JP2000235099A - Incineration disposal of graphite waste containing radioactive nuclide - Google Patents

Incineration disposal of graphite waste containing radioactive nuclide

Info

Publication number
JP2000235099A
JP2000235099A JP11038270A JP3827099A JP2000235099A JP 2000235099 A JP2000235099 A JP 2000235099A JP 11038270 A JP11038270 A JP 11038270A JP 3827099 A JP3827099 A JP 3827099A JP 2000235099 A JP2000235099 A JP 2000235099A
Authority
JP
Japan
Prior art keywords
graphite
graphite waste
incineration
waste material
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.)
Granted
Application number
JP11038270A
Other languages
Japanese (ja)
Other versions
JP3173599B2 (en
Inventor
Minoru Murata
実 村田
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials 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 Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP03827099A priority Critical patent/JP3173599B2/en
Publication of JP2000235099A publication Critical patent/JP2000235099A/en
Application granted granted Critical
Publication of JP3173599B2 publication Critical patent/JP3173599B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To prevent dust explosion, and to reduce mandays for incineration, by not pulverizing a graphite waste into fine powder but leaving it as it is or only crushing it into a block form to carry out volume-reducing treatment by the incineration. SOLUTION: A graphite waste 11 used in a nuclear reactor to be waste- disposed is stored in a fusion furnace 16 as it is or after crushed into a block form. The waste 11 is heated by an induction heating coil 14 and an induction thermal plasma torch 13 to be burnt while supplying oxygen or air into the furnace 16. Fluorine gas or chlorine gas ionized and heated by the plasma torch 13 is emitted thereafter from the torch 13 toward an incineration ash of the graphite waste 11 generated by the burning, in a condition where the incineration ash of the graphite waste 11 generated in the burning remains in the fusion furnace 16, and a radioactive nuclide contained in the incineration ash is converted into a fluoride or a chloride to be vaporized.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、原子炉内で使用さ
れた後に廃棄処分される黒鉛減速材等の、放射性核種を
含む黒鉛廃材を焼却処理する方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for incinerating waste graphite containing radionuclides, such as graphite moderator, which is discarded after being used in a nuclear reactor.

【0002】[0002]

【従来の技術】従来、この種の黒鉛廃材は粉砕して微粒
子化した後に、流動床式焼却炉で焼却されていた。この
流動床式焼却炉は容器内に多孔板などのような整流板を
有し、この多孔板の孔から加熱された酸素又は空気が吹
き上げられるように構成される。この焼却炉の容器に黒
鉛廃材の微粒子群を入れると、これらの微粒子群が上記
加熱酸素等により浮遊し、懸濁状態になって焼却され
る。
2. Description of the Related Art Conventionally, this kind of graphite waste material has been pulverized into fine particles and then incinerated in a fluidized bed incinerator. This fluidized bed incinerator has a flow straightening plate such as a perforated plate in a container, and is configured such that heated oxygen or air is blown up from holes of the perforated plate. When the fine particles of graphite waste material are put into the container of the incinerator, the fine particles are suspended by the above-mentioned heated oxygen and the like, suspended and incinerated.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記従来の黒
鉛廃材の粉砕後に流動床式焼却炉により焼却する方法で
は、黒鉛廃材を粉砕したときに、放射性核種を含む微粒
子群が大気中に放散されるのを防止するために密閉容器
内で粉砕しなければならず、粉砕装置が複雑になる不具
合があった。また黒鉛廃材の微粒子群は可燃性物質であ
り、この微粒子群が空気中に浮遊すると、粉塵爆発を発
生するおそれがあるため、爆発防止対策を講じなければ
ならない問題点もあった。本発明の目的は、黒鉛廃材を
微粒子化せずに、そのまま或いはブロック状に破砕する
だけで、焼却して減容処理することができるので、粉塵
爆発を防止できるとともに焼却工数を低減できる、放射
性核種を含む黒鉛廃材の焼却処理方法を提供することに
ある。本発明の別の目的は、黒鉛廃材の焼却後に残った
焼却灰に含まれる放射性核種を比較的容易に除染でき、
溶融炉内の耐火物交換等の保守作業における被曝低減を
図ることができる、放射性核種を含む黒鉛廃材の焼却処
理方法を提供することにある。
However, in the above-mentioned conventional method of incinerating graphite waste material by incineration with a fluidized bed incinerator, when the graphite waste material is pulverized, fine particles containing radionuclides are diffused into the atmosphere. In order to prevent the crushing, the crushing must be performed in a closed container, and there is a problem that the crushing device becomes complicated. Further, the fine particles of graphite waste material are flammable substances. If the fine particles are suspended in the air, a dust explosion may occur. Therefore, there is also a problem that explosion prevention measures must be taken. SUMMARY OF THE INVENTION An object of the present invention is to reduce the volume of waste graphite by incineration or by simply crushing it into a block without breaking it down into fine particles, so that dust explosion can be prevented and the number of incineration man-hours can be reduced. An object of the present invention is to provide a method for incinerating waste graphite containing nuclides. Another object of the present invention is to relatively easily decontaminate radionuclides contained in incinerated ash remaining after incineration of graphite waste material,
An object of the present invention is to provide a method for incinerating waste graphite containing radionuclides, which can reduce exposure during maintenance work such as refractory replacement in a melting furnace.

【0004】[0004]

【課題を解決するための手段】請求項1に係る発明は、
図1に示すように、原子炉内で使用されて廃棄処分され
る黒鉛廃材11を溶融炉16内にそのまま又はブロック
状に破砕して収容する工程と、溶融炉16内に酸素又は
空気を供給しながら黒鉛廃材11を誘導加熱コイル14
及び誘導熱プラズマトーチ13により加熱して燃焼させ
る工程と、燃焼により生成した黒鉛廃材11の焼却灰が
溶融炉16内に残った状態で、誘導熱プラズマトーチ1
3により電離して加熱したフッ素ガス又は塩素ガスを誘
導熱プラズマトーチ13から焼却灰に向って放出するこ
とにより、焼却灰中の放射性核種をそのフッ化物又は塩
化物に変換して揮発させる工程とを含む黒鉛廃材の焼却
処理方法である。
The invention according to claim 1 is
As shown in FIG. 1, a step of accommodating the graphite waste material 11 used in the nuclear reactor and discarded in a melting furnace 16 as it is or in a block shape, and supplying oxygen or air into the melting furnace 16. While the graphite waste material 11 is being
And a step of heating and burning by the induction thermal plasma torch 13, and a step of heating the induction thermal plasma torch 1 with the incinerated ash of the graphite waste material 11 generated by the combustion remaining in the melting furnace 16.
Converting the radionuclides in the incinerated ash to fluorides or chlorides and volatilizing them by discharging fluorine gas or chlorine gas heated by ionization from 3 toward the incinerated ash from the induction thermal plasma torch 13; This is a method for incineration of graphite waste materials containing.

【0005】この請求項1に記載された黒鉛廃材の焼却
処理方法では、黒鉛廃材11を微粒子化せずに、そのま
ま或いはブロック状に破砕するだけで、焼却して減容処
理することができるので、焼却工数を低減できるととも
に粉塵爆発の発生を防止できる。また黒鉛廃材11の焼
却後に残った焼却灰に含まれる放射性核種をそのフッ化
物又は塩化物に変換して揮発させることができるので、
焼却灰に含まれる放射性核種を比較的容易に除染でき、
溶融炉16内の耐火物交換等の保守作業における被曝低
減を図ることができる。
In the method for incinerating waste graphite according to the first aspect, the waste graphite 11 can be incinerated and reduced in volume simply by crushing the waste graphite 11 as it is or without breaking it into fine particles. In addition, the number of incineration steps can be reduced, and the occurrence of dust explosion can be prevented. Further, since radionuclides contained in the incineration ash remaining after the incineration of the graphite waste material 11 can be converted into their fluorides or chlorides and volatilized,
Radionuclide contained in incineration ash can be decontaminated relatively easily,
Exposure can be reduced in maintenance work such as replacement of refractories in the melting furnace 16.

【0006】[0006]

【発明の実施の形態】次に本発明の実施の形態を図面に
基づいて説明する。図1に示すように、黒鉛廃材11は
この実施の形態では原子炉内で使用された後に廃棄処分
される黒鉛減速材であり、この黒鉛廃材11は焼却処理
装置12で焼却処理される。また使用済みの黒鉛廃材の
全体形状が小さい場合には、図示しないがそのまま焼却
処理装置12に投入される。黒鉛廃材が大きい場合に
は、図示するように破砕して所定の大きさの小円筒状の
黒鉛廃材11にした後に焼却処理装置12に投入され
る。上記焼却処理装置12では加熱源として誘導熱プラ
ズマトーチ13及び誘導加熱コイル14が併用される。
焼却処理装置12は黒鉛廃材11を収容可能な溶融炉1
6と、溶融炉16の周囲に設けられた上記誘導加熱コイ
ル14と、溶融炉16内の黒鉛廃材に対向して設けられ
た上記誘導熱プラズマトーチ13と、溶融炉16の底部
に形成された排出口16aを開閉するバルブ17とを備
える。
Embodiments of the present invention will now be described with reference to the drawings. As shown in FIG. 1, the graphite waste material 11 is a graphite moderator which is discarded after being used in a nuclear reactor in this embodiment, and the graphite waste material 11 is incinerated by an incinerator 12. Further, when the entire shape of the used graphite waste material is small, it is directly introduced into the incineration apparatus 12 though not shown. When the graphite waste material is large, it is crushed into a small cylindrical graphite waste material 11 having a predetermined size as shown in the figure, and then is put into the incineration treatment device 12. In the incineration apparatus 12, an induction thermal plasma torch 13 and an induction heating coil 14 are used together as a heating source.
The incinerator 12 is a melting furnace 1 capable of storing the graphite waste material 11.
6, the induction heating coil 14 provided around the melting furnace 16, the induction thermal plasma torch 13 provided facing the graphite waste material in the melting furnace 16, and formed at the bottom of the melting furnace 16. A valve 17 for opening and closing the discharge port 16a.

【0007】溶融炉16は上記黒鉛廃材11を収容可能
に形成された椀状のロア炉体18と、このロア炉体18
に被せられた伏せ椀状のアッパ炉体19とを有する。ロ
ア炉体18及びアッパ炉体19は耐熱性を有するマグネ
シア系若しくはアルミナ系の耐火物等により形成され、
ロア炉体18及びアッパ炉体19の外面はロア断熱壁2
1及びアッパ断熱壁22によりそれぞれ被覆される。ア
ッパ炉体19の外周面にはガス排出管23の一端が接続
され、ガス排出管23の他端には排ガス浄化装置(図示
せず)を介してブロワ(図示せず)に接続される。
The melting furnace 16 has a bowl-shaped lower furnace body 18 formed so as to be able to accommodate the graphite waste material 11, and the lower furnace body 18.
And an upper furnace body 19 shaped like a bowl. The lower furnace body 18 and the upper furnace body 19 are formed of a magnesia-based or alumina-based refractory having heat resistance, and the like.
The outer surfaces of the lower furnace body 18 and the upper furnace body 19 are
1 and the upper heat insulating wall 22 respectively. One end of a gas discharge pipe 23 is connected to the outer peripheral surface of the upper furnace body 19, and the other end of the gas discharge pipe 23 is connected to a blower (not shown) via an exhaust gas purification device (not shown).

【0008】排ガス処理装置は図示しないが未燃焼のカ
ーボンや一酸化炭素、水素等を燃焼させる二次燃焼器
と、二次燃焼器から出る排ガスを水スプレーにより冷却
する冷却塔と、粉塵及びダスト状のダイオキシンを除去
するセラミックフィルタ又はバグフィルタと、放射性核
種を殆ど全てを取除くHEPA(High Efficiency Part
iculate Air)フィルタと、塩化ビニールやゴムの燃焼
による塩化水素や硫黄酸化物を中和するアルカリスクラ
バと、溶融炉16内でのプラズマ燃焼による窒素酸化物
を取除く脱硝塔とを有する。またアッパ炉体19の上面
には黒鉛廃材11を投入可能な投入筒24が接続され、
この投入筒24の上端の投入口は蓋24aにより開放可
能に閉止される。投入筒24の外周面は筒断熱壁24b
により被覆される。図1の符号26はアッパ炉体19に
設けられ溶融炉16内の黒鉛廃材12の焼却状況を監視
するための覗き窓である。
Although not shown, the exhaust gas treatment apparatus includes a secondary combustor for burning unburned carbon, carbon monoxide, hydrogen, etc., a cooling tower for cooling the exhaust gas from the secondary combustor with water spray, dust and dust. Ceramic or bag filter that removes dioxins in a form, and HEPA (High Efficiency Part) that removes almost all radionuclides.
an air filter), an alkaline scrubber for neutralizing hydrogen chloride and sulfur oxides caused by burning vinyl chloride and rubber, and a denitration tower for removing nitrogen oxides caused by plasma combustion in the melting furnace 16. A charging cylinder 24 into which the graphite waste material 11 can be charged is connected to the upper surface of the upper furnace body 19,
The charging port at the upper end of the charging cylinder 24 is openably closed by a lid 24a. The outer peripheral surface of the charging cylinder 24 is a cylindrical heat insulating wall 24b.
Coated. Reference numeral 26 in FIG. 1 is a viewing window provided in the upper furnace body 19 for monitoring the incineration status of the graphite waste material 12 in the melting furnace 16.

【0009】誘導加熱コイル14はロア炉体18の外周
面を囲むようにロア断熱壁21内に埋設され、図示しな
いが高周波電源に電気的に接続される。また誘導熱プラ
ズマトーチ13はアッパ断熱壁22の外周面にロア炉体
18内に向って取付けられ、図では1個しか示していな
いがアッパ炉体19の軸心に対して等間隔に複数個取付
けられることが好ましい。プラズマトーチ11は図2に
詳しく示すように、アッパ断熱壁22の外周面に取付け
られたベース板27と、このベース板27上に立設され
た小径セラミック管28と、この小径セラミック管28
に遊嵌され小径セラミック管28より大径の大径セラミ
ック管29と、大径セラミック管29に嵌入して下端を
ベース板27に取付けることにより大径セラミック管2
9の中央部を保持する中央保持具33と、大径セラミッ
ク管29の上部に嵌入され下端が中央保持具33の上面
に取付けられた上部保持具34と、下端が小径セラミッ
ク管28の上端に臨むように上部保持具34に挿通され
所定のガスを小径セラミック管28内に導入するガス導
入管36a,36bとを有する。
The induction heating coil 14 is buried in the lower heat insulating wall 21 so as to surround the outer peripheral surface of the lower furnace body 18, and is electrically connected to a high-frequency power source (not shown). Further, the induction thermal plasma torch 13 is attached to the outer peripheral surface of the upper heat insulating wall 22 toward the inside of the lower furnace body 18, and only one is shown in FIG. Preferably, it is attached. As shown in detail in FIG. 2, the plasma torch 11 includes a base plate 27 attached to the outer peripheral surface of the upper heat insulating wall 22, a small-diameter ceramic tube 28 erected on the base plate 27, and a small-diameter ceramic tube 28
A large-diameter ceramic tube 29 which is loosely fitted to the small-diameter ceramic tube 28 and which is fitted into the large-diameter ceramic tube 29 and whose lower end is attached to the base plate 27.
9, a central holder 33 for holding the central part of the tube 9, an upper holder 34 fitted to the upper part of the large-diameter ceramic tube 29 and a lower end attached to the upper surface of the central holder 33, and a lower end to the upper end of the small-diameter ceramic tube 28. Gas inlet pipes 36a and 36b are inserted through the upper holder 34 so as to face and introduce a predetermined gas into the small-diameter ceramic pipe 28.

【0010】アッパ断熱壁22及びベース板27には同
一孔心を有するテーパ状の放出孔22a及び連通孔27
aがそれぞれ形成され、アッパ炉体19には上記放出孔
22a及び連通孔27aを臨む大径の孔19aが形成さ
れる。上記ガス導入管36a,36bから小径セラミッ
ク管28内に導入される所定のガスは、黒鉛廃材11の
燃焼時には酸素又は空気であり、黒鉛廃材11の燃焼後
に残った焼却灰に含まれる放射性核種の除去時にはフッ
素ガス又は塩素ガスである。大径セラミック管29の下
部にはトーチ用誘導コイル37が巻回され、このコイル
37は高周波電源38に電気的に接続される。またベー
ス板27には小径セラミック管28と大径セラミック管
29との間に形成された冷却水通路39の下端に連通す
る供給通路27bが形成され、上部保持具34には冷却
水通路39の上端に連通する排出通路34aが形成され
る。
The upper insulating wall 22 and the base plate 27 have tapered discharge holes 22a and communication holes 27 having the same hole center.
a is formed, and a large-diameter hole 19 a facing the discharge hole 22 a and the communication hole 27 a is formed in the upper furnace body 19. The predetermined gas introduced into the small-diameter ceramic tube 28 from the gas introduction pipes 36a and 36b is oxygen or air when the graphite waste material 11 is burned, and the radionuclide contained in the incinerated ash remaining after the combustion of the graphite waste material 11 is performed. At the time of removal, it is fluorine gas or chlorine gas. A torch induction coil 37 is wound below the large diameter ceramic tube 29, and the coil 37 is electrically connected to a high frequency power supply 38. A supply passage 27b is formed in the base plate 27 to communicate with a lower end of a cooling water passage 39 formed between the small-diameter ceramic tube 28 and the large-diameter ceramic tube 29. A discharge passage 34a communicating with the upper end is formed.

【0011】供給通路27bにはポンプ(図示せず)に
より冷却水タンク(図示せず)の冷却水が供給され、冷
却水通路39及び排出通路34aを通った冷却水は冷却
器(図示せず)を通って冷却水タンクに戻るように構成
される。この冷却水は小径セラミック管28又は大径セ
ラミック管29が割れた場合の水漏れを防ぐために、大
気圧よりも低い圧力で循環する。ガス導入管36a,3
6bの基端は上記酸素又は空気を貯留する第1タンク
(図示せず)と、上記フッ素ガス又は塩素ガスを貯留す
る第2タンクとに接続され、図示しない開閉弁により酸
素又は空気或いはフッ素ガス又は塩素ガスのいずれかを
小径セラミック管28に導入するように切換え可能に構
成される。図2の符号41はプラズマトーチ13を覆う
電磁シールド部材である。
The cooling water in a cooling water tank (not shown) is supplied to the supply passage 27b by a pump (not shown), and the cooling water passing through the cooling water passage 39 and the discharge passage 34a is cooled by a cooler (not shown). ) To return to the cooling water tank. This cooling water is circulated at a pressure lower than the atmospheric pressure in order to prevent water leakage when the small-diameter ceramic tube 28 or the large-diameter ceramic tube 29 is broken. Gas inlet pipes 36a, 3
The base end of 6b is connected to a first tank (not shown) for storing the oxygen or air and a second tank for storing the fluorine gas or chlorine gas. Alternatively, it is configured to be switchable so that either the chlorine gas is introduced into the small-diameter ceramic tube 28. Reference numeral 41 in FIG. 2 denotes an electromagnetic shield member that covers the plasma torch 13.

【0012】図1に戻って、排出口16aは黒鉛廃材1
1の燃焼時に溶融炉16内に酸素又は空気を供給するた
めと、溶融炉16内に残った焼却灰を排出するために設
けられ、バルブ17は溶融炉16の下面に取付けられ
る。バルブ17はスライドバルブである。このバルブ1
7は図3及び図4に詳しく示すように、溶融炉16の下
面に取付けられ排出口16aに連通するベース孔43a
を有するベース板43と、排出口16a及びベース孔4
3aに挿入されノズル孔44aを有するインサートノズ
ル44と、ベース板43の下面に取付けられたボトムプ
レート46及びシールプレート47と、ボトムプレート
46及びシールプレート47間に摺動可能に挿入された
スライドプレート48と、ベース板43に取付けられス
ライドプレート48を駆動する油圧シリンダ49とを有
する。ボトムプレート46及びシールプレート47には
ノズル孔44aに連通する孔46a,47aがそれぞれ
形成される。スライドプレート48には上記孔46a,
47aに連通可能な連通孔48aと、連通孔48a近傍
にノズル孔44aに向って酸素又は空気を吹込み可能な
多数の小孔(図示せず)とが形成される。これらの小孔
はスライドプレート48内に形成された吹込み通路48
bを介して図示しない酸素タンク又は空気タンクに接続
される。またスライドプレート48は連結具50を介し
て油圧シリンダ49のピストン49aに接続される。油
圧シリンダ49のピストン49aを突出させると排出口
16aがスライドプレート48により閉止されかつ上記
小孔が排出口16aに臨み、ピストン49aを引込むと
排出口16aがスライドプレート48の連通孔48aに
連通して開放されるように構成される。図3及び図4の
符号51はシュート孔51aを有するシュートノズルで
ある。
Returning to FIG. 1, the discharge port 16a is provided with the waste graphite material 1.
The valve 17 is provided for supplying oxygen or air into the melting furnace 16 at the time of combustion of 1 and for discharging the incinerated ash remaining in the melting furnace 16, and a valve 17 is attached to the lower surface of the melting furnace 16. The valve 17 is a slide valve. This valve 1
Reference numeral 7 denotes a base hole 43a attached to the lower surface of the melting furnace 16 and communicating with the discharge port 16a, as shown in detail in FIGS.
A base plate 43 having a discharge port 16a and a base hole 4
3a, an insert nozzle 44 having a nozzle hole 44a, a bottom plate 46 and a seal plate 47 attached to the lower surface of the base plate 43, and a slide plate slidably inserted between the bottom plate 46 and the seal plate 47. And a hydraulic cylinder 49 attached to the base plate 43 and driving the slide plate 48. Holes 46a and 47a communicating with the nozzle holes 44a are formed in the bottom plate 46 and the seal plate 47, respectively. The slide plate 48 has the holes 46a,
A communication hole 48a that can communicate with 47a and a number of small holes (not shown) that can blow oxygen or air toward the nozzle hole 44a are formed near the communication hole 48a. These small holes are formed in blowing passages 48 formed in the slide plate 48.
b, it is connected to an oxygen tank or an air tank (not shown). The slide plate 48 is connected to a piston 49a of a hydraulic cylinder 49 via a connector 50. When the piston 49a of the hydraulic cylinder 49 is projected, the discharge port 16a is closed by the slide plate 48 and the small hole faces the discharge port 16a. When the piston 49a is retracted, the discharge port 16a communicates with the communication hole 48a of the slide plate 48. It is configured to be open. Reference numeral 51 in FIGS. 3 and 4 denotes a chute nozzle having a chute hole 51a.

【0013】なお、この実施の形態では、黒鉛廃材とし
て黒鉛減速材を挙げたが、放射性核種を含む黒鉛製の部
品であれば、廃棄物の焼却炉若しくは溶融炉の黒鉛耐火
物、或いは核融合炉の耐熱壁等でもよい。これらの黒鉛
廃材は角ブロック状に破砕した後に焼却処理装置に投入
されることが好ましい。また、この実施の形態では、連
通孔をボトムプレート、スライドプレート及びシールプ
レートの3枚で閉止するバルブを挙げたが、ボトムプレ
ート及びシールプレートの2枚で閉止するバルブでもよ
い。更に、この実施の形態では、バルブを油圧シリンダ
により駆動したが、エアシリンダ又はその他のアクチュ
エータにより駆動してもよい。
In this embodiment, graphite moderator has been described as graphite waste material. However, graphite refractories of waste incinerators or melting furnaces, or nuclear fusion materials, may be used for graphite parts containing radionuclides. A heat-resistant wall of a furnace may be used. It is preferable that these waste graphite materials are crushed into square blocks and then charged into an incineration treatment device. Further, in this embodiment, the valve that closes the communication hole with the three plates of the bottom plate, the slide plate, and the seal plate has been described, but a valve that closes the communication hole with the two plates of the bottom plate and the seal plate may be used. Further, in this embodiment, the valve is driven by a hydraulic cylinder, but may be driven by an air cylinder or another actuator.

【0014】このように構成された焼却処理装置を用い
て黒鉛廃材を焼却処理する方法を説明する。先ずバルブ
17を閉止した状態で(図3)排出口16に砂52を充
填し、スライドプレート48の吹込み通路48bを通っ
て小孔(図示せず)から酸素又は空気を溶融炉16内に
連続的に吹込む。次いで蓋24b(図1)をあけて溶融
炉16内に黒鉛廃材11を投入した後に蓋24bを閉じ
る。この状態で誘導加熱コイル14に高周波電圧を印加
すると、溶融炉16内の黒鉛廃材11に電磁誘導により
誘導電流が流れ、このとき発生するジュール熱により黒
鉛廃材11が燃焼する。
A method of incinerating waste graphite using the incineration apparatus configured as described above will be described. First, with the valve 17 closed (FIG. 3), the discharge port 16 is filled with sand 52, and oxygen or air is introduced into the melting furnace 16 through small holes (not shown) through the blowing passage 48b of the slide plate 48. Blow continuously. Next, the lid 24b (FIG. 1) is opened and the graphite waste material 11 is charged into the melting furnace 16, and then the lid 24b is closed. When a high-frequency voltage is applied to the induction heating coil 14 in this state, an induction current flows through the graphite waste material 11 in the melting furnace 16 by electromagnetic induction, and the Joule heat generated at this time burns the graphite waste material 11.

【0015】一方、誘導熱プラズマトーチ13の供給通
路27b、冷却水通路39及び排出通路34aに冷却水
を流し、ガス導入管36a,36bから小径セラミック
管28内に酸素又は空気を流した後、誘導熱プラズマト
ーチ13に高周波電圧を印加して上記酸素又は空気を電
離させ、この電離した酸素又は空気をトーチ用誘導コイ
ル37で誘導加熱すると、約10000℃の高温のプラ
ズマガス13aが発生し、このガス13aが連通孔27
a、放出孔22a及び大径の孔19aを通って溶融炉1
6内に放出される。このプラズマガス11aは溶融炉1
6に放出されると約3000℃になるが、この高温のプ
ラズマガス13aの熱により上記黒鉛廃材11が更に速
やかに燃焼する、即ち黒鉛廃材11の燃焼は促進され
る。黒鉛廃材11の燃焼時に発生するガスはガス排出管
23を通って排ガス処理装置(図示せず)に導かれて浄
化された後、ブロワ(図示せず)により排気される。
On the other hand, cooling water flows through the supply passage 27b, the cooling water passage 39, and the discharge passage 34a of the induction thermal plasma torch 13, and oxygen or air flows through the gas introduction pipes 36a and 36b into the small diameter ceramic pipe 28. When a high frequency voltage is applied to the induction thermal plasma torch 13 to ionize the oxygen or air, and the ionized oxygen or air is induction heated by the torch induction coil 37, a high-temperature plasma gas 13a of about 10,000 ° C. is generated, This gas 13a is connected to the communication hole 27.
a through the discharge hole 22a and the large-diameter hole 19a.
6 is released. This plasma gas 11a is supplied to the melting furnace 1
When released to 6, the temperature becomes about 3000 ° C., but the heat of the high-temperature plasma gas 13a causes the graphite waste material 11 to burn more quickly, that is, the combustion of the graphite waste material 11 is promoted. The gas generated during the combustion of the graphite waste material 11 is guided to an exhaust gas treatment device (not shown) through a gas discharge pipe 23, purified, and then exhausted by a blower (not shown).

【0016】更に上記黒鉛廃材11の燃焼が完了する
と、溶融炉16内には黒鉛廃材11の焼却灰が少量だけ
残る。この焼却灰にはコバルト60等の放射性核種が含
まれる。そこでスライドプレート48の吹込み通路48
bからの酸素又は空気の溶融炉16内への吹込みを停止
し、かつガス導入管36a,36bから小径セラミック
管28内への酸素又は空気の供給を停止した後に、ガス
導入管36a,36bから小径セラミック管28内にフ
ッ素ガス又は塩素ガスを流した後に、誘導熱プラズマト
ーチ11に高周波電圧を印加して上記フッ素ガス又は塩
素ガスを電離させ、この電離したフッ素ガス又は塩素ガ
スをトーチ用誘導コイル37で誘導加熱する。
Further, when the combustion of the graphite waste material 11 is completed, a small amount of the incinerated ash of the graphite waste material 11 remains in the melting furnace 16. This incinerated ash contains radionuclides such as cobalt 60. Therefore, the blowing passage 48 of the slide plate 48
b, the supply of oxygen or air from the gas introduction tubes 36a, 36b into the small-diameter ceramic tube 28 is stopped, and then the gas introduction tubes 36a, 36b After flowing fluorine gas or chlorine gas into the small-diameter ceramic tube 28, a high-frequency voltage is applied to the induction thermal plasma torch 11 to ionize the fluorine gas or chlorine gas, and the ionized fluorine gas or chlorine gas is used for the torch. Induction heating is performed by the induction coil 37.

【0017】このとき約10000℃の高温のプラズマ
ガス11aが発生し、連通孔27a、放出孔22a及び
大径の孔19aを通って溶融炉16内に放出される。こ
のプラズマガス11aは溶融炉16に放出されると約3
000℃になるが、この高温のプラズマガス11aは上
記放射性核種と反応してその放射性核種をそのフッ化物
又は塩化物に変換して揮発させる。この揮発した放射性
核種のフッ化物又は塩化物はガス排出管23を通って排
ガス処理装置に導かれて浄化された後、ブロワにより排
気される。この結果、上記焼却灰に含まれる放射性核種
は減少する、即ち焼却灰の放射能レベルが低下するの
で、溶融炉16内の耐火物交換等の保守作業における被
曝低減を図ることができる。なお、溶融炉16内の焼却
灰が所定量に達すると、バルブ17を油圧シリンダ49
により摺動し、スライドプレート48の連通孔48aが
排出口16aに連通する(図4)。このとき先ず砂52
がシュートノズル51のシュート孔51aから排出さ
れ、続いて放射能レベルが低下した焼却灰が排出され
る。
At this time, a high-temperature plasma gas 11a of about 10,000 ° C. is generated and discharged into the melting furnace 16 through the communication hole 27a, the discharge hole 22a and the large-diameter hole 19a. When this plasma gas 11a is released into the melting furnace 16, about 3
Although the temperature becomes 000 ° C., the high-temperature plasma gas 11a reacts with the radionuclide to convert the radionuclide into its fluoride or chloride and volatilize it. The volatilized radionuclide fluoride or chloride is led to the exhaust gas treatment device through the gas discharge pipe 23 and purified, and then exhausted by the blower. As a result, the radionuclide contained in the incinerated ash is reduced, that is, the radioactivity level of the incinerated ash is reduced, so that it is possible to reduce the exposure in maintenance work such as refractory exchange in the melting furnace 16. When the amount of incinerated ash in the melting furnace 16 reaches a predetermined amount, the valve 17 is set to the hydraulic cylinder 49.
, And the communication hole 48a of the slide plate 48 communicates with the discharge port 16a (FIG. 4). At this time, first sand 52
Is discharged from the chute hole 51a of the chute nozzle 51, and subsequently, the incinerated ash whose radioactivity level has decreased is discharged.

【0018】[0018]

【発明の効果】以上述べたように、本発明によれば、溶
融炉内に酸素等を供給しながら黒鉛廃材を誘導加熱コイ
ル及び誘導熱プラズマトーチにより加熱して燃焼させ、
溶融炉内に黒鉛廃材の焼却灰が残った状態で、誘導熱プ
ラズマトーチにより電離して加熱したフッ素ガス又は塩
素ガスを焼却灰に向って放出することにより、焼却灰中
の放射性核種をそのフッ化物又は塩化物に変換して揮発
させたので、放射性核種を含む微粒子群が大気中に放散
されるのを防止するために密閉容器内で粉砕しなければ
ならない、従来の黒鉛廃材を微粒子化して焼却する方法
と比較して、本発明では、黒鉛廃材を微粒子化せずに、
そのまま或いはブロック状に破砕するだけで、焼却して
減容処理することができ、焼却工数を低減できる。
As described above, according to the present invention, graphite waste material is heated and burned by an induction heating coil and an induction heat plasma torch while supplying oxygen and the like into a melting furnace.
In the state where the incinerated ash of the graphite waste remains in the melting furnace, the radionuclide in the incinerated ash is discharged by discharging the fluorine gas or the chlorine gas heated by ionization with the induction thermal plasma torch toward the incinerated ash. Converted to chlorides or chlorides and volatilized, it must be crushed in a closed container to prevent fine particles containing radionuclides from being released into the atmosphere. Compared with the method of incineration, in the present invention, the graphite waste material is not atomized,
By crushing as it is or by simply crushing it into a block, incineration and volume reduction can be performed, and the number of incineration steps can be reduced.

【0019】また粉塵爆発を発生するおそれがあるた
め、爆発防止対策を講じなければならない、従来の黒鉛
廃材を微粒子化して焼却する方法と比較して、本発明で
は、黒鉛廃材を微粒子化せずにそのまま或いはブロック
状に破砕するだけで済むので、粉塵爆発が発生すること
はない。更に本発明では、黒鉛廃材の焼却後に残った焼
却灰に含まれる放射性核種をそのフッ化物又は塩化物に
変換して揮発させることができるので、焼却灰に含まれ
る放射性核種を比較的容易に除染できる。この結果、溶
融炉内の耐火物交換等の保守作業における被曝低減を図
ることができる。
Further, in comparison with the conventional method of making graphite waste fine and burning it, the present invention does not make the waste graphite fine because there is a possibility that a dust explosion may occur. No dust explosion occurs because it is only necessary to crush it as it is or in a block shape. Further, according to the present invention, since radionuclides contained in the incinerated ash remaining after the incineration of graphite waste can be converted into fluorides or chlorides and volatilized, the radionuclides contained in the incinerated ash can be relatively easily removed. I can dye it. As a result, it is possible to reduce the exposure in maintenance work such as refractory replacement in the melting furnace.

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

【図1】本発明実施形態の黒鉛廃材を焼却処理する装置
の縦断面図。
FIG. 1 is a longitudinal sectional view of an apparatus for incinerating graphite waste according to an embodiment of the present invention.

【図2】図1のA部拡大断面図。FIG. 2 is an enlarged sectional view of a portion A in FIG.

【図3】図1のB部拡大断面図。FIG. 3 is an enlarged sectional view of a portion B in FIG. 1;

【図4】バルブのスライドプレートをスライドして溶融
炉の排出口が開放された状態を示す図3に対応する断面
図。
FIG. 4 is a sectional view corresponding to FIG. 3, showing a state in which a discharge plate of a melting furnace is opened by sliding a slide plate of a valve.

【符号の説明】[Explanation of symbols]

11 黒鉛廃材 13 誘導熱プラズマトーチ 14 誘導加熱コイル 16 溶融炉 11 Waste Graphite 13 Induction Thermal Plasma Torch 14 Induction Heating Coil 16 Melting Furnace

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) F23G 7/00 ZAB F23J 1/00 A F23J 1/00 G21F 9/02 501Z G21F 9/02 501 B09B 3/00 303J Fターム(参考) 3K061 AA23 AB01 AC09 BA04 BA05 BA10 CA13 CA14 DA02 DB11 DB17 DB20 NA01 NA07 NA18 NA19 4D004 AA50 AB09 CA04 CA27 CA28 CB13 CB33 CB50 ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 7 Identification symbol FI Theme coat ゛ (Reference) F23G 7/00 ZAB F23J 1/00 A F23J 1/00 G21F 9/02 501Z G21F 9/02 501 B09B 3 / 00 303J F-term (reference) 3K061 AA23 AB01 AC09 BA04 BA05 BA10 CA13 CA14 DA02 DB11 DB17 DB20 NA01 NA07 NA18 NA19 4D004 AA50 AB09 CA04 CA27 CA28 CB13 CB33 CB50

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 原子炉内で使用されて廃棄処分される黒
鉛廃材(11)を溶融炉(16)内にそのまま又はブロック状に
破砕して収容する工程と、 前記溶融炉(16)内に酸素又は空気を供給しながら前記黒
鉛廃材(11)を誘導加熱コイル(14)及び誘導熱プラズマト
ーチ(13)により加熱して燃焼させる工程と、 前記燃焼により生成した黒鉛廃材(11)の焼却灰が前記溶
融炉(16)内に残った状態で、前記誘導熱プラズマトーチ
(13)により電離して加熱したフッ素ガス又は塩素ガスを
前記誘導熱プラズマトーチ(13)から前記焼却灰に向って
放出することにより、前記焼却灰中の放射性核種をその
フッ化物又は塩化物に変換して揮発させる工程とを含む
黒鉛廃材の焼却処理方法。
A step of crushing and storing a graphite waste material (11) used in a nuclear reactor and discarded in a melting furnace (16) as it is or in a block shape; Heating and burning the graphite waste material (11) with an induction heating coil (14) and an induction thermal plasma torch (13) while supplying oxygen or air; and incineration ash of the graphite waste material (11) generated by the combustion. Is left in the melting furnace (16), and the induction thermal plasma torch is
By releasing the fluorine gas or chlorine gas ionized and heated by (13) from the induction thermal plasma torch (13) toward the incineration ash, the radionuclide in the incineration ash is converted into its fluoride or chloride. Converting and volatilizing the waste.
JP03827099A 1999-02-17 1999-02-17 Incineration method of waste graphite containing radionuclides Expired - Lifetime JP3173599B2 (en)

Priority Applications (1)

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Application Number Priority Date Filing Date Title
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Country Status (1)

Country Link
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JP2009061393A (en) * 2007-09-06 2009-03-26 Kurimoto Mec Ltd Waste tire treatment apparatus
WO2011036208A1 (en) * 2009-09-23 2011-03-31 Sgl Carbon Se Method and reactor for treating bulk material containing carbon
TWI418260B (en) * 2005-04-28 2013-12-01 E E R Env Energy Resrc Israel An improved plasma torch for use in a waste processing chamber
JP2016161422A (en) * 2015-03-03 2016-09-05 清水建設株式会社 Method for processing activated concrete
CN110715301A (en) * 2019-10-20 2020-01-21 安徽航天环境工程有限公司 Plasma treatment device for household garbage
CN113012841A (en) * 2021-03-17 2021-06-22 中国科学院上海应用物理研究所 Device for desorbing multiple nuclides in graphite
CN113393952A (en) * 2021-05-27 2021-09-14 中国辐射防护研究院 Fluidized bed reactor for treating radioactive waste graphite

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20030039871A (en) * 2001-11-16 2003-05-22 대한민국(서울대학교) Apparatus and method for treatment of waste matter using plasma
TWI418260B (en) * 2005-04-28 2013-12-01 E E R Env Energy Resrc Israel An improved plasma torch for use in a waste processing chamber
JP2009061393A (en) * 2007-09-06 2009-03-26 Kurimoto Mec Ltd Waste tire treatment apparatus
WO2011036208A1 (en) * 2009-09-23 2011-03-31 Sgl Carbon Se Method and reactor for treating bulk material containing carbon
US20120251434A1 (en) * 2009-09-23 2012-10-04 Hubert Jaeger Method and reactor for treating bulk material containing carbon
AU2010299920B2 (en) * 2009-09-23 2014-10-23 Sgl Cfl Ce Gmbh Method and reactor for treating bulk material containing carbon
RU2586350C2 (en) * 2009-09-23 2016-06-10 Сгл Карбон Се Method of treating carbonaceous bulk material
JP2016161422A (en) * 2015-03-03 2016-09-05 清水建設株式会社 Method for processing activated concrete
CN110715301A (en) * 2019-10-20 2020-01-21 安徽航天环境工程有限公司 Plasma treatment device for household garbage
CN113012841A (en) * 2021-03-17 2021-06-22 中国科学院上海应用物理研究所 Device for desorbing multiple nuclides in graphite
CN113393952A (en) * 2021-05-27 2021-09-14 中国辐射防护研究院 Fluidized bed reactor for treating radioactive waste graphite

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