JPH03279705A - Incinerator of combustion temperature controlling type - Google Patents
Incinerator of combustion temperature controlling typeInfo
- Publication number
- JPH03279705A JPH03279705A JP7710990A JP7710990A JPH03279705A JP H03279705 A JPH03279705 A JP H03279705A JP 7710990 A JP7710990 A JP 7710990A JP 7710990 A JP7710990 A JP 7710990A JP H03279705 A JPH03279705 A JP H03279705A
- Authority
- JP
- Japan
- Prior art keywords
- incinerator
- refractory
- air
- steam
- furnace
- 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.)
- Granted
Links
- 238000002485 combustion reaction Methods 0.000 title claims abstract description 21
- 239000011810 insulating material Substances 0.000 claims abstract description 5
- 239000000463 material Substances 0.000 claims description 12
- 230000009970 fire resistant effect Effects 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 12
- 239000002699 waste material Substances 0.000 abstract description 6
- 239000010815 organic waste Substances 0.000 abstract description 5
- 239000011449 brick Substances 0.000 abstract description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 3
- 229910052799 carbon Inorganic materials 0.000 abstract description 3
- 229920003023 plastic Polymers 0.000 abstract description 3
- 239000004033 plastic Substances 0.000 abstract description 3
- 230000000694 effects Effects 0.000 description 4
- 239000000123 paper Substances 0.000 description 3
- 239000013502 plastic waste Substances 0.000 description 3
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 238000007873 sieving Methods 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000009834 vaporization Methods 0.000 description 1
- 230000008016 vaporization Effects 0.000 description 1
Landscapes
- Incineration Of Waste (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
【発明の詳細な説明】
〔産業上の利用分野]
本発明は、焼却炉に関し、更に詳しくは紙、有機廃棄物
、プラスチック廃棄物を炉の焼却温度を制御しながら完
全に燃焼させて公害を防止するのに適した焼却温度制御
型焼却炉に関する。[Detailed Description of the Invention] [Field of Industrial Application] The present invention relates to an incinerator, and more specifically, to completely burn paper, organic waste, and plastic waste while controlling the incineration temperature of the incinerator to reduce pollution. The present invention relates to an incineration temperature controlled incinerator suitable for preventing the incineration.
焼却炉は古くから各種被燃物、例えば紙、有機廃棄物、
プラスチックの固型廃棄物を燃焼処理する装置として広
く利用されている。しかしながら、これらの各種廃棄物
を完全燃焼させて無公害化させるという観点からすれば
、まだかかることを満足し得る焼却炉は開発されていな
いのが現状である。Incinerators have long been used to store various combustible materials, such as paper, organic waste,
It is widely used as a device for burning solid plastic waste. However, from the viewpoint of completely burning these various wastes to make them non-polluting, at present no incinerator has been developed that can satisfy this requirement.
従って、本発明は前記した従来の焼却炉の問題点を解決
して、紙、有機廃棄物、プラスチ・ツク廃棄物を効率よ
く完全に燃焼させるのに適した焼却温度制御型焼却炉を
提供することを目的とする。Therefore, the present invention solves the problems of the conventional incinerator described above and provides a temperature-controlled incinerator suitable for efficiently and completely burning paper, organic waste, and plastic waste. The purpose is to
本発明に従えば、耐火断熱性材料製の底壁部及び側壁部
並びに被燃焼処理物投入口、空気導入口及び燃焼排気口
を備えた上部から構成される焼却炉において、炉内下方
部に耐火性礫層を設け、該耐火性礫層の内部または下方
に、下向きに複数個の開口を孔設した空気及び水蒸気供
給管を配設したことを特徴とする燃焼温度制御型焼却炉
が提供される。According to the present invention, in an incinerator comprising a bottom wall portion and a side wall portion made of a fire-resistant and heat-insulating material, and an upper portion provided with a material to be burned inlet, an air inlet, and a combustion exhaust port, a lower part of the incinerator is provided. Provided is a combustion temperature controlled incinerator, characterized in that a refractory gravel layer is provided, and air and steam supply pipes with a plurality of downward openings are provided inside or below the refractory gravel layer. be done.
以下、添付図面を参照し乍ら本発明の好ましい実施例を
説明するが、本発明の技術的範囲を以下の実施例に限定
するものでないことはいうまでもない。Preferred embodiments of the present invention will be described below with reference to the accompanying drawings, but it goes without saying that the technical scope of the present invention is not limited to the following embodiments.
第1図において、焼却炉1は耐火断熱性材料製の底壁部
2及び灰取出し口を備えた側壁部3並びに被燃焼処理物
投入口5、空気導入口6及び燃焼排気口(煙突)7を備
えた上部4から構成される。In FIG. 1, an incinerator 1 includes a bottom wall part 2 made of a fire-resistant and heat-insulating material, a side wall part 3 having an ash outlet, an inlet for materials to be burned 5, an air inlet 6, and a combustion exhaust outlet (chimney) 7. It consists of an upper part 4 with a
焼却炉底壁部2及び側壁部3は焼却炉内での燃焼に耐え
る材料であれば任意の材料とすることができるが、通常
は耐火レンガを耐火断熱性材料とすることができる。な
お、これらの炉壁材料として鋼材壁(例えば内側S U
S、外側SS)を空洞に構成し、内部に耐熱保温材料
を封入して使用することもできる。The incinerator bottom wall part 2 and side wall part 3 can be made of any material as long as it can withstand combustion in the incinerator, but usually firebrick can be used as a fireproof and heat-insulating material. Note that these furnace wall materials include steel walls (for example, inner SU
It is also possible to construct the outer part (S, outer SS) into a cavity, and to use it by sealing a heat-resistant and heat-retaining material inside.
焼却炉の上部4には各種廃棄物投入口5が設けられてお
り、この投入口5には蓋8を設け、廃棄物をパノ千方式
で投入するよう設備されている。The upper part 4 of the incinerator is provided with an inlet 5 for various kinds of waste, and the inlet 5 is provided with a lid 8 and is equipped to input waste in a pano-thousand manner.
なお、蓋8の構造には特に限定はないが、スプリング式
で焼却炉Iの上部4に取付けて安全弁としての機能を持
たせるのが好ましい。焼却炉の上部4には1個又は複数
個の空気導入口6(例えばオリフィス状又は適当な制御
弁を取イ」けて流M調節できるようにする)が設TJら
れており、被燃物の燃焼を行なわ−ける。Although there is no particular limitation on the structure of the lid 8, it is preferable that the lid 8 be attached to the upper part 4 of the incinerator I with a spring type so as to function as a safety valve. The upper part 4 of the incinerator is provided with one or more air inlets 6 (for example, an orifice-like or suitable control valve so that the flow M can be adjusted). combustion.
焼却炉1の側壁部には、灰取出し口のほか、着火時及び
自燃しにくい場合の補助として、バーナが設けられてい
る。In addition to an ash outlet, the side wall of the incinerator 1 is provided with a burner to assist in ignition and in cases where self-combustion is difficult.
焼却炉1の下方部には面]火性礫層9(例えばレンガ、
ガレキ、その他の耐火材料粉砕物)が設けられており、
例えば径50〜70+nm程度の礫を、第1図に示すよ
うに、炉底部に直接又は適当な支承物を介して充填する
。この耐火性礫層9は従来の炉のロスドルの機能を果た
すが、通常例えば鋼製の一般的なロスドルに比較してメ
ンテナンスが容易で、また保熱効果を有する(即ち、連
続してハツチ方式で焼却する際に1ハツチから次の回に
切り替える際、礫層に熱が保持され、次回の焼却開始機
能が容易になる)。In the lower part of the incinerator 1, there is a surface] fire gravel layer 9 (for example, brick,
rubble and other crushed refractory materials).
For example, gravel with a diameter of about 50 to 70+ nm is filled into the bottom of the furnace directly or via a suitable support, as shown in FIG. This refractory gravel layer 9 performs the function of a conventional furnace rosdol, but it is usually easier to maintain than a general rosdol made of steel, for example, and has a heat retention effect (i.e., it is continuously When switching from one hatch to the next during incineration, the gravel layer retains heat, making it easier to start the next incineration).
本発明に従えば、耐火性礫層9の内部(第1図参照)又
は耐火性礫層の下(図示せず)に、空気及び水蒸気供給
管10を、両端の支持耐火レンガにより水平に保持され
るように配設して、空気及び水蒸気を炉内へ供給する。According to the present invention, the air and steam supply pipe 10 is held horizontally within the refractory gravel layer 9 (see FIG. 1) or under the refractory gravel layer (not shown) by supporting refractory bricks at both ends. The furnace is arranged so that air and steam are supplied into the furnace.
このため管10には複数個の開口を下向き配置になるよ
う設けて空気及び水蒸気が炉内に均一に供給されるよう
にされている。空気及び水蒸気の供給は、それぞれ、配
管11及び12からコン1−ロール弁13及び14を通
して炉内温度を所定値に保つよう行なわれる。炉内温度
制御は温度センサー15で炉内温度を検知し、コントロ
ーラー16で実施する。所望の炉内温度は被燃物の種類
などによって変動するが、一般的には1200°Cぐら
いを最高温度よしている。本発明では500〜1000
°Cにコントロールする。For this purpose, the tube 10 is provided with a plurality of openings oriented downward so that air and steam are uniformly supplied into the furnace. Air and steam are supplied from pipes 11 and 12 through control valves 13 and 14, respectively, to maintain the temperature inside the furnace at a predetermined value. The temperature inside the furnace is controlled by a temperature sensor 15 that detects the temperature inside the furnace, and a controller 16 that detects the temperature inside the furnace. The desired temperature inside the furnace varies depending on the type of material to be burned, but generally the maximum temperature is about 1200°C. In the present invention, 500 to 1000
Control at °C.
空気及び水蒸気供給管10の開口の全開口面積は設計仕
様条件によって適宜変更することができるが、一般的に
は管10の断面積の50〜90%、好ましくは70〜8
0%とするのが適当である。また空気及び水蒸気の供給
比には特に限定はなく、炉内温度が所定値になるようコ
ントロール弁13及び14テ適宜コントロールされる。Although the total opening area of the air and steam supply pipe 10 can be changed as appropriate depending on the design specification conditions, it is generally 50 to 90% of the cross-sectional area of the pipe 10, preferably 70 to 8%.
It is appropriate to set it to 0%. Further, there is no particular limitation on the supply ratio of air and steam, and the control valves 13 and 14 are appropriately controlled so that the temperature inside the furnace becomes a predetermined value.
空気及び水蒸気供給管10に供給される水蒸気は外部よ
り供給することもできるが、第1図に示すように炉1の
上部に内部に水を充填した藩気発生器17を設け、焼却
によって発生する燃焼熱によって水蒸気を生成せしめて
炉底部に供給することができる。従って、本発明に従え
ば、水蒸気を外部から供給する必要はなく、系内で自給
することができるという利点がある。The steam supplied to the air and steam supply pipe 10 can be supplied from the outside, but as shown in FIG. The combustion heat produced can generate steam and supply it to the bottom of the furnace. Therefore, according to the present invention, there is no need to supply water vapor from the outside, and there is an advantage that the system can be self-supplied within the system.
本発明の焼却炉1で燃焼された排気は例えばステンレス
製の適当な金網18で同伴固型物などをふるい落として
排気口(煙突)7から大気中へ排出される。なお、金網
18の下流の第二燃焼ゾーン19には更に空気及び水蒸
気が供給できるように設備されており、必要に応じ更に
燃焼させて排気を無害化することができる。The exhaust gas combusted in the incinerator 1 of the present invention is discharged into the atmosphere from an exhaust port (chimney) 7 after sieving out entrained solid matter with a suitable wire mesh 18 made of stainless steel, for example. Note that the second combustion zone 19 downstream of the wire mesh 18 is equipped so that air and steam can be further supplied, and the exhaust gas can be rendered harmless by further combustion if necessary.
本発明に従って、各種焼却物に対し、完全無煙燃焼を行
なわせるには、被焼却物ごとに必要な空気量、温度を調
整することが必要である。特にプラスチックの場合、あ
まり温度を上げ過ぎても溶融化が進行し、ガス化せず完
全燃焼が妨げられる。According to the present invention, in order to cause complete smokeless combustion of various types of incineration materials, it is necessary to adjust the amount of air and temperature required for each type of incineration material. Particularly in the case of plastic, if the temperature is raised too high, it will continue to melt and will not turn into gas, preventing complete combustion.
従来の焼却炉では、−Mにここまで取り入れたものはな
く、せいぜい被焼却物投入量の増減とか空気量の調整を
行なっているくらいであり、これでは燃焼温度の調整が
出来ないし、作業性も悪い。In conventional incinerators, -M has not been incorporated to this extent, and at most the amount of material to be incinerated is increased or decreased, or the amount of air is adjusted.This makes it impossible to adjust the combustion temperature and reduces work efficiency. Too bad.
これに対し、本発明は、供給空気の中に水蒸気を注入又
は供給空気とは別に水蒸気を供給することによって、燃
焼温度をコントロールする方法である。すなわち温゛度
が上がり過ぎた時(一般には1000°C以上)には、
水蒸気の供給量を増し温度が下がり過ぎたら水蒸気量を
凍らす。これによって温度を効率よくコントロールする
ことが可能となる。In contrast, the present invention is a method of controlling combustion temperature by injecting steam into the supply air or supplying steam separately from the supply air. In other words, when the temperature rises too much (generally over 1000°C),
Increase the amount of water vapor supplied and freeze the amount of water vapor if the temperature drops too much. This makes it possible to control the temperature efficiently.
水蒸気の代わりに水を用いるものもあるが、この場合水
の蒸発潜熱が大きいので燃焼温度のコンI・ロールが難
しく好ましくない。Some use water instead of steam, but in this case, the latent heat of vaporization of water is large, making it difficult to control the combustion temperature, which is not preferred.
ここで、水蒸気の供給は当該焼却炉からの自家発生のも
のを用いてもよいし、他から導入しても差し支えない。Here, the steam may be supplied by self-generated steam from the incinerator, or may be introduced from another source.
また、供給水茎気量及び空気量のコントロール方法とし
ては手動でもよいが、自動制御機構を取入れることで更
に作業性の向」二が図れる。Further, although the amount of water stem air and air supplied may be controlled manually, work efficiency can be further improved by incorporating an automatic control mechanism.
なお、水蒸気を用いる効用としては、このほか、100
0°C以」二で燃焼させてもよい場合、炭素と反応して
水性ガスを生成し、これが燃焼に寄与するという副次効
果もある。In addition, there are 100 other benefits of using water vapor.
When it is allowed to burn at temperatures below 0°C, it also has the side effect of reacting with carbon to produce water gas, which contributes to combustion.
本発明に従えば、上で説明したように、紙、有機廃棄物
及びプラスチックの焼却を水茎気による温度制御効果に
よって燃焼温度をコントロールすることができ、また炉
内で1000°C以上になった場合には条件によっては
水蒸気と炭素が反応して水性ガスが発生し、燃焼性を高
めるごともあるので、前記各種被燃焼物を完全燃焼して
無公害化することができる。According to the present invention, as explained above, the combustion temperature of paper, organic waste, and plastics can be controlled by the temperature control effect of water stalks, and the temperature in the furnace can exceed 1000°C. In some cases, depending on the conditions, water vapor and carbon may react to generate water gas, which may increase combustibility, so that the various substances to be combusted can be completely combusted and become non-polluting.
第1図は本発明に係る焼却炉の好ましい態様を示す図面
である。図中の主要符号は以下の通りである。
■・・・焼却炉、 2・・・底壁部、 3・・・側
壁部4・・・上部、訃・・排気物投入ロ
ア・・排気口(煙突)、 9・・・耐火性礫層10・
・・空気及び水蒸気供給管
17・・・水藤発器FIG. 1 is a drawing showing a preferred embodiment of the incinerator according to the present invention. The main symbols in the figure are as follows. ■...Incinerator, 2...Bottom wall part, 3...Side wall part 4...Top part, carcass...Exhaust material input lower...Exhaust port (chimney), 9...Refractory gravel layer 10・
... Air and steam supply pipe 17 ... Suito generator
Claims (1)
処理物投入口、空気導入口及び燃焼排気口を備えた上部
から構成される焼却炉において、炉内下方部に耐火性礫
層を設け、該耐火性礫層の内部又は下方に、下向きに複
数個の開口を孔設した空気及び水蒸気供給管を配設した
ことを特徴とする燃焼温度制御型焼却炉。1. In an incinerator consisting of a bottom wall and side walls made of fire-resistant and heat-insulating material, and an upper part equipped with an inlet for materials to be burned, an air inlet, and a combustion exhaust outlet, a layer of refractory gravel is installed in the lower part of the furnace. A combustion temperature controlled incinerator characterized in that an air and steam supply pipe having a plurality of downward openings is disposed inside or below the refractory gravel layer.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7710990A JPH0680367B2 (en) | 1990-03-28 | 1990-03-28 | Combustion temperature control type incinerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7710990A JPH0680367B2 (en) | 1990-03-28 | 1990-03-28 | Combustion temperature control type incinerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH03279705A true JPH03279705A (en) | 1991-12-10 |
JPH0680367B2 JPH0680367B2 (en) | 1994-10-12 |
Family
ID=13624618
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7710990A Expired - Lifetime JPH0680367B2 (en) | 1990-03-28 | 1990-03-28 | Combustion temperature control type incinerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0680367B2 (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07198118A (en) * | 1993-11-01 | 1995-08-01 | Shizuo Kobayashi | Incineration furnace |
US5664504A (en) * | 1994-10-27 | 1997-09-09 | Kobayashi; Shizuo | Combustion apparatus having inverse temperature distribution by forced convection |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2002048319A (en) * | 2000-08-04 | 2002-02-15 | Hiroisa Koizumi | Water vapor/combustion gas combustion furnace system |
-
1990
- 1990-03-28 JP JP7710990A patent/JPH0680367B2/en not_active Expired - Lifetime
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH07198118A (en) * | 1993-11-01 | 1995-08-01 | Shizuo Kobayashi | Incineration furnace |
US5664504A (en) * | 1994-10-27 | 1997-09-09 | Kobayashi; Shizuo | Combustion apparatus having inverse temperature distribution by forced convection |
Also Published As
Publication number | Publication date |
---|---|
JPH0680367B2 (en) | 1994-10-12 |
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