JPH11267603A - Treatment of waste and its device - Google Patents

Treatment of waste and its device

Info

Publication number
JPH11267603A
JPH11267603A JP10077946A JP7794698A JPH11267603A JP H11267603 A JPH11267603 A JP H11267603A JP 10077946 A JP10077946 A JP 10077946A JP 7794698 A JP7794698 A JP 7794698A JP H11267603 A JPH11267603 A JP H11267603A
Authority
JP
Japan
Prior art keywords
steam
waste
drying
combustion
burned
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.)
Withdrawn
Application number
JP10077946A
Other languages
Japanese (ja)
Inventor
Katsuyuki Nakanishi
克之 中西
Masayuki Sumi
誠之 角
Tsuneo Aihara
恒雄 相原
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.)
JFE Steel Corp
Original Assignee
Kawasaki Steel Corp
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 Kawasaki Steel Corp filed Critical Kawasaki Steel Corp
Priority to JP10077946A priority Critical patent/JPH11267603A/en
Publication of JPH11267603A publication Critical patent/JPH11267603A/en
Withdrawn legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel

Landscapes

  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To attain a continuous operation of an incinerator and to suppress a discharge of a harmful material by providing the first stage in which the waste such as city waste is crushed and screened, slaked lime is added, and the mixture is dried to form a powdery particle and the second stage in which the powdery particle is burned to generate steam and utilizing a part of the generated steam as a heat source for drying. SOLUTION: The city waste 1 is crushed by a crushing/screening machine 2 to screen and remove metals 3 such as iron, aluminum, etc., then the slaked lime supplied from an addition device 31 is added and dried with a drying device 5 to form the dried powdery particle 6 hardly causing putrefaction and malodor, and the particle 6 is stored in a storage tank 7. Then the particle 6 is burned in a combustion furnace 8 and the steam is generated in a boiler 10 by this combustion gas. A waste gas 15 is discharged to atmosphere after being treated at a waste gas treating stage 11. The generated steam 12 is used for an electricity generation and other heat utilization at a steam utilizing device 13 and also a part of the steam 21 is used as a drying heat source of the drying device 5, and the waste gas 22 of the drying device 5 is burned in the boiler 10 to deodorize and detoxicate.

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、都市ごみ等の廃棄
物の処理方法に関する。
The present invention relates to a method for treating waste such as municipal waste.

【0002】[0002]

【従来の技術】都市ごみ等の廃棄物の内、焼却処理可能
なものは焼却によって減量処理されている。都市ごみ焼
却装置は、市町村単位で運営されており、処理量が50
トン/日以下の焼却装置が施設数の50%を占めてい
る。このような処理量の都市ごみ焼却装置は1日8時間
操業の機械化バッチ炉又は1日16時間操業の準連続処
理炉の中小規模の間歇運転炉を採用している。このよう
な従来の都市ごみ焼却処理技術では、毎日ごみ焼却の運
転停止を伴なう間歇運転をするようになっており、焼却
開始、停止の過渡条件の時、安定した燃焼状態の維持と
有害成分の排出抑制を、燃焼の最適化技術だけで達成す
ることは非常に困難である。このため公害防止装置を設
置する必要があり、これに要する費用がかさむ。また中
小規模の処理炉では公害防止装置設置の対費用効果も低
い。
2. Description of the Related Art Among wastes such as municipal waste, those that can be incinerated are reduced in weight by incineration. Municipal solid waste incinerators are operated on a municipal basis and have a processing volume of 50%.
Less than tons / day of incinerators account for 50% of facilities. The municipal solid waste incinerator having such a throughput employs a mechanized batch furnace operating for 8 hours a day or a small-scale intermittent operation furnace for a semi-continuous processing furnace operating for 16 hours a day. In such conventional municipal waste incineration technology, intermittent operation is performed every day with shutdown of refuse incineration. It is very difficult to achieve emission control only with combustion optimization technology. For this reason, it is necessary to install a pollution control device, and the cost required for this is increased. In small and medium-sized processing furnaces, installing a pollution control device is not cost-effective.

【0003】そこで、都市ごみ等の廃棄物を焼却処理す
るのではなく、粉砕、成形工程を経て、可燃成分をペレ
ット状のごみ成形燃料(RDF)として回収し、大型燃
焼装置等の燃料として利用することによって、小規模間
歇焼却操業による問題を回避する技術が開発されてい
る。この場合、ごみを乾燥粉砕した後、ペレットに成形
する工程が必要である。
[0003] Therefore, instead of incinerating waste such as municipal waste, the flammable components are recovered as pellet-shaped waste molding fuel (RDF) through a crushing and molding process and used as fuel for large-scale combustion equipment and the like. By doing so, techniques have been developed to avoid the problems of small-scale intermittent incineration operations. In this case, a step of forming the pellets after the refuse is dried and pulverized is required.

【0004】また、都市ごみ等の廃棄物を乾燥する工程
では、従来、乾燥熱源の発生炉に灯油を使用しており、
また、乾燥工程から発生する発生ガスを脱臭及び無害化
するために脱臭炉を設け、その熱源として灯油を使用し
ている。このような現状のもとで、ダイオキシン類の排
出を抑制して環境保全を達成し、エネルギー資源をリサ
イクルする技術として図3に示すような都市ごみ処理装
置が提案されている。図3に示す都市ごみ処理装置で
は、都市ごみ1を破砕2し、鉄、アルミニウム等3を選
別除去した後、乾燥5し、乾燥したごみ6を燃焼炉8で
燃焼し、燃焼ガス9をボイラ10に導入して蒸気12を
発生しこの蒸気12を蒸気利用装置13で利用し、ドレ
ン14はボイラ10に戻し燃焼排ガス15は排ガス処理
11を行った後大気放出する。このプロセスでは、都市
ごみの乾燥工程5の熱源として灯油41を熱源発生炉4
2で燃焼させており、その熱43を乾燥工程5に供給
し、また、乾燥工程5から排出した排出ガス44を灯油
46を用いた脱臭炉45で処理して大気中に放散させて
いる。
In the process of drying waste such as municipal solid waste, kerosene is conventionally used in a drying heat source generator.
In addition, a deodorizing furnace is provided for deodorizing and detoxifying generated gas generated from the drying process, and kerosene is used as a heat source. Under such circumstances, a municipal solid waste treatment apparatus as shown in FIG. 3 has been proposed as a technique for controlling the emission of dioxins to achieve environmental conservation and recycling energy resources. In the municipal solid waste treatment apparatus shown in FIG. 3, municipal solid waste 1 is crushed 2, and iron, aluminum and the like 3 are selectively removed, dried 5, dried garbage 6 is burned in a combustion furnace 8, and combustion gas 9 is boiled. The steam 12 is introduced into the steam generator 10, and the steam 12 is used in the steam utilization device 13. The drain 14 is returned to the boiler 10, and the flue gas 15 is discharged to the atmosphere after the exhaust gas treatment 11. In this process, kerosene 41 is used as a heat source in drying step 5 of municipal solid waste,
The heat 43 is supplied to the drying step 5, and the exhaust gas 44 discharged from the drying step 5 is treated in a deodorizing furnace 45 using kerosene 46 to be radiated into the atmosphere.

【0005】また、特開平8−332496号公報で
は、都市ごみ等の廃棄物から固形物燃料を製造する製造
装置と、固形物燃料貯留場と、固形物燃料を燃焼する燃
焼装置と、蒸気又は温水を発生するボイラとを備え、蒸
気、温水、電力等のエネルギーを発生させる一貫複合シ
ステムを開示しており、蒸気又は温水を固形物燃料製造
装置の混合加熱反応機の加熱用熱源として用いる技術も
開示している。
Japanese Patent Application Laid-Open No. 8-332496 discloses a manufacturing apparatus for manufacturing solid fuel from waste such as municipal solid waste, a solid fuel storage, a combustion apparatus for burning solid fuel, steam, Disclosed is an integrated combined system that includes a boiler that generates hot water and generates energy such as steam, hot water, and electric power, and uses steam or hot water as a heat source for heating a mixed heating reactor of a solid fuel production device. Are also disclosed.

【0006】[0006]

【発明が解決しようとする課題】本発明は、上記都市ご
み等の廃棄物の処理技術の改善を図ることを目的とする
もので、本発明の課題は、次のとおりである。 (a)都市ごみ等の廃棄物をペレット状の成形燃料(R
DF)まで処理しないで、成形工程を省略すると共に防
腐、防臭処理を施し、貯留可能な乾燥粉粒体とする。
SUMMARY OF THE INVENTION An object of the present invention is to improve the technology for treating the above-mentioned waste such as municipal solid waste. The objects of the present invention are as follows. (A) Waste such as municipal solid waste is converted to pelletized fuel (R
Without the treatment up to DF), the molding step is omitted, and preservative and deodorant treatments are applied to obtain a dry powder that can be stored.

【0007】(b)この乾燥粉粒体を24時間連続燃焼
し、従来の都市ごみ焼却の間歇操業による焼却炉からの
有害排出物抑制の困難性を克服する。 (c)燃焼工程から蒸気を発生し、その一部を乾燥工程
に使用し、乾燥熱源の灯油の使用を不必要とする。 (d)乾燥工程から発生する発生ガスを燃焼工程雰囲気
中に送入し、脱臭、無害化のための灯油の使用を取り止
める。
(B) The dry powder is continuously burned for 24 hours to overcome the difficulty of controlling harmful emissions from an incinerator by intermittent operation of conventional municipal waste incineration. (C) Steam is generated from the combustion process, a part of which is used in the drying process, and the use of kerosene as a drying heat source is unnecessary. (D) The gas generated from the drying step is sent into the atmosphere of the combustion step, and the use of kerosene for deodorization and detoxification is stopped.

【0008】上記(a)(b)により、設備費を低減
し、有害物質の排出を抑制し、合理化を図る。上記
(c)(d)により、灯油の使用をなくし、ごみの有効
利用を図り、エネルギー消費の低減を図る。
[0008] By the above (a) and (b), equipment costs are reduced, emission of harmful substances is suppressed, and rationalization is achieved. According to the above (c) and (d), use of kerosene is eliminated, waste is effectively used, and energy consumption is reduced.

【0009】[0009]

【課題を解決するための手段】本発明は、上記課題を達
成するために、次の技術手段を講じたことを特徴とする
ものである。本発明は、都市ごみ等の廃棄物を破砕、選
別、消石灰添加、乾燥して貯留可能な粉粒体とする第1
工程と、該粉粒体を燃焼して蒸気を発生して熱利用する
第2工程とからなり、発生した蒸気の一部を前記乾燥用
の熱源として利用することを特徴とする廃棄物の処理方
法である。
The present invention is characterized by taking the following technical means in order to achieve the above object. The first aspect of the present invention is the first method of crushing, sorting, adding slaked lime, drying and storing powdered municipal solid waste.
And a second step of burning the powder and granules to generate steam and utilizing heat, wherein a part of the generated steam is used as a heat source for drying. Is the way.

【0010】この場合に、前記第2工程には、蒸気ター
ビンを用い、前記蒸気の一部は蒸気タービンの中間段か
らの抽気とすれば、適切な圧力の蒸気を使用することが
でき、タービンの低圧段を合理的にし、かつエネルギー
経済的に好適となる。また、前記乾燥時に発生する発生
ガスを前記粉粒体を燃焼する燃焼雰囲気中に送入し、脱
臭及び無害化することとすると、このための灯油使用を
なくすることができ、好適である。
In this case, in the second step, if a steam turbine is used and a part of the steam is extracted from an intermediate stage of the steam turbine, steam at an appropriate pressure can be used. Low-pressure stage is rational and energy-economically favorable. In addition, it is preferable that the generated gas generated during the drying be sent into a combustion atmosphere in which the powder and granules are burned to be deodorized and made harmless, because the use of kerosene for this purpose can be eliminated.

【0011】さらに、前記第1工程は間歇操業、例えば
1日8時間操業でも差し支えないが、前記第2工程を2
4時間連続操業とすることにより、燃焼工程の運転開始
及び運転終了時の過渡的な非定常運転をなくすることが
でき、有害物質の排出を防止することができる。また自
動化、無人化等の合理化運転が可能となる。また第2工
程の装置を小型化することが可能となり、設備コストの
低減を図ることができる。
Further, the first step may be an intermittent operation, for example, an operation for 8 hours a day.
By performing the continuous operation for four hours, it is possible to eliminate the transient unsteady operation at the start and end of the operation of the combustion process, and to prevent the emission of harmful substances. In addition, rationalized operation such as automation and unmanned operation becomes possible. In addition, it is possible to reduce the size of the device in the second step, and it is possible to reduce equipment costs.

【0012】上記方法を好適に実施をすることができる
本発明の装置は、都市ごみ等の廃棄物の破砕装置、選別
装置、消石灰添加装置、乾燥装置及び貯留装置とからな
る第1の処理装置と、該粉粒体の燃焼装置、蒸気発生装
置、熱利用装置とからなる第2の処理装置とからなり、
蒸気発生装置からの発生蒸気の一部を前記乾燥装置に供
給する系路を設けたことを特徴とする廃棄物の処理装置
である。
[0012] The apparatus of the present invention capable of suitably carrying out the above method is a first processing apparatus comprising a crushing apparatus for waste such as municipal waste, a sorting apparatus, a slaked lime adding apparatus, a drying apparatus and a storage apparatus. And a second processing device including a combustion device for the powder and granules, a steam generation device, and a heat utilization device,
An apparatus for treating waste, comprising a system for supplying a part of steam generated from a steam generator to the drying device.

【0013】この場合に、前記第2の処理装置の単位時
間当りの処理能力を、前記第1の処理装置の単位時間当
りの処理能力に対して、1/(1.5〜3)とし、小さ
な装置で連続運転をするようにすることによって、装置
を安価にすることができる。また、前記貯留装置の貯留
能力を前記第2の処理装置の定期修理期間相当分の容量
とすることによって、第2の処理装置を複数系列とする
ことなく、1系列のみとすることができ、設備投資を少
なくすることができる。
In this case, the processing capacity per unit time of the second processing unit is 1 / (1.5 to 3) with respect to the processing capacity per unit time of the first processing unit. By operating continuously with a small device, the device can be made inexpensive. In addition, by setting the storage capacity of the storage device to a capacity corresponding to the period of the periodic repair of the second processing device, it is possible to use only one system without using a plurality of second processing devices, Capital investment can be reduced.

【0014】消石灰の添加量は、防腐、防臭効果を得て
廃棄物を長期間貯留可能にするものである。この貯留は
貯留段階より上流側、すなわち乾燥粉粒体の製造装置の
能力を1日8時間操業の適する規模とし、下流側すなわ
ち乾燥粉粒体の燃焼能力を24時間操業に合致する規模
とするためのバッファーとしての容量を充足する。この
場合下流側の処理能力は連続操業に対応するものとし、
間歇運転による始動停止に伴なう非定常運転をなくし、
ダイオキシンその他の有害物質の排出を抑制し、連続操
業によるプラントの自動化、効率化、小型化を図る。
[0014] The amount of slaked lime added is such that preservative and deodorant effects are obtained, and waste can be stored for a long period of time. In this storage, the upstream side of the storage stage, that is, the capacity of the apparatus for producing dry granules is set to a scale suitable for operation for 8 hours a day, and the downstream side, that is, the combustion capacity of the dry granules is set to a scale suitable for 24 hours operation. The capacity as a buffer for In this case, the downstream processing capacity corresponds to continuous operation,
Eliminates unsteady operation that accompanies starting and stopping due to intermittent operation,
Reduce emissions of dioxins and other harmful substances, and automate, increase efficiency, and reduce the size of plants through continuous operation.

【0015】また貯留能力を、下流工程の定期修理等に
おける休止期間中の貯留量に対応する大きさとする。こ
のために必要な貯蔵期間中の粉粒体の防腐、防臭、質的
変化防止を図る。このような長期間の粉粒体の貯留を可
能にするためには、粉粒体の含水分の低減を適切な消石
灰添加量が重要である。またこの定期修理期間に対応す
る貯留容量を確保することによって、下流工程の複数系
列装備をなくすることができ、適正燃焼処理能力の1系
列の装置を備えればよく、設備費低減、運転操作の簡易
化、自動化を達成することができる。
[0015] The storage capacity is set to a magnitude corresponding to the storage amount during the suspension period in the periodic repair or the like in the downstream process. For this purpose, preservation, deodorization, and prevention of qualitative change of the granular material during the storage period necessary for the purpose are aimed at. In order to enable such a long-term storage of the powder and granules, it is important to appropriately add slaked lime to reduce the water content of the powder and granules. In addition, by securing the storage capacity corresponding to this regular repair period, it is possible to eliminate the equipment of multiple lines in the downstream process, and it is sufficient to provide a single line of equipment with the appropriate combustion processing capacity, thus reducing equipment costs and operating operations. Simplification and automation can be achieved.

【0016】[0016]

【発明の実施の形態】以下図面を参照して本発明の実施
の形態を説明する。図1は本発明の実施例の廃棄物の処
理方法を示す工程図である。都市ごみ1は、破砕/選別
装置2で破砕され、鉄やアルミニウム又はこれらの合金
等3を選別除去し、消石灰添加装置31から供給される
消石灰を添加し、乾燥装置5で乾燥され、乾燥粉粒体6
となる。この乾燥粉粒体6は、含有水分が10重量%以
下で消石灰を1重量%程度含有することによって、腐
敗、悪臭を防止し、長期間貯留することができ、貯留槽
7に貯留される。この乾燥粉粒体6は、燃焼炉8で燃焼
され、燃焼ガス9はボイラ10に導かれ、ここで蒸気を
発生する。排ガス15は排ガス処理工程11で処理さ
れ、無害化されて大気中に放出される。蒸気12は蒸気
利用装置13で、発電その他の熱利用に供される。一部
の蒸気21は乾燥工程5の乾燥熱源として用いられる。
また乾燥工程5から発生する排ガス22はボイラ10の
燃焼室に導入され、ここで燃焼、熱分解することにより
脱臭され無害化される。乾燥工程5の熱源及び乾燥工程
5の排ガス22の脱臭には、灯油を用いる必要がないか
ら、外来エネルギーを節約し、ごみの高効率有効利用を
図ることができる。
Embodiments of the present invention will be described below with reference to the drawings. FIG. 1 is a process chart showing a waste disposal method according to an embodiment of the present invention. The municipal solid waste 1 is crushed by a crushing / sorting device 2 to sort and remove iron, aluminum, or an alloy thereof 3 and the like, and slaked lime supplied from a slaked lime adding device 31 is added thereto. Granule 6
Becomes The dry powder 6 has a water content of 10% by weight or less and contains about 1% by weight of slaked lime, thereby preventing decay and odor, can be stored for a long time, and is stored in the storage tank 7. The dry powder 6 is burned in a combustion furnace 8, and a combustion gas 9 is guided to a boiler 10, where steam is generated. The exhaust gas 15 is treated in the exhaust gas treatment step 11, rendered harmless, and released into the atmosphere. The steam 12 is used for power generation and other heat utilization by a steam utilization device 13. Some of the steam 21 is used as a drying heat source in the drying step 5.
The exhaust gas 22 generated from the drying step 5 is introduced into the combustion chamber of the boiler 10, where it is deodorized and detoxified by burning and thermal decomposition. Since it is not necessary to use kerosene for the deodorization of the heat source in the drying step 5 and the exhaust gas 22 in the drying step 5, it is possible to save external energy and achieve efficient and efficient use of waste.

【0017】また、都市ごみ1を貯留可能な乾燥粉粒体
6とし、これを燃焼することによって、固形ごみ成形燃
料を得るための成形工程を省略することができ、設備投
資の削減、電力、人力等の節減を図ることができる。ま
た、燃焼炉8以降の装置を連続操業することができ、間
歇操業に伴なう有害成分の排出等を抑制することが容易
にできる。さらに、乾燥粉粒体を貯留槽7に貯留するこ
とができるから、乾燥粉粒体製造までの上流工程を下流
工程の操業と無関係に短時間間歇操業、例えば1日8時
間操業とすることが可能である。また、燃焼炉以降の下
流工程は、ボイラ等の定期修理を必要とする装置となる
が、貯留槽7の大きさを定期修理の休止期間中の量の貯
留能力を備えることによって、下流工程の装置を一系列
とすることができる。
Further, by forming the municipal solid waste 1 into a dry granular material 6 that can be stored and burning it, it is possible to omit a molding process for obtaining a solid refuse molding fuel, thereby reducing capital investment, reducing electric power, It is possible to save human power. Further, the apparatus after the combustion furnace 8 can be operated continuously, and the emission of harmful components accompanying the intermittent operation can be easily suppressed. Further, since the dry powder can be stored in the storage tank 7, the upstream process up to the dry powder production can be performed for a short period of time intermittently, for example, 8 hours a day, regardless of the operation of the downstream process. It is possible. Further, the downstream process after the combustion furnace is a device requiring periodic repair of a boiler or the like. However, by providing the storage tank 7 with a storage capacity of an amount during the suspension period of the periodic repair, the downstream process can be performed. The devices can be in a series.

【0018】図2に示す実施例では、乾燥粉粒体6を燃
焼する装置は、廃棄物のガス化灰溶融炉32を備え、粉
粒体をガス化してガス燃料とし、灰分をスラグ33とし
て排出し、ガス燃料を燃焼ボイラ10に供給して燃焼さ
せる。ボイラ10から発生した蒸気12は、蒸気タービ
ン34、発電機35により電力を発生する。蒸気タービ
ンの中間段から抽気された一部の蒸気21は乾燥工程5
に乾燥用熱源として送られる。乾燥装置5からの廃棄物
の発生排ガス22を前記燃焼ボイラの燃焼室に送入し、
脱臭及び無害化処理する。以上により、このシステムは
高効率化したものとなる。なお、乾燥粉粒体の燃焼装置
は、図1に示した燃焼炉、図2に示した廃棄物のガス化
灰溶融炉に限るものではなく、乾燥粉粒体を燃焼する形
式の燃焼ボイラ、例えば流動層ボイラなどとしてもよ
い。
In the embodiment shown in FIG. 2, the apparatus for burning the dry powder 6 is provided with a gasification ash melting furnace 32 for waste, which gasifies the powder to gas fuel, and converts the ash to slag 33. The gas is discharged and supplied to the combustion boiler 10 for combustion. The steam 12 generated from the boiler 10 generates electric power by a steam turbine 34 and a generator 35. Part of the steam 21 extracted from the intermediate stage of the steam turbine is
Sent as a heat source for drying. The waste gas 22 generated from the drying device 5 is sent to the combustion chamber of the combustion boiler,
Deodorize and detoxify. As described above, this system becomes highly efficient. In addition, the combustion device of the dry powder is not limited to the combustion furnace shown in FIG. 1 and the gasification ash melting furnace for waste shown in FIG. 2, but a combustion boiler of a type for burning the dry powder, For example, a fluidized bed boiler may be used.

【0019】[0019]

【発明の効果】本発明によれば、都市ごみ等の廃棄物を
防腐、防臭処理を施し、貯留可能な乾燥粉粒体として貯
留し、この乾燥粉粒体を24時間連続燃焼し、蒸気を発
生し、発電等を行って熱利用を図ることとしたので、ペ
レット状の成形燃料(RDF)を製造する成形工程を省
略でき、燃焼工程以降の装置を小型化でき、従って、設
備投資を低減することができ、有害物質の排出抑制を効
果的に実施することができる。また、乾燥熱源の灯油の
使用を不必要とし、乾燥工程から発生する発生ガスを燃
焼工程雰囲気中に送入し、灯油を用いることなく脱臭、
無害化する。
According to the present invention, waste such as municipal solid waste is subjected to antiseptic and deodorizing treatments, stored as dry powder that can be stored, and the dry powder is continuously burned for 24 hours to generate steam. Since the heat is generated and the heat is used by performing power generation, etc., it is possible to omit the molding process for producing a pellet-shaped molded fuel (RDF), to reduce the size of the apparatus after the combustion process, and thus to reduce the capital investment. Harmful substances can be effectively suppressed. Also, the use of kerosene as a drying heat source is unnecessary, and the gas generated from the drying process is sent into the combustion process atmosphere, and deodorization is performed without using kerosene
Harmless.

【0020】以上、総合的に、設備費の低減、有害物質
の排出の抑制、灯油の不使用により、都市ごみ等の廃棄
物の有効利用を図り、エネルギー消費の低減を図ること
ができる。
As described above, by reducing equipment costs, suppressing emission of harmful substances, and not using kerosene, it is possible to effectively utilize waste such as municipal waste and reduce energy consumption.

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

【図1】実施例の廃棄物の処理方法を示す工程図であ
る。
FIG. 1 is a process chart showing a waste disposal method according to an embodiment.

【図2】実施例の廃棄物の処理方法を示す工程図であ
る。
FIG. 2 is a process chart showing a waste disposal method according to an embodiment.

【図3】従来の廃棄物の処理方法を示す工程図である。FIG. 3 is a process chart showing a conventional waste treatment method.

【符号の説明】[Explanation of symbols]

1 都市ごみ 2 破砕(破砕/選別装置) 3 鉄、アルミニウム等 5 乾燥(工程)(乾燥装置) 6 乾燥したごみ 7 貯留槽 8 燃焼炉 9 燃焼ガス 10 ボイラ 11 排ガス処理(工程) 12 蒸気 13 蒸気利用装置 14 ドレン 15 燃焼排ガス 21 一部の蒸気(抽気) 22 乾燥炉排出ガス 31 消石灰添加装置 32 ガス化灰溶融炉 33 スラグ 34 蒸気タービン 35 発電機 41 灯油 42 熱源発生炉 43 熱 44 排出ガス 45 脱臭炉 46 灯油 Reference Signs List 1 municipal waste 2 crushing (crushing / sorting device) 3 iron, aluminum, etc. 5 drying (process) (drying device) 6 dried refuse 7 storage tank 8 combustion furnace 9 combustion gas 10 boiler 11 exhaust gas treatment (process) 12 steam 13 steam Utilization device 14 Drain 15 Combustion exhaust gas 21 Partial steam (extraction) 22 Drying furnace exhaust gas 31 Slaked lime addition device 32 Gasification ash melting furnace 33 Slag 34 Steam turbine 35 Generator 41 Kerosene 42 Heat source generating furnace 43 Heat 44 Exhaust gas 45 Deodorizing furnace 46 Kerosene

Claims (7)

【特許請求の範囲】[Claims] 【請求項1】 廃棄物を破砕、選別、消石灰添加、乾燥
して貯留可能な粉粒体とする第1工程と、該粉粒体を燃
焼して蒸気を発生して熱利用する第2工程とからなり、
該蒸気の一部を前記乾燥用の熱源として利用することを
特徴とする廃棄物の処理方法。
1. A first step in which waste is crushed, sorted, slaked lime added, and dried to obtain a powder that can be stored, and a second step in which the powder is burned to generate steam and utilize heat. Consisting of
A method for treating waste, wherein a part of the steam is used as the heat source for drying.
【請求項2】 前記熱利用には、蒸気タービンを用い、
前記蒸気の一部は蒸気タービンの中間段からの抽気であ
ることを特徴とする請求項1記載の廃棄物の処理方法。
2. A steam turbine is used for the heat utilization.
The method according to claim 1, wherein a part of the steam is extracted from an intermediate stage of a steam turbine.
【請求項3】 前記乾燥時に発生する発生ガスを前記粉
粒体を燃焼する燃焼雰囲気中に送入し、脱臭及び無害化
することを特徴とする請求項1又は2記載の廃棄物の処
理方法。
3. The method for treating waste according to claim 1, wherein the generated gas generated during the drying is sent into a combustion atmosphere in which the powder and granules are burned, and deodorized and made harmless. .
【請求項4】 前記第1工程を間歇操業とし、前記第2
工程を連続操業とすることを特徴とする請求項1〜3の
何れかに記載の廃棄物の処理方法。
4. The method according to claim 1, wherein the first step is an intermittent operation,
The method for treating waste according to any one of claims 1 to 3, wherein the process is a continuous operation.
【請求項5】 廃棄物の破砕装置、選別装置、消石灰添
加装置、乾燥装置及び貯留装置からなる第1の処理装置
と、該粉粒体の燃焼装置、蒸気発生装置及び熱利用装置
からなる第2の処理装置とからなり、蒸気発生装置から
の発生蒸気の一部を前記乾燥装置に供給する系路を設け
たことを特徴とする廃棄物の処理装置。
5. A first treatment device comprising a waste crushing device, a sorting device, a slaked lime adding device, a drying device and a storage device, and a first treatment device comprising a combustion device, a steam generation device and a heat utilization device for the granular material. A wastewater treatment apparatus, comprising: a system for supplying a part of the steam generated from the steam generation apparatus to the drying apparatus.
【請求項6】 前記第2の処理装置の単位時間当りの処
理能力を、前記第1の処理装置の単位時間当りの処理能
力に対して、1/(1.5〜3)としたことを特徴とす
る請求項5記載の廃棄物の処理装置。
6. The processing capacity per unit time of the second processing device is set to 1 / (1.5 to 3) with respect to the processing capacity per unit time of the first processing device. The waste disposal apparatus according to claim 5, wherein
【請求項7】 前記貯留装置の貯留能力を前記第2の処
理装置の定期修理期間相当分の容量とし、第2の処理装
置を1系列としたことを特徴とする請求項5又は6記載
の廃棄物の処理装置。
7. The storage device according to claim 5, wherein the storage capacity of the storage device is set to a capacity corresponding to a periodic repair period of the second processing device, and the second processing device is provided in one line. Waste treatment equipment.
JP10077946A 1998-03-25 1998-03-25 Treatment of waste and its device Withdrawn JPH11267603A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10077946A JPH11267603A (en) 1998-03-25 1998-03-25 Treatment of waste and its device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10077946A JPH11267603A (en) 1998-03-25 1998-03-25 Treatment of waste and its device

Publications (1)

Publication Number Publication Date
JPH11267603A true JPH11267603A (en) 1999-10-05

Family

ID=13648213

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10077946A Withdrawn JPH11267603A (en) 1998-03-25 1998-03-25 Treatment of waste and its device

Country Status (1)

Country Link
JP (1) JPH11267603A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100823639B1 (en) * 2007-04-06 2008-04-22 이재영 Night-soil incinerator used by high temperature vapor of an incinerator
KR100845131B1 (en) 2007-06-19 2008-07-10 정암환경(주) Waste materials treating process and apparatus for batch type drying and vertical type carbonizing

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100823639B1 (en) * 2007-04-06 2008-04-22 이재영 Night-soil incinerator used by high temperature vapor of an incinerator
KR100845131B1 (en) 2007-06-19 2008-07-10 정암환경(주) Waste materials treating process and apparatus for batch type drying and vertical type carbonizing

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