JP6596208B2 - Method and apparatus for producing waste oil solidified body - Google Patents

Method and apparatus for producing waste oil solidified body Download PDF

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JP6596208B2
JP6596208B2 JP2015038877A JP2015038877A JP6596208B2 JP 6596208 B2 JP6596208 B2 JP 6596208B2 JP 2015038877 A JP2015038877 A JP 2015038877A JP 2015038877 A JP2015038877 A JP 2015038877A JP 6596208 B2 JP6596208 B2 JP 6596208B2
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尚志 川上
博文 稲川
祐二 石山
丈志 出水
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Description

本発明は、原子力発電プラントから排出される放射性廃棄物のうち、タービン油や潤滑油、EHC油などの廃油を焼却処理する処理技術に関し、廃油を固化体に成形するものである。   The present invention relates to a processing technique for incinerating waste oil such as turbine oil, lubricating oil, EHC oil, etc., from radioactive waste discharged from a nuclear power plant, and molding the waste oil into a solidified body.

原子力発電プラントでは、様々な油を使用している。一例としては、タービン油やポンプなど回転機器の潤滑油、EHC油、などがある。これらの油類は、使用後は液体状の放射性廃棄物となり、処分前にはドラム缶に充填されてプラント内で保管されている。
廃油を処理する方法として、現状は焼却処分直前に紙類に吸収させて可燃性廃棄物と共に焼却炉に投入し焼却処分している。油類は一般的には焼却可能ではあるが、液体であるため焼却炉への投入時に漏洩などの危険性があり、原子力発電プラントから排出される廃油は放射性廃棄物として取り扱われるため、漏洩すると放射能汚染域が拡大するという問題がある。また、紙類に吸収させているため、不完全燃焼を起して煤が発生し、焼却炉の後段にあるフィルタの差圧を上昇させてしまう可能性があること、またEHC油の場合にはリン化合物が飛散して焼却炉の後段にあるフィルタの差圧を上昇させてしまう可能性があることなどの理由から、処分が進まずにプラント内で保管されている現状にあり、その貯蔵量は増加の一途を辿っている。また、超臨界技術を利用することで有機物は容易に分解可能であることは言を持たないが、装置が高価であること、放射性物質を取り扱うには維持管理が容易でないことの理由から、実用化された事例はない。
Nuclear power plants use a variety of oils. Examples include lubricating oil for rotating equipment such as turbine oil and pumps, EHC oil, and the like. These oils become liquid radioactive waste after use, and are filled in drums and stored in the plant before disposal.
As a method of treating waste oil, the present situation is that it is absorbed by paper immediately before incineration and put into an incinerator together with combustible waste for incineration. Oils are generally incinerated, but because they are liquid, there is a risk of leakage when they are put into an incinerator, and waste oil discharged from nuclear power plants is handled as radioactive waste. There is a problem that the radioactive contamination area expands. In addition, because it is absorbed by paper, incomplete combustion may occur and soot may be generated, which may increase the differential pressure of the filter at the rear stage of the incinerator, and in the case of EHC oil Is currently stored in the plant without disposal, due to the possibility that phosphorus compounds may scatter and increase the differential pressure of the filter at the rear of the incinerator. The volume is steadily increasing. In addition, there is no saying that organic matter can be easily decomposed by using supercritical technology, but it is practical because it is expensive and the maintenance is not easy to handle radioactive materials. There has been no case.

また、EHC油を処理する方法としては、水酸化ナトリウム水溶液と混合して加水分解し、リン酸化合物を形成し、その後に焼却処分する方法が提唱されているが(非特許文献1)、水酸化ナトリウム水溶液は危険物であるため取り扱いが容易でないことに加え、そのような水溶液からリン酸化合物を取り出すにはフィルタープレスなどの操作が必要となる。しかし、危険物及び放射性物質を取り扱うことは困難であり実用化はされていない。   In addition, as a method for treating EHC oil, a method of mixing and hydrolyzing with an aqueous sodium hydroxide solution to form a phosphoric acid compound, and then incineration disposal has been proposed (Non-patent Document 1). Since an aqueous sodium oxide solution is a hazardous material, it is not easy to handle, and an operation such as a filter press is required to take out a phosphate compound from such an aqueous solution. However, it is difficult to handle dangerous materials and radioactive materials, and they have not been put to practical use.

一方、本出願人は、廃イオン交換樹脂を簡易に処理する方法として、可燃性結合材と廃イオン交換樹脂を混合、若しくは更にカルシウム塩を加えてブレンドして集合固化体を製造する方法を提唱した(特許文献1、2)。この製造方法は、廃イオン交換樹脂の水分を粗切りし、これに石油系ワックスなどの可燃性結合材を混合して、混練成形機にて加熱成形するものである。しかし、これらの特許で取り扱う対象は廃イオン交換樹脂であり、難燃性の固形物をワックスと共に固形化して焼却処分する方法に関するものであり、液体を対象としたものではない。   On the other hand, the present applicant proposes a method for producing an aggregate solidified body by mixing a combustible binder and a waste ion exchange resin, or further blending by adding a calcium salt as a method for easily treating the waste ion exchange resin. (Patent Documents 1 and 2). In this manufacturing method, the moisture of the waste ion exchange resin is roughly cut, and a combustible binder such as petroleum wax is mixed therewith and then heat-molded by a kneading machine. However, the object dealt with in these patents is a waste ion exchange resin, which relates to a method of solidifying a flame-retardant solid with a wax and incineration disposal, and is not intended for a liquid.

特開2005-31060号公報JP 2005-31060 特開2007-136274号公報JP 2007-136274 A

「制御油(EHC油)廃油の燃焼処理法の開発」中部電力株式会社 技術開発ニュースNo.148/2013-7“Development of Combustion Treatment Method for Control Oil (EHC Oil) Waste Oil” Chubu Electric Power Co., Ltd. Technology Development News No.148 / 2013-7

本発明の目的は、低コストで効率的、且つ安定的な焼却処理を可能にする放射性廃油集
合固化体の製造方法、及び製造装置を提供することにある。より具体的には、廃油と可燃性結合材とを撹拌し、安定して集合固化体を製造できる方法及び装置を提供することになる。なお、「集合固化体」とは、可燃性結合材をバインダとして、廃油を結合させてなる集合体を固形化したもの全般を意味する。
The objective of this invention is providing the manufacturing method and manufacturing apparatus of a radioactive waste oil aggregate solidified body which enable efficient and stable incineration processing at low cost. More specifically, a method and an apparatus that can stir waste oil and a combustible binder and stably produce an aggregated solid body are provided. The “aggregated solidified body” means all solidified aggregates formed by combining waste oil with a combustible binder as a binder.

上記課題を解決するために、本発明者らは鋭意研究した結果、廃油と可燃性結合材を加熱混合することで溶融混合し、その後冷却することで廃油と可燃性結合材が分離することなく固化できることを見出した。具体的には、廃油と、石油ワックスや植物性ワックスなどの比較的低融点で且つ常温で固体である可燃性結合材を混合し、加熱しながら撹拌し、球状、円柱状、角柱状など所望の形状に成形し、冷却することによって、既設の焼却炉に容易に装荷して、不完全燃焼による煤などを発生させることなく焼却処理できる廃油の固化体を安定的に製造できることを知見し、本発明を完成させた。   In order to solve the above-mentioned problems, the present inventors have intensively studied. As a result, the waste oil and the combustible binder are melt-mixed by heating and mixing, and then the waste oil and the combustible binder are not separated by cooling. It was found that it can be solidified. Specifically, waste oil is mixed with a combustible binder having a relatively low melting point such as petroleum wax or vegetable wax and solid at room temperature, and stirred while heating to obtain a desired shape such as spherical, cylindrical, prismatic, etc. Knowing that it is possible to stably produce a solidified body of waste oil that can be easily loaded into an existing incinerator and incinerated without generating soot due to incomplete combustion, The present invention has been completed.

また、廃油にイオンやリンなどの元素を含む場合、カルシウムを含む無機化合物を混合することで、SOX(硫黄酸化物)の発生やリン化合物によるフィルタ差圧上昇事象などを発生させることなく、廃油固化体を焼却できることを知見し、本発明を完成させた。   In addition, when the waste oil contains elements such as ions and phosphorus, the waste oil can be mixed with an inorganic compound containing calcium without causing the generation of SOX (sulfur oxide) or an increase in the filter differential pressure due to the phosphorus compound. It was found that the solidified body could be incinerated, and the present invention was completed.

本発明において処理することができる廃油としては、原子力発電施設などで発生する廃油を挙げることができる。   Examples of the waste oil that can be treated in the present invention include waste oil generated in a nuclear power generation facility.

本発明において処理することができる廃油は、原子力発電プラントから排出される廃油であれば特に限定されるものではないが、メタノールなどの低沸点物質を除き、タービン油や潤滑油、EHC油、重油、軽油、ガソリンなどを好ましく挙げることができる。   The waste oil that can be treated in the present invention is not particularly limited as long as it is waste oil discharged from a nuclear power plant, except for low-boiling substances such as methanol, turbine oil, lubricating oil, EHC oil, heavy oil. Preferable examples include diesel oil and gasoline.

本発明で用いることができる可燃性結合材は、軟化点が水の沸点以下で且つ常温で固体である物質であることが好ましく、石油ワックス、植物性ワックス、木蝋、白蝋などを好ましく挙げることができる。石油ワックスとしては、軟化温度範囲が45〜55℃のパラフィンワックス、例えばJISK2235に規定されている125P、130P、135P、140P、145P、150P、155Pなどを好ましく用いることができる。本発明において可燃性結合材を加熱成形する場合には、可燃性結合材を融点に至らない温度での軟化した状態で用いることが好ましい。融点を超えると可燃性結合材の液状化現象が起こり、収量が極端に低下するので好ましくない。可燃性結合材を粉末又は粒状で用いる場合には、155P(粒状、顆粒状、紛状)や140P(顆粒状)が好ましい。なお、パラフィンワックスについて「融点」とは、溶融した試料を既定の条件で放冷したとき、試料の温度降下速度が規定の速度以下となったときの温度である(JISK2235)。   The combustible binder that can be used in the present invention is preferably a substance that has a softening point below the boiling point of water and is solid at room temperature, and preferably includes petroleum wax, vegetable wax, wood wax, white wax, and the like. Can do. As the petroleum wax, a paraffin wax having a softening temperature range of 45 to 55 ° C., for example, 125P, 130P, 135P, 140P, 145P, 150P, 155P, etc. defined in JISK2235 can be preferably used. In the present invention, when the combustible binder is thermoformed, the combustible binder is preferably used in a softened state at a temperature that does not reach the melting point. Exceeding the melting point is not preferable because a liquefaction phenomenon of the combustible binder occurs and the yield is extremely reduced. When the combustible binder is used in powder or granular form, 155P (granular, granular, powdery) or 140P (granular) is preferred. Note that the “melting point” of paraffin wax is the temperature at which the temperature drop rate of the sample falls below a prescribed rate when the molten sample is allowed to cool under predetermined conditions (JISK2235).

可燃性結合材の含有量は、廃油100質量部に対して33質量部〜200質量部の範囲であることが好ましく、50質量部〜150質量部の範囲であることがより好ましい。この範囲であれば、廃油と可燃性結合材の混合体は、安定した形状を保つことが可能であり、その上、可燃性結合材の使用量を減少させることができるので経済的観点からも有利である。   The content of the combustible binder is preferably in the range of 33 to 200 parts by mass and more preferably in the range of 50 to 150 parts by mass with respect to 100 parts by mass of the waste oil. Within this range, the mixture of waste oil and combustible binder can maintain a stable shape, and in addition, the amount of combustible binder used can be reduced, so from an economic point of view. It is advantageous.

本発明において用いることができるカルシウムを含む無機化合物としては、硝酸カルシウム、水酸化カルシウム、酢酸カルシウム、酸化カルシウムなどの炭酸塩を除くカルシウム塩を好ましく挙げることができる。カルシウム塩は、廃EHC油中の燐酸イオンと反応して、リン酸カルシウムとして析出するため、液中へのリンの排出を抑止する。   Preferred inorganic compounds containing calcium that can be used in the present invention include calcium salts excluding carbonates such as calcium nitrate, calcium hydroxide, calcium acetate, and calcium oxide. Since the calcium salt reacts with phosphate ions in the waste EHC oil and precipitates as calcium phosphate, the discharge of phosphorus into the liquid is suppressed.

本発明において用いることができるカルシウム塩の量は、廃油100質量部に対して33質量部以上100質量部以下であることが好ましく、より好ましくは50質量部以上7
5質量部以下である。カルシウム塩を多量に用いることは、燃焼効率の向上及び燃焼残渣の低減には資するが、廃油の焼却処理の運転コストが高くなってしまうので好ましくない。
The amount of calcium salt that can be used in the present invention is preferably 33 parts by mass or more and 100 parts by mass or less, more preferably 50 parts by mass or more and 7 parts by mass or less with respect to 100 parts by mass of waste oil.
5 parts by mass or less. Use of a large amount of calcium salt contributes to improvement of combustion efficiency and reduction of combustion residues, but is not preferable because the operating cost of incineration treatment of waste oil becomes high.

したがって、本発明によれば、廃油と、可燃性結合材と、場合によってはカルシウム塩とを含む廃油の集合固化体が提供される。本発明による廃油の集合固化体の形状、寸法は、特に限定されるものではないが、原子力発電プラントなどが保有する通常の焼却設備で焼却処理可能な形状及び寸法であることが好ましい。焼却炉の投入口を通過する大きさであれば、焼却処理は可能であるが、人による運搬を考慮し20kg以下が好ましい。さらに、本発明の廃油の集合固化体は、一般的な原子力発電所が保有する焼却設備で焼却することができるような強度を有することが好ましい。集合固化体は、焼却設備に投入する際に大部分が粉砕しない程度の強度、積載時の荷重や、運搬時の重機を使った衝撃に耐える程度の強度を持つことが好ましい。   Therefore, according to this invention, the aggregate solidified body of the waste oil containing waste oil, a combustible binder, and the calcium salt depending on the case is provided. The shape and size of the aggregate and solidified body of waste oil according to the present invention are not particularly limited, but it is preferably a shape and size that can be incinerated with ordinary incineration facilities owned by a nuclear power plant or the like. An incineration process is possible if it is a size that passes through the inlet of the incinerator, but 20 kg or less is preferable in consideration of transportation by humans. Furthermore, it is preferable that the aggregated solidified body of waste oil of the present invention has such strength that it can be incinerated with an incineration facility owned by a general nuclear power plant. The aggregated solid body preferably has a strength that does not pulverize most when it is put into an incineration facility, a strength that can withstand a load during loading, and an impact using a heavy machine during transportation.

また、本発明によれば、本発明の廃油の集合固化体の製造方法を実施する製造装置が提供される。本発明の廃油集合固化体の製造装置は、廃油の貯槽と、軟化点が水の沸点以下で且つ常温で固体である石油ワックス、植物性ワックス、木蝋、白蝋から選択される可燃性結合材の貯槽と、カルシウムを含む無機化合物の貯槽と、該廃油の貯槽からの廃油、該可燃性結合材の貯槽からの可燃性結合材、及び無機化合物の貯槽からの無機化合物をそれぞれ計量する計量機構と、該計量機構によりそれぞれ計量された廃油、可燃性結合材、吸水材及び無機化合物を受け入れ、混合する混合槽と、加熱手段を具備し、混合物を加熱混練しながら所望形状の成形体に成形する撹拌混合槽と、成形体を冷却する冷却手段とを具備する。   Moreover, according to this invention, the manufacturing apparatus which enforces the manufacturing method of the aggregate solidification body of the waste oil of this invention is provided. The waste oil aggregate solidified body production apparatus of the present invention comprises a waste oil storage tank, and a combustible binder selected from petroleum wax, vegetable wax, wood wax, and white wax having a softening point below the boiling point of water and solid at room temperature , A storage tank for an inorganic compound containing calcium, a waste oil from the storage tank for the waste oil, a flammable binder from the storage tank for the flammable binder, and a measuring mechanism for measuring the inorganic compound from the storage tank for the inorganic compound And a mixing tank for receiving and mixing waste oil, combustible binder, water absorbing material and inorganic compound respectively measured by the measuring mechanism, and heating means, and forming the mixture into a desired shape while heating and kneading the mixture. And a cooling means for cooling the molded body.

本方法により得られた集合固化体は、目視確認により、廃油と可燃性結合材とが均一に混合しており、大きな割れ、引け巣がなく、既存の焼却設備に投入しても粉砕せずに必要な寸法を維持できるので、充分に焼却処理可能である。   The aggregated solid obtained by this method has been confirmed by visual confirmation that the waste oil and the combustible binder are uniformly mixed, have no large cracks or shrinkage cavities, and do not pulverize even when thrown into an existing incinerator. Therefore, it is possible to incinerate sufficiently.

また、可燃性結合材とブレンドした後の集合固化体の成形も、単に放冷するだけで行うことができるので、非常に簡便である。   In addition, since the aggregated solid body after blending with the combustible binder can be formed simply by cooling, it is very simple.

図1は、本発明の廃油集合固化体の製造装置による製造方法の工程を示す概略フロー図である。FIG. 1 is a schematic flow diagram showing the steps of a production method using a production apparatus for a waste oil aggregate solidified body of the present invention. 図2は、廃油固化体の外観写真である。FIG. 2 is an external view photograph of the waste oil solidified body.

好ましい実施形態Preferred embodiment

本方法の一実施形態として、原子力発電施設から排出される廃油を例にして、図面を参照しながら詳細に説明する。   As an embodiment of the method, waste oil discharged from a nuclear power generation facility will be described as an example with reference to the drawings.

図1は、本発明の油固化体の製造装置による製造方法の工程を示す概略フロー図である。   FIG. 1 is a schematic flow diagram showing the steps of a production method using the oil-solidified production apparatus of the present invention.

原子力発電プラントから排出される廃油に、軟化点が水の沸点以下で且つ常温で固体である石油ワックス、植物性ワックス、木蝋、白蝋から選択される粉末又は粒状の可燃性結合材を、前記廃油100質量部に対して33質量部〜200質量部の範囲の比率で添加し混合する可燃性結合材添加工程(5)と、これらの混合物を撹拌混合槽に供給して、廃油と該可燃性結合材とを可燃性結合材の軟化点以上で溶融点に至らない温度に維持しながら混練して、所望の形状の成形体に成形する混練成形工程(6)と、該成形体を冷却し固体
化する冷却固化工程(7)と、を含む。
A powder or granular combustible binder selected from petroleum wax, vegetable wax, wood wax, and white wax having a softening point below the boiling point of water and solid at room temperature to waste oil discharged from a nuclear power plant, A combustible binder addition step (5) for adding and mixing at a ratio in a range of 33 parts by mass to 200 parts by mass with respect to 100 parts by mass of waste oil, and supplying the mixture to a stirring and mixing tank to thereby produce waste oil and the combustible A kneading and molding step (6) for kneading the combustible binder while maintaining the temperature above the softening point of the combustible binder and not reaching the melting point to form a molded body of a desired shape, and cooling the molded body And cooling and solidifying step (7) for solidifying.

また、前記廃油がリン元素を含む場合、当該廃油と可燃性結合材との混合物に、カルシウムを含む無機化合物を前記廃油100質量部に対して33質量部以上100質量部以下の範囲で添加するカルシウム塩添加工程(5)をさらに含むことが好ましい。   Further, when the waste oil contains phosphorus element, an inorganic compound containing calcium is added to the mixture of the waste oil and the combustible binder in a range of 33 parts by mass or more and 100 parts by mass or less with respect to 100 parts by mass of the waste oil. It is preferable to further include a calcium salt addition step (5).

また本発明の製造装置は、図1に示すように、廃油貯槽10と、可燃性結合材貯槽20と、廃油貯槽10からの廃油を供給する定量供給機構40と、可燃性結合材貯槽20からの可燃性結合材を計量する計量機構50と、加熱手段を具備し、定量供給機構40により供給された廃油、計量機構50により計量された可燃性結合材を受け入れ、混合する撹拌混合槽60と、混合物を成形する成形装置70と、成形体を冷却する冷却手段と、を具備する。図1に示すように、さらに、無機化合物貯槽30及び無機化合物貯槽30からの無機化合物を計量して撹拌混合槽60に供給する計量機構50を具備することが好ましい。本発明の製造装置は、さらに成形装置70により成形された集合固化体を貯蔵する固化体貯槽80を具備し、該固化体貯槽80は冷却手段としても作用する構成であることが好ましい。また、固化体貯槽80は、焼却炉(図示せず)に集合固化体を投入する投入手段を具備するものでもよい。尚、廃油貯槽10から攪拌混合槽60への廃油の定量供給は、撹拌混合槽60の液位や移送流量等で供給量を監視しながらポンプ等で移送することもできる。   Further, as shown in FIG. 1, the manufacturing apparatus of the present invention includes a waste oil storage tank 10, a combustible binder storage tank 20, a quantitative supply mechanism 40 that supplies waste oil from the waste oil storage tank 10, and a combustible binder storage tank 20. A metering mechanism 50 for metering the combustible binder, and a stirring and mixing tank 60 that includes heating means, receives the waste oil supplied by the metering supply mechanism 40, and the combustible binder metered by the metering mechanism 50 and mixes them. And a molding device 70 for molding the mixture, and a cooling means for cooling the molded body. As shown in FIG. 1, it is preferable to further include an inorganic compound storage tank 30 and a metering mechanism 50 that measures the inorganic compound from the inorganic compound storage tank 30 and supplies it to the stirring and mixing tank 60. It is preferable that the manufacturing apparatus of the present invention further includes a solidified body storage tank 80 for storing the aggregate solidified body formed by the forming apparatus 70, and the solidified body storage tank 80 also functions as a cooling means. Further, the solidified body storage tank 80 may be provided with a charging means for charging the aggregated solidified body into an incinerator (not shown). In addition, the fixed supply of the waste oil from the waste oil storage tank 10 to the stirring and mixing tank 60 can be transferred by a pump or the like while monitoring the supply amount by the liquid level of the stirring and mixing tank 60 or the transfer flow rate.

以下、実施例を参照しながら本発明を説明するが、本発明はこれらに限定されるものではない。   EXAMPLES Hereinafter, although this invention is demonstrated referring an Example, this invention is not limited to these.

図1に示す製造装置を用いて、廃油を定量供給機構40にて計量して混合撹拌槽60に供給し、次に可燃性結合材(石油ワックス:日本製蝋(株)社製顆粒状ワックス:PF-155;適性軟化温度範囲45〜55℃)を計量機構50にて計量して撹拌混合槽60に添加して、両者を混合し、撹拌機で加熱しながら混練・成形して成形体を形成し、撹拌混合槽60の底部より排出して成形機70にて受け入れ、成形した後冷却することで、本発明の廃油集合固化体を製造した。本実施例において、廃油1重量部に対して、ワックス1重量部を混合した。固化体外観を図2に示す。堅牢な固化体を製造することが出来た。また、700℃の電気炉を用いて焼却したところ、完全に焼却できることを確認した。   Using the production apparatus shown in FIG. 1, waste oil is measured by the quantitative supply mechanism 40 and supplied to the mixing and stirring tank 60, and then combustible binder (petroleum wax: granular wax manufactured by Nippon Wax Co., Ltd.). : PF-155; suitable softening temperature range 45 to 55 ° C.) is measured by the measuring mechanism 50 and added to the stirring and mixing tank 60, and the two are mixed, kneaded and molded while heating with a stirrer Was formed, discharged from the bottom of the stirring and mixing tank 60, received by the molding machine 70, molded, and then cooled to produce the waste oil aggregate solidified body of the present invention. In this example, 1 part by weight of wax was mixed with 1 part by weight of waste oil. The appearance of the solidified body is shown in FIG. A robust solidified body could be produced. Moreover, when it incinerated using the 700 degreeC electric furnace, it confirmed that it could incinerate completely.

図1に示す製造装置を用いて、廃EHC油を定量供給機構40にて計量して撹拌混合槽60に供給し、次に可燃性結合材(石油ワックス:日本製蝋(株)社製顆粒状ワックス:PF-155;適性軟化温度範囲45〜55℃)及び消石灰をそれぞれ計量機構50にて計量して撹拌混合槽60に添加し、撹拌混合槽60で加熱しながら廃油とワックスの混合流体を形成し、撹拌混合槽60底部より排出して成形機70にて受け入れ、成形した後冷却することで、本発明の廃油集合固化体を製造した。本実施例において、廃油1重量部に対して、ワックス1重量部、消石灰0.5重量部を混合したものである。実施例1と同様、堅牢な固化体を製造することが出来た。また、700℃の電気炉を用いて焼却したところ、完全に焼却でき、残渣はリン酸カルシウムであることを確認した。   1, the waste EHC oil is weighed by the quantitative supply mechanism 40 and supplied to the stirring and mixing tank 60, and then combustible binder (petroleum wax: granule manufactured by Nippon Wax Co., Ltd.). Wax: PF-155; suitable softening temperature range 45-55 ° C.) and slaked lime are weighed by the measuring mechanism 50 and added to the stirring and mixing tank 60, and the mixed fluid of waste oil and wax is heated in the stirring and mixing tank 60 , Discharged from the bottom of the stirring and mixing tank 60, received by the molding machine 70, molded, and then cooled, to produce the waste oil aggregate solidified body of the present invention. In this embodiment, 1 part by weight of waste oil is mixed with 1 part by weight of wax and 0.5 part by weight of slaked lime. As in Example 1, a solidified product could be produced. Moreover, when it incinerated using the 700 degreeC electric furnace, it was able to incinerate completely and it confirmed that the residue was a calcium phosphate.

本発明によれば、廃油を既設の焼却設備で焼却処理可能な形態とした集合固化体が製造される。   According to the present invention, an aggregate solidified body in which waste oil is in a form that can be incinerated with existing incineration equipment is manufactured.

本発明により製造される集合固化体は、従来提案されている廃油の処理方法の問題点を
解決し、低コストで効率的、且つ安定的な焼却処理を可能にする。
The solidified aggregate produced according to the present invention solves the problems of the conventionally proposed methods for treating waste oil, and enables efficient and stable incineration at low cost.

特に、廃EHC油などのリンを含む廃油の場合には、カルシウム塩を添加することにより、安定的に集合固化体を製造すると共に、焼却時に発生するリン酸化合物の飛散を抑制することができ、焼却炉フィルタの差圧上昇問題を解決することができる。非特許文献1に記載の方法では、水酸化ナトリウムを添加することが必要であるが、本方法では焼却炉にて高温加熱するため水酸化ナトリウムの添加は不要となり、取り扱いが容易となり、薬剤コストも削減できる。   In particular, in the case of waste oil containing phosphorus such as waste EHC oil, by adding a calcium salt, it is possible to stably produce an aggregated solid and to suppress the scattering of phosphate compounds generated during incineration. The problem of increasing the differential pressure of the incinerator filter can be solved. In the method described in Non-Patent Document 1, it is necessary to add sodium hydroxide. However, in this method, it is not necessary to add sodium hydroxide because it is heated at a high temperature in an incinerator. Can also be reduced.

また、本発明によれば、原子力発電施設などにおいて、これまで適切な処理方法がないため液体のまま大量に保管され、今後も増加することが予測されている放射性廃棄物としての廃油を可燃性結合材と一緒に集合固化体に成形することにより、焼却処分前の長期貯蔵が可能となり、各原子力発電施設などが保有している既設の焼却設備を用いて容易に焼却処理可能にする。よって、新規な処理設備又は既設の処理設備を改良するなどの設備投資を伴わずに、大量に保管されている廃油を従来の雑固体を焼却する態様で容易に且つ効率的に、低コストで焼却処理可能とする。   In addition, according to the present invention, in nuclear power generation facilities and the like, waste oil as radioactive waste that has been stored in a large amount as a liquid and is expected to increase in the future because there is no appropriate treatment method so far is combustible. By forming into a solidified body together with a binder, it can be stored for a long time before incineration, and can be easily incinerated using existing incineration facilities owned by each nuclear power generation facility. Therefore, waste oil stored in large quantities can be easily and efficiently incinerated with conventional miscellaneous solids at low cost without capital investment such as improvement of new processing facilities or existing processing facilities. Incineration is possible.

Claims (4)

原子力発電プラントから排出される廃油に、軟化点が水の沸点以下で且つ常温で固体である石油ワックス、木蝋、白蝋から選択される粉末又は粒状の可燃性結合材を、前記廃油100質量部に対して33質量部〜200質量部の範囲の比率で添加し混合する可燃性結合材添加工程と、
これらの混合物を撹拌混合槽に供給して、可燃性結合材の軟化点以上で溶融点に至らない温度に維持しながら、廃油と該可燃性結合材とを混練して、所望の形状の成形体に成形する混練成形工程と、
該成形体を冷却し固体化する冷却固化工程と、
を含むことを特徴とする、廃油の集合固化体の製造方法。
100 parts by mass of waste oil discharged from a nuclear power plant with a powder or granular combustible binder selected from petroleum wax, wood wax and white wax having a softening point below the boiling point of water and solid at room temperature A combustible binder addition step of adding and mixing at a ratio in the range of 33 parts by mass to 200 parts by mass,
While supplying these mixtures to a stirring and mixing tank and maintaining the temperature not lower than the melting point above the softening point of the combustible binder , the waste oil and the combustible binder are kneaded to form a desired shape. A kneading and forming step for forming into a body;
A cooling and solidifying step of cooling and solidifying the molded body;
The manufacturing method of the aggregate solidified body of waste oil characterized by including this.
前記廃油は、リン元素を含み、当該廃油と可燃性結合材との混合物に、カルシウムを含む無機化合物を前記廃油100質量部に対して33質量部以上100質量部以下の範囲で添加するカルシウム塩添加工程をさらに含む、請求項1に記載の廃油の集合固化体の製造方法。   The waste oil contains a phosphorus element, and a calcium salt in which an inorganic compound containing calcium is added to a mixture of the waste oil and the combustible binder in a range of 33 parts by mass to 100 parts by mass with respect to 100 parts by mass of the waste oil. The method for producing a solidified body of waste oil according to claim 1, further comprising an adding step. 原子力発電プラントから排出される廃油の貯槽と、
軟化点が水の沸点以下で且つ常温で固体である石油ワックス、木蝋、白蝋から選択される可燃性結合材の貯槽と、
当該廃油の貯槽からの廃油を計量して供給する廃油定量供給機構、及び当該可燃性結合材の貯槽からの可燃性結合材を計量する可燃性結合材計量機構と、
当該廃油定量供給機構及び可燃性結合材計量機構にてそれぞれ計量された廃油及び可燃性結合材を受け入れ、混合する混合槽と、
加熱手段を具備し、当該混合槽からの混合物を受け入れ、可燃性結合材の軟化点以上で溶融点に至らない温度に加熱混練しながら所望形状の成形体に成形する成形装置と、
当該成形体を冷却する冷却手段と、
を具備する、廃油の集合固化体の製造装置。
A tank of waste oil discharged from the nuclear power plant,
A flammable binder reservoir selected from petroleum wax, wood wax, and white wax having a softening point below the boiling point of water and solid at room temperature;
A waste oil metering mechanism for measuring and supplying waste oil from the waste oil storage tank, and a combustible binder measurement mechanism for measuring the combustible binder from the combustible binder storage tank;
A mixing tank for receiving and mixing the waste oil and the combustible binder measured by the waste oil quantitative supply mechanism and the combustible binder measuring mechanism, respectively;
A molding apparatus comprising a heating means, receiving a mixture from the mixing tank, and molding the molded body into a desired shape while heating and kneading to a temperature not exceeding the softening point of the combustible binder and reaching the melting point ;
Cooling means for cooling the molded body;
An apparatus for producing a solidified body of waste oil, comprising:
前記廃油はリン元素を含み、
カルシウムを含む無機化合物の貯槽と、
当該無機化合物の貯槽からの無機化合物を計量する無機化合物計量機構と、をさらに具備し、
前記混合槽は、前記廃油及び可燃性結合材に加えて当該無機化合物計量機構にて計量された無機化合物を受け入れる、請求項3に記載の廃油の集合固化体の製造装置。
The waste oil contains phosphorus element,
A reservoir of inorganic compounds containing calcium;
An inorganic compound measuring mechanism for measuring an inorganic compound from the inorganic compound storage tank;
The said mixing tank receives the inorganic compound measured by the said inorganic compound measuring mechanism in addition to the said waste oil and a combustible binder, The manufacturing apparatus of the aggregate solidified body of the waste oil of Claim 3.
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