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JP4124103B2 - Waste incineration method and incinerator - Google Patents
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JP4124103B2 - Waste incineration method and incinerator - Google Patents

Waste incineration method and incinerator Download PDF

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JP4124103B2
JP4124103B2 JP2003385235A JP2003385235A JP4124103B2 JP 4124103 B2 JP4124103 B2 JP 4124103B2 JP 2003385235 A JP2003385235 A JP 2003385235A JP 2003385235 A JP2003385235 A JP 2003385235A JP 4124103 B2 JP4124103 B2 JP 4124103B2
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waste
mineral
incineration
gehlenite
incinerated
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克明 松澤
伸彦 久保田
俊一朗 上野
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IHI Corp
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Description

本発明は、廃棄物の焼却方法及び焼却装置に関し、特に、廃棄物の焼却灰を建設・土木資材等として再利用する技術に関する。   The present invention relates to a waste incineration method and an incineration apparatus, and more particularly to a technique for reusing waste incineration ash as construction / civil engineering materials.

廃棄物の焼却灰を建設・土木資材等として再利用するには、環境面から、焼却灰に含まれる所定の金属(主に重金属)の溶出を抑制する必要があり、その基準として、例えば、「土壌の汚染に係る環境基準」(平成3.8.23、環告46)がある。   In order to recycle waste incineration ash as construction and civil engineering materials, it is necessary to suppress elution of certain metals (mainly heavy metals) contained in incineration ash from the environmental viewpoint. There is "Environmental standards for soil contamination" (Heisei 3,8.23, notice 46).

焼却灰からの重金属の溶出を抑制する方法としては、焼却灰を1300℃程度以上で溶融しスラグ化する技術が一般に知られている。
しかしながら、焼却灰の溶融処理は、既存の廃棄物の焼却装置では能力的に難しく、溶融設備の追加が必要な場合が多い。また、溶融可能な設備であっても、1300℃以上の高温処理を必要とすることから、エネルギーコストが高い。
As a method for suppressing elution of heavy metals from the incinerated ash, a technique for melting the incinerated ash at about 1300 ° C. or more to form slag is generally known.
However, melting treatment of incineration ash is difficult in terms of performance with existing waste incinerators, and it is often necessary to add melting equipment. Moreover, even if the equipment can be melted, the energy cost is high because a high temperature treatment of 1300 ° C. or higher is required.

そこで、焼却灰の処理技術として、炉内の酸素濃度を制御することにより、比較的低温での熱処理によって焼却灰からの重金属の溶出を抑制する技術が提案されている(例えば、特許文献1参照)。
特開2003−190910号公報
Thus, as a treatment technique for incineration ash, a technique has been proposed in which elution of heavy metals from the incineration ash is suppressed by heat treatment at a relatively low temperature by controlling the oxygen concentration in the furnace (see, for example, Patent Document 1). ).
JP 2003-190910 A

上記した炉内の酸素濃度を制御する技術では、焼却灰を溶融する技術に比べて、処理温度の低温化が図れるものの、既存の焼却設備に適用するには、重金属溶出をより確実に抑制できることが望まれる。特に、低温での焼却灰の熱処理技術では、処理温度に応じて鉛(Pb)の溶出量が変化しやすいことから、環境基準を満たす上で、鉛(Pb)の溶出を確実に抑制可能な技術の開発が望まれている。   Although the technology for controlling the oxygen concentration in the furnace described above can reduce the processing temperature compared to the technology for melting incineration ash, it can more reliably suppress elution of heavy metals when applied to existing incineration facilities. Is desired. In particular, in the heat treatment technology of incineration ash at low temperatures, the elution amount of lead (Pb) is likely to change depending on the treatment temperature, so that the elution of lead (Pb) can be reliably suppressed to meet environmental standards. Technology development is desired.

本発明は、上記事情に鑑みてなされたものであり、低温での熱処理によって焼却灰からの重金属の溶出、特に、鉛(Pb)の溶出を抑制することが可能な廃棄物の焼却方法及び焼却装置を提供することを目的とする。   The present invention has been made in view of the above circumstances, and a waste incineration method and incineration capable of suppressing elution of heavy metals from incineration ash, in particular, elution of lead (Pb), by heat treatment at a low temperature. An object is to provide an apparatus.

上記した本発明の目的は、焼却対象の廃棄物に、Si及びCaを含む物質を添加することにより、焼却中の処理物内で前記廃棄物からの重金属の溶出を抑制するCaを含む鉱物相を発達させることを特徴とする廃棄物の焼却方法により達成される。 An object of the present invention described above is to add a substance containing Si and Ca to a waste to be incinerated, thereby suppressing a mineral phase containing Ca to suppress elution of heavy metals from the waste in the treated product being incinerated. It is achieved by a waste incineration method characterized by developing

これにより、低温での熱処理によって焼却灰からの重金属の溶出、特に、鉛の溶出を抑制することが可能となる。 Thereby, it becomes possible to suppress elution of heavy metals from incineration ash, in particular, elution of lead, by heat treatment at a low temperature.

前記廃棄物の焼却方法において、前記Caを含む鉱物相は、例えば、ゲーレナイト(Gehlenite:SiCaAl)を含む。 In the waste incineration method, the mineral phase containing Ca includes, for example, Gehlenite (SiCa 2 Al 2 O 7 ).

この場合、前記物質は、Si、Ca、Alをモル比で、Si:Ca:Al=1:2:2の割合で含むのが好ましい。   In this case, the substance preferably contains Si, Ca, and Al in a molar ratio of Si: Ca: Al = 1: 2: 2.

また、前記廃棄物の焼却方法においては、前記物質として前記Caを含む鉱物相を有する鉱物を予め生成し、該生成した鉱物を焼却対象の廃棄物に添加してもよい。 Further, in the waste incineration method, a mineral having a mineral phase containing the Ca as the substance may be generated in advance, and the generated mineral may be added to the waste to be incinerated.

この場合、予め生成する鉱物としては、例えば、ゲーレナイト(SiCaAl)が挙げられる。 In this case, as the minerals generated in advance, for example, gehlenite (SiCa 2 Al 2 O 7) .

前記廃棄物の焼却方法は、焼却対象の廃棄物に、焼却中の処理物内で前記廃棄物からの重金属の溶出を抑制するCaを含む鉱物相を発達させるSi及びCaを含む物質を投入するための投入口を備えることを特徴とする廃棄物の焼却装置により実施できる。 In the incineration method of the waste, a substance containing Si and Ca that develops a mineral phase containing Ca that suppresses elution of heavy metals from the waste in the treatment object being incinerated is thrown into the waste to be incinerated. It can be implemented by a waste incinerator characterized by having an inlet for the purpose.

また、前記廃棄物の焼却方法は、焼却中の処理物内で前記廃棄物からの重金属の溶出を抑制するCaを含む鉱物相を発達させるSi及びCaを含む物質として、前記Caを含む鉱物相を有する鉱物を生成するための鉱物生成装置を備えることを特徴とする廃棄物の焼却装置によっても実施できる。 Further, the method for incinerating waste includes a mineral phase containing Ca as a substance containing Si and Ca that develops a mineral phase containing Ca that suppresses elution of heavy metals from the waste in the treated product being incinerated. It can also be implemented by a waste incineration apparatus comprising a mineral generating device for generating a mineral having

この場合、前記鉱物としては、例えば、ゲーレナイト(SiCaAl)が挙げられる。 In this case, examples of the mineral include gehlenite (SiCa 2 Al 2 O 7 ).

本発明の廃棄物の焼却方法及び焼却装置によれば、焼却中の処理物内でCaを含む鉱物相を発達させることにより、低温での熱処理によって焼却灰からの重金属の溶出、特に、鉛(Pb)の溶出を抑制することが可能となる。   According to the incineration method and the incineration apparatus of the present invention, the elution of heavy metals from incineration ash by heat treatment at low temperature, particularly lead ( It becomes possible to suppress elution of Pb).

以下、本発明について説明する。
本発明者らは、上記文献(特開2003−190910号公報)に記載の技術に着目し、焼却灰の低温熱処理に関する研究を進めた結果、熱処理中の処理物内でCaを含む鉱物相を発達させることにより、焼却灰からの重金属の溶出量、特に、鉛(Pb)の溶出量を減少させることができることを解明し、この鉱物相の核となる物質あるいは鉱物相の成長を促す物質として、焼却対象の廃棄物に、Si及びCaを含む物質を添加することにより本発明を完成した。
The present invention will be described below.
The present inventors paid attention to the technique described in the above-mentioned document (Japanese Patent Laid-Open No. 2003-190910), and as a result of research on low-temperature heat treatment of incinerated ash, As a result of elucidating that it is possible to reduce the amount of elution of heavy metals from incineration ash, in particular, the amount of elution of lead (Pb), and as a substance that promotes the growth of the mineral phase or the core of this mineral phase The present invention was completed by adding substances containing Si and Ca to the waste to be incinerated.

すなわち、本発明の廃棄物の焼却方法においては、Si及びCaを含む物質を、焼却処理前あるいは焼却中の廃棄物に添加することにより、焼却中の処理物内でCaを含む鉱物相を発達させ、これにより、廃棄物の焼却灰を、重金属の溶出、特に、鉛(Pb)の溶出の少ないものにする。   That is, in the waste incineration method of the present invention, a mineral phase containing Ca is developed in the treated product during incineration by adding a substance containing Si and Ca to the waste before or during the incineration treatment. As a result, the incineration ash of the waste is reduced in elution of heavy metals, in particular, elution of lead (Pb).

なお、本発明では、廃棄物の焼却処理過程において、焼却灰の重金属溶出抑制化を図っている。つまり、廃棄物の焼却処理後に、焼却灰を別途熱処理する工程を必ずしも必要としない。これは、工程並びに装置構成の簡素化を図る上で有利である。なお、廃棄物の焼却灰に、Si及びCaを含む物質(Caを含む鉱物を含む)を添加し、それに対して熱処理を行っても同様の抑制効果が得られることは言うまでもない。   In the present invention, heavy metal elution is suppressed in the incineration ash during the waste incineration process. That is, it is not always necessary to separately heat the incineration ash after the waste incineration. This is advantageous in simplifying the process and the apparatus configuration. Needless to say, the same suppression effect can be obtained by adding a substance containing Si and Ca (including a mineral containing Ca) to the incinerated ash of the waste, and subjecting it to heat treatment.

ここで、Caを含む鉱物相の発達により重金属の溶出が抑制される理由は、例えば次の2つが考えられる。
(1)鉱物相が発達すると処理物中の重金属が鉱物相内に取り込まれる。そして、その重金属が鉱物相の組織として固定化されることで、重金属の溶出が抑制される。
(2)鉱物相が発達すると処理物中のCaを代表とするアルカリ土類またはアルカリ金属が鉱物相内に取り込まれる。アルカリ土類またはアルカリ金属が鉱物相の組織として固定化されることで、アルカリ土類またはアルカリ金属の溶出が抑制される。その結果、溶出液のpHの上昇が抑制され、溶出液のpHが酸性に傾く。溶出液のpHが酸性に傾くことにより、重金属の溶解度が低下し、重金属の溶出が抑制される。
Here, there are two possible reasons why elution of heavy metals is suppressed by the development of the mineral phase containing Ca.
(1) When the mineral phase develops, heavy metals in the processed material are taken into the mineral phase. And the elution of a heavy metal is suppressed because the heavy metal is fixed as a structure | tissue of a mineral phase.
(2) When the mineral phase develops, an alkaline earth or alkali metal typified by Ca in the treated product is taken into the mineral phase. By fixing the alkaline earth or alkali metal as a mineral phase structure, elution of the alkaline earth or alkali metal is suppressed. As a result, an increase in pH of the eluate is suppressed, and the pH of the eluate is inclined to be acidic. When the pH of the eluate is inclined to be acidic, the solubility of heavy metals is lowered and elution of heavy metals is suppressed.

前記Caを含む鉱物相としては、例えば、ゲーレナイト(SiCaAl)が挙げられる。
Si、Ca、Alを含む物質を、焼却前あるいは焼却中の廃棄物中に添加することにより、焼却処理時の廃棄物の昇温に伴って、処理物中にゲーレナイト(SiCaAl)の核を生成させ、処理物内でゲーレナイト相を発達させることが可能である。この場合、ゲーレナイト相を良好に発達させる上で、前記物質に、Si、Ca、Alがモル比で、Si:Ca:Al=1:2:2の割合で含まれるのが好ましい。なお、廃棄物中には一般にAlが多く含まれ、また焼却処理空間には酸素が含まれることから、添加する物質にAlが含まれてなくてもよい。すなわち、少なくともSi及びCaを含む物質を廃棄物中に添加することにより、焼却中の処理物内でゲーレナイト相を発達させることが可能である。
Examples of the mineral phase containing Ca include gehlenite (SiCa 2 Al 2 O 7 ).
By adding a substance containing Si, Ca, and Al to waste before incineration or during incineration, as the temperature of the waste during incineration increases, the treated material contains gehlenite (SiCa 2 Al 2 O 7 ) Nuclei and a gehlenite phase can be developed in the processed material. In this case, in order to satisfactorily develop the gehlenite phase, it is preferable that Si, Ca, and Al are included in the substance in a molar ratio of Si: Ca: Al = 1: 2: 2. Since waste generally contains a large amount of Al, and the incineration space contains oxygen, the substance to be added may not contain Al. That is, by adding a substance containing at least Si and Ca to the waste, it is possible to develop a gehlenite phase in the treated product during incineration.

また、本発明の廃棄物の焼却方法において、ゲーレナイトなどのCaを含む鉱物を予め生成しておき、その鉱物を焼却対象の廃棄物に投入/添加することにより、より確実に、焼却中の処理物内でCaを含む鉱物相(ゲーレナイト相など)を発達させることが可能である。ゲーレナイトは、例えば、次式(1)、(2)に基づいて生成可能である。
SiO+2CaO+Al→SiCaAl …(1)
SiO+2CaCO+Al→SiCaAl+2CO …(2)
Further, in the waste incineration method of the present invention, a mineral containing Ca such as gehlenite is generated in advance, and the mineral is input / added to the waste to be incinerated, so that the treatment during incineration can be performed more reliably. It is possible to develop a mineral phase containing Ca (Gelenite phase, etc.) in the object. The gehlenite can be generated based on, for example, the following formulas (1) and (2).
SiO 2 + 2CaO + Al 2 O 3 → SiCa 2 Al 2 O 7 (1)
SiO 2 + 2CaCO 3 + Al 2 O 3 → SiCa 2 Al 2 O 7 + 2CO 2 (2)

次に、前記本発明の廃棄物の焼却方法を実施可能な焼却装置について説明する。
廃棄物の焼却装置としては、例えば、回転式ストーカ炉や、移動層式ストーカ炉などを用いることができる。回転式ストーカ炉の構成は、例えば、特開平11−257616号公報に記載されている。また、移動層式ストーカ炉の構成は、例えば、特開2002−181311号公報に記載されている。
図1は、本発明に係る廃棄物の焼却装置を回転式ストーカ炉に適用した例を模式的に示す図である。
Next, an incinerator capable of implementing the waste incineration method of the present invention will be described.
As the waste incinerator, for example, a rotary stoker furnace or a moving bed stoker furnace can be used. The configuration of the rotary stoker furnace is described in, for example, JP-A-11-257616. The configuration of the moving bed stoker furnace is described in, for example, Japanese Patent Application Laid-Open No. 2002-181311.
FIG. 1 is a diagram schematically showing an example in which the waste incinerator according to the present invention is applied to a rotary stoker furnace.

図1において、焼却装置1は、回転自在に配設される円筒状の燃焼炉2と、この燃焼炉2で発生した燃焼ガスが導入されるボイラ3と、ボイラ3から排出される排ガスが導入されるエコノマイザー4と、廃棄物Wに添加される鉱物を生成するための鉱物生成装置20とを含んで構成されている。   In FIG. 1, an incinerator 1 has a cylindrical combustion furnace 2 disposed rotatably, a boiler 3 into which combustion gas generated in the combustion furnace 2 is introduced, and exhaust gas discharged from the boiler 3 is introduced. The economizer 4 and the mineral generator 20 for generating the mineral added to the waste W are configured.

燃焼炉2の導入部2aには、廃棄物Wを一時貯蔵する供給ホッパ5と、供給ホッパ5から廃棄物Wを適宜燃焼炉2内へ送るためのスクリューフィーダ6とが設置されている。供給ホッパ5には、鉱物生成装置20で生成された鉱物を廃棄物W中に投入するための投入口5aが設けられている。また、燃焼炉2の排出部2bは、燃焼灰を排出するための落下抗7に接続されている。円筒状の燃焼炉2は、導入部2aに比べて排出部2bが低くなるように、回転軸が傾けて配されている。燃焼炉2の下部側面には、燃焼炉2内に燃焼用空気を供給するための複数の空気吹出部10a〜10dが配設されている。複数の空気吹出部10a〜10dはそれぞれ、燃焼用空気の組成を適宜調整する燃焼空気生成装置15に接続されており、複数の空気吹出部10a〜10dから吹き出される空気は、廃棄物Wの種類や燃焼炉2の燃焼条件等に応じて酸素濃度や供給量等が個々に制御される。鉱物生成装置20は、原料を昇温するための熱処理炉を備えており、熱処理炉内の温度や環境条件が適宜制御される。   A supply hopper 5 for temporarily storing the waste W and a screw feeder 6 for appropriately sending the waste W from the supply hopper 5 into the combustion furnace 2 are installed in the introduction part 2 a of the combustion furnace 2. The supply hopper 5 is provided with an input port 5a for supplying the mineral generated by the mineral generating device 20 into the waste W. Moreover, the discharge part 2b of the combustion furnace 2 is connected to the drop resister 7 for discharging the combustion ash. The cylindrical combustion furnace 2 is disposed with the rotation axis inclined so that the discharge part 2b is lower than the introduction part 2a. A plurality of air blowing portions 10 a to 10 d for supplying combustion air into the combustion furnace 2 are disposed on the lower side surface of the combustion furnace 2. Each of the plurality of air blowing portions 10a to 10d is connected to a combustion air generating device 15 that appropriately adjusts the composition of the combustion air, and the air blown from the plurality of air blowing portions 10a to 10d is the waste W Depending on the type, the combustion conditions of the combustion furnace 2, etc., the oxygen concentration, the supply amount, etc. are individually controlled. The mineral generator 20 includes a heat treatment furnace for raising the temperature of the raw material, and the temperature and environmental conditions in the heat treatment furnace are appropriately controlled.

上記構成の焼却装置1においては、まず、鉱物生成装置20において、Caを含む鉱物、本例ではゲーレナイト(SiCaAl)が生成される。ゲーレナイトは、例えば、SiO、CaO(あるいはCaCO)、Alの混合物を熱処理炉21内に投入して昇温することにより生成することができる。生成したゲーレナイトは、供給ホッパ5の投入口5aを介して焼却前の廃棄物Wに添加される。ゲーレナイトの添加は、自動で行ってもよく、作業者が行ってもよい。また、ゲーレナイトの添加量は、廃棄物Wの種類や燃焼炉2の燃焼条件等に応じて設定される。 In the incinerator 1 having the above-described configuration, first, the mineral generating device 20 generates Ca-containing mineral, in this example, gehlenite (SiCa 2 Al 2 O 7 ). The gehlenite can be produced, for example, by putting a mixture of SiO 2 , CaO (or CaCO 3 ), and Al 2 O 3 into the heat treatment furnace 21 and raising the temperature. The produced gehlenite is added to the waste W before incineration through the inlet 5a of the supply hopper 5. The addition of gehlenite may be performed automatically or by an operator. Further, the addition amount of gehlenite is set according to the type of waste W, the combustion conditions of the combustion furnace 2, and the like.

そして、ゲーレナイトが添加された廃棄物Wが焼却炉2内に導入され、廃棄物Wが焼却処理される。廃棄物Wの焼却時、複数の空気吹出部10a〜10dを介して燃焼用空気が燃焼炉2内に供給される。燃焼によって発生した排ガス(燃焼ガス)は、排出部2bからボイラ3に導入されて熱回収され、さらに、エコノマイザー4へ導かれる。   Then, the waste W to which gelenite is added is introduced into the incinerator 2, and the waste W is incinerated. When the waste W is incinerated, combustion air is supplied into the combustion furnace 2 through the plurality of air blowing portions 10a to 10d. Exhaust gas (combustion gas) generated by the combustion is introduced into the boiler 3 from the discharge part 2b, recovered by heat, and further guided to the economizer 4.

また、廃棄物Wの燃焼時、焼却中の処理物(廃棄物W、廃棄物Wの炭化物、燃焼灰など)内では、添加されたゲーレナイト(SiCaAl)を核として、廃棄物Wあるいは燃焼灰に含まれるSi、Ca、Alや重金属(Pbなど)を取り込みながら、ゲーレナイト相が発達する。ゲーレナイト相の発達により、排出部2bから排出される焼却灰は、重金属の溶出、特に、鉛(Pb)の溶出の少ないものになる。燃焼灰は、落下抗7を介して回収され、建設・土木資材(骨材など)等として再利用される。 In addition, when the waste W is burned, in the incinerated processed material (waste W, the carbide of the waste W, combustion ash, etc.), the added gehlenite (SiCa 2 Al 2 O 7 ) is used as the core for the waste. While taking in Si, Ca, Al, and heavy metals (such as Pb) contained in W or combustion ash, the gehlenite phase develops. Due to the development of the gehlenite phase, the incineration ash discharged from the discharge part 2b becomes one with less elution of heavy metals, in particular, lead (Pb). Combustion ash is collected through the fall shield 7 and reused as construction / civil engineering materials (eg aggregate).

なお、本例では、燃焼炉2に導入する前の廃棄物Wに鉱物(ゲーレナイト)を添加しているが、燃焼炉2内にゲーレナイトを投入/添加してもよい。この場合、ゲーレナイトの投入位置は、ゲーレナイト相が発達する時間を確保する上で、燃焼炉2の導入部2aに近い位置であるのが好ましく、燃焼炉2の最高温度地点よりも上流側であるのが好ましい。   In this example, mineral (gerenite) is added to the waste W before being introduced into the combustion furnace 2, but gehlenite may be charged / added into the combustion furnace 2. In this case, in order to secure the time for the development of the gehlenite phase, the galenite charging position is preferably a position close to the introduction part 2a of the combustion furnace 2 and upstream of the maximum temperature point of the combustion furnace 2. Is preferred.

[ラボ試験によるゲーレナイト添加試験]
表1下段に示す実灰相当の組成になるように、市販試薬を混合して表1上段に示す模擬灰(以後、試料1と称す)を作成した。また、表1下段に示す実灰相当の組成になるように、ゲーレナイトと市販試薬の混合物とを1:4の重量比で混合した試料(以後、試料2と称す)を作成した。
[Gelenite addition test by laboratory test]
A commercially available reagent was mixed so as to have a composition corresponding to real ash shown in the lower part of Table 1, and a simulated ash (hereinafter referred to as Sample 1) shown in the upper part of Table 1 was prepared. In addition, a sample (hereinafter referred to as sample 2) was prepared by mixing gehlenite and a mixture of commercially available reagents at a weight ratio of 1: 4 so as to have a composition corresponding to real ash shown in the lower part of Table 1.

Figure 0004124103
Figure 0004124103

ゲーレナイトは次のように作成した。
SiO、CaCO、Alの各試薬をモル比で1:2:1で混合し、マッフル炉で10℃/min で1500℃まで昇温し、その後3時間保持し、自然放冷した。X線回折装置によりゲーレナイト(Gehlenite:SiCaAl)が生成していることを確認した。
Gehlenite was created as follows.
Each reagent of SiO 2 , CaCO 3 , and Al 2 O 3 is mixed at a molar ratio of 1: 2: 1, heated to 1500 ° C. at 10 ° C./min in a muffle furnace, then held for 3 hours, and then allowed to cool naturally. did. It was confirmed that gehlenite (SiCa 2 Al 2 O 7 ) was generated by an X-ray diffractometer.

次に、試料1と試料2とを、10℃/min で、所定の処理温度(800℃、900℃、1000℃、1100℃)まで昇温し、1時間保持後取り出して大気放冷した。その処理物について、環告46号試験に準じて、溶出試験を行い、溶出液のpHとPb濃度を分析した。試験結果を図2に示す。   Next, the sample 1 and the sample 2 were heated to a predetermined processing temperature (800 ° C., 900 ° C., 1000 ° C., 1100 ° C.) at 10 ° C./min, held for 1 hour, taken out, and allowed to cool to the atmosphere. The treated product was subjected to a dissolution test in accordance with Test No. 46, and the pH and Pb concentration of the eluate were analyzed. The test results are shown in FIG.

図2に示すように、ゲーレナイトの添加により、鉛溶出量が 1/10 以上に減少する結果が得られた。また、ゲーレナイトを添加した条件では、処理温度の上昇に従い、鉱物量の発達が顕著に見られた。また、ゲーレナイトの添加により、溶出液のpHの値も著しく低下した。   As shown in FIG. 2, the result that lead elution amount decreased to 1/10 or more by the addition of gehlenite was obtained. In addition, under the condition where gehlenite was added, the development of the amount of minerals was noticeable as the treatment temperature increased. In addition, the pH value of the eluate was significantly reduced by the addition of gehlenite.

このように、模擬灰を用いた試験において、ゲーレナイトの添加により、鉛の溶出量を抑制できることが確認された。   Thus, in the test using simulated ash, it was confirmed that the elution amount of lead can be suppressed by adding gelenite.

以上、添付図面を参照しながら本発明に係る好適な実施形態について説明したが、本発明は係る例に限定されないことは言うまでもない。上述した例において示した各構成部材の諸形状や組み合わせ等は一例であって、本発明の主旨から逸脱しない範囲において設計要求等に基づき種々変更可能である。   As described above, the preferred embodiments according to the present invention have been described with reference to the accompanying drawings, but the present invention is not limited to the examples. Various shapes, combinations, and the like of the constituent members shown in the above-described examples are examples, and various modifications can be made based on design requirements and the like without departing from the gist of the present invention.

本発明に係る廃棄物の焼却装置を回転式ストーカ炉に適用した例を模式的に示す図である。It is a figure which shows typically the example which applied the incinerator of the waste which concerns on this invention to a rotary stoker furnace. 模擬灰を用い、鉱物(ゲーレナイト)の添加による鉛溶出抑制効果を試験した結果を示すグラフ図である。It is a graph which shows the result of having tested the lead elution inhibitory effect by addition of a mineral (gerenite) using simulated ash.

符号の説明Explanation of symbols

1…焼却装置、2…燃焼炉、W…廃棄物、20…鉱物生成装置、5…供給ホッパ、5a…投入口。   DESCRIPTION OF SYMBOLS 1 ... Incinerator, 2 ... Combustion furnace, W ... Waste, 20 ... Mineral production | generation apparatus, 5 ... Supply hopper, 5a ... Input port.

Claims (8)

廃棄物を焼却処理する方法において、焼却対象の廃棄物に、Si及びCaを含む物質を添加することにより、焼却中の処理物内で前記廃棄物からの重金属の溶出を抑制するCaを含む鉱物相を発達させることを特徴とする廃棄物の焼却方法。 In a method for incineration of waste , a mineral containing Ca that suppresses elution of heavy metals from the waste in the incinerated waste by adding a substance containing Si and Ca to the waste to be incinerated Waste incineration method characterized by developing phases . 前記Caを含む鉱物相は、ゲーレナイト(SiCaAl)を含むことを特徴とする請求項に記載の廃棄物の焼却方法。 The waste incineration method according to claim 1 , wherein the Ca-containing mineral phase includes gehlenite (SiCa 2 Al 2 O 7 ). 前記物質は、Si、Ca、Alをモル比で、Si:Ca:Al=1:2:2の割合で含むことを特徴とする請求項1または請求項2のいずれかに記載の廃棄物の焼却方法。 3. The waste according to claim 1, wherein the substance contains Si, Ca, and Al in a molar ratio of Si: Ca: Al = 1: 2: 2. Incineration method. 前記物質として前記Caを含む鉱物相を有する鉱物を予め生成し、該生成した鉱物を焼却対象の廃棄物に添加することを特徴とする請求項1から請求項3のいずれかに記載の廃棄物の焼却方法。 The waste according to any one of claims 1 to 3 , wherein a mineral having a mineral phase containing Ca as the substance is generated in advance, and the generated mineral is added to the waste to be incinerated. Incineration method. 予め生成する鉱物は、ゲーレナイト(SiCaAl)であることを特徴とする請求項に記載の廃棄物の焼却方法。 The waste incineration method according to claim 4 , wherein the mineral produced in advance is gehlenite (SiCa 2 Al 2 O 7 ). 廃棄物を焼却処理する装置において、焼却対象の廃棄物に、焼却中の処理物内で前記廃棄物からの重金属の溶出を抑制するCaを含む鉱物相を発達させるSi及びCaを含む物質を投入するための投入口を備えることを特徴とする廃棄物の焼却装置。 In a device for incineration of waste, a substance containing Si and Ca that develops a mineral phase containing Ca that suppresses the elution of heavy metals from the waste in the incinerated waste is input to the incinerated waste An incinerator for waste, comprising an inlet for carrying out the process. 廃棄物を焼却処理する装置において、焼却中の処理物内で前記廃棄物からの重金属の溶出を抑制するCaを含む鉱物相を発達させるSi及びCaを含む物質として、前記Caを含む鉱物相を有する鉱物を生成するための鉱物生成装置を備えることを特徴とする廃棄物の焼却装置。 In an apparatus for incinerating waste , a mineral phase containing Ca as a substance containing Si and Ca that develops a mineral phase containing Ca that suppresses elution of heavy metals from the waste in the incinerated waste. A waste incineration apparatus comprising a mineral generation apparatus for generating a mineral having the same . 前記鉱物は、ゲーレナイト(SiCaAl)であることを特徴とする請求項に記載の廃棄物の焼却方法。 The waste mineral incineration method according to claim 7 , wherein the mineral is gehlenite (SiCa 2 Al 2 O 7 ).
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