JPH08200654A - Incinerator of waste - Google Patents
Incinerator of wasteInfo
- Publication number
- JPH08200654A JPH08200654A JP868295A JP868295A JPH08200654A JP H08200654 A JPH08200654 A JP H08200654A JP 868295 A JP868295 A JP 868295A JP 868295 A JP868295 A JP 868295A JP H08200654 A JPH08200654 A JP H08200654A
- Authority
- JP
- Japan
- Prior art keywords
- steam
- temperature
- heat transfer
- incinerator
- boiler
- 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
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、可燃性廃棄物(以下、
単に廃棄物と呼ぶ)を燃焼させる廃棄物焼却炉に係り、
特に、焼却炉の熱を蒸気発生に利用するシステム、例え
ば、廃棄物発電システムに使用するに好適な廃棄物焼却
炉に関する。BACKGROUND OF THE INVENTION The present invention relates to combustible waste (hereinafter referred to as
We call it a waste incinerator that burns waste)
In particular, the present invention relates to a waste incinerator suitable for use in a system that utilizes the heat of an incinerator for steam generation, for example, a waste power generation system.
【0002】[0002]
【従来の技術】従来、廃棄物焼却炉の熱を利用して発生
させた蒸気で蒸気タービンを駆動し発電するシステム、
すなわち、廃棄物発電システムでは、焼却炉の燃焼ガス
出口部に設けたボイラによって蒸気を発生させていた
(講演資料「ごみ焼却設備の高温腐食対策とごみ発電の
最新動向」におけるI.ごみ焼却発電の現状と今後の課
題:KNOWHOW SUPPORT CENTER 発行、P.I−6(平成5
年12月15日)参照)。しかも、ボイラ伝熱管が腐食
性ガスを含む燃焼ガスと接触すると320℃を越える温
度で高温腐食を起こすため、発生蒸気は300℃以下の
低い温度に抑えられていた。この結果、廃棄物発電シス
テムの発電効率は、高々15%程度の低い値にとどまっ
ていた。2. Description of the Related Art Conventionally, a system for driving a steam turbine to generate electricity by using steam generated by utilizing heat of a waste incinerator,
That is, in the waste power generation system, steam was generated by the boiler installed at the combustion gas outlet of the incinerator (see I. Waste incineration power generation in the presentation material "The latest trends in high temperature corrosion countermeasures for waste incineration facilities and waste power generation"). Status and future issues: Issued by KNOWHOW SUPPORT CENTER, PI-6 (1993)
(December 15, 2012)). Moreover, when the boiler heat transfer tube comes into contact with the combustion gas containing corrosive gas, high temperature corrosion occurs at a temperature exceeding 320 ° C., so that the generated steam is suppressed to a low temperature of 300 ° C. or less. As a result, the power generation efficiency of the waste power generation system remained at a low value of at most about 15%.
【0003】[0003]
【発明が解決しようとする課題】廃棄物発電システムの
発電効率を高める最も効果的な手段は、蒸気タービン入
口の蒸気温度を高めることである。言い替えれば、いか
に伝熱管の腐食を促進させずに高温蒸気を取り出すかと
いう課題を解決する必要がある。The most effective means for increasing the power generation efficiency of a waste power generation system is to raise the steam temperature at the steam turbine inlet. In other words, it is necessary to solve the problem of how to take out high temperature steam without promoting the corrosion of the heat transfer tube.
【0004】本発明の目的は、伝熱管の腐食を促進させ
ずに高温蒸気を得られる廃棄物焼却炉を提供することに
ある。An object of the present invention is to provide a waste incinerator capable of obtaining high temperature steam without promoting corrosion of heat transfer tubes.
【0005】[0005]
【課題を解決するための手段】廃棄物焼却炉は耐火レン
ガで構成され、焼却炉内と炉外とを断熱する構造となっ
ており、燃焼ガス温度は、焼却炉の寿命を考慮して、通
常の燃焼ガスは比較的低い温度である800〜900℃
程度に抑えられている。[Means for Solving the Problems] The waste incinerator is constructed of refractory bricks, and has a structure that insulates the inside and outside of the incinerator. The combustion gas temperature is set in consideration of the life of the incinerator. Normal combustion gas has a relatively low temperature of 800 to 900 ° C.
It is suppressed to some extent.
【0006】このことは同時に焼却炉の内壁温度が80
0〜900℃であることも意味している。すなわち、3
00℃を越える温度の耐火レンガ内に蒸気流路となる伝
熱管を埋め込むか、高温の耐火レンガと伝熱管とを良好
な伝熱状態となるように接触させることによって、腐食
性ガスを含む燃焼ガスと伝熱管との直接接触なしに30
0℃以上の高温蒸気を得ることが可能となる。At the same time, the inner wall temperature of the incinerator is 80
It also means 0 to 900 ° C. That is, 3
Combustion containing a corrosive gas by embedding a heat transfer tube serving as a steam flow path in a refractory brick having a temperature exceeding 00 ° C or by bringing the high temperature refractory brick and the heat transfer tube into contact with each other so as to obtain a good heat transfer 30 without direct contact between gas and heat transfer tubes
It becomes possible to obtain high temperature steam of 0 ° C. or higher.
【0007】本発明の廃棄物焼却炉は、焼却炉を構成す
る炉壁内部に蒸気配管を設けた構成とする。The waste incinerator of the present invention has a structure in which a steam pipe is provided inside a furnace wall which constitutes the incinerator.
【0008】[0008]
【作用】上記の構成によれば、伝熱管は耐火レンガによ
って囲まれた状態で熱交換を行うことができるので、腐
食性ガスを含む燃焼ガスと伝熱管との直接接触なしに、
すなわち、高温腐食を促進させることなく300℃以上
の高温蒸気を得ることができる。その結果、より高温の
蒸気を蒸気タービンに供給でき、発電効率を高めること
ができる。According to the above structure, the heat transfer tube can perform heat exchange in a state surrounded by refractory bricks, so that the heat transfer tube is not directly contacted with the combustion gas containing corrosive gas.
That is, high temperature steam of 300 ° C. or higher can be obtained without promoting high temperature corrosion. As a result, higher temperature steam can be supplied to the steam turbine and power generation efficiency can be improved.
【0009】[0009]
【実施例】以下、図面を参照しながら本発明である廃棄
物焼却炉の実施例について、ストーカ炉形式を例に取り
説明する。Embodiments of the waste incinerator according to the present invention will be described below with reference to the drawings, taking a stoker furnace type as an example.
【0010】図1は、ごみ発電システムにおける廃棄物
焼却炉の一実施例を示す断面図である。廃棄物焼却炉1
は図1の破線で囲まれた部分であり、ごみ投入ホッパ2
と,ごみ投入ホッパ2の底部に階段状に設けられた乾燥
ストーカ3,燃焼ストーカ4,後燃焼ストーカ5と,こ
れらストーカの上方部に燃焼空間6を形成する炉壁7と
から構成される。また、押込みファン8を介して空気供
給管9が各ストーカへ接続されている。FIG. 1 is a sectional view showing an embodiment of a waste incinerator in a refuse power generation system. Waste incinerator 1
Is the part surrounded by the broken line in FIG.
And a stoker 3, a combustor stoker 4, a post-combustor stoker 5, which are provided at the bottom of the dust input hopper 2, in a stepwise manner, and a furnace wall 7 forming a combustion space 6 above these stokers. Further, an air supply pipe 9 is connected to each stoker via the pushing fan 8.
【0011】蒸気系統の構成については、燃焼ガス10
が排出される廃棄物焼却炉1の出口部にボイラ11が設
置され、ボイラ11からは蒸気配管12が炉壁7の内部
を貫通したのち高圧蒸気だめ13へと接続されている。
高圧蒸気だめ13は高圧蒸気配管14によって、発電機
15とカップリングされた蒸気タービン16に接続され
ている。蒸気タービン16からは低圧蒸気配管17が復
水器18に接続され、復水器18からは水配管19がボ
イラ11へ接続されている。Regarding the structure of the steam system, the combustion gas 10
A boiler 11 is installed at the outlet of the waste incinerator 1 from which the steam is discharged. From the boiler 11, a steam pipe 12 penetrates the inside of the furnace wall 7 and is then connected to a high-pressure steam sump 13.
The high-pressure steam reservoir 13 is connected by a high-pressure steam pipe 14 to a steam turbine 16 coupled with a generator 15. A low-pressure steam pipe 17 is connected to the condenser 18 from the steam turbine 16, and a water pipe 19 is connected to the boiler 11 from the condenser 18.
【0012】次に本実施例の動作について説明する。Next, the operation of this embodiment will be described.
【0013】ごみ投入ホッパ2に投入されたごみ20
は、乾燥ストーカ3,燃焼ストーカ4,後燃焼ストーカ
5の順に移送されながら押込みファン8によって空気供
給管9から各ストーカへ供給された空気により燃焼され
る。燃焼ガス10は炉壁7によって形成された燃焼空間
6を通り、炉壁7の出口部に設置されたボイラ11に熱
を与える。ボイラ11で発生させる蒸気は、ボイラ伝熱
管における高温腐食速度があまり大きくならない300
℃以下の温度に保持される。300℃以下の蒸気は、3
00℃を越える温度の炉壁7の内部を貫通するように設
けられた蒸気配管12を流通することにより、400℃
程度に昇温される。400℃程度に昇温された蒸気は高
圧蒸気だめ13に送られたのち、高圧蒸気配管14を経
由して蒸気タービン16に供給され、蒸気タービン16
を駆動し発電機15を回す。蒸気タービン16で動力を
回収したのちの蒸気は、低圧蒸気配管17によって復水
器18に導かれ、凝縮水となる。凝縮水は水配管19に
よってボイラ11へ返送され、再び蒸気として利用され
る。Waste 20 thrown into the waste throw hopper 2
Is transferred by the drying stoker 3, the combustion stoker 4, and the post-combustion stoker 5 in this order, and is combusted by the air supplied from the air supply pipe 9 to each stoker by the pushing fan 8. The combustion gas 10 passes through the combustion space 6 formed by the furnace wall 7 and gives heat to the boiler 11 installed at the outlet of the furnace wall 7. The steam generated in the boiler 11 has a high-temperature corrosion rate in the boiler heat transfer tube that does not increase so much.
It is kept at a temperature below ℃. Steam below 300 ℃ is 3
By passing through the steam pipe 12 provided so as to penetrate the inside of the furnace wall 7 having a temperature exceeding 00 ° C., 400 ° C.
The temperature is raised to a certain degree. The steam heated to about 400 ° C. is sent to the high-pressure steam reservoir 13 and then supplied to the steam turbine 16 via the high-pressure steam pipe 14, and the steam turbine 16
To drive the generator 15. The steam after the power is recovered by the steam turbine 16 is guided to the condenser 18 by the low pressure steam pipe 17 and becomes condensed water. The condensed water is returned to the boiler 11 by the water pipe 19 and is used again as steam.
【0014】本実施例によれば、蒸気による熱回収によ
って焼却炉の炉壁温度を低下させることができるので、
寿命の長い廃棄物焼却炉を提供できる。According to this embodiment, since the temperature of the furnace wall of the incinerator can be lowered by recovering the heat by the steam,
It is possible to provide a waste incinerator with a long life.
【0015】図2は本発明の廃棄物焼却炉の縦方向断面
図であり、図3は耐火レンガの構造例である。FIG. 2 is a longitudinal sectional view of the waste incinerator of the present invention, and FIG. 3 is an example of the structure of refractory bricks.
【0016】図2は蒸気配管12が炉壁7の内部を貫通
して設けられた状態を示している。炉壁7を構成する耐
火レンガ21には、図3に示したように、蒸気配管12
が貫通するためのスペース22が設けられている。スペ
ース22は耐火レンガ21を組み合わせた場合に形成さ
れる。スペース22に蒸気配管12を敷設したのちに形
成される耐火レンガ21と蒸気配管12との間隙には、
伝熱促進剤23例えば金属粉とセメントとの混合物が充
填される。これらの構成によって、蒸気配管12内を流
れる蒸気は高温の耐火レンガ21を介して燃焼ガス10
より熱を与えられて300℃以上の温度に昇温される。FIG. 2 shows a state in which the steam pipe 12 is provided so as to penetrate the inside of the furnace wall 7. As shown in FIG. 3, the steam piping 12 is provided on the refractory bricks 21 forming the furnace wall 7.
Is provided with a space 22. The space 22 is formed when the refractory bricks 21 are combined. In the space between the fire brick 21 and the steam pipe 12 formed after the steam pipe 12 is laid in the space 22,
The heat transfer accelerator 23, for example, a mixture of metal powder and cement is filled. With these configurations, the steam flowing in the steam pipe 12 passes through the high-temperature refractory brick 21 and the combustion gas 10
It is given more heat and heated to a temperature of 300 ° C. or higher.
【0017】本実施例によれば、耐火レンガと耐火レン
ガのあいだに金属粉とセメントとの混合物を充填したの
で、廃棄物焼却炉を構成する耐火レンガの補強ができ
る。According to this embodiment, since the mixture of metal powder and cement is filled between the refractory bricks, the refractory bricks constituting the waste incinerator can be reinforced.
【0018】[0018]
【発明の効果】本発明によって、伝熱管の腐食を促進さ
せずに高温蒸気を得られる廃棄物焼却炉を提供すること
ができる。According to the present invention, it is possible to provide a waste incinerator capable of obtaining high temperature steam without promoting corrosion of the heat transfer tube.
【図1】ごみ発電システムにおける本発明の廃棄物焼却
炉の一実施例を示す断面図。FIG. 1 is a sectional view showing an embodiment of a waste incinerator of the present invention in a refuse power generation system.
【図2】本発明の一実施例を示す廃棄物焼却炉の断面
図。FIG. 2 is a sectional view of a waste incinerator showing an embodiment of the present invention.
【図3】本発明の一実施例を示す廃棄物焼却炉における
耐火レンガの構造の説明図。FIG. 3 is an explanatory view of the structure of a refractory brick in a waste incinerator showing an embodiment of the present invention.
1…廃棄物焼却炉、2…ごみ投入ホッパ、6…燃焼空
間、7…炉壁、10…燃焼ガス、11…ボイラ、12…
蒸気配管、13…高圧蒸気だめ、15…発電機、16…
蒸気タービン、18…復水器。1 ... Waste incinerator, 2 ... Waste input hopper, 6 ... Combustion space, 7 ... Furnace wall, 10 ... Combustion gas, 11 ... Boiler, 12 ...
Steam piping, 13 ... High-pressure steam reservoir, 15 ... Generator, 16 ...
Steam turbine, 18 ... Condenser.
Claims (3)
焼却炉を構成する炉壁内部に蒸気配管を設けたことを特
徴とする廃棄物焼却炉。1. An incinerator for burning waste, characterized in that a steam pipe is provided inside a furnace wall constituting the incinerator.
伝熱促進剤を塗布した廃棄物焼却炉。2. The waste incinerator according to claim 1, wherein the outer surface of the steam pipe is coated with a heat transfer accelerator.
粉とセメントとの混合物である廃棄物焼却炉。3. The waste incinerator according to claim 2, wherein the heat transfer accelerator is a mixture of metal powder and cement.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP868295A JPH08200654A (en) | 1995-01-24 | 1995-01-24 | Incinerator of waste |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP868295A JPH08200654A (en) | 1995-01-24 | 1995-01-24 | Incinerator of waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH08200654A true JPH08200654A (en) | 1996-08-06 |
Family
ID=11699702
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP868295A Pending JPH08200654A (en) | 1995-01-24 | 1995-01-24 | Incinerator of waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08200654A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113251427A (en) * | 2021-06-01 | 2021-08-13 | 上海康恒环境股份有限公司 | Anti-corrosion arrangement structure and method for heating surface of waste incineration boiler |
-
1995
- 1995-01-24 JP JP868295A patent/JPH08200654A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN113251427A (en) * | 2021-06-01 | 2021-08-13 | 上海康恒环境股份有限公司 | Anti-corrosion arrangement structure and method for heating surface of waste incineration boiler |
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