JP4129191B2 - Combustible dust injection equipment for waste melting furnaces - Google Patents

Combustible dust injection equipment for waste melting furnaces Download PDF

Info

Publication number
JP4129191B2
JP4129191B2 JP2003046112A JP2003046112A JP4129191B2 JP 4129191 B2 JP4129191 B2 JP 4129191B2 JP 2003046112 A JP2003046112 A JP 2003046112A JP 2003046112 A JP2003046112 A JP 2003046112A JP 4129191 B2 JP4129191 B2 JP 4129191B2
Authority
JP
Japan
Prior art keywords
combustible dust
dust
combustible
cooling
screw conveyor
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.)
Expired - Lifetime
Application number
JP2003046112A
Other languages
Japanese (ja)
Other versions
JP2004085174A (en
Inventor
光正 戸高
秀樹 大田
俊二 古庄
英三 龍田
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.)
Nippon Steel Engineering Co Ltd
Nippon Steel Plant Designing Corp
Original Assignee
Nittetsu Plant Designing Corp
Nippon Steel Engineering Co 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 Nittetsu Plant Designing Corp, Nippon Steel Engineering Co Ltd filed Critical Nittetsu Plant Designing Corp
Priority to JP2003046112A priority Critical patent/JP4129191B2/en
Publication of JP2004085174A publication Critical patent/JP2004085174A/en
Application granted granted Critical
Publication of JP4129191B2 publication Critical patent/JP4129191B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Description

【0001】
【発明の属する技術分野】
本発明は、一般廃棄物、産業廃棄物等の廃棄物を熱分解溶融処理する廃棄物溶融炉の可燃性ダスト吹込設備に関する。
【0002】
【従来の技術】
一般廃棄物、産業廃棄物等の廃棄物の処理方法として、廃棄物をシャフト炉式の廃棄物溶融炉に装入し、廃棄物を乾燥、予熱、熱分解、燃焼、溶融し、スラグやメタルとして取り出す熱分解溶融炉処理方法が知られている。
【0003】
前記廃棄物溶融炉の操業では、炉内において、装入物中の可燃物が熱分解して残渣が発生する。発生した熱分解残渣は羽口から送られてきた空気によって燃焼するかあるいは炉内に堆積していくが、微細なものは、羽口から送られてきた空気によって燃焼されることなく、気流に乗って炉から可燃性ダストとして飛散する。
【0004】
廃棄物溶融炉で飛散する可燃性ダストの処理技術として、例えば特許文献1に可燃性ダストを羽口から吹き込む設備が記載されている。
【0005】
図4は前記文献に記載された可燃性ダスト供給ラインの説明図である。同図において、廃棄物溶融炉1で発生した可燃性ダストは除塵器2で捕集され、可燃性ダストホッパー3に貯留される。可燃性ダストホッパー3のスクリューコンベア3aは、可燃性ダストを冷却するための水冷式のスクリューコンベア6と切替ダンパ4を介して配管5で接続されると共に、燃焼室9と切替ダンパ7及び可燃性ダストを投入する燃焼室9用のスクリューコンベア8を介して接続される。吹き込み側の水冷式のスクリューコンベア6と燃焼室9用のスクリューコンベア8への可燃性ダストの供給は、可燃性ダストホッパー3のスクリューコンベア3aを正転あるいは逆転することにより行い、その際、可燃性ダストを搬送する側の切替ダンパ4ないし7を開にし、他方のダンパを閉にする。
【0006】
吹き込み側へ可燃性ダストを供給する際は、配管5の切替ダンパ4を開にし、スクリューコンベア3a、水冷式のスクリューコンベア6、篩装置10を経て、中間ホッパー11に可燃性ダストを落下させる。中間ホッパー11では、上部ダンパ11a、下部ダンパ11bを交互に開閉させることにより、可燃性ガス及び搬送空気を混合させずに、可燃性ダストを吹込装置12に落下させている。
【0007】
その後、吹込装置12内の可燃性ダストは、モータMによりサークルフィーダ13の回転数を調節して、吹き込み量を調整し、ブロワ14により各羽口15に吹き込まれる。
【0008】
燃焼室9への可燃性ダストの供給は、切替ダンパ7を開にし、スクリューコンベア8を経て行う。燃焼室9への供給量は、重量指示調節計WICでモータMの回転数を調節しながら行う。
【0009】
【特許文献1】
特開2001−108209号公報
【0010】
【発明が解決しようとする課題】
前述の文献によれば、廃棄物溶融炉1で発生した可燃性ダストを捕集する除塵器2、可燃性ダストホッパー3、スクリューコンベア3a,8、配管5、水冷式のスクリューコンベア6、篩装置10、中間ホッパー11、吹込装置12と順に廃棄物溶融炉の建屋床に設置されている。
【0011】
さらに、除塵器2から吹込装置12までは廃棄物溶融炉の建屋床の2階から6階に渡って各々別々に各床に設置されている。このため、設備コストが高く、設備の設置スペースが大きく建築施工費及び据付工事費がかかる。また、設計も煩雑であり、設計費もかかる。
【0012】
そこで、本発明は、設備コストが安く、設備の設置スペースが小さく建築施工費、据付工事費及び設計費が安くなる可燃性ダスト吹込設備を提供するものである。
【0013】
【課題を解決するための手段】
上記課題を解決するため、請求項1記載の廃棄物溶融炉の可燃性ダスト吹込設備は、廃棄物溶融炉からの可燃性ダストを除塵器で捕集し、捕集した可燃性ダストを可燃性ダストホッパーから切り出して吹込装置へ搬送し、羽口から空気搬送により吹き込む廃棄物溶融炉の可燃性ダスト吹込設備において、可燃性ダストホッパーと吹込装置との間の可燃性ダストの搬送経路に、可燃性ダストを切り出すスクリューコンベアとそのスクリューコンベアと同軸に連結されて回転する可燃性ダストを冷却するための円筒形の回転ドラム式冷却装置、さらにその回転ドラム式冷却装置と同軸に連結されて回転する円筒形の回転篩を設け、その回転篩の下方に可燃性ダストの排出口を設け、その回転篩の出側の下方に可燃性ダスト中の大塊の排出口を設けた可燃性ダストの冷却、篩装置を1つの装置にし、前記回転ドラム式冷却装置には、前記スクリューコンベアのスクリュー軸を介して冷却水を供給することを特徴とする。
【0014】
請求項2記載の廃棄物溶融炉の可燃性ダスト吹込設備は、廃棄物溶融炉からの可燃性ダストを除塵器で捕集し、捕集した可燃性ダストを可燃性ダストホッパーから切り出して吹込装置へ搬送し、羽口から空気搬送により吹き込む廃棄物溶融炉の可燃性ダスト吹込設備において、可燃性ダストホッパーと吹込装置との間の可燃性ダストの搬送経路に、可燃性ダストを切り出すスクリューコンベアとそのスクリューコンベアと同軸に連結されて回転する可燃性ダストを冷却するための円筒形の回転ドラム式冷却装置、さらにその回転ドラム式冷却装置と同軸に連結されて回転する円筒形の回転篩を設け、その回転篩の下方に可燃性ダストの排出口を設け、前記回転ドラム式冷却装置には、前記スクリューコンベアのスクリュー軸を介して冷却水が供給される可燃性ダスト冷却、篩装置を一体化してケーシング内に配設したことを特徴とする。
【0018】
【発明の実施の形態】
以下、本発明の実施の形態を図面に示す実施例に基づき説明する。
【0019】
実施例1
図1は本発明の第1実施例を示す説明図である。前述の図4に示す構成と同一の構成には同一符号を付し、その説明は省略する。
【0020】
図1において設備上流側の構成については図示を省略しているが、図4に示す従来例と同じであり、廃棄物溶融炉1で発生して飛散した可燃性ダストを除塵器2で捕集し、可燃性ダストホッパー3に一時貯留するようになっている。そして、可燃性ダストホッパー3に所定量の可燃性ダストが貯留されると配管5の切替ダンパ4を開にし、可燃性ダスト冷却、篩装置16に可燃性ダストを供給する。
【0021】
可燃性ダスト冷却、篩装置16はケーシング16a内に可燃性ダストを冷却ドラム16dに切り出すスクリュー軸16bを有するスクリューコンベア16cが設けられ、そのスクリューコンベア16cと冷却ドラム16dはスクリュー軸16bに同軸に連結されて回転する。
【0022】
冷却ドラム16dにはスクリュー軸16bを介して冷却水が供給され、円筒形の短尺な冷却ドラム16dの内側に設けたスクリュー状の冷却フィン16eにて可燃性ダストを回転しながら効率よく冷却するとともに篩16fに搬出する。
【0023】
篩16fもスクリュー軸16bに同軸に連結され、スクリューコンベア16c及び冷却ドラム16dと同軸に連結されて回転する。篩16fは多孔の開いたパンチングメタル等で構成された円筒形であり、スクリュー軸16bと同軸回転することにより、篩16fの下方の排出口16gより可燃性ダスト中から搬送の支障になる大塊等を除去したダストを篩下ダストとして排出し、また大塊等をパドル16hにより篩16fの出側まで送り、下方の排出口16iより排出する。
【0024】
排出口16gは、2重ダンパーとして上部ダンパー17a及び下部ダンパー17bを介して可燃性ダストの吹込装置12に直接接続されている。
【0025】
さらに、上部ダンパー17a、下部ダンパー17bにて接続された可燃性ダストの冷却、篩装置16及び吹込装置12は、サークルフィーダ13、ブロワ14を含めて共通架台18に搭載されている。
【0026】
前記構成において、可燃性ダストホッパー3に所定量の可燃性ダストが貯留されていることを重量指示計WIで確認すると、配管5の切替ダンパ4を開の状態にし(図4参照)、さらに上部ダンパー17aを開、下部ダンパー17bを閉の状態にして、可燃性ダスト冷却、篩装置16のスクリュー軸16bのモータMを駆動させ、スクリューコンベア16cを回転させて可燃性ダストを冷却ドラム16dへ送る。可燃性ダストは冷却ドラム16dで発火しない程度の温度、例えば、40℃程度に冷却されて篩16fに送られ、篩下の可燃性ダストは排出口16gより下部ダンパー17bへ落下し、篩上ダストは排出口16iより篩上ダスト搬送ラインに落下する。
【0027】
可燃性ダストの供給は可燃性ダストホッパー3の重量指示調節計WICでモータMの回転数を調節しながら行う(図4参照)。所定量の可燃性ダストの切り出しが終了すると、上部ダンパー17aを閉じ、その後、下部ダンパー17bを開いて可燃性ダストを可燃性ダストの吹込装置12へ投入する。
【0028】
投入後、下部ダンパー17bを閉じて、上部ダンパー17aを開く。以後の上部ダンパー17a、下部ダンパー17bの動作は、繰り返しとなる。
【0029】
吹込装置12内の可燃性ダストは、重量指示調節計WICでモータMによりサークルフィーダ13の回転数を調節して、吹き込み量を調整し、ブロワ14により各羽口15に吹き込まれる。
【0030】
実施例2
図2は本発明の第2実施例を示す説明図である。前述の図4に示す構成と同一の構成には同一符号を付し、その説明は省略する。
【0031】
図2において、廃棄物溶融炉1で発生して飛散した可燃性ダストを捕集するサイクロンなどの除塵器2の下部に、可燃性ダストを一時貯留するホッパー19及び可燃性ダストを切り出すロータリーシール弁などの切出装置20が設置されている。
【0032】
切出装置20と吹込装置12との間の可燃性ダストの搬送経路においては、可燃性ダストを冷却、篩い分けする可燃性ダスト冷却、篩装置22がダンパ21を介して切出装置20に接続されている。その可燃性ダスト冷却、篩装置22の篩22aの下方に可燃性ダストを吹込装置12に投入するための下面が平坦なホッパー23が設置され、その下部に撹拌式の排出機24が設置されている。ホッパー23はダンパ25を介して吹込装置12に接続されている。
【0033】
可燃性ダスト冷却、篩装置22は、例えば、スクリューコンベア22bを介し、可燃性ダストを冷却ドラム22cにて冷却すると共に篩22aに搬送する。篩22aは、可燃性ダスト中から搬送の支障になる大塊等を除去したダストを篩下ダストとしてホッパー23に排出し、ホッパー23の下部の排出機24は撹拌羽根24aをモータMにて回転させ吹込装置12に投入する。
【0034】
また、吹込装置12と燃焼室9との間に可燃性ダストの搬送経路を設け、その可燃性ダストの搬送経路と、羽口15と吹込装置12との間の可燃性ダストの搬送経路とをダンパ26a,26bを開閉することにより切り替え可能にしている。
【0035】
前記構成において、ダンパ21を開、ダンパ25を閉の状態にして、可燃性ダスト冷却、篩装置22のモータMを駆動させ、スクリューコンベア22bを回転させて、切出装置20にて可燃性ダストを切り出し冷却ドラム22cへ送る。可燃性ダストは冷却ドラム22cで発火しない程度の温度、例えば、40℃程度に冷却されて篩22aに送られ、篩下の可燃性ダストはホッパー23に排出される。
【0036】
所定量の可燃性ダストの排出が終了すると、ダンパ21を閉じ、その後、ダンパ25を開いて可燃性ダストを吹込装置12へ投入する。その時、切出装置20のロータリーシール弁は一時停止し、可燃性ダストがホッパー19に一時貯留される。
【0037】
投入後、ダンパ25を閉じて、ダンパ21を開く。以後のダンパ21、ダンパ25の動作は、繰り返しとなる。
【0038】
吹込装置12内の可燃性ダストは、重量指示調節計WICでモータMによりサークルフィーダ13の回転数を調節して、吹き込み量を調整し、ブロワ14により各羽口15に吹き込まれる。このとき、ダンパ26aは閉、ダンパ26bは開の状態としておく。
【0039】
一方、ダンパ26aを開、ダンパ26bを閉とすることにより、可燃性ダストの搬送経路は燃焼室9に向かう搬送経路に切り替わり、可燃性ダストが燃焼室9に吹き込まれる。
【0040】
実施例3
図3は本発明の第3実施例を示す説明図である。前述の図2に示す構成と同一の構成には同一符号を付し、その説明は省略する。
【0041】
本実施例では、切出装置20と吹込装置12との間の可燃性ダストの搬送経路において、可燃性ダストを冷却、篩い分けする可燃性ダスト冷却、篩装置22が上部ダンパ27a及び下部ダンパ27bを介して切出装置20に接続され、その可燃性ダスト冷却、篩装置22は直接吹込装置12に接続されている。
【0042】
この構成において、上部ダンパ27aを開、下部ダンパ27bを閉の状態にして、所定量の可燃性ダストの排出が終了すると、上部ダンパ27aを閉じ、上部ダンパ27a及び下部ダンパ27bの均圧を行うため、均圧弁27cを開き、均圧されたことが確認されれば、下部ダンパ27bを開いて可燃性ダストを可燃性ダスト冷却、篩装置22へ排出する。その時、切出装置20のロータリーシール弁は一時停止し、可燃性ダストがホッパー19に一時貯留される
排出後、均圧弁27c、下部ダンパ27bを閉じて、上部ダンパ27aを開く。以後の上部ダンパ27a、下部ダンパ27b、均圧弁27cの動作は、繰り返しとなる。
【0043】
次に、可燃性ダスト冷却、篩装置22のモータMを駆動させ、スクリューコンベア22bを回転させて、下部ダンパ27bにて排出された可燃性ダストを冷却ドラム22cへ送る。可燃性ダストは冷却ドラム22cで発火しない程度の温度、例えば、40℃程度に冷却されて篩22aに送られ、篩下の可燃性ダストは吹込装置12に排出される。
【0044】
吹込装置12内の可燃性ダストは、レベル計LAでモータMによりサークルフィーダ13の回転数を調節して、その吹き込み量が調整され、ブロワにより各羽口15に吹き込まれる。
【0045】
【発明の効果】
請求項1記載の発明では、可燃性ダストの冷却、篩装置は可燃性ダストの冷却能力が高く設置スペースが小さくて済む回転ドラム式冷却装置と、回転式のため耐久性に優れた回転篩が1つの装置であり設備コストが安くなる。また、回転ドラム式冷却装置には、スクリューコンベアのスクリュー軸を介して冷却水が供給されるため、その冷却効率が向上する。
【0046】
請求項2記載の発明では、可燃性ダストの冷却、篩装置が一体化されてケーシング内に配設されているので、設備の設置スペースが小さく建築施工費、据付工事費及び設計費が大幅に安くなる。また、可燃性ダストの冷却、篩装置の回転ドラム式冷却装置には、スクリューコンベアのスクリュー軸を介して冷却水が供給されるため、その冷却効率が向上する。
【図面の簡単な説明】
【図1】 本発明の第1実施例を示す説明図である。
【図2】 本発明の第実施例を示す説明図である。
【図3】 本発明の第3実施例を示す説明図である。
【図4】 従来の可燃性ダスト供給ラインの説明図である。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a combustible dust blowing facility for a waste melting furnace for pyrolyzing and melting waste such as general waste and industrial waste.
[0002]
[Prior art]
As a waste disposal method such as general waste and industrial waste, waste is charged into a shaft furnace type waste melting furnace, and the waste is dried, preheated, pyrolyzed, combusted, melted, slag and metal There is known a pyrolysis melting furnace treatment method to be taken out as
[0003]
In the operation of the waste melting furnace, combustibles in the charge are thermally decomposed in the furnace to generate a residue. The generated pyrolysis residue is combusted by the air sent from the tuyere or accumulated in the furnace, but the fine one is not burned by the air sent from the tuyere, Ride as a flammable dust from the furnace.
[0004]
As a technique for treating combustible dust scattered in a waste melting furnace, for example, Patent Document 1 describes a facility for blowing combustible dust from a tuyere.
[0005]
FIG. 4 is an explanatory diagram of the combustible dust supply line described in the above-mentioned document. In the figure, combustible dust generated in the waste melting furnace 1 is collected by a dust remover 2 and stored in a combustible dust hopper 3. The screw conveyor 3a of the combustible dust hopper 3 is connected to the water-cooled screw conveyor 6 for cooling the combustible dust by the pipe 5 through the switching damper 4, and the combustion chamber 9, the switching damper 7, and the combustibility. It connects via the screw conveyor 8 for the combustion chamber 9 which throws in dust. The combustible dust is supplied to the water-cooled screw conveyor 6 on the blowing side and the screw conveyor 8 for the combustion chamber 9 by rotating the screw conveyor 3a of the combustible dust hopper 3 forward or reverse. The switching dampers 4 to 7 on the side carrying the dust are opened and the other damper is closed.
[0006]
When supplying combustible dust to the blowing side, the switching damper 4 of the pipe 5 is opened, and the combustible dust is dropped onto the intermediate hopper 11 through the screw conveyor 3a, the water-cooled screw conveyor 6, and the sieve device 10. In the intermediate hopper 11, the upper and lower dampers 11 a and 11 b are alternately opened and closed to drop the combustible dust into the blowing device 12 without mixing the combustible gas and the carrier air.
[0007]
Thereafter, the combustible dust in the blowing device 12 is blown into the tuyere 15 by the blower 14 by adjusting the rotation amount of the circle feeder 13 by the motor M and adjusting the blowing amount.
[0008]
The combustible dust is supplied to the combustion chamber 9 through the screw conveyor 8 with the switching damper 7 opened. The supply amount to the combustion chamber 9 is performed while adjusting the number of revolutions of the motor M with the weight indicating controller WIC.
[0009]
[Patent Document 1]
Japanese Patent Laid-Open No. 2001-108209
[Problems to be solved by the invention]
According to the above-mentioned documents, a dust remover 2 that collects combustible dust generated in the waste melting furnace 1, a combustible dust hopper 3, screw conveyors 3a and 8, pipe 5, a water-cooled screw conveyor 6, a sieve device 10, the intermediate hopper 11 and the blowing device 12 are installed in this order on the building melting furnace floor.
[0011]
Further, the dust remover 2 to the blowing device 12 are installed on each floor separately from the second floor to the sixth floor of the building floor of the waste melting furnace. For this reason, the equipment cost is high, the installation space for the equipment is large, and the construction construction cost and the installation construction cost are required. In addition, the design is complicated and a design cost is required.
[0012]
Therefore, the present invention provides a combustible dust injection facility that has low equipment costs, a small installation space for equipment, and a low construction work cost, installation work cost, and design cost.
[0013]
[Means for Solving the Problems]
In order to solve the above-mentioned problem, the combustible dust blowing equipment of the waste melting furnace according to claim 1 collects the combustible dust from the waste melting furnace with a dust remover, and combusts the collected combustible dust. In the combustible dust blowing equipment of the waste melting furnace, which is cut out from the dust hopper and transported to the blowing device and blown from the tuyere by air transportation, the combustible dust is transported to the combustible dust transport path between the combustible dust hopper and the blowing device. Screw conveyor for cutting out dust, a cylindrical rotating drum cooling device for cooling combustible dust rotating coaxially with the screw conveyor, and further rotating coaxially connected with the rotating drum cooling device a cylindrical rotating sieve provided, the outlet of the combustible dust below the rotating sieve is provided, it provided the outlet of the large mass of combustible in the dust beneath the exit side of the rotary sieve Of combustible dusts cooling, the sieve device into one device, the said rotary drum type cooling device, and supplying the cooling water via the screw shaft of the screw conveyor.
[0014]
The combustible dust blowing equipment for a waste melting furnace according to claim 2 is configured to collect the combustible dust from the waste melting furnace with a dust remover and cut out the collected combustible dust from the combustible dust hopper. A screw conveyor that cuts out flammable dust in the flammable dust transfer path between the flammable dust hopper and the blowing device in the flammable dust blowing equipment of the waste melting furnace that is blown by air transfer from the tuyere A cylindrical rotating drum type cooling device for cooling combustible dust that is connected coaxially with the screw conveyor and rotating, and a cylindrical rotating sieve that is connected coaxially with the rotating drum type cooling device are provided. the outlet of the combustible dust below the rotating sieve is provided, on the said rotary drum-type cooling device, the cooling water via the screw shaft of the screw conveyor Sheet is the combustible dust cooling, by integrating the sieve device, characterized in that disposed in the casing.
[0018]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, embodiments of the present invention will be described based on examples shown in the drawings.
[0019]
Example 1
FIG. 1 is an explanatory view showing a first embodiment of the present invention. The same components as those shown in FIG. 4 are denoted by the same reference numerals, and the description thereof is omitted.
[0020]
In FIG. 1, the configuration on the upstream side of the facility is not shown, but is the same as the conventional example shown in FIG. 4, and combustible dust generated and scattered in the waste melting furnace 1 is collected by the dust remover 2. However, it is temporarily stored in the combustible dust hopper 3. When a predetermined amount of combustible dust is stored in the combustible dust hopper 3, the switching damper 4 of the pipe 5 is opened, and combustible dust is supplied to the combustible dust cooling and sieving device 16.
[0021]
The combustible dust cooling and sieving device 16 is provided with a screw conveyor 16c having a screw shaft 16b for cutting the combustible dust into a cooling drum 16d in a casing 16a, and the screw conveyor 16c and the cooling drum 16d are coaxially connected to the screw shaft 16b. Rotate.
[0022]
Cooling water is supplied to the cooling drum 16d via the screw shaft 16b, and the flammable dust is efficiently cooled while rotating the combustible dust by the screw-like cooling fins 16e provided inside the short cylindrical cooling drum 16d. It is carried out to the sieve 16f.
[0023]
The sieve 16f is also coaxially connected to the screw shaft 16b, and is coaxially connected to the screw conveyor 16c and the cooling drum 16d to rotate. The sieve 16f has a cylindrical shape made of perforated punched metal or the like, and is a large lump that interferes with conveyance from combustible dust from the discharge port 16g below the sieve 16f by rotating coaxially with the screw shaft 16b. The dust from which etc. are removed is discharged as under-sieving dust, and a large lump is sent to the exit side of the sieve 16f by the paddle 16h and discharged from the lower discharge port 16i.
[0024]
The discharge port 16g is directly connected to the combustible dust blowing device 12 as a double damper via an upper damper 17a and a lower damper 17b.
[0025]
Further, the combustible dust cooling, the sieving device 16 and the blowing device 12 connected by the upper damper 17 a and the lower damper 17 b are mounted on the common frame 18 including the circle feeder 13 and the blower 14.
[0026]
In the above configuration, when the weight indicator WI confirms that a predetermined amount of combustible dust is stored in the combustible dust hopper 3, the switching damper 4 of the pipe 5 is opened (see FIG. 4), and further The damper 17a is opened and the lower damper 17b is closed, the combustible dust is cooled, the motor M of the screw shaft 16b of the sieving device 16 is driven, the screw conveyor 16c is rotated, and the combustible dust is sent to the cooling drum 16d. . The combustible dust is cooled to a temperature not ignited by the cooling drum 16d, for example, about 40 ° C., and sent to the sieve 16f. The combustible dust under the sieve falls to the lower damper 17b from the discharge port 16g, and the dust on the sieve Falls to the dust transport line on the sieve from the discharge port 16i.
[0027]
The combustible dust is supplied while adjusting the rotation speed of the motor M with the weight indicating controller WIC of the combustible dust hopper 3 (see FIG. 4). When the predetermined amount of combustible dust is cut out, the upper damper 17a is closed, and then the lower damper 17b is opened, and the combustible dust is put into the combustible dust blowing device 12.
[0028]
After the loading, the lower damper 17b is closed and the upper damper 17a is opened. The subsequent operations of the upper damper 17a and the lower damper 17b are repeated.
[0029]
The combustible dust in the blowing device 12 is blown into the tuyere 15 by the blower 14 by adjusting the number of rotations of the circle feeder 13 by the motor M with the weight indicating controller WIC to adjust the blowing amount.
[0030]
Example 2
FIG. 2 is an explanatory view showing a second embodiment of the present invention. The same components as those shown in FIG. 4 are denoted by the same reference numerals, and the description thereof is omitted.
[0031]
In FIG. 2, a hopper 19 for temporarily storing flammable dust and a rotary seal valve for cutting out the flammable dust at a lower portion of a dust remover 2 such as a cyclone for collecting the flammable dust generated and scattered in the waste melting furnace 1. A cutting device 20 is installed.
[0032]
In the combustible dust conveyance path between the cutting device 20 and the blowing device 12, combustible dust cooling for cooling and sieving the combustible dust, the sieve device 22 is connected to the cutting device 20 via the damper 21. Has been. A hopper 23 having a flat bottom surface for injecting combustible dust into the blowing device 12 is installed below the sieve 22a of the flammable dust cooling and sieving device 22, and a stirring type discharger 24 is installed below the hopper 23. Yes. The hopper 23 is connected to the blowing device 12 via a damper 25.
[0033]
The combustible dust cooling and sieving device 22 cools the flammable dust by the cooling drum 22c and conveys it to the sieve 22a via, for example, the screw conveyor 22b. The sieve 22a discharges dust from which lumps or the like that hinder the conveyance from combustible dust are discharged to the hopper 23 as sieving dust, and the discharger 24 below the hopper 23 rotates the stirring blade 24a by the motor M. The blower 12 is charged.
[0034]
Further, a combustible dust transport path is provided between the blowing device 12 and the combustion chamber 9, and the combustible dust transport path and a combustible dust transport path between the tuyere 15 and the blowing device 12 are provided. Switching is possible by opening and closing the dampers 26a and 26b.
[0035]
In the above configuration, the damper 21 is opened, the damper 25 is closed, the combustible dust is cooled, the motor M of the sieving device 22 is driven, the screw conveyor 22b is rotated, and the combustible dust is removed by the cutting device 20. Is cut out and sent to the cooling drum 22c. The combustible dust is cooled to a temperature at which it is not ignited by the cooling drum 22 c, for example, about 40 ° C. and sent to the sieve 22 a, and the combustible dust under the sieve is discharged to the hopper 23.
[0036]
When the discharge of the predetermined amount of combustible dust is completed, the damper 21 is closed, and then the damper 25 is opened to introduce the combustible dust into the blowing device 12. At that time, the rotary seal valve of the cutting device 20 is temporarily stopped, and combustible dust is temporarily stored in the hopper 19.
[0037]
After the introduction, the damper 25 is closed and the damper 21 is opened. Subsequent operations of the damper 21 and the damper 25 are repeated.
[0038]
The combustible dust in the blowing device 12 is blown into the tuyere 15 by the blower 14 by adjusting the number of rotations of the circle feeder 13 by the motor M with the weight indicating controller WIC to adjust the blowing amount. At this time, the damper 26a is closed and the damper 26b is opened.
[0039]
On the other hand, by opening the damper 26 a and closing the damper 26 b, the combustible dust transport path is switched to the transport path toward the combustion chamber 9, and combustible dust is blown into the combustion chamber 9.
[0040]
Example 3
FIG. 3 is an explanatory view showing a third embodiment of the present invention. The same components as those shown in FIG. 2 are denoted by the same reference numerals, and the description thereof is omitted.
[0041]
In the present embodiment, in the combustible dust conveyance path between the cutting device 20 and the blowing device 12, the combustible dust cooling and sieving device 22 for cooling and sieving the combustible dust, the upper device 27a and the lower material 27b. The flammable dust cooling and sieving device 22 is directly connected to the blowing device 12.
[0042]
In this configuration, when the upper damper 27a is opened and the lower damper 27b is closed and the discharge of the predetermined amount of combustible dust is completed, the upper damper 27a is closed and the upper damper 27a and the lower damper 27b are equalized. Therefore, the pressure equalizing valve 27c is opened, and if it is confirmed that the pressure is equalized, the lower damper 27b is opened to discharge the combustible dust to the combustible dust cooling and sieving device 22. At that time, the rotary seal valve of the cutting device 20 is temporarily stopped, and after the combustible dust is temporarily stored in the hopper 19, the pressure equalizing valve 27c and the lower damper 27b are closed, and the upper damper 27a is opened. The subsequent operations of the upper damper 27a, the lower damper 27b, and the pressure equalizing valve 27c are repeated.
[0043]
Next, the motor M of the combustible dust cooling and sieving device 22 is driven, the screw conveyor 22b is rotated, and the combustible dust discharged by the lower damper 27b is sent to the cooling drum 22c. The combustible dust is cooled to a temperature at which it is not ignited by the cooling drum 22c, for example, about 40 ° C. and sent to the sieve 22a, and the combustible dust under the sieve is discharged to the blowing device 12.
[0044]
The combustible dust in the blower 12 is blown into each tuyere 15 by a blower after the level of LA is adjusted by the motor M to adjust the rotation speed of the circle feeder 13 and the blower amount is adjusted.
[0045]
【The invention's effect】
In the first aspect of the invention, the combustible dust cooling and sieving device includes a rotating drum type cooling device that has a high flammable dust cooling capacity and requires a small installation space, and a rotary screen that has excellent durability because of the rotary type. This is one device and the equipment cost is reduced. Moreover, since cooling water is supplied to a rotating drum type cooling device via the screw shaft of a screw conveyor, the cooling efficiency improves.
[0046]
In the invention of claim 2, since the cooling of the combustible dust and the sieving device are integrated and arranged in the casing, the installation space for the facility is small, and the construction construction cost, the installation construction cost and the design cost are greatly increased. Become cheap. Further, since cooling water is supplied to the cooling device for the combustible dust and the rotating drum type cooling device of the sieving device via the screw shaft of the screw conveyor, the cooling efficiency is improved.
[Brief description of the drawings]
FIG. 1 is an explanatory diagram showing a first embodiment of the present invention.
FIG. 2 is an explanatory view showing a second embodiment of the present invention.
FIG. 3 is an explanatory diagram showing a third embodiment of the present invention.
FIG. 4 is an explanatory diagram of a conventional combustible dust supply line.

Claims (2)

廃棄物溶融炉からの可燃性ダストを除塵器で捕集し、捕集した可燃性ダストを可燃性ダストホッパーから切り出して吹込装置へ搬送し、羽口から空気搬送により吹き込む廃棄物溶融炉の可燃性ダスト吹込設備において、
可燃性ダストホッパーと吹込装置との間の可燃性ダストの搬送経路に、可燃性ダストを切り出すスクリューコンベアとそのスクリューコンベアと同軸に連結されて回転する可燃性ダストを冷却するための円筒形の回転ドラム式冷却装置、さらにその回転ドラム式冷却装置と同軸に連結されて回転する円筒形の回転篩を設け、その回転篩の下方に可燃性ダストの排出口を設け、その回転篩の出側の下方に可燃性ダスト中の大塊の排出口を設けた可燃性ダストの冷却、篩装置を1つの装置にし、前記回転ドラム式冷却装置には、前記スクリューコンベアのスクリュー軸を介して冷却水を供給することを特徴とする廃棄物溶融炉の可燃性ダスト吹込設備。
Combustible dust from a waste melting furnace is collected by a dust remover, and the collected combustible dust is cut out from a combustible dust hopper and transported to a blowing device. In the dust blowing equipment
A screw conveyor that cuts out the combustible dust in the combustible dust transfer path between the combustible dust hopper and the blowing device, and a cylindrical rotation for cooling the combustible dust that is connected to the screw conveyor and rotates coaxially. drum-type cooling device, further the rotary drum-type cooling device and the rotation sieve cylindrical rotating coupled coaxially provided, the outlet of the combustible dust below the rotating sieve is provided, the rotating sieve outlet side of the The combustible dust cooling and sieving device provided with a large mass outlet in the combustible dust below is a single device, and cooling water is supplied to the rotating drum type cooling device via the screw shaft of the screw conveyor. A combustible dust blowing facility for a waste melting furnace characterized by supplying.
廃棄物溶融炉からの可燃性ダストを除塵器で捕集し、捕集した可燃性ダストを可燃性ダストホッパーから切り出して吹込装置へ搬送し、羽口から空気搬送により吹き込む廃棄物溶融炉の可燃性ダスト吹込設備において、
可燃性ダストホッパーと吹込装置との間の可燃性ダストの搬送経路に、可燃性ダストを切り出すスクリューコンベアとそのスクリューコンベアと同軸に連結されて回転する可燃性ダストを冷却するための円筒形の回転ドラム式冷却装置、さらにその回転ドラム式冷却装置と同軸に連結されて回転する円筒形の回転篩を設け、その回転篩の下方に可燃性ダストの排出口を設け、前記回転ドラム式冷却装置には、前記スクリューコンベアのスクリュー軸を介して冷却水が供給される可燃性ダスト冷却、篩装置を一体化してケーシング内に配設したことを特徴とする廃棄物溶融炉の可燃性ダスト吹込設備。
Combustible dust from a waste melting furnace is collected by a dust remover, and the collected combustible dust is cut out from a combustible dust hopper and transported to a blowing device. In the dust blowing equipment
A screw conveyor that cuts out the combustible dust in the combustible dust transfer path between the combustible dust hopper and the blowing device, and a cylindrical rotation for cooling the combustible dust that is connected to the screw conveyor and rotates coaxially. A drum-type cooling device , and a cylindrical rotary sieve rotating coaxially with the rotary drum-type cooling device are provided. A combustible dust discharge port is provided below the rotary sieve, and the rotary drum-type cooling device is provided. Is a combustible dust cooling facility for a waste melting furnace, in which combustible dust cooling and a sieving device to which cooling water is supplied via a screw shaft of the screw conveyor are integrated and disposed in a casing.
JP2003046112A 2002-06-24 2003-02-24 Combustible dust injection equipment for waste melting furnaces Expired - Lifetime JP4129191B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2003046112A JP4129191B2 (en) 2002-06-24 2003-02-24 Combustible dust injection equipment for waste melting furnaces

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
JP2002182865 2002-06-24
JP2003046112A JP4129191B2 (en) 2002-06-24 2003-02-24 Combustible dust injection equipment for waste melting furnaces

Publications (2)

Publication Number Publication Date
JP2004085174A JP2004085174A (en) 2004-03-18
JP4129191B2 true JP4129191B2 (en) 2008-08-06

Family

ID=32071552

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2003046112A Expired - Lifetime JP4129191B2 (en) 2002-06-24 2003-02-24 Combustible dust injection equipment for waste melting furnaces

Country Status (1)

Country Link
JP (1) JP4129191B2 (en)

Also Published As

Publication number Publication date
JP2004085174A (en) 2004-03-18

Similar Documents

Publication Publication Date Title
JP4721601B2 (en) Method and apparatus for incineration of combustible waste during the manufacture of cement clinker
CN109442387A (en) Biomass rotary fire grate combustor
JP2000167487A (en) Classifier with dryer
JP4129191B2 (en) Combustible dust injection equipment for waste melting furnaces
JP4377825B2 (en) Waste melting furnace operation method
CN209371225U (en) Biomass rotary fire grate combustor
JP2001246276A (en) Installation for pulverizing coal
JP3506617B2 (en) Method and apparatus for discharging pyrolysis residue
EP1734322B1 (en) Method and apparatus for recovering energy from waste materials by combustion in a cement clinker production line
JP6534423B2 (en) Fly ash cooling system
JPH08159430A (en) Method of combustion treatment for rubber waste
JP2959899B2 (en) Crushing and drying equipment for wet ash
JP3811322B2 (en) Incineration equipment for combustible dust in waste melting furnaces
JP2000097425A (en) Waste melting system
JP3940636B2 (en) Waste melting furnace combustible dust treatment facility
JP3637230B2 (en) Maintenance method and maintenance apparatus for pyrolysis drum equipment
JP4392137B2 (en) Method and apparatus for treating combustible dust in waste melting furnace
JP2004188292A (en) Apparatus and method for treating fly ash
JP4188548B2 (en) Method for predicting properties of coal ash and manufacturing method for artificial lightweight aggregate
JP2005066423A (en) Pyrolysis residue separator
JP2005155974A (en) Method and system of treating incinerated ash prior to melting
JP4173025B2 (en) Dust supply device and fluidized bed furnace system
JP2001334215A (en) Heat decomposition residue sorting device
JP4355663B2 (en) Method of blowing combustible dust in waste melting furnace
JP3905845B2 (en) Melting equipment

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20050914

A711 Notification of change in applicant

Free format text: JAPANESE INTERMEDIATE CODE: A712

Effective date: 20060804

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A821

Effective date: 20060818

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20060818

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20070914

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20071026

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20080111

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20080227

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20080418

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20080516

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110523

Year of fee payment: 3

R150 Certificate of patent or registration of utility model

Ref document number: 4129191

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150

Free format text: JAPANESE INTERMEDIATE CODE: R150

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110523

Year of fee payment: 3

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120523

Year of fee payment: 4

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20120523

Year of fee payment: 4

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

S531 Written request for registration of change of domicile

Free format text: JAPANESE INTERMEDIATE CODE: R313531

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20130523

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20140523

Year of fee payment: 6

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

S533 Written request for registration of change of name

Free format text: JAPANESE INTERMEDIATE CODE: R313533

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

S111 Request for change of ownership or part of ownership

Free format text: JAPANESE INTERMEDIATE CODE: R313115

R350 Written notification of registration of transfer

Free format text: JAPANESE INTERMEDIATE CODE: R350

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

EXPY Cancellation because of completion of term