JPH07158831A - Combustion method of sludge etc - Google Patents
Combustion method of sludge etcInfo
- Publication number
- JPH07158831A JPH07158831A JP30502493A JP30502493A JPH07158831A JP H07158831 A JPH07158831 A JP H07158831A JP 30502493 A JP30502493 A JP 30502493A JP 30502493 A JP30502493 A JP 30502493A JP H07158831 A JPH07158831 A JP H07158831A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- gas
- gas turbine
- sludge
- turbine
- 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
- Gasification And Melting Of Waste (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は、省エネルギー化を企
画した汚泥等の焼却方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for incinerating sludge or the like which is designed to save energy.
【0002】[0002]
【従来の技術】一般に、下水処理施設等から出る汚泥を
処理するには、埋め立て地への投棄が行われてきた。し
かし、埋め立て地は近年次第に確保しにくくなってきて
おり、汚泥を焼却等によって減容したり、汚泥のコンポ
スト化により再利用を図っていた。2. Description of the Related Art Generally, in order to treat sludge discharged from a sewage treatment facility, etc., it has been dumped to a landfill. However, it has become difficult to secure landfill sites in recent years, and the volume of sludge was reduced by incineration, etc., and sludge was reused by composting.
【0003】[0003]
【発明が解決しようとする課題】脱水汚泥等を焼却する
ための流動床型または流動層型の焼却炉は、同焼却炉に
熱風炉から熱風を吹き込む方法や、始動時に該焼却炉に
熱風炉から熱風を送り込んで運転を開始し、炉の排ガス
ラインに設けられた空気予熱器からの空気が、炉の温度
上昇に伴って昇温した時点で、熱風炉からの熱風を予熱
器からの熱風に切り替えて運転を続ける方法等により運
転されている。A fluidized bed type or fluidized bed type incinerator for incinerating dewatered sludge or the like is a method of blowing hot air from the hot air oven into the incinerator, or a hot air oven for starting the incinerator. When hot air is sent from the preheater to start the operation, the air from the air preheater installed in the exhaust gas line of the furnace rises in temperature as the temperature of the furnace rises. It is operated by switching to and continuing the operation.
【0004】汚泥には悪臭や有害物質等が含まれている
ため、これらを熱分解するには例えば800℃以上の高
温での燃焼が必要であり、そのためには、焼却炉への熱
風は、500℃程度の高温と、熱風の押込みのための送
風力とを必要とする。Since sludge contains odors, harmful substances, etc., it is necessary to burn them at a high temperature of, for example, 800 ° C. or more in order to decompose them. Therefore, the hot air to the incinerator is It requires a high temperature of about 500 ° C. and a blowing force for pushing hot air.
【0005】一方、ガスタービンは発電等の動力に使用
され、ガスタービンの排ガスは500℃程度の熱風とガ
スタービンの回転力による送風力を持っている。On the other hand, the gas turbine is used for power such as power generation, and the exhaust gas of the gas turbine has hot air of about 500 ° C. and wind power sent by the rotational force of the gas turbine.
【0006】流動床炉では、汚泥の熱分解を行うために
炉内温度は800℃以上まで上げられ、そのため高温の
排ガスが出る。In the fluidized bed furnace, the temperature in the furnace is raised to 800 ° C. or higher in order to thermally decompose the sludge, so that high temperature exhaust gas is emitted.
【0007】そこで、この発明は、これらのエネルギー
を有効に活用するシステムを構築することにより省エネ
ルギーを達成することができる汚泥等の焼却方法を提供
することを目的とする。Therefore, an object of the present invention is to provide a method for incinerating sludge or the like that can achieve energy saving by constructing a system that effectively utilizes these energies.
【0008】[0008]
【課題を解決するための手段】この発明による汚泥等の
焼却方法は、上記目的を達成すべく工夫されたもので、
脱水汚泥等を焼却する炉にガスタービン排ガスを吹き込
んで燃焼を促進し、燃焼によって発生する熱で高圧蒸気
を得て、該蒸気を蒸気タービンまたは上記ガスタービン
の動力として用いることを特徴とする。The method for incinerating sludge and the like according to the present invention is devised to achieve the above object.
The gas turbine exhaust gas is blown into a furnace for incinerating dewatered sludge or the like to promote combustion, high pressure steam is obtained by the heat generated by the combustion, and the steam is used as power of the steam turbine or the gas turbine.
【0009】最近の汚泥は高いカロリーを有し、泥炭程
度のカロリーがあり、外から500℃程度の熱風を注入
することにより汚泥の自燃と熱分解に必要な温度まで温
度を上昇させることができる。[0009] Recent sludge has high calorie and calorie level of peat. By injecting hot air of about 500 ° C from the outside, the temperature can be raised to the temperature required for self-combustion and thermal decomposition of sludge. .
【0010】また、タービン排ガスの温度500℃を汚
泥の焼却により800℃に昇温し、エネルギーの効率的
な利用を促進することができる。Further, the temperature of the turbine exhaust gas of 500 ° C. can be raised to 800 ° C. by incinerating the sludge to promote efficient use of energy.
【0011】[0011]
実施例1 図1において、ガスタービン(1) の駆動軸には発電機
(2) が連結されている。ガスタービン(1) は供給された
燃料によって駆動され、その駆動力で発電機(2)が運転
される。発電機(2) の運転により発生された電力は例え
ば下水処理場内の様々な設備の電源として使用される。Example 1 In FIG. 1, a generator is installed on a drive shaft of a gas turbine (1).
(2) is linked. The gas turbine (1) is driven by the supplied fuel, and the driving force drives the generator (2). The electric power generated by the operation of the generator (2) is used, for example, as a power source for various facilities in the sewage treatment plant.
【0012】流動層型の焼却炉(3) に乾燥汚泥を投入
し、ガスタービン(1) の排ガス(約550℃、酸素約1
5%)をガスタービンの排出力を利用して焼却炉(3) に
吹き込み、焼却炉内の汚泥の燃焼を促進し、これにより
炉内温度を有害物質を熱分解するに必要な800℃以上
の温度まで昇温する。The dry sludge was put into the fluidized bed type incinerator (3), and the exhaust gas (about 550 ° C., oxygen about 1) of the gas turbine (1)
5%) is blown into the incinerator (3) by utilizing the exhaust power of the gas turbine to accelerate the combustion of sludge in the incinerator, thereby increasing the temperature in the furnace to 800 ° C or higher required for pyrolyzing harmful substances. Up to the temperature of.
【0013】焼却炉(3) の高温排ガス排出路に配置され
た熱交換器(4) に供給水を通し、この水から高圧蒸気を
得、これを蒸気タービン(5) へ送って同タービンを駆動
させる。蒸気タービン(5) の駆動により発電機(6) を運
転する。Feed water is passed through a heat exchanger (4) arranged in the hot exhaust gas discharge passage of the incinerator (3), high-pressure steam is obtained from this water, and this is sent to a steam turbine (5) to drive the turbine. Drive it. The generator (6) is driven by driving the steam turbine (5).
【0014】なお、図1中、(7) (8) は焼却炉(3) から
出る高温排ガスの排出路に配置されたサイクロン、(9)
は電気集塵機、(10)は煙突、(11)は焼却灰コンベヤ、(1
2)は焼却灰サイロである。In FIG. 1, (7) and (8) are cyclones arranged in the discharge passage of high temperature exhaust gas from the incinerator (3), and (9)
Is an electric dust collector, (10) is a chimney, (11) is an incinerator ash conveyor, and (1
2) is incineration ash silo.
【0015】こうして、エネルギーの総合的な有効利用
を図り、下水処理施設における省エネルギーを達成す
る。In this way, comprehensive effective utilization of energy is achieved and energy saving in the sewage treatment facility is achieved.
【0016】実施例2 焼却炉(3) の高温排ガス排出路に配置された熱交換器
(4) によって高圧蒸気を得、これをガスタービン(1) へ
送って同タービンを駆動させる。ガスタービン(1) の駆
動により上記の如く発電機(2) を運転する。Example 2 A heat exchanger arranged in a high temperature exhaust gas discharge passage of an incinerator (3)
High pressure steam is obtained by (4) and sent to the gas turbine (1) to drive the turbine. The generator (2) is operated as described above by driving the gas turbine (1).
【0017】この点を除いて、実施例1と同じ操作を行
う。Except for this point, the same operation as in Example 1 is performed.
【0018】[0018]
【発明の効果】この発明による汚泥等の焼却方法では、
脱水汚泥等を焼却する炉にガスタービン排ガスを吹き込
んで燃焼を促進し、燃焼によって発生する熱で高圧蒸気
を得て、該蒸気を蒸気タービンまたは上記ガスタービン
の動力として用いるので、エネルギーの総合的な有効利
用を図り、下水処理施設における省エネルギーを達成す
ることができる。The method of incinerating sludge and the like according to the present invention,
Gas turbine exhaust gas is blown into a furnace that incinerates dehydrated sludge, etc. to promote combustion, and high-pressure steam is obtained by the heat generated by combustion, and this steam is used as power for the steam turbine or the gas turbine. Energy saving in sewage treatment facilities can be achieved through effective use.
【図1】この発明の実施例1を示すフローシートであ
る。FIG. 1 is a flow sheet showing a first embodiment of the present invention.
(1) ……ガスタービン (2) ……発電機 (3) ……焼却炉 (4) ……熱交換器 (5) ……蒸気タービン (6) ……発電機 (1) …… Gas turbine (2) …… Generator (3) …… Incinerator (4) …… Heat exchanger (5) …… Steam turbine (6) …… Generator
Claims (1)
排ガスを吹き込んで燃焼を促進し、燃焼によって発生す
る熱で高圧蒸気を得て、該蒸気を蒸気タービンまたは上
記ガスタービンの動力として用いることを特徴とする汚
泥等の焼却方法。1. Use of a gas turbine exhaust gas blown into a furnace for incinerating dewatered sludge or the like to accelerate combustion, obtain high-pressure steam by heat generated by the combustion, and use the steam as power for a steam turbine or the gas turbine. A method for incinerating sludge, etc.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30502493A JPH07158831A (en) | 1993-12-06 | 1993-12-06 | Combustion method of sludge etc |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP30502493A JPH07158831A (en) | 1993-12-06 | 1993-12-06 | Combustion method of sludge etc |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07158831A true JPH07158831A (en) | 1995-06-20 |
Family
ID=17940177
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP30502493A Pending JPH07158831A (en) | 1993-12-06 | 1993-12-06 | Combustion method of sludge etc |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07158831A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010016772A (en) * | 1999-08-03 | 2001-03-05 | 김재숙 | The drying system for sludge |
JP2006263555A (en) * | 2005-03-23 | 2006-10-05 | Sumitomo Heavy Ind Ltd | System and method for recovering energy |
US8156662B2 (en) * | 2006-01-18 | 2012-04-17 | Earthrenew, Inc. | Systems for prevention of HAP emissions and for efficient drying/dehydration processes |
-
1993
- 1993-12-06 JP JP30502493A patent/JPH07158831A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20010016772A (en) * | 1999-08-03 | 2001-03-05 | 김재숙 | The drying system for sludge |
JP2006263555A (en) * | 2005-03-23 | 2006-10-05 | Sumitomo Heavy Ind Ltd | System and method for recovering energy |
JP4652093B2 (en) * | 2005-03-23 | 2011-03-16 | 住友重機械エンバイロメント株式会社 | Energy recovery system and energy recovery method |
US8156662B2 (en) * | 2006-01-18 | 2012-04-17 | Earthrenew, Inc. | Systems for prevention of HAP emissions and for efficient drying/dehydration processes |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
A02 | Decision of refusal |
Free format text: JAPANESE INTERMEDIATE CODE: A02 Effective date: 20030318 |