JPS5931039B2 - Acid digestion treatment method using a tantalum acid digestion pot - Google Patents
Acid digestion treatment method using a tantalum acid digestion potInfo
- Publication number
- JPS5931039B2 JPS5931039B2 JP55065789A JP6578980A JPS5931039B2 JP S5931039 B2 JPS5931039 B2 JP S5931039B2 JP 55065789 A JP55065789 A JP 55065789A JP 6578980 A JP6578980 A JP 6578980A JP S5931039 B2 JPS5931039 B2 JP S5931039B2
- Authority
- JP
- Japan
- Prior art keywords
- acid
- acid digestion
- tantalum
- pot
- sulfuric acid
- 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
Links
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/62—Plastics recycling; Rubber recycling
Landscapes
- Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)
- Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
- Processing Of Solid Wastes (AREA)
Description
【発明の詳細な説明】
本発明はタンタル製酸消化釜による廃棄有機高分子物質
の酸消化処理方法に関し、特に酸消化処理工程で生ずる
タンタル製酸消化釜の腐食及び水素吸収脆化を防止する
方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for acid digestion treatment of waste organic polymer materials using a tantalum acid digestion pot, and in particular, to prevent corrosion and hydrogen absorption embrittlement of the tantalum acid digestion pot that occurs during the acid digestion process. It is about the method.
本発明で酸消化処理の対象となる廃棄有機高分子物質と
しては、天然もしくは合成の各種ゴム製品、綿・毛・ナ
イロン・ビニロン等の天然もしくは合成の各種繊維製品
、ポリエチレン・ポリプロピレン等の合成樹脂フィルム
やシート、更にはその他の熱可塑性又は熱硬化性樹脂製
の各種成形品等のあらゆる廃棄有機高分子物質(以下単
に有機物という)を包含するが、以下では放射能汚染を
受けた有機物製品の処理を例にとつて説明する。核燃料
を取扱う施設、或はその他放射性同位元素を扱う施設で
は、人体を保護する為に種々の機材や調度品が用いられ
る。塩化ビニル、塩化ビニリデン、クロロプレン等の含
塩素ビニル系モノマーを(共)重合させたゴム製品はそ
の代表例であるが、放射能汚染を受けたこれらの有機物
製品を処理する技術としては、これらを減容安定化し、
コンパクトに固めて貯蔵する方法がある。減容安定化の
為に採用される手段としては、高温高濃度の硫酸浴中に
上記有機物を投入して酸消化させる方法が検討されてい
る。The waste organic polymer substances to be subjected to acid digestion treatment in the present invention include various natural or synthetic rubber products, various natural or synthetic fiber products such as cotton, wool, nylon, and vinylon, and synthetic resins such as polyethylene and polypropylene. It includes all kinds of waste organic polymer materials (hereinafter simply referred to as organic materials) such as films, sheets, and various other thermoplastic or thermosetting resin molded products. The processing will be explained using an example. Facilities that handle nuclear fuel or other radioactive isotopes use various equipment and furnishings to protect the human body. Rubber products made by (co)polymerizing chlorine-containing vinyl monomers such as vinyl chloride, vinylidene chloride, and chloroprene are typical examples. Volume reduction and stabilization
There is a way to compact and store it. As a means to be adopted for volume reduction and stabilization, a method is being considered in which the above-mentioned organic matter is put into a high-temperature, high-concentration sulfuric acid bath and acid-digested.
この方法は次の2つの工程からなるもので、その条件は
極めて過酷である。(ハ硫酸による有機物の分解工程
(ポリ塩化ビニルの場合)
(C2H3Ct)n+ nH2SO4一→2nC+NS
O2+2nH20+NHCt(2)硫酸添加による炭素
の酸化工程3C+2HN03
+4N0+3C02+2H20
上記における第1工程は、通常850I)、200℃以
上の硫酸浴中で約5時間程度行なわれ、引続いて硝酸が
添加され、更に約2時間程度を要して第2工程が実施さ
れる。This method consists of the following two steps, and the conditions are extremely harsh. (Decomposition process of organic matter using sulfuric acid (in the case of polyvinyl chloride) (C2H3Ct)n+ nH2SO4-→2nC+NS
O2 + 2nH20 + NHCt (2) Carbon oxidation step by adding sulfuric acid 3C + 2HN03 + 4N0 + 3C02 + 2H20 The first step in the above is usually carried out in a sulfuric acid bath at 200°C or higher for about 5 hours, followed by the addition of nitric acid, and then about 2 The second step is carried out over a period of time.
この様な厳しい条件に耐え得る材料としては、一般に白
金、高珪素鋳鉄、グラスライニング鋼、タンタル(合金
を含む)等が考えられる。Generally, platinum, high-silicon cast iron, glass-lined steel, tantalum (including alloys), etc. are considered as materials that can withstand such severe conditions.
しかし白金は高価であり、高珪素鋳鉄は脆いという欠点
があジ、更にグラスライニング鋼では複雑な形状を呈す
る部分の加工が困難であると共に、熱履歴を受けると割
れることがあるという問題がある。そこで残されたタン
タル(合金を含む:但し以後は単にTaと表わす)がク
ローズ・アツプされている。しかしTaの場合は、極め
て微量ながら腐食という問題があ如、又該腐食に伴なつ
て発生する水素を吸収して脆化するという懸念がある。However, platinum is expensive, high-silicon cast iron is brittle, and glass-lined steel has the disadvantage that it is difficult to process parts with complex shapes and may crack when subjected to thermal history. . The remaining tantalum (including alloys; hereinafter simply referred to as Ta) is shown in a close-up. However, in the case of Ta, there is a problem of corrosion, albeit in a very small amount, and there is also a concern that it absorbs hydrogen generated as a result of the corrosion and becomes brittle.
従つてこれらの問題が解決されない限只酸消化釜用材料
として不十分である。Taの腐食防止に関する従来の研
究実績は極めて僅かであり、実質的に未開拓の分野であ
るが、水素吸収脆化を予防する方法としては、Taの表
面一部に白金箔を貼ジ付けて一種の犠牲陰極効果をもた
らす方法が知られている。Therefore, it is insufficient as a material for a limited acid digester unless these problems are solved. There has been very little previous research on corrosion prevention of Ta, and it is a virtually unexplored field, but one way to prevent hydrogen absorption embrittlement is to attach platinum foil to a part of the surface of Ta. Methods are known that provide a type of sacrificial cathode effect.
しかるに白金の腐食溶損は極めて早く進行し再三取り換
える必要があるから、作業性及び経済性の両面に卦いて
欠点があつた。本発明はこれらの事晴に着目してなされ
たものであつてTaの腐食劣化と水素吸収脆化を、同時
に、且つ効果的に、又作業性及び経済性において問題な
く防止できる方法の提供を目的とするものである。However, corrosion and erosion of platinum progresses extremely quickly, requiring repeated replacement, which is disadvantageous in terms of both workability and economy. The present invention has been made in view of these circumstances, and it is an object of the present invention to provide a method that can simultaneously and effectively prevent corrosion deterioration and hydrogen absorption embrittlement of Ta without any problems in terms of workability and economy. This is the purpose.
しかして本発明に}いては、有機物の分解工程に先立つ
て、硝酸若しくは亜硝酸又はこれらの塩を高温高濃度の
硫酸浴中に加えて酸消化を行なう点に要旨が存在するも
のである。Therefore, the gist of the present invention is to perform acid digestion by adding nitric acid, nitrous acid, or salts thereof to a high-temperature, high-concentration sulfuric acid bath prior to the decomposition process of organic matter.
即ち本発明は、高温高濃度の硫酸浴中に硝酸又は亜硝酸
を、遊離酸又は塩の形で添加することにより、Taの腐
食が抑制され、且つ水素吸収が防止されるという知見を
基にしてなされたものであり、以下実験例を基にして本
発明の構成及び作用効果を明らかにしていく。第1図は
腐食試験装置の概略を示す説明図で、トレイ1には、数
個(図では3個)のマントルヒタ2を配置し、夫々には
、冷却用コンデンサー5付きのセパラブル・フラスコ3
を安置している。That is, the present invention is based on the knowledge that corrosion of Ta is suppressed and hydrogen absorption is prevented by adding nitric acid or nitrous acid in the form of free acid or salt to a high-temperature, high-concentration sulfuric acid bath. The structure and effects of the present invention will be clarified below based on experimental examples. FIG. 1 is an explanatory diagram showing the outline of a corrosion test apparatus. Several (three in the figure) mantle heaters 2 are arranged on a tray 1, each of which has a separable flask 3 equipped with a cooling condenser 5.
is enshrined here.
各フラスコ3には、夫々濃度の異なる硫酸溶液9が収容
され、且つ一定大きさ(実験では2mm×20mmX2
0mm)のTa板10を浸漬した。尚冷却水は矢印Aに
沿つて導入され、ストツプバルブ8を経て矢印B,C,
Dに沿つて各コンデンサー5を経由し、更に矢印E方向
に放流される。尚又、4は測温センサー、6は断水セン
サー、7は液漏洩センサーであり、夫々を鎖線で囲む制
御部に配置して安全運転を期した。各フラスコ3は、9
5%硫酸を収容し硝酸、亜硝酸及びこれらの塩の添加、
訃よび無添加の群に分け、硫酸浴温を250℃に維持し
つつ500時間の保持実験を行なつた。Each flask 3 contains a sulfuric acid solution 9 with a different concentration, and has a fixed size (2 mm x 20 mm x 2 in the experiment).
A Ta plate 10 (0 mm) was immersed. The cooling water is introduced along the arrow A, passes through the stop valve 8, and then flows through the arrows B, C,
The water passes through each condenser 5 along line D and is further discharged in the direction of arrow E. Furthermore, 4 is a temperature sensor, 6 is a water cutoff sensor, and 7 is a liquid leakage sensor, and each is placed in the control section surrounded by a chain line to ensure safe operation. Each flask 3 has 9
Addition of nitric acid, nitrous acid and their salts, containing 5% sulfuric acid;
A holding experiment was conducted for 500 hours while maintaining the sulfuric acid bath temperature at 250° C. by dividing the samples into groups with no additives and those with no additives.
実験終了後試験片を取り出して乾燥し、重量を測定する
と共に、Ta中の水素濃度を分析した。試験前後の重量
変化から平均腐食速度を求めて第1表に示した。即ち塩
の種類によつて添加効果の大小はあるが、いずれの場合
も無添加の場合にくらべて顕著な減少効果を示しており
、且つその効果は、添加量依存性が殆んど無かつた。After the experiment was completed, the test piece was taken out, dried, weighed, and the hydrogen concentration in Ta was analyzed. The average corrosion rate was determined from the weight change before and after the test and is shown in Table 1. In other words, the effect of addition varies depending on the type of salt, but in all cases it shows a remarkable reduction effect compared to the case without addition, and the effect has almost no dependence on the amount added. Ta.
各種金属塩の中では、比較的電離性が良好と思われるア
ルカリ金属塩やアンモニウム塩よジも、銅族、アルカリ
土類金属、鉄属等に属する元素の塩の方法が、より顕著
な効果を示した。尚硝酸塩と亜硝酸塩の間には実質的な
相違が存在しないことも明らかになつた。塩の種類は上
記の如く例示したものに限定されず、Mg,Ca,Cd
,Mn,At,In等との単純塩の他、硝酸塩化モリブ
デン、硝酸ガドリニウムニツケルの様な複塩や錯塩等と
して添加することを排除するものではない。本発明で添
加される硝酸若しくは亜硝酸又はそれらの塩は、以上述
べた如く広義の意味を有するが、これらを硫酸浴中に加
える時期は、有機物の分解工程前に硫酸浴を調製する段
階、有機物投入の段階、硫酸浴の温度が高温に達した段
階等の中から任意に選択すればよいが、可及的早い時期
が望まれることは言う迄もない。Among various metal salts, alkali metal salts and ammonium salts, which are thought to have relatively good ionizability, have a more pronounced effect when using salts of elements belonging to the copper group, alkaline earth metals, iron group, etc. showed that. It has also been found that there is no substantial difference between nitrate and nitrite. The types of salts are not limited to those exemplified above, but include Mg, Ca, Cd
, Mn, At, In, etc., addition as a double salt or complex salt such as molybdenum nitrate or gadolinium nickel nitrate is not excluded. The nitric acid or nitrous acid or their salts added in the present invention have a broad meaning as described above, but the timing of adding them to the sulfuric acid bath is determined at the stage of preparing the sulfuric acid bath before the decomposition process of organic matter, It may be selected arbitrarily from the stage of adding organic substances, the stage of sulfuric acid bath temperature reaching a high temperature, etc., but it goes without saying that the earliest possible stage is desired.
又その濃度が制限されないことも前述の記載によつて理
解される通Dである。本発明は上記の如く構成されてい
るから、極めて簡単な手段によつて、しかも安価に、T
aの腐食と水素吸収を同時に且つ確実に抑制することが
できる。It is also understood from the above description that the concentration is not limited. Since the present invention is constructed as described above, T.
Corrosion of a and hydrogen absorption can be simultaneously and reliably suppressed.
従つて有機物の酸消化による減容安定化が、Ta製酸消
化釜によつて安全に実施できる様になつた訳で、放射性
元素に汚染された有機物の処理技術を大きく前進させる
ことができる。Therefore, volume reduction and stabilization by acid digestion of organic matter can now be carried out safely using a Ta acid digestion kettle, making it possible to greatly advance the treatment technology of organic matter contaminated with radioactive elements.
第1図は実験装置の概要を示す説明図である。 9・・・硫酸溶液、10・・・Ta板。 FIG. 1 is an explanatory diagram showing an outline of the experimental apparatus. 9...Sulfuric acid solution, 10...Ta plate.
Claims (1)
高温高濃度の硫酸浴中で分解する工程、及び硝酸を添加
して更に酸化する工程、を含む有機高分子物質の酸消化
処理方法において、前記分解工程に先立つて、硫酸浴中
に硝酸、亜硝酸、硝酸塩及び亜硝酸塩よりなる群から選
択される1種以上を添加しておくことを特徴とするタン
タル製酸消化釜による酸消化処理方法。1. A method for acid digestion treatment of an organic polymer substance, which includes the steps of decomposing the organic polymer substance contained in a tantalum acid digestion pot in a high-temperature, high-concentration sulfuric acid bath, and further oxidizing it by adding nitric acid. , Acid digestion treatment using a tantalum acid digestion pot, characterized in that, prior to the decomposition step, one or more selected from the group consisting of nitric acid, nitrous acid, nitrates, and nitrites is added to the sulfuric acid bath. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55065789A JPS5931039B2 (en) | 1980-05-16 | 1980-05-16 | Acid digestion treatment method using a tantalum acid digestion pot |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55065789A JPS5931039B2 (en) | 1980-05-16 | 1980-05-16 | Acid digestion treatment method using a tantalum acid digestion pot |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5761996A JPS5761996A (en) | 1982-04-14 |
| JPS5931039B2 true JPS5931039B2 (en) | 1984-07-30 |
Family
ID=13297142
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55065789A Expired JPS5931039B2 (en) | 1980-05-16 | 1980-05-16 | Acid digestion treatment method using a tantalum acid digestion pot |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5931039B2 (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5834080A (en) * | 1981-08-25 | 1983-02-28 | Toyo Eng Corp | Treatment of acid-digested waste liquid |
| JPS59200167A (en) * | 1983-04-27 | 1984-11-13 | 三洋電機株式会社 | Air-conditioning system |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS56133474A (en) * | 1980-03-24 | 1981-10-19 | Jgc Corp | Apparatus made of tantalum and usable for hot sulfuric acid and preventing method for corrosion and hydrogen embrittlement of said apparatus |
-
1980
- 1980-05-16 JP JP55065789A patent/JPS5931039B2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5761996A (en) | 1982-04-14 |
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