JP2005270901A - Method and equipment for treating molten fly ash - Google Patents

Method and equipment for treating molten fly ash Download PDF

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JP2005270901A
JP2005270901A JP2004091116A JP2004091116A JP2005270901A JP 2005270901 A JP2005270901 A JP 2005270901A JP 2004091116 A JP2004091116 A JP 2004091116A JP 2004091116 A JP2004091116 A JP 2004091116A JP 2005270901 A JP2005270901 A JP 2005270901A
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fly ash
molten fly
molten
dioxins
melt
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Satoshi Wada
聰 和田
Yuichi Yagawa
雄一 矢川
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Kubota Corp
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Kubota Corp
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a method and equipment for treating molten fly ash capable of highly maintaining the removal efficiency of dioxins and enhancing the operation efficiency with respect to the treatment of dioxins. <P>SOLUTION: The equipment for treating molten fly ash is provided with a heater 2 for heating molten fly ash, a crusher 3 for crushing molten fly ash heated by the heater after cooling and a discrimination mechanism 4 for discriminating the molten property of the molten fly ash from the crushing state of the molten fly ash by means of the crusher 3. In addition, a sorter 5 for sorting into easily fusible molten fly ash and hardly fusible molten fly ash based on the discrimination result of the discrimination mechanism 4 is disposed. <P>COPYRIGHT: (C)2006,JPO&NCIPI

Description

本発明は、溶融飛灰を処理して、その溶融飛灰中に含まれるダイオキシン類を分解除去する分解工程を行う溶融飛灰処理方法および装置に関する。   The present invention relates to a molten fly ash treatment method and apparatus for performing a decomposition step of treating molten fly ash and decomposing and removing dioxins contained in the molten fly ash.

従来焼却飛灰や溶融飛灰にはダイオキシン類が数ppb程度含まれていることが知られており、このようなダイオキシン類は毒性が強く、環境を害するものとして溶融飛灰中から除去されることが望まれている。
しかしダイオキシン類は、容易には分解されないことが知られており、種々の処理方法が検討されている。
Conventionally, incinerated fly ash and molten fly ash are known to contain several ppb of dioxins. Such dioxins are highly toxic and are removed from molten fly ash as harmful to the environment. It is hoped that.
However, it is known that dioxins are not easily decomposed, and various treatment methods are being studied.

このような処理方法としては、ダイオキシン類を高温に加熱することにより分解する加熱処理、ダイオキシン類を分解する分解剤を添加してダイオキシンを除去する薬品処理(特許文献1参照)が知られており、焼却飛灰や溶融飛灰をいずれかの方法で処理する技術が実用化されている。   As such a treatment method, a heat treatment that decomposes dioxins by heating to high temperature, and a chemical treatment that removes dioxins by adding a decomposition agent that decomposes dioxins (see Patent Document 1) are known. A technique for treating incineration fly ash or molten fly ash by any method has been put into practical use.

特開2002−45820号公報JP 2002-45820 A

飛灰を加熱処理する場合には、400℃〜500℃の高温で処理するために、ダイオキシン類を99.5%以上分解除去できるという利点があるものの、加熱するためのエネルギーコストが嵩む。また、飛灰の性状によっては、飛灰そのものが溶融してしまい、飛灰が搬送経路中で冷却されて付着凝固し、その搬送経路を閉塞してしまう虞がある。そのために、保守点検を必要以上に十分行わねばならないなど運転効率上の問題があり、飛灰が溶融しない低温での処理が望まれている。   In the case where fly ash is heat-treated, dioxins can be decomposed and removed by 99.5% or more because they are treated at a high temperature of 400 ° C. to 500 ° C., but the energy cost for heating increases. Further, depending on the properties of the fly ash, the fly ash itself may be melted, and the fly ash may be cooled and adhered and solidified in the transport path, thereby blocking the transport path. For this reason, there is a problem in operation efficiency such that maintenance and inspection must be performed more than necessary, and treatment at a low temperature at which fly ash does not melt is desired.

そこで、前記薬品処理が適用されるのであるが、薬品処理によると、100℃〜150℃の低温でもダイオキシン類を除去できるという利点があるものの、そのダイオキシン類の除去率は、焼却飛灰の処理を行う場合にも85%程度にとどまることが知られている。   Therefore, the chemical treatment is applied, but the chemical treatment has an advantage that dioxins can be removed even at a low temperature of 100 ° C. to 150 ° C., but the removal rate of the dioxins is the treatment of incineration fly ash. It is known that it is only about 85% even when performing the above.

そのため、ダイオキシン類の除去効率の向上と、ダイオキシン類の処理にかかる運転効率の向上とを両立することは困難であった。   For this reason, it has been difficult to achieve both improvement in the removal efficiency of dioxins and improvement in operation efficiency for the treatment of dioxins.

そこで、本発明の目的は、ダイオキシン類の除去効率を高く維持し、ダイオキシン類の処理にかかる運転効率の向上を図る点にある。   Accordingly, an object of the present invention is to maintain high removal efficiency of dioxins and to improve the operation efficiency related to the treatment of dioxins.

上記目的のため本発明の溶融飛灰処理方法の特徴手段は、溶融飛灰を処理して、その溶融飛灰中に含まれるダイオキシン類を分解除去する分解工程を行う溶融飛灰処理方法であって、前記分解工程の前に、溶融飛灰の溶融性を判別する溶融性確認工程を行い、溶融容易な溶融飛灰と、溶融困難な溶融飛灰とを分別する分別工程を行う点にある。   For the above purpose, the characteristic means of the molten fly ash treatment method of the present invention is a molten fly ash treatment method in which a molten fly ash is treated and a decomposition step of decomposing and removing dioxins contained in the molten fly ash is performed. In addition, prior to the decomposition step, a meltability confirmation step for determining the meltability of the molten fly ash is performed, and a separation step for separating the melted fly ash that is easy to melt and the melted fly ash that is difficult to melt is performed. .

つまり、溶融性確認工程を行うことによって、前記溶融飛灰の溶融温度を知ることができる。溶融温度は厳密に知る必要はないが、少なくとも大まかな溶融温度を知ることによって、溶融容易か、溶融困難かを知ることができる。これにより、前記溶融飛灰を加熱処理して、ダイオキシン類を分解除去する分解工程を行った場合に、その分解工程が良好に行われるかどうかを予測することができる。この予測に基づき、分別工程を行えば、分別された溶融飛灰ごとに適した分解工程を行うことができる。   That is, the melting temperature of the molten fly ash can be known by performing the meltability confirmation step. Although it is not necessary to know the melting temperature strictly, it is possible to know whether it is easy to melt or difficult to melt by knowing at least a rough melting temperature. Thereby, when the decomposition process which decomposes | disassembles and removes dioxins is performed by heat-processing the said molten fly ash, it can be estimated whether the decomposition process is performed favorably. If a separation process is performed based on this prediction, a decomposition process suitable for each separated molten fly ash can be performed.

また、本発明の溶融飛灰処理方法の第2の特徴手段は、溶融容易と判断された前記溶融飛灰を、ダイオキシン類を分解する分解剤を添加してダイオキシンを除去する薬品処理を行う分解工程に供し、溶融困難と判断された前記溶融飛灰を、ダイオキシン類を加熱処理により分解除去する分解工程に供する点にある。   Moreover, the second characteristic means of the molten fly ash treatment method of the present invention is a decomposition in which the molten fly ash determined to be easily melted is subjected to chemical treatment for removing dioxins by adding a decomposition agent for decomposing dioxins. The molten fly ash, which has been subjected to a process and determined to be difficult to melt, is subjected to a decomposition process in which dioxins are decomposed and removed by heat treatment.

従って、溶融飛灰の溶融性に応じて分解処理工程として薬品処理と、加熱処理とを使い分けることができるので、可能な限り加熱処理による高いダイオキシン類の分解除去効率を達成し、加熱処理によると保守点検等による運転効率の低下が予測される場合には、薬品処理により運転効率を高くすることができる。   Therefore, chemical treatment and heat treatment can be properly used as the decomposition treatment process according to the meltability of the molten fly ash, so that the high decomposition and removal efficiency of dioxins by heat treatment is achieved as much as possible. When a decrease in operation efficiency due to maintenance inspection or the like is predicted, the operation efficiency can be increased by chemical treatment.

本発明の溶融飛灰処理装置の特徴構成は、溶融飛灰を加熱する加熱装置と、前記加熱装置で加熱された溶融飛灰を冷却後破砕する破砕装置と、前記破砕装置による溶融飛灰の破砕状況から溶融飛灰の溶融性を判別する判別機構とを設け、前記判別機構の判別結果に基づき、溶融容易な溶融飛灰と溶融困難な溶融飛灰とを分別する分別装置を設けた点にある。   The characteristic configuration of the molten fly ash treatment apparatus of the present invention includes a heating device that heats the molten fly ash, a crushing device that crushes the molten fly ash heated by the heating device, and then crushes the molten fly ash by the crushing device. A discriminating mechanism for discriminating the meltability of the molten fly ash from the crushing situation, and a separation device for separating the melted fly ash that is easily meltable and the melted fly ash that is difficult to melt based on the discrimination result of the discriminating mechanism It is in.

つまり、加熱装置により溶融飛灰を加熱すると、前記溶融飛灰が、その加熱装置の加熱条件に応じた加熱状態になる。このとき、たとえば、ダイオキシン類の加熱処理温度に近い温度にまで前記溶融飛灰が加熱されると、前記溶融飛灰が加熱処理温度において溶融容易なものである場合、溶融飛灰の溶融が観測され、溶融困難なものである場合、加熱による溶融飛灰の粒子形状は変化しない。   That is, when the molten fly ash is heated by the heating device, the molten fly ash becomes a heating state according to the heating condition of the heating device. At this time, for example, when the molten fly ash is heated to a temperature close to the heat treatment temperature of dioxins, when the molten fly ash is easily melted at the heat treatment temperature, melting of the molten fly ash is observed. However, when it is difficult to melt, the particle shape of the molten fly ash by heating does not change.

前記溶融飛灰が前記加熱装置によって溶融させられると、破砕装置による破砕を行う前に冷却固化して一体化する際に大きな粒径のものになるので、前記破砕装置に溶融飛灰が供された場合に、前記破砕装置における溶融飛灰破砕処理の負荷が大きくなる。
一方、前記溶融飛灰が溶融せず、粒子形状が変化していない場合、前記破砕装置による破砕を行っても、前記溶融飛灰の粒径は大きくなっていないから、前記破砕装置に溶融飛灰が供された場合に、前記破砕装置における溶融飛灰破砕処理の負荷は小さいままである。また、破砕負荷のみならず、破砕される溶融飛灰の性状等の破砕状況は前記溶融飛灰の溶融性により大きく異なってくる。
When the melted fly ash is melted by the heating device, the melted fly ash is provided to the crushing device because the molten fly ash has a large particle size when cooled and solidified and integrated before crushing by the crushing device. The load of the molten fly ash crushing process in the crushing device increases.
On the other hand, when the molten fly ash is not melted and the particle shape is not changed, the particle size of the molten fly ash is not increased even when crushing by the crushing device. When ash is provided, the load of the molten fly ash crushing process in the crushing device remains small. Moreover, not only the crushing load but also the crushing conditions such as the properties of the molten fly ash to be crushed vary greatly depending on the meltability of the molten fly ash.

そのため、前記破砕装置による溶融飛灰破砕負荷等の破砕状況から前記溶融飛灰の溶融性を前記判別機構によって判断することができ、その溶融性に応じて前記分別装置が溶融飛灰を分別する。分別された溶融飛灰を、それぞれ、その溶融性に応じた分解工程に供することにより、可能な限り加熱処理による高いダイオキシン類の分解除去効率を達成することができ、加熱処理によると保守点検等による運転効率の低下が予測される場合にも、薬品処理により運転効率を高くすることができる。   Therefore, the meltability of the molten fly ash can be determined by the discriminating mechanism from the crushing situation such as the molten fly ash crushing load by the crushing device, and the sorting device sorts the molten fly ash according to the meltability. . By subjecting the separated molten fly ash to a decomposition process according to its meltability, it is possible to achieve as high a decomposition and removal efficiency of dioxins as possible by heat treatment. Even when a decrease in the operation efficiency due to is predicted, the operation efficiency can be increased by chemical treatment.

本発明の溶融飛灰処理装置の異なる形態としての特徴構成は、溶融飛灰を加熱する加熱装置と、前記加熱装置で加熱された溶融飛灰の溶融状況を観察する画像処理装置と、前記画像処理装置による溶融飛灰の溶融状況から溶融飛灰の溶融性を判別する判別機構とを設け、前記判別機構の判別結果に基づき、溶融容易な溶融飛灰と溶融困難な溶融飛灰とを分別する分別装置とを設けた点にある。   A characteristic configuration as a different form of the molten fly ash treatment apparatus of the present invention includes a heating apparatus that heats the molten fly ash, an image processing apparatus that observes a melting state of the molten fly ash heated by the heating apparatus, and the image A discriminating mechanism that discriminates the meltability of the molten fly ash from the melting status of the molten fly ash by the processing device is provided, and based on the discrimination result of the discriminating mechanism, the molten fly ash that is easy to melt and the molten fly ash that is difficult to melt are separated And a separation device for performing the above.

先の溶融飛灰処理装置によると、破砕装置により溶融飛灰の溶融性を判別したが、溶融飛灰の溶融状況を画像処理して、その流動性等を知ることによっても、溶融飛灰の溶融性を判別することができる。前記分別装置により、前記溶融飛灰を溶融性に従って分別すると、先と同様に高いダイオキシン類の分解除去効率と、高い運転効率とを両立させやすくなる。   According to the previous molten fly ash treatment device, the meltability of the molten fly ash was determined by the crushing device, but the melting state of the molten fly ash was image-processed, and the fluidity etc. The meltability can be determined. When the molten fly ash is separated according to the meltability by the sorting device, it is easy to achieve both high decomposition efficiency of dioxins and high operating efficiency, as before.

また、本発明の溶融飛灰処理装置の特徴構成は、ダイオキシン類を分解する分解剤を添加して、溶融容易な溶融飛灰からダイオキシンを除去する薬品処理装置を備える点にあり、溶融困難な溶融飛灰を加熱して、ダイオキシン類を分解する加熱分解装置を備えてもよい。   In addition, the characteristic configuration of the molten fly ash treatment apparatus of the present invention is that it is provided with a chemical treatment apparatus that removes dioxins from easily melted molten fly ash by adding a decomposition agent that decomposes dioxins, and is difficult to melt. You may provide the thermal decomposition apparatus which heats molten fly ash and decomposes | disassembles dioxins.

つまり、分別された溶融飛灰を、それぞれ、その溶融性に応じた分解工程に供することにより、可能な限り加熱処理による高いダイオキシン類の分解除去効率を達成することができ、加熱処理によると保守点検等による運転効率の低下が予測される場合にも、薬品処理により運転効率を高くすることができる。   In other words, each of the separated molten fly ash can be subjected to a decomposition process according to its meltability to achieve as high a decomposition and removal efficiency of dioxins as possible by heat treatment. Even when a decrease in operation efficiency due to inspection or the like is predicted, the operation efficiency can be increased by chemical treatment.

以下、本発明の実施例を図面に基づいて説明する。   Embodiments of the present invention will be described below with reference to the drawings.

図1に示すように、この発明の溶融飛灰処理装置は、焼却設備等に設けられる飛灰溶融炉において発生する溶融飛灰を、バグフィルタにより捕捉回収した溶融飛灰を被処理物とし、基本的な構成として、被処理物としての溶融飛灰を貯留するための貯留槽1を備え、前記貯留槽1からの溶融飛灰を溶融飛灰を加熱する加熱装置2と、前記加熱装置で加熱された溶融飛灰を冷却後破砕する破砕装置3と、前記破砕装置による溶融飛灰の破砕状況から溶融飛灰の溶融性を判別する判別機構4とを設け、前記判別機構の判別結果に基づき、溶融容易な溶融飛灰と溶融困難な溶融飛灰とを分別する分別装置5を設けてある。また、ダイオキシン類を分解する分解剤を添加して、溶融容易な溶融飛灰からダイオキシンを除去する薬品処理装置6を備え、溶融困難な溶融飛灰を加熱して、ダイオキシン類を分解する加熱分解装置7を備える。   As shown in FIG. 1, the molten fly ash treatment apparatus of the present invention uses molten fly ash generated in a fly ash melting furnace provided in an incineration facility or the like as a processing object, As a basic configuration, a storage tank 1 for storing molten fly ash as an object to be processed is provided, and the heating apparatus 2 that heats the molten fly ash from the storage tank 1 and the heating apparatus A crushing device 3 that crushes the heated molten fly ash after cooling, and a discriminating mechanism 4 that discriminates the meltability of the molten fly ash from the crushing state of the molten fly ash by the crushing device are provided. Based on this, there is provided a separation device 5 for separating molten fly ash that is easy to melt and molten fly ash that is difficult to melt. In addition, it is equipped with a chemical treatment device 6 that adds a decomposing agent that decomposes dioxins and removes dioxins from easily melted molten fly ash, and heat decomposes by heating molten fly ash that is difficult to melt to decompose dioxins. A device 7 is provided.

前記貯留槽1は、溶融飛灰を定量切出して前記加熱装置2へ移送する。加熱装置2では、前記溶融飛灰を400℃に加熱して、破砕装置3に搬送する。破砕装置3に搬送された溶融飛灰は搬送過程で冷却され、塊状となっている。破砕装置3において、前記塊状の溶融飛灰は粒状に破砕される。   The storage tank 1 extracts a quantity of molten fly ash and transfers it to the heating device 2. In the heating device 2, the molten fly ash is heated to 400 ° C. and conveyed to the crushing device 3. The molten fly ash transported to the crushing device 3 is cooled in the transport process and is in a lump shape. In the crushing device 3, the massive molten fly ash is crushed into granules.

ここで、前記搬送過程で冷却された溶融飛灰は、一旦溶融されたものは、大きな塊状となり破砕するのに大きな負荷が必要になり、そうでないものは、破砕するのに小さな負荷で十分となる。そこで、前記破砕装置3には、例えばモータの負荷電流、トルクを計測する装置等、破砕に要する負荷の大小を測定する計測装置31を設けるとともに、前記判別機構では、その計測装置31による測定負荷を基に前記溶融飛灰の溶融性を判断する(溶融性確認工程)。   Here, the melted fly ash cooled in the transporting process is once melted and becomes a large lump and requires a large load to be crushed, and if not, a small load is sufficient for crushing. Become. Therefore, the crushing device 3 is provided with a measuring device 31 for measuring the magnitude of the load required for crushing, such as a motor load current and a device for measuring torque, and the discriminating mechanism has a measuring load by the measuring device 31. Based on the above, the meltability of the molten fly ash is judged (meltability confirmation step).

前記分別装置5は、前記破砕装置3を経由した溶融飛灰を受け入れる投入部51を備えるとともに、低融点溶融飛灰排出部52と高融点溶融飛灰排出部53とを備え、溶融飛灰を低融点溶融飛灰排出部52と高融点溶融飛灰排出部53とのいずれに誘導するかを切り替える切替部54を備え、前記切替部54が、前記判別機構4により切替制御される構成としてある。   The sorting device 5 includes a charging unit 51 that receives molten fly ash that has passed through the crushing device 3, and also includes a low melting point molten fly ash discharge unit 52 and a high melting point molten fly ash discharge unit 53, A switching unit 54 for switching between the low melting point molten fly ash discharge unit 52 and the high melting point molten fly ash discharge unit 53 is provided, and the switching unit 54 is controlled to be switched by the determination mechanism 4. .

前記高融点溶融飛灰排出部53には加熱分解装置7を接続してあり、誘導された溶融飛灰をその加熱分解装置7に導入する。また、前記低融点溶融飛灰排出部52には薬品処理装置6を接続してあり、誘導された溶融飛灰を導入する(分別工程)。   The high-melting point molten fly ash discharge unit 53 is connected to a thermal decomposition apparatus 7, and the induced molten fly ash is introduced into the thermal decomposition apparatus 7. In addition, a chemical treatment device 6 is connected to the low melting point molten fly ash discharge unit 52 to introduce the induced molten fly ash (sorting step).

<加熱分解装置>
前記加熱分解装置7は、加熱キルン71、冷却キルン72を順に備えるとともに、冷却キルン72から排出された溶融飛灰を一旦貯留した後、重金属等をキレート剤等の処理剤で除去して排出する混練機74を備える。
<Thermal decomposition equipment>
The thermal decomposition apparatus 7 includes a heating kiln 71 and a cooling kiln 72 in this order, and after temporarily storing the molten fly ash discharged from the cooling kiln 72, removes heavy metals and the like with a processing agent such as a chelating agent and discharges them. A kneader 74 is provided.

前記加熱キルン71では、供給される溶融飛灰を400℃〜500℃に加熱して、高熱により溶融飛灰中に含まれるダイオキシン類を分解除去する(加熱処理による分解工程)。加熱キルン71を通過した溶融飛灰は、即座に冷却キルン72に投入され、100℃〜120℃に急冷させられ、ダイオキシン類の再合成が抑制させられるようにしてある。冷却させられた溶融飛灰は、一旦貯留部73で貯留される。貯留部73の溶融飛灰は、所定量ごとに混練機74に搬送され、溶融飛灰に処理材貯留槽75から供給される処理材を混練して、排出される溶融飛灰中に含まれる重金属を低減させられる構成としてある。   In the heating kiln 71, the supplied molten fly ash is heated to 400 ° C. to 500 ° C., and dioxins contained in the molten fly ash are decomposed and removed by high heat (decomposition step by heat treatment). The molten fly ash that has passed through the heating kiln 71 is immediately put into the cooling kiln 72 and rapidly cooled to 100 ° C. to 120 ° C., so that resynthesis of dioxins is suppressed. The cooled molten fly ash is temporarily stored in the storage unit 73. The molten fly ash in the storage unit 73 is conveyed to the kneading machine 74 for each predetermined amount, and the processing material supplied from the processing material storage tank 75 is kneaded with the molten fly ash and is contained in the discharged molten fly ash. This is a configuration capable of reducing heavy metals.

<薬品処理装置>
前記薬品処理装置6は、溶融飛灰に混練されるべき分解剤を貯留するための分解剤貯留槽61と、分解剤とともに用いられる促進剤を貯留するための促進剤貯留槽62と、これらを混練する混練部63を備える。
<Chemical treatment equipment>
The chemical treatment apparatus 6 includes a decomposition agent storage tank 61 for storing a decomposition agent to be kneaded with molten fly ash, an accelerator storage tank 62 for storing an accelerator used together with the decomposition agent, and the like. A kneading unit 63 for kneading is provided.

前記分解剤貯留槽61は、飛灰中に含まれるダイオキシン類を分解するために添加する分解剤を貯留し、順次混練部63に搬送自在に構成してある。つぎに、前記促進剤貯留槽62は、飛灰中に含まれるダイオキシン類を分解するために添加する分解剤の反応性を高めるために添加する促進剤を貯留し、順次混練部63に搬送自在に構成してある。これにより溶融飛灰に含まれるダイオキシン類が分解させられる(薬品処理による分解工程)。   The decomposition agent storage tank 61 is configured to store a decomposition agent added to decompose dioxins contained in fly ash and to be sequentially transported to the kneading unit 63. Next, the accelerator storage tank 62 stores an accelerator added to increase the reactivity of the decomposer added to decompose the dioxins contained in the fly ash, and can be sequentially conveyed to the kneading unit 63. It is configured. Thereby, dioxins contained in the molten fly ash are decomposed (decomposition process by chemical treatment).

前記分解剤および促進剤としては、たとえば、金属酸化物を主成分とする微粒子をオイルコーティングしてある分解剤と、アルカリ金属化合物の水溶液,過酸化水素水,洗剤水,1価もしくは多価アルコールの水溶液または有機キレート剤の水溶液を主成分とする促進剤とからなるものが好適に用いられる。   Examples of the decomposing agent and the accelerator include a decomposing agent in which fine particles mainly composed of metal oxide are oil-coated, an aqueous solution of an alkali metal compound, hydrogen peroxide solution, detergent water, monovalent or polyhydric alcohol. And an accelerator composed mainly of an aqueous solution of the above or an aqueous solution of an organic chelating agent is preferably used.

前記混練部63は、移送投入された溶融飛灰と分解剤と促進剤とを混練するものとして構成されている。そして、前記混練部63は、飛灰と分解剤と促進剤を混練するロータリーキルンから構成してあり、混練工程が行われ、前記混練部63内を加熱するための加熱部64を備えて混練工程に引き続き加熱工程を行う。この加熱部64としては、バーナが有効に用いられる。   The kneading unit 63 is configured to knead the molten fly ash, the decomposer, and the accelerator that have been transferred. The kneading part 63 is composed of a rotary kiln for kneading fly ash, a decomposing agent, and an accelerator. A kneading step is performed, and a kneading step is provided with a heating part 64 for heating the inside of the kneading part 63. The heating process is subsequently performed. A burner is effectively used as the heating unit 64.

前記バーナは、前記ロータリーキルンの出口端側において、前記ロータリーキルンの外周面側から火炎で加熱する構成となっており、前記ロータリーキルン内で混練物が混練されると速やかに昇温させられるよう、前記ロータリーキルンにおける前記溶融飛灰と分解剤との合流位置よりもやや下流から前記ロータリーキルンの出口端にわたる広範囲での加熱を可能とする。   The burner is configured to be heated by a flame from the outer peripheral surface side of the rotary kiln at the outlet end side of the rotary kiln, and the rotary kiln is rapidly heated when the kneaded material is kneaded in the rotary kiln. Heating in a wide range from slightly downstream to the exit end of the rotary kiln from the position where the molten fly ash and the decomposition agent join.

前記ロータリーキルンには、内部の混練物を観察するITV65を設けてあり、前記ITV65の撮像から前記混練物の温度を判別し、この温度判別結果に基づき、前記バーナを燃焼させる燃焼制御機構66を設けて構成してある。前記燃焼制御機構66により前記混練物の温度が120〜150℃に維持されるよう前記バーナが燃焼制御される。   The rotary kiln is provided with an ITV 65 for observing the internal kneaded material, and provided with a combustion control mechanism 66 for determining the temperature of the kneaded material from the image of the ITV 65 and burning the burner based on the temperature determination result. Configured. The combustion is controlled by the combustion control mechanism 66 so that the temperature of the kneaded product is maintained at 120 to 150 ° C.

また、溶融飛灰中の水分量を調節して前記分解剤の反応性を維持するための水を前記混合部に供給するための水添加部67を、さらに設けてあっても良い。   Further, a water addition unit 67 for supplying water for adjusting the amount of water in the molten fly ash and maintaining the reactivity of the decomposition agent to the mixing unit may be further provided.

図2に示すように、この発明の溶融飛灰処理装置は、焼却設備等に設けられる飛灰溶融炉において発生する溶融飛灰を、バグフィルタにより捕捉回収した溶融飛灰を被処理物とし、基本的な構成として、被処理物としての溶融飛灰を貯留するための貯留槽1を備える。また、前記貯留槽1からの溶融飛灰を溶融飛灰を加熱する加熱装置2を備え、前記加熱装置で加熱された溶融飛灰を冷却後破砕する破砕装置3と、前記加熱装置で加熱された溶融飛灰の溶融状況を観察する画像処理装置8と、前記画像処理装置8による溶融飛灰の溶融状況から溶融飛灰の溶融性を判別する判別機構4とを設けてある。また、前記判別機構4の判別結果に基づき、溶融容易な溶融飛灰と溶融困難な溶融飛灰とを分別する分別装置5を設けてある。また、ダイオキシン類を分解する分解剤を添加して、溶融容易な溶融飛灰からダイオキシンを除去する薬品処理装置6を備え、溶融困難な溶融飛灰を加熱して、ダイオキシン類を分解する加熱分解装置7を備える。   As shown in FIG. 2, the molten fly ash treatment apparatus of the present invention uses molten fly ash generated in a fly ash melting furnace provided in an incineration facility or the like as a processing object, As a basic configuration, a storage tank 1 for storing molten fly ash as an object to be processed is provided. Moreover, the heating apparatus 2 which heats the molten fly ash from the said storage tank 1 is heated by the crushing apparatus 3 which crushes the molten fly ash heated with the said heating apparatus after cooling, and the said heating apparatus. An image processing apparatus 8 for observing the melting state of the molten fly ash and a discrimination mechanism 4 for determining the meltability of the molten fly ash from the melting state of the molten fly ash by the image processing apparatus 8 are provided. Further, based on the discrimination result of the discriminating mechanism 4, there is provided a sorting device 5 for sorting the melted fly ash that is easy to melt and the melted fly ash that is difficult to melt. In addition, it is equipped with a chemical treatment device 6 that adds a decomposing agent that decomposes dioxins and removes dioxins from easily melted molten fly ash, and heat decomposes by heating molten fly ash that is difficult to melt to decompose dioxins. A device 7 is provided.

前記貯留槽1は、溶融飛灰を定量吐出して前記加熱装置2へ移送する。加熱装置2では、前記溶融飛灰を400℃に加熱する。前記画像処理装置8は、加熱装置2で加熱される溶融飛灰をITV81等で捉え、その撮像を放射温度計等からの溶融飛灰温度情報やその流動性等を加味して解析装置82により解析する。その解析結果に基づき前記判別機構4は前記溶融飛灰の溶融性を判断する。尚、前記破砕装置3は、加熱装置2により加熱された際に塊状となった溶融飛灰を粒状に破砕し、後続のダイオキシン類の分解除去を容易に行えるようにする。   The storage tank 1 discharges a fixed amount of molten fly ash and transfers it to the heating device 2. In the heating device 2, the molten fly ash is heated to 400 ° C. The image processing device 8 captures the molten fly ash heated by the heating device 2 with an ITV 81 or the like, and the imaging device 8 considers the molten fly ash temperature information from a radiation thermometer or the like, its fluidity, etc. To analyze. Based on the analysis result, the determination mechanism 4 determines the meltability of the molten fly ash. The crushing device 3 crushes the molten fly ash that has been agglomerated when heated by the heating device 2 into particles, so that subsequent dioxins can be easily decomposed and removed.

後続の分別装置5以下の構成は、前述の実施例1と同様であるので説明を省略する。   Since the configuration after the subsequent sorting device 5 is the same as that of the first embodiment, the description thereof is omitted.

焼却炉、溶融炉等から発生する溶融飛灰を効率よく処理して、溶融飛灰とともに排出されるダイオキシン類の量を低減させることができる。   The amount of dioxins discharged together with the molten fly ash can be reduced by efficiently treating the molten fly ash generated from an incinerator, a melting furnace or the like.

本発明の溶融飛灰処理装置の概略図Schematic of the molten fly ash treatment apparatus of the present invention 薬品処理装置の概略図Schematic diagram of chemical treatment equipment 加熱分解装置の概略図Schematic diagram of thermal decomposition equipment 本発明の異なる溶融飛灰処理装置の概略図Schematic of different molten fly ash treatment equipment of the present invention

符号の説明Explanation of symbols

2 加熱装置
3 破砕装置
4 判別機構
5 分別装置
2 Heating device 3 Crushing device 4 Discriminating mechanism 5 Sorting device

Claims (6)

溶融飛灰を処理して、その溶融飛灰中に含まれるダイオキシン類を分解除去する分解工程を行う溶融飛灰処理方法であって、
前記分解工程の前に、溶融飛灰の溶融性を判別する溶融性確認工程を行い、
溶融容易な溶融飛灰と、溶融困難な溶融飛灰とを分別する分別工程を行う溶融飛灰処理方法。
A molten fly ash treatment method for treating a molten fly ash and performing a decomposition step of decomposing and removing dioxins contained in the molten fly ash,
Before the decomposition step, perform a meltability confirmation step to determine the meltability of the molten fly ash,
A molten fly ash treatment method for performing a separation step of separating molten fly ash that is easy to melt and molten fly ash that is difficult to melt.
溶融容易と判断された前記溶融飛灰を、ダイオキシン類を分解する分解剤を添加してダイオキシンを除去する薬品処理を行う分解工程に供し、
溶融困難と判断された前記溶融飛灰を、ダイオキシン類を加熱処理により分解除去する分解工程に供する請求項1記載の溶融飛灰処理方法。
The molten fly ash determined to be easily melted is subjected to a decomposition process for performing chemical treatment to remove dioxins by adding a decomposition agent that decomposes dioxins,
The molten fly ash treatment method according to claim 1, wherein the molten fly ash determined to be difficult to melt is subjected to a decomposition step in which dioxins are decomposed and removed by heat treatment.
溶融飛灰を加熱する加熱装置と、
前記加熱装置で加熱された溶融飛灰を冷却後破砕する破砕装置と、
前記破砕装置による溶融飛灰の破砕状況から溶融飛灰の溶融性を判別する判別機構とを設け、
前記判別機構の判別結果に基づき、溶融容易な溶融飛灰と溶融困難な溶融飛灰とを分別する分別装置を設けた
溶融飛灰処理装置。
A heating device for heating the molten fly ash;
A crushing device for crushing the molten fly ash heated by the heating device after cooling;
A discriminating mechanism for discriminating the meltability of the molten fly ash from the crushing status of the molten fly ash by the crushing device;
A molten fly ash treatment apparatus provided with a separation device for separating molten fly ash that is easily meltable and molten fly ash that is difficult to melt based on the determination result of the determination mechanism.
溶融飛灰を加熱する加熱装置と、
前記加熱装置で加熱された溶融飛灰の溶融状況を観察する画像処理装置と、
前記画像処理装置による溶融飛灰の溶融状況から溶融飛灰の溶融性を判別する判別機構とを設け、
前記判別機構の判別結果に基づき、溶融容易な溶融飛灰と溶融困難な溶融飛灰とを分別する分別装置とを設けた
溶融飛灰処理装置。
A heating device for heating the molten fly ash;
An image processing device for observing the melting state of the molten fly ash heated by the heating device;
A discriminating mechanism for discriminating the meltability of the molten fly ash from the melting state of the molten fly ash by the image processing device,
A molten fly ash treatment apparatus provided with a separation device for separating molten fly ash that is easy to melt and molten fly ash that is difficult to melt based on the determination result of the determination mechanism.
ダイオキシン類を分解する分解剤を添加して、溶融容易な溶融飛灰からダイオキシンを除去する薬品処理装置を備えた請求項3または4に記載の溶融飛灰処理装置。   The molten fly ash treatment apparatus according to claim 3 or 4, further comprising a chemical treatment apparatus that adds a decomposing agent that decomposes dioxins and removes dioxins from easily melted molten fly ash. 溶融困難な溶融飛灰を加熱して、ダイオキシン類を分解する加熱分解装置を備えた請求項3または4に記載の溶融飛灰処理装置。   The molten fly ash treatment apparatus according to claim 3, further comprising a thermal decomposition apparatus that decomposes dioxins by heating molten fly ash that is difficult to melt.
JP2004091116A 2004-03-26 2004-03-26 Method and equipment for treating molten fly ash Pending JP2005270901A (en)

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