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JPH0640159B2 - Method for solidifying radioactive waste - Google Patents
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JPH0640159B2 - Method for solidifying radioactive waste - Google Patents

Method for solidifying radioactive waste

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Publication number
JPH0640159B2
JPH0640159B2 JP60253803A JP25380385A JPH0640159B2 JP H0640159 B2 JPH0640159 B2 JP H0640159B2 JP 60253803 A JP60253803 A JP 60253803A JP 25380385 A JP25380385 A JP 25380385A JP H0640159 B2 JPH0640159 B2 JP H0640159B2
Authority
JP
Japan
Prior art keywords
solid waste
radioactive
waste
exchange resin
treatment
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP60253803A
Other languages
Japanese (ja)
Other versions
JPS62114692A (en
Inventor
賢三 左右田
明俊 横田
三郎 城多
伊彦 内田
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
JGC Corp
Original Assignee
JGC Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by JGC Corp filed Critical JGC Corp
Priority to JP60253803A priority Critical patent/JPH0640159B2/en
Priority to US06/814,101 priority patent/US4772430A/en
Priority to GB8600435A priority patent/GB2171638A/en
Priority to ES551407A priority patent/ES8700980A1/en
Priority to DE19863600537 priority patent/DE3600537A1/en
Priority to FR868600292A priority patent/FR2575943B1/en
Priority to IT1905986A priority patent/IT1204431B/en
Publication of JPS62114692A publication Critical patent/JPS62114692A/en
Publication of JPH0640159B2 publication Critical patent/JPH0640159B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は放射性廃棄物の固形化処理方法に関し、詳しく
は原子力発電所等で発生する放射性の使用済みイオン交
換樹脂と固体廃棄物とを安定な固形物として固定化し、
一時的貯蔵あるいは最終処分に便利な形態に変換し、放
射能による侵出を防止し得る放射性廃棄物の固形化処理
方法に関するものである。
TECHNICAL FIELD The present invention relates to a method for solidifying radioactive waste, and more specifically, it stabilizes radioactive used ion exchange resin and solid waste generated in a nuclear power plant or the like. Immobilized as a solid material,
The present invention relates to a method for solidifying radioactive waste, which can be converted into a form convenient for temporary storage or final disposal and can prevent leaching due to radioactivity.

[従来の技術および発明が解決しようとする課題] 今日、原子力発電所等の原子力施設で復水浄化あるいは
廃水処理等の目的でイオン交換樹脂が用いられている。
このイオン交換樹脂を廃棄処理する際には、放射能に汚
染されているため、その廃棄処理する方法が問題とな
る。
[Problems to be Solved by Conventional Techniques and Inventions] Today, ion exchange resins are used in nuclear facilities such as nuclear power plants for the purpose of condensate purification or wastewater treatment.
When this ion-exchange resin is disposed of, since it is contaminated with radioactivity, the method of disposal is a problem.

例えば、使用済みイオン交換樹脂のあるものは放射能が
101〜10-2μCi/ccと高く、また長半減期核種のCs
ゃSrを含んでいるため、より安全な形での長期貯蔵の
必要上、その処理は焼却あるいは湿式分解等の分解減容
か、もしくはセメント固化、アスファルト固化またはプ
ラスチック固化等の直接固化処理する方法が開発研究さ
れ、その一部は実用化されている。しかしながら、前者
の分解減容のうち焼却による方法は高温で処理するため
イオン交換樹脂のうちカチオン樹脂の交換基が分解し、
SOxガスを発生し、その発生した排ガスの処理設備の
材質問題や、SOxガスの回収等に問題が有る。また、
湿式分解にあってはSO4 2-が分解液中に残存するので
苛性ソーダ等で中和してから蒸発濃縮させる等の後処理
が必要であると共に分解剤が高価である等、経済性に問
題がある。後者の直接固形化処理方法においては減容性
が悪かったり、処理設備が高価である等の問題がある。
For example, some of the used ion exchange resins have
High as 10 1 -10 -2 μCi / cc and Cs of long half-life nuclide
Since it contains Sr and Sr, long-term storage in a safer form is necessary, and therefore the treatment is carried out by decomposition or volume reduction such as incineration or wet decomposition, or by direct solidification treatment such as cement solidification, asphalt solidification or plastic solidification. Has been developed and researched, and part of it has been put to practical use. However, in the former method of decomposition and volume reduction by incineration, the exchange group of the cation resin of the ion exchange resin decomposes because it is processed at high temperature,
There is a problem in that SOx gas is generated, the material of the treatment equipment for the generated exhaust gas is a problem, and the SOx gas is recovered. Also,
In wet decomposition, SO 4 2- remains in the decomposition liquid, so post-treatment such as neutralization with caustic soda and evaporative concentration is necessary, and the decomposition agent is expensive, which is a problem in economic efficiency. There is. The latter direct solidification treatment method has problems such as poor volume reduction and expensive treatment equipment.

一方、放射能の強度が極低レベルでほとんど無害なイオ
ン交換樹脂であっても、米国等では放射性物質というこ
とで高健全性容器(HIC)に収納して処分しなければ
ならない。しかし、このHICは高価であるため放射能
の強度が中レベル以下のイオン交換樹脂処理にはコスト
的に適用しづらい等の問題があるため、一般にはタンク
貯蔵を行ない、実際上処理を行なっている所は少ない。
On the other hand, even an ion-exchange resin, which has an extremely low level of radioactivity and is almost harmless, must be disposed of in a highly sound container (HIC) because it is a radioactive substance in the United States. However, since this HIC is expensive, there is a problem in that it is difficult to apply costly to the ion exchange resin treatment with a medium or lower level of radioactivity, so that it is generally stored in a tank and actually treated. There are few places.

また、原子力施設から発生する放射性固体廃棄物の処理
においても、焼却処理等の一般固体廃棄物による処理を
そのまま適用することが困難であるため種々の課題を有
している。
Further, in the treatment of radioactive solid waste generated from a nuclear facility, it is difficult to directly apply the treatment using general solid waste such as incineration treatment, so that there are various problems.

本発明の目的は、原子力発電所等で生ずる放射性の使用
済みイオン交換樹脂および固体廃棄物を新たな2次廃棄
物を発生させることなく、固形化する、経済性に優れ、
かつ安定な固形化物が得られる放射性固体廃棄物の固形
化処理方法を提供することにある。
An object of the present invention is to solidify radioactive used ion-exchange resin and solid waste generated in a nuclear power plant etc. without generating new secondary waste, which is highly economical.
Another object of the present invention is to provide a method for solidifying radioactive solid waste, which can obtain a stable solidified product.

[課題を解決するための手段] 本発明は、上述のような課題に対応して検討した結果完
成したものであり、使用済み放射性イオン交換樹脂と放
射性固体廃棄物の混合物を細断ないしは破砕、粉砕して
設定サイズに処理した後、圧縮スクリューを有する押出
成形機にて、摩擦熱により生じる100〜190℃の温度条件
で圧縮し、該放射性固体廃棄物中に含まれる熱可塑性樹
脂を固形化材の一部または全部として固形化することを
特徴とする放射性廃棄物の固形化処理方法である。
[Means for Solving the Problems] The present invention has been completed as a result of an examination in response to the above problems, and shreds or crushes a mixture of a used radioactive ion exchange resin and a radioactive solid waste, After crushing and processing to a set size, it is compressed in an extruder having a compression screw at a temperature condition of 100 to 190 ° C generated by frictional heat to solidify the thermoplastic resin contained in the radioactive solid waste. A method for solidifying radioactive waste, which comprises solidifying a part or all of the material.

すなわち前述の先行技術の問題を以下の処理方針で解決
した。先ず、SOxガスについては処理を低温で行ない
SOxガスの発生を防止した。次に直接固化処理におけ
る減容できないという課題に対しては、放射性固体廃棄
物(以下、単に固体廃棄物という)に含まれる熱可塑性
樹脂および必要によって一部を外部から導入した熱可塑
性樹脂を固形化材として混合圧縮し、総合的にみて減容
化させることにより解消させた。放射能を含んでいると
いう課題については固形化材で閉じ込めることにより、
その侵出は防げる。さらに、使用済み放射性イオン交換
樹脂(以下、単に使用済みイオン交換樹脂という)中の
自由水は、本発明により得られた固形化物中には処理過
程において蒸発してほとんどがなくなる。そのため、高
価なHICを使用しなくても放射能の侵出が防止可能で
通常のドラム缶による貯蔵が可能となる。
That is, the problem of the above-mentioned prior art was solved by the following processing policy. First, the SOx gas was treated at a low temperature to prevent the SOx gas from being generated. Next, with respect to the problem that the volume cannot be reduced in the direct solidification treatment, the thermoplastic resin contained in the radioactive solid waste (hereinafter simply referred to as solid waste) and the thermoplastic resin partially introduced from the outside as necessary are solidified. It was solved by mixing and compressing as a chemical agent and reducing the volume as a whole. Regarding the problem of containing radioactivity, by confining it with solidified material,
The exudation can be prevented. Furthermore, the free water in the used radioactive ion exchange resin (hereinafter simply referred to as the used ion exchange resin) is almost completely evaporated in the treatment process in the solidified product obtained by the present invention. Therefore, it is possible to prevent radioactivity from leaching out without using an expensive HIC, and it is possible to store it in an ordinary drum.

具体的には、上記の固形化材とは廃棄物として発生する
固体廃棄物を使い、この内に含まれるポリエチレン(P
E)やポリ塩化ビニル(PVC)等の熱可塑性樹脂を固
形化させる。また、PEやPVC等の熱可塑性樹脂が溶
融する温度範囲内である100〜190℃で、使用済みイオン
交換樹脂および固体廃棄物の混合物を撹拌圧縮すること
により、SOxガスは発生せず(SOxガスが発生する
温度は200〜350℃である)、またイオン交換樹脂中の水
分が蒸発し成形物の自由水も無くなるため、HICを使
用する必要が無くなるわけである。
Specifically, the solidifying material is solid waste generated as waste, and polyethylene (P
E) or a thermoplastic resin such as polyvinyl chloride (PVC) is solidified. Further, by stirring and compressing the mixture of the used ion exchange resin and the solid waste at 100 to 190 ° C., which is the temperature range in which the thermoplastic resin such as PE or PVC is melted, SOx gas is not generated (SOx gas). The temperature at which the gas is generated is 200 to 350 ° C.), and since the water in the ion exchange resin evaporates and the free water of the molded product also disappears, there is no need to use HIC.

本発明において、熱可塑性樹脂を含む固体廃棄物は細か
く細断ないしは破砕されている方が好ましい。これは、
固形化処理が押出成形によって行なわれるので、押出機
のダイス口径に対応できるような程度の大きさに細分化
することが必要なためであり、細断ないしは破砕後に、
さらに粉砕することが望ましい。
In the present invention, the solid waste containing the thermoplastic resin is preferably finely chopped or crushed. this is,
Since the solidification treatment is carried out by extrusion molding, it is necessary to subdivide into a size that can correspond to the die diameter of the extruder, and after shredding or crushing,
Further crushing is desirable.

また、使用済みイオン交換樹脂は水切り程度の脱水がさ
れていることが好ましい。
Further, the used ion exchange resin is preferably dehydrated to the extent of draining.

なお、始めから固体廃棄物中に使用済みイオン交換樹脂
が含まれていても本発明により固形化処理可能であるこ
とはいうまでもない。
Needless to say, the solid waste can be solidified by the present invention even if the solid waste contains the used ion exchange resin.

本発明においては、固形化材として前述のように熱可塑
性樹脂を使用するが、この種類、性状については何ら問
われず、固形化する際に必要とする程度の成形性が備わ
っていれば良い。この熱可塑性樹脂は、通常、固体廃棄
物中に含まれるPE、PVC等が利用されるが、一部を
外部より導入して用いてもよい。外部から導入する際も
固形化処理することから、新品である必要はなく、再生
品でもあるいは一般に排出されている熱可塑性プラスチ
ック系廃棄物を使用しても良い。
In the present invention, the thermoplastic resin is used as the solidifying material as described above, but the kind and property thereof are not limited, and it is sufficient that the resin has moldability to the extent required for solidification. As the thermoplastic resin, PE, PVC or the like contained in solid waste is usually used, but a part thereof may be introduced from the outside and used. Since it is solidified even when it is introduced from the outside, it does not need to be a new product, and a recycled product or a generally discharged thermoplastic waste may be used.

上記のごとく熱可塑性樹脂であれば、どのような樹脂で
も使用できるが、100〜190℃程度の温度で軟化ないしは
融解するものが最も利用しやすい。また、固形化するに
際して、熱可塑性樹脂の含有量は10重量%以上の範囲に
あることが必要であり、また水分も少ない方が良いが30
重量%までは固形化可能である。なお、この範囲の熱可
塑性樹脂の含有量は、外部から導入した量も含むもので
ある。
As described above, any resin can be used as long as it is a thermoplastic resin, but a resin that softens or melts at a temperature of about 100 to 190 ° C. is most easily used. Further, when solidified, the content of the thermoplastic resin needs to be in the range of 10% by weight or more, and it is better that the water content is less than 30%.
Up to wt% can be solidified. The content of the thermoplastic resin within this range includes the amount introduced from the outside.

本発明においては、使用済みイオン交換樹脂等の固形化
は、押出成形機によりなされるが、機内壁と圧縮スクリ
ューとの間隙で固体廃棄物の摺動により摩擦熱が発生す
るため、外部よりの加熱を要しないか、またはダイス部
分の補助加熱で固形化が行なわれる。
In the present invention, the solidification of the used ion-exchange resin or the like is performed by an extruder, but friction heat is generated due to sliding of solid waste in the gap between the inner wall of the machine and the compression screw. No heating is required, or solidification is performed by auxiliary heating of the die part.

[作用] 本発明をさらに個別的に説明する。第1図は本発明によ
る放射性廃棄物の固形化処理方法の工程を示すブロック
図である。
[Operation] The present invention will be described further individually. FIG. 1 is a block diagram showing steps of a method for solidifying radioactive waste according to the present invention.

例えば原子力発電所などから排出された低レベル放射性
の使用済みイオン交換樹脂および固体廃棄物をホッパか
ら細断機または破砕機に導入し、粗砕し、場合によって
更に粉砕機で粉砕した後、混合定量供給装置に連絡する
貯槽に貯留し、次いで押出成形機で固形化する。熱可塑
性樹脂の一部を外部から供給する場合には、ホッパに供
給する。この押出成形機において、使用済みイオン交換
樹脂および固体廃棄物は混練を受けたのち一定の形、例
えばロッド状、ストランド状あるいはこれを切断したペ
レット状に成形して、ドラム缶等の貯蔵容器に貯蔵され
る。さらに、より減容性の高い焼却溶融処理を行なう場
合にも、これらの形状になっているため取扱いが容易で
あるという利点もある。また、使用済みイオン交換樹脂
は粒状または粉状であるので直接混合定量供給装置に供
給してもよい。
For example, used ion-exchange resin and solid waste of low-level radiation discharged from a nuclear power plant, etc. are introduced into a shredder or crusher from a hopper, coarsely crushed, and optionally further crushed by a crusher, and then mixed. It is stored in a storage tank which communicates with a constant quantity supply device, and then solidified by an extruder. When a part of the thermoplastic resin is supplied from the outside, it is supplied to the hopper. In this extruder, the used ion-exchange resin and solid waste are kneaded and then molded into a certain shape, for example, rod-shaped, strand-shaped or cut pellet-shaped, and stored in a storage container such as a drum can. To be done. Further, even when performing incineration and melting treatment with a higher volume reduction property, there is an advantage that handling is easy because of these shapes. Further, since the used ion exchange resin is granular or powdery, it may be directly supplied to the mixing / quantitative supply device.

この固形化処理においては、押出成形機の圧縮比など適
当な選択することにより、摩擦発熱で熱可塑性樹脂の軟
化ないしは融解を起こさせるものであり、運転開始当初
を除き、特に押出成形機のダイス部近傍への外部から熱
の供給を行なわないで済み、あるいは補助加熱程度で良
く省エネルギーの見地からも好ましい。また、この押出
成形機での固形化はおよそ100〜190℃の温度で行なわれ
る。
In this solidification treatment, the thermoplastic resin is softened or melted by friction heat generation by appropriately selecting the compression ratio of the extruder, etc. It is not necessary to supply heat to the vicinity of the part from the outside, or only auxiliary heating is sufficient, which is preferable from the viewpoint of energy saving. The solidification in this extruder is carried out at a temperature of about 100 to 190 ° C.

このような処理を行なうことにより、使用済みイオン交
換樹脂および固体廃棄物は、いわばプラスチックに埋込
まれた固形化物となるので極めてコンパクトでしかも得
られた固形化物の外表面が融解プラスチックに密に覆わ
れているので水中に浸漬しても安定な物体となり減容効
果は格段に向上させ得る。また、通常は熱可塑性樹脂を
外部から導入せずに、固体廃棄物中に含まれるもののみ
でまかなうことができるので、減容効果が相剰的に発揮
されることになる。
By carrying out such a treatment, the used ion-exchange resin and the solid waste are, so to speak, a solidified product embedded in the plastic, so that it is extremely compact, and the outer surface of the solidified product is closely packed in the molten plastic. Since it is covered, it becomes a stable object even when immersed in water, and the volume reduction effect can be greatly improved. Moreover, since it is usually possible to use only the resin contained in the solid waste without introducing the thermoplastic resin from the outside, the volume-reducing effect is additionally exerted.

[実施例] 以下、実施例および参考例に基づき本発明を具体的に説
明する。
[Examples] Hereinafter, the present invention will be specifically described based on Examples and Reference Examples.

実施例1〜4および参考例 第1表は、水切り脱水した使用済みイオン交換樹脂(水
分42wt%)に模擬廃棄物の混合率を変えて混合し、固形
化処理した場合を示す。実施例1〜4に見られるように
投入廃棄物50リットル前後に対して、固形化処理後のペ
レットの体積が10リットル前後と約1/5の減容になって
いることが分かる。
Examples 1 to 4 and Reference Example Table 1 shows the case where the used ion-exchange resin (water content 42 wt%) that had been drained and dehydrated was mixed by changing the mixing ratio of the simulated waste and solidified. As can be seen from Examples 1 to 4, the volume of pellets after the solidification treatment is about 10 liters, which is about 1/5 of the volume of the input wastes of about 50 liters.

第1表に示した投入廃棄物の固形化処理はこれらの混合
物をカッターミルで4mm角以下に粉砕したのち、第2図
に示した如き押出成形機に供給して行なった。第2図
中、1はホッパ、2は定量供給機、3は圧縮スクリュ
ー、4はダイスである。なお、この圧縮スクリュー3は
先端部分(ダイス4に近い方)の羽根がカッター状にな
っており、ここで破砕、粉砕された混合物の混合が充分
に行なわれる。
The solidification treatment of the input waste shown in Table 1 was carried out by crushing the mixture into 4 mm square or less with a cutter mill and then supplying the mixture to an extruder as shown in FIG. In FIG. 2, 1 is a hopper, 2 is a constant quantity feeder, 3 is a compression screw, and 4 is a die. The blade of the compression screw 3 at the tip (closer to the die 4) has a cutter shape, and the crushed and crushed mixture is sufficiently mixed therein.

ホッパ1から定量供給機2を経て回転数150rpmの圧縮ス
クリュー3に供給された模擬廃棄物は、圧縮混練を受け
ながら、この押出成形機バレル面における発熱により、
熱可塑性樹脂が軟化ないしは融解状態となり圧縮スクリ
ュー3の開放端側に向い、ここで回転しているカッター
状部の剪断力を受けたのちダイス4を通って外部に連続
的に20本、12mm径のロッド状またはストランド状に送り
出されてきたので適当な長さに達した時、束ねて引きち
ぎった。これらを放冷したところ、実施例1〜4は参考
例と同様に互に融着することなく良好な固形化物が得ら
れた。
The simulated waste supplied from the hopper 1 to the compression screw 3 having a rotation speed of 150 rpm through the constant quantity feeder 2 is compressed and kneaded, and heat generated on the barrel surface of the extruder causes
The thermoplastic resin is in a softened or melted state and faces the open end of the compression screw 3, where it is subjected to the shearing force of the rotating cutter-like part, and then continuously passes through the die 4 to the outside to obtain 20 pieces with a diameter of 12 mm. Since it was sent out in the form of rod or strand, when it reached an appropriate length, it was bundled and torn off. When these were allowed to cool, in Examples 1 to 4, good solidified products were obtained without mutual fusion, as in Reference Example.

このようにして得られた固形化物の水分はすべて2wt%
以下であった。また、樹脂混合率が増加するに従い、固
形化物の表面は良好となった。固形化物を室温水中に、
3カ月間浸漬したがもとの形状、重量と同じであり、耐水
性が良好なことが分かった。
The water content of the solid thus obtained is 2 wt%
It was below. Moreover, the surface of the solidified product became better as the resin mixing ratio increased. The solidified product in room temperature water,
After soaking for 3 months, it was found that the shape and weight were the same and the water resistance was good.

第3図の装置は、本発明の固形化を行なうのに適した装
置の他の一例であり、固形化処理する混合物をカッター
ミルで4kg角以下に粉砕した後、回転数16rpmで150mmφ
の2軸パドルスクリュー型混合定量供給機により押出成
形機に供給し、8mmφ×62個の孔のあるダイス(130mmφ
×35mm)部に押出成形する装置である。
The apparatus shown in FIG. 3 is another example of the apparatus suitable for carrying out the solidification of the present invention. After the mixture to be solidified is crushed into 4 kg square or less by a cutter mill, the rotation speed is 16 rpm and the diameter is 150 mmφ.
It is supplied to the extrusion molding machine by the twin-screw paddle screw type constant-quantity feeder, and the die with 8mmφ × 62 holes (130mmφ
It is a device that extrudes into a 35 mm section.

[発明の効果] 以上説明したごとく、本発明に従えば、処理に困難性が
伴なう放射性の使用済みイオン交換樹脂および固体廃棄
物を実質的に加熱を必要とせずに併せて処理が可能であ
り、得られる固形化物の物性は良好で、プラスチックで
固化したものおよびセメントで固化した場合と同様に放
射能等の侵出は少い。
[Effects of the Invention] As described above, according to the present invention, radioactive used ion-exchange resin and solid waste, which are difficult to process, can be processed together without substantially heating. The physical properties of the obtained solidified product are good, and the leaching of radioactivity and the like is small as in the case of solidified with plastic and solidified with cement.

また、この放射性廃棄物の処理処分費はHIC、分解後
処理、直接固化したものと比較して2倍から10倍以上も
経済的でかつ簡易に放射性の使用済みイオン交換樹脂お
よび固体廃棄物を減容化処理することが可能となる。こ
れは初期設備費、運転費、分解剤、固形化材費等が本発
明の方法においては極めて低いためであり、特に固形化
材の大部分を放射性固体廃棄物中に含まれる熱可塑性樹
脂でまかなうため、経済性の向上に著しく寄与するもの
である。
In addition, the treatment and disposal cost of this radioactive waste is 2 to 10 times more than that of HIC, post-decomposition treatment, and direct solidification. It is possible to reduce the volume. This is because the initial equipment cost, operating cost, decomposing agent, solidifying material cost, etc. are extremely low in the method of the present invention. Especially, most of the solidifying material is a thermoplastic resin contained in radioactive solid waste. Since it is covered, it will significantly contribute to the improvement of economic efficiency.

【図面の簡単な説明】[Brief description of drawings]

第1図は本発明の工程を示すフローシート、 第2図は一具体例として使用した押出成形装置の側面
図、 第3図は他の具体例である押出成形装置の側面図であ
る。 1……ホッパ、2……定量供給機、 3……圧縮スクリュー、4……ダイス、 5……2軸パドルスクリュー型混合定量供給機。
FIG. 1 is a flow sheet showing the steps of the present invention, FIG. 2 is a side view of an extrusion molding apparatus used as one specific example, and FIG. 3 is a side view of an extrusion molding apparatus which is another specific example. 1 ... Hopper, 2 ... Constant quantity feeder, 3 ... Compression screw, 4 ... Die, 5 ... Twin screw paddle screw type mixed constant quantity feeder.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 城多 三郎 東京都文京区千駄木4−2―20 (72)発明者 内田 伊彦 神奈川県横須賀市粟田1−20―1 (56)参考文献 特開 昭58−82200(JP,A) 特開 昭52−13100(JP,A) 特開 昭50−90900(JP,A) 特開 昭57−48700(JP,A) 特開 昭53−40200(JP,A) ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Inventor Saburo Jota 4-2-20 Sendagi, Bunkyo-ku, Tokyo (72) Inventor Ihiko Uchida 1-20-1 Awata, Yokosuka City, Kanagawa Prefecture (56) References JP-A-58-82200 (JP, A) JP-A-52-13100 (JP, A) JP-A-50-90900 (JP, A) JP-A-57-48700 (JP, A) JP-A-53-40200 (JP , A)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】使用済み放射性イオン交換樹脂と放射性固
体廃棄物の混合物を細断ないしは破砕、粉砕して設定サ
イズに処理した後、圧縮スクリューを有する押出成形機
にて、摩擦熱によって生じる100〜190℃の温度条件で圧
縮し、該放射性固体廃棄物中に含まれる熱可塑性樹脂を
固形化材の一部または全部として固形化することを特徴
とする放射性廃棄物の固形化処理方法。
1. A mixture of a used radioactive ion exchange resin and a radioactive solid waste is shredded or crushed, crushed and processed to a set size, and then 100 to 100 to be generated by friction heat in an extruder having a compression screw. A method for solidifying radioactive waste, comprising compressing under a temperature condition of 190 ° C. to solidify the thermoplastic resin contained in the radioactive solid waste as a part or all of a solidifying material.
JP60253803A 1985-01-11 1985-11-14 Method for solidifying radioactive waste Expired - Lifetime JPH0640159B2 (en)

Priority Applications (7)

Application Number Priority Date Filing Date Title
JP60253803A JPH0640159B2 (en) 1985-11-14 1985-11-14 Method for solidifying radioactive waste
US06/814,101 US4772430A (en) 1985-01-11 1985-12-27 Process for compacting and solidifying solid waste materials, apparatus for carrying out the process and overall system for disposal of such waste materials
GB8600435A GB2171638A (en) 1985-01-11 1986-01-09 Process and apparatus for compacting and solidifying solid waste materials, and overall system for disposal of such waste materials
ES551407A ES8700980A1 (en) 1985-01-11 1986-01-10 Process for compacting and solidifying solid waste materials, apparatus for carrying out the process and overall system for disposal of such waste materials
DE19863600537 DE3600537A1 (en) 1985-01-11 1986-01-10 METHOD FOR COMPRESSING AND STRENGTHENING SOLID WASTE MATERIALS, DEVICE FOR CARRYING OUT THE METHOD AND OVERALL SYSTEM FOR FASTENING SUCH WASTE MATERIALS
FR868600292A FR2575943B1 (en) 1985-01-11 1986-01-10 PROCESS FOR COMPACTING AND SOLIDIFYING SOLID WASTE, APPARATUS FOR IMPLEMENTING SAID WASTE
IT1905986A IT1204431B (en) 1985-01-11 1986-01-10 PROCESS FOR COMPACTING AND SOLIDIFYING SOLID WASTE MATERIALS, EQUIPMENT FOR CONDUCTING THE PROCESS, AND COMPLEX OF THE PLANT FOR THE ELIMENATION OF SUCH WASTE MATERIALS

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60253803A JPH0640159B2 (en) 1985-11-14 1985-11-14 Method for solidifying radioactive waste

Publications (2)

Publication Number Publication Date
JPS62114692A JPS62114692A (en) 1987-05-26
JPH0640159B2 true JPH0640159B2 (en) 1994-05-25

Family

ID=17256366

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60253803A Expired - Lifetime JPH0640159B2 (en) 1985-01-11 1985-11-14 Method for solidifying radioactive waste

Country Status (1)

Country Link
JP (1) JPH0640159B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101155177B1 (en) * 2003-03-27 2012-06-13 테르모셀렉트 악티엔게젤샤프트 Waste treatment in the form of dust and / or particles

Family Cites Families (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE2361732C2 (en) * 1973-12-12 1982-09-09 Kernforschungszentrum Karlsruhe Gmbh, 7500 Karlsruhe Screw shaft extruder for fixing radioactive and / or toxic waste materials
DE2531584A1 (en) * 1975-07-15 1977-01-20 Kraftwerk Union Ag PROCEDURE FOR DISPOSAL OF RADIANT PLASTIC WASTE AND EQUIPMENT FOR IT
JPS6022996B2 (en) * 1977-08-02 1985-06-05 オルガノ株式会社 Method for solidifying waste containing anion exchange resin
JPS57136984A (en) * 1981-02-20 1982-08-24 Hitachi Ltd Method for solidification of waste
DE3142356A1 (en) * 1981-10-26 1983-05-11 Alkem Gmbh, 6450 Hanau "METHOD FOR FINAL CONDITIONING RADIOACTIVE AND / OR TOXIC WASTE"

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101155177B1 (en) * 2003-03-27 2012-06-13 테르모셀렉트 악티엔게젤샤프트 Waste treatment in the form of dust and / or particles

Also Published As

Publication number Publication date
JPS62114692A (en) 1987-05-26

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