JPS5811302A - Waste heat recovering heat exchanger - Google Patents

Waste heat recovering heat exchanger

Info

Publication number
JPS5811302A
JPS5811302A JP10768681A JP10768681A JPS5811302A JP S5811302 A JPS5811302 A JP S5811302A JP 10768681 A JP10768681 A JP 10768681A JP 10768681 A JP10768681 A JP 10768681A JP S5811302 A JPS5811302 A JP S5811302A
Authority
JP
Japan
Prior art keywords
heat
heat exchanger
heat insulating
exhaust
exhaust gas
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP10768681A
Other languages
Japanese (ja)
Inventor
誠 小川
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP10768681A priority Critical patent/JPS5811302A/en
Publication of JPS5811302A publication Critical patent/JPS5811302A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本*VS紘例えばガスタービンの排ガス中の残留熱を有
効に活用すべく、この熱でもって蒸気タービン用の蒸気
を発生させる;ンΔインPすイクルで発電で使用する排
熱回収熱交換lIIの改爽に関する。
Detailed Description of the Invention: For example, in order to effectively utilize the residual heat in the exhaust gas of a gas turbine, this heat is used to generate steam for a steam turbine; This invention relates to the refreshing of exhaust heat recovery heat exchange III.

コンバインドサイクル発電とは、ガスタービンと蒸気タ
ービンを組み合せることによってプテント効率を高めた
発電シヌテムであシ、このコンバインドすイクル発電と
して種々のサイクルが考えられている。その典型的なサ
イクルとして従来用いられているものについて第1図を
参照にして説明すゐ。
Combined cycle power generation is a power generation system that increases patent efficiency by combining a gas turbine and a steam turbine, and various cycles have been considered as this combined cycle power generation. A typical cycle conventionally used will be explained with reference to FIG.

すなわち、図示し碌い燃焼器によりて作られる高圧高温
O燃焼ガスは、ガスタービン1に流入して、これを高速
で回転させることによって、圧力、温度が低下して排出
される。仁の排気ガ310温度紘、普通Boo 〜60
0℃であるため、この壜ま排気fxとして捨てるOは非
常に不経済である。ζOようなことから設けられたのが
排熱回収熱交換器1である。こO排熱回収熱交換器1#
i、排熱回収熱交換器本体(以下単に本体と称す)1内
に多数の伝熱管4を有し、ガスタービン10高温排気ガ
jEld、本体jに有する入口!タトIを通って本体J
内に強制熱伝達手段によ)送られ、水と排気ガスとO熱
交換管行なうものである。
That is, high-pressure, high-temperature O combustion gas produced by the sophisticated combustor shown in the figure flows into the gas turbine 1 and is rotated at high speed, thereby decreasing its pressure and temperature and being discharged. Jin's exhaust gas temperature 310, normal Boo ~60
Since the temperature is 0°C, the O discarded from this bottle as exhaust air fx is extremely uneconomical. The exhaust heat recovery heat exchanger 1 was provided for this reason. This waste heat recovery heat exchanger 1#
i. The exhaust heat recovery heat exchanger main body (hereinafter simply referred to as the main body) 1 has a large number of heat transfer tubes 4, and the gas turbine 10 high-temperature exhaust gas has an inlet in the main body j! Main body J through Tato I
(by forced heat transfer means) and exchanges water and exhaust gas with O heat exchange tubes.

本体1内に流入した排気ガxd、上方に向つノマイデ8
を通って本体3の出ロダクトクから図示しない煙突へ抜
ける。ここで、蒸発器#およびエコノマイザ8は多数の
伝熱管4によって構成されておシ、この伝熱管4内を蒸
気および水が流れる。エコノマイデIO伝熱管40片側
端は、給水管10に接続しておシ、伝熱管4の他端は、
蒸気ドラム11の下部に接続している。
Exhaust gas xd flowing into the main body 1, Nomide 8 facing upward
It exits through the outlet duct of the main body 3 to a chimney (not shown). Here, the evaporator # and the economizer 8 are constituted by a large number of heat exchanger tubes 4, and steam and water flow inside the heat exchanger tubes 4. One end of the Economide IO heat transfer tube 40 is connected to the water supply pipe 10, and the other end of the heat transfer tube 4 is connected to the water supply pipe 10.
It is connected to the lower part of the steam drum 11.

また、蒸発器6の伝熱管40両端共蒸気ド2五11に取
付けられている。さらに蒸気ドラム11の上端部に主蒸
気管11が接続してお〕、主蒸気管11は蒸気タービン
JJK導ひかれている。
Further, both ends of the heat transfer tube 40 of the evaporator 6 are attached to the steam door 2511. Further, a main steam pipe 11 is connected to the upper end of the steam drum 11], and the main steam pipe 11 is led to a steam turbine JJK.

を九、蒸気タービンIJと連設して復水器14が設置さ
れている。
9. A condenser 14 is installed in series with the steam turbine IJ.

以上の構成において、蒸気タービン12の排気蒸気は、
復水器14にて復水となp1給水ポアfllによって給
水管10からエコノマイザ8へ圧送される。エコノマイ
ザ1で加熱された給水は、蒸気ドラム110下部に流入
する。蒸気ドラム11の饋水は、ドツト−麿部から移送
ポンfl #によりて、蒸発器σに送られ伝熱管4内で
蒸発して蒸気と麦シ再び蒸気ドラム1ノの上部へ戻る。
In the above configuration, the exhaust steam of the steam turbine 12 is
The condensed water is condensed in the condenser 14 and is force-fed to the economizer 8 from the water supply pipe 10 by the p1 water supply pore fll. The feed water heated by the economizer 1 flows into the lower part of the steam drum 110. The water in the steam drum 11 is sent from the bottom of the steam drum 11 to the evaporator σ by the transfer pump fl#, evaporates in the heat transfer tube 4, and returns to the upper part of the steam drum 1 again as steam and barley.

蒸気ドラムll内の蒸気は、この蒸気ドラム11上部か
ら抽出されて、主蒸気管1zから蒸気タービンJJK導
入され、再び復水器14へ流入する。このような構成の
排熱回収形コンバインドサイクル発電プラントでは、高
温のガヌタービン排気が有効に利用されるためにプラン
ト熱効率が、従来よシ数チ上昇することが確認されてい
る。
Steam in the steam drum 11 is extracted from the upper part of the steam drum 11, introduced into the steam turbine JJK from the main steam pipe 1z, and flows into the condenser 14 again. It has been confirmed that in an exhaust heat recovery type combined cycle power plant with such a configuration, the plant thermal efficiency is increased by several orders of magnitude compared to conventional plants because the high-temperature Ganu turbine exhaust gas is effectively used.

以上説明した排熱回収熱交換器1を実際に設置する場合
、第2図に示すように蒸発器C1排ガヌ脱硝装置1、エ
コノマイザ1等は、それぞれ一つの箱形翼ニットとして
、別々に製造、組立てその後令息ニットをフランジ11
を介してIルFにて結合し全体を排熱回収熱交換器架構
1#に据付ける。その際、エルがダクト19や出口ダク
トtも7ツンジ11によって結合される。排熱回収形フ
ンバインドサ′イクル発電!ラントでは、高温ガスター
ビン排気ガスを有効に利用するため、排熱回収熱交換器
を構成する各ユニットの外板10からの放熱を最少限に
することから保温材による保温施工が必要不可欠である
When actually installing the exhaust heat recovery heat exchanger 1 described above, the evaporator C1 exhaust gas denitrification device 1, economizer 1, etc. are each installed separately as one box-shaped blade knit, as shown in Fig. 2. After manufacturing and assembling, the younger knit is flange 11
are connected at IF via IF, and the whole is installed in exhaust heat recovery heat exchanger frame 1#. At this time, the L duct 19 and the outlet duct t are also connected by the seven twisters 11. Exhaust heat recovery type humbind cycle power generation! In order to effectively utilize high-temperature gas turbine exhaust gas, it is essential to use heat insulating materials to minimize heat radiation from the outer panels 10 of each unit that constitutes the exhaust heat recovery heat exchanger. .

この一般的な保温材の施工方法としては、施工がきわめ
て簡単なことから各ユニットの外板20の外側に保温材
を壜付ける外部保温方式が考えられる。しかし、#熱回
収熱交換器2内を流れるガヌタービンの排讐ガヌは、通
常500〜600℃と高温である丸め、1排熱回収熱交
換gSjを構成し、強度部材の一部でもある各二二ッF
の外板1°に排ガスが直接竺れると1、各−一・トの外
板10は排ガス温度に近い500℃位の高温になる。こ
のため、各ユニット外板1#は、同温度域で長時間の使
用が可能であって、かつ十分な強度を有する材料鵞用吟
なければならない。この材料として例えば炭素鋼がある
が、炭素鋼は500℃近くになると機械的強度が極端に
低下し実用に供し見な一欠点がある。このため、機械的
強度の低下を補うKは、板厚を増す必要があ〕、結果的
には重量が増し、省資源に反するばか)で擾く、建設費
も増大する。
As a general method for applying the heat insulating material, an external heat insulating method is considered, in which the heat insulating material is placed in a bottle on the outside of the outer panel 20 of each unit, since the construction is extremely simple. However, the exhaust gas of the Ganu turbine flowing inside the #heat recovery heat exchanger 2 is usually at a high temperature of 500 to 600 degrees Celsius, and each component that constitutes the 1 exhaust heat recovery heat exchange gSj and is also a part of the strength member 22F
When exhaust gas is directly applied to the outer plate 1° of 1, the outer plate 10 of 1, 1 and 1 becomes as high as 500° C., which is close to the temperature of the exhaust gas. Therefore, each unit outer plate 1# must be made of a material that can be used for a long time in the same temperature range and has sufficient strength. Carbon steel is an example of this material, but carbon steel has a drawback in that it is not suitable for practical use because its mechanical strength is extremely reduced when the temperature approaches 500°C. For this reason, it is necessary to increase the plate thickness to compensate for the decrease in mechanical strength, which results in an increase in weight, which goes against the grain of resource conservation, and increases construction costs.

一方前述の材料としてヌテンレヌ鋼があるが、これは前
述の炭素鋼の欠点、を補うことができる反面、きわめて
高価であるため実用的でない。
On the other hand, the above-mentioned material is Nutenrenu steel, which can compensate for the disadvantages of the above-mentioned carbon steel, but is extremely expensive and therefore impractical.

本発明は上記欠点を改善するためKなされたもので、そ
の目的とするところは、各ユニッFの外板の内面に保温
材およびラギングを装着し外板。温度、低門よ保っ員に
6脚素鋼、V使用を可能にし、ラギングの取付穴を大き
くするととKよ〕、外板とラギングとの温度差によるラ
ギングの伸びを容易に吸収し、かつ強度的に十分耐える
転量コンパクトな排熱回収熱交換器を提供することKT
oる。
The present invention has been made in order to improve the above-mentioned drawbacks, and its purpose is to attach heat insulating material and lagging to the inner surface of the outer panel of each unit F. Temperatures are low, making it possible to use 6-legged bare steel for gatekeepers, making the lagging mounting holes larger (K), easily absorbing the elongation of the lagging due to the temperature difference between the outer panel and the lagging, and To provide a compact waste heat recovery heat exchanger with sufficient strength and durability.KT
oru.

以下、本実F!A!第3図に示す一寅施例に基づいて説
明する。なセ第1図および第2図にて説明した部分と同
一の部分には同一の符号を付し、その説明は省略すそ。
Below is Honji F! A! The explanation will be based on the embodiment shown in FIG. The same parts as those explained in FIGS. 1 and 2 are designated by the same reference numerals, and their explanations will be omitted.

WJ3図は本発明による外板20内面の保温材xio取
付部の拡大図を方、したものである。すなわち、排熱回
収熱交換器2を構成する各ユニットの外板2oの内面に
多数の保温材取付ピン21を溶接部によ〕取付ける。保
温材JJKは保温材取付ピン22と同じ位置に取付穴を
設ける。又保温材xiに杜外板20と接する面に耐熱接
着剤JIJtIk布し、保温材取付ピンJJに装着する
。保温材z1の内面にはラギング(保温外被材)24を
設け、この2ギング24が直接、保温材21と接しない
様にワッシャJ5を設ける。又、2ji’ンダJl14
の取付穴は、保温材取付ピン、22の直径よシも大きな
取付穴とし、その上にワッシャ2Jを設け、このワッシ
ャ2jと保温材取付ピン2Jとを溶接することによシ、
保温材111および2ギング24を外板20に固定する
構造となりている。
Figure WJ3 is an enlarged view of the attachment portion of the heat insulating material xio on the inner surface of the outer panel 20 according to the present invention. That is, a large number of heat insulating material attachment pins 21 are attached to the inner surface of the outer plate 2o of each unit constituting the exhaust heat recovery heat exchanger 2 by welding. The heat insulating material JJK has a mounting hole at the same position as the heat insulating material mounting pin 22. In addition, heat-resistant adhesive JIJtIk is applied to the surface of the heat insulating material xi in contact with the forest outer panel 20, and the heat insulating material xi is attached to the heat insulating material mounting pin JJ. Lagging (thermal outer covering material) 24 is provided on the inner surface of the heat insulating material z1, and a washer J5 is provided so that the two laggings 24 do not come into direct contact with the heat insulating material 21. Also, 2ji'anda Jl14
By making the mounting hole larger than the diameter of the insulation material mounting pin 22, installing a washer 2J on it, and welding this washer 2j and the insulation material mounting pin 2J,
It has a structure in which the heat insulating material 111 and the 2-ging 24 are fixed to the outer panel 20.

次にこのように構成された排熱回収熱交換器の作用につ
いて説明する。排熱回収熱交換器11m成する各二二ツ
)0外板goは、この内面に装着した保温材21によ〕
、高温の排気ガスの熱が速断されるため1.外板2−の
温度は常に低温状態になる。一方、外板20の内面に装
着された2ギン114は高温の排気ガスに接している九
め、常に排fil温度が500℃位の状態にな夛、外板
2#との温度差による伸差が生じる。ラギング14と外
板20の温度差によシ生じるツイン110の伸び差は、
ライング200取付大の径を、保温材取付ピン22の径
よシも大きくした取付穴の変位によシ容易に吸収するこ
とが出来る。tた、2ギング14と保温材110間に、
ワッシャ2Jを設けることによシ、ラギング14と保温
材11とに隙間を設はラギング14が伸びた時の保温材
21の摩耗を防止すると共にラギング14の伸び゛を容
易にしている。
Next, the operation of the exhaust heat recovery heat exchanger configured as described above will be explained. Exhaust heat recovery heat exchanger 11m consists of 22 pieces each) 0 outer plate is attached to the inner surface of the heat insulating material 21]
1. Because the heat of the high-temperature exhaust gas is cut off quickly. The temperature of the outer plate 2- is always at a low temperature. On the other hand, the 2nd gear 114 attached to the inner surface of the outer panel 20 is in contact with high-temperature exhaust gas, and the exhaust gas temperature is always around 500°C, causing expansion due to the temperature difference with the outer panel 2#. It makes a difference. The difference in elongation of the twin 110 caused by the temperature difference between the lagging 14 and the outer plate 20 is
The diameter of the line 200 can be easily accommodated by the displacement of the mounting hole, which is also larger than the diameter of the heat insulating material mounting pin 22. Between the 2-ring 14 and the insulation material 110,
By providing the washer 2J, a gap is provided between the lagging 14 and the heat insulating material 11, which prevents wear of the heat insulating material 21 when the lagging 14 is extended, and also facilitates the extension of the lagging 14.

したがりて、外板1#内面に装着した保温材J1および
2イング14は、外板10の温度を低温状態にし、かつ
外板20とラギングJ4の温度差による伸びを吸収する
ことが可能となる。
Therefore, the heat insulating materials J1 and 2 ings 14 attached to the inner surface of the outer panel 1# can keep the temperature of the outer panel 10 at a low temperature and absorb the elongation due to the temperature difference between the outer panel 20 and the lagging J4. Become.

以上、述べた本発明によれば、外板を低温状態にし、外
板と2ギングの温度差による伸びを容易に徴収すること
の出来る排熱回収熱交換器を提供することが出来る。
According to the present invention described above, it is possible to provide an exhaust heat recovery heat exchanger that can bring the outer panel into a low temperature state and easily collect the elongation due to the temperature difference between the outer panel and the second gear.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、排熱回収形コンバインド号イクル発電!ツン
トの概略系統図、第2図は、従来の排熱回収熱交換器の
一例を示す構成図、第3図は本発明による排熱回収熱交
換器の一実施例の保温材取付部分のみを拡大して示す図
である。 1−・ガスタービン、1−・排熱回収熱交換器、3・・
・排熱回収熱交換器本体、4−伝熱管、J−・・入ロダ
!ト、6・・・蒸発器、1.・・・排ガス脱硝装置、8
・・・エコノマイザ、9−・・出口〆クト、10・・・
給水管、11−・蒸気ドラム、12・−主蒸気管、13
・−蒸気タービン 14・−復水器、15・・・給水ポ
ンプ、1#・・・移送4ンプ、17・・・72ンジ、1
8・・・排熱回収熱交換器架構、1#−エルがダク)、
J#−・・各ユニットの外板、Jll−保温材、22−
・保温材取付ピン、11・・・耐熱接着剤、24・・・
2ギング、25−ワッシャ。 第3図 昭和56p−8・J4日 特許庁長官  島田春樹 、殿 1、事件の表示 特願昭56−10了686 号 2、 発明の名称 排熱回収熱交換器 3、補正をする者 事件との関係  特許出願人 αの 東京芝浦電気株式会社 4、代理人 5、自発補正 明細書の浄書(内容に変便なし)
Figure 1 shows exhaust heat recovery type combined cycle power generation! A schematic system diagram of the Zundt, Fig. 2 is a configuration diagram showing an example of a conventional waste heat recovery heat exchanger, and Fig. 3 shows only the heat insulation material attachment part of an embodiment of the waste heat recovery heat exchanger according to the present invention. It is an enlarged view. 1-・Gas turbine, 1-・Exhaust heat recovery heat exchanger, 3.
・Exhaust heat recovery heat exchanger body, 4-heat transfer tube, J-...input rod! g, 6... evaporator, 1. ...Exhaust gas denitrification equipment, 8
...Economizer, 9-...Exit shutoff, 10...
Water supply pipe, 11--Steam drum, 12--Main steam pipe, 13
・-Steam turbine 14・-Condenser, 15... Water pump, 1#...Transfer 4 pump, 17...72 engine, 1
8...Exhaust heat recovery heat exchanger frame, 1#-L is dak),
J#--Outer panel of each unit, Jll-insulating material, 22-
・Heat insulation material mounting pin, 11...Heat-resistant adhesive, 24...
2 gings, 25-washers. Figure 3: Haruki Shimada, Commissioner of the Patent Office, J4, p. 8, 1983, No. 1, Indication of the case, Patent Application No. 686, No. 10, 1983, Name of the invention: Exhaust heat recovery heat exchanger 3, Person making the amendment: Relationship: Patent applicant α's Tokyo Shibaura Electric Co., Ltd. 4, agent 5, engraving of voluntarily amended specification (no changes in content)

Claims (1)

【特許請求の範囲】[Claims] ガヌターv:/′o排ガヌで蒸気タービン用蒸気を発生
するコンバインドサイクル発電に用いる排熱回収熱交換
器において、熱交換器エニットの外板が高温の排ガスに
加熱されないように外板の内面に保温層を設け、保温ラ
イングに設ける取付穴を取付部材の外径よ〕も大きくシ
、前記外板と前記保温層との温度差によp生じる伸びを
吸収可能にした排熱回収熱交換器。
Ganuta v:/'o In the exhaust heat recovery heat exchanger used for combined cycle power generation in which the exhaust gas is used to generate steam for the steam turbine, the inner surface of the outer panel of the heat exchanger Enit is protected from being heated by the high temperature exhaust gas. A heat insulating layer is provided on the heat insulating layer, and the mounting hole provided in the heat insulating lining is made larger than the outside diameter of the mounting member, making it possible to absorb the elongation caused by the temperature difference between the outer panel and the heat insulating layer. vessel.
JP10768681A 1981-07-10 1981-07-10 Waste heat recovering heat exchanger Pending JPS5811302A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10768681A JPS5811302A (en) 1981-07-10 1981-07-10 Waste heat recovering heat exchanger

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10768681A JPS5811302A (en) 1981-07-10 1981-07-10 Waste heat recovering heat exchanger

Publications (1)

Publication Number Publication Date
JPS5811302A true JPS5811302A (en) 1983-01-22

Family

ID=14465391

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10768681A Pending JPS5811302A (en) 1981-07-10 1981-07-10 Waste heat recovering heat exchanger

Country Status (1)

Country Link
JP (1) JPS5811302A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60155804A (en) * 1983-12-22 1985-08-15 スタン・アンデユストリイ Metallic flue for boiler receiving temperature gradient
JP2011064451A (en) * 2009-09-15 2011-03-31 General Electric Co <Ge> Direct evaporator apparatus and energy recovery system
JP2015096800A (en) * 2013-11-15 2015-05-21 アルストム テクノロジー リミテッドALSTOM Technology Ltd Internally stiffened extended-service heat recovery steam generator apparatus

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS60155804A (en) * 1983-12-22 1985-08-15 スタン・アンデユストリイ Metallic flue for boiler receiving temperature gradient
JP2011064451A (en) * 2009-09-15 2011-03-31 General Electric Co <Ge> Direct evaporator apparatus and energy recovery system
JP2015096800A (en) * 2013-11-15 2015-05-21 アルストム テクノロジー リミテッドALSTOM Technology Ltd Internally stiffened extended-service heat recovery steam generator apparatus
US10145626B2 (en) 2013-11-15 2018-12-04 General Electric Technology Gmbh Internally stiffened extended service heat recovery steam generator apparatus

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