JPH05272743A - Municipal waste incinerator - Google Patents
Municipal waste incineratorInfo
- Publication number
- JPH05272743A JPH05272743A JP4070483A JP7048392A JPH05272743A JP H05272743 A JPH05272743 A JP H05272743A JP 4070483 A JP4070483 A JP 4070483A JP 7048392 A JP7048392 A JP 7048392A JP H05272743 A JPH05272743 A JP H05272743A
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- reheater
- white smoke
- combustion
- incinerator
- 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
Links
Landscapes
- Chimneys And Flues (AREA)
Abstract
Description
【０００１】[0001]
【産業上の利用分野】本発明は、焼却炉からの排ガスに
対する廃熱回収ボイラを設け、前記廃熱回収ボイラから
の発生蒸気を、高圧側タービンと低圧側タービンとから
なる発電用蒸気タービンに供給する蒸気供給路を設け、
前記蒸気供給路中の蒸気を昇温するための燃焼式過熱器
を設けると共に、前記高圧側タービンからの排出蒸気を
前記低圧側タービンに導く再加熱用配管の途中に再加熱
器を設けた都市ゴミ焼却装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention provides a waste heat recovery boiler for exhaust gas from an incinerator, and generates steam from the waste heat recovery boiler in a steam turbine for power generation composed of a high pressure side turbine and a low pressure side turbine. Provide a steam supply path to supply
A city where a combustion type superheater for raising the temperature of the steam in the steam supply path is provided, and a reheater is provided in the middle of a reheating pipe that guides the exhaust steam from the high pressure side turbine to the low pressure side turbine. Regarding waste incineration equipment.
【０００２】[0002]
【従来の技術】従来、この種の都市ゴミ焼却装置は、前
記燃焼式過熱器からの排ガスはそのまま大気中に排出す
ると共に、前記再加熱器も専用の燃焼装置により発生し
た熱で再加熱する燃焼式とし、その排ガスは、そのまま
大気中に排出し、更に又、前記焼却炉からの排ガスは、
排熱回収ボイラと熱交換した後、集塵装置、洗煙装置を
経てそのまま煙突から排出する構成にしてあった。2. Description of the Related Art Conventionally, in this type of municipal waste incinerator, the exhaust gas from the combustion type superheater is discharged to the atmosphere as it is, and the reheater is also reheated by the heat generated by a dedicated combustion device. Combustion type, the exhaust gas is directly discharged into the atmosphere, and the exhaust gas from the incinerator is also
After exchanging heat with the exhaust heat recovery boiler, it was configured to be discharged directly from the chimney via the dust collector and smoke washing device.
【０００３】[0003]
【発明が解決しようとする課題】前記洗煙装置は、焼却
炉からの排ガスを、例えば水やアルカリ水溶液等の吸収
液と気液接触させることにより排ガス中の塩素ガスやＳ
０ｘ等を前記吸収液に吸収させて除去するためのもので
あるが、洗煙装置で気液接触する際に生ずる飽和水蒸気
が、煙突から排出される途中で冷却され、煙突から排出
されると外気に触れて更に冷却されて、白い湯気からな
る白煙を生ずることが多く、この白煙が、例えば塩酸等
の酸性のミストを含む場合には、環境保全上好ましくな
い影響を及ぼすことも考えられ、又、前記洗煙装置にお
いて酸性のミスト等が完全に除去されて、前記白煙が水
分だけからなるものであるとしても、この白煙が有害物
を含んでいるのではないかという第３者の疑いを招きや
すく、或いは又、美観を損ねることもあるので、排ガス
は白煙を無くした状態で放出したいという要求があっ
た。In the above-mentioned smoke washing device, the exhaust gas from the incinerator is brought into gas-liquid contact with an absorbing liquid such as water or an alkaline aqueous solution, whereby chlorine gas or S in the exhaust gas is discharged.
Although it is intended to remove 0x and the like by absorbing it in the absorbing liquid, saturated water vapor generated when gas-liquid contact is made in the smoke washing device is cooled while being discharged from the chimney and discharged from the chimney. When exposed to the outside air, it is further cooled and often produces white smoke consisting of white steam.If this white smoke contains acidic mist such as hydrochloric acid, it is thought that it may have an unfavorable effect on environmental protection. Moreover, even if the acid mist is completely removed in the smoke washing device and the white smoke is composed of only water, the white smoke may contain harmful substances. There is a demand for the exhaust gas to be emitted in a state of eliminating white smoke, since it is likely to cause doubts among the three parties or may impair the aesthetics.
【０００４】そこで、本発明の目的は、省エネルギーを
図りながら、焼却炉からの排ガスを、白煙を無くした状
態で、煙突から放出することのできる都市ゴミ焼却装置
を提供することにある。Therefore, an object of the present invention is to provide an incinerator for municipal waste which is capable of discharging exhaust gas from an incinerator from a chimney while eliminating white smoke while saving energy.
【０００５】[0005]
【課題を解決するための手段】この目的を達成するため
の本発明にかかる都市ゴミ焼却装置の特徴構成は、焼却
炉からの排ガスに対する廃熱回収ボイラを設け、前記廃
熱回収ボイラからの発生蒸気を、高圧側タービンと低圧
側タービンとからなる発電用蒸気タービンに供給する蒸
気供給路を設け、前記蒸気供給路中の蒸気を昇温するた
めの燃焼式過熱器を設けると共に、前記高圧側タービン
からの排出蒸気を前記低圧側タービンに導く再加熱用配
管の途中に再加熱器を設けた都市ゴミ焼却装置焼却炉に
おいて、前記焼却炉からの燃焼排ガスを煙突に導く燃焼
排ガス路の途中に、前記煙突から放出される排ガス中の
水滴の生成を防止するための白煙防止装置を設け、前記
燃焼式過熱器からの燃焼排ガスを前記再加熱器に供給す
る過熱器排ガス供給路を設けると共に、前記白煙防止装
置に前記再加熱器からの排ガスの熱を供給するための白
煙防止空気供給路を設けてあることにある。To achieve this object, the municipal waste incinerator according to the present invention is characterized in that a waste heat recovery boiler for exhaust gas from an incinerator is provided and the waste heat recovery boiler generates the waste heat. The steam is provided with a steam supply path for supplying steam to a power generation steam turbine including a high-pressure side turbine and a low-pressure side turbine, and a combustion type superheater for raising the temperature of the steam in the steam supply path is provided. In a municipal waste incinerator incinerator provided with a reheater in the middle of the reheating pipe that guides the exhaust steam from the turbine to the low-pressure side turbine, in the middle of the combustion exhaust gas path that guides the combustion exhaust gas from the incinerator to the chimney A superheater exhaust gas supply for supplying the combustion exhaust gas from the combustion type superheater to the reheater by providing a white smoke prevention device for preventing the formation of water droplets in the exhaust gas discharged from the chimney. Provided with a road, lies in that is provided with the white smoke prevention air supply passage for supplying the exhaust gas heat from the reheater to the white smoke prevention device.
【０００６】[0006]
【作用】前記高圧側タービンからの排出蒸気を低圧側タ
ービンに導く再加熱用配管の途中に設けた前記再加熱器
に、燃焼式過熱器からの燃焼排ガスを供給する過熱器排
ガス供給路を設けてあるので、この過熱器排ガス供給路
を介して、燃焼式過熱器からの燃焼排ガスを再加熱器に
その熱源として供給し、高圧側タービンからの排出蒸気
を、再加熱することができる。従って、排出蒸気に再加
熱器から熱を与えさせるために従来のように別途燃料を
使用する必要がない。或いは、別途燃料を使用するとし
ても、その使用量を削減することができる。更に、前記
白煙防止装置に再加熱器からの燃焼排ガスの熱を供給す
るための白煙防止空気供給路を設けてあるため、再加熱
器からの排ガスを白煙防止空気供給路を介して白煙防止
装置に導き、洗煙装置からの排ガスと合流させることに
よって、或いは、洗煙装置からの排ガスと熱交換させる
ことによって、洗煙装置からの排ガスを昇温させ、露点
よりも充分高い温度にして煙突から排出することができ
るので、外気で冷却されても、前記白煙を生ぜしめるこ
となく、煙突からの排ガスを大気中に拡散させることが
できる。尚、前記白煙を防止する目的を達成するため、
例えば前記廃熱回収ボイラからの発生蒸気の一部を白煙
防止装置に導いて間接加熱することも考えられるが、こ
の構成では、配管が長くなるばかりでなく、発電用蒸気
タービンに供給される蒸気量がそれだけ減少するため、
発電効率が悪くなるのに比し、本件の構成によれば、再
加熱器からの排ガスを利用することができるので、発電
効率に影響を及ぼすことなく、短い配管で白煙防止の目
的を達成することができる。The superheater exhaust gas supply path for supplying the combustion exhaust gas from the combustion type superheater is provided to the reheater provided in the middle of the reheating pipe for guiding the exhaust steam from the high pressure side turbine to the low pressure side turbine. Therefore, the combustion exhaust gas from the combustion type superheater can be supplied as a heat source to the reheater through the superheater exhaust gas supply passage to reheat the exhaust steam from the high pressure side turbine. Therefore, it is not necessary to use a separate fuel as in the conventional case in order to heat the exhaust steam from the reheater. Alternatively, even if a separate fuel is used, the amount used can be reduced. Furthermore, since the white smoke prevention device is provided with a white smoke prevention air supply passage for supplying heat of the combustion exhaust gas from the reheater, the exhaust gas from the reheater is supplied through the white smoke prevention air supply passage. The exhaust gas from the smoke washing device is heated to a temperature higher than the dew point by leading it to the white smoke prevention device and joining it with the exhaust gas from the smoke washing device or by exchanging heat with the exhaust gas from the smoke washing device. Since the temperature can be discharged from the chimney, the exhaust gas from the chimney can be diffused into the atmosphere without producing the white smoke even when cooled by the outside air. In order to achieve the purpose of preventing the white smoke,
For example, it is conceivable that a part of the steam generated from the waste heat recovery boiler is guided to a white smoke prevention device to be indirectly heated, but in this configuration, not only the piping becomes long, but also it is supplied to the steam turbine for power generation. Because the amount of steam is reduced by that much,
With this configuration, exhaust gas from the reheater can be used as compared with the case where power generation efficiency deteriorates, so the purpose of white smoke prevention can be achieved with short piping without affecting power generation efficiency. can do.
【０００７】[0007]
【発明の効果】つまり、前記燃焼式過熱器からの燃焼排
ガスの熱量を有効に利用することによって、従来再加熱
器に用いていた燃料を省くこと、或いは節減することが
できるばかりでなく、更に再加熱器からの燃焼排ガスを
有効に利用することによって、特に新たなエネルギー源
を用いることなく、焼却炉からの排ガスを、白煙を無く
した状態で、煙突から放出することができ、美観を損ね
る等の不都合を解消することができる都市ゴミ焼却装置
を提供することができた。That is, by effectively utilizing the heat quantity of the combustion exhaust gas from the combustion type superheater, not only the fuel conventionally used in the reheater can be omitted or saved, but further, By effectively using the combustion exhaust gas from the reheater, the exhaust gas from the incinerator can be discharged from the chimney without white smoke without using a new energy source, which gives a beautiful appearance. It was possible to provide an incinerator for municipal solid waste that can eliminate the inconvenience such as damage.
【０００８】[0008]
【実施例】次に、本発明による都市ゴミ焼却装置の実施
例を、図面に基づいて説明する。図１に示すように、４
５０ｔ／ｄの都市ゴミを焼却処理するストーカ式の焼却
炉１、及び、焼却炉１から発生する１１．４×１０4Ｎ
ｍ3／ｈの排ガスを処理する排ガス処理装置２、並び
に、排ガスの熱を利用して発電する発電装置３によって
都市ゴミ焼却装置を構成してある。前記焼却炉１を構成
するに、都市ゴミの被処理物を受け入れる受入れホッパ
４と、この受入れホッパ４から受け入れた被処理物を搬
送するストーカを、炉本体に配置し、前記受入れホッパ
４を設けた側とは反対側の壁面に、助燃兼点火用バーナ
ー５を設け、受入れホッパ４から受け入れた前記被処理
物を順次移送させて、乾燥させながら燃焼させるように
形成してある。未燃焼ガスの燃焼を完結させるために、
上部空間には、二次燃焼空間７を形成して、４００℃、
２．０×１０ 4Ｎｍ3／ｈの空気を供給する二次燃焼空気
供給部９を前記二次燃焼空間７に臨ませて設けると共
に、前記二次燃焼空間７の下流側には、廃熱回収ボイラ
収容空間８を形成し、燃焼排ガスの持つ熱量の一部を回
収する廃熱回収ボイラ６を設けてある。前記排ガス処理
装置２は、その排ガス入口を前記廃熱回収ボイラ収容空
間８の下流側に開口させた燃焼排ガス路１０を設けると
共に、この燃焼排ガス路１０の煙突１１に至るまでの流
路途中に、バグフィルター１２、洗煙装置１３、白煙防
止装置１４を接続して構成してある。前記発電装置３
は、高圧側タービン１５と低圧側タービン１６からなる
発電用蒸気タービン１７と、これによって駆動される発
電機１８と、前記廃熱回収ボイラ６から発生する蒸気を
前記高圧側タービン１５に供給する蒸気供給路１９とを
設けてある。この蒸気供給路１９の途中には、前記廃熱
回収ボイラ６から発生する３１０℃の蒸気を５００℃に
昇温するための過熱用バーナー３０を備えた燃焼式過熱
器２０を設けると共に、前記高圧側タービン１５からの
蒸気を再加熱して低圧側タービン１６に供給するために
再加熱用配管２７を設け、その途中に再加熱器２１を設
けてある。再加熱器２１は、その再加熱用熱源として、
過熱器排ガス供給路３６を介して供給される前記燃焼式
過熱器２０からの燃焼排ガスを用い、再加熱器２１から
は４００℃、３．９×１０4Ｎｍ3／ｈの燃焼排ガスが得
られる構成にすると共に、この再加熱器２１からの燃焼
排ガスを前記白煙防止装置１４に供給するための白煙防
止空気供給路３１を配管してある。前記燃焼式過熱器２
０からの排ガスは、その一部２．０×１０4Ｎｍ3／ｈを
４００°Ｃで、焼却炉１における二次燃焼用空気とし
て、二次燃焼空気供給部９に二次空気供給路２２を介し
て供給される。尚、燃焼式過熱器２０からの排ガスの残
部は、焼却炉１における被処理物の乾燥用空気及び燃焼
用空気として、乾燥用空気供給部２３と一次燃焼空気供
給部２４に、それぞれ４００°Ｃで、３．１５×１０4
Ｎｍ3／ｈずつ供給できるように、前記二次空気供給路
２２の途中から分岐した配管で、乾燥用空気供給路３
３、一次燃焼空気供給路３４を設けてある。図中２８，
２９、及び３５は空気流量調整用のダンパーである。前
記低圧側タービン１６からの５２℃の蒸気乃至水は、焼
却炉１の排ガスとの熱交換によって２５０℃まで加温さ
れた状態で前記廃熱回収ボイラ６に供給することができ
るように、前記焼却炉１の燃焼排ガス路１０内を通る熱
交換用配管２５を設けてある。熱交換用配管２５の途中
には、補給水供給部２６を設けてある。前記廃熱回収ボ
イラ６に熱を与えて３００℃となった排ガスは、１５０
℃で前記バグフィルター１２に入り、９１℃で前記洗煙
装置１３に入り、６５℃で前記白煙防止装置１４に入
り、ここで、再加熱器２１からの４００℃、３．９×１
０ 4Ｎｍ3／ｈの燃焼排ガスと合流して昇温され、１５０
℃、１５．３×１０4Ｎｍ3／ｈの排ガスとして、白煙を
消去した状態で前記煙突１１から大気中に排出される。EXAMPLE Next, implementation of the municipal waste incinerator according to the present invention
An example will be described with reference to the drawings. As shown in FIG.
Stoker-type incineration to incinerate 50t / d municipal waste
11.4 × 10 generated from furnace 1 and incinerator 1FourN
m3Exhaust gas treatment device 2, which processes exhaust gas of / h
In addition, by the power generation device 3 that uses the heat of the exhaust gas to generate electricity
It constitutes an incinerator for municipal waste. Configure the incinerator 1
The receiving hopper that accepts the waste to be treated
4 and the object to be processed received from the receiving hopper 4
The stoker to be sent is placed in the furnace body, and the receiving hopper is placed.
On the wall surface on the side opposite to the side on which No. 4 is provided, a burner for auxiliary combustion and ignition
-5 is provided, and the object to be processed is received from the receiving hopper 4.
Transfer the items in sequence and burn them while drying
Has been formed. In order to complete the combustion of unburned gas,
A secondary combustion space 7 is formed in the upper space, and the temperature is 400 ° C.
2.0 x 10 FourNm3Combustion air to supply air of 1 / h
When the supply unit 9 is provided so as to face the secondary combustion space 7,
At the downstream side of the secondary combustion space 7, a waste heat recovery boiler is installed.
The accommodation space 8 is formed and a part of the heat quantity of combustion exhaust gas is recovered.
A waste heat recovery boiler 6 for collecting the waste heat is provided. Exhaust gas treatment
The device 2 has an exhaust gas inlet for the waste heat recovery boiler accommodation space.
When the combustion exhaust gas passage 10 opened on the downstream side of the space 8 is provided,
Together, the flow up to the chimney 11 of this combustion exhaust gas passage 10
Along the way, a bag filter 12, a smoke washing device 13, a white smoke control
It is configured by connecting a stop device 14. The power generator 3
Consists of a high pressure side turbine 15 and a low pressure side turbine 16.
The steam turbine 17 for power generation and the generator driven by this
Steam generated from the electric heat 18 and the waste heat recovery boiler 6
The steam supply path 19 for supplying to the high pressure side turbine 15
It is provided. In the middle of this steam supply path 19, the waste heat
310 ℃ steam generated from the recovery boiler 6 to 500 ℃
Combustion type superheat equipped with superheat burner 30 for raising temperature
From the high pressure side turbine 15
To reheat the steam and supply it to the low pressure side turbine 16
A reheating pipe 27 is provided, and a reheater 21 is installed on the way.
There is a mark. The reheater 21 serves as a heat source for reheating.
The combustion type that is supplied via the superheater exhaust gas supply path 36
Combustion exhaust gas from the superheater 20 is used, and from the reheater 21
Is 400 ° C., 3.9 × 10FourNm3/ H combustion exhaust gas is obtained
Combustion from this reheater 21
White smoke prevention for supplying exhaust gas to the white smoke prevention device 14
The still air supply passage 31 is provided as a pipe. The combustion type superheater 2
Exhaust gas from 0 is partly 2.0 × 10FourNm3/ H
At 400 ° C, as the secondary combustion air in the incinerator 1
Through the secondary air supply passage 22 to the secondary combustion air supply unit 9.
Supplied. The residual exhaust gas from the combustion type superheater 20
Part is for drying air and combustion of the object to be treated in the incinerator 1.
As the supply air, the drying air supply unit 23 and the primary combustion air supply
3.15 × 10 at 400 ° C. in each feeding part 24Four
Nm3/ H, so that the secondary air supply path
22 is a pipe branched from the middle of 22 to provide the drying air supply path 3
3. A primary combustion air supply passage 34 is provided. 28 in the figure,
29 and 35 are dampers for adjusting the air flow rate. Previous
The steam or water at 52 ° C from the low pressure side turbine 16 is burnt.
Heat up to 250 ° C by heat exchange with exhaust gas from incinerator 1
Can be supplied to the waste heat recovery boiler 6 in a stored state.
Heat passing through the combustion exhaust gas passage 10 of the incinerator 1
A replacement pipe 25 is provided. In the middle of heat exchange pipe 25
A makeup water supply unit 26 is provided in the. The waste heat recovery box
Exhaust gas that has been heated to 300 ° C by applying heat to Ira 6 is 150
Enter the bag filter 12 at ℃, wash the smoke at 91 ℃
Enter the device 13 and enter the white smoke prevention device 14 at 65 ° C.
Where 400 ° C. from the reheater 21, 3.9 × 1
0 FourNm3/ H
° C, 15.3 x 10FourNm3White smoke as exhaust gas of / h
The erased state is discharged from the chimney 11 to the atmosphere.
【０００９】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。It should be noted that reference numerals are given in the claims for convenience of comparison with the drawings, but the present invention is not limited to the configurations of the accompanying drawings by the entry.
【図１】本発明による都市ゴミ焼却装置の実施例を示す
説明図FIG. 1 is an explanatory view showing an embodiment of an incinerator of municipal waste according to the present invention.
１ 焼却炉 ６ 廃熱回収ボイラ １０ 燃焼排ガス路 １１ 煙突 １４ 白煙防止装置 １５ 高圧側タービン １６ 低圧側タービン １７ 発電用蒸気タービン １９ 蒸気供給路 ２０ 燃焼式過熱器 ２１ 再加熱器 ２７ 再加熱用配管 ３１ 白煙防止空気供給路 ３６ 過熱器排ガス供給路 1 Incinerator 6 Waste Heat Recovery Boiler 10 Combustion Exhaust Gas Channel 11 Chimney 14 White Smoke Prevention Device 15 High Pressure Side Turbine 16 Low Pressure Side Turbine 17 Steam Steam Generator 19 Steam Supply Channel 20 Combustion Superheater 21 Reheater 27 Reheating Pipe 31 White smoke prevention air supply path 36 Superheater exhaust gas supply path
Claims (1)
回収ボイラ（６）を設け、前記廃熱回収ボイラ（６）か
らの発生蒸気を、高圧側タービン（１５）と低圧側ター
ビン（１６）とからなる発電用蒸気タービン（１７）に
供給する蒸気供給路（１９）を設け、前記蒸気供給路
（１９）中の蒸気を昇温するための燃焼式過熱器（２
０）を設けると共に、前記高圧側タービン（１５）から
の排出蒸気を前記低圧側タービン（１６）に導く再加熱
用配管（２７）の途中に再加熱器（２１）を設けた都市
ゴミ焼却装置であって、 前記焼却炉（１）からの燃焼排ガスを煙突（１１）に導
く燃焼排ガス路（１０）の途中に、前記煙突（１１）か
ら放出される排ガス中の水滴の生成を防止するための白
煙防止装置（１４）を設け、前記燃焼式過熱器（２０）
からの燃焼排ガスを前記再加熱器（２１）に供給する過
熱器排ガス供給路（３６）を設けると共に、前記白煙防
止装置（１４）に前記再加熱器（２１）からの排ガスの
熱を供給するための白煙防止空気供給路（３１）を設け
てある都市ゴミ焼却装置。1. A waste heat recovery boiler (6) for exhaust gas from an incinerator (1) is provided, and steam generated from the waste heat recovery boiler (6) is supplied to a high pressure side turbine (15) and a low pressure side turbine (16). And a combustion type superheater (2) for raising the temperature of the steam in the steam supply path (19).
0) and a reheater (21) in the middle of a reheating pipe (27) for guiding the exhaust steam from the high pressure side turbine (15) to the low pressure side turbine (16). In order to prevent the formation of water droplets in the exhaust gas discharged from the chimney (11) in the middle of the combustion exhaust gas passage (10) that guides the combustion exhaust gas from the incinerator (1) to the chimney (11) And a combustion type superheater (20) provided with a white smoke prevention device (14)
An exhaust gas supply passage (36) for supplying combustion exhaust gas from the reheater (21) to the reheater (21) is provided, and heat of exhaust gas from the reheater (21) is supplied to the white smoke prevention device (14). A city refuse incinerator provided with a white smoke prevention air supply passage (31) for operating.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4070483A JPH05272743A (en) | 1992-03-27 | 1992-03-27 | Municipal waste incinerator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP4070483A JPH05272743A (en) | 1992-03-27 | 1992-03-27 | Municipal waste incinerator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH05272743A true JPH05272743A (en) | 1993-10-19 |
Family
ID=13432818
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP4070483A Pending JPH05272743A (en) | 1992-03-27 | 1992-03-27 | Municipal waste incinerator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH05272743A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10160110A (en) * | 1996-11-27 | 1998-06-19 | Mitsubishi Heavy Ind Ltd | Power generation plant combined with refuse incineration |
| JP2016148317A (en) * | 2015-02-13 | 2016-08-18 | 株式会社タクマ | Power generation facility utilizing heat recovery from combustion exhaust gas |
| JP2019094792A (en) * | 2017-11-20 | 2019-06-20 | 株式会社タクマ | Heat recovery power generation facility from flue gas and control method for the same |
-
1992
- 1992-03-27 JP JP4070483A patent/JPH05272743A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH10160110A (en) * | 1996-11-27 | 1998-06-19 | Mitsubishi Heavy Ind Ltd | Power generation plant combined with refuse incineration |
| JP2016148317A (en) * | 2015-02-13 | 2016-08-18 | 株式会社タクマ | Power generation facility utilizing heat recovery from combustion exhaust gas |
| JP2019094792A (en) * | 2017-11-20 | 2019-06-20 | 株式会社タクマ | Heat recovery power generation facility from flue gas and control method for the same |
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