JP6670037B2 - Processing method of fly ash containing radioactive material - Google Patents

Processing method of fly ash containing radioactive material Download PDF

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JP6670037B2
JP6670037B2 JP2014170090A JP2014170090A JP6670037B2 JP 6670037 B2 JP6670037 B2 JP 6670037B2 JP 2014170090 A JP2014170090 A JP 2014170090A JP 2014170090 A JP2014170090 A JP 2014170090A JP 6670037 B2 JP6670037 B2 JP 6670037B2
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fly ash
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ash containing
radioactive substance
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JP2016045098A (en
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田中 宜久
宜久 田中
重 品川
重 品川
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Taiheiyo Cement Corp
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Description

本発明は、放射性物質による汚染物を焼却、焼成、溶融した際等に発生する放射性物質を含む飛灰を処理する方法に関する。 The present invention relates to contamination by radioactive material incineration, calcination, to how to process the fly ash containing radioactive substances generated in such when melted.

震災に伴う原発事故で飛散したセシウム等の放射性物質に汚染された汚染物、例えば樹木や枯葉等の草木類、家庭ごみ、土壌、瓦礫等を焼却、焼成、溶融等の手段で熱処理すると、セシウム134、セシウム137等の放射性物質が揮発し、その後冷却され固化することで、放射性物質が濃縮した焼却飛灰や溶融飛灰等が発生する。この飛灰は、熱処理前の汚染物の数十倍の放射能濃度となる。   When contaminants contaminated by radioactive materials such as cesium scattered in the nuclear accident accompanying the earthquake, such as plants such as trees and dead leaves, household waste, soil, rubble, etc., heat treatment by means such as incineration, firing, melting, etc. Radioactive substances such as cesium-134 and cesium-137 are volatilized, and then cooled and solidified to generate incinerated fly ash and molten fly ash in which the radioactive substance is concentrated. This fly ash has a radioactivity concentration several tens times that of the contaminants before the heat treatment.

そこで、このような飛灰は、放射性物質含有量に応じて適切な処理がなされている。放射性物質の含有量が8,000Bq/kg以下の飛灰は一般的な廃棄物と同様に処分され、8,000Bq/kg〜100,000Bq/kgの飛灰は放射性物質が溶出しないようにセメント固化等の対策を施された上で処分され、100,000Bq/kgを超える飛灰は中間貯蔵施設又は遮断型処分場等に保管・管理される。   Therefore, such fly ash has been appropriately treated in accordance with the radioactive substance content. Fly ash with a radioactive material content of 8,000 Bq / kg or less is disposed of in the same manner as general waste, and fly ash with a content of 8,000 Bq / kg to 100,000 Bq / kg is cemented so that the radioactive material does not elute. Fly ash exceeding 100,000 Bq / kg is stored and managed in an interim storage facility or cut-off type disposal site after being disposed of after taking measures such as solidification.

しかし、上記飛灰を一般的な廃棄物と同様に処分する埋立地の確保は容易ではなく、飛灰から放射性物質が溶出するのを防ぐには多大なコストを要し、中間貯蔵施設や遮断型処分場等に保管・管理することが可能な飛灰の量には限りがあった。また、飛灰は一般に粒径数ミクロンで嵩密度が0.2〜0.4g/cm3と小さく飛散しやすいため、ブリッジやラットホール、アーチング、閉塞、付着残留等の詰まりを発生させる虞があり、貯蔵や輸送等のハンドリングの点で改善の余地があった。 However, it is not easy to secure a landfill that disposes of the fly ash in the same way as general waste, and it requires a great deal of cost to prevent radioactive substances from being eluted from the fly ash. There was a limit to the amount of fly ash that could be stored and managed at the landfill site. In addition, fly ash is generally small in particle size of several microns and has a bulk density of 0.2 to 0.4 g / cm 3 and is easy to be scattered. There was room for improvement in handling such as storage and transportation.

そこで、埋立地の確保を容易にし、飛灰からの放射性物質の溶出を防止するためのコスト、及び飛灰の保管・管理コストを低減し、飛灰の貯蔵や輸送等のハンドリングを容易にするため、飛灰を加圧成型によって減容固化して処理することが有効である。   Therefore, it is easy to secure landfills, reduce the cost of preventing the elution of radioactive materials from fly ash, reduce the storage and management costs of fly ash, and facilitate the handling of fly ash storage and transportation. Therefore, it is effective to reduce and solidify the fly ash by pressure molding for treatment.

上記加圧成型に関する技術として、特許文献1には、焼却灰に結合剤及び水を加えて混合し、これを加圧成形して減容固化する方法が記載されている。また、特許文献2には、石炭灰に消石灰、石膏、粘土又はセメント等の固結剤及び水を添加して混合し、混練物をロール式加圧成形機で加圧成形する方法が記載されている。さらに、特許文献3には、セメント飛灰を連続ロール加圧成形法により加圧成形する方法が記載されている。   As a technique related to the pressure molding, Patent Literature 1 describes a method in which a binder and water are added to incinerated ash, mixed, and then subjected to pressure molding to reduce the volume and solidify. Patent Document 2 describes a method in which a binding agent such as slaked lime, gypsum, clay or cement and water are added to coal ash and mixed, and the kneaded material is pressure-formed by a roll-type pressure forming machine. ing. Further, Patent Literature 3 discloses a method in which cement fly ash is pressure-formed by a continuous roll pressure forming method.

特開平10−202219号公報JP-A-10-202219 特開平9−75890号公報JP-A-9-75890 特開2000−140793号公報JP 2000-140793 A

しかし、上記特許文献1及び特許文献2に記載の方法では、加圧成形の対象物である焼却灰や石炭灰に結合剤や固結剤及び水を添加する必要があるため、これらの添加装置や混合装置を要し、装置コスト及び運転コストが増加する。また、上記特許文献3に記載の方法では、嵩比重が小さい飛灰は加振脱気させてもロール間に噛み込ませるのが容易ではなく、ロール間隔を変更してもこの状況に変化はなく、成形品を得るのが困難である。   However, in the methods described in Patent Literature 1 and Patent Literature 2, since it is necessary to add a binder, a binder, and water to incineration ash or coal ash, which are objects of pressure molding, these adding devices are used. And a mixing device, which increases the cost of the device and the cost of operation. Further, according to the method described in Patent Document 3, fly ash having a low bulk specific gravity is not easy to be caught between rolls even when vibrated and degassed. And it is difficult to obtain a molded product.

そこで、本発明は、上記従来技術における問題点に鑑みてなされたものであって、低コストで効率よく放射性物質を含む飛灰を処理することを目的とする。   Therefore, the present invention has been made in view of the above-described problems in the related art, and has an object to efficiently and efficiently process fly ash containing a radioactive substance at low cost.

上記目的を達成するため、本発明は、放射性物質を含む飛灰の処理方法であって、放射性物質を含み、嵩密度が0.2〜0.4g/cm 3 飛灰を油圧プレス機によって加圧成型し、該加圧成型によって得られた成型品を解砕することを特徴とする。 To achieve the above object, the present invention provides a method of treating fly ash containing radioactive materials, including radioactive materials, fly ash bulk density of 0.2-0.4 g / cm 3 by a hydraulic press It is characterized by performing pressure molding and pulverizing a molded product obtained by the pressure molding.

本発明によれば、放射性物質を含む飛灰を油圧プレス機で加圧成型することで、結合剤、固結剤及び水を用いなくとも、嵩比重の小さい飛灰を高い減容化率で加圧成型することができる。また、油圧プレス機の成型品をそのままの形状で保管、貯蔵すると間隙が生じるが、成型品を解砕することでさらに減容化率を高めることができる。   According to the present invention, fly ash containing a radioactive substance is formed by pressure molding with a hydraulic press, so that fly ash having a low bulk specific gravity can be formed at a high volume reduction rate without using a binder, a binder and water. It can be molded under pressure. Further, when a molded product of the hydraulic press machine is stored and stored in its original shape, a gap is generated. However, by shredding the molded product, the volume reduction rate can be further increased.

また、前記成型圧力を0.5t/cm2以上2.5t/cm2以下とすることで、成型圧力を適切に維持して運転コストの上昇を抑えながら高い減容化率を得ることができる。 Further, by setting the molding pressure to 0.5 t / cm 2 or more and 2.5 t / cm 2 or less, a high volume reduction rate can be obtained while appropriately maintaining the molding pressure and suppressing an increase in operating cost. .

さらに、解砕品の50mm通過分が100質量%、10mm通過分が80質量%以上100質量%以下、5mm通過分が70質量%以上90質量%以下、1mm通過分が10質量%以上60質量%以下、0.5mm通過分が10質量%以上40質量%以下となるように前記成型品を解砕することができ、解砕品の嵩密度を高めることができる。   Furthermore, the 50 mm passage of the crushed product is 100 mass%, the 10 mm passage is 80 mass% to 100 mass%, the 5 mm passage is 70 mass% to 90 mass%, and the 1 mm passage is 10 mass% to 60 mass%. The molded product can be crushed so that the amount of passage through 0.5 mm is 10% by mass or more and 40% by mass or less, and the bulk density of the crushed product can be increased.

前記放射性物質を含む飛灰を、放射性物質を含む廃棄物を焼却、焼成、溶融等の熱処理により得られたものとすることができ、放射性物質を含む廃棄物の焼却等に伴って発生した飛灰を低コストで効率よく処理することができる。   The fly ash containing the radioactive material can be obtained by heat treatment such as incineration, burning, and melting of the radioactive waste, and the fly ash generated by the incineration of the radioactive waste and the like. Ash can be efficiently treated at low cost.

以上のように、本発明によれば、低コストで効率よく放射性物質を含む飛灰を処理することができる。   As described above, according to the present invention, fly ash containing a radioactive substance can be efficiently processed at low cost.

本発明に係る放射性物質を含む飛灰の処理方法を実施するための装置の一を示す全体構成図である。BRIEF DESCRIPTION OF THE DRAWINGS It is a whole block diagram which shows an example of the apparatus for implementing the processing method of the fly ash containing a radioactive substance which concerns on this invention. 図1に示す飛灰の処理装置の油圧プレス機の運転例を示すグラフである。It is a graph which shows the operation example of the hydraulic press of the fly ash processing apparatus shown in FIG. コンパクティングマシンの運転例を示すグラフである。It is a graph which shows the operation example of a compacting machine. 図1に示す飛灰の処理装置のハンマーミルの運転例を示すグラフである。It is a graph which shows the operation example of the hammer mill of the fly ash processing apparatus shown in FIG.

次に、本発明を実施するための形態について、図面を参照しながら詳細に説明する。   Next, embodiments for carrying out the present invention will be described in detail with reference to the drawings.

図1は本発明に係る放射性物質を含む飛灰の処理方法を実施するための装置の一を示し、この処理装置1は、放射性物質による汚染物を焼却する焼却炉等の排ガスG1から除塵する集塵機2と、集塵機2で回収した飛灰Aを加圧成型する油圧プレス機3と、油圧プレス機3による成型品Pを解砕するハンマーミル4と、ハンマーミル4による解砕品Qを保管する保管容器5とを備える。 FIG. 1 shows an example of an apparatus for carrying out a method for treating fly ash containing a radioactive substance according to the present invention. A dust collector 2, a hydraulic press machine 3 for press-molding fly ash A collected by the dust collector 2, a hammer mill 4 for crushing a molded product P by the hydraulic press machine 3, and a crushed product Q by the hammer mill 4. And a storage container 5.

集塵機2にはバグフィルタ等を用いることができ、粒径が数ミクロンで嵩密度が0.2〜0.4g/cm3と小さい飛灰Aを捕集することができるものを使用する。 A bag filter or the like can be used as the dust collector 2, and a filter capable of collecting fly ash A having a particle size of several microns and a bulk density of 0.2 to 0.4 g / cm 3 can be used.

油圧プレス機3は、供給された飛灰Aを金型内で油圧シリンダにより加圧して直径100mm程度の円柱状に成型する装置であり、汎用の油圧プレス機を用いることができる。油圧シリンダの油圧を調整して成型圧力を変化させることができる。   The hydraulic press 3 is a device that pressurizes the supplied fly ash A with a hydraulic cylinder in a mold to form a column having a diameter of about 100 mm, and a general-purpose hydraulic press can be used. The molding pressure can be changed by adjusting the hydraulic pressure of the hydraulic cylinder.

ハンマーミル4は、成型品Pを解砕するために備えられ、図示を省略するが、複数のハンマーを外周に取り付けた円筒等を回転させ、衝撃及び摩擦により成型品Pを解砕する。ハンマーミル4の代わりに、ナイフ状のハンマを高速回転させるフェザーミルや、ローターに装着したカッター刃とケーシングに装着した固定刃を備えるカッターミル等を用いることができ、これらのミルに篩を組み合わせて用いることもできる。   The hammer mill 4 is provided for pulverizing the molded product P. Although not shown, the hammer mill 4 rotates a cylinder or the like having a plurality of hammers mounted on the outer periphery, and crushes the molded product P by impact and friction. Instead of the hammer mill 4, a feather mill for rotating a knife-shaped hammer at a high speed, a cutter mill having a cutter blade mounted on a rotor and a fixed blade mounted on a casing, and the like can be used. Can also be used.

次に、上記構成を有する処理装置1の動作について、図1を参照しながら説明する。   Next, the operation of the processing apparatus 1 having the above configuration will be described with reference to FIG.

セシウム等の放射性物質による汚染物を焼却、溶融する焼却炉や溶融炉等の排ガス、例えば放射性物質を含む土壌から放射性物質を除去するロータリキルンの排ガスG1から、放射性物質を含む飛灰Aを集塵機2で捕集し、集塵後の排ガスG2を排気すると共に、回収した飛灰Aを油圧プレス機3に供給して成型し、円柱状の成型品Pを得る。   A dust collector that removes fly ash A containing radioactive substances from exhaust gas from incinerators and melting furnaces that incinerates and melts contaminants due to radioactive substances such as cesium, for example, exhaust gas G1 from a rotary kiln that removes radioactive substances from soil containing radioactive substances The exhaust gas G2 after collection and dust collection is exhausted, and the collected fly ash A is supplied to the hydraulic press machine 3 and molded to obtain a cylindrical molded product P.

図2は、嵩密度が0.2g/cm3程度の飛灰Aを油圧プレス機3で成型した際の成型圧力と成型品Pの密度との関係を示している。成型圧力が高くなるに従い成型品Pの密度も増加し、成型品Pの密度は成型前の約10倍である2.0g/cm3前後まで増加させることができる。従って、成型品Pを高密度にするために成型圧力は0.5t/cm2以上とすることが望ましく、より望ましくは1.0t/cm2以上とすることができる。成型圧力が2.5t/cm2を超えると、成型品Pの密度は2.0g/cm3程度で略々一定に推移するため、運転コストの増加を考慮して成型圧力を2.5t/cm2以下とすることが望ましく、より望ましくは2.0t/cm2以上とすることができる。
FIG. 2 shows that the bulk density is 0 . The relationship between the molding pressure when the fly ash A of about 2 g / cm 3 is molded by the hydraulic press 3 and the density of the molded product P is shown. As the molding pressure increases, the density of the molded article P also increases, and the density of the molded article P can be increased to about 2.0 g / cm 3 which is about 10 times that before molding. Therefore, the molding pressure is desirably 0.5 t / cm 2 or more, and more desirably 1.0 t / cm 2 or more, in order to increase the density of the molded article P. When the molding pressure exceeds 2.5 t / cm 2 , the density of the molded article P is approximately constant at about 2.0 g / cm 3. cm 2 or less, more preferably 2.0 t / cm 2 or more.

一方、図3は、縦スクリューにより飛灰を強制的に2個のロール間に供給し、回転する2個のロール間で、上記と同様の物性を有する飛灰Aを圧縮成型したコンパクティングマシンの運転例を示している。得られた成型品の寸法と質量から成型品の密度を算出した。同図より、ロール加圧力又はロール間隔を変化させても成型品の密度に大きな差はなく、成型品の密度は1g/cm3を超えないことが判る。 On the other hand, FIG. 3 shows a compacting machine in which fly ash is forcibly supplied between two rolls by a vertical screw, and fly ash A having the same physical properties as above is compression-molded between the two rotating rolls. The example of operation of FIG. The density of the molded product was calculated from the dimensions and mass of the obtained molded product. It can be seen from the figure that there is no significant difference in the density of the molded product even when the roll pressure or the roll interval is changed, and the density of the molded product does not exceed 1 g / cm 3 .

図2及び図3より、コンパクティングマシン等のロールプレス機よりも油圧プレス機を用いた方が高密度の成型品が得られることが判る。   From FIGS. 2 and 3, it can be seen that a molded product having a higher density can be obtained by using a hydraulic press than by using a roll press such as a compacting machine.

説明は図1に戻り、油圧プレス機3で生成した成型品Pをハンマーミル4で解砕し、解砕した解砕品Qを保管容器5で保管する。   Returning to FIG. 1, the molded product P generated by the hydraulic press 3 is crushed by the hammer mill 4 and the crushed product Q is stored in the storage container 5.

表1は、油圧プレス機3で得られた成型品Pをハンマーミル4で解砕した解砕品Qの粒度分布及び嵩密度を示す。また、図4は、解砕品Qの粒度分布をグラフ化したものである。これらより、解砕品Qの粒径ごとの割合が均等に近い場合(実施例1〜3)は、解砕品Qの嵩密度が大きいが、解砕品Qの粒径ごとの割合が粗粒側又は微粒側に偏った場合(実施例4〜9)は解砕品Qの嵩密度が小さいことが判る。   Table 1 shows the particle size distribution and bulk density of a crushed product Q obtained by crushing a molded product P obtained by the hydraulic press 3 with a hammer mill 4. FIG. 4 is a graph of the particle size distribution of the crushed product Q. From these, when the ratio of each particle size of the crushed product Q is nearly equal (Examples 1 to 3), the bulk density of the crushed product Q is large, but the ratio of each particle size of the crushed product Q is on the coarse side or the fine side. It can be seen that in the case of a bias (Examples 4 to 9), the bulk density of the crushed product Q is small.

Figure 0006670037
Figure 0006670037

以上のように、本実施の形態によれば、放射性物質を含む飛灰Aを油圧プレス機3で加圧成型することで、結合剤、固結剤及び水を用いなくとも、嵩比重の小さい飛灰Aを高い減容化率で加圧成型することができる。また、油圧プレス機3の成型品Pをそのままの形状で保管、貯蔵すると間隙が生じるが、成型品Pを解砕することでさらに減容化率を高めることができる。   As described above, according to the present embodiment, the fly ash A containing a radioactive substance is pressure-molded by the hydraulic press 3, so that the bulk specific gravity is small without using a binder, a binder and water. Fly ash A can be pressure molded at a high volume reduction rate. Further, when the molded product P of the hydraulic press 3 is stored and stored in the shape as it is, a gap is generated. However, by disintegrating the molded product P, the volume reduction rate can be further increased.

また、ハンマーミル4に用いるハンマーの種類、数もしくは回転数等を調整したり、ハンマーミルの代わりにフェザーミルやカッターミルを用いる、或いは篩を組み合わせて用いることなどで、解砕品Qの粒度分布を調整することができる。   In addition, the particle size distribution of the crushed product Q is adjusted by adjusting the type, number or rotation speed of the hammer used for the hammer mill 4, using a feather mill or a cutter mill instead of the hammer mill, or using a combination of sieves. Can be adjusted.

1 放射性物質を含む飛灰の処理装置
2 集塵機
3 油圧プレス機
4 ハンマーミル
5 保管容器
A 飛灰
G1、G2 排ガス
P 成型品
Q 解砕品
Reference Signs List 1 Processing device for fly ash containing radioactive substances 2 Dust collector 3 Hydraulic press machine 4 Hammer mill 5 Storage container A Fly ash G1, G2 Exhaust gas P Molded product Q Disintegrated product

Claims (4)

放射性物質を含み、嵩密度が0.2〜0.4g/cm 3 飛灰を油圧プレス機によって加圧成型し、
該加圧成型によって得られた成型品を解砕することを特徴とする放射性物質を含む飛灰の処理方法。
The fly ash containing a radioactive substance and having a bulk density of 0.2 to 0.4 g / cm 3 is pressure-formed by a hydraulic press machine,
A method for treating fly ash containing a radioactive substance, wherein the molded article obtained by the pressure molding is crushed.
前記成型圧力を0.5t/cm2以上2.5t/cm2以下とすることを特徴とする請求項1に記載の放射性物質を含む飛灰の処理方法。 The method for treating fly ash containing a radioactive substance according to claim 1, wherein the molding pressure is set to 0.5 t / cm 2 or more and 2.5 t / cm 2 or less. 解砕品の50mm通過分が100質量%、10mm通過分が80質量%以上100質量%以下、5mm通過分が70質量%以上90質量%以下、1mm通過分が10質量%以上60質量%以下、0.5mm通過分が10質量%以上40質量%以下となるように前記成型品を解砕することを特徴とする請求項1又は2に記載の放射性物質を含む飛灰の処理方法。   100% by mass for 50mm passage of the crushed product, 80% by mass or more and 100% by mass or less for 10mm passage, 70% by mass or more and 90% by mass or less for 5mm passage, 10% by mass or more and 60% by mass or less for 0mm passage The method for treating fly ash containing a radioactive substance according to claim 1 or 2, wherein the molded product is pulverized so that a passage amount of 0.5 mm is 10% by mass or more and 40% by mass or less. 前記放射性物質を含む飛灰は、放射性物質を含む廃棄物を熱処理して得られたものであることを特徴とする請求項1、2又は3に記載の放射性物質を含む飛灰の処理方法。   The method for treating fly ash containing a radioactive substance according to claim 1, wherein the fly ash containing a radioactive substance is obtained by heat-treating waste containing a radioactive substance.
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