JPH10160110A - Power generation plant combined with refuse incineration - Google Patents

Power generation plant combined with refuse incineration

Info

Publication number
JPH10160110A
JPH10160110A JP8316125A JP31612596A JPH10160110A JP H10160110 A JPH10160110 A JP H10160110A JP 8316125 A JP8316125 A JP 8316125A JP 31612596 A JP31612596 A JP 31612596A JP H10160110 A JPH10160110 A JP H10160110A
Authority
JP
Japan
Prior art keywords
steam
heater
steam turbine
temperature
waste heat
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
JP8316125A
Other languages
Japanese (ja)
Inventor
Nobuyoshi Okada
宣好 岡田
Tetsuo Nakamura
哲夫 中村
Mitsuko Yamagishi
晃子 山岸
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP8316125A priority Critical patent/JPH10160110A/en
Publication of JPH10160110A publication Critical patent/JPH10160110A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide power generation plant combined with refuse incineration which achieves a higher heat efficiency of the plant as a whole by improving the heat efficiency of a heater in an attempt to overcome failure in successfully upgrading the heat efficiency of the plant because of worse heat efficiency of the heater in the conventional garbage incineration power generation plant in which the upgrading of a turbine efficiency is made by using a superheating part alone for the heater for heating steam from a waste heat boiler. SOLUTION: Steam generated by a waste heat boiler 2 is heated by a heater 4 to raise the temperature thereof and the steam heated up to a higher temperature is supplied to a steam turbine 6 to drive the steam turbine 6. Thereafter, an exhaust discharged from the steam turbine 6 or the steam extracted from a step in the course of the steam turbine 6 is returned to the heater 4 again for reheating. The steam reheated up to a higher temperature is supplied to the steam turbine 6 to drive the steam turbine 6. This achieves a higher heat efficiency of the heater 4 thereby improving the efficiency as plant.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ごみ焼却炉におい
て発生する廃熱を、廃熱ボイラで回収して発生させた蒸
気で、発電を行うようにしたごみ焼却発電プラントに係
り、特に、廃熱ボイラで発生させた蒸気を、廃熱ボイラ
とは独立して設けられ、都市ガス等の外部燃料を燃焼さ
せて加熱する加熱器で過熱、若しくは加熱して蒸気ター
ビンに供給し、高効率の発電を行うようにしたごみ焼却
発電プラントに関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a refuse incineration power plant in which waste heat generated in a refuse incinerator is recovered by a waste heat boiler and generated using steam, and more particularly, to a waste incineration power plant. The steam generated by the heat boiler is provided independently of the waste heat boiler, and is overheated by a heater that burns and heats external fuel such as city gas, or is supplied to a steam turbine by heating. The present invention relates to a refuse incineration power plant that generates power.

【0002】[0002]

【従来の技術】ごみ焼却炉におけるごみ焼却に付随して
発生する廃熱を利用して、発電を行うようにしたごみ焼
却発電プラントが各地に建設され、稼動を始めている。
このような、ごみ焼却炉で焼却するごみは、種々雑多の
ものが含まれるため、燃焼温度を高くすると、ごみ焼却
炉の損傷が著しく進むこと、また焼却するごみに塩素化
合物が混じているとダイオキシン等の有害物質が発生す
ること等から、燃焼ガス温度は、ガス、石油等の特定の
燃料のみを燃焼させて蒸気を発生させる産業用ボイラプ
ラントに比較して、低くおさえられている。一方、発電
機を駆動する蒸気タービンにとっては、低温、低圧の蒸
気を使用する場合は、タービン効率が悪くなり、高効率
のごみ焼却発電プラントにできないという不具合があっ
た。
2. Description of the Related Art Waste incineration power plants that generate electric power by utilizing waste heat generated in association with waste incineration in waste incinerators have been constructed and started to operate in various places.
Such garbage to be incinerated in a garbage incinerator contains various miscellaneous things, so if the combustion temperature is increased, the damage to the garbage incinerator will progress significantly, Due to the generation of harmful substances such as dioxin, the temperature of the combustion gas is kept lower than that of an industrial boiler plant that generates steam by burning only a specific fuel such as gas or oil. On the other hand, when a low-temperature, low-pressure steam is used for the steam turbine that drives the generator, the turbine efficiency deteriorates, and there is a problem that a high-efficiency waste incineration power plant cannot be realized.

【0003】このため、従来のごみ焼却発電プラントに
おいても、ごみ焼却炉において発生する廃熱を、廃熱ボ
イラで回収して発生させた蒸気を、廃熱ボイラとは独立
して設けられ、都市ガス等の外部燃料を燃焼させて、そ
の燃焼ガスによって加熱する加熱器で過熱、若しくは加
熱(以下併せて単に加熱という)し、蒸気を高温、高圧
にして蒸気条件を上げて蒸気タービンに供給し、高効率
で発電を行うことができるようにしたごみ焼却発電プラ
ントがある。
[0003] For this reason, in a conventional refuse incineration power plant, steam generated by collecting waste heat generated in a refuse incinerator by a waste heat boiler is provided independently of the waste heat boiler. An external fuel such as gas is burned, and overheated or heated (hereinafter, also simply referred to as heating) by a heater that heats the combustion gas. There is a refuse incineration power plant that can generate power with high efficiency.

【0004】図3は、このような高効率の発電ができる
ようにした、従来のごみ焼却発電プラントを示すブロッ
ク図である。図に示すように、回収されたごみを焼却す
るごみ焼却炉01で発生する排ガスG 1 は、廃熱ボイラ
02に導入され、廃熱ボイラ02にて排ガス中の廃熱が
回収され、蒸気Sを発生させる。
FIG. 3 shows such high-efficiency power generation.
Of a conventional waste incineration power plant
FIG. Incinerate the collected garbage as shown in the figure
Exhaust gas G generated in rubbish incinerator 01 1Is a waste heat boiler
02, and the waste heat in the exhaust gas is
Collected to generate steam S.

【0005】この蒸気Sは、主蒸気ライン03を介し
て、上述したごみ焼却炉01、又は廃熱ボイラ02とは
独立して設けられ、都市ガス等を貯留した燃料供給源0
7、若しくは都市ガス管から直接供給される燃料Fの燃
焼ガスにより加熱する加熱器04の過熱部05に導びか
れ、温度を上昇させた後、蒸気タービン06に導びか
れ、図示省略した発電機に結合された蒸気タービン06
を駆動して発電を行う。また、蒸気Sを発生する給水W
は、蒸気タービン06から排出される排気を図示省略し
た復水器で復水する等して貯留した給水Wを、給水タン
ク08から給水ポンプ09を介して廃熱ボイラ02に給
水するようにしている。
The steam S is provided via a main steam line 03 independently of the above-described waste incinerator 01 or the waste heat boiler 02, and is provided with a fuel supply source 0 storing city gas and the like.
7 or a superheated portion 05 of a heater 04 which is heated by the combustion gas of the fuel F supplied directly from a city gas pipe, and after raising the temperature, is guided to a steam turbine 06 to generate power (not shown). Turbine 06 coupled to the machine
To generate electricity. Also, feed water W that generates steam S
Is configured to supply the stored water W by condensing the exhaust gas discharged from the steam turbine 06 with a condenser not shown in the drawing, from the water supply tank 08 to the waste heat boiler 02 via the water supply pump 09. I have.

【0006】さらに、廃熱ボイラ02で給水Wを加熱
し、蒸気Sを発生させた排ガスG1 は、通常のごみ焼却
プラントと同様に、排ガス処理が施された後、煙突01
0から大気中へ放出される。また、都市ガス等の燃料F
を燃焼させた燃焼ガスで、廃熱ボイラ02から導入され
た蒸気Sの温度を上昇させた後の排ガスG2 は、排ガス
1 と同様に排ガス処理が施された後、煙突010によ
って大気中へ放出される。
Further, the exhaust gas G 1, which has heated the feed water W in the waste heat boiler 02 to generate the steam S, is subjected to exhaust gas treatment in the same manner as in a normal refuse incineration plant, and then the chimney 01
Emitted from 0 to the atmosphere. In addition, fuel F such as city gas
The flue gas G 2 after the temperature of the steam S introduced from the waste heat boiler 02 is increased by the flue gas G 2 is subjected to flue gas treatment in the same manner as the flue gas G 1 , Released to

【0007】このような、ごみ焼却発電プラントでは、
上述したように、廃熱ボイラ02で発生させた蒸気Sを
そのまま蒸気タービン06に供給して発電を行うのでは
なく、加熱器04で蒸気Sの温度を高めて、蒸気タービ
ン06に供給するようにしているので、タービン効率が
向上し、ごみ焼却発電プラント全体としての熱効率を高
め、高効率の発電を行うことのできるごみ焼却発電プラ
ントとすることができる。
[0007] In such a waste incineration power plant,
As described above, instead of supplying the steam S generated by the waste heat boiler 02 to the steam turbine 06 as it is to generate power, the temperature of the steam S is increased by the heater 04 and supplied to the steam turbine 06. Therefore, the turbine efficiency is improved, the thermal efficiency of the entire incineration power plant is increased, and a waste incineration power plant capable of performing high-efficiency power generation can be provided.

【0008】しかしながら、上述した従来のごみ焼却発
電プラントでは、廃熱ボイラ02からの蒸気Sを、都市
ガス等の外部燃料Fの燃焼ガスで過熱するようにした加
熱器04では、蒸気Sを過熱部05で加熱した排ガスG
2 は、そのまま大気へ放出するようにしているために、
外部燃料Fの使用面で効率的でないという不具合があっ
た。
[0008] However, in the above-mentioned conventional refuse incineration power plant, the heater S in which the steam S from the waste heat boiler 02 is superheated by the combustion gas of the external fuel F such as city gas, heats the steam S. Exhaust gas G heated in section 05
2 is to release it to the atmosphere as it is,
There was a problem that the use of the external fuel F was not efficient.

【0009】すなわち、過熱器05の内部の流体温度を
示す図4に示されるように、過熱器05内で燃焼した燃
料Fの燃焼ガス温度がG2 1 からG2 2 低下するこ
とにより、主蒸気ライン03を介して過熱部05に導か
れた蒸気の温度は、ST1 からST2 まで上昇する。こ
のために、蒸気Sを加熱した排ガスG2 の温度G2 2
は、過熱部05で加熱された蒸気Sの温度ST2 よりも
下がることはなく、高温のまま大気放出されることにな
る。ちなみに、この加熱器04から大気へ放出される排
ガスG2 の温度は、300℃〜350℃程度もあり、外
部燃料Fの使用の面で、熱の有効利用が不十分であると
いう不具合があった。
[0009] That is, as shown in FIG. 4 showing the fluid temperature inside the superheater 05, the combustion gas temperature of the fuel F which is burned in the superheater 05 by G 2 T 2 decreases from G 2 T 1 , the temperature of the steam introduced to the superheated portion 05 through a main steam line 03 rises from ST 1 to ST 2. For this purpose, the temperature G 2 T 2 of the exhaust gas G 2 heating the steam S
Is never drops below the temperature ST 2 of the steam S that has been heated by the heating unit 05, will be discharged to the atmosphere remain hot. Incidentally, the temperature of the exhaust gas G 2 emitted to the atmosphere from the heater 04 is also approximately 300 ° C. to 350 ° C., in terms of the use of external fuel F, there is a problem of effective utilization of heat is insufficient Was.

【0010】[0010]

【発明が解決しようとする課題】本発明は、上述した従
来のごみ焼却発電プラントの不具合を解消するため、蒸
気タービンに供給され、蒸気タービンを駆動した蒸気
を、再加熱して、加熱器から大気へ放出される排ガスの
温度を、低くくして大気に放出するようにして、熱の有
効利用を図り、さらに高効率の発電を行えるようにした
ごみ焼却発電プラントの提供を課題とする。
SUMMARY OF THE INVENTION The present invention solves the above-mentioned problems of the conventional refuse incineration power plant by reheating the steam supplied to the steam turbine and driving the steam turbine, and reheating the steam from the heater. An object of the present invention is to provide a refuse incineration power plant that lowers the temperature of exhaust gas discharged to the atmosphere and discharges the exhaust gas to the atmosphere, thereby effectively utilizing heat and generating electric power with higher efficiency.

【0011】[0011]

【課題を解決するための手段】このため、本発明のごみ
焼却発電プラントは、次の手段とした。ごみ焼却炉で、
ごみを焼却して発生する廃熱を廃熱ボイラで回収して蒸
気を発生させ、この蒸気をごみ焼却炉および廃熱ボイラ
とは独立して設けられ、都市ガス等の外部燃料の燃焼ガ
スで加熱する加熱器で昇温させ、この昇温した蒸気を蒸
気タービンに供給して、発電を行うようにしたごみ焼却
発電プラントにおいて、蒸気タービンから排出された排
気、若しくは蒸気タービンの途中の段落から抽出される
蒸気を再度加熱器に戻して再加熱し、再加熱されて昇温
した蒸気を再び蒸気タービンに供給して、蒸気タービン
を駆動するようにした。
Therefore, the refuse incineration power plant of the present invention has the following means. In garbage incinerator,
Waste heat generated by incineration of garbage is recovered by a waste heat boiler to generate steam, and this steam is provided independently of the refuse incinerator and waste heat boiler, and is generated by the combustion gas of external fuel such as city gas. In a refuse incineration power plant that raises the temperature with a heating heater and supplies the heated steam to a steam turbine to generate power, the exhaust gas discharged from the steam turbine, or from the middle stage of the steam turbine The steam to be extracted was returned to the heater again to be reheated, and the reheated and heated steam was again supplied to the steam turbine to drive the steam turbine.

【0012】本発明のごみ焼却発電プラントは、上述の
手段により、加熱器から高温で大気中に放出されてい
た、排気ガスは、蒸気タービンから戻された熱エネルギ
ー(温度)の低い蒸気タービンの排気、若しくは抽気蒸
気と熱交換して、低温となって大気中に放出される。ま
た、排気ガスと熱交換して熱エネルギーが高められて、
蒸気タービンに戻された排気若しくは抽気蒸気は、蒸気
タービンにさらに戻されて、蒸気タービンを駆動できる
ようになる。
In the refuse incineration power plant according to the present invention, the exhaust gas which has been discharged into the atmosphere at a high temperature from the heater by the above-mentioned means is supplied to the steam turbine having a low thermal energy (temperature) returned from the steam turbine. The heat is exchanged with the exhaust gas or the extracted steam, so that the temperature is lowered to be released into the atmosphere. Also, heat exchange with exhaust gas increases heat energy,
The exhaust or extracted steam returned to the steam turbine is further returned to the steam turbine to drive the steam turbine.

【0013】すなわち、従来のごみ焼却発電プラントに
設置されている加熱器では、図2のゾーンAに示すよう
に、主蒸気ラインを介して廃熱ボイラから加熱器(過熱
部)に導かれた蒸気の温度を、ST1 からST2 まで上
昇させるために、加熱器で燃焼させた燃料Fの燃焼ガス
温度がG2 1 からG2 2 低下し、排出される排ガス
2 の温度G2 2 は、加熱器で加熱された蒸気温度S
2 よりも下げることは不可能であったものが、蒸気タ
ービンからの排気、若しくは抽気蒸気の温度ST3 をS
4 まで高めるようにしたために、本発明のごみ焼却発
電プラントの加熱器では、G2 2 からG2 3 まで低
下させることができるようになる。
That is, in a heater installed in a conventional refuse incineration power plant, as shown in zone A of FIG. 2, the heater was guided from a waste heat boiler to a heater (superheater) via a main steam line. the temperature of the vapor, to raise from ST 1 to ST 2, the combustion gas temperature of the fuel F is burned in heater G 2 T 2 decreases from G 2 T 1, the temperature G of the exhaust gas G 2 discharged 2 T 2 is the temperature of the steam heated by the heater S
Those it was impossible to lower than T 2 is the exhaust from the steam turbine, or the temperature ST 3 the extraction steam S
To the so increased to T 4, the heater waste incineration power plant of the present invention, it is possible to reduce the G 2 T 2 to G 2 T 3.

【0014】このことは、排ガスG2 の温度をG2 2
からG2 3 まで低下させて、温度をST3 からST4
まで昇温させて、蒸気タービンに再び供給され、蒸気タ
ービンを駆動する排気、若しくは抽気蒸気の駆動力の分
だけ、従来のごみ焼却発電プラントに比較して、本発明
のごみ焼却発電プラントでは効率を向上させたことにな
る。
This means that the temperature of the exhaust gas G 2 is reduced to G 2 T 2
To G 2 T 3 and reduce the temperature from ST 3 to ST 4
The waste incineration power plant according to the present invention has a higher efficiency than the conventional waste incineration power plant by the amount of the exhaust gas that is supplied again to the steam turbine and drives the steam turbine or the driving force of the extracted steam. Has been improved.

【0015】[0015]

【発明の実施の形態】以下、本発明のごみ焼却発電プラ
ントの実施の一形態を図面にもとづき説明する。図1は
本発明のごみ焼却発電プラントの実施の第1形態を示す
ブロック図である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS One embodiment of a refuse incineration power plant according to the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing a first embodiment of a waste incineration power plant according to the present invention.

【0016】図に示すように、収集されたごみを焼却す
るごみ焼却炉1で発生する高温の排ガスG1 は、廃熱ボ
イラ2に導入され、廃熱ボイラ2にて排ガス中の廃熱が
回収され、温度ST1 の蒸気Sが発生する。この蒸気S
は、主蒸気ライン3を介して、都市ガスを燃焼させて加
熱する、上述したごみ焼却炉1、又は廃熱ボイラ2とは
独立して設けられた加熱器4の過熱部5で、温度をST
2 にまで上昇させた後、蒸気タービン6に供給され、発
電機11に軸結された蒸気タービン6を駆動し発電を行
う。
As shown in the figure, a high-temperature exhaust gas G 1 generated in a refuse incinerator 1 for incinerating collected refuse is introduced into a waste heat boiler 2, and waste heat in the waste gas is discharged from the waste heat boiler 2. is recovered, the steam S temperature ST 1 is generated. This steam S
Is heated through a main steam line 3 by heating the city gas by a superheater 5 of a heater 4 provided independently of the refuse incinerator 1 or the waste heat boiler 2 described above. ST
After being raised to 2 , the steam is supplied to the steam turbine 6 and drives the steam turbine 6 connected to the generator 11 to generate power.

【0017】このように、蒸気タービン6を駆動し、S
3 にまで温度が低下し、蒸気タービン6から抽気され
た蒸気Sは、再び加熱器4の再熱部12に導入され、蒸
気SをST1 からST2 にまで昇温させることによっ
て、G2 1 からG2 2 まで温度が低下した、都市ガ
スの燃焼ガスによって再熱される。そして、加熱器4で
ST3 からST4 にまで加熱された再熱蒸気は、再び蒸
気タービン6に供給され、蒸気タービン6の駆動を再び
行う。また、蒸気6を駆動し、蒸気タービン6から排気
される排気は、復水器13に導入され、凝縮されて復水
となる。
As described above, the steam turbine 6 is driven and S
The temperature of the steam S extracted from the steam turbine 6 decreases to T 3 , and is again introduced into the reheating unit 12 of the heater 4, and the temperature of the steam S is increased from ST 1 to ST 2. temperature is lowered from 2 T 1 to G 2 T 2, it is reheated by combustion gas city gas. The reheat steam that is heated from ST 3 in the heater 4 to the ST 4 is again supplied to the steam turbine 6 again to drive the steam turbine 6. Further, the exhaust that drives the steam 6 and is exhausted from the steam turbine 6 is introduced into the condenser 13 and is condensed to be condensed.

【0018】さらに、ごみ焼却場に必要とする蒸気は、
蒸気タービン6から必要な圧力で抽気10され、抽気ラ
イン14によって蒸気Sを必要とする設備に供給され
る。なお、上述した実施の形態では、加熱器6の再熱部
12に導入する蒸気は蒸気タービン6で抽気した抽気蒸
気としたが、蒸気タービン6の排気の一部を導入するよ
うにしても良いものである。
Further, the steam required for the incineration plant is
Bleed air 10 is extracted from the steam turbine 6 at a required pressure, and supplied to equipment that requires steam S via an extraction line 14. In the above-described embodiment, the steam introduced into the reheating unit 12 of the heater 6 is the extracted steam extracted by the steam turbine 6, but a part of the exhaust gas of the steam turbine 6 may be introduced. Things.

【0019】次に、復水器13で凝縮された復水は、給
水Wとなって復水ポンプ15や給水ポンプ9を含む、そ
の他の給水設備を介して廃熱ボイラ2に供給される。ま
た、廃熱ボイラ2に導入され、給水Wを加熱し、蒸気S
を発生させた排ガスG 1 は、従前通り排ガス処理が施さ
れた後、煙突10から大気中へ放出される。また、都市
ガスが燃焼して、廃熱ボイラ2から導入された蒸気S、
および蒸気タービン6から返された再熱蒸気の温度を上
昇させた排ガスG2 は、排ガスG1 と同様に排ガス処理
が施された後、煙突10によって大気中へ放出される。
Next, the condensed water condensed in the condenser 13 is supplied to
Including water condensing pump 15 and water supply pump 9 as water W,
Is supplied to the waste heat boiler 2 through another water supply facility. Ma
Introduced into the waste heat boiler 2 to heat the feed water W
Exhaust gas G which generated 1Is subject to exhaust gas treatment as before
After being released, it is released from the chimney 10 into the atmosphere. Also city
The gas burns, and the steam S introduced from the waste heat boiler 2
And the temperature of the reheated steam returned from the steam turbine 6
Exhaust gas G raisedTwoIs exhaust gas G1Exhaust gas treatment as well
Is released to the atmosphere by the chimney 10.

【0020】図2は上述した本実施の形態のごみ焼却発
電プラントにおける蒸気および燃焼ガスの流体温度につ
いての説明図である。図において、縦軸は温度を示し、
横軸は部位を示す。すなわち、A部は図1に示す過熱部
5を示し、B部は再熱部12を示す。なお、A部におけ
るG2 1 は過熱器5の入口ガス温度、すなわち都市ガ
スを燃焼させた燃料ガスの過熱器5の入口における温
度、G2 2 は過熱器5の出口における燃焼ガス温度、
ST1 は廃熱ボイラ2から供給される蒸気Sの過熱器5
の入口における温度、ST2 は過熱器5の出口における
蒸気Sの温度をそれぞれ示し、過熱部5で過熱された蒸
気Sは、温度ST2 となって蒸気タービン6に導びかれ
ることを示している。
FIG. 2 is an explanatory diagram of fluid temperatures of steam and combustion gas in the above-described waste incineration power plant according to the present embodiment. In the figure, the vertical axis indicates temperature,
The horizontal axis indicates the site. That is, part A shows the superheated part 5 shown in FIG. 1 and part B shows the reheat part 12. In the section A, G 2 T 1 is the inlet gas temperature of the superheater 5, that is, the temperature of the fuel gas obtained by burning the city gas at the inlet of the superheater 5, and G 2 T 2 is the combustion gas temperature at the outlet of the superheater 5. ,
ST 1 is a superheater 5 for the steam S supplied from the waste heat boiler 2
Temperature at the inlet, ST 2 represents the temperature of the steam S at the outlet of the superheater 5, respectively, the steam S that has been superheated by the superheating unit 5, indicates that wither Shirubebi the steam turbine 6 becomes temperature ST 2 I have.

【0021】なお、一般的に加熱器4等の熱交換器で伝
熱が行われる場合、構造的に伝熱限界が生じる(ピンチ
ポイントΔT)ため、ガス側の温度G2 2 は、蒸気温
度ST2 +ΔTで決定される。従って、図3に示す加熱
器04のように、過熱部05だけの熱交換では、図4に
示すように、この温度G2 2 の排ガスG2 がそのまま
大気へ放出されるが、本実施の形態のごみ焼却発電プラ
ントでは、蒸気タービン6から温度ST3 の蒸気を抽気
して、再度この加熱器4の再熱部12に戻すようにした
ことにより、蒸気SはB部に示すように温度ST3 から
ST4 まで加熱される。また、燃焼ガスはG2 2 から
2 3 まで熱回収されることになる。このG2 3
2 2 と同様に、ピンチポイントΔTを加算した再熱
蒸気ST 4 にて決定されることになる。
In general, the heat is transferred by a heat exchanger such as the heater 4.
When heat is applied, there is a structural heat transfer limit (pinch
Point ΔT), the gas side temperature GTwoTTwoIs the steam temperature
Degree STTwo+ ΔT. Therefore, the heating shown in FIG.
In the case of heat exchange only in the superheated section 05 as in the vessel 04, FIG.
As shown, this temperature GTwoTTwoExhaust gas GTwoIs as it is
Although released to the atmosphere, the waste incineration power generation
, The temperature ST from the steam turbine 6ThreeBleed steam
Then, the heater 4 was returned to the reheating section 12 again.
As a result, the steam S reaches the temperature ST as shown in part B.ThreeFrom
STFourHeated until. The combustion gas is GTwoTTwoFrom
GTwoTThreeHeat recovery. This GTwoTThreeAlso
GTwoTTwoReheat with the addition of the pinch point ΔT
Steam ST FourWill be determined.

【0022】[0022]

【発明の効果】以上説明したように、本発明のごみ焼却
発電プラントによれば、特許請求の範囲に示す構成によ
り、プラントの効率を向上させるため、ごみ焼却装置と
は別に設置された装置に外部から供給される燃料の有効
利用を計ることができ、従来のごみ焼却発電プラントに
比較して、さらに熱効率を向上させたものにすることが
できる。
As described above, according to the refuse incineration power plant of the present invention, the configuration shown in the claims makes it possible to improve the efficiency of the plant by using a device installed separately from the refuse incineration device. Effective utilization of fuel supplied from the outside can be measured, and the thermal efficiency can be further improved as compared with a conventional refuse incineration power plant.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明のごみ焼却発電プラントの実施の第1形
態を示すブロック図、
FIG. 1 is a block diagram showing a first embodiment of a waste incineration power plant according to the present invention;

【図2】図1に示す加熱器における流体温度を示す図、FIG. 2 is a view showing a fluid temperature in the heater shown in FIG. 1;

【図3】従来のごみ焼却発電プラントを示すブロック
図、
FIG. 3 is a block diagram showing a conventional refuse incineration power plant.

【図4】図3に示す加熱器における流体温度を示す図で
ある。
FIG. 4 is a diagram showing a fluid temperature in the heater shown in FIG. 3;

【符号の説明】[Explanation of symbols]

1,01 ごみ焼却炉 2,02 廃熱ボイラ 3,03 主蒸気ライン 4,04 加熱器 5,05 過熱部 6,06 蒸気タービン 7,07 都市ガス(燃料供給源) 8,08 復水器(給水タンク) 9,09 給水ポンプ 10,010 煙突 11 発電機 12 (加熱器)再熱部 13 復水器 14 抽気ライン 15 復水ポンプ 1,01 Waste incinerator 2,02 Waste heat boiler 3,03 Main steam line 4,04 Heater 5,05 Superheater 6,06 Steam turbine 7,07 City gas (fuel supply source) 8,08 Condenser ( Water supply tank) 9,09 Water supply pump 10,010 Chimney 11 Generator 12 (Heating device) Reheat unit 13 Condenser 14 Extraction line 15 Condensate pump

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ごみ焼却炉で発生する廃熱を回収する廃
熱ボイラで発生させた蒸気を、独立して設置され、外部
燃料を燃焼させる加熱器で加熱して、発電機に連結され
た蒸気タービンに供給し、駆動するようにしたごみ焼却
発電プラントにおいて、前記蒸気タービンから抽出され
た蒸気、もしくは前記蒸気タービンから排出された蒸気
を前記加熱器で再加熱して、前記蒸気タービンに供給す
るようにしたことを特徴とするごみ焼却発電プラント。
1. A steam generated by a waste heat boiler for recovering waste heat generated in a refuse incinerator is independently installed, heated by a heater for burning external fuel, and connected to a generator. In a refuse incineration power plant that is supplied to and driven by a steam turbine, steam extracted from the steam turbine or steam discharged from the steam turbine is reheated by the heater and supplied to the steam turbine. A refuse incineration power plant characterized in that:
JP8316125A 1996-11-27 1996-11-27 Power generation plant combined with refuse incineration Pending JPH10160110A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8316125A JPH10160110A (en) 1996-11-27 1996-11-27 Power generation plant combined with refuse incineration

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8316125A JPH10160110A (en) 1996-11-27 1996-11-27 Power generation plant combined with refuse incineration

Publications (1)

Publication Number Publication Date
JPH10160110A true JPH10160110A (en) 1998-06-19

Family

ID=18073534

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8316125A Pending JPH10160110A (en) 1996-11-27 1996-11-27 Power generation plant combined with refuse incineration

Country Status (1)

Country Link
JP (1) JPH10160110A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8863521B2 (en) 2010-04-07 2014-10-21 Kabushiki Kaisha Toshiba Steam turbine plant
JP2019148377A (en) * 2018-02-27 2019-09-05 三菱日立パワーシステムズ株式会社 Existing boiler utilization high steam condition boiler plant
KR20190116707A (en) * 2018-04-05 2019-10-15 한밭대학교 산학협력단 Power generator by using combustible waste

Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH048703U (en) * 1990-05-10 1992-01-27
JPH05272743A (en) * 1992-03-27 1993-10-19 Kubota Corp Municipal waste incinerator
JPH07119414A (en) * 1993-10-25 1995-05-09 Kubota Corp Method of controlling operation of refuse incinerator waste heat utilizing combined plant
JPH07119415A (en) * 1993-10-25 1995-05-09 Kubota Corp Operation method of refuse incinerator waste heat utilizing combined plant
JPH07243305A (en) * 1994-03-03 1995-09-19 Kubota Corp Waste heat recovery combined plant for garbage burning incinerator
JPH0835406A (en) * 1994-07-27 1996-02-06 Hitachi Zosen Corp Power generating facility by waste incineration
JPH0835405A (en) * 1994-07-27 1996-02-06 Hitachi Zosen Corp Power generating facility by waste incineration
JPH08109808A (en) * 1994-10-13 1996-04-30 Hitachi Zosen Corp Power generation system by burning garbage
JPH09203305A (en) * 1996-01-26 1997-08-05 Hitachi Ltd Power generating system utilizing waste incinerating heat

Patent Citations (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH048703U (en) * 1990-05-10 1992-01-27
JPH05272743A (en) * 1992-03-27 1993-10-19 Kubota Corp Municipal waste incinerator
JPH07119414A (en) * 1993-10-25 1995-05-09 Kubota Corp Method of controlling operation of refuse incinerator waste heat utilizing combined plant
JPH07119415A (en) * 1993-10-25 1995-05-09 Kubota Corp Operation method of refuse incinerator waste heat utilizing combined plant
JPH07243305A (en) * 1994-03-03 1995-09-19 Kubota Corp Waste heat recovery combined plant for garbage burning incinerator
JPH0835406A (en) * 1994-07-27 1996-02-06 Hitachi Zosen Corp Power generating facility by waste incineration
JPH0835405A (en) * 1994-07-27 1996-02-06 Hitachi Zosen Corp Power generating facility by waste incineration
JPH08109808A (en) * 1994-10-13 1996-04-30 Hitachi Zosen Corp Power generation system by burning garbage
JPH09203305A (en) * 1996-01-26 1997-08-05 Hitachi Ltd Power generating system utilizing waste incinerating heat

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8863521B2 (en) 2010-04-07 2014-10-21 Kabushiki Kaisha Toshiba Steam turbine plant
JP2019148377A (en) * 2018-02-27 2019-09-05 三菱日立パワーシステムズ株式会社 Existing boiler utilization high steam condition boiler plant
KR20190116707A (en) * 2018-04-05 2019-10-15 한밭대학교 산학협력단 Power generator by using combustible waste

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