JP3762450B2 - Control method of air blowing rate of upper tuyere of waste melting furnace - Google Patents

Control method of air blowing rate of upper tuyere of waste melting furnace Download PDF

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Publication number
JP3762450B2
JP3762450B2 JP08981395A JP8981395A JP3762450B2 JP 3762450 B2 JP3762450 B2 JP 3762450B2 JP 08981395 A JP08981395 A JP 08981395A JP 8981395 A JP8981395 A JP 8981395A JP 3762450 B2 JP3762450 B2 JP 3762450B2
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Prior art keywords
tuyere
air
furnace
melting furnace
blown
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Expired - Fee Related
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JP08981395A
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JPH08285248A (en
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吉浩 石田
也寸彦 加藤
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Nippon Steel Corp
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Nippon Steel Corp
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    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/12Heat utilisation in combustion or incineration of waste
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E20/00Combustion technologies with mitigation potential
    • Y02E20/34Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery

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  • Incineration Of Waste (AREA)
  • Gasification And Melting Of Waste (AREA)

Description

【0001】
【産業上の利用分野】
本願発明は、一般廃棄物あるいは産業廃棄物等を処理するシャフト炉方式の廃棄物溶融炉の操業方法に関し、特に、廃棄物溶融炉の上段羽口空気吹き込み量の制御方法に関する。
【0002】
【従来の技術】
シャフト炉方式の廃棄物溶融炉による廃棄物処理は、炉に装入された一般廃棄物あるいは産業廃棄物等を乾燥、熱分解、燃焼、溶融の過程を経て、廃棄物をスラグとして取り出すものである。
【0003】
例えば、特公昭60ー11766号公報には、図3に示すように、廃棄物溶融炉1は、円形断面のシャフト型の炉体をしており、炉内に装入された廃棄物を乾燥、熱分解、燃焼及び溶融させるために、燃料であるコークスを燃焼させる。前記コークス燃焼のために、炉体の下部には複数段の羽口が設けられ、これら羽口のうち、炉床部近くに配置された下段羽口2は酸素を富化した空気を吹き込み、また、下段羽口の上に配置された上段羽口3は空気を吹き込むようになっている。
【0004】
前記廃棄物溶融炉の操業では、装入物中の可燃分の熱分解により発生した可燃性の残渣は、上段羽口から吹き込まれた空気により燃焼されるが、可燃性残渣燃焼速度が可燃性残渣発生速度より小さいために未燃焼の可燃性残渣が炉内に堆積する。その可燃性残渣のうち、微細な可燃性残渣は、羽口から送られてきた酸素によって炉内で燃焼されることなく、気流にのって炉頂より可燃性ダストとして飛散する。
【0005】
【発明が解決しようとする課題】
ところが、可燃性残渣の部分的な燃焼で発生した燃焼ガスにより可燃性残渣層の上部にある装入物が乾燥、熱分解されて体積縮小するためにその上の装入物が降下し、さらに、可燃性残渣の燃焼、飛散によって体積が縮小し装入物は降下するが、装入物の通気抵抗が炉断面で不均一なため、上記の燃焼ガスの流れが不均一になり易く熱分解残渣層の堆積厚さが部分的に異なり、その結果、装入物の荷下がりも不均一となり易い。
【0006】
装入物の荷下がりが不均一になると、空洞化による荷下がり不良や吹き抜けが生じ、安定した炉操業が非常に困難となる。
【0007】
また、不安定な炉操業により、飛散する可燃性ダストの割合が大きくなると、炉内で利用可能な炭素、水素等の可燃物の割合が減少することになるため、廃棄物と共に装入されるコークス等の副原料の割合を増加させる必要があった。
【0008】
さらに、飛散した可燃性ダストは、後段の2次燃焼室で完全燃焼されるが、飛散量が変動すると、未燃COを発生させたりクリンカが生成されることから、好ましくない。
【0009】
そこで、本願発明は、シャフト炉方式の廃棄物溶融炉内における装入物の荷下がりを均一にして、炉操業を安定化させる溶融炉の上段羽口空気吹き込み量の制御方法を提供するものである。
【0010】
【課題を解決するための手段】
本発明の廃棄物溶融炉の上段羽口からの空気吹き込み量制御方法は、炉体の下部に複数段の羽口を設け、該羽口のうち下段羽口からは酸素を富化した空気を吹き込み、上段羽口からは空気を吹き込む、シャフト炉方式の廃棄物溶融炉の平面方向に複数本設置された上段羽口の空気吹き込み量の制御方法において、前記上段羽口の各羽口に吹き込む空気を遮断する遮断弁と空気量を調整する流量調整弁を連結し、該遮断弁をあらかじめ設定したスケジュールにしたがって一定時間ごとに周期的に開閉して前記各羽口ごとに空気の吹き込み及びその停止を周期的に行い、各上段羽口からの空気吹き込み量を調整することを特徴とする。
【0011】
【作用】
本願発明により、高さ方向及び平面方向に設置された複数本の上段羽口の空気吹き込み量を各羽口毎に増減を行なって炉内ガス流れを積極的に撹拌するので、装入物の荷下がりが均一になる。また、装入物は通常、断面方向で均一でないため、ガスは装入物の最も流れ易い場所に向かう偏った流れとなるが、前記空気の増減は、減じた時に装入物の浮力を抑え、荷下りを促進するため、そのガス流れの偏りを抑制する作用もある。
【0012】
【実施例】
本願発明の実施例を図面を用いて説明する。
【0013】
本願発明が適用されるシャフト炉方式の溶融炉1は、炉床部1aの周囲に下段羽口2を有し、下段羽口2の上部に上段羽口3が朝顔部1bの周囲に配置されている。本実施例では、上段羽口3は、ヘッダ管5から分岐されて、上側羽口3a及び下側羽口3bが2段、平面方向に4本設けられている。上側羽口3aの設置レベルは、装入物の乾燥完了レベルに近いほど効果がある。上段羽口3の上側羽口3a及び下側羽口3bには空気が供給され、下段羽口2には酸素を富化した空気が供給され、溶融炉1に吹き込まれる。各羽口により炉内へ吹き込まれる空気あるいは酸素富化空気の量は、遮断弁6をあらかじめ設定されたタイムスケジュールにしたがって開閉する。
【0014】
本実施例では、上側羽口3a及び下側羽口3bの空気吹き込み量を変化させるものであるが、図3に示されたタイムチャートにより空気吹き込みの切り換えについて説明する。
【0015】
送風が開始されると、No.1羽口(上側及び下側の羽口。以下同じ。)では空気を吹き込まず、残りのNo.2〜No.4羽口から同量の空気を吹き込む。10分経過後、No.2羽口のみ空気吹き込みを停止すると同時にNo.1羽口の空気吹き込みを開始する。10分経過したら、No.3羽口のみ空気吹き込みを停止すると同時にNo.2羽口の空気吹き込みを再び開始する。10分経過後、No.4羽口のみ空気吹き込みを停止すると同時にNo.3羽口の空気吹き込みを再び開始する。更に10分経過後、No.1羽口のみ空気吹き込みを停止すると同時にNo.4羽口の空気吹き込みを再び開始する。以上の動作を周期的に行なう。なお、No.1〜No.4羽口の吹き込み及びその停止にかかわらず、上段羽口の単位時間当たりの総風量は、炉内反応に必要な空気量から、図3に示すとおり一定である。
【0016】
空気吹き込み量と時間の具体的な値は、例えば、処理量20t/日で、羽口段数2段、羽口数4本/段の溶融炉の場合、総風量500Nm3/hで空気を吹き込む各羽口を順次10分間吹き込み停止させるパターンを繰り返した結果、吹き抜け、荷下り不良は発生しなかった。
【0017】
【発明の効果】
本願発明の効果は次のとおりである。
【0018】
(1)上段羽口からの空気量を周期的に変化させることで、炉内の熱分解残渣層厚をコントロールし、通気圧損を低くし安定化させるため、装入物の浮力を減じ、吹き抜け、荷下り不良等の非定常的な現象を抑制する効果がある。
【0019】
(2)(1)の結果、発電によるエネルギー回収を行う場合、発電量を安定化する効果がある。
【図面の簡単な説明】
【図1】本願発明の実施例で使用される廃棄物溶融炉の概略図。
【図2】本願発明の実施例で使用される廃棄物溶融炉の上段羽口部分の横断面概略図。
【図3】本願発明の実施例のタイムチャート。
【図4】従来の廃棄物溶融炉の概略図。
【符号の説明】
1 シャフト炉方式の溶融炉、 2 下段羽口、 3 上段羽口、 3a 上側羽口、 3b 下側羽口、 4 流量調整弁、 5 ヘッダ管、 6、遮断弁
[0001]
[Industrial application fields]
The present invention relates to a method for operating a shaft furnace type waste melting furnace for treating general waste or industrial waste, and more particularly to a method for controlling the upper tuyere air blowing rate of a waste melting furnace.
[0002]
[Prior art]
Waste treatment using a shaft furnace type waste melting furnace takes out the waste as slag through the process of drying, pyrolysis, combustion and melting of general waste or industrial waste charged in the furnace. is there.
[0003]
For example, in Japanese Examined Patent Publication No. 60-11766, as shown in FIG. 3, the waste melting furnace 1 has a shaft-type furnace body having a circular cross section, and the waste charged in the furnace is dried. The coke as a fuel is burned for pyrolysis, combustion and melting. For the coke combustion, a plurality of tuyere are provided in the lower part of the furnace body, and among these tuyere, the lower tuyere 2 disposed near the hearth part blows air enriched with oxygen, The upper tuyere 3 disposed on the lower tuyere is designed to blow air.
[0004]
In the operation of the waste melting furnace, the flammable residue generated by the thermal decomposition of the combustible material in the charge is burned by the air blown from the upper tuyere, but the flammable residue burning rate is combustible. Since it is smaller than the residue generation rate, unburned combustible residue accumulates in the furnace. Among the flammable residues, fine flammable residues are scattered as flammable dust from the top of the furnace without being burned in the furnace by oxygen sent from the tuyere.
[0005]
[Problems to be solved by the invention]
However, the charge above the combustible residue layer is dried and pyrolyzed by the combustion gas generated by the partial combustion of the combustible residue, and the volume of the charge is reduced due to the volume reduction. The volume of the combustible residue is reduced due to combustion and scattering of the combustible residue, and the charge falls. However, since the flow resistance of the charge is non-uniform in the cross section of the furnace, the combustion gas flow tends to be non-uniform and pyrolysis The deposit thickness of the residue layer is partially different, and as a result, the load unloading tends to be uneven.
[0006]
If the load of the charged material becomes uneven, unloading failure or blow-through due to cavitation occurs, and stable furnace operation becomes very difficult.
[0007]
Also, if the proportion of combustible dust that scatters increases due to unstable furnace operation, the proportion of combustible materials such as carbon and hydrogen that can be used in the furnace will decrease, so it will be charged with waste. It was necessary to increase the proportion of the auxiliary materials such as coke.
[0008]
Further, the scattered combustible dust is completely combusted in the secondary combustion chamber at the subsequent stage. However, if the amount of scattering fluctuates, unburned CO is generated and clinker is generated, which is not preferable.
[0009]
Accordingly, the present invention provides a method for controlling the upper tuyere air blowing amount of the melting furnace that stabilizes the furnace operation by uniforming the unloading of the charge in the shaft furnace type waste melting furnace. is there.
[0010]
[Means for Solving the Problems]
The method for controlling the amount of air blown from the upper tuyere of the waste melting furnace according to the present invention is provided with a plurality of tuyere at the lower part of the furnace body, and oxygen enriched air is supplied from the lower tuyere of the tuyere. In the method for controlling the amount of air blown in the upper tuyere installed in the plane direction of the shaft furnace type waste melting furnace, the air is blown into each tuyere of the upper tuyere. A shut-off valve that shuts off air and a flow rate adjusting valve that regulates the amount of air are connected, and the shut-off valve is periodically opened and closed at regular intervals according to a preset schedule to blow air into each tuyere and Stopping is performed periodically and the amount of air blown from each upper tuyere is adjusted.
[0011]
[Action]
According to the present invention, the amount of air blown into a plurality of upper tuyere installed in the height direction and the plane direction is increased or decreased for each tuyere and the gas flow in the furnace is actively stirred. Unloading becomes uniform. In addition, since the charge is usually not uniform in the cross-sectional direction, the gas flows in a biased direction toward the place where the charge flows most easily, but the increase or decrease in the air suppresses the buoyancy of the charge when it is reduced. In order to promote unloading, there is also an effect of suppressing the deviation of the gas flow.
[0012]
【Example】
Embodiments of the present invention will be described with reference to the drawings.
[0013]
A shaft furnace type melting furnace 1 to which the present invention is applied has a lower tuyere 2 around the hearth part 1a, and an upper tuyere 3 is arranged around the morning glory part 1b above the lower tuyere 2. ing. In the present embodiment, the upper tuyere 3 is branched from the header pipe 5, and the upper tuyere 3a and the lower tuyere 3b are provided in two stages and four in the plane direction. The closer the installation level of the upper tuyere 3a is to the dry completion level of the charge, the more effective. Air is supplied to the upper tuyere 3 a and the lower tuyere 3 b of the upper tuyere 3, and air enriched with oxygen is supplied to the lower tuyere 2 and blown into the melting furnace 1. The amount of air or oxygen-enriched air blown into the furnace by each tuyere opens and closes the shut-off valve 6 according to a preset time schedule.
[0014]
In the present embodiment, the air blowing amount of the upper tuyere 3a and the lower tuyere 3b is changed. Switching of the air blowing will be described with reference to the time chart shown in FIG .
[0015]
When air blowing is started, No. No air is blown into one tuyere (upper tuyeres on the upper and lower sides, the same shall apply hereinafter), and the remaining No. 2-No. Blow the same amount of air through the four tuyere. After 10 minutes, no. No. 2 at the same time the air blowing is stopped at the two tuyere. Start 1-air blow. After 10 minutes, no. No. 3 at the same time the air blowing was stopped for only the three tuyere. Start the 2 tuyere air blow again. After 10 minutes, no. No. 4 at the same time the air blowing was stopped at only the four tuyere. Start the 3 tuyere air blow again. After a further 10 minutes, no. At the same time as stopping the air blowing for only one tuyere, Start the 4 tuyere air blow again. The above operation is performed periodically. In addition, No. 1-No. 4 birds mouth blown and regardless of the stop of the total air volume per unit of time the upper tuyeres, from the air amount required for reaction in the reactor, is constant as shown in FIG.
[0016]
For example, in the case of a melting furnace having a processing rate of 20 t / day, a number of tuyere stages of 2, and a number of tuyeres of 4 per stage, the specific values of the air blowing amount and time are each blown with a total air volume of 500 Nm 3 / h. As a result of repeating the pattern in which the tuyere was sequentially blown and stopped for 10 minutes, no blow-through or unloading failure occurred.
[0017]
【The invention's effect】
The effects of the present invention are as follows.
[0018]
(1) By periodically changing the amount of air from the upper tuyere, the pyrolysis residue layer thickness in the furnace is controlled, and the air pressure loss is lowered and stabilized, so the buoyancy of the charge is reduced and blown through. It has the effect of suppressing unsteady phenomena such as unloading defects.
[0019]
(2) As a result of (1), when recovering energy by power generation, there is an effect of stabilizing the power generation amount.
[Brief description of the drawings]
FIG. 1 is a schematic view of a waste melting furnace used in an embodiment of the present invention.
FIG. 2 is a schematic cross-sectional view of an upper tuyere portion of a waste melting furnace used in an embodiment of the present invention.
FIG. 3 is a time chart of an embodiment of the present invention.
FIG. 4 is a schematic view of a conventional waste melting furnace.
[Explanation of symbols]
1 shaft furnace type melting furnace, 2 lower tuyere, 3 upper tuyere, 3a upper tuyere, 3b lower tuyere, 4 flow control valve, 5 header pipe, 6, shutoff valve

Claims (1)

炉体の下部に複数段の羽口を設け、該羽口のうち下段羽口からは酸素を富化した空気を吹き込み、上段羽口からは空気を吹き込む、シャフト炉方式の廃棄物溶融炉の平面方向に複数本設置された上段羽口の空気吹き込み量の制御方法において、
前記上段羽口の各羽口に吹き込む空気を遮断する遮断弁と空気量を調整する流量調整弁を連結し、該遮断弁をあらかじめ設定したスケジュールにしたがって一定時間ごとに周期的に開閉して前記各羽口ごとに空気の吹き込み及びその停止を周期的に行い、各上段羽口からの空気吹き込み量を調整することを特徴とする廃棄物溶融炉の上段羽口からの空気吹き込み量制御方法。
A shaft furnace type waste melting furnace is provided with a plurality of tuyere at the bottom of the furnace body, in which oxygen-enriched air is blown from the lower tuyere and air is blown from the upper tuyere. In the control method of the air blowing amount of the upper tuyere installed in the plane direction,
Wherein connecting the shut-off valve and flow control valve for adjusting the amount of air that blocks air blown into the tuyeres of the upper tuyere, and periodically opened and closed at regular time intervals according to the schedule set the shut-off valve in advance A method for controlling the amount of air blown from the upper tuyere of the waste melting furnace, characterized by periodically blowing and stopping air for each tuyere and adjusting the amount of air blown from each upper tuyere.
JP08981395A 1995-04-14 1995-04-14 Control method of air blowing rate of upper tuyere of waste melting furnace Expired - Fee Related JP3762450B2 (en)

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