JPH0778553B2 - Method for highly concentrating and drying and solidifying radioactive liquid waste - Google Patents
Method for highly concentrating and drying and solidifying radioactive liquid wasteInfo
- Publication number
- JPH0778553B2 JPH0778553B2 JP1019342A JP1934289A JPH0778553B2 JP H0778553 B2 JPH0778553 B2 JP H0778553B2 JP 1019342 A JP1019342 A JP 1019342A JP 1934289 A JP1934289 A JP 1934289A JP H0778553 B2 JPH0778553 B2 JP H0778553B2
- Authority
- JP
- Japan
- Prior art keywords
- solidifying
- liquid
- drying
- highly concentrated
- waste
- 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 - Fee Related
Links
- 238000000034 method Methods 0.000 title claims description 15
- 238000001035 drying Methods 0.000 title claims description 13
- 230000002285 radioactive effect Effects 0.000 title claims description 7
- 239000010808 liquid waste Substances 0.000 title description 8
- 239000000047 product Substances 0.000 claims description 24
- 239000007788 liquid Substances 0.000 claims description 23
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 claims description 14
- KGBXLFKZBHKPEV-UHFFFAOYSA-N boric acid Chemical compound OB(O)O KGBXLFKZBHKPEV-UHFFFAOYSA-N 0.000 claims description 14
- 239000004327 boric acid Substances 0.000 claims description 14
- 239000002699 waste material Substances 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- 239000010409 thin film Substances 0.000 claims description 10
- 239000000292 calcium oxide Substances 0.000 claims description 7
- 235000012255 calcium oxide Nutrition 0.000 claims description 7
- 239000002244 precipitate Substances 0.000 claims description 7
- 239000002901 radioactive waste Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 5
- 239000011347 resin Substances 0.000 claims description 4
- 229920005989 resin Polymers 0.000 claims description 4
- 239000000725 suspension Substances 0.000 claims description 4
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims description 3
- 239000003456 ion exchange resin Substances 0.000 claims description 3
- 229920003303 ion-exchange polymer Polymers 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 239000000126 substance Substances 0.000 claims description 3
- 239000007791 liquid phase Substances 0.000 claims description 2
- 238000007711 solidification Methods 0.000 claims description 2
- 230000008023 solidification Effects 0.000 claims description 2
- 229920001187 thermosetting polymer Polymers 0.000 claims description 2
- 239000007787 solid Substances 0.000 claims 2
- 239000011343 solid material Substances 0.000 claims 2
- 239000010419 fine particle Substances 0.000 claims 1
- 239000008187 granular material Substances 0.000 claims 1
- 229910052751 metal Inorganic materials 0.000 claims 1
- 239000002184 metal Substances 0.000 claims 1
- 150000002739 metals Chemical class 0.000 claims 1
- 229920005992 thermoplastic resin Polymers 0.000 claims 1
- 239000004568 cement Substances 0.000 description 5
- BTBUEUYNUDRHOZ-UHFFFAOYSA-N Borate Chemical compound [O-]B([O-])[O-] BTBUEUYNUDRHOZ-UHFFFAOYSA-N 0.000 description 4
- 230000006835 compression Effects 0.000 description 4
- 238000007906 compression Methods 0.000 description 4
- 230000005484 gravity Effects 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 238000001556 precipitation Methods 0.000 description 4
- 229920006305 unsaturated polyester Polymers 0.000 description 4
- 239000004342 Benzoyl peroxide Substances 0.000 description 3
- OMPJBNCRMGITSC-UHFFFAOYSA-N Benzoylperoxide Chemical compound C=1C=CC=CC=1C(=O)OOC(=O)C1=CC=CC=C1 OMPJBNCRMGITSC-UHFFFAOYSA-N 0.000 description 3
- JLTDJTHDQAWBAV-UHFFFAOYSA-N N,N-dimethylaniline Chemical compound CN(C)C1=CC=CC=C1 JLTDJTHDQAWBAV-UHFFFAOYSA-N 0.000 description 3
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 239000010426 asphalt Substances 0.000 description 3
- 235000019400 benzoyl peroxide Nutrition 0.000 description 3
- -1 polyethylene Polymers 0.000 description 3
- 239000000853 adhesive Substances 0.000 description 2
- 230000001070 adhesive effect Effects 0.000 description 2
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 2
- 239000000920 calcium hydroxide Substances 0.000 description 2
- 235000011116 calcium hydroxide Nutrition 0.000 description 2
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002910 solid waste Substances 0.000 description 2
- VLCLHFYFMCKBRP-UHFFFAOYSA-N tricalcium;diborate Chemical compound [Ca+2].[Ca+2].[Ca+2].[O-]B([O-])[O-].[O-]B([O-])[O-] VLCLHFYFMCKBRP-UHFFFAOYSA-N 0.000 description 2
- 239000004698 Polyethylene Substances 0.000 description 1
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 229910017052 cobalt Inorganic materials 0.000 description 1
- 239000010941 cobalt Substances 0.000 description 1
- GUTLYIVDDKVIGB-UHFFFAOYSA-N cobalt atom Chemical compound [Co] GUTLYIVDDKVIGB-UHFFFAOYSA-N 0.000 description 1
- UFMZWBIQTDUYBN-UHFFFAOYSA-N cobalt dinitrate Chemical compound [Co+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O UFMZWBIQTDUYBN-UHFFFAOYSA-N 0.000 description 1
- 229910001981 cobalt nitrate Inorganic materials 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 239000003822 epoxy resin Substances 0.000 description 1
- 150000004679 hydroxides Chemical class 0.000 description 1
- 239000010857 liquid radioactive waste Substances 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- LGQLOGILCSXPEA-UHFFFAOYSA-L nickel sulfate Chemical compound [Ni+2].[O-]S([O-])(=O)=O LGQLOGILCSXPEA-UHFFFAOYSA-L 0.000 description 1
- 229910000363 nickel(II) sulfate Inorganic materials 0.000 description 1
- 239000004033 plastic Substances 0.000 description 1
- 229920003023 plastic Polymers 0.000 description 1
- 239000000088 plastic resin Substances 0.000 description 1
- 229920000647 polyepoxide Polymers 0.000 description 1
- 229920000573 polyethylene Polymers 0.000 description 1
- 235000011121 sodium hydroxide Nutrition 0.000 description 1
- 239000002900 solid radioactive waste Substances 0.000 description 1
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Description
【発明の詳細な説明】 産業上の利用分野 本発明は放射性を持つ液体廃棄物特に加圧軽水炉で発生
するホウ酸を含有する放射性廃棄物を前処理した後濃縮
器あるいは薄膜蒸発器等の乾燥器で高度に濃縮するか、
あるいは完全に乾燥した後に粒状化するか、高度濃縮液
又は乾燥物を単独あるいは固体廃棄物と混合してセメン
ト,アスファルトあるいはプラスチックで固化させる方
法に関するものである。TECHNICAL FIELD The present invention relates to a method for pre-treating radioactive liquid waste, particularly radioactive waste containing boric acid generated in a pressurized light water reactor, and then drying it in a concentrator or a thin film evaporator. Highly concentrated in a container,
Alternatively, the present invention relates to a method of completely drying and granulating, or a highly concentrated liquid or a dried product alone or mixed with solid waste and solidified with cement, asphalt or plastic.
従来の技術 このような廃液の処理法として公知である日本公開特許
公報昭48−44700号の技術は濃縮廃液にフェロシアン化
物と硝酸コバルトあるいは硫酸ニッケルを入れて不溶化
するか、あるいはホウ酸が含まれている加圧軽水炉の廃
液の場合硫酸アルミニウムあるいはカ性ソーダで前処理
した後水平形の薄膜蒸発器で乾燥され、また沸騰軽水炉
の場合可動翼をもつ軸を用いて垂直形遠心膜蒸発器を用
いて乾燥させるようになっている。2. Description of the Related Art The technique disclosed in Japanese Laid-Open Patent Publication No. 48-44700, which is known as a treatment method for such a waste liquid, is insolubilized by adding ferrocyanide and cobalt nitrate or nickel sulfate to a concentrated waste liquid, or containing boric acid In the case of liquid waste from a pressurized light water reactor, it is pretreated with aluminum sulfate or caustic soda and then dried in a horizontal thin film evaporator, and in the case of a boiling light water reactor, a vertical centrifugal membrane evaporator using a shaft with movable blades. It is designed to be dried using.
発明が解決しようとする問題点 しかしこの方法では廃液中の無機物と前処理により生じ
るホウ酸塩等が乾燥される時互いに結合力と付着力を有
するようになり乾燥器の伝熱壁面や軸に付着し完全な乾
燥が難しいという欠点がある。However, in this method, when the inorganic substance in the waste liquid and the borate generated by the pretreatment have a binding force and an adhesive force to each other when they are dried, the heat transfer wall surface and shaft of the dryer are It has the drawback that it adheres and is difficult to completely dry.
本発明の目的は液体及び固体の放射性廃棄物の減容比を
高めることと固化体の物理化学的な特性を改良すること
である。The object of the present invention is to increase the volume reduction ratio of liquid and solid radioactive waste and to improve the physicochemical properties of the solidified body.
問題点を解決するための手段その1 本発明の特徴は液体廃棄物中で存在するかあるいは前処
理工程で生成される各種の塩類を乾燥する際発生する乾
燥物の結合力及び伝熱壁面に対する付着力を除去するこ
とにある。Means for Solving the Problems Part 1 The features of the present invention are to the binding force and the heat transfer wall surface of the dried matter generated when various salts existing in the liquid waste or produced in the pretreatment step are dried. It is to remove the adhesive force.
発明の効果 したがって薄膜蒸発器等の乾燥器を用い乾燥する際乾燥
物は乾燥器の伝熱壁面又は回転軸等に付着し、回転負荷
を増加させたり、伝熱効果を低下させたりする等の欠点
をなくしてホウ酸を含有する液体廃棄物を容易に薄膜蒸
発器等で高度濃縮するかあるいは完全に乾燥させ粉末状
の乾燥物を得ることができる。そしてこれを粒状化する
かあるいは乾燥物単独にまたは乾燥物に廃イオン交換樹
脂あるいは焼却灰等の固形廃棄物と混合し、セメント,
溶融アスファルト,液相の熱硬化性樹脂(不飽和ポリエ
ステル,エポキシ樹脂等)あるいは溶融可塑性樹脂(ポ
ルエチレン等)で固化させることができる。Effects of the Invention Therefore, when dried using a drier such as a thin film evaporator, the dried material adheres to the heat transfer wall surface or the rotating shaft of the drier, which increases the rotation load or reduces the heat transfer effect. The liquid waste containing boric acid can be easily highly concentrated with a thin film evaporator or the like or completely dried to obtain a powdery dried product without any drawbacks. Then, this is granulated, or the dried product alone or the dried product is mixed with solid waste such as waste ion exchange resin or incinerated ash, and cement,
It can be solidified with molten asphalt, liquid phase thermosetting resin (unsaturated polyester, epoxy resin, etc.) or molten plastic resin (polyethylene, etc.).
作用 本発明においてはこのような従来の欠点を除去するため
に前処理工程でお互い結合力をもつ塩類、特にホウ酸化
物を粒子状子の不溶性の沈澱物を得て、この沈澱物の粒
子周囲を結合力が大きい他の化合物でとり囲まらなくに
することにより粒子間の結合力を除去し、前処理された
懸濁液を現在一般的に用いられている固定軸の垂直形薄
膜蒸発器等の乾燥器を用いて高度に濃縮するかあるいは
粉末状に乾燥させる方法が提供される。In the present invention, in order to eliminate such conventional defects, insoluble precipitates of particles are obtained by using salts having a binding force with each other, particularly borate, in a pretreatment step, and surrounding the particles of the precipitates. The binding force between particles is eliminated by not surrounding it with another compound having a large binding force, and the pre-treated suspension is generally used in the fixed axis vertical thin film evaporator etc. A method of highly concentrating or drying to a powder using a dryer of the present invention is provided.
問題点を解決するための手段その2 本発明の要旨を工程実施例と連係させ、詳細に説明する
と次のとおりである。Means for Solving Problems Part 2 The gist of the present invention will be described in detail in conjunction with the process embodiments.
本発明は一時的には放射性濃縮廃液を前処理し、これを
濃縮器または薄膜蒸発器等の乾燥器を用いて高度に濃縮
された液を得る、あるいは水分がない微細な粉末に乾燥
するものである。即ち加圧軽水炉の一次冷却系統の液体
廃棄物は放射性をもつ核種とホウ酸を含有しているが核
種の濃度はホウ酸の濃度に比べて極めて低いので蒸発濃
縮の限界及び乾燥条件はホウ酸及びホウ酸化物の濃度に
大きく依存することになる。したがって一次冷却水系統
の液体廃棄物はホウ酸の溶解度または核種飛散の物理化
学的な特性により現在ではホウ酸の濃度が12重量比がな
るように濃縮した後この濃縮廃液をセメントあるいはア
スファルト等で固化処理する方法が大部分である。The present invention temporarily pre-treats radioactive concentrated waste liquid and obtains a highly concentrated liquid by using a dryer such as a concentrator or a thin film evaporator, or it is dried into a fine powder without water. Is. That is, liquid waste in the primary cooling system of a pressurized light water reactor contains radioactive nuclides and boric acid, but the concentration of nuclides is extremely low compared to the concentration of boric acid, so the evaporative concentration limit and drying conditions are boric acid. And, it will depend largely on the concentration of borate. Therefore, due to the solubility of boric acid or the physicochemical characteristics of nuclide scattering, the liquid waste of the primary cooling water system is currently concentrated so that the concentration of boric acid becomes 12% by weight, and then this concentrated waste liquid is used as cement or asphalt. Most of them are solidified.
したがって本発明においてもホウ酸は12重量比から26重
量比間に濃縮された濃縮廃液に50メッシュから400メッ
シュの粒度をもつ生石灰をホウ酸のモル比に対して0.7
モル比以上添加して攪拌するのでホウ酸は生石灰の表面
から、継続的に内部へ反応し不溶性のホウ酸カルシウム
化合物となり全て沈澱し、また反応に加わって残った過
剰の生石灰は水と反応し消石灰になると同時にホウ酸カ
ルシウム化合物の周囲の一部分をとり囲んで、沈澱した
ホウ酸カルシウム間の結合力をなくしホウ酸カルシウム
を粒子状の不溶性沈澱物になるようにする。これととも
に消石灰の有するアルカリ性によって前処理槽の液性は
アルカリになることにより、コバルト等の多価核種は不
溶性の水酸化物として同時に沈澱される。したがって固
化後固化体からの沈出率が非常に低くなる。このように
して得た前処理槽の懸濁液を100℃以上で維持される濃
縮器または垂直形薄膜蒸発器等の乾燥器により高度濃縮
するかあるいは微細な粉末に乾燥する。このように高度
濃縮されたあるいは乾燥されたものは粒状化あるいは固
化媒質によって固化される。これに対する実施例は次に
ようである。Therefore, in the present invention as well, boric acid is added to the concentrated waste liquid concentrated between 12 weight ratio and 26 weight ratio with quick lime having a particle size of 50 mesh to 400 mesh being 0.7% with respect to the molar ratio of boric acid.
Since more than the molar ratio is added and the mixture is stirred, boric acid continuously reacts from the surface of the quick lime to the inside to form an insoluble calcium borate compound and all precipitates.The excess quick lime remaining after the reaction reacts with water. At the same time as it becomes slaked lime, it surrounds a part of the periphery of the calcium borate compound, so that the binding force between the precipitated calcium borate is lost and the calcium borate becomes a particulate insoluble precipitate. At the same time, the alkalinity of slaked lime makes the liquid in the pretreatment tank alkaline, so that polyvalent nuclides such as cobalt are simultaneously precipitated as insoluble hydroxides. Therefore, the rate of precipitation from the solidified body after solidification is very low. The suspension thus obtained in the pretreatment tank is highly concentrated by a condenser such as a condenser or a vertical thin film evaporator maintained at 100 ° C. or higher, or is dried into a fine powder. The highly concentrated or dried product is solidified by the granulating or solidifying medium. An example for this is as follows.
実施例 実施例1 ホウ酸371gを水に溶解し12重量パーセントから26重量パ
ーセントの溶液をつくりそこに生石灰250gを加えると沈
澱生成物が得られた。Example 1 371 g of boric acid was dissolved in water to form a solution of 12 to 26% by weight, and 250 g of quick lime was added thereto to obtain a precipitation product.
実施例2 実施例1より得られた生成物を薄膜蒸発器等の乾燥器を
用い乾燥物506gを得た。Example 2 The product obtained in Example 1 was dried in a dryer such as a thin film evaporator to obtain 506 g of a dried product.
実施例3 実施例1より得られた生成物を30重量パーセントの水を
含有するように高度に濃縮するか、あるいは実施例2よ
り得られた乾燥物に30重量パーセントの水を加えてか
ら、2000kg/cm2の圧力で圧縮し粒状化すると比重の1.6
の粒状化したものが得られた。Example 3 The product obtained from Example 1 is highly concentrated to contain 30% by weight of water, or 30% by weight of water is added to the dried product obtained from Example 2 and then When compressed at a pressure of 2000 kg / cm 2 and granulated, the specific gravity is 1.6
A granulated product was obtained.
実施例4 実施例2より得られた乾燥物75.8gを不飽和ポリエステ
ル70gと過酸化ベンゾイル0.2g及びジメチルアニリン0.1
mlを加えてからよく混合した後硬化させた。この時得ら
れた固化体は比重は1.59gであり、圧縮強度が1670kg/cm
2であった。Example 4 75.8 g of the dried product obtained in Example 2 was mixed with 70 g of unsaturated polyester, 0.2 g of benzoyl peroxide and 0.1 of dimethylaniline.
After adding ml, they were mixed well and then cured. The solidified product obtained at this time has a specific gravity of 1.59 g and a compression strength of 1670 kg / cm.
Was 2 .
実施例5 水を除却した湿潤樹脂79gに実施例2より得られた乾燥
物10gを入れ、さらに不飽和ポリエステル50gと過酸化ベ
ンゾイル0.3gとジメチルアニリン0.15mlを加えてからよ
く混合した後硬化させた。この時硬化された固化体は比
重は1.27であり、圧縮強度が232kg/cm2であった。Example 5 To 79 g of wet resin from which water was removed was added 10 g of the dried product obtained in Example 2, 50 g of an unsaturated polyester, 0.3 g of benzoyl peroxide and 0.15 ml of dimethylaniline were added, followed by thorough mixing and curing. It was The solidified product cured at this time had a specific gravity of 1.27 and a compressive strength of 232 kg / cm 2 .
そして湿潤樹脂8gに実施例2より得られた乾燥物81gを
入れ、さらに不飽和ポリエステル80gと過酸化ベンゾイ
ル0.3gとジメチルアニリン0.15mlを加えてからよく混合
した後硬化させた。この時硬化された固化体は比重は1.
52であり、圧縮強度は1620kg/cm2であった。Then, 81 g of the dried product obtained in Example 2 was added to 8 g of the wet resin, 80 g of the unsaturated polyester, 0.3 g of benzoyl peroxide and 0.15 ml of dimethylaniline were added, mixed well, and then cured. At this time, the solidified body cured has a specific gravity of 1.
The compression strength was 52 and the compression strength was 1620 kg / cm 2 .
実施例6 実施例1より得られた沈澱反応物を濃縮して水の量がホ
ウ酸化物等の乾燥された沈澱物に対して重量比が0.62と
なるようにする。そしてそこにセメントを乾燥した沈澱
物の重量比として0.875になるように加え、よく混合し
た後4週間硬化させた。この際得られた固化体の圧縮強
度は115kg/cm2であった。一方実施例2より得られた乾
燥物120gとセメント150gに75gの水を入れよく混合した
後4週間硬化させた。この際得られた固化体は115kg/cm
2の圧縮強度があった。Example 6 The precipitation reaction product obtained in Example 1 is concentrated so that the amount of water becomes 0.62 by weight with respect to the dried precipitation product such as borate. Then, cement was added thereto so that the weight ratio of the dried precipitate was 0.875, mixed well, and then cured for 4 weeks. The compression strength of the solidified product obtained at this time was 115 kg / cm 2 . On the other hand, 120 g of the dried product obtained in Example 2 and 150 g of cement were mixed with 75 g of water, mixed well, and then cured for 4 weeks. The solidified product obtained at this time is 115 kg / cm
There was a compressive strength of 2 .
このような本発明により有害性の放射性を有する液体廃
棄物を効率的に乾燥及び固化処理することによって廃棄
物の発生量が激減され、また固化体の安全性をはるかに
向上させることができる。According to the present invention, by efficiently drying and solidifying a liquid waste having harmful radioactivity, the amount of waste generated can be drastically reduced, and the safety of the solidified body can be greatly improved.
以上を要約するに、本発明は放射性廃液を処理するため
にこれを高度濃縮及び乾燥固化させる方法に関するもの
であり放射性濃縮廃液に粉末状生石灰を添加し、相互結
合力のない粒子状の沈澱物につくりこの懸濁液を濃縮器
または薄膜蒸発器等の乾燥器を用いて高度濃縮液として
得るかあるいは粉末状に乾燥させる方法または高度に濃
縮するかあるいは乾燥した後水を加えてから圧縮し粒状
化したり高度濃縮液及び乾燥物を各種の媒質で固化する
ことを特徴とする。To summarize the above, the present invention relates to a method for highly concentrating and drying and solidifying a radioactive waste liquid for treating the radioactive waste liquid, in which powdered quick lime is added to the radioactive concentrated waste liquid to form a particulate precipitate having no mutual binding force. This suspension is obtained as a highly concentrated liquid by using a dryer such as a concentrator or a thin film evaporator, or a method of drying it into a powder form, or a method of highly concentrating or after drying, add water and then compress. It is characterized by granulating or solidifying the highly concentrated liquid and the dried product in various media.
Claims (3)
のモル比に対して0.7モル比以上添加し相互結合力のな
い微粒子状の沈澱物につくり、この懸濁液を濃縮器また
は薄膜蒸発器等の乾燥器を用いて高度濃縮液として得る
かあるいは粉末状に完全乾燥させる方法を含み、また、
放射性濃縮廃液に粉末状の生石灰をホウ酸のモル比に対
して0.7モル比以上添加し、これを濃縮器または乾燥器
で高度濃縮するかあるいは乾燥した後水を加えてから圧
縮し粒状化したり高度濃縮液あるいは乾燥物を各種の媒
質で固化することを特徴とする放射性廃液の高度濃縮及
び乾燥固化方法。1. A powdery quicklime is added to a radioactive concentrated waste liquid in an amount of 0.7 molar ratio or more relative to the molar ratio of boric acid to form a fine particle precipitate having no mutual binding force, and this suspension is used as a concentrator or a thin film. Including a method of obtaining a highly concentrated liquid using a dryer such as an evaporator or completely drying into a powder,
Powdered quicklime is added to radioactive concentrated waste liquid in an amount of 0.7 mole ratio or more with respect to the molar ratio of boric acid, and this is highly concentrated in a concentrator or dryer, or after drying, add water and then compress and granulate. A method of highly concentrating and drying and solidifying a radioactive waste liquid, which comprises solidifying a highly concentrated liquid or a dried product in various media.
ン交換樹脂,焼却灰等の固形物質とともに液相の熱硬化
性樹脂と混合し、固化させる手段を含んで、高度濃縮液
あるいは乾燥物単独または廃イオン交換樹脂,焼却灰等
の固形物質と共に溶融した熱可塑性樹脂と混合し固化さ
せる手段を含むことを特徴とする請求項1記載の放射性
廃液の高度濃縮及び乾燥固化方法。2. A highly concentrated liquid or a dried product alone or a means for mixing and solidifying with a liquid phase thermosetting resin together with a solid substance such as a waste ion exchange resin or incineration ash, and a highly concentrated liquid or a dried product alone. 2. The method for highly concentrating and drying and solidifying radioactive waste liquid according to claim 1, further comprising means for mixing and solidifying with a molten thermoplastic resin together with a solid substance such as waste ion exchange resin and incineration ash.
に廃フィルタ及び金属類を入れて一緒に固化させる段階
からなることを特徴とする請求項2記載の放射性廃液の
高度濃縮及び乾燥固化方法。3. A highly concentrated and dry solidification of a radioactive waste liquid according to claim 2, comprising the step of putting a solid material mixed with a solidifying medium with a waste filter and metals to solidify the solid material together. Method.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1019342A JPH0778553B2 (en) | 1989-01-27 | 1989-01-27 | Method for highly concentrating and drying and solidifying radioactive liquid waste |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1019342A JPH0778553B2 (en) | 1989-01-27 | 1989-01-27 | Method for highly concentrating and drying and solidifying radioactive liquid waste |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH02208600A JPH02208600A (en) | 1990-08-20 |
| JPH0778553B2 true JPH0778553B2 (en) | 1995-08-23 |
Family
ID=11996727
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1019342A Expired - Fee Related JPH0778553B2 (en) | 1989-01-27 | 1989-01-27 | Method for highly concentrating and drying and solidifying radioactive liquid waste |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0778553B2 (en) |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6139288B2 (en) | 2013-06-18 | 2017-05-31 | 株式会社東芝 | Method and apparatus for solidifying cement of waste liquid containing boric acid |
| JP6672014B2 (en) | 2015-03-16 | 2020-03-25 | 株式会社東芝 | Treatment of radioactive liquid waste |
| TWI741802B (en) * | 2020-09-21 | 2021-10-01 | 黃慶村 | Method of processing liquid borate waste |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS52104700A (en) * | 1976-11-03 | 1977-09-02 | Belgonucleaire Sa | Method of drying boric acid containing solution |
-
1989
- 1989-01-27 JP JP1019342A patent/JPH0778553B2/en not_active Expired - Fee Related
Also Published As
| Publication number | Publication date |
|---|---|
| JPH02208600A (en) | 1990-08-20 |
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