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JP4851895B2 - Shredder dust melting method - Google Patents
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JP4851895B2 - Shredder dust melting method - Google Patents

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JP4851895B2
JP4851895B2 JP2006248425A JP2006248425A JP4851895B2 JP 4851895 B2 JP4851895 B2 JP 4851895B2 JP 2006248425 A JP2006248425 A JP 2006248425A JP 2006248425 A JP2006248425 A JP 2006248425A JP 4851895 B2 JP4851895 B2 JP 4851895B2
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furnace
tuyere
temperature
shredder dust
oxygen
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JP2008070033A (en
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健 高宮
宏和 田中
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Nippon Steel Engineering Co Ltd
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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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/82Recycling of waste of electrical or electronic equipment [WEEE]

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Description

本発明は、シュレッダーダストをシャフト炉式ガス化溶融炉にて溶融処理する際にタール分の滞留を抑えて安定して操業できるシュレッダーダストの溶融処理方法に関するものである。   The present invention relates to a shredder dust melting method that can stably operate while suppressing the retention of tar when melting shredder dust in a shaft furnace type gasification melting furnace.

廃棄された自動車、家電製品等の解体処理時には、シュレッダマシン等により細かく裁断されたシュレダーダストが発生する。シュレダーダストの処理方法として、シャフト炉式ガス化溶融炉においてシュレッダーダストを溶融処理して再資源化する方法が知られている。この溶融処理は、シャフト炉式ガス化溶融炉へシュレッダーダスト、その他の廃棄物とともにコークス、石灰石等の副原料を投入し、炉底部の下段羽口から空気及び酸素が吹き込まれ、シャフト部上部での乾燥帯で廃棄物を乾燥させ、可燃性物質をシャフト部下部から朝顔部の熱分解帯で熱分解し、熱分解残渣を熱分解帯の下方の燃焼溶融帯で燃焼溶融するものである。   Shredder dust finely cut by a shredder machine or the like is generated at the time of dismantling of discarded automobiles, home appliances, and the like. As a method for treating shredder dust, there is known a method in which shredder dust is melted and recycled in a shaft furnace type gasification melting furnace. In this melting process, shredder dust and other waste materials as well as coke and limestone are added to the shaft furnace type gasification melting furnace, and air and oxygen are blown from the lower tuyere at the bottom of the furnace. In this drying zone, the waste is dried, the combustible substance is pyrolyzed from the lower part of the shaft part in the pyrolysis zone of the morning glory part, and the pyrolysis residue is burned and melted in the combustion melting zone below the pyrolysis zone.

シュレッダーダストはウレタンなどのプラスチック系材料を多く含む。そのため、シュレッダーダストをシャフト炉式ガス化溶融炉に投入すると、乾燥帯の上方の温度が500℃以下となっているので、タール分の発生割合が高くなる。発生したタール分は、固液状化し乾燥帯の上方に滞留し、投入されている廃棄物や炉壁に付着して通気抵抗層となる結果、操業が不安定になる。また、排ガスを排気するガス管内にタール分が付着してガス管を閉塞させるという問題も発生する。   Shredder dust contains many plastic materials such as urethane. Therefore, when the shredder dust is put into the shaft furnace type gasification melting furnace, the temperature above the drying zone is 500 ° C. or less, so that the tar generation rate increases. The generated tar content is solidified into liquid and stays above the drying zone, and adheres to the waste and the furnace wall that has been added to form a ventilation resistance layer, resulting in unstable operation. In addition, there arises a problem that a tar component adheres to the gas pipe exhausting the exhaust gas to block the gas pipe.

そこで、本出願人は、シュレッダーダストの溶融処理方法において、発生するタール分が乾燥帯の上方に滞留するのを防止する技術を提案した(特許文献1参照)。   Therefore, the present applicant has proposed a technique for preventing the generated tar content from staying above the dry zone in the shredder dust melting method (see Patent Document 1).

図4は前記特許文献1のシュレッダーダストの溶融処理方法において、(a)は羽口の位置を示し、(b)は炉内雰囲気温度の変化を示す図である。   4A and 4B are diagrams illustrating a shredder dust melting method of Patent Document 1 in which (a) shows the position of the tuyere and (b) shows changes in the furnace atmosphere temperature.

図4(a)において、シャフト炉式ガス化溶融炉1は、被処理物が上下にシール弁を備えた装入装置8から廃棄物が炉内に投入され、下段羽口2からエア+酸素が吹き込まれて溶融処理される。炉内の温度は温度計5、炉頂温度計6、耐火物内の温度は耐火物温度計7で計測される。シャフト炉式ガス化溶融炉1のストックラインに近接し、且つ、ストックラインを越えない位置に配置した羽口4から、ストックライン近傍の炉内雰囲気温度が550℃〜650℃になるように炉内の被処理物充填層内に空気又は酸素を吹き込むものである。
特開2003−247708号公報
In FIG. 4 (a), the shaft furnace type gasification melting furnace 1 is configured such that a waste material is introduced into a furnace from a charging device 8 provided with seal valves on the upper and lower sides, and air + oxygen is supplied from a lower tuyere 2 to the furnace. Is blown and melted. The temperature in the furnace is measured by a thermometer 5, a furnace top thermometer 6, and the temperature in the refractory is measured by a refractory thermometer 7. Furnace so that the atmosphere temperature in the furnace near the stock line is 550 ° C. to 650 ° C. from the tuyere 4 arranged close to the stock line of the shaft furnace type gasification melting furnace 1 and not exceeding the stock line. Air or oxygen is blown into the object to be processed packed bed.
Japanese Patent Laid-Open No. 2003-247708

しかしながら、前記特許文献1により操業した場合、図4(b)に示すように、炉床部の燃焼溶融帯が約1800℃、ソリューションロス反応帯が約1000℃と高いが、朝顔から上方のシャフト部の熱分解帯・乾燥帯においては、ごみ充填上端部は600℃以上あっても、ソリューションロス反応の吸熱により一旦550℃未満に温度が低下する部分があった。その結果、ストックライン近傍は羽口からの送風により550〜650℃でタール分の滞留の防止はできても、ストックライン近傍より下部でタールが滞留し残渣が炉内で凝着し、棚つりをおこす結果、荷下がりが不良となり、処理量が低下する場合があった。また、棚つりが解消した際にはチャーが飛散し、後流の燃焼室温度が急激に上昇し、燃焼室内にクリンカが生成するため、炉を停止して定期的に除去する必要があった。   However, when operated according to Patent Document 1, as shown in FIG. 4B, the combustion melting zone of the hearth is about 1800 ° C. and the solution loss reaction zone is about 1000 ° C., but the shaft above the morning glory is high. In the pyrolysis zone / dry zone, even if the upper end portion of the dust filling was 600 ° C. or higher, there was a portion where the temperature once decreased to less than 550 ° C. due to the endothermic heat of the solution loss reaction. As a result, even though the vicinity of the stock line can prevent the stay of tar at 550 to 650 ° C by blowing from the tuyere, the tar stays in the lower part of the vicinity of the stock line, and the residue adheres in the furnace. As a result, the unloading becomes poor and the processing amount may be reduced. In addition, when shelves are resolved, char is scattered, the temperature of the combustion chamber in the rear stream rises rapidly, and clinker is generated in the combustion chamber. Therefore, it was necessary to stop the furnace and remove it periodically. .

そこで、本発明は、シャフト炉式ガス化溶融炉でシュレッダーダストを溶融処理する際に、タール分の滞留を防止するとともに炉内雰囲気温度の低下を防止して確実に安定した操業ができるようにすることを目的とする。   Therefore, the present invention prevents a stagnation of the tar content and prevents a decrease in the furnace atmosphere temperature when the shredder dust is melted in the shaft furnace type gasification melting furnace so that stable operation can be performed reliably. The purpose is to do.

本発明のシャフト炉式ガス化溶融炉によるシュレッダーダストの溶融処理方法は、シャフト部又は朝顔部においてソリューションロス反応の吸熱により炉内雰囲気温度が低下する領域又はそれよりも下方から、空気又は酸素を吹き込んで炉内雰囲気を全域に亘り500℃以上として、温度の部分的な低下(500℃未満)を防止するものである。   In the method for melting shredder dust by the shaft furnace type gasification melting furnace of the present invention, air or oxygen is supplied from the region where the atmospheric temperature in the furnace is lowered or lower than that in the shaft portion or morning glory portion due to the endotherm of the solution loss reaction. It blows in and makes the atmosphere in a furnace 500 degreeC or more over the whole region, and prevents the partial fall (less than 500 degreeC) of temperature.

前記特許文献1のシュレッダーダストの溶融処理方法において、操業が不安定となる現象が見られた原因を究明したところ、(1)ストックライン近傍の羽口よりも上方で完全に乾留できなかった一部のシュレッダーダストが炉内を降下した際に、ソリューションロス反応の吸熱により温度の低下したガスでは固体の昇温が進まず、低温領域がシャフト部あるいは朝顔部に形成さることがわかった。この低温領域は、揮発しきれないタール分が滞留して炉内チャー(乾留残渣)とまじって通気抵抗層となったり、(2)前記低温領域で熱分解速度が低下することにより体積収縮が抑制され、荷下がりが不良となったりすることが分かった。   In the method for melting shredder dust of Patent Document 1, the cause of the phenomenon of unstable operation was investigated. (1) It was impossible to completely dry distillation above the tuyere near the stock line. It was found that when the temperature of the shredder dust dropped in the furnace, the temperature of the solid did not increase with the gas whose temperature decreased due to the endotherm of the solution loss reaction, and the low temperature region was formed in the shaft or morning glory. In this low temperature region, the tar component that cannot be volatilized stays and turns into a ventilation resistance layer around the furnace char (dry distillation residue). (2) Volume shrinkage occurs due to a decrease in the thermal decomposition rate in the low temperature region. It was suppressed, and it was found that the unloading was poor.

そこで、ソリューションロス反応の吸熱による部分的な低温領域が形成されるのを防止するため、雰囲気温度が低下する領域またはそれよりも下方に、羽口を設置し空気又は酸素を吹込み炉内のタール、ガス、乾留残渣中の可燃分を燃やすことにより、溶融炉内雰囲気温度を500℃以上に確保することにより揮発しきれない、タール分の滞留による通気抵抗層の形成を防止し、また、熱分解速度が低下することにより体積収縮が抑制されて荷下がりが不良となることを防止する。   Therefore, in order to prevent the formation of a partial low-temperature region due to the endothermic heat of the solution loss reaction, tuyere is installed in the region where the ambient temperature is lowered or below it, and air or oxygen is blown into the furnace. By burning the combustible matter in the tar, gas, and carbonization residue, preventing the formation of a ventilation resistance layer due to retention of the tar, which cannot be volatilized by securing the atmospheric temperature in the melting furnace to 500 ° C. or higher, Decreasing the thermal decomposition rate suppresses volume shrinkage and prevents unloading.

そのため、本発明は、炉内の被処理物充填層内に空気又は酸素を吹き込む上段羽口の位置をストックラインから下方の位置で、且つストックラインからストックラインと下段羽口との距離の40%未満の位置に1段以上設置するとともに、同様に40%〜60%の位置に1段以上設置し、朝顔及びシャフト部の炉内雰囲気を全域に亘り、500℃以上に維持する。なお、ストックラインは、定常運転時に、炉内に投入される被処理物で形成される被処理物充填層の表面レベルであり、下段羽口は炉床部に設けられるエア+酸素を吹き込む羽口である。   Therefore, according to the present invention, the position of the upper tuyere that blows air or oxygen into the workpiece packed bed in the furnace is a position below the stock line and the distance from the stock line to the stock line and the lower tuyere is 40. One or more stages are installed at a position of less than%, and similarly one or more stages are installed at a position of 40% to 60%, and the furnace atmosphere of the morning glory and the shaft part is maintained at 500 ° C. or more over the entire area. The stock line is the surface level of the workpiece packed bed formed by the workpiece to be put into the furnace during steady operation, and the lower tuyere is a feather that blows air + oxygen provided in the hearth The mouth.

図3のグラフに示すようにシャフト炉式ガス化溶融炉では上段羽口から吹き込む酸素量を増やすと炉内の温度が上昇することがわかった。従って上記上段羽口から吹き込む酸素量は全体に吹き込む酸素量の50体積%以上とし、シュレッダーダストの処理割合を被処理量の80質量%以下にして、温度の部分的な低下(500℃未満)を防止することができる。   As shown in the graph of FIG. 3, in the shaft furnace type gasification melting furnace, it was found that the temperature in the furnace rises when the amount of oxygen blown from the upper tuyere is increased. Therefore, the amount of oxygen blown from the upper tuyere is set to 50% by volume or more of the amount of oxygen blown to the whole, and the treatment ratio of shredder dust is set to 80% by weight or less of the amount to be treated, and the temperature is partially decreased (less than 500 ° C.). Can be prevented.

本発明は、シャフト炉式ガス化溶融炉でシュレッダーダストの溶融処理する際に、ソリューションロス反応の吸熱による温度低下領域に位置する羽口から酸素又は空気を送風することにより、溶融炉炉内雰囲気を500℃以上とすることができるので、タール分の滞留による通気抵抗層の形成を防止することができ、炉内の差圧は低下した。また、熱分解速度の低下を防止できるので、安定操業が可能となる。さらに、詰まり、荷下がりが安定し、処理量が増加するとともに、燃焼室温度変動は小さくなり、燃焼室内のクリンカの生成が大きく抑制され、クリンカ除去作業の負荷も低くなった。   The present invention provides a melting furnace furnace atmosphere by blowing oxygen or air from a tuyere located in a temperature lowering region due to heat absorption of a solution loss reaction when a shredder dust is melted in a shaft furnace type gasification melting furnace. Can be set to 500 ° C. or higher, the formation of the ventilation resistance layer due to the retention of the tar content can be prevented, and the pressure difference in the furnace is reduced. In addition, since a decrease in the thermal decomposition rate can be prevented, stable operation is possible. Furthermore, clogging and unloading were stabilized, the amount of processing increased, combustion chamber temperature fluctuations were reduced, clinker generation in the combustion chamber was greatly suppressed, and the clinker removal work load was also reduced.

本発明の実施例について図を参照して説明する。図1は本発明のシュレッダーダストの溶融処理方法において、(a)は羽口の位置を示し、(b)は炉内雰囲気温度の状態を示す図、図2は本発明において上部羽口位置における水平断面部の羽口構成を示す図で、前述の図4と同一構成には同一符号を付す。   Embodiments of the present invention will be described with reference to the drawings. FIG. 1 shows a shredder dust melting method according to the present invention, wherein (a) shows the position of the tuyere, (b) shows the state of the furnace atmosphere temperature, and FIG. 2 shows the upper tuyere position in the present invention. It is a figure which shows the tuyere structure of a horizontal cross-section part, and attaches | subjects the same code | symbol to the same structure as above-mentioned FIG.

上段羽口3aはストックラインから下方の方向で、充填層全体の高さ(下段羽口〜ストックラインの距離)Lの0%から40%の距離(L)に少なくとも1段以上設置し、上段羽口3bは、同様に40%超の距離(L超)から60%の距離(L+L)に少なくとも1段以上設置する。上段羽口3a、3bから吹き込む空気や酸素から換算した上段羽口部酸素量は、総酸素量の50体積%以上とする。 The upper tuyere 3a is installed at least one stage at a distance (L 1 ) from 0% to 40% of the entire packed bed height (distance from the lower tuyere to the stock line) L 0 in the downward direction from the stock line. , upper tuyere 3b is similarly placed at least one or more stages from a distance of over 40% (L 1 than) 60% of the distance (L 2 + L 1). The upper tuyere portion oxygen amount converted from the air and oxygen blown from the upper tuyere 3a and 3b is 50% by volume or more of the total oxygen amount.

図1(a)に示すように、酸素富化空気を吹き込む下段羽口2からシャフト炉式ガス化溶融炉1でシュレッダーダストを溶融処理する際に、低温領域の形成を防止するために、ソリューションロス反応の吸熱により炉内雰囲気温度が低下する領域近傍に配置された羽口3a、3bから空気又は酸素を吹き込む。   As shown in FIG. 1 (a), when the shredder dust is melted in the shaft furnace type gasification melting furnace 1 from the lower tuyere 2 into which oxygen-enriched air is blown, a solution is provided to prevent the formation of a low temperature region. Air or oxygen is blown from the tuyere 3a, 3b arranged in the vicinity of the region where the furnace atmosphere temperature is lowered by the endothermic reaction of the loss reaction.

図1(b)に示すように、炉内雰囲気温度は、炉床部の燃焼溶融帯が約1800℃、ソリューションロス反応帯が約1000℃、朝顔部1aから上方のシャフト部1bは熱分解帯・乾燥帯となり、ソリューションロス反応により温度が低下していくが、羽口3a、3bから空気又は酸素富化空気を吹き込むことによりシャフト部1bの炉内雰囲気温度が昇温して熱分解帯・乾燥帯を500℃以上の範囲に維持することができる。なお、今回はシャフト中間部、朝顔上部から温度計5を差し込み複数点で温度測定を行い、平均したが、測定箇所はシャフト部、朝顔部であればどこでもよい。また、温度実測結果と代表点、例えば耐火物内温度を測定する耐火物温度計7や炉頂部の温度計6の測定値との相関を予め把握し、間接的に耐火物温度や炉頂部のガス温度で管理・制御しても良い。   As shown in FIG. 1 (b), the furnace ambient temperature is about 1800 ° C. in the combustion melting zone of the hearth, about 1000 ° C. in the solution loss reaction zone, and the shaft portion 1b above the morning glory 1a is in the pyrolysis zone.・ It becomes a dry zone and the temperature decreases due to the solution loss reaction, but by blowing air or oxygen-enriched air from the tuyere 3a, 3b, the temperature in the furnace of the shaft portion 1b rises and the pyrolysis zone The drying zone can be maintained in the range of 500 ° C. or higher. In addition, this time, the thermometer 5 was inserted from the middle part of the shaft and the upper part of the morning glory, and the temperature was measured at a plurality of points and averaged. In addition, the correlation between the actual temperature measurement result and the measured value of the representative point, for example, the refractory thermometer 7 for measuring the temperature inside the refractory and the thermometer 6 at the top of the furnace, is grasped in advance, and the refractory temperature and the top of the furnace are indirectly monitored. You may manage and control by gas temperature.

表1に本実施例で溶融処理したA社のシュレッダーダストの性状を示す。   Table 1 shows the properties of the shredder dust of company A melt-treated in this example.

表2に同B市の一般ごみの性状を示す。

Figure 0004851895
Figure 0004851895
Table 2 shows the properties of general waste in B city.
Figure 0004851895
Figure 0004851895

表1に示すシュレッダーダストに表2に示す一般ごみを混合した時の溶融処理条件及び処理結果を表3に示す。

Figure 0004851895
Table 3 shows melting treatment conditions and treatment results when the general waste shown in Table 2 is mixed with the shredder dust shown in Table 1.
Figure 0004851895

本実施例では、シャフト部、朝顔部の温度が550℃〜650℃に維持され、タール分の滞留が防止され、棚つりを起こすことなく安定した操業を行うことができた。   In this example, the temperature of the shaft portion and the morning glory portion was maintained at 550 ° C. to 650 ° C., retention of the tar content was prevented, and stable operation could be performed without causing shelves.

(a)は本発明における羽口の位置を示し、(b)は炉内雰囲気温度の状態を示す図である。(A) shows the position of the tuyere in this invention, (b) is a figure which shows the state of furnace atmospheric temperature. 本発明において上部羽口位置における水平断面部の羽口構成を示す図である。It is a figure which shows the tuyere structure of the horizontal cross-section part in an upper tuyere position in this invention. 上段羽口から吹き込む酸素割合と平均溶融炉内温度との関係を示すグラフである。It is a graph which shows the relationship between the oxygen ratio which blows in from an upper tuyere, and average melting furnace temperature. 従来のシュレッダーダストの溶融処理方法において、(a)は羽口の位置を示し、(b)は炉内雰囲気温度の変化を示す図である。In the conventional shredder dust melting method, (a) shows the position of the tuyere and (b) shows the change in the furnace atmosphere temperature.

符号の説明Explanation of symbols

1:シャフト炉式ガス化溶融炉
1a:朝顔部
1b:シャフト部
2:下段羽口
3a、3b:上部羽口
4:上部羽口
5:温度計
6:炉頂部温度計
7:耐火物温度
8:装入装置
1: shaft furnace type gasification melting furnace 1a: morning glory part 1b: shaft part 2: lower tuyere 3a, 3b: upper tuyere 4: upper tuyere 5: thermometer 6: furnace top thermometer 7: refractory temperature 8 : Loading device

Claims (1)

下段羽口を設けた炉床部、朝顔及びシャフト部を有するシャフト炉式ガス化溶融炉によるシュレッダーダストの溶融処理方法において、
炉内の被処理物充填層内に空気又は酸素を吹き込む上段羽口の位置をストックラインから下方の位置で、且つストックラインからストックラインと下段羽口との距離の40%未満の位置に1段以上設置するとともに、同様に40%〜60%の位置に1段以上設置し、朝顔及びシャフト部の炉内雰囲気を全域に亘り、500℃以上に維持し、上記上段羽口から吹き込む酸素量を、全体に吹き込む酸素量の50体積%以上とし、シュレッダーダストの処理割合を被処理量の80質量%以下にしてタール分の滞留を防止することを特徴とするシュレッダーダストの溶融処理方法。
In the melting treatment method of shredder dust by the shaft furnace type gasification melting furnace having the hearth part, morning glory and shaft part provided with the lower tuyere,
The position of the upper tuyere that blows air or oxygen into the workpiece packed bed in the furnace is a position below the stock line and less than 40% of the distance from the stock line to the stock line and the lower tuyere. Install one or more stages, and similarly install one or more stages at 40% to 60%, maintain the morning glory and the atmosphere in the furnace of the shaft section at 500 ° C or higher, and the amount of oxygen blown from the upper tuyere The amount of oxygen blown into the whole is 50 vol% or more, the shredder dust treatment ratio is 80 mass% or less of the amount to be treated, and the retention of tar content is prevented .
JP2006248425A 2006-09-13 2006-09-13 Shredder dust melting method Expired - Fee Related JP4851895B2 (en)

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