JPS60237400A - Decontamination method - Google Patents

Decontamination method

Info

Publication number
JPS60237400A
JPS60237400A JP25167183A JP25167183A JPS60237400A JP S60237400 A JPS60237400 A JP S60237400A JP 25167183 A JP25167183 A JP 25167183A JP 25167183 A JP25167183 A JP 25167183A JP S60237400 A JPS60237400 A JP S60237400A
Authority
JP
Japan
Prior art keywords
freon
abrasive
abrasive material
path
processing chamber
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.)
Pending
Application number
JP25167183A
Other languages
Japanese (ja)
Inventor
柳原 和夫
向井 碩哉
末代史 大倉
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.)
Daido Steel Co Ltd
Original Assignee
Daido Steel Co Ltd
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 Daido Steel Co Ltd filed Critical Daido Steel Co Ltd
Priority to JP25167183A priority Critical patent/JPS60237400A/en
Publication of JPS60237400A publication Critical patent/JPS60237400A/en
Pending legal-status Critical Current

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Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は例えば原子力発電所で使用せられ放射性物質に
よって表面を汚染された工具、装置部品等の除染を行う
方法に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for decontaminating tools, equipment parts, etc. used in nuclear power plants, for example, whose surfaces are contaminated with radioactive substances.

従来、除染方法としては放射性物質によって汚染された
表面にビーズ状プラスチック、鉄粒子。
Traditionally, decontamination methods involve applying beads of plastic or iron particles to surfaces contaminated with radioactive materials.

ガラス粒子等の研摩材とともに水または空気のような流
体を噴射し、流体噴射圧と研摩材の研摩効果によって該
表面から放射性物質を除去する方法が提供されている。
A method is provided in which a fluid such as water or air is injected together with an abrasive material such as glass particles, and radioactive materials are removed from the surface by the fluid injection pressure and the abrasive effect of the abrasive material.

しかし該方法によれば使用後の流体と研摩材の両者を清
浄にすることが困難でこれらの廃棄には多々の問題が生
ずるものである。
However, according to this method, it is difficult to clean both the fluid and the abrasive material after use, and many problems arise in their disposal.

本発明は上記従来の問題点を解決して除染に使用した流
体と研摩材の両者を容易に清浄することを目的とし、流
体としてフレオンを用いることを骨子とするものである
The present invention aims to solve the above conventional problems and easily clean both the fluid and abrasive material used for decontamination, and its main feature is to use Freon as the fluid.

本発明を以下に詳細に説明する。The invention will be explained in detail below.

本発明に用いられるフレオンとは灰化水素のフルオルク
ロル置換体類を言い、代表的なものとしてはフレオン−
22(C田’llF2:8点−160°C1沸点−40
.8℃)、フレオン−12(Cα2F2:融点−158
°C9沸点−29,8°C)、フレオン−113(C(
ml!2F−C(17F2:融点−35℃、沸点47.
6°C)等があり、高沸点を有するフレオン=113を
用いることが望ましい。
The freon used in the present invention refers to fluorochloro substituted products of hydrogen ash, and a typical example is freon-
22 (C field'llF2: 8 points -160°C1 boiling point -40
.. 8℃), freon-12 (Cα2F2: melting point -158
°C9 boiling point -29,8 °C), Freon-113(C(
ml! 2F-C (17F2: melting point -35°C, boiling point 47.
6°C), and it is desirable to use Freon=113, which has a high boiling point.

本発明に用いられる研摩材としては鉄、ステンVスヌチ
ーμ、アルミニウム等の金属粒子、アルミナ、Vリカ、
ジルコニア等のセラミクス粒子、ガラス粒子 7eリコ
ン力−バイド粒子、砂等の硬質研摩材、ポリメチルメタ
クリレート、ポリスチレン等のプラスチック粒子、木材
粒子9種子殻等の木質粒子等の軟質研摩材がある。特に
上記軟質研摩材は被処理表面への衝突によっても粉砕さ
れにくく再使用も可能であり、したがって周囲に散乱し
て汚染するおそれのある微粉を生じないし、また使用後
の焼却処理も可能であるから望ましいものであるが、軟
質に過ぎると被処理表面に対する研摩効果が低下する。
The abrasives used in the present invention include metal particles such as iron, stainless steel V Snuchy μ, aluminum, alumina, V-rica,
There are ceramic particles such as zirconia, glass particles, hard abrasives such as 7e recon force-bide particles, sand, plastic particles such as polymethyl methacrylate and polystyrene, and soft abrasives such as wood particles such as wood particles 9 seed shells. In particular, the above-mentioned soft abrasive material is resistant to pulverization even when it hits the surface to be treated, and can be reused.Therefore, it does not generate fine powder that may be scattered around and contaminate the surrounding area, and it can also be incinerated after use. However, if it is too soft, the polishing effect on the surface to be treated will be reduced.

これらのバランスからみて軟質研摩材の中でもくろみ殻
小片、特にウオールナツト殻小片が望ましいものである
。上記研摩材は略0.4〜3. Off程度の小片(粒
子)にされるのが一般的である。
In view of these balances, among the soft abrasives, black walnut shell pieces, especially walnut shell pieces, are preferable. The above abrasive material has a diameter of about 0.4 to 3. Generally, it is made into small pieces (particles) of about 100 ml.

本発明の実施例を以下に記す。Examples of the present invention are described below.

第1図において、(1)は処理室であり研摩材Pの備蓄
槽(2)に連絡しバルブ(3)Aを有する研摩材供給路
(3)とフレオンFの備蓄槽(4)Eに連絡しバルブ(
4)A、(4)Bおよび!圧ポー/7”(4)0.ボン
y”(4) Dを有スルフレオン供給路(4)が夫々連
絡する噴射ノズル(5)が内挿され、放射性物質によっ
て表面を汚染された被処理物は該処理室(1)内で噴射
ノズル(5)から噴射されるフレオンFと研摩材Pとに
よる噴射圧と研摩効果によって放射性物質は該表面から
除去される。この際の噴射圧は略5o〜150#/d程
度に広くとられることが出来、研摩材量は噴射圧にも依
存するがフレオン11あたり略5o〜300g(ウオー
ルナツト殻の場合)程度である。
In Fig. 1, (1) is a processing chamber connected to an abrasive material P storage tank (2), an abrasive material supply path (3) having a valve (3) A, and a Freon F storage tank (4) E. Contact valve (
4) A, (4) B and! An injection nozzle (5) connected to a sulfurion supply channel (4) with a pressure port/7" (4) 0.bony" (4) D is inserted, and the workpiece has a surface contaminated with radioactive substances. The radioactive substance is removed from the surface by the injection pressure and polishing effect of Freon F and abrasive P that are injected from the injection nozzle (5) in the processing chamber (1). The injection pressure at this time can be set broadly from about 5o to 150 #/d, and the amount of abrasive depends on the injection pressure, but it is about 5o to 300g per Freon 11 (in the case of walnut shell). .

使用後のフレオンは処理室(1)内に設けられている赤
外線ヒーター(6)によって気化せられ、プロワ(7)
によって処理室(1)外へ排除され、排出路(8)によ
ってコンデンサー(9)に導びかれ、コンデンサー(9
)テ凝縮したフレオンはパルプαOAの介在する還流路
Q1を介して再び備蓄槽(4)Eに戻される。更にコン
デンサー(9)で凝縮されない残余のフレオンはデミス
タ−αηAの介在する返送路αηを介して再び処理室(
1)に戻され、デミスタ−(11)Aで捕集されたフレ
オンミストはパルプ(12Aの介在する合流路(2)を
介して還流路α1のフレオンと合流する。一方使用後の
研摩材は処理室(1)内で気化しなかったフレオンと共
にバルブ(L3Aの介在する流下路a3を介して分離槽
0尋へ流下し、該分離槽04において研摩材Pとフレオ
ンFとに分離される。研摩材Pがウオールナツト殻の場
合はフレオンFとの比重差が大であり、研摩材Pけフレ
オンFと明確に浮上分離する。
The used Freon is vaporized by an infrared heater (6) installed in the processing chamber (1), and then heated to a blower (7).
is removed from the processing chamber (1) by
) The condensed Freon is returned to the storage tank (4)E via the reflux path Q1 through which the pulp αOA exists. Furthermore, the remaining freons that are not condensed in the condenser (9) are returned to the processing chamber (
1) and collected by the demister (11) A merges with the freon in the reflux path α1 via the merging path (2) where the pulp (12A) is interposed. On the other hand, the abrasive after use The Freon that has not been vaporized in the processing chamber (1) flows down to the separation tank 0 fathom via the flow path a3 interposed by the valve (L3A), and is separated into the abrasive P and the Freon F in the separation tank 04. When the abrasive material P is a walnut shell, the difference in specific gravity between the abrasive material P and Freon F is large, and the abrasive material P and Freon F clearly float and separate.

分離された研摩材Pはスラリーポンプα0によって分離
槽04から取出され返還路OQを介して研摩材Pの備蓄
槽(2)に戻される。備蓄f! (2)で更に残余のフ
レオンFが分離されパルプ0ηAの介在する返還路Qη
を介して分離槽α◆に戻される。備蓄槽(2)において
はレベルゲージ(2)Aが挿着せられ、該レベルゲージ
(2)Aで研摩材Pの表面位を検出しスラリーポンプa
9を該検出値により制御して研摩材Pの分離槽α々から
の戻し量を調節する。分離槽α−において分離されたフ
レオンFはフィルターθ〜を介してバルブQ’JAの介
在する取出し路α窃および分離槽a4底部に連絡しバル
ブ(1)Aの介在する取出し路(1)を介してポンプ(
ロ)により取出され、汚染度の少ない場合はパルプUA
の介在する炉液路(イ)から炉液槽(ホ)に備蓄され、
パルプ(ハ)Aの介在する合流路(ハ)を介してフレオ
ン供給路(4)のフレオンと合流する。
The separated abrasive P is taken out from the separation tank 04 by the slurry pump α0 and returned to the abrasive P storage tank (2) via the return path OQ. Stockpile f! In (2), the remaining Freon F is further separated and the return path Qη is interposed with pulp 0ηA.
is returned to the separation tank α◆. A level gauge (2) A is inserted in the storage tank (2), and the level gauge (2) A detects the surface position of the abrasive material P, and the slurry pump a
9 is controlled by the detected value to adjust the amount of abrasive P returned from the separation tanks α. Freon F separated in the separation tank α- connects through the filter θ to the take-out path α interposed with the valve Q'JA and the bottom of the separation tank a4, and then connects to the take-out path (1) interposed with the valve (1)A. Pump (via
b) If the degree of contamination is low, pulp UA
is stored in the furnace liquid tank (e) from the furnace liquid path (a) where
The pulp (c) merges with the freon in the freon supply path (4) via the merging path (c) in which A is interposed.

一方フレオンの汚染度が大きくなったらバルブ(イ)A
の介在する再生路(イ)を介して蒸留器(ハ)に導びか
れ、熱源(2119Aによって気化されコンデンサー(
ハ)の介在する再生路(ロ)を介して凝縮して備蓄槽(
4)Eに戻され、蒸溜残渣はバlレブIMAの介在する
排出路翰から残渣槽(至)に取出される。なお備蓄槽(
4)E。
On the other hand, if the degree of Freon contamination increases, valve (A)
It is led to the distiller (c) through the regeneration path (a) with an intervening
It condenses through the regeneration path (b) intervening in the storage tank (c).
4) Returned to E, the distillation residue is taken out to the residue tank (to) from the discharge passageway interposed by the valve IMA. In addition, the storage tank (
4)E.

炉液槽(ハ)、蒸溜器(7)には夫々レベルゲージ(4
1)E。
There are level gauges (4) in the furnace liquid tank (c) and distiller (7), respectively.
1)E.

四A、(ハ)Aが挿着されフレオン液位を検出してフレ
オンFの取出し一取入れ量を制御している。
Four A and (c) A are inserted to detect the Freon liquid level and control the amount of Freon F to be taken out and taken in.

上記実施例にかえて処理室c11)を第2図に示すよう
なものとしてもよい。第2図において処理室G1)の上
壁から噴射ノズ/l/(至)が垂下され、処理室01)
の水平方向入口側と出口側には夫々ゴム等の柔軟材から
なるシーfi7@、に)が設けられ、ロールコンベア(
ロ)、04によってパイプ、電線ケーブル等の長尺物の
被処理物干を矢印方向に連続的に搬入、搬出しつつ噴射
ノズlv(ト)によシ処理を行う。更に処理室(41)
は第3図に示すように移動可能にされてもよい。第3図
において処理室(41)は底に口(42)し、該開口(
42)を被処理物1表面に当接し、噴射ノズ/l/ (
45)によって処理しつつ処理室(41)を移動せしめ
る。この際排出路(48) 、フレオン供給路(44)
Instead of the above embodiment, the processing chamber c11) may be as shown in FIG. In Fig. 2, an injection nozzle /l/(to) is suspended from the upper wall of the processing chamber G1), and
A sea fi7 made of flexible material such as rubber is installed on the horizontal inlet and outlet sides of the roll conveyor (
B) and 04, the long articles to be treated such as pipes and electric cables are continuously carried in and out in the direction of the arrows and processed by the injection nozzle lv (g). Furthermore, processing room (41)
may be made movable as shown in FIG. In FIG. 3, the processing chamber (41) has an opening (42) at the bottom, and the opening (
42) is brought into contact with the surface of the workpiece 1, and the injection nozzle /l/ (
45), the processing chamber (41) is moved while processing. At this time, the discharge path (48) and the Freon supply path (44)
.

研摩材供給路(43)等は当然フレキシブルにされる。The abrasive supply path (43) and the like are naturally made flexible.

なお、フレオンとウオールナツト各小片の分離及び回収
方法については、上記第1¥旬に示す実施例に限らず種
々の方法が採用できる。
Note that the method for separating and recovering the freon and walnut pieces is not limited to the embodiment shown in the first period above, and various methods can be adopted.

本発明は上記したようにフレオンを流体として用いるか
らフレオンの溶剤としての本来の洗浄性に加えて引火の
心配もなく気化させ易いから研摩材との分離、精製が極
めて効率良く行われ、また研摩材を添加するからフレ万
ンの噴出圧のみならず研摩材の研摩効果によっても放射
性物質は除去され、除染効率は格段に向上し、また研摩
材として軟質のもの、特にウオールナツト殻を用いれば
被処理面への衝突によるも破砕しにくく原形を保ち、し
たがって再使用が可能となるし、フレオンとウオールナ
ツト殻との比重差によシ浮上分離も効率よく出来る。
As mentioned above, in the present invention, Freon is used as a fluid, so in addition to the inherent cleaning properties of Freon as a solvent, it is easy to vaporize without fear of ignition, so separation and purification from abrasive materials can be carried out extremely efficiently. Since radioactive materials are added, radioactive substances are removed not only by the ejection pressure of the flexible material, but also by the abrasive effect of the abrasive material, greatly improving decontamination efficiency.In addition, soft materials, especially walnut shells, can be used as the abrasive material. In this case, it is difficult to break and maintains its original shape even when it collides with the surface to be treated, so it can be reused, and the difference in specific gravity between Freon and walnut shells allows efficient flotation and separation.

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

第1図は本発明の一実施例の系統図、第2図は他の実施
例の処理室説明図、第3図は更に他の実施例の処理室説
明図である。 図中、(2)・・・・研摩材備蓄槽、(3)・・・・研
摩材供給路、(4)・・・・フレオン供給路、(4)E
・・・・フレオン備11槽、(5)・・・・噴射ノズル
、F・・・・フレオン、P・・・・研摩材 特許出願人 大同特殊鋼株式会社 井 2 閃 牙 3 閃 手続補正書勧式) %式% 1、事件の表示 昭和58年特許願第251671号 2、発明の名称 除 染 方 法 3、補正をする者 事件との関係 特許出願人 住所 名古屋市南区星崎町字繰出66番地名称(371
)大同特殊鋼株式会社 代表取締役 秋 1)正 彌 、41代理人 〒467 住所 名古屋市瑞穂区弥富町月見ケ丘32番地6、補正
により増加する発明の数 7、補正の対象 明細書「発明の名称」の欄方法」と訂
正致します。
FIG. 1 is a system diagram of one embodiment of the present invention, FIG. 2 is an explanatory diagram of a processing chamber of another embodiment, and FIG. 3 is an explanatory diagram of a processing chamber of still another embodiment. In the figure, (2)... Abrasive material storage tank, (3)... Abrasive material supply path, (4)... Freon supply path, (4) E
... Freon equipment 11 tanks, (5) ... Injection nozzle, F ... Freon, P ... Abrasive material patent applicant Daido Steel Co., Ltd. I 2 Senga 3 Senga procedure amendment 1. Indication of the case Patent Application No. 251671 filed in 1982 2. Name of the invention Decontamination method 3. Person making the amendment Relationship with the case Patent applicant address Aza Kazudashi, Hoshizaki-cho, Minami-ku, Nagoya City Address 66 name (371
) Daido Steel Co., Ltd. Representative Director Autumn 1) Masaya, 41 Agent 467 Address 32-6 Tsukimigaoka, Yatomi-cho, Mizuho-ku, Nagoya Number of inventions increased by 7 due to amendment, subject of amendment Specification "Name of invention" The column “Method” has been corrected.

Claims (3)

【特許請求の範囲】[Claims] (1)放射性物質によって汚染された表面に研摩材とと
もにフレオンを吹付けることを特徴とする除染方法
(1) A decontamination method characterized by spraying Freon together with an abrasive onto a surface contaminated with radioactive substances
(2)該研摩材は軟質である「特許請求の範囲(1)」
に記載の除染方法
(2) “Claim (1)” that the abrasive is soft
Decontamination method described in
(3)該軟質研摩材はウオールナツト殻の小片である「
特許請求の範囲(2) J K記載の除染方法
(3) The soft abrasive is a small piece of walnut shell.
Claim (2) Decontamination method described in JK
JP25167183A 1983-12-24 1983-12-24 Decontamination method Pending JPS60237400A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP25167183A JPS60237400A (en) 1983-12-24 1983-12-24 Decontamination method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP25167183A JPS60237400A (en) 1983-12-24 1983-12-24 Decontamination method

Publications (1)

Publication Number Publication Date
JPS60237400A true JPS60237400A (en) 1985-11-26

Family

ID=17226284

Family Applications (1)

Application Number Title Priority Date Filing Date
JP25167183A Pending JPS60237400A (en) 1983-12-24 1983-12-24 Decontamination method

Country Status (1)

Country Link
JP (1) JPS60237400A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62111598U (en) * 1985-12-27 1987-07-16
JPH02145259A (en) * 1988-11-22 1990-06-04 Fuji Kihan:Kk Cleaning method for power generating turbine of boiling water nuclear power generation equipment
JP2013224852A (en) * 2012-04-20 2013-10-31 Toyo Union:Kk Contaminant removing apparatus

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS62111598U (en) * 1985-12-27 1987-07-16
JPH02145259A (en) * 1988-11-22 1990-06-04 Fuji Kihan:Kk Cleaning method for power generating turbine of boiling water nuclear power generation equipment
JP2013224852A (en) * 2012-04-20 2013-10-31 Toyo Union:Kk Contaminant removing apparatus

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