JP2003207121A - Oxygen enriched mixture blow-in type waste incinerator with settled fire grate - Google Patents
Oxygen enriched mixture blow-in type waste incinerator with settled fire grateInfo
- Publication number
- JP2003207121A JP2003207121A JP2002040782A JP2002040782A JP2003207121A JP 2003207121 A JP2003207121 A JP 2003207121A JP 2002040782 A JP2002040782 A JP 2002040782A JP 2002040782 A JP2002040782 A JP 2002040782A JP 2003207121 A JP2003207121 A JP 2003207121A
- Authority
- JP
- Japan
- Prior art keywords
- grate
- waste
- oxygen
- combustion furnace
- mixture
- 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.)
- Pending
Links
- 239000002699 waste material Substances 0.000 title claims abstract description 46
- 239000000203 mixture Substances 0.000 title claims abstract description 39
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 21
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 20
- 239000001301 oxygen Substances 0.000 title claims abstract description 20
- 238000002485 combustion reaction Methods 0.000 claims abstract description 59
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims abstract description 15
- 238000007664 blowing Methods 0.000 claims abstract description 5
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 claims abstract 4
- 239000007789 gas Substances 0.000 claims description 20
- 239000000446 fuel Substances 0.000 claims description 15
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 8
- 230000000903 blocking effect Effects 0.000 claims description 8
- NJPPVKZQTLUDBO-UHFFFAOYSA-N novaluron Chemical compound C1=C(Cl)C(OC(F)(F)C(OC(F)(F)F)F)=CC=C1NC(=O)NC(=O)C1=C(F)C=CC=C1F NJPPVKZQTLUDBO-UHFFFAOYSA-N 0.000 claims description 8
- 229910002091 carbon monoxide Inorganic materials 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 238000005260 corrosion Methods 0.000 claims description 5
- 230000007797 corrosion Effects 0.000 claims description 5
- 239000000428 dust Substances 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 238000000354 decomposition reaction Methods 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 3
- 239000011449 brick Substances 0.000 claims description 2
- 230000003028 elevating effect Effects 0.000 claims description 2
- 238000011084 recovery Methods 0.000 claims description 2
- 239000000919 ceramic Substances 0.000 claims 1
- 229910001220 stainless steel Inorganic materials 0.000 claims 1
- 239000010935 stainless steel Substances 0.000 claims 1
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 238000010304 firing Methods 0.000 abstract 1
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 5
- 229910000831 Steel Inorganic materials 0.000 description 4
- 239000010959 steel Substances 0.000 description 4
- 238000012790 confirmation Methods 0.000 description 2
- 102220008421 rs193922681 Human genes 0.000 description 2
- 239000004071 soot Substances 0.000 description 2
- 101001062854 Rattus norvegicus Fatty acid-binding protein 5 Proteins 0.000 description 1
- 101001094026 Synechocystis sp. (strain PCC 6803 / Kazusa) Phasin PhaP Proteins 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/34—Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery
Landscapes
- Incineration Of Waste (AREA)
- Chimneys And Flues (AREA)
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Air Supply (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】純酸素吹込み型排気物の焼却
炉に関する。TECHNICAL FIELD The present invention relates to a pure oxygen blown type exhaust gas incinerator.
【0002】[0002]
【従来の技術】従来の廃棄物焼却炉においては、予め純
酸素と外気を任意の混合比に混合して、間接的に炉内に
吹き込むものはなく、純酸素を鋼管等によって炉内に直
接吹き込んでいるため、吹込み管すなわちランスパイプ
の腐食による消耗や、バックファイヤなどがおこる可能
性があり、また、投入する廃棄物は空気との接触面を多
くするため、予め細かく粉砕する場合がしばしば見受け
られ、さらに、炉内底部の廃棄物は空気に接する機会が
少なく、不完全燃焼のまま残留することが多かった。2. Description of the Related Art In a conventional waste incinerator, there is no one in which pure oxygen and outside air are mixed in advance at an arbitrary mixing ratio and blown indirectly into the furnace. Pure oxygen is directly fed into the furnace by a steel pipe or the like. Since it is blown in, there is a possibility that it will be consumed due to corrosion of the blow-in pipe, that is, the lance pipe, and backfire, etc.In addition, since the waste to be input has many contact surfaces with air, it may be pulverized beforehand in advance. Often found, the waste at the bottom of the furnace has little chance of coming into contact with air and often remains as incomplete combustion.
【0003】[0003]
【発明が解決しようとする課題】不完全燃焼残留物を皆
無とし、かつ、ダイオキシンの発生を抑制可能な廃棄物
焼却炉を構築する。A waste incinerator capable of eliminating incomplete combustion residues and suppressing generation of dioxins is constructed.
【0004】[0004]
【課題を解決するための手段】助燃材として純酸素を使
用し、予め純酸素を外気と混合した、酸素富化混合気を
吹き込むことにより炉内雰囲気温度を高温にして、さら
に、高温に熱せられた複数のブレードを有する沈下式火
格子を自重によって廃棄物上に沈下させ、熱せられたブ
レードが廃棄物中を進行することにより、炉内底部に残
留する廃棄物をも完全燃焼させる。[Means for Solving the Problems] Pure oxygen is used as an auxiliary combustion material, and the oxygen-enriched air-fuel mixture in which pure oxygen is mixed with the outside air in advance is blown to raise the temperature of the atmosphere inside the furnace to a high temperature, and then heat it to a high temperature. A subsidence grate having a plurality of blades set down is settled on the waste by its own weight, and the heated blade advances in the waste, thereby completely burning the waste remaining in the bottom of the furnace.
【0005】[0005]
【発明の実施の形態】発明の実施の形態を図にもとづい
て説明する。請求項1を実現するために鋼板等からな
る、一次燃焼炉外殻(アウターシェル)18と耐火煉瓦
等の耐高温、耐腐食性の材料によって製造された一次燃
焼炉内壁19(インナーシェル)によって構成される一
次燃焼炉9の下部ピット35内に波型底板20を、レベ
ル調整脚37と蝶番27によって連結された台座26、
当該台座26を焼却完了まで、燃焼炉底部に保持し、燃
焼完了後に台座26を降下させる昇降装置28、台座2
6下降時に波型底板20を、蝶番27を中心とする傾斜
角θと平行に傾斜させるためのストッパー36を設け
る。BEST MODE FOR CARRYING OUT THE INVENTION Embodiments of the present invention will be described with reference to the drawings. In order to achieve claim 1, a primary combustion furnace outer shell (outer shell) 18 made of a steel plate and a primary combustion furnace inner wall 19 (inner shell) made of a high temperature and corrosion resistant material such as refractory bricks are used. A pedestal 26 in which the corrugated bottom plate 20 is connected to the lower pit 35 of the constructed primary combustion furnace 9 by a level adjusting leg 37 and a hinge 27,
An elevating device 28 for holding the pedestal 26 at the bottom of the combustion furnace until completion of incineration, and lowering the pedestal 26 after completion of combustion, the pedestal 2
6. A stopper 36 is provided for inclining the corrugated bottom plate 20 parallel to the inclination angle θ about the hinge 27 when descending.
【0006】一次燃焼炉内壁19の上部には一次燃焼炉
排気筒22及び炉内燃焼を均一にし、排気の整流をおこ
なう目的で排煙整流コーン35を設ける。On the upper part of the inner wall 19 of the primary combustion furnace, a flue gas rectifying cone 35 is provided for the purpose of uniformizing the primary combustion furnace exhaust pipe 22 and the combustion in the furnace and rectifying the exhaust gas.
【0007】一次燃焼炉内壁19の正面壁には廃棄物投
入扉兼滑落ガイド板33及び耐熱ガラスを嵌め込んだ燃
焼確認窓23を設け、炉内下部には混合気供給ダクト3
4を前後又は左右の任意の位置に設置する。The front wall of the primary combustion furnace inner wall 19 is provided with a waste input door / slide guide plate 33 and a combustion confirmation window 23 in which heat resistant glass is fitted, and the mixture supply duct 3 is provided in the lower part of the furnace.
Install 4 at any position on the front or back or left and right.
【0008】さらに、複数の火格子ブレード21を取り
付けた火格子枠兼混合気遮断枠32を、一次燃焼炉内壁
19に設けた火格子フック昇降用スリット25を貫通し
て、当該枠の四隅に取り付けた火格子フック30に火格
子昇降用巻揚げ鋼索24を緊縛、当該鋼索24を外部の
巻揚げ装置等により、火格子枠兼混合気遮断枠32を上
方へ巻揚げ、又は懸架のまま保持、又は任意の高さまで
降下させ、以後は火格子枠兼混合気遮断枠32の自重に
よって沈下することが可能なものとする。Furthermore, a grate frame / mixture blocking frame 32, to which a plurality of grate blades 21 are attached, penetrates the grate hook lifting slits 25 provided on the inner wall 19 of the primary combustion furnace, and is provided at four corners of the frame. The grate lifting hoisting steel rope 24 is tightly bound to the attached grate hook 30 and the steel rope 24 is hoisted upward by an external hoisting device or the like, or is held as it is suspended. Or, it can be lowered to an arbitrary height, and thereafter, it can be submerged by its own weight of the grate frame / air mixture blocking frame 32.
【0009】上記一次燃焼炉9に廃棄物8を粉砕するこ
となく、原型のまま投入すると炉内底部に保持されてい
る波型底板20の凹凸にとって廃棄物8は適度に分散
し、火格子枠兼混合気遮断枠32を適度に分散した廃棄
物8上に降下させた後、火格子枠兼混合気遮断枠32の
自重による自由沈下が可能となるよう外部に設置した巻
揚げ機を解放する。When the waste 8 is put into the primary combustion furnace 9 without being crushed and is left as it is, the waste 8 is appropriately dispersed due to the unevenness of the corrugated bottom plate 20 held at the bottom of the furnace, and the grate frame is provided. After lowering the combined gas / air mixture blocking frame 32 on the appropriately dispersed waste 8, the hoisting machine installed outside is released so that the grate frame / mixed gas blocking frame 32 can be freely submerged by its own weight. .
【0010】廃棄物8を投入後、加圧送風機(a)5の
電動機40を始動させ、空気取入れ口1から外気を吸引
すると、途中に設けられたベンチュリー管38内の狭窄
部の気圧が減少して、狭窄部に設けられた純酸素送出管
39から流量調整弁4によって、流量を制御された純酸
素タンク3内の純酸素が同様に吸引され、外気と混合
し、酸素富化混合気を生成する。After the waste 8 is charged, the electric motor 40 of the pressure blower (a) 5 is started to suck the outside air from the air intake port 1, and the air pressure in the narrowed portion in the venturi pipe 38 provided on the way is reduced. Then, the pure oxygen in the pure oxygen tank 3 whose flow rate is controlled is similarly sucked from the pure oxygen delivery pipe 39 provided in the narrowed portion by the flow rate adjusting valve 4 and mixed with the outside air to form the oxygen-enriched mixture. To generate.
【0011】前記によって生成された酸素富化混合気を
混合気供給ダクト34及び波型底板20の凹部を通じて
一次燃焼炉内壁19内の底部に供給し、炉内雰囲気を酸
素富化状態にして、石油バーナーあるいは着火剤等によ
って廃棄物に着火する。The oxygen-enriched air-fuel mixture generated as described above is supplied to the bottom of the inner wall 19 of the primary combustion furnace through the air-fuel mixture supply duct 34 and the concave portion of the corrugated bottom plate 20, so that the atmosphere in the furnace is enriched with oxygen. Ignite the waste with a petroleum burner or an igniter.
【0012】前記によって燃焼を開始すると、廃棄物は
焼却灰となって減容し、それとともに廃棄物上に置かれ
た火格子枠兼混合気遮断枠32は沈下するとともに、当
該枠を構成する高温に加熱された複数の火格子ブレード
21が、下方の未燃焼廃棄物の中に進入して、燃焼限界
すなわち波形底板20の凹部基底に滞留した廃棄物が焼
却灰に至るまで進行して、廃棄物を完全燃焼することが
出来る。When the combustion is started as described above, the waste becomes incinerated ash and is reduced in volume, and at the same time, the grate frame / mixture blocking frame 32 placed on the waste sinks and constitutes the frame. A plurality of grate blades 21 heated to a high temperature enter the lower unburned waste, and the waste that has stayed at the combustion limit, that is, the recess base of the corrugated bottom plate 20, progresses to incineration ash, Can completely burn waste.
【0013】請求項2を実現するために、図7及び図8
のごとき断面を有する、複数の火格子ブレード21から
構成される火格子枠兼混合気遮断枠32が沈下すると、
混合気供給ダクト34の出口を次第に塞ぎはじめ、火格
子ブレード21が燃焼限界すなわち波型底板20の基底
部又はその上に堆積した焼却灰まで沈下、到達すると当
該ダクト34の混合気排出口を完全に塞ぎ、当該ダクト
34内の混合気圧力が上昇する。In order to implement claim 2, FIG. 7 and FIG.
When the grate frame / mixture blocking frame 32 composed of a plurality of grate blades 21 having a cross section such as
The outlet of the air-fuel mixture supply duct 34 is gradually closed, and the grate blade 21 sinks to the combustion limit, that is, the bottom of the corrugated bottom plate 20 or the incineration ash accumulated on it, and when it reaches the exhaust gas outlet of the duct 34 is completely completed. The air-fuel mixture pressure in the duct 34 rises.
【0014】混合気供給ダクト34内に設置された圧力
センサー6は、前記によって混合気圧力の変化情報を加
圧送風機(a)5と連動している電動機40を制御する
制御装置7に送り、当該制御装置は、予め設定された変
域内において、電動機40の回転を減速又は停止するこ
とにより、炉内に吹き込む混合気の量を自動的に調整又
は遮断する。The pressure sensor 6 installed in the air-fuel mixture supply duct 34 sends the change information of the air-fuel mixture pressure to the control device 7 for controlling the electric motor 40 linked with the pressure blower (a) 5 as described above. The control device automatically adjusts or cuts off the amount of the air-fuel mixture blown into the furnace by decelerating or stopping the rotation of the electric motor 40 within a preset variable range.
【0015】請求項3を実現するために、一次燃焼炉9
から排出された排気を、一次燃焼炉排気筒22を経由し
て二次燃焼炉10に導入し、当該二次燃焼炉内における
排気流の任意の位置に耐高温、耐腐蝕素材による楔型
(又は三角形)の支柱を図11及び図12のごとく設置
して楔型乱流発生板41とする。In order to achieve claim 3, the primary combustion furnace 9
The exhaust gas discharged from the exhaust gas is introduced into the secondary combustion furnace 10 through the primary combustion furnace exhaust pipe 22, and the wedge shape (corresponding to the high temperature and corrosion resistant material is formed at an arbitrary position of the exhaust flow in the secondary combustion furnace). (Or triangular) columns are installed as shown in FIGS. 11 and 12 to form a wedge-type turbulent flow generation plate 41.
【0016】前記楔型乱流発生板41の直前に、混合気
供給ダクト34によって酸素富化混合気を再び吹込み、
楔型乱流発生板41を冷却すると同時に、当該楔形乱流
発生板41の後方に発生する乱流によって、まだ一酸化
炭素(CO)を充分に含んでいる一次燃焼炉9から排出
された排気と酸素富化混合気を混合して一酸化炭素(C
O)を除去する。Immediately before the wedge-shaped turbulence generating plate 41, the oxygen-enriched mixture is blown again by the mixture supply duct 34,
At the same time as cooling the wedge-shaped turbulence generating plate 41, the exhaust gas discharged from the primary combustion furnace 9 that still contains sufficient carbon monoxide (CO) due to the turbulent flow generated behind the wedge-shaped turbulent generating plate 41. Carbon monoxide (C
O) is removed.
【0017】請求項4を実現するために、予め二次燃焼
炉10からの排気中の煤塵を、一般的に知られているサ
イクロン12によって除去する。In order to realize the fourth aspect, the soot dust in the exhaust gas from the secondary combustion furnace 10 is removed in advance by a generally known cyclone 12.
【0018】前記によって煤塵が除去された二次燃焼炉
10からの排気を排気導入筒42によって図13に示す
がごとき減温炉13に導入する。Exhaust gas from the secondary combustion furnace 10 from which the soot and dust have been removed by the above is introduced into the temperature reducing furnace 13 as shown in FIG.
【0019】図13の減温炉13において排気筒17の
下端レベルy1、排気導入筒42の中心線y2、外気供
給管の中心線y3の高さ関係はy1<y2<y3にあ
り、高温な排気は上昇し、低温な外気は下降することに
より、効率よく対流が発生して、減温した二次燃焼炉1
0からの排気を排気筒17によって、大気に直接排出、
又は市販されている、又は開発中のダイオキシン分解装
置15に送出することが可能となる。The lower level y 1 of the exhaust tube 17 in the temperature reducing furnace 13 in FIG. 13, the center line y 2 exhaust introduction pipe 42, the height relationship between the center line y 3 of the outside air supply pipe is y 1 <y 2 <y 3 , the high temperature exhaust rises and the low temperature outside air falls, so that convection is efficiently generated and the temperature of the secondary combustion furnace 1 is lowered.
The exhaust from 0 is directly discharged to the atmosphere by the exhaust stack 17,
Alternatively, it can be delivered to a dioxin decomposing device 15 which is commercially available or under development.
【0020】前記のいずれの排出法においても、バグフ
ィルター16を通して最終排出筒17より排出すること
が必要であり、サイクロン12の下部及び減温炉13下
部の粉塵収集筒43からの排出においても同様にバグフ
ィルターを必要とする。In any of the above-mentioned discharge methods, it is necessary to discharge from the final discharge cylinder 17 through the bag filter 16, and the same applies to the discharge from the dust collecting cylinder 43 below the cyclone 12 and the temperature lowering furnace 13. Need a bug filter on.
【0021】請求項5を実現するために、廃棄物の焼却
が完了し、焼却炉底部すなわち波型底板20の基底部に
堆積した焼却灰を、一次燃焼炉下部のピット35内に設
置された焼却灰回収容器29に回収するために、昇降装
置28の上部位置保持状態を解除して、昇降装置28が
連結されている台座26、及びその上に蝶番27で連結
され、レベル調整脚37で水平を保持している波型底板
20を予め設定した高さまで下降させる。In order to achieve claim 5, the incineration ash deposited on the bottom of the incinerator, that is, the base of the corrugated bottom plate 20 after the incineration of the waste is completed is placed in the pit 35 below the primary combustion furnace. In order to collect in the incineration ash recovery container 29, the upper position holding state of the lifting device 28 is released, and the pedestal 26 to which the lifting device 28 is connected, and the hinge 27 on the pedestal 26 are connected thereto, and the level adjusting legs 37 The corrugated bottom plate 20 holding the horizontal position is lowered to a preset height.
【0022】前記において、予め設定される高さとは、
ピット35内に設置されたストッパー36に波型底板2
0の底面があたり、蝶番27の中心とストッパー36と
波型底板20の底面の接点が作り出す、焼却灰を回収す
るのに最も適した角度θをつくり出す高さである。In the above description, the preset height is
The corrugated bottom plate 2 is attached to the stopper 36 installed in the pit 35.
The bottom surface of 0 corresponds to the height at which the most suitable angle θ for collecting incinerated ash is created by the contact points between the center of the hinge 27, the stopper 36 and the bottom surface of the corrugated bottom plate 20.
【0023】請求項6を実現するために、図9の如く波
型底板20の基底部上面に、凸部又は凹部と平行な二次
元断面に緩やかな円弧上の水分だまりを設ける。In order to achieve the sixth aspect, as shown in FIG. 9, on the upper surface of the base portion of the corrugated bottom plate 20, a water pool in a gentle arc is provided in a two-dimensional cross section parallel to the convex portion or the concave portion.
【0024】[0024]
【発明の効果】本発明は、以上説明したように構成され
ているので、以下に記載されるような効果を奏する。Since the present invention is constructed as described above, it has the following effects.
【0025】予め混合装置によって外気と純酸素を混合
して、酸素富化混合気として焼却炉内に吹き込むことに
より、炉内雰囲気が均一となり燃焼の偏りを避けること
が出来る。By mixing the outside air and pure oxygen with a mixing device in advance and blowing them into the incinerator as an oxygen-enriched mixture, the atmosphere in the furnace becomes uniform and uneven combustion can be avoided.
【0026】酸素富化混合気を吹き込むことにより高温
燃焼が可能となり、ダイオキシンの分解抑制に必要な国
の基準(>800℃)を満たす、燃焼温度が確保可能で
あり、水分を多量に含む廃棄物の完全燃焼も可能とな
る。By blowing in an oxygen-enriched mixture, high-temperature combustion becomes possible, and a combustion temperature that can meet the national standards (> 800 ° C) necessary for suppressing the decomposition of dioxin can be secured, and waste containing a large amount of water. It is also possible to completely burn things.
【0027】純酸素を間接的に吹き込むことにより、バ
ックファイヤの危険性を回避出来る。By injecting pure oxygen indirectly, the risk of backfire can be avoided.
【0028】高温に加熱された火格子ブレードを廃棄物
の中に、燃焼とともに進行させ、焼却炉底部の廃棄物に
至るまで完全燃焼させることが出来る。The grate blade heated to a high temperature can be advanced into the waste along with the combustion, and can be completely burned to the waste at the bottom of the incinerator.
【0029】焼却炉底面を波型として、投入された廃棄
物を粉砕することなく分散して、凹部を混合気吹込みダ
クトの延長として利用する。The bottom of the incinerator has a corrugated shape, and the input waste is dispersed without crushing and the recess is used as an extension of the air-fuel mixture blowing duct.
【0030】減温炉を用いることによりダイオキシン抑
制に関する排気ガス温度(<400℃)を達成すること
が可能であるうえ、市販又は開発されているダイオキシ
ン分解装置への接続が可能である。By using a decompression furnace, it is possible to achieve an exhaust gas temperature (<400 ° C.) for suppressing dioxin, and it is possible to connect to a commercially available or developed dioxin decomposition apparatus.
【図1】本焼却炉の全体構成図である。FIG. 1 is an overall configuration diagram of a main incinerator.
【図2】一次燃焼炉の正面図である。FIG. 2 is a front view of a primary combustion furnace.
【図3】一次燃焼炉中の火格子上面図である。FIG. 3 is a top view of a grate in the primary combustion furnace.
【図4】一次燃焼炉の廃棄物投入扉を開いた状態の右側
面図である。FIG. 4 is a right side view of the primary combustion furnace with a waste input door opened.
【図5】一次燃焼炉の右側面図である。FIG. 5 is a right side view of the primary combustion furnace.
【図6】焼却灰回収時に底面の波型底板をθ度傾斜させ
た時の右側面図である。FIG. 6 is a right side view when the corrugated bottom plate on the bottom surface is inclined by θ degrees when recovering incineration ash.
【図7】火格子ブレード及び波型底板の正面断面図であ
る。FIG. 7 is a front sectional view of a grate blade and a corrugated bottom plate.
【図8】火格子ブレード及び波型底板の側面断面図であ
る。FIG. 8 is a side sectional view of a grate blade and a corrugated bottom plate.
【図9】波型底板基底の側面断面図である。FIG. 9 is a side sectional view of a corrugated bottom plate base.
【図10】ベンチュリー管からなる混合装置及び加圧送
風機の断面図である。FIG. 10 is a cross-sectional view of a mixing device including a Venturi tube and a pressure blower.
【図11】二次燃焼炉の上部断面図である。FIG. 11 is an upper sectional view of a secondary combustion furnace.
【図12】二次燃焼炉の側面断面図である。FIG. 12 is a side sectional view of a secondary combustion furnace.
【図13】減温炉の断面図である。FIG. 13 is a cross-sectional view of a temperature reducing furnace.
1 外気取入れ口 2 空気混合装置 3 純酸素タンク 4 流量調整弁 5 加圧送風機(a) 6 圧力センサー 7 制御装置 8 廃棄物 9 一次燃焼炉 10 二次燃焼炉 11 焼却灰 12 サイクロン 13 減温炉 14 加圧送風機(b) 15 ダイオキシン分解装置 16 バグフィルター 17 排気筒 18 一次燃焼炉外殻(アウターシェル) 19 一次燃焼炉内壁(インナーシェル9 20 波型底板 21 火格子ブレード 22 一次燃焼炉排気筒 23 燃焼確認窓 24 火格子昇降用巻揚げ鋼索 25 火格子フック昇降用スリット 26 台座 27 蝶番 28 昇降装置 29 焼却灰回収容器 30 火格子枠フック 31 鋼索貫通穴 32 火格子枠兼混合気遮断枠 33 廃棄物投入扉兼滑落ガイド板 34 混合気供給ダクト 35 排気整流コーン 36 ストッパー 37 レベル調整脚 38 ベンチュリー管 39 純酸素送出管 40 電動機 41 楔形乱流発生板 42 排気導入筒 43 外気供給管 44 粉塵収集筒 y1 排気筒下端レベル y2 排気導入筒中心線 y3 外気供給管中心線1 Outside Air Intake Port 2 Air Mixing Device 3 Pure Oxygen Tank 4 Flow Rate Control Valve 5 Pressurized Blower (a) 6 Pressure Sensor 7 Control Device 8 Waste 9 Primary Combustion Furnace 10 Secondary Combustion Furnace 11 Incinerator Ash 12 Cyclone 13 Decompressor 14 Pressurized Blower (b) 15 Dioxin Decomposing Device 16 Bag Filter 17 Exhaust Cylinder 18 Primary Combustion Furnace Outer Shell (Outer Shell) 19 Primary Combustion Furnace Inner Wall (Inner Shell 9 20 Corrugated Bottom Plate 21 Grate Blade 22 Primary Combustion Furnace Exhaust Cylinder 23 Combustion Confirmation Window 24 Grate Lifting Steel Cable 25 Grate Hook Lifting Slit 26 Pedestal 27 Hinge 28 Lifting Device 29 Incinerated Ash Collection Container 30 Grate Frame Hook 31 Steel Cable Penetration Hole 32 Grate Frame and Mixture Block 33 Waste input door and sliding guide plate 34 Mixture supply duct 35 Exhaust flow rectifying cone 36 Stopper 37 Level adjusting leg 38 Ben Jury tube 39 pure oxygen delivery tube 40 motor 41 wedge turbulence generating plate 42 exhaust introduction pipe 43 outside air supply pipe 44 the dust collecting vessel y 1 chimney lower level y 2 exhaust introduction pipe centerline y 3 outside air supply pipe center line
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23J 15/06 F23L 7/00 A 3K078 F23L 7/00 F27D 17/00 104D 4K056 F27D 17/00 104 104G F23G 5/00 110 // F23G 5/00 110 F23J 15/00 K Fターム(参考) 3K023 JA02 3K061 GA06 JA12 JA15 3K062 AA16 AB01 BA01 CB03 DA11 DB05 3K065 AA16 AB01 GA03 GA13 GA23 GA33 3K070 DA05 DA29 DA47 3K078 BA03 BA22 CA02 CA11 CA25 4K056 AA19 BA07 BB01 CA20 DB03 DB04 DB05 DB13 FA03 FA08─────────────────────────────────────────────────── ─── Continuation of front page (51) Int.Cl. 7 Identification code FI theme code (reference) F23J 15/06 F23L 7/00 A 3K078 F23L 7/00 F27D 17/00 104D 4K056 F27D 17/00 104 104G F23G 5/00 110 // F23G 5/00 110 F23J 15/00 K F Term (reference) 3K023 JA02 3K061 GA06 JA12 JA15 3K062 AA16 AB01 BA01 CB03 DA11 DB05 3K065 AA16 AB01 GA03 GA13 GA23 GA33 3K070 DA05 DA29 DA47 3K078 BA03 CA25 4K056 AA19 BA07 BB01 CA20 DB03 DB04 DB05 DB13 FA03 FA08
Claims (6)
よって製造された一次燃焼炉9の底面に昇降装置28に
よって底面と同一レベルに保持されている波型底板20
の上に廃棄物投入口21より廃棄物8を原型のまま投入
し、同時に電動機40によって作動する加圧送風機
(a)5によって吸引された外気と、流量調整弁4を経
由して純酸素タンク3に貯蔵されている酸素(O2)を
空気混合装置2によって、予め設定された混合比によっ
て混合して酸素富化混合気を生成し、当該混合気を混合
気供給ダクト34及び一次燃焼炉内壁19内の下部に保
持されている波型底板20の凹部を通じて当該一次燃焼
炉9に吹き込みをおこなって廃棄物8に着火し、他方、
一次燃焼炉内壁19内の上部に懸架されていた、ステン
レス鋼又はセラミックス等の耐高温、耐腐蝕性の素材に
よって製造された、複数の火格子ブレード21から構成
される火格子枠兼混合気遮断枠32の上部位置保持状態
を解除し、自重によって、投入された廃棄物8上に沈下
せしめ、酸素富化混合気が充満する炉内雰囲気での燃焼
によって高温に熱せられた火格子ブレード21が、廃棄
物8の燃焼とともに、下部の未燃焼廃棄物8の中に沈
下、進行して当該未燃焼廃棄物8に着火して燃焼を促進
することが可能な沈下式火格子を有する酸素富化混合気
吹込型廃棄物焼却炉。1. A corrugated bottom plate 20 which is held at the same level as the bottom surface by an elevating device 28 on the bottom surface of a primary combustion furnace 9 made of a material having high temperature resistance and corrosion resistance such as refractory bricks.
The waste 8 is put in the original form through the waste input port 21 as it is, and at the same time, the pure oxygen tank is passed through the outside air sucked by the pressure blower (a) 5 operated by the electric motor 40 and the flow rate adjusting valve 4. The oxygen (O2) stored in 3 is mixed by the air mixing device 2 at a preset mixing ratio to generate an oxygen-enriched mixture, and the mixture is supplied to the mixture supply duct 34 and the inner wall of the primary combustion furnace. The primary combustion furnace 9 is blown into the primary combustion furnace 9 through the concave portion of the corrugated bottom plate 20 held in the lower part of 19 to ignite the waste material 8, while
Suspended above the inner wall 19 of the primary combustion furnace, made of a material having high temperature and corrosion resistance, such as stainless steel or ceramics, which is composed of a plurality of grate blades 21 and serves as a grate frame and mixture cutoff. The upper position holding state of the frame 32 is released, and the grate blade 21 which is heated to a high temperature by being burned in the furnace atmosphere filled with the oxygen-enriched air-fuel mixture is caused to sink by the dead weight on the injected waste 8. , As the waste 8 burns, sinks into the lower unburned waste 8 and progresses to ignite the unburned waste 8 to promote combustion and promote oxygen enrichment. Air-blown waste incinerator.
とにより、複数の火格子ブレード21から構成される火
格子枠兼混合気遮断枠32が沈下し、火格子ブレード2
1が波型底板20の凹部基底にほぼ到達することによ
り、火格子ブレード21の周囲の枠すなわち火格子枠兼
混合気遮断枠32が混合気供給ダクト34の混合気排出
口を塞ぐことで、混合気供給ダクト34内の圧力が上昇
し、混合気供給ダクト34内に設置された圧力センサー
6によって検知された圧力変化情報が加圧送風機(a)
5の制御装置7に送られ、加圧送風機の電動機40の減
速又は停止をおこなうことが可能な沈下式火格子を有す
る酸素富化混合気吹込型廃棄物焼却炉。2. The grate blade 2 according to claim 1, when the waste material 8 burns, a grate frame / mixture blocking frame 32 composed of a plurality of grate blades 21 sinks, and the grate blade 2
1 almost reaches the base of the concave portion of the corrugated bottom plate 20, so that the frame around the grate blade 21, that is, the grate frame / mixture blocking frame 32 closes the mixture discharge port of the mixture supply duct 34, The pressure in the air-fuel mixture supply duct 34 rises, and the pressure change information detected by the pressure sensor 6 installed in the air-fuel mixture supply duct 34 is the pressure blower (a).
5. An oxygen-enriched mixture-blown waste incinerator having a subsidence grate capable of decelerating or stopping the electric motor 40 of the pressure blower, which is sent to the controller 7 of FIG.
酸化炭素(CO)を完全除去する目的で、内部に楔形乱
流発生板41を設け、当該楔形乱流発生板41の直前
に、混合気供給ダクト34を経由して酸素富化混合気を
吹込み、当該楔形乱流発生板41を冷却すると同時に、
当該楔形乱流発生板41の後方に発生する乱流によっ
て、一次燃焼炉9から排出された排気と酸素富化混合気
を効率よく混合して一酸化炭素(CO)を除去すること
が可能な、二次燃焼炉10を設置した沈下式火格子を有
する酸素富化混合気吹込型廃棄物焼却炉。3. A wedge-shaped turbulent flow generation plate 41 is provided inside the exhaust gas discharged from the primary combustion furnace 9 in front of the wedge-shaped turbulent flow generation plate 41 for the purpose of completely removing carbon monoxide (CO). At the same time as blowing the oxygen-enriched air-fuel mixture through the air-fuel mixture supply duct 34 to cool the wedge-shaped turbulent flow generation plate 41,
Due to the turbulent flow generated behind the wedge-shaped turbulent flow generation plate 41, it is possible to efficiently mix the exhaust gas discharged from the primary combustion furnace 9 and the oxygen-enriched air-fuel mixture to remove carbon monoxide (CO). , An oxygen-enriched mixture-blown waste incinerator having a subsidence grate provided with a secondary combustion furnace 10.
キシンを低減して排気を大気中に直接放出、又はダイオ
キシンを除去することを目的とするダイオキシン分解装
置15に排気を送出するために、サイクロン12によっ
て粉塵を除去した二次燃焼炉10から排出された排気
を、排気導入筒42を経由して導入し、加圧送風機
(b)13によって外気を吹き込んで外気と混合するこ
とにより、排気温度を急速に減ずることが可能な減温炉
を設置した沈下式火格子を有する酸素富化混合気吹込型
廃棄物焼却炉。4. In order to rapidly reduce the exhaust gas temperature, reduce the dioxin in the exhaust gas and release the exhaust gas directly into the atmosphere, or to send the exhaust gas to a dioxin decomposition device 15 for removing dioxin, Exhaust gas discharged from the secondary combustion furnace 10 from which dust has been removed by the cyclone 12 is introduced through the exhaust gas introduction tube 42, and external air is blown in by the pressure blower (b) 13 to mix with the external air, thereby producing the exhaust gas. An oxygen-enriched mixture-blown waste incinerator with a subsidence grate equipped with a decommissioning furnace capable of rapidly reducing the temperature.
置した昇降装置28によって、廃棄物8の焼却完了後、
燃焼炉底部すなわち波型底板20を台座26ごと下降せ
しめ、予め蝶番27を中心とする傾斜角θが得られるよ
う、ピット35の内壁にストッパーを設置して、波型底
板20内に残留している焼却灰を焼却灰回収容器29に
落下せしむることが可能な沈下式火格子を有する酸素富
化混合気吹込型廃棄物焼却炉。5. After the incineration of the waste 8 is completed by the lifting device 28 installed in the pit 35 at the bottom of the primary combustion furnace 9,
The bottom of the combustion furnace, that is, the corrugated bottom plate 20 is lowered together with the pedestal 26, and a stopper is installed on the inner wall of the pit 35 so that the inclination angle θ around the hinge 27 can be obtained in advance, and the corrugated bottom plate 20 remains in the corrugated bottom plate 20. An oxygen-enriched mixture-blown waste incinerator having a sinking grate capable of dropping the existing incineration ash into the incineration ash recovery container 29.
の基底部表面に緩やかな凹部を設けて水分だまりとした
沈下式火格子を有する酸素富化混合気吹込型廃棄物焼却
炉。6. A corrugated bottom plate 20 included in the primary combustion furnace 9.
Oxygen-enriched mixture-blown waste incinerator with a subsidence grate that has a gentle recess on the bottom surface of the tank and has pooled water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002040782A JP2003207121A (en) | 2002-01-15 | 2002-01-15 | Oxygen enriched mixture blow-in type waste incinerator with settled fire grate |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2002040782A JP2003207121A (en) | 2002-01-15 | 2002-01-15 | Oxygen enriched mixture blow-in type waste incinerator with settled fire grate |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JP2003207121A true JP2003207121A (en) | 2003-07-25 |
Family
ID=27655162
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2002040782A Pending JP2003207121A (en) | 2002-01-15 | 2002-01-15 | Oxygen enriched mixture blow-in type waste incinerator with settled fire grate |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2003207121A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112524621A (en) * | 2020-12-10 | 2021-03-19 | 西安西热控制技术有限公司 | Automatic slag tapping control system and method for combustion furnace of thermal power plant |
| CN115325545A (en) * | 2022-09-13 | 2022-11-11 | 合肥工业大学 | An energy-saving and environmentally friendly graded combustion organic waste incinerator |
-
2002
- 2002-01-15 JP JP2002040782A patent/JP2003207121A/en active Pending
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112524621A (en) * | 2020-12-10 | 2021-03-19 | 西安西热控制技术有限公司 | Automatic slag tapping control system and method for combustion furnace of thermal power plant |
| CN112524621B (en) * | 2020-12-10 | 2022-09-16 | 西安西热控制技术有限公司 | A kind of automatic slag control system and method for combustion furnace of thermal power plant |
| CN115325545A (en) * | 2022-09-13 | 2022-11-11 | 合肥工业大学 | An energy-saving and environmentally friendly graded combustion organic waste incinerator |
| CN115325545B (en) * | 2022-09-13 | 2024-05-28 | 合肥工业大学 | Energy-saving environment-friendly staged combustion organic waste incinerator |
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