JP3600811B2 - Waste support plate in vertical incinerator and control method thereof - Google Patents

Waste support plate in vertical incinerator and control method thereof Download PDF

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JP3600811B2
JP3600811B2 JP2001251639A JP2001251639A JP3600811B2 JP 3600811 B2 JP3600811 B2 JP 3600811B2 JP 2001251639 A JP2001251639 A JP 2001251639A JP 2001251639 A JP2001251639 A JP 2001251639A JP 3600811 B2 JP3600811 B2 JP 3600811B2
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support plate
refuse
incinerator
layer
combustion
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JP2003065518A (en
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雄二 栗原
将人 山入
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Plantec Inc
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Plantec Inc
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Description

【0001】
【発明の属する技術分野】
本発明は、医療系廃棄物を含む産業廃棄物や、ごみ質の変動が大きい一般廃棄物を焼却する竪型焼却炉におけるごみ支持板及びその制御方法に関する。
【0002】
【従来の技術】
産業廃棄物は、有害物質が多く含まれるだけでなく、高発熱量物質や難燃物あるいは、不燃物が混在しているほか、固体・液体・粘体とその性状は多種多様であるため、過去に使用されていた固定バッチ燃焼式焼却炉では、このような産業廃棄物の完全焼却処理は非常に困難であった。
【0003】
特に、ごみ質のバラツキが大きく、病源性ウイルスを含む危険な感染性物質や、ガラス等の溶融しやすい物質を含む医療系廃棄物の焼却処理として一般に用いられている、ロータリーキルン式、または傾斜回転炉床式等の焼却炉は、何れも廃棄物を転回・攪拌して燃焼させる方式であるために、燃えやすい物だけが先燃えして、難燃物が残る燃えむらができて完全焼却・滅菌は不可能であるだけでなく、炉出口部にガラス類が溶融・付着して操業継続ができなくなるという欠陥があった。
【0004】
また、ごみ質の変動が大きい一般廃棄物を焼却する場合も同様の現象が生じていた。
【0005】
図5は、これらの問題を解決するために、特開平4−158110号公報に開示された「竪型焼却炉及びその焼却方法」の概要を示す縦断面図である。
【0006】
図5において、焼却炉本体aの頂部には燃焼ガス排出口bが、上部にはフィーダを有するホッパcと着火用バーナdとが設置され、焼却炉本体a内下方には出没自在なごみ支持板e,eが設けられ、底部には開閉自在な焼却灰排出板f,fが配置されている。
【0007】
上記ごみ支持板e,eは、通常は図示するように焼却炉本体a内から没した状態に配置され、焼却灰排出板f,fが開放して焼却灰を排出する時にのみ、図において1点鎖線で示すように灰層gの上層に突出して、このごみ支持板e,eよりも上部にあるごみ及び燃焼した焼却灰の荷重を支持する。
【0008】
また、ごみ支持板e,eが位置する焼却炉本体aの両側には、ごみ支持板e,eが焼却炉本体a内から没した時に、このごみ支持板e,eを収納する収納室h,hが設けられており、焼却炉本体aと収納室h,hとの間に形成された間隙i,iから焼却灰が収納室h,h側に進入しないように、常温の空気jが供給されている。
【0009】
焼却灰排出板f,fは焼却炉本体aの底部において、水平位置から1点鎖線で示す垂直位置まで開閉自在に設けられている。そして、ごみ支持板e,eによって焼却炉本体a内下部の灰層gの上層から上を支持したのち、焼却灰排出板f,fを下方に転回することによって、焼却灰を焼却炉本体aの下方に設けられた灰搬出装置kに排出することができる。
【0010】
つまり、前記ごみ支持板e,eは、焼却灰排出板f,fによる焼却灰の排出を補助するために設けられている。
【0011】
また、焼却炉本体aの上部、中部、下部にはそれぞれ温度調節された燃焼用空気m,n,pがダンパq,r,sを介して供給されている。これら燃焼用空気m,n,pはごみ質に応じて最適の温度に調節されている。
【0012】
焼却炉本体aのホッパcの反対側に設置された着火用バーナdは、始業時のごみ着火または炉内温度低下時の助燃に利用される。
【0013】
次に、このように構成された竪型焼却炉によるごみの焼却方法について説明する。
【0014】
ここで、平常操業時における焼却炉本体a内では、ごみの燃焼状態により位置が移動するものの、上から火炎層t、ごみ層u、おき燃焼層v及び灰層gを形成している。
【0015】
ホッパcから焼却炉本体a内に供給されたごみは、始業時においては焼却炉本体aの底部にある灰層g上に堆積され、着火用バーナdにより加熱され、燃焼用空気m,nによって燃焼を始め、燃え易いごみから焼却されて灰となり、難燃性のごみとともに火種を保有しながらおき燃焼層vに堆積する。
【0016】
その状態でごみを供給すれば、ごみはごみ層uに堆積され、おき燃焼層vの熱と燃焼用空気mにより易燃物から着火を始め、徐々に燃焼がごみ層u全体に拡がって、平常操業状態に移行する。
【0017】
この燃焼時において、おき燃焼層v及びごみ層uの下層で発生した燃焼ガスwは、ごみ層u内を通過して上昇し、その熱で上部のごみの着火及びガス化を促進するとともに、生ごみの乾燥を行う。
【0018】
さらに、火炎層tまで上昇した燃焼ガスwは、この上部に供給されている常温の2次空気xによって再燃焼されたのち、燃焼ガス排出口bから排ガスとして次工程に排出される。
【0019】
この火炎層tにおける燃焼時の放射熱によって、ごみ層に投入されたごみの予備乾燥を行うとともに、発火点の低い紙やプラスチックスを燃やして火種になるのを促進する。
【0020】
焼却灰の燃焼が完結すると、この段階でごみ支持板e,eを焼却炉本体a内の灰層gの上層に突出させ、ごみ支持板e,eよりも上部に位置するごみ層u、おき燃焼層v、灰層gの上層の焼却灰及びごみの荷重を支持する。
【0021】
この突出時において、ごみ支持板e,eの位置ではごみの燃焼が完結しているため、ごみによる抵抗が少なく、ごみ支持板e,eはスムースに突出することができる。
【0022】
このようにごみ支持板e,eを突出させたのち、焼却灰排出板f,fを下方に転回させ、ごみ支持板e,eよりも下方の焼却灰を灰搬出装置kに落下させる。
【0023】
焼却灰排出後は、焼却灰排出板f,fを上方に復帰させたのち、ごみ支持板e,eを焼却炉本体a内から収納室h,h内へと没し、ごみ支持板e,eの上部にある残余の焼却灰及びおき燃焼層vの焼却残渣を底部の焼却灰排出板f,f上に落下させるとともに、ごみ層uも頂次落下させる。
【0024】
この落下時のショックにより、灰層gの通気性が良くなるのみでなく、おき燃焼層v及びごみ層uにおける未燃物の塊が崩壊されるため、層全体の通気性が良くなるとともに、塊の内部まで空気が通るようになる。このため、高温の燃焼空気n,pを供給すると残留していた火種により、焼却灰中の未燃物が容易に燃焼する。
【0025】
【発明が解決しようとする課題】
しかしながら、図5に示す従来の竪型焼却炉では、産業廃棄物、特に医療系廃棄物の場合には、ごみ質が多様化しているため、完全燃焼・滅菌が困難なだけでなく、その中に多量に含まれている注射器、試験管や瓶等のガラス類が400〜700℃で軟化・溶融したり、発泡スチロール等のプラスチック類や紙・繊維類等の高発熱量物質の部分燃焼による高熱で、灰分が溶融して強固なクリンカが発生することが多い。
【0026】
そのため、焼却炉本体aの下方のおき燃焼層v付近において閉塞事故が発生して上方のごみや焼却灰の降下を阻害してその除去のために操業を停止したり、単純な単板構造または、例えば櫛形をした複数の支持棒を併設した形状で強制冷却手段を有しない場合には、上記クリンカがごみ支持板e,eの突出を阻害して最悪の場合にはごみ支持板e,eを損傷するという問題点があった。
【0027】
また、竪型焼却炉が大容量になると、ごみ支持板e,eは片持構造であるためにその強度が不足して、クリンカが発生した場合にごみ支持板e,eが折損することがあった。
【0028】
さらに、下部の灰を焼却灰排出板f,f上に落下させる際に、不燃分が少ない場合には灰層gの層厚が薄くなり、おき燃焼層vの一部が落下して空間Gで燃焼し、また、未燃物が残存している場合には、上記落下時のショックで未燃物が崩壊して、同じく空間Gで燃焼するために、クリンカが発生して、焼却灰Aの排出時に突出するごみ支持板e,eを損傷する虞があった。
【0029】
【課題を解決するための手段】
請求項1に係る発明の竪型焼却炉におけるごみ支持板は、産業廃棄物や一般廃棄物を焼却する竪型焼却炉において、焼却炉下端に配設された開閉自在な焼却灰排出板の上方に若干の空間を隔てて位置し、焼却灰排出時に焼却炉内に突出して、焼却炉内に堆積するごみ及び焼却灰の荷重を支持するごみ支持板であって、上記ごみ支持板は、冷却用流体貫流のために中空構造とした複数の管体を配置して強度を増強したうえ、これら管体先端を中空の突出部で繋いだ構造の支持棒を取付枠上に複数列併設した支持板本体を備え、該支持板本体は冷却用流体により冷却されて、外部駆動機構により出没自在になされるとともに、上記ごみ支持板の炉内への突出時に各支持棒先端の突出部を挿入保持する複数の挿入孔を有する耐熱構造の支持板保持部を、ごみ支持板に対峙する中間位置に設けたものである。
【0030】
請求項2に係る発明の竪型焼却炉におけるごみ支持板の制御方法は、産業廃棄物や一般廃棄物を焼却する竪型焼却炉において、焼却炉下端に配設された開閉自在な焼却灰排出板の上方に若干の空間を隔てて位置し、焼却灰排出時に焼却炉内に突出して、焼却炉内に堆積するごみ及び焼却灰の荷重を支持するごみ支持板の制御方法であって、上記焼却灰排出板とごみ支持板の空間に設けられた空間温度検出器の検出値が設定値を超えた場合には、警報を発して、焼却灰排出板の開放動作を停止するとともにごみ支持板を後退させることを特徴とする。
【0032】
【発明の実施の形態】
以下、本発明の実施の形態について図面を参照して説明する。
【0033】
図1は、本発明に係る竪型焼却炉要部の概略構成を示す縦断面図であり、図2は該焼却炉におけるごみ支持板の概略構造を示す平面図、図3は同支持板及び支持板保持部の概略構造を示す縦断面図である。なお、図5で説明した部材と同一の部材には同一の符号を付し、詳細説明は省略する。
【0034】
図1において、1は焼却炉本体であり、上部耐火物11と下部耐火物12及びこれら上部耐火物11と下部耐火物12を囲繞する鋼材によって構築されている。
【0035】
この焼却炉本体の上半分に位置する火炎層tには、その側部に生ごみRの投入口13が開閉自在な投入ダンパを備えて設けられるとともに、上部耐火物11の側壁部には着火用バーナd及び、図示しない温度検出器、炉内監視カメラ等が配設され、また、燃焼ガスwの旋回兼2次燃焼のために、常温の2次空気xを送入する複数の燃焼ガス旋回兼用の2次空気ノズル14が配設されている。
【0036】
焼却炉本体1の中間部以降は、ごみ層を厚くして性状の異なるごみ質を平準化させるために漏斗状に絞られているが、該漏斗部の側壁を構成する下部耐火物12の上方の角部15から下の外面は、例えば上部は空冷ジャケット16、下部は水冷ジャケット17に分割された冷却ケーシングによって冷却されており、おき燃焼層vと灰層gとには、複数の温度検出器群18と図示しないレベル測定用検出座が設けられている。
【0037】
そして漏斗部分に形成されるごみ層u、おき燃焼層vと灰層gとには、押込送風機21から各層に燃焼空気22a〜cを供給する複数の燃焼用1次空気ノズル23a〜cがダンパ24a〜cを伴って適宜配設されている。
【0038】
焼却炉本体1の底部には、出没動作が容易にできるように、図2及び図3にその一例を示すような1対のごみ支持板3,3と支持板保持部4及び、該支持板3,3の下方に空間G(図1参照)を隔てて開閉自在な焼却灰排出板f,fとが、後述する外部駆動機構等を備えて配設されている。
【0039】
上述のごみ支持板3,3は、強度と耐熱性を高めるために、例えば、中空構造の管体としての角パイプ31を上下2段に積重ねて溶接したうえ、該両パイプの先端に流体通路を有する突出部32を接続した構造の支持棒33を取付枠34に複数列併設した支持板本体Eに、冷却用流体の導入管35と同排出管36及びごみ支持板3,3の外部駆動機構37を備えて水平方向に配置したものである。
【0040】
支持板保持部4は、図3に一例を示す如く、上部に冷却手段を備えケーシング38に取付けられた山形部41と、複数の支持棒33の突出部32を挿入保持するための複数の挿入孔42が配設された側板43とからなり、側板43の両端はケーシング38に固定され、下端は開放されている。
【0041】
上述のごみ支持板3,3と支持板保持部4及び、焼却灰排出板f,fとは、ケーシング38に内蔵されており、このケーシング38は、その側面に空間温度検出器39と、後述の高温の後燃焼空気25を供給する後燃焼空気ダクト26が接続されるとともに、下部は灰搬出装置kに挿入されている。
【0042】
一方、焼却炉本体1の上方には、燃焼ガス旋回兼用の2次空気ノズル14からの空気噴射により回転運動を始めた燃焼ガスwを更に確実に旋回せしめるための排ガス混合手段51を介して再燃焼室52が載置されており、該再燃焼室52の天井部には、空気予熱器53が配設され、図示しないガス冷却室へと連接されている。
【0043】
なお、焼却炉本体1及び再燃焼室52と空気予熱器53との外部は、図示しない保温材等で保温工事が施されている。
【0044】
次に、このように構成された竪型焼却炉における各廃棄物の燃焼状況及びごみ支持板の操作状況について、主に焼却炉本体1の下部における状況を説明した図4により、必要に応じて図1及び図3を参照して説明する。なお、火炎層t、ごみ層u、おき燃焼層vと灰層gの形成状況及び、平常操業状態に移行するまでの燃焼状態については、前述の従来技術と同様であるので、詳細説明は省略する。
【0045】
平常操業状態において、ごみ層uでは、火炎層tでの燃焼ガスw及び後述の未燃ガス61の2次燃焼による放射熱がごみ層uの表面に照射されるとともに、燃焼空気22aの供給と、おき燃焼層vから上昇する未燃ガス61の加熱によって、プラスチック類や紙・繊維類等の高発熱量の易燃物が着火されてガス化燃焼し、水分の多いごみや雑誌等の難燃物は、乾燥されるとともに炭化燃焼を続けて末燃ガス61を発生させる。
【0046】
この際、下部耐火物12の上部は、冷却送風機62により送風された常温の空気jで冷却された空冷ジャケット16で徐冷されているため、表面は700℃程度以下を保持できており、漏斗部での燃焼を阻害することはなく、また、易燃物の部分燃焼によるクリンカの溶着を防止している。
【0047】
おき燃焼層vは、ごみ層uで燃焼できなかった未燃炭化物や難燃物を、後述する灰層gから上昇する熱気と、燃焼空気22bと22cとの供給を受けて、時間をかけておき燃焼させる部位であり、該おき燃焼により未燃ガス61が発生される。
【0048】
この際、下部耐火物12下部の表面温度は、冷却水で冷却された水冷ジャケット17の冷却効果により400〜500℃に止まり、ガラス溶融物の溶着・固化を防止している。
【0049】
また、灰層gは、空気予熱器53によって250〜300℃程度に加熱された後燃焼空気25(図1参照)と燃焼空気22cとの送入によって、なおかつ残留する未燃炭化物を燃焼し尽くして焼却灰Aとするとともに、焼却灰Aを冷却して熱気を上部のおき燃焼層vに供給する部位であり、灰層g下部の焼却灰Aは、前述の後燃焼空気25の通気と水冷ジャケット17によって300℃程度まで冷却されている。
【0050】
この灰層gは、複数の温度検出器群18(図1参照)の検出値によって燃焼進行状態を確認した結果で制御されるごみ支持板3,3及び焼却灰排出板f,fの動作により、灰搬出装置kに排出されるまで滞留される。
【0051】
上記操業において、ごみ中の不燃分が少ない場合には灰層gの層厚が薄くなり、焼却灰Aの排出時におき燃焼層vの一部が空間Gに落下しておき燃焼を始めたり、未燃物の塊が残存して空間Gへの落下時のショックで崩壊して燃焼を始める場合には、空間Gの温度が上昇してクリンカを発生させるとともに、次回の焼却灰排出のために突出させたごみ支持板3,3を加熱する虞がある。
【0052】
そのために、突出中の支持板本体Eを冷却するとともに、空間温度検出器39の設定温度以上に空間Gの温度が上昇した場合には、警報を発して上述の焼却灰排出板f,fを閉止したままごみ支持板3,3を収納室h,h内に後退させて空間Gの温度回復を図る。
【0053】
一方、火炎層tで2次燃焼を終えた燃焼ガスwは、排ガス混合手段51を通過することにより旋回流となって再燃焼室52内に入り、滞留時間を有効に延長して再燃焼を完結した結果、残留するダイオキシン類を完全に熱分解した再燃焼ガス63となって上昇し、空気予熱器53を通過したのち、図示しない次工程のガス冷却室に入る(図1参照) 。
【0054】
この空気予熱器53を通過する際に、空冷ジャケット16を冷却して昇温した温空気64と熱交換して高温となった後燃焼空気25は、後燃焼空気ダクト26を経て後燃焼空気ノズル27からケーシング38内に送入され、灰層gの冷却とおき燃焼層vのおき燃焼を行う(図1参照) 。
【0055】
冷却送風機62から送風された常温の空気jは、上述の空冷ジャケット16の冷却以外に、ごみ支持板3,3及び支持板保持部4に送られ、一方は冷却用流体の導入管35から取付枠34を通じて中空構造の角パイプ31と突出部32を通って支持棒33を冷却した後、排出管36から排出され、他方は山形部41を通過して支持板保持部4を冷却する。さらに収納室h,hに送られた常温の空気jは、間隙i,iから灰層g側に送出されて、収納室h,hへの灰の進入を防いでいる(図3参照) 。
【0056】
なお、冷却ケーシングは空冷ジャケット16と水冷ジャケット17との組み合わせで説明したが、その組み合わせ及び冷却媒体の種類を固定するものではなく、ごみ支持板3,3と支持板保持部4の冷却媒体を常温の空気jで説明したが、冷却水を使用しても差支えない。
【0057】
また、支持棒33は中空構造の角パイプ31を積重ねて溶接すると説明したが、強度を増強する方法であれば、いかなる形状を採用してもよい。
【0058】
さらに、ごみ支持板3,3と焼却灰排出板f,fは左右各1対のものを図示したが、その対の数はいくつでもよく、焼却灰排出板f,fは、その機能を発揮する物であれば形状を特定するものではない。
【0059】
【発明の効果】
以上述べたように、本発明の竪型焼却炉におけるごみ支持板及びその制御方法によれば、ごみ支持板は中空構造の複数の管体を配置して冷却する構造であるために、強度が増加するとともに耐熱性も向上して、クリンカによるごみ支持板の突出動作の阻害や損傷あるいは焼損を防止することができる。
【0060】
また、耐熱構造の支持板保持部が配設されているため、ごみ支持板の突出時にその先端を保持でき、特に大容量の焼却炉の場合にごみ支持板の強度を増加させている。
【0061】
さらに、焼却灰排出板とごみ支持板の空間に設けられた空間温度検出器により、当該空間における温度過上昇の場合に焼却灰Aの排出操作を停止することができ、ごみ支持板の焼損を防止することができる。
【図面の簡単な説明】
【図1】本発明に係る竪型焼却炉要部の概略構成を示す縦断面図である。
【図2】竪型焼却炉におけるごみ支持板の概略構造を示す平面図である。
【図3】ごみ支持板及び支持板保持部の概略構造を示す縦断面図である。
【図4】主に焼却炉本体の下部における状況を説明するための縦断面図である。
【図5】従来の竪型焼却炉及びその焼却方法の概要を示す縦断面図である。
【符号の説明】
1 焼却炉本体
3 ごみ支持板
31 角パイプ(管体)
32 突出部
33 支持棒
34 取付枠
37 外部駆動機構
39 空間温度検出器
4 支持板保持部
f 焼却灰排出板
E 支持板本体
[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a refuse support plate in a vertical incinerator for incinerating industrial waste including medical waste and general waste having large fluctuations in refuse quality, and a control method therefor.
[0002]
[Prior art]
Industrial waste contains not only a large amount of harmful substances but also high calorific substances, flame retardants or non-combustibles, and solid, liquid and viscous substances and their properties are diverse. In the fixed batch combustion type incinerator used in the above, complete incineration of such industrial waste was very difficult.
[0003]
In particular, the rotary kiln type or inclined rotation, which is generally used for incineration of dangerous infectious substances containing pathogenic viruses and medical waste containing substances that are easy to melt, such as glass, with large variability in waste quality Since all incinerators, such as hearths, invert and agitate and burn waste, only flammable materials are burned first, and incombustible materials remain, leaving incombustible materials. Not only is sterilization impossible, but the glass also melts and adheres to the outlet of the furnace, making it impossible to continue operation.
[0004]
In addition, the same phenomenon occurred when incinerating municipal waste with large fluctuations in waste quality.
[0005]
FIG. 5 is a longitudinal sectional view showing an outline of a "vertical incinerator and its incineration method" disclosed in Japanese Patent Application Laid-Open No. 4-158110 in order to solve these problems.
[0006]
In FIG. 5, a combustion gas discharge port b is provided at the top of the incinerator main body a, a hopper c having a feeder and an ignition burner d are provided at the top, and a garbage support plate which can be retracted and set inside the incinerator main body a. e and e are provided, and incineration ash discharge plates f and f which can be opened and closed are arranged at the bottom.
[0007]
The above-mentioned refuse support plates e, e are usually arranged in a state of being buried from the incinerator main body a as shown in the figure, and only when the incineration ash discharge plates f, f open to discharge the incineration ash, 1 in FIG. As shown by the dashed line, it protrudes above the ash layer g to support the load of the refuse above the refuse support plates e and the burned incineration ash.
[0008]
Further, on both sides of the incinerator main body a where the refuse support plates e and e are located, a storage chamber h for storing the refuse support plates e and e when the refuse support plates e and e are submerged from the inside of the incinerator main body a. , H are provided, and air j at normal temperature is supplied from the gaps i, i formed between the incinerator body a and the storage chambers h, h so that the incineration ash does not enter the storage chambers h, h. Supplied.
[0009]
The incineration ash discharge plates f, f are provided at the bottom of the incinerator main body a so as to be openable and closable from a horizontal position to a vertical position indicated by a chain line. Then, after the ash layer g at the lower portion in the incinerator main body a is supported from the upper layer by the refuse support plates e, e, the incineration ash is turned down by turning the incineration ash discharge plates f, f downward. Can be discharged to an ash discharge device k provided below the ash discharge device.
[0010]
That is, the refuse support plates e, e are provided to assist the incineration ash discharge by the incineration ash discharge plates f, f.
[0011]
Further, combustion air m, n, and p whose temperature has been adjusted are supplied to upper, middle, and lower portions of the incinerator body a via dampers q, r, and s, respectively. These combustion airs m, n, and p are adjusted to optimal temperatures according to the quality of the refuse.
[0012]
The ignition burner d installed on the side of the incinerator main body a opposite to the hopper c is used for igniting dust at the start of operation or assisting combustion when the temperature in the furnace is lowered.
[0013]
Next, a method of incinerating refuse using the vertical incinerator thus configured will be described.
[0014]
Here, in the incinerator main body a during normal operation, although the position moves depending on the combustion state of the refuse, a flame layer t, a refuse layer u, a flammable combustion layer v, and an ash layer g are formed from above.
[0015]
The refuse supplied from the hopper c into the incinerator main body a is deposited on the ash layer g at the bottom of the incinerator main body a at the start of operation, is heated by the ignition burner d, and is heated by the combustion air m, n. Starting from the combustion, the flammable waste is incinerated into ash, and is deposited on the combustion layer v while holding a fire with the flame-resistant waste.
[0016]
If the refuse is supplied in that state, the refuse is deposited on the refuse layer u, and ignited from the flammable material by the heat of the combustion layer v and the combustion air m, and the combustion gradually spreads throughout the refuse layer u. Transition to normal operation.
[0017]
At the time of this combustion, the combustion gas w generated in the lower layer of the primary combustion layer v and the lower layer of the refuse layer u rises through the refuse layer u and promotes the ignition and gasification of the upper refuse by the heat, Dry the garbage.
[0018]
Further, the combustion gas w which has risen to the flame layer t is reburned by the secondary air x at room temperature supplied to the upper portion thereof, and then discharged from the combustion gas outlet b as exhaust gas to the next step.
[0019]
The radiant heat at the time of combustion in the flame layer t performs pre-drying of the refuse introduced into the refuse layer and promotes burning of paper or plastics having a low ignition point to become a fire.
[0020]
When the combustion of the incineration ash is completed, at this stage, the refuse support plates e, e are made to protrude above the ash layer g in the incinerator body a, and the refuse layer u, which is located above the refuse support plates e, e, is disposed. It supports the load of incineration ash and refuse in the upper layer of the combustion layer v and the ash layer g.
[0021]
At the time of this projection, since the combustion of the refuse is completed at the position of the refuse support plates e, e, the resistance due to the refuse is small, and the refuse support plates e, e can protrude smoothly.
[0022]
After the refuse support plates e, e are thus protruded, the incineration ash discharge plates f, f are turned downward, and the incineration ash below the refuse support plates e, e is dropped into the ash discharge device k.
[0023]
After the incineration ash is discharged, the incineration ash discharge plates f, f are returned to the upper side, and then the refuse support plates e, e are immersed from the incinerator main body a into the storage chambers h, h. The remaining incineration ash at the top of e and the incineration residue of the main combustion layer v are dropped onto the bottom incineration ash discharge plates f, f, and the trash layer u is also dropped to the top.
[0024]
Due to the shock at the time of the drop, not only the air permeability of the ash layer g is improved, but also the lump of unburned matter in the primary combustion layer v and the refuse layer u is collapsed, so that the air permeability of the entire layer is improved, The air passes through to the inside of the mass. Therefore, when the high-temperature combustion air n, p is supplied, the unburned matter in the incineration ash easily burns due to the remaining fire.
[0025]
[Problems to be solved by the invention]
However, in the case of the conventional vertical incinerator shown in FIG. 5, in the case of industrial waste, particularly in the case of medical waste, since the waste quality is diversified, not only complete combustion and sterilization is difficult, but also Glasses such as syringes, test tubes, bottles, etc., contained in large amounts in the softening and melting at 400-700 ° C, or high heat due to partial combustion of high calorific substances such as plastics such as styrofoam and papers and fibers In this case, the ash is often melted to generate a strong clinker.
[0026]
For this reason, a blockage accident occurs in the vicinity of the main combustion layer v below the incinerator main body a, hinders the fall of the upper refuse and incineration ash, and stops the operation for its removal. For example, in the case where a plurality of comb-shaped support rods are provided side by side and the forced cooling means is not provided, the clinker hinders the projection of the dust support plates e, and in the worst case, the dust support plates e, e There was a problem that it was damaged.
[0027]
In addition, when the vertical incinerator has a large capacity, the dust support plates e and e have a cantilever structure, so that their strength is insufficient, and when the clinker occurs, the dust support plates e and e may break. there were.
[0028]
Further, when the lower ash is dropped onto the incineration ash discharge plates f, f, if the non-combustible content is small, the thickness of the ash layer g becomes thinner, and a part of the ash layer v falls and the space G If the unburned matter remains, the unburned matter collapses due to the shock at the time of the fall, and burns in the space G as well. There is a possibility that the dust support plates e, e projecting at the time of discharging the dust may be damaged.
[0029]
[Means for Solving the Problems]
The garbage support plate in the vertical incinerator of the invention according to claim 1 is disposed above the openable and closable incineration ash discharge plate disposed at the lower end of the incinerator in a vertical incinerator for incinerating industrial waste and general waste. A garbage support plate that is located at a small space between the ash and protrudes into the incinerator at the time of incineration ash discharge and supports the load of refuse and incineration ash that accumulates in the incinerator. In order to increase the strength by arranging a plurality of tubes with a hollow structure for fluid flow through the support, a support rod with a structure in which the ends of these tubes are connected by hollow protrusions is arranged in multiple rows on the mounting frame A plate body, the support plate body is cooled by a cooling fluid, and can be made to come and go by an external drive mechanism. At the time of projecting the refuse support plate into the furnace, the projecting portions of the tips of the support rods are inserted and held. Support plate holder with heat resistant structure having multiple insertion holes But on the intermediate position facing the refuse supporting plates.
[0030]
A method for controlling a refuse support plate in a vertical incinerator according to the invention according to claim 2 is a vertical incinerator for incinerating industrial waste or general waste, wherein the openable and closable incineration ash discharge disposed at the lower end of the incinerator is provided. A method for controlling a refuse support plate which is located above a plate with a small space therebetween, protrudes into the incinerator at the time of incineration ash discharge, and supports the load of refuse and incineration ash deposited in the incinerator, If the detected value of the space temperature detector provided in the space between the incineration ash discharge plate and the refuse support plate exceeds the set value, an alarm is issued, the opening operation of the incineration ash discharge plate is stopped, and the refuse support plate Is retracted.
[0032]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, embodiments of the present invention will be described with reference to the drawings.
[0033]
FIG. 1 is a longitudinal sectional view showing a schematic configuration of a main part of a vertical incinerator according to the present invention, FIG. 2 is a plan view showing a schematic structure of a refuse support plate in the incinerator, and FIG. It is a longitudinal cross-sectional view which shows schematic structure of a support plate holding part. Note that the same members as those described in FIG. 5 are denoted by the same reference numerals, and detailed description thereof will be omitted.
[0034]
In FIG. 1, reference numeral 1 denotes an incinerator main body, which is constructed of an upper refractory 11 and a lower refractory 12 and a steel material surrounding the upper refractory 11 and the lower refractory 12.
[0035]
In the flame layer t located in the upper half of the incinerator main body, an input port 13 for the garbage R is provided on its side with an openable and closable input damper, and the side wall of the upper refractory 11 is ignited. A burner d, a temperature detector (not shown), an in-furnace monitoring camera, and the like are provided, and a plurality of combustion gases that feed secondary air x at normal temperature for swirling and secondary combustion of the combustion gas w. A secondary air nozzle 14 for both swirling is provided.
[0036]
After the middle part of the incinerator main body 1, it is squeezed in a funnel shape in order to thicken the refuse layer and level refuse having different properties, but above the lower refractory 12 constituting the side wall of the funnel portion. The outer surface below the corner 15 is cooled by, for example, a cooling casing divided into an air cooling jacket 16 at the upper part and a water cooling jacket 17 at the lower part. An instrument group 18 and a level measurement detection seat (not shown) are provided.
[0037]
A plurality of primary combustion air nozzles 23a to 23c for supplying combustion air 22a to 22c to the respective layers from the forced blower 21 are provided on the refuse layer u, the remaining combustion layer v, and the ash layer g formed in the funnel. 24a to 24c are provided as appropriate.
[0038]
At the bottom of the incinerator main body 1, a pair of refuse support plates 3, 3 and a support plate holder 4, as shown in FIGS. Incinerated ash discharge plates f, f, which can be opened and closed via a space G (see FIG. 1) below 3, 3 are provided with an external drive mechanism and the like to be described later.
[0039]
In order to enhance the strength and heat resistance, for example, the above-mentioned refuse support plates 3 and 3 are formed by stacking and welding two square pipes 31 each having a hollow structure as a tubular body, and furthermore, a fluid passage is provided at the ends of the two pipes. Externally driving the cooling fluid introduction pipe 35 and the cooling fluid discharge pipe 36 and the dust support plates 3, 3 in a support plate body E in which a plurality of rows of support rods 33 having a structure connected to the projections 32 having It has a mechanism 37 and is arranged in the horizontal direction.
[0040]
As shown in an example in FIG. 3, the support plate holding portion 4 includes a cooling portion at an upper portion thereof, a chevron 41 attached to a casing 38, and a plurality of insertions for inserting and holding the protrusions 32 of the plurality of support rods 33. A side plate 43 is provided with a hole 42. Both ends of the side plate 43 are fixed to the casing 38, and the lower end is open.
[0041]
The above-described refuse support plates 3 and 3, the support plate holding portion 4, and the incineration ash discharge plates f and f are built in a casing 38, and the casing 38 has a space temperature detector 39 on a side surface thereof and a later described. A post-combustion air duct 26 for supplying high-temperature post-combustion air 25 is connected, and the lower portion is inserted into the ash discharge device k.
[0042]
On the other hand, above the incinerator main body 1, the combustion gas w which has started to rotate by the air injection from the secondary air nozzle 14, which also serves as the combustion gas swirl, is recirculated via the exhaust gas mixing means 51 for more reliably swirling. A combustion chamber 52 is mounted, and an air preheater 53 is provided on the ceiling of the reburn chamber 52 and is connected to a gas cooling chamber (not shown).
[0043]
The outside of the incinerator main body 1, the reburning chamber 52, and the air preheater 53 is subjected to heat insulation with a heat insulation material (not shown).
[0044]
Next, regarding the combustion state of each waste and the operation state of the refuse support plate in the vertical incinerator configured as described above, the situation mainly in the lower part of the incinerator main body 1 will be described with reference to FIG. This will be described with reference to FIGS. Note that the formation state of the flame layer t, the refuse layer u, the primary combustion layer v, and the ash layer g, and the combustion state up to the transition to the normal operation state are the same as those in the above-described conventional technology, and thus detailed description is omitted. I do.
[0045]
In the normal operation state, in the refuse layer u, the surface of the refuse layer u is irradiated with the radiant heat of the combustion gas w in the flame layer t and the secondary combustion of the unburned gas 61 described below, and the supply of the combustion air 22a is performed. By heating the unburned gas 61 rising from the main combustion layer v, a high calorific value flammable substance such as plastics, paper, or fibers is ignited and gasified and burned, thereby making it difficult to remove garbage or magazines having a lot of moisture. The combustible is dried and carbonized and burned to generate a burned gas 61.
[0046]
At this time, since the upper part of the lower refractory 12 is gradually cooled by the air cooling jacket 16 cooled by the normal temperature air j blown by the cooling blower 62, the surface can be maintained at about 700 ° C. or less, and the funnel It does not hinder combustion in the part, and also prevents clinker welding due to partial combustion of flammable substances.
[0047]
Each of the combustion layers v receives the unburned carbides and flame retardants that could not be burned in the refuse layer u from the ash layer g, which will be described later, and the supply of the combustion air 22b and 22c. This is a site where pre-burning is performed, and unburned gas 61 is generated by the pre-combustion.
[0048]
At this time, the surface temperature of the lower portion of the lower refractory 12 is kept at 400 to 500 ° C. due to the cooling effect of the water cooling jacket 17 cooled by the cooling water, thereby preventing the glass melt from welding and solidifying.
[0049]
Further, the ash layer g is heated to about 250 to 300 ° C. by the air preheater 53, and then burns out the remaining unburned carbon by feeding the combustion air 25 (see FIG. 1) and the combustion air 22c. And the incineration ash A is cooled and the hot air is supplied to the upper combustion layer v. The incineration ash A below the ash layer g is formed by the ventilation of the post-combustion air 25 and the water cooling. Cooled down to about 300 ° C. by the jacket 17.
[0050]
The ash layer g is generated by the operation of the refuse support plates 3 and 3 and the incineration ash discharge plates f and f which are controlled based on the result of confirming the progress of combustion by the detection values of the plurality of temperature detector groups 18 (see FIG. 1). , And stays until discharged to the ash discharge device k.
[0051]
In the above operation, when the amount of incombustibles in the refuse is small, the layer thickness of the ash layer g becomes thin, and when the incineration ash A is discharged, a part of the combustion layer v falls into the space G and starts burning, When the unburned mass remains and collapses due to the shock at the time of falling into the space G to start burning, the temperature of the space G rises to generate clinker and to discharge the next incineration ash. There is a possibility that the projecting dust support plates 3 and 3 may be heated.
[0052]
For this reason, the projecting support plate body E is cooled, and when the temperature of the space G rises above the set temperature of the space temperature detector 39, an alarm is issued and the above-mentioned incineration ash discharge plates f, f are moved. The temperature of the space G is recovered by retreating the dust support plates 3 and 3 into the storage chambers h and h while being closed.
[0053]
On the other hand, the combustion gas w that has completed the secondary combustion in the flame layer t passes through the exhaust gas mixing means 51 to form a swirling flow and enters the reburning chamber 52, effectively extending the residence time to perform the reburning. As a result, the residual dioxins are completely thermally decomposed to form a reburning gas 63, which rises, passes through the air preheater 53, and then enters a gas cooling chamber (not shown) in the next step (see FIG. 1).
[0054]
When passing through the air preheater 53, the post-combustion air 25 is cooled by cooling the air-cooling jacket 16 and exchanges heat with the heated air 64, which becomes high in temperature. The ash layer g is fed into the casing 38 through the ash layer 27, and the ash layer g is cooled and the ignited combustion layer v is ignited (see FIG. 1).
[0055]
The normal-temperature air j blown from the cooling blower 62 is sent to the refuse support plates 3 and 3 and the support plate holding unit 4 in addition to the above-described cooling of the air cooling jacket 16, and one of them is attached from the cooling fluid introduction pipe 35. After cooling the support rod 33 through the hollow pipe 31 and the protrusion 32 having the hollow structure through the frame 34, the support rod 33 is discharged from the discharge pipe 36, and the other passes through the chevron 41 to cool the support plate holder 4. Further, the normal temperature air j sent to the storage chambers h, h is sent out from the gaps i, i to the ash layer g side to prevent the ash from entering the storage chambers h, h (see FIG. 3).
[0056]
Although the cooling casing has been described as a combination of the air-cooling jacket 16 and the water-cooling jacket 17, the combination and the type of the cooling medium are not fixed, and the cooling medium of the refuse support plates 3 and 3 and the support plate holding unit 4 is not used. Although the description has been made with the air j at normal temperature, cooling water may be used.
[0057]
In addition, although the support rod 33 is described as stacking and welding the square pipes 31 having a hollow structure, any shape may be adopted as long as the strength is increased.
[0058]
Furthermore, although the garbage support plates 3 and 3 and the incineration ash discharge plates f and f are shown as a pair each on the left and right, any number of pairs may be used, and the incineration ash discharge plates f and f exhibit their functions. It does not specify the shape if it does.
[0059]
【The invention's effect】
As described above, according to the refuse support plate and the method of controlling the refuse support in the vertical incinerator of the present invention, the refuse support plate has a structure in which a plurality of hollow tubes are arranged and cooled, so that the strength is low. With the increase, the heat resistance is also improved, so that it is possible to prevent the clinker from hindering the projection operation of the dust support plate, preventing damage or burning.
[0060]
In addition, since the support plate holding portion having the heat-resistant structure is provided, the tip of the dust support plate can be held when the dust support plate protrudes, and the strength of the dust support plate is increased particularly in the case of a large-capacity incinerator.
[0061]
Further, by the space temperature detector provided in the space between the incineration ash discharge plate and the refuse support plate, the discharge operation of the incineration ash A can be stopped in a case where the temperature in the space is excessively increased, and the burnout of the refuse support plate is reduced. Can be prevented.
[Brief description of the drawings]
FIG. 1 is a longitudinal sectional view showing a schematic configuration of a main part of a vertical incinerator according to the present invention.
FIG. 2 is a plan view showing a schematic structure of a refuse support plate in the vertical incinerator.
FIG. 3 is a longitudinal sectional view showing a schematic structure of a dust support plate and a support plate holding unit.
FIG. 4 is a longitudinal sectional view mainly for explaining a situation in a lower portion of the incinerator main body.
FIG. 5 is a longitudinal sectional view showing an outline of a conventional vertical incinerator and its incineration method.
[Explanation of symbols]
1 incinerator body 3 garbage support plate 31 square pipe (tube)
32 Projection 33 Support rod 34 Mounting frame 37 External drive mechanism 39 Space temperature detector 4 Support plate holder f Incineration ash discharge plate E Support plate body

Claims (2)

産業廃棄物や一般廃棄物を焼却する竪型焼却炉において、焼却炉下端に配設された開閉自在な焼却灰排出板の上方に若干の空間を隔てて位置し、焼却灰排出時に焼却炉内に突出して、焼却炉内に堆積するごみ及び焼却灰の荷重を支持するごみ支持板であって、In a vertical incinerator that incinerates industrial and general waste, it is located with a small space above an openable and incinerated ash discharge plate installed at the bottom of the incinerator. A garbage support plate that protrudes into the
上記ごみ支持板は、冷却用流体貫流のために中空構造とした複数の管体を配置して強度を増強したうえ、これら管体先端を中空の突出部で繋いだ構造の支持棒を取付枠上に複数列併設した支持板本体を備え、該支持板本体は冷却用流体により冷却されて、外部駆動機構により出没自在になされるとともに、The above-mentioned refuse support plate is provided with a plurality of hollow tubes for cooling fluid flow through to enhance the strength by arranging a plurality of tubes, and a supporting rod having a structure in which the ends of these tubes are connected by hollow protrusions is attached to a mounting frame. A support plate body provided in a plurality of rows is provided on the upper side, and the support plate body is cooled by a cooling fluid, and can be made to come and go by an external drive mechanism,
上記ごみ支持板の炉内への突出時に各支持棒先端の突出部を挿入保持する複数の挿入孔を有する耐熱構造の支持板保持部を、ごみ支持板に対峙する中間位置に設けたことを特徴とする竪型焼却炉におけるごみ支持板。A support plate holding portion having a heat-resistant structure having a plurality of insertion holes for inserting and holding the protruding portion of each support rod tip when the dust support plate projects into the furnace is provided at an intermediate position facing the dust support plate. A garbage support plate for vertical incinerators.
産業廃棄物や一般廃棄物を焼却する竪型焼却炉において、焼却炉下端に配設された開閉自在な焼却灰排出板の上方に若干の空間を隔てて位置し、焼却灰排出時に焼却炉内に突出して、焼却炉内に堆積するごみ及び焼却灰の荷重を支持するごみ支持板の制御方法であって、In a vertical incinerator that incinerates industrial and general waste, it is located with a small space above an openable and incinerated ash discharge plate installed at the bottom of the incinerator. A method of controlling a refuse support plate that protrudes into and supports a load of refuse and incineration ash deposited in an incinerator,
上記焼却灰排出板とごみ支持板の空間に設けられた空間温度検出器の検出値が設定値を超えた場合には、警報を発して、焼却灰排出板の開放動作を停止するとともにごみ支持板を後退させることを特徴とする竪型焼却炉におけるごみ支持板の制御方法。If the detected value of the space temperature detector provided in the space between the incineration ash discharge plate and the refuse support plate exceeds a set value, an alarm is issued and the opening operation of the incineration ash discharge plate is stopped and the refuse support A method for controlling a refuse support plate in a vertical incinerator, comprising retreating the plate.
JP2001251639A 2001-08-22 2001-08-22 Waste support plate in vertical incinerator and control method thereof Expired - Fee Related JP3600811B2 (en)

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