be set slightly smaller than the thickness of the projection 71 , and the pressing member 8 may be elastically deformed to press the projection 71 against the upstream tube sheet 21 . Alternatively, a cut-and-raised piece that presses the projection 71 may be formed on the pressing member 8 .

図1および図2に戻って、入口ダクト4内にはノズル構造体5が設けられている。ノズル構造体5は、入口ダクト4内に導入された空気を、上流管板21における吸熱板7が取り付けられた部分へ吹き付ける複数のノズル50を形成する。換言すれば、各ノズル50の中心線の延長線上に吸熱板7が存在する。 Returning to FIGS. 1 and 2, a nozzle structure 5 is provided within the inlet duct 4 . The nozzle structure 5 forms a plurality of nozzles 50 for blowing the air introduced into the inlet duct 4 onto the portion of the upstream tube sheet 21 to which the heat absorbing plate 7 is attached. In other words, the heat absorbing plate 7 exists on the extension line of the center line of each nozzle 50 .

本実施形態では、ノズル50の数が吸熱板7の数と同数であり、左右方向に並んでいる。各ノズル50は、前後方向から見たときに上下方向に長い長方形状の開口である。ただし、ノズル50は、吸熱板7と同一のピッチで左右方向に並ぶ複数の線上に配置された複数の穴であってもよい。 In this embodiment, the number of nozzles 50 is the same as the number of heat absorbing plates 7, and they are arranged in the horizontal direction. Each nozzle 50 is a rectangular opening elongated in the vertical direction when viewed from the front-rear direction. However, the nozzles 50 may be a plurality of holes arranged on a plurality of lines arranged in the horizontal direction at the same pitch as the heat absorbing plates 7 .

より詳しくは、ノズル構造体5は、各ノズル50を挟んで離間する第1ガイド51および第2ガイド52を含む。本実施形態では、上述したように入口ダクト4の流入口が左右方向に沿って開口しているために、第1ガイド51と第2ガイド52のうちの流入口と反対側に位置する第2ガイド52は、対応するノズル50に空気を誘い込む役割を果たす。 More specifically, the nozzle structure 5 includes a first guide 51 and a second guide 52 spaced apart with each nozzle 50 therebetween. In this embodiment, since the inlet of the inlet duct 4 is opened along the left-right direction as described above, the second guide 51 and the second guide 52 located on the opposite side of the inlet of the first guide 51 and the second guide 52 Guides 52 serve to guide air to corresponding nozzles 50 .

以上説明したように、本実施形態の空気加熱器1では、伝熱管3の間で上流管板21に吸熱板7が取り付けられているので、腐食性ガスの熱を吸熱板7を介して上流管板21に伝達することができる。これにより、入口ダクト4内に導入された空気を積極的に加熱することができる。従って、上流管板21および伝熱管3の上流管板21側の端部が低温腐食を起こすことを抑制することができる。 As described above, in the air heater 1 of the present embodiment, the heat absorption plate 7 is attached to the upstream tube sheet 21 between the heat transfer tubes 3, so that the heat of the corrosive gas is transferred to the upstream through the heat absorption plate 7. It can be transmitted to the tube sheet 21 . Thereby, the air introduced into the inlet duct 4 can be actively heated. Therefore, the upstream tube sheet 21 and the ends of the heat transfer tubes 3 on the upstream tube sheet 21 side can be prevented from being subjected to low-temperature corrosion.

さらに、本実施形態では、各吸熱板7が上流管板21に対して着脱可能であるので、
吸熱板7が低温腐食を起こしたときには、吸熱板7を交換することができる。特に、本実施形態のように入口ダクト4内にノズル構造体5が設けられている場合には、各ノズル50から上流管板21へ吹き付けられる空気によって対応する吸熱板7が上流管板21を介して冷却されるため、各吸熱板7の温度が低くなって吸熱板7に低温腐食が起きやすい。従って、各吸熱板7が上流管板21に対して着脱可能であることは、入口ダクト4内にノズル構造体5が設けられている場合に特に有効である。
Furthermore, in this embodiment, each heat absorbing plate 7 is detachable from the upstream tube plate 21,
When the heat absorbing plate 7 causes low temperature corrosion, the heat absorbing plate 7 can be replaced. In particular, when the nozzle structure 5 is provided in the inlet duct 4 as in the present embodiment, the air blown from each nozzle 50 toward the upstream tube sheet 21 causes the corresponding heat absorption plate 7 to move the upstream tube sheet 21. Since the temperature of each heat absorbing plate 7 is lowered, low-temperature corrosion of the heat absorbing plate 7 is likely to occur. Therefore, the detachability of each heat absorbing plate 7 from the upstream tube plate 21 is particularly effective when the nozzle structure 5 is provided inside the inlet duct 4 .

(変形例)
本発明は上述した実施形態に限定されるものではなく、本発明の要旨を逸脱しない範囲で種々の変形が可能である。
(Modification)
The present invention is not limited to the embodiments described above, and various modifications are possible without departing from the gist of the present invention.

例えば、入口ダクト4内にはノズル構造体5が設けられなくてもよい。ただし、前記実施形態のようにノズル構造体5が設けられていれば、入口ダクト4内に導入された空気が上流管板21における吸熱板7が取り付けられた部分に衝突した後に伝熱管3内に流入する。従って、ノズル構造体5が設けられない場合に比べて、入口ダクト4内に導入された空気をより効果的に加熱することができる。 For example, no nozzle structure 5 may be provided in the inlet duct 4 . However, if the nozzle structure 5 is provided as in the above embodiment, the air introduced into the inlet duct 4 collides with the portion of the upstream tube sheet 21 where the heat absorbing plate 7 is attached, and then flow into Therefore, compared to the case where the nozzle structure 5 is not provided, the air introduced into the inlet duct 4 can be heated more effectively.

1 空気加熱器
10 流路
21 上流管板
22 下流管板
3 伝熱管
4 入口ダクト
5 ノズル構造体
7 吸熱板
71 突起
8 押え部材
REFERENCE SIGNS LIST 1 air heater 10 flow path 21 upstream tube sheet 22 downstream tube sheet 3 heat transfer tube 4 inlet duct 5 nozzle structure 7 heat absorbing plate 71 projection 8 pressing member

Claims (4)

腐食性ガスによって空気を加熱する空気加熱器であって、
腐食性ガスが流れる流路を挟んで互いに対向する上流管板および下流管板と、
前記上流管板と前記下流管板とに跨って延びる複数の伝熱管と、
前記上流管板に面する空間を覆う入口ダクトと、
前記複数の伝熱管の間で前記上流管板に取り付けられた吸熱板と、
を備える、空気加熱器。
An air heater that heats air with a corrosive gas,
an upstream tube sheet and a downstream tube sheet facing each other across a flow path through which the corrosive gas flows;
a plurality of heat transfer tubes extending across the upstream tube sheet and the downstream tube sheet;
an inlet duct covering the space facing the upstream tube sheet;
a heat absorption plate attached to the upstream tube sheet between the plurality of heat transfer tubes;
an air heater.
前記入口ダクト内には、当該入口ダクト内に導入された空気を、前記上流管板における前記吸熱板が取り付けられた部分へ吹き付けるノズルを形成するノズル構造体が設けられている、請求項1に記載の空気加熱器。 2. The apparatus according to claim 1, wherein the inlet duct is provided with a nozzle structure that forms a nozzle for blowing air introduced into the inlet duct onto a portion of the upstream tube sheet to which the heat absorption plate is attached. Air heater as described. 前記吸熱板は、前記上流管板に着脱可能に取り付けられている、請求項1または2に記載の空気加熱器。 3. The air heater according to claim 1, wherein said heat absorbing plate is detachably attached to said upstream tube sheet. 前記吸熱板の前記上流管板側の端部には、当該吸熱板の厚さ方向の両側に突出する一対の突起が設けられており、
前記上流管板には、当該上流管板との間に前記一対の突起が挿入される溝を形成する一対の押え部材が設けられている、請求項3に記載の空気加熱器。
A pair of protrusions protruding to both sides in the thickness direction of the heat absorption plate is provided at the end of the heat absorption plate on the upstream tube sheet side,
4. The air heater according to claim 3, wherein the upstream tube sheet is provided with a pair of holding members forming grooves into which the pair of projections are inserted between the upstream tube sheet and the upstream tube sheet.
JP2018245143A 2018-12-27 2018-12-27 air heater Active JP7183035B2 (en)

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Citations (1)

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Publication number Priority date Publication date Assignee Title
US20140352931A1 (en) 2013-05-31 2014-12-04 Steve Turner Corrosion Resistant Air Preheater with Lined Tubes

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JP2705545B2 (en) * 1993-12-14 1998-01-28 日本鋼管株式会社 Low temperature corrosion prevention structure of heat exchanger
JPH11183063A (en) * 1997-12-19 1999-07-06 Abb Kk Plate heat exchanger

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20140352931A1 (en) 2013-05-31 2014-12-04 Steve Turner Corrosion Resistant Air Preheater with Lined Tubes

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