JP3586599B2 - Waste incinerator with boiler - Google Patents
Waste incinerator with boiler Download PDFInfo
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- JP3586599B2 JP3586599B2 JP30608099A JP30608099A JP3586599B2 JP 3586599 B2 JP3586599 B2 JP 3586599B2 JP 30608099 A JP30608099 A JP 30608099A JP 30608099 A JP30608099 A JP 30608099A JP 3586599 B2 JP3586599 B2 JP 3586599B2
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Description
【0001】
【発明の属する技術分野】
本発明はボイラ付廃棄物焼却炉に係り、特に廃棄物が投入される一次燃焼室の上方に、燃焼ガス生成物等が再燃焼される二次燃焼域を設け、少なくとも該二次燃焼域の外内壁側に耐火物を介して水管集合体が囲撓されているボイラ付廃棄物焼却炉に関する。
【0002】
【従来の技術】
従来より廃棄物焼却炉にはストーカ式焼却炉と流動層式焼却炉が主流を占めているが、いずれも廃棄物が投入される一次燃焼室の上方に、二次空気により燃焼ガス生成物等が再燃焼される二次燃焼域を設け、二次空気を効果的に吹き込むことにより完全燃焼を達成させ、ダイオキシン等の低減を図るように構成している。
一方、前記廃棄物から得られる排熱の有効利用を図るために、前記一次燃焼室及びその上方の二次燃焼域を形成する炉壁内壁側(炉壁内も含む)にボイラ水管を配設している。
図4は従来のストーカ式焼却炉にボイラ水管を配設したボイラ付廃棄物焼却炉の概略側面を示している。
図4において、11は廃棄物が入る投入ホッパーで12はその廃棄物を乾燥させながらストーカ側へ押し出す供給フィーダ、13はその乾燥した廃棄物を燃焼させるストーカで、該ストーカの上方に一次燃焼室13Aが形成される。30はそのストーカ13上の一次燃焼室13Aで廃棄物を燃焼させることにより発生する燃焼ガスである。
【0003】
14はそのストーカ13上で発生する燃焼ガス30の熱を回収するボイラであり、前記一次燃焼室13A及び二次燃焼室16、更にその上方の炉壁内壁側に、図2、図3に示すような水管集合体22(図2、図3は本発明の実施例)が囲撓されて構成されている。15は燃焼ガス30の通過断面積が縮小または、空気、排ガスの吹き込み等、燃焼ガス30の混合が促進される混合部で、一般的には二次空気供給ノズル29が配設されている。16は、混合部15より上方に位置する再燃焼域(二次燃焼域)で、燃焼ガス30を略850℃以上で2秒以上滞留することによりダイオキシン等の低減が可能である。
炉壁内壁側には二次燃焼域16の水管集合体22を高温の燃焼ガス30から保護する耐火物17が配設されており、該耐火物によりその外側に位置するで水管集合体22を燃焼ガス30から覆うように構成されている。
【0004】
【発明が解決しようとする課題】
さて、前記耐火物は一般に耐火ブロックとモルタルで形成されており、水管集合体22を高温の燃焼ガス30から保護する以外に、廃棄物が燃焼し飛灰となりその飛灰が溶融しクリンカとなって耐火物17へ付着し成長し廃棄物焼却炉の運転ができなくなるのを防ぐ必要がある。そのため、耐火物17の材質として、熱伝導率の高い、炭化珪素質の耐火物が主に使用される。
【0005】
しかしながら、かかる従来技術にあっては、次のような問題点を有している。
すなわち、近年、廃棄物焼却施設から排出されるダイオキシンが社会問題化しており、そのダイオキシンの排出を抑制するためには、二次燃焼域16で燃焼ガス30を高温で長時間滞留させることが望ましい。しかし従来、二次燃焼域16全域では、クリンカの付着を防ぐために熱伝導率の高い炭化珪素質の耐火物が使用されており、二次燃焼域16の燃焼ガス30は、冷却されやすくなり、ダイオキシンの排出を抑制するためには逆効果として働く。
【0006】
本発明はかかる技術的課題に鑑み、ボイラ水管を高温の燃焼ガスから保護しつつ、廃棄物の燃焼飛灰の溶融を阻止しクリンカとなって耐火物へ付着し成長するのを防ぎ、さらには高温で燃焼ガスの滞留時間を確保してダイオキシンの発生防止を図るボイラ付廃棄物焼却炉、特にボイラ水冷壁耐火物の構成を提供することを目的とする。
【0007】
【課題を解決するための手段】
本発明はかかる課題を解決するために、廃棄物が投入される一次燃焼室の上方に、燃焼ガス生成物等が再燃焼される二次燃焼域を設け、少なくとも該二次燃焼域に耐火物を介して水管集合体が配設されているボイラ付廃棄物焼却炉において、
前記二次燃焼域を囲撓する耐火物材料の少なくとも一部を上下に区分けし、下層耐火物を上層耐火物に対し相対的に熱伝導性の良い材料で形成することを第1の要旨としている。
【0008】
又本発明は、前記二次燃焼域のうち、上層二次燃焼域が略850℃〜950℃の温度で燃焼ガス生成物等が燃焼され、一方下層二次燃焼域の耐火物表面温度が略850℃以下の温度で燃焼ガス生成物等が燃焼されるように、前記耐火物材料と水管集合体形状を選択し、
前記水管集合体形状が、ボイラ水管と該水管同士を水平方向、あるいは垂直方向に接続して補強する平面リブとで構成され、前記耐火物材料が前記水管集合体の水管の外周面及び平面リブの表面の形状に沿うように形成されている事も要旨とする。ここで略850℃としたのはダイオキシンの低減を図る燃焼温度を考慮したものである。
【0009】
尚、前記耐火物は一般に耐火ブロックとモルタルで形成され、これらの耐火物材料の内下層耐火物材料がSiCを主成分とするか若しくは薄肉キャスタブルであり、一方、前記上層耐火物材料がAl2O3、SiO2、Zr2O3、Cr2O3、MgO、SiCのいずれかを主成分とするか若しくは厚肉キャスタブルであるのがよい。
【0010】
そして前記耐火物は耐火ブロックとモルタルで形成されるが、この場合前記耐火ブロックと前記水管集合体との間のモルタルを2種類以上の異なる熱伝導率を持ったモルタルで構成し、二次燃焼域下部と二次燃焼域上部とで下方が相対的に良熱伝導性になる様に熱伝導率の異なるモルタルを上下に張り分けても良い。
【0011】
かかる発明によれば、二次燃焼域において、二次燃焼域下部と二次燃焼域上部とで熱伝導率の異なる耐火物材料で上下に区分けし、下層耐火物を上層耐火物に対し相対的に熱伝導性の良い材料で形成した為、一次燃焼室上の二次空気混合部で発生した高温の燃焼ガスは熱伝導率の高い耐火物材料が施工されている2次燃焼部下層部ではボイラ水管により降温されるために、該下層部を通過する際は、耐火物表面温度が略850℃以下に低下しているために、廃棄物燃焼により生じた飛灰が溶融してクリンカとして炉壁に付着することなく、この付着を防止することが可能となる。
【0012】
また略850℃〜950℃以下に一旦降温された燃焼ガスは2次燃焼部下層部16a通過後、二次燃焼域上層部を通過するが、ここには熱伝導率の低い耐火物が施工されているためボイラ水管により降温されることなく燃焼ガス温度は約900℃前後を維持した状態で再燃焼がなされ、これにより燃焼ガスを高温で長時間滞留させることが可能となりダイオキシンの発生を抑制することができる。
つまり、熱伝導率の異なる耐火物をこの二次燃焼域16で上下に張り分けることにより、ボイラの水管を高温の燃焼ガス30から保護しながら、廃棄物が燃焼し飛灰となりその飛灰が溶融しクリンカとなって耐火物へ付着し成長するのを防ぎ、さらには高温で燃焼ガスの滞留時間を確保することがを可能となる。
【0013】
【発明の実施の形態】
以下、本発明を図に示した実施例を用いて詳細に説明する。但し、この実施例に記載される構成部品の寸法、形状、その相対配置などは特に特定的な記載がない限り、この発明の範囲をそれのみに限定する趣旨ではなく単なる説明例に過ぎない。
【0014】
図1は本発明の実施形態にかかる図4は従来のストーカ式焼却炉にボイラ水管を配設したボイラ付廃棄物焼却炉の概略側面を示している。
図1において、11は廃棄物が入る投入ホッパーで12はその廃棄物を乾燥させながらストーカ側へ押し出す供給フィーダ、13はその乾燥した廃棄物を燃焼させるストーカで、該ストーカの上方に一次燃焼室13Aが形成される。30はそのストーカ13上の一次燃焼室13Aで廃棄物を燃焼させることにより発生する燃焼ガスである。
【0015】
14はそのストーカ上で発生する燃焼ガス30の熱を回収するボイラであり、前記一次燃焼室13A及び二次燃焼室16、更にその上方の炉壁内壁側に、図2、図3に示す水管集合体22が囲撓されて構成されている。15は燃焼ガス30の通過断面積が縮小または、空気、排ガスの吹き込み等、燃焼ガス30の混合が促進される混合部で、一般的には二次空気供給ノズル29が配設されている。16a、16bは、混合部15より上方に位置する二次燃焼室(二次燃焼域の下部と上部)で、その炉壁内壁側には二次燃焼域16の水管集合体22を高温の燃焼ガス30から保護する耐火物17aと17bが上層部と下層部で熱伝導率を異ならせて上下に区分けして配設されており、該耐火物17a、17bによりその外側に位置する水管集合体22を燃焼ガス30から覆うように構成されている。
【0016】
そして本実施形態においては前記耐火物を耐火ブロックとモルタルで形成しているが、本実施形態では耐火ブロックの熱伝導率を異ならせている。即ち17aは、二次燃焼域下部16aに施工される耐火ブロックであり、この下層部では燃焼ガス30の温度は、かなり高く、クリンカが付着しやすいため、炭化珪素質等の比較的熱伝導率が高いものを使用してボイラ水管である水管集合体側の吸熱を多くして略850℃以下に降温を図っている。
17bは、二次燃焼域上部16bに施工される耐火ブロックであり、耐火ブロック17aと比較して熱伝導率の低い耐火物、例えばアルミナ質等を使用して、二次燃焼域下部16aを通過した燃焼ガス30の再燃焼による温度を850℃以上に高温に維持しつつ、ダイオキシンの排出を抑制する。
【0017】
図2及び図3は前記二次燃焼域下部16aと二次燃焼域上部16bに施工される耐火ブロックの構成を示し、図において20はボイラ水管、21は該水管20同士を水平方向、あるいは垂直方向に接続して補強するための平面リブで該水管20及び平面リブ21により水管集合体22を構成する。
17aは、二次燃焼域下部16aにおいて前記水管集合体21を燃焼ガス30から覆うように設けられた耐火ブロックである。また、前記水管集合体22の平面リブ21にはアーム部18が立設されている。一方、前記耐火ブロック17aには前記アーム部18に対応する凹み部19が形成されている。そして、それぞれのアーム部18と凹み部19との間及び水管集合体22と耐火ブロックとの間にはモルタル23が充填される。
図3において17bは、二次燃焼域上部16bにおいて前記水管集合体21を燃焼ガス30から覆うように設けられた耐火ブロックである。
【0018】
そして本実施形態においては、耐火ブロック17a、17bとモルタル23で形成される耐火物のうち、いずれか一方を物理的若しくは化学的に熱伝導率を異ならせれば良い。
物理的に異ならせる方法は、耐火ブロック17a、17bを形成するキャスタブルの厚みを変えることである。即ち耐火ブロックの内下層耐火ブロック17aを薄肉キャスタブル、一方、前記上層耐火ブロック17bを相対的に厚肉のキャスタブルで構成する。
又モルタル側の厚みを変えても良いが、接着性の面で考慮する必要がある。
化学的に変える方法としては耐火ブロックの内下層耐火ブロック17a材料をSiCを主成分とするキャスタブルで形成し、一方、上層耐火ブロック17b材料をAl2O3、SiO2、Zr2O3、Cr2O3、MgOのいずれかを主成分とするキャスタブルで構成すれば良い。
又耐火ブロック17側でなく、前記耐火ブロックと前記水管集合体との間のモルタルを2種類以上の異なる熱伝導率を持ったモルタル23で構成してもよい。
【0019】
かかる実施形態によれば、二次燃焼域16において、二次燃焼域下部16aと二次燃焼域上部16bとで下方が相対的に良熱伝導性になる様に熱伝導率の異なる耐火ブロック17aと耐火ブロック17b若しくはモルタルを上下に張り分ける。これによりストーカ13上の一次燃焼室で発生した高温の燃焼ガス30は熱伝導率の高い耐火物が施工されている2次燃焼域下部16aを通過する際にボイラ水管側で吸熱されて、耐火物表面温度を略850℃以下の低い温度に設定でき、飛灰の溶融を防止しクリンカの発生及び付着を防止できる。
【0020】
また2次燃焼域下部16a通過後、約850℃前後に低下した燃焼ガスは再燃焼しながら二次燃焼域上部を通過するが、ここには熱伝導率の低い耐火物が施工されているため燃焼ガス温度は前記再燃焼により昇温し約900℃前後の温度を維持する。これにより燃焼ガスを二次燃焼域上部で高温で長時間滞留させることが可能となりダイオキシンの発生を抑制することができる。
つまり、熱伝導率の異なる耐火ブロック若しくはモルタルをこの二次燃焼域16で物理的若しくは化学的に下層が良熱伝導性になる様に上下層に張り分けることにより、ボイラ水管を高温の燃焼ガス30から保護しながら、廃棄物が燃焼して生成した飛灰の溶融を阻止しこれによりクリンカとなって耐火物へ付着し成長するのを防ぐとともに、さらにはその上層部で高温で燃焼ガスの滞留時間を確保することがを可能となる。
【0021】
【発明の効果】
以上記載のごとく本発明によれば、ボイラ水管を高温の燃焼ガスから保護しつつ、廃棄物の燃焼飛灰の溶融を阻止しクリンカとなって耐火物へ付着し成長するのを防ぎ、さらには高温で燃焼ガスの滞留時間を確保してダイオキシンの発生防止を図ることが出来る。
【図面の簡単な説明】
【図1】本発明の第1実施形態に係るボイラ付廃棄物焼却炉の概要を示す側面図である。
【図2】図1のA−A線断面図で特に下層二次燃焼域を構成する耐火物と水管集合体の構成を示す断面図である。
【図3】図1のB−B線断面図で特に上層二次燃焼域を構成する耐火物と水管集合体の構成を示す断面図である。
【図4】従来技術にかかるボイラ付廃棄物焼却炉の概要を示す側面図である。
【符号の説明】
11 投入ホッパー
12 供給フィーダ
13 ストーカ
13A 一次燃焼室
14 ボイラ
15 燃焼ガス混合部
16 二次燃焼室(二次燃焼域)
17a 二次燃焼域下部16aに施工される耐火ブロック
17b 二次燃焼域上部16bに施工される耐火ブロック
22 水管集合体[0001]
TECHNICAL FIELD OF THE INVENTION
The present invention relates to a waste incinerator with a boiler, and particularly, a secondary combustion zone in which combustion gas products and the like are reburned is provided above a primary combustion chamber into which waste is charged, and at least the secondary combustion zone is provided. The present invention relates to a waste incinerator with a boiler in which a water tube assembly is surrounded by a refractory on an outer and inner wall side.
[0002]
[Prior art]
Conventionally, stoker type incinerators and fluidized bed type incinerators have been the mainstream of waste incinerators, but in both cases above the primary combustion chamber where the waste is injected, combustion gas products etc. Is provided with a secondary combustion zone in which the secondary air is reburned, complete combustion is achieved by effectively blowing secondary air, and dioxin and the like are reduced.
On the other hand, in order to effectively use the waste heat obtained from the waste, a boiler water pipe is arranged on the inner wall side of the furnace wall (including the inside of the furnace wall) forming the primary combustion chamber and a secondary combustion area above the primary combustion chamber. are doing.
FIG. 4 shows a schematic side view of a waste incinerator with a boiler in which a boiler water pipe is provided in a conventional stoker-type incinerator.
In FIG. 4,
[0003]
Reference numeral 14 denotes a boiler for recovering the heat of the combustion gas 30 generated on the
On the inner wall side of the furnace wall, a refractory 17 for protecting the water pipe assembly 22 in the secondary combustion zone 16 from the high-temperature combustion gas 30 is disposed, and the refractory is used to dispose the water pipe assembly 22 located outside thereof. It is configured to cover from the combustion gas 30.
[0004]
[Problems to be solved by the invention]
The refractory is generally formed of a refractory block and mortar. Besides protecting the water pipe assembly 22 from the high-temperature combustion gas 30, the waste burns and becomes fly ash, and the fly ash melts to become a clinker. Therefore, it is necessary to prevent the waste incinerator from operating and becoming inoperable due to adhesion to the refractory 17 and growing. Therefore, as a material of the
[0005]
However, such a conventional technique has the following problems.
That is, in recent years, dioxin emitted from waste incineration facilities has become a social problem, and in order to suppress the emission of dioxin, it is desirable that the combustion gas 30 be retained at a high temperature for a long time in the secondary combustion zone 16. . However, conventionally, in the entire region of the secondary combustion region 16, a silicon carbide refractory having a high thermal conductivity is used to prevent the adhesion of clinker, and the combustion gas 30 in the secondary combustion region 16 is easily cooled, In order to suppress the emission of dioxin, it works counterproductively.
[0006]
In view of such technical problems, the present invention protects a boiler water pipe from high-temperature combustion gas, prevents melting of waste combustion fly ash, and prevents clinker from growing on a refractory as a clinker. It is an object of the present invention to provide a boiler-equipped waste incinerator for preventing the generation of dioxin by securing a residence time of combustion gas at a high temperature, in particular, a configuration of a boiler water wall refractory.
[0007]
[Means for Solving the Problems]
For the present invention to solve such problems, above the primary combustion chamber waste is turned on, provided the secondary combustion zone of the combustion gas product or the like is re-burned, refractory to at least the secondary combustion zone In a waste incinerator with a boiler in which a water pipe assembly is arranged via a material,
The first gist is that at least a part of the refractory material surrounding the secondary combustion zone is divided into upper and lower parts, and the lower refractory is formed of a material having good thermal conductivity relative to the upper refractory. I have.
[0008]
Further, in the present invention, among the secondary combustion zones, the upper secondary combustion zone burns combustion gas products and the like at a temperature of approximately 850 ° C. to 950 ° C., while the lower refractory surface temperature of the lower secondary combustion zone is substantially reduced. The refractory material and the shape of the water tube assembly are selected so that the combustion gas product or the like is burned at a temperature of 850 ° C. or less ,
The water pipe assembly shape is composed of boiler water pipes and flat ribs connecting the water pipes in the horizontal direction or the vertical direction to reinforce the water pipes, and the refractory material is made of an outer peripheral surface and a flat rib of the water pipe of the water pipe assembly. The gist is also formed so as to conform to the shape of the surface. Here, the reason why the temperature is set to approximately 850 ° C. is in consideration of the combustion temperature for reducing dioxin.
[0009]
The refractory is generally formed of a refractory block and a mortar. Of these refractory materials, the lower refractory material is mainly composed of SiC or a thin castable material, while the upper refractory material is Al 2. It is preferable that any one of O 3 , SiO 2 , Zr 2 O 3 , Cr 2 O 3 , MgO, and SiC is used as a main component, or it is a thick castable .
[0010]
And in front Symbol refractories are formed by refractory blocks and mortar, constitute a mortar between the case before Symbol refractory block and the water tube assembly with mortar having two or more different thermal conductivities Mortars having different thermal conductivities may be vertically arranged such that the lower part of the secondary combustion zone and the upper part of the secondary combustion zone have relatively good thermal conductivity .
[0011]
According to this invention, in the secondary combustion zone, the lower refractory is divided into upper and lower refractory materials having different thermal conductivities in the lower secondary combustion zone and the upper secondary combustion zone, and the lower refractory is relative to the upper refractory. The high-temperature combustion gas generated in the secondary air mixing section on the primary combustion chamber is made of a material with high thermal conductivity, so the refractory material with high thermal conductivity is used in the lower layer of the secondary combustion section. When passing through the lower part because the temperature is lowered by the boiler water pipe, the refractory surface temperature is reduced to approximately 850 ° C. or less. This adhesion can be prevented without adhering to the wall.
[0012]
Further, the combustion gas once cooled to approximately 850 ° C. to 950 ° C. or lower passes through the lower part 16a of the secondary combustion part and then passes through the upper part of the secondary combustion area, where a refractory having a low thermal conductivity is applied. As a result, the combustion gas temperature is maintained at about 900 ° C. without being cooled by the boiler water pipe, and recombustion is performed. As a result, the combustion gas can be retained at a high temperature for a long time, thereby suppressing the generation of dioxin. be able to.
In other words, refractories having different thermal conductivities are vertically divided in the secondary combustion area 16 to protect the water pipe of the boiler from the high-temperature combustion gas 30 while burning the waste to produce fly ash. It is possible to prevent the molten gas from becoming a clinker and sticking to the refractory and growing, and furthermore, it is possible to secure the residence time of the combustion gas at a high temperature.
[0013]
BEST MODE FOR CARRYING OUT THE INVENTION
Hereinafter, the present invention will be described in detail using embodiments shown in the drawings. However, unless otherwise specified, the dimensions, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention, but are merely illustrative examples.
[0014]
FIG. 1 shows an embodiment of the present invention, and FIG. 4 shows a schematic side view of a waste incinerator with a boiler in which a boiler water pipe is arranged in a conventional stoker type incinerator.
In FIG. 1,
[0015]
Reference numeral 14 denotes a boiler for recovering the heat of the combustion gas 30 generated on the stoker. The boiler is provided on the
[0016]
In the present embodiment, the refractory is formed of a refractory block and a mortar, but in the present embodiment, the thermal conductivity of the refractory block is different. That is, reference numeral 17a denotes a refractory block constructed in the lower part 16a of the secondary combustion zone. In this lower part, the temperature of the combustion gas 30 is considerably high and clinker easily adheres. The temperature is lowered to approximately 850 ° C. or less by increasing the heat absorption on the water tube assembly side, which is the boiler water tube, by using a high-temperature material.
Reference numeral 17b denotes a refractory block constructed on the upper part 16b of the secondary combustion zone, which passes through the lower part 16a of the secondary combustion zone using a refractory having a lower thermal conductivity than the refractory block 17a, such as alumina. The emission of dioxins is suppressed while maintaining the temperature of the recombusted combustion gas 30 at a high temperature of 850 ° C. or higher.
[0017]
2 and 3 show the construction of a refractory block constructed in the lower part 16a of the secondary combustion zone and the upper part 16b of the secondary combustion zone. In the drawings, reference numeral 20 denotes a boiler water pipe, and 21 denotes a horizontal or vertical direction between the water pipes 20. A water pipe assembly 22 is formed by the water pipes 20 and the flat ribs 21 with plane ribs for connection and reinforcement in the directions.
Reference numeral 17a denotes a refractory block provided to cover the water pipe assembly 21 from the combustion gas 30 in the lower part 16a of the secondary combustion zone. An arm 18 is provided upright on the flat rib 21 of the water pipe assembly 22. On the other hand, a concave portion 19 corresponding to the arm portion 18 is formed in the refractory block 17a. The mortar 23 is filled between each of the arm portions 18 and the concave portions 19 and between the water pipe assembly 22 and the refractory block.
In FIG. 3, reference numeral 17b denotes a refractory block provided so as to cover the water pipe assembly 21 from the combustion gas 30 in the upper part 16b of the secondary combustion zone.
[0018]
In the present embodiment, one of the refractories formed of the refractory blocks 17a and 17b and the mortar 23 may be made to have different thermal conductivity physically or chemically.
A physically different method is to change the thickness of the castables forming the refractory blocks 17a and 17b. That is, the inner lower refractory block 17a of the refractory block is made of a thin castable, while the upper refractory block 17b is made of a relatively thick castable.
Although the thickness of the mortar may be changed, it is necessary to consider the adhesiveness.
As a method of chemically changing the material, the material of the inner lower refractory block 17a of the refractory block is formed by castable mainly composed of SiC, while the material of the upper refractory block 17b is Al 2 O 3 , SiO 2 , Zr 2 O 3 , Cr. 2 O 3, any of MgO may be formed in castable mainly.
Further, instead of the
[0019]
According to such an embodiment, in the secondary combustion zone 16, the refractory blocks 17a having different thermal conductivities so that the lower portion of the secondary combustion zone lower portion 16a and the upper portion of the secondary combustion zone 16b have relatively good thermal conductivity. And the refractory block 17b or mortar are vertically divided. As a result, the high-temperature combustion gas 30 generated in the primary combustion chamber on the
[0020]
After passing through the lower portion 16a of the secondary combustion zone, the combustion gas that has dropped to about 850 ° C. passes through the upper portion of the secondary combustion zone while reburning, because a refractory having a low thermal conductivity is installed here. The temperature of the combustion gas is raised by the above-mentioned re-combustion and maintained at a temperature of about 900 ° C. Thereby, the combustion gas can be retained at a high temperature for a long time in the upper part of the secondary combustion region, and the generation of dioxin can be suppressed.
In other words, the refractory blocks or mortars having different thermal conductivities are divided into upper and lower layers physically or chemically in the secondary combustion zone 16 so that the lower layer has good thermal conductivity, so that the boiler water pipe is heated with high temperature combustion gas. While protecting from the waste, the fly ash generated by the burning of the waste is prevented from melting, thereby preventing it from becoming a clinker and adhering to and growing on the refractory. It is possible to secure a residence time.
[0021]
【The invention's effect】
As described above, according to the present invention, while protecting the boiler water pipe from high-temperature combustion gas, it prevents melting of the combustion fly ash of the waste and prevents it from growing as a clinker attached to the refractory, The retention time of the combustion gas at a high temperature can be ensured to prevent the generation of dioxin.
[Brief description of the drawings]
FIG. 1 is a side view showing an outline of a waste incinerator with a boiler according to a first embodiment of the present invention.
FIG. 2 is a cross-sectional view taken along the line AA of FIG. 1 and particularly shows a configuration of a refractory and a water pipe assembly constituting a lower secondary combustion zone.
FIG. 3 is a cross-sectional view taken along the line BB of FIG. 1, particularly showing a configuration of a refractory and a water pipe assembly constituting an upper secondary combustion zone.
FIG. 4 is a side view showing an outline of a waste incinerator with a boiler according to the related art.
[Explanation of symbols]
11
17a Fireproof block 17b installed in lower part 16a of secondary combustion zone Fireproof block 22 installed in upper part 16b of secondary combustion area Water pipe assembly
Claims (5)
前記二次燃焼域を囲撓する、耐火ブロックとモルタルで形成された耐火物を上下に区分けし、下層耐火物を上層耐火物に対し相対的に熱伝導性の良い材料で形成するとともに、
前記耐火ブロックの内、下層耐火ブロックがSiCを主成分とする材料で形成され、一方、前記上層耐火ブロックがAl 2 O 3 、SiO 2 、Zr 2 O 3 、Cr 2 O 3 、MgOのいずれかを主成分とする材料で形成されていることを特徴とするボイラ付廃棄物焼却炉。A secondary combustion zone in which combustion gas products and the like are reburned is provided above the primary combustion chamber into which waste is charged, and a water pipe assembly is disposed at least in the secondary combustion zone via a refractory. Waste incinerator with boiler
Surrounding the secondary combustion zone, the refractory formed of a refractory block and mortar is divided into upper and lower, and the lower refractory is formed of a material having good thermal conductivity relative to the upper refractory ,
Of the refractory blocks, the lower refractory block is formed of a material containing SiC as a main component, while the upper refractory block is formed of any one of Al 2 O 3 , SiO 2 , Zr 2 O 3 , Cr 2 O 3 , and MgO. A waste incinerator with a boiler, characterized by being formed of a material mainly composed of:
前記二次燃焼域を囲撓する、耐火ブロックとモルタルで形成された耐火物を上下に区分けし、下層耐火物を上層耐火物に対し相対的に熱伝導性の良い材料で形成するとともに、
前記耐火ブロックの内、下層耐火ブロックが薄肉キャスタブルであり、一方、前記上層耐火ブロックが厚肉キャスタブルであることを特徴とするボイラ付廃棄物焼却炉。 A secondary combustion zone in which combustion gas products and the like are reburned is provided above the primary combustion chamber into which waste is charged, and a water pipe assembly is disposed at least in the secondary combustion zone via a refractory. Waste incinerator with boiler
Surrounding the secondary combustion zone, the refractory formed of a refractory block and mortar is divided into upper and lower, and the lower refractory is formed of a material having good thermal conductivity relative to the upper refractory,
Wherein among the refractory block, the lower refractory block is a thin castable, while the upper layer refractory block characteristics and be Rubo Ira with waste incinerators that the thick castable.
前記二次燃焼域を囲撓する、耐火ブロックとモルタルで形成された耐火物を上下に区分けし、下層耐火物を上層耐火物に対し相対的に熱伝導性の良い材料で形成するとともに、
前記耐火ブロックと水管集合体との間のモルタルを2種類以上の異なる熱伝導率を持ったモルタルで構成し、二次燃焼域下部と二次燃焼域上部とで下方が相対的に良熱伝導性になる様に熱伝導率の異なるモルタルを上下に張り分けたことを特徴とするボイラ付廃棄物焼却炉。 A secondary combustion zone in which combustion gas products and the like are reburned is provided above the primary combustion chamber into which waste is charged, and a water pipe assembly is disposed at least in the secondary combustion zone via a refractory. Waste incinerator with boiler
Surrounding the secondary combustion zone, the refractory formed of a refractory block and mortar is divided into upper and lower, and the lower refractory is formed of a material having good thermal conductivity relative to the upper refractory,
The mortar between the refractory block and the water pipe assembly is composed of mortar having two or more kinds of different thermal conductivity, and the lower part of the secondary combustion zone and the lower part of the secondary combustion area have relatively good heat conduction. features and be Rubo Ira with waste incinerators that the different thermal conductivity mortar so as to become a sex were divided tension up and down.
前記水管集合体形状が、ボイラ水管と該水管同士を水平方向、あるいは垂直方向に接続して補強する平面リブとで構成され、前記耐火物材料が前記水管集合体の水管の外周面及び平面リブの表面の形状に沿うように形成されていることを特徴とする請求項1、2若しくは3記載のボイラ付廃棄物焼却炉。 Among the secondary combustion zones, the upper secondary combustion zone burns combustion gas products and the like at a temperature of approximately 850 ° C. to 950 ° C., while the lower refractory surface temperature of the lower secondary combustion zone is approximately 850 ° C. or lower. In such a way that the combustion gas products and the like are burned, the refractory material and the water pipe assembly shape are selected,
The water pipe assembly shape is composed of boiler water pipes and flat ribs connecting the water pipes in the horizontal direction or the vertical direction to reinforce the water pipes, and the refractory material is made of an outer peripheral surface and a flat rib of the water pipe of the water pipe assembly. The waste incinerator with a boiler according to claim 1 , wherein the waste incinerator is formed so as to conform to the surface shape of the boiler.
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JP30608099A JP3586599B2 (en) | 1999-10-27 | 1999-10-27 | Waste incinerator with boiler |
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JP2007057113A (en) * | 2005-08-22 | 2007-03-08 | Plantec Inc | Vertical refuse incinerator provided with water tube wall |
CH699405B1 (en) * | 2008-08-26 | 2021-06-15 | Mokesys Ag | Refractory wall, especially for an incinerator. |
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