JPS6127720B2 - - Google Patents
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- Publication number
- JPS6127720B2 JPS6127720B2 JP10730681A JP10730681A JPS6127720B2 JP S6127720 B2 JPS6127720 B2 JP S6127720B2 JP 10730681 A JP10730681 A JP 10730681A JP 10730681 A JP10730681 A JP 10730681A JP S6127720 B2 JPS6127720 B2 JP S6127720B2
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- JP
- Japan
- Prior art keywords
- combustion
- section
- vaporization
- treated
- liquid
- 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
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- Incineration Of Waste (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Description
【発明の詳細な説明】
本発明は、ラジオアイソトープ研究室、実験
室、病院等で使用される液体シンチレーター等の
放射性物質を含む廃液を処理する処理装置に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a treatment device for treating waste liquid containing radioactive substances, such as a liquid scintillator used in radioisotope laboratories, laboratories, hospitals, etc.
従来、ラジオアイソトープ研究室、実験室、病
院等で使用される液体シンチレーターは、トルエ
ン、ベンゼン、キシレン等の溶媒中にテルフエミ
ル等の発光物質を溶解し、発光強度の増加をした
り、発光スペクトルを変更するために微量の活性
剤を加えたものであり、主に測定試料を液体シン
チレーターの中に混合してその放射能を測定する
ものであるが、使用済の液体シンチレーターは許
容規制値以上の放射性物質、例えば3Hや14Cを含
むがために所定タンク毎に収容されたまま野積み
の状態に放置されていたものである。また、他の
放射性物質を含む廃液の処理にあつては電気炉や
耐火レンガ炉等で焼却処理するものもあるが、こ
れ等の炉は大型の設備となるばかりでなく、廃液
を完全に気化して燃焼することができず、有害な
ススを生じ、かつ炉体内を損傷する等の欠点のあ
つたものである。 Conventionally, liquid scintillators used in radioisotope research laboratories, laboratories, hospitals, etc. dissolve luminescent substances such as terphemyl in a solvent such as toluene, benzene, or xylene, and increase the luminescence intensity or change the emission spectrum. A small amount of activator is added to change the radioactivity, and the measurement sample is mainly mixed into a liquid scintillator and its radioactivity is measured. Because it contains radioactive materials such as 3H and 14C , it was stored in designated tanks and left in the open. In addition, waste liquid containing other radioactive substances may be incinerated in electric furnaces or firebrick furnaces, but these furnaces not only require large equipment, but also completely remove the waste liquid. It has many drawbacks, such as being unable to combust, producing harmful soot, and damaging the inside of the furnace.
本発明はこれらに鑑みて発明されたものであ
り、被処理液たる、放射性物質を含む廃液を完全
に気化し、かつ燃焼でき、また従来の前記焼却炉
に比べて小型の装置となりうるものを提供するこ
とを目的とする。 The present invention was invented in view of the above, and provides an apparatus that can completely vaporize and burn waste liquid containing radioactive substances, which is the liquid to be treated, and that can be made smaller than the conventional incinerator. The purpose is to provide.
上記目的を達成するため、本発明は、炉体の上
部に配置し、被処理液を空気と混合したのち気化
する気化部、該気化部からの気化ガスを燃焼させ
る燃焼室、該燃焼室から排出される燃焼ガスの通
路に位置して設け、該燃焼ガス中の不完全燃焼成
分を完全燃焼させるための触媒体、とからなる気
化燃焼部と、炉体の中央部に位置し、かつ前記気
化燃焼部に連接して設け、前記気化燃焼部からの
燃焼ガスを通過させる通路を内側に形成する内板
と、該内板の外周を囲む外板との間に、前記燃焼
室に連通する空気導入路を備えた熱交換部と、炉
体の下部に配置し、かつ前記熱交換部に連接して
設け、前記熱交換部かならの燃焼ガスを冷却液化
する冷却機構を備える液化部とから構成した放放
射性物質を含む廃液の処理装置において、前記気
化部は、外周部に補助ヒーターを付設した耐熱性
を有する多孔性物質で形成した気化部材と、前記
気化部材の内部に配置し、周面に任意数個の透孔
を穿設すると共に、その内側に、前記被処理液を
送り込むための被処理液の送入管と、前記被処理
液中で気泡を生じさせるべく空気を送り込むため
の供給管とのそれぞれの開口端を配置して構成す
るものである。 In order to achieve the above object, the present invention provides a vaporizing section that is disposed in the upper part of a furnace body and that vaporizes a liquid to be treated after mixing it with air, a combustion chamber that burns vaporized gas from the vaporizing section, and a combustion chamber that combusts vaporized gas from the vaporizing section. a catalytic combustion section located in the passageway of the combustion gas to be discharged and configured to completely burn incompletely burned components in the combustion gas; An inner plate that is connected to the vaporization combustion section and forms a passage inside thereof through which combustion gas from the vaporization combustion section passes, and an outer plate that surrounds the outer periphery of the inner plate and communicates with the combustion chamber. a heat exchange section equipped with an air introduction passage; and a liquefaction section provided with a cooling mechanism disposed at the lower part of the furnace body and connected to the heat exchange section to cool and liquefy the combustion gas from the heat exchange section. In the apparatus for treating waste liquid containing a radioactive substance, the vaporization section includes a vaporization member made of a heat-resistant porous material with an auxiliary heater attached to the outer peripheral part, and a vaporization member disposed inside the vaporization member, An arbitrary number of through holes are bored on the circumferential surface, and inside the holes, a feed tube for the liquid to be treated is provided for feeding the liquid to be treated, and air is sent to generate bubbles in the liquid to be treated. It is constructed by arranging the respective open ends of the supply pipes for the
次に本発明の実施例を添付図面に基づいて詳細
に説明する。 Next, embodiments of the present invention will be described in detail based on the accompanying drawings.
第1図は、装置全体の縦断正面図、第2図は、
気化燃焼部の横断平面図、第3図は、気化燃焼部
の拡大縦断面図である。 Figure 1 is a vertical sectional front view of the entire device, Figure 2 is
FIG. 3 is a cross-sectional plan view of the vaporization combustion section, and FIG. 3 is an enlarged longitudinal sectional view of the vaporization combustion section.
本発明に係る装置は、縦長の箱形のケーシング
1内に設けるステンレス鋼製の炉体2の上部に位
置し、被処理液たる放射性物質を含む廃液を気化
させる気化部、該気化部で生じさせた気化ガスを
燃焼させる燃焼室8、該燃焼室8の下方に位置
し、前記燃焼後の燃焼ガス中に含まれる不完全燃
焼物を完全燃焼させるべく設けた、白金からなる
触媒体23、とを備えた気化燃焼部3と、前記炉
体2の中央部に位置し、その内側に前記気化燃焼
部3からの高温燃焼ガスを通過させるとともに、
その外周に燃焼用空気を通して前記気化燃焼部3
に導入される該燃焼用の空気を加熱しうる熱交換
部4と、前記炉体2の下部に位置し、前記熱交換
部4を通過してきた燃焼ガスを冷却して液化する
液化部5とから構成するものである。 The apparatus according to the present invention is located at the upper part of a stainless steel furnace body 2 provided in a vertically long box-shaped casing 1, and includes a vaporizing section that vaporizes a waste liquid containing radioactive substances, which is a liquid to be treated; a combustion chamber 8 in which the vaporized gas is combusted; a catalyst body 23 made of platinum located below the combustion chamber 8 and provided to completely burn incompletely combusted substances contained in the combustion gas after the combustion; and a vaporizing combustion section 3 located at the center of the furnace body 2, through which high-temperature combustion gas from the vaporizing combustion section 3 passes,
The vaporization combustion section 3 passes combustion air around its outer periphery.
a heat exchange section 4 that can heat the combustion air introduced into the furnace; a liquefaction section 5 that is located at the lower part of the furnace body 2 and that cools and liquefies the combustion gas that has passed through the heat exchange section 4; It consists of:
以下に上記各部の構成を詳細に説明する。 The configuration of each of the above parts will be explained in detail below.
前記気化燃焼部3の気化部は、上部を機密フラ
ンジ13により密閉され、下部を解放した円筒部
7、該円筒部7の内部に収容した、セラミツク・
フアイバー等の耐熱性を有する多孔性物質からな
る気化部材10、該円筒部7の外周囲に付設した
補助ヒーターH2、該気化部材10の略中央位置
に埋設し、その周面に任意数個の透孔12……を
穿設した混合筒11、該混合筒11の内部にそれ
ぞれ開口端を位置させ、被処理液たる廃液を該混
合筒11内に送り込むための送入管20および該
混合筒11内の廃液を気泡状にするための空気を
供給する供給管21、前記気化部材10の下方に
位置させて前記混合筒11の底板に固定した連結
棒14の下端に固定し、前記気化部材10の外径
と略等しい外径を有する受け皿15からなる。な
お、該受け皿15は、気化部材10を取り出すた
めのもので、気密フランジ13とともに混合筒1
1を引き抜けば、該受け皿15に気化部材10が
引つ掛かつて上方へ引き出されるのである。 The vaporization part of the vaporization combustion part 3 includes a cylindrical part 7 whose upper part is sealed by a sealing flange 13 and whose lower part is open, and a ceramic cylinder housed inside the cylindrical part 7.
A vaporizing member 10 made of a heat-resistant porous material such as fiber, an auxiliary heater H2 attached to the outer periphery of the cylindrical portion 7, and an arbitrary number of heaters embedded approximately in the center of the vaporizing member 10 on its circumferential surface. A mixing cylinder 11 having through-holes 12 . A supply pipe 21 for supplying air to make the waste liquid in 11 into bubbles is fixed to the lower end of a connecting rod 14 located below the vaporizing member 10 and fixed to the bottom plate of the mixing cylinder 11, and connected to the vaporizing member 11. It consists of a receiving tray 15 having an outer diameter approximately equal to the outer diameter of 10. Note that the receiving tray 15 is for taking out the vaporizing member 10, and is used together with the airtight flange 13 to hold the mixing cylinder 1.
1, the vaporizing member 10 is caught on the tray 15 and pulled upward.
また前記気化燃焼部3の燃焼室8は、前記気化
部の円筒部7の下方に位置し、かつ該円筒部7に
連接して設けるもので、後述の燃焼用空気の供給
量を調節すべくダンパー9を備えた燃焼用空気の
入口と、前記受け皿15の下方に配置した燃焼始
動ヒーターH2を設けてある。 The combustion chamber 8 of the vaporization combustion section 3 is located below the cylindrical section 7 of the vaporization section and is connected to the cylindrical section 7 to adjust the amount of combustion air supplied, which will be described later. A combustion air inlet equipped with a damper 9 and a combustion starting heater H2 arranged below the receiving tray 15 are provided.
さらに前記炉体2の前記気化燃焼部3の配置部
位には、該気化燃焼部3の周側全体を囲む断熱材
6および気化燃焼部3の上部を囲む断熱材17を
充填してある。 Further, the area where the vaporization combustion section 3 of the furnace body 2 is arranged is filled with a heat insulating material 6 surrounding the entire peripheral side of the vaporization combustion section 3 and a heat insulating material 17 surrounding the upper part of the vaporization combustion section 3.
前記送入管20は、その開口端を混合筒11の
略中央に位置させる一方、他端を混合筒11内か
ら炉体2の外側に伸ばし、かつケーシング1内壁
に沿つて配設し、ケーシング1の内壁の所定部位
に設けた被処理液送出用のポンプP3を介して、
ケーシング1の下部内側に収容した被処理液タン
ク19に連結する。また前記供給管21は、前記
送入管20により混合筒11内に送入された被処
理液に空気を吹き込み気泡状とするため、その開
口端を前記送入管20の開口端より下方である混
合筒11の下部に位置せしめる一方、他端を混合
筒11内から炉体2の外側に伸ばし、かつケーシ
ング1内壁に沿つて配設し、ケーシング1の内壁
の所定部位に設けた空気の供給ポンプP1に連結
する。 The feed pipe 20 has its open end located approximately at the center of the mixing cylinder 11, while the other end extends from inside the mixing cylinder 11 to the outside of the furnace body 2, and is disposed along the inner wall of the casing 1. 1 through a pump P3 for delivering the liquid to be treated, which is provided at a predetermined portion of the inner wall of the
It is connected to a liquid to be treated tank 19 housed inside the lower part of the casing 1 . In addition, the supply pipe 21 has its open end located below the open end of the feed pipe 20 in order to blow air into the liquid to be treated that is fed into the mixing cylinder 11 by the feed pipe 20 to form bubbles. It is located at the lower part of a certain mixing cylinder 11, while the other end extends from inside the mixing cylinder 11 to the outside of the furnace body 2, and is arranged along the inner wall of the casing 1. Connected to supply pump P1.
なお第1図および第2図中符号16は炉体2の
上蓋であり、該上蓋16と気密フランジ13間と
を、前記断熱材17を介してネジ18,18によ
つて固定してある。 Reference numeral 16 in FIGS. 1 and 2 is an upper lid of the furnace body 2, and the upper lid 16 and the space between the airtight flange 13 are fixed with screws 18, 18 through the heat insulating material 17.
前記熱交換部4は、前記気化燃焼部3の下端に
連設し、気化燃焼部3の触媒体23からの燃焼ガ
スが下降しつつ通過するための内部通路ご形成す
べく設けた内板22と、該内板22の外周部を適
宜の空間をもつて囲む炉体2の中央部たる外板2
4とからなる。該外板24には、その上部に、前
記内板22の燃焼用の空気導入路たる外周部空間
と、前記燃焼室8の燃焼用空気の導入口を連絡す
る通路を形成すべく、傾斜板25を設け、またそ
の略中央部で、かつ前記燃焼室8の空気導入口の
下方位置となる一側に、切り込み状の段部26を
形成する。そして前記内板22には、該段部26
と相対する外板24に向けて水平状のじやま板2
7を、適宜の間の空所28を外板24との間に形
成するように付設する。また該熱交換部4には、
前記段部26の下方に位置して前記内板22と外
板24間に空気吸入口29および該空気吸入口2
9に近い部位のケーシング1の側面壁にフイルタ
ーを嵌着した空気の取入口30を設けてあり、該
空気の取入口30を通つて空気吸入口29から内
板22と外板24間に吸入された燃焼用の空気
は、内板22の外周部に沿つて回転しながら上昇
し空所28を経てさらに上昇して、傾斜板25部
位から空気の入口を通つて前記燃焼室8内に入る
のである。 The heat exchange section 4 includes an inner plate 22 which is connected to the lower end of the vaporization combustion section 3 and is provided to form an internal passage through which the combustion gas from the catalyst body 23 of the vaporization combustion section 3 passes while descending. and an outer plate 2 which is the central part of the furnace body 2 and surrounds the outer periphery of the inner plate 22 with an appropriate space.
It consists of 4. The outer plate 24 has an inclined plate on its upper part to form a passage connecting the outer peripheral space of the inner plate 22, which is a combustion air introduction passage, with the combustion air introduction port of the combustion chamber 8. 25, and a notch-shaped step 26 is formed approximately in the center thereof and on one side below the air inlet of the combustion chamber 8. The inner plate 22 has a stepped portion 26.
A horizontal wall board 2 facing the outer board 24 facing the
7 is attached so as to form an appropriate space 28 between it and the outer panel 24. In addition, the heat exchange section 4 includes
An air intake port 29 located below the step portion 26 and between the inner plate 22 and the outer plate 24;
An air intake port 30 fitted with a filter is provided on the side wall of the casing 1 at a location close to 9, and air is drawn between the inner plate 22 and the outer plate 24 from the air intake port 29 through the air intake port 30. The combustion air thus generated rises while rotating along the outer circumference of the inner plate 22, passes through the cavity 28, further rises, and enters the combustion chamber 8 through the air inlet from the inclined plate 25. It is.
前記液化部5は、前記熱交換部4の内板22の
内部と連結した炉体2の下部外周を囲む形体の循
環パイプ31を設け、また該循環パイプ31には
冷却水を循環すべく、ケーシング1の下部に配置
した冷却水タンク32に接続する一方、下部炉体
2の底部に傾斜底板33を設け、該傾斜底板33
下端の排出口にはドレーンコツク34を備えた回
収タンク35のドレーン管36を連結して構成さ
れている。該斜底板33の排出口近傍の下部炉体
2側面に設ける開口37は、吸気管38によつ
て、ケーシング1内に配置した真空式のブロワー
P2に連結する一方、該プロワーP2の排気口は
ケーシング1の内壁の沿つて上方に延設した排気
管39の下端と連結し、また該排気管39の上端
はケーシング1の上方外部に突出させ、放射性物
質を吸着する吸着フイルター41を内設したダク
ト40に連結する。 The liquefaction section 5 is provided with a circulation pipe 31 configured to surround the lower outer periphery of the furnace body 2 and connected to the inside of the inner plate 22 of the heat exchange section 4, and the circulation pipe 31 is provided with a circulation pipe 31 for circulating cooling water. While connected to a cooling water tank 32 disposed at the bottom of the casing 1, an inclined bottom plate 33 is provided at the bottom of the lower furnace body 2, and the inclined bottom plate 33
A drain pipe 36 of a recovery tank 35 equipped with a drain tank 34 is connected to the discharge port at the lower end. An opening 37 provided on the side surface of the lower furnace body 2 near the exhaust port of the slanted bottom plate 33 is connected to a vacuum type blower P2 disposed inside the casing 1 via an intake pipe 38, while an exhaust port of the blower P2 is It is connected to the lower end of an exhaust pipe 39 extending upward along the inner wall of the casing 1, and the upper end of the exhaust pipe 39 projects upwardly to the outside of the casing 1, and an adsorption filter 41 for adsorbing radioactive substances is installed therein. Connected to the duct 40.
なお、第1図中に示す符号T1,T2,T3,
は炉体2の各部に配設した温度検知器であり、本
装置の後述する作動時における炉体2の各部の温
度を検知するためのもので、温度検知器T1は気
化部に、温度検知器T2は燃焼室8と触媒体23
間に、温度検知器T3は気化燃焼部3と熱交換部
4間にそれぞれ付設してある。またT4は液化部
5の循環パイプ31の温度を検知する冷却水の温
度検知器、T5は排気管39に付設する排ガス温
度検知器である。 Note that the symbols T1, T2, T3, shown in FIG.
T1 is a temperature sensor installed in each part of the furnace body 2, and is used to detect the temperature of each part of the furnace body 2 during operation, which will be described later. The vessel T2 includes the combustion chamber 8 and the catalyst body 23.
In between, temperature detectors T3 are attached between the vaporization combustion section 3 and the heat exchange section 4, respectively. Further, T4 is a cooling water temperature detector that detects the temperature of the circulation pipe 31 of the liquefaction section 5, and T5 is an exhaust gas temperature detector attached to the exhaust pipe 39.
次に上記のように構成した本装置の操作および
作動について説明する。 Next, the operation and operation of the apparatus configured as described above will be explained.
被処理液、例えば液体シンチレーターの廃液を
処理するには、始めに、気化用空気の供給ポンプ
P1と液化部5の開口37と連結するプロワーP
2を一定時間作動させると、気化用空気の供給ポ
ンプP1の作動により供給管21の開口端から混
合筒11内へ空気が送られ、この空気が気化部材
10を通る際、気化部材10に残留していた前回
作動時の気化ガスを燃焼室8へ送り出す一方、ブ
ロワーP2の作動によつてケーシング1の外部の
空気が、空気取入口30、空気吸入口29を経て
空気導入口から燃焼室8内へ入り、前記残留気化
ガスと混じつて、さらに炉体2内部を下降して炉
体2内全体にある他の残留物もいつしよに、下部
炉体2たる液化部5に設けた開口37から吸気管
38、ブロワーP2の排気管39、ダクト40を
経て排出され、残留気化ガガス等の排除をなす。 In order to treat the liquid to be treated, for example, the waste liquid of a liquid scintillator, first, a pump P1 for supplying vaporizing air and a blower P connected to the opening 37 of the liquefaction section 5 are used.
2 is operated for a certain period of time, air is sent from the open end of the supply pipe 21 into the mixing cylinder 11 by the operation of the vaporizing air supply pump P1, and when this air passes through the vaporizing member 10, it remains in the vaporizing member 10. While the vaporized gas from the previous operation is sent to the combustion chamber 8, air from outside the casing 1 is sent from the air inlet to the combustion chamber 8 via the air intake port 30 and the air intake port 29 by the operation of the blower P2. The remaining gas enters the inside of the furnace body 2, mixes with the residual vaporized gas, and further descends inside the furnace body 2, and other residues present throughout the furnace body 2 also pass through the opening provided in the liquefaction section 5, which is the lower furnace body 2. 37, the air is discharged through an intake pipe 38, an exhaust pipe 39 of the blower P2, and a duct 40, and residual vaporized gas and the like are removed.
次にブロワーP2を停止し、始動用ヒーターH
2を作動して気化部材10の予熱を行うととも
に、始動用ヒーターH1を作動させて燃焼室8内
および触媒体23の予熱も行う。 Next, stop blower P2, and start heater H.
2 to preheat the vaporizing member 10, and also to preheat the inside of the combustion chamber 8 and the catalyst body 23 by operating the starting heater H1.
補助ヒーターH2に設けた温度検知器T2およ
び触媒体23の下方に設けた温度検知器T3がそ
れぞれの部位の燃焼における適正温度を検知確認
したところで、すなわち気化部材10、燃焼室8
および触媒体23がそれぞれ被処理液の気化ある
いは燃焼に必要な温度条件を充足したところで、
被処理液送り込み用のポンプP3を作動すると被
処理液タンク19から導入管20を通つて被処理
液が混合筒11内へ滴下する。該滴下された被処
理液は、供給管21からの空気によりバブリング
作用で気泡状となり、透孔12……から空気混合
気体となつて、補助ヒーターH2により加熱され
ている気化部材10中に入り、気化されて気化ガ
スとなる。該気化ガスは加熱されて燃焼室8内に
噴出し、始動用ヒーターH1によつて燃焼を始め
る。そして前記ブロワーP2に吸引されて下降す
る該燃焼ガスは触媒体23を通過する時、その不
完全燃焼成分を該触媒体23との反応によつて略
完全に燃焼するのである。なお、この燃焼時に
3H,14Cはそれぞれ水および炭酸ガスとなつて処
理される。 When the temperature sensor T2 provided on the auxiliary heater H2 and the temperature sensor T3 provided below the catalyst body 23 detect and confirm the appropriate temperature for combustion in each part, that is, the vaporization member 10 and the combustion chamber 8.
When the catalyst body 23 satisfies the temperature conditions necessary for vaporizing or burning the liquid to be treated,
When the pump P3 for feeding the liquid to be treated is operated, the liquid to be treated drops into the mixing cylinder 11 from the liquid to be treated tank 19 through the introduction pipe 20. The dropped liquid to be treated becomes bubble-like due to the bubbling effect of the air from the supply pipe 21, becomes an air mixture gas through the through holes 12, and enters the vaporizing member 10 heated by the auxiliary heater H2. , is vaporized and becomes vaporized gas. The vaporized gas is heated and ejected into the combustion chamber 8, and combustion is started by the starting heater H1. When the combustion gas sucked into the blower P2 and descending passes through the catalyst body 23, its incompletely combusted components are almost completely combusted by reaction with the catalyst body 23. In addition, during this combustion
3 H and 14 C are processed into water and carbon dioxide, respectively.
一旦燃焼が始まると、熱交換部4内を高温の燃
焼ガスが通る時、内板22を介して燃焼用空気に
該燃焼ガスの熱が伝わり、始動用ヒーターH1を
切つても、燃焼室内は安定した燃焼状態を維持す
るための適正温度に保たれるのである。また前記
燃焼始動操作にあつては、燃焼室8および触媒体
23内を適温にまで加熱して安定した燃焼状態を
維持するまでの予備段階として、ダンパー9の開
閉度の調整に応じたブロワーP2による燃焼室8
への供給空気量と始動用ヒーターH1の発熱量と
の割合を適宜調整し、またブロワーP2と始動用
ヒーターH1との作動を交互に適宜時間ずつ行う
ことによつて、始動用ヒーターH1の発熱量を最
小限に押さえながら前記燃焼室8および触媒体2
3の温度制御を行う。そして、炉体2内の各部に
設けた温度検知器T2がまえもつて規定した温度
を表示した時点で始動用ヒーターH1を切る。つ
まり、始動用ヒーターH1を切つても、燃焼室8
内は安定した燃焼状態を維持するための適正温度
に保たれている。 Once combustion starts, when high-temperature combustion gas passes through the heat exchanger 4, the heat of the combustion gas is transferred to the combustion air via the inner plate 22, and even if the starting heater H1 is turned off, the combustion chamber remains The temperature is maintained at an appropriate level to maintain stable combustion conditions. In addition, in the combustion starting operation, as a preliminary step until the inside of the combustion chamber 8 and the catalyst body 23 are heated to an appropriate temperature and a stable combustion state is maintained, the blower P2 is operated according to the adjustment of the opening/closing degree of the damper 9. Combustion chamber 8
The heat generated by the starting heater H1 can be reduced by adjusting the ratio of the amount of air supplied to the starting heater H1 and the amount of heat generated by the starting heater H1, and by alternately operating the blower P2 and the starting heater H1 for an appropriate amount of time. The combustion chamber 8 and the catalyst body 2 while keeping the amount to a minimum
3. Perform temperature control. Then, when the temperature detectors T2 provided in various parts of the furnace body 2 display a predetermined temperature, the starting heater H1 is turned off. In other words, even if the starting heater H1 is turned off, the combustion chamber 8
The inside temperature is maintained at the appropriate temperature to maintain stable combustion conditions.
前記炉体2内を下降する燃焼ガスは、熱交換部
4にてその温度を一旦下げられ、さらに下降して
液化部5に入ると、循環パイプ31内を循環する
冷却水によつてさらに低温に冷やされる。ここ
で、前記燃焼によつて規制値以下にされた3Hを
含んだだ水素の燃焼物たる水分は液化され回収タ
ンク35に収納され、また、14Cを含んだ炭素は
炭酸ガスとなつて気化部の開口37より吸気管3
8へ吸気され、排気管39を通つてダクト40へ
排気される。 The temperature of the combustion gas descending within the furnace body 2 is lowered once in the heat exchange section 4, and when it further descends and enters the liquefaction section 5, it is further lowered to a lower temperature by the cooling water circulating within the circulation pipe 31. cooled down to Here, water, which is a combustion product of hydrogen containing 3 H, which has been reduced to below the regulation value by the combustion, is liquefied and stored in the recovery tank 35, and carbon containing 14 C is converted into carbon dioxide gas. Intake pipe 3 from opening 37 of the vaporizing section
Air is taken in to the duct 8 and exhausted to the duct 40 through the exhaust pipe 39.
被処理液タンク19内の全廃液が燃焼処理を終
えたら、補助ヒーターH2と被処理液送用のポン
プP3を停止し、温度検知器T1、温度検知器T
3および排気ガス温度検知器T5がそれぞれの規
定温度を検知確認するまでポンプP1とブロワー
P2の作動を所定時間継続して気化部材10およ
び炉体2内の残留ガスを排気する。残留ガスの排
気後に前記ポンプP1を停止し、次いで温度検知
器T2、温度検知器T3にて触媒体23の上下部
位の温度を確認した上でブロワーP2を停止する
ものである。 When all the waste liquid in the liquid to be treated tank 19 has been burned, the auxiliary heater H2 and the pump P3 for feeding the liquid to be treated are stopped, and the temperature detector T1 and the temperature detector T are turned off.
The operation of the pump P1 and the blower P2 is continued for a predetermined period of time until the respective specified temperatures are detected and confirmed by the exhaust gas temperature detector T5 and the exhaust gas temperature detector T5, thereby exhausting the residual gas in the vaporizing member 10 and the furnace body 2. After exhausting the residual gas, the pump P1 is stopped, and then the temperature of the upper and lower portions of the catalyst body 23 is checked using the temperature detector T2 and the temperature sensor T3, and then the blower P2 is stopped.
以上のように本発明は、炉体の上部に配置し、
被処理液を、空気と混合したのち気化させる気化
部、該気化部からの気化ガスを燃焼させる燃焼
室、該燃焼室から排出される燃焼ガスの通路に位
置して設け、該燃焼ガス中の不完全燃焼成分を完
全燃焼させるための触媒体、とからなる気化燃焼
部と、炉体の中央部に位置し、かつ前記気化燃焼
部の触媒体に連接して設け、内板によつて形成さ
れる前記気化燃焼部からの燃焼ガスを通過させる
通路を備える一方、前記内板とその外周を囲む外
板との間で形成される前記燃焼室に連通する空気
導入路を備えた熱交換部と、炉体の下部に配置
し、かつ前記熱交換部の燃焼ガスを通過させる通
路に連接して設け、前記熱交換部からの燃焼ガス
を冷却液化する冷却機構を備える液化部とから構
成した放射性物質を含む廃液の処理装置におい
て、前記気化燃焼部における気化部は、外周部に
補助ヒーターを付設した耐熱性を有する多孔性物
質で形成した気化部材と、前記気化部材の内部に
配置し、周面に任意数個の透孔を穿設した混合筒
とを備え、該混合筒内には、前記被処理液を送り
込むための被処理液の送入管と、前記被処理液中
で気泡を生じさせるべく空気を送り込むための供
給管との開口端をそれぞれ配置して構成したの
で、放射性物質を含む廃液を、確実に気化できる
とともに完全に燃焼でき、有害なスス等を生じる
ことなく処理できる。また、従来の大型の電気炉
や耐火レンガ炉に比べ全体をコンパクトにするこ
とができ、設置面積も少なくて済み、ラジオアイ
ソトープ研究所、実験室や病院等のそれぞれに無
理なく設置することが可能となり、これらの施設
において、自ら放射性物質を含んだ廃液の処理を
安全かつ簡単に行えるようになる等の効果を奏す
るものである。 As described above, the present invention is arranged in the upper part of the furnace body,
A vaporization section that mixes the liquid to be treated with air and then vaporizes it; a combustion chamber that burns the vaporized gas from the vaporization section; and a combustion chamber that burns the vaporized gas from the combustion chamber. a catalytic body for completely combusting incompletely burned components; and a catalytic combustion part located in the center of the furnace body and connected to the catalytic body of the evaporative combustion part, and formed by an inner plate. a heat exchange section that includes a passage through which combustion gas from the vaporization combustion section is passed, and an air introduction passage that communicates with the combustion chamber formed between the inner plate and an outer plate surrounding the outer periphery thereof; and a liquefaction section, which is disposed at the lower part of the furnace body and connected to a passage through which the combustion gas of the heat exchange section passes, and includes a cooling mechanism that cools and liquefies the combustion gas from the heat exchange section. In an apparatus for treating waste liquid containing radioactive substances, the vaporizing section in the vaporizing combustion section includes a vaporizing member formed of a heat-resistant porous material with an auxiliary heater attached to the outer periphery, and disposed inside the vaporizing member, It is equipped with a mixing cylinder having an arbitrary number of through holes bored in its circumferential surface, and inside the mixing cylinder there is a feed pipe for the liquid to be treated for feeding the liquid to be treated, and an air bubble in the liquid to be treated. Since the opening ends of the supply pipes for sending air are arranged in order to produce a can. Additionally, the overall structure can be made more compact than conventional large electric furnaces and firebrick furnaces, requiring less installation space and can be easily installed in radioisotope research laboratories, laboratories, hospitals, etc. This has the effect of allowing these facilities to safely and easily dispose of waste liquid containing radioactive materials themselves.
第1図は部分を縦断して示す正面図、第2図は
横断平面図、第3図は要部の拡大縦断面図であ
る。
1……ケーシング、2……炉体、3……気化燃
焼部、4……熱交換部、5……液化部、8……燃
焼室、9……ダンパー、10……気化部材、11
……混合筒、12……透孔、15……受け皿、1
9……被処理液タンク、20……送入管、21…
…供給管、23……触媒体、29……空気吸入
口、31……循環パイプ、P1,P3……ポン
プ、P2……ブロワー、T1,T2,T3,T
4,T5……温度検知器、H1……始動用ヒータ
ー、H2……補助ヒーター。
FIG. 1 is a front view showing a section longitudinally, FIG. 2 is a cross-sectional plan view, and FIG. 3 is an enlarged vertical sectional view of the main part. DESCRIPTION OF SYMBOLS 1... Casing, 2... Furnace body, 3... Vaporization combustion section, 4... Heat exchange section, 5... Liquefaction section, 8... Combustion chamber, 9... Damper, 10... Vaporization member, 11
...Mixing tube, 12...Through hole, 15...Saucer, 1
9...Liquid tank to be treated, 20...Feed pipe, 21...
... Supply pipe, 23 ... Catalyst body, 29 ... Air intake port, 31 ... Circulation pipe, P1, P3 ... Pump, P2 ... Blower, T1, T2, T3, T
4, T5...temperature detector, H1...starting heater, H2...auxiliary heater.
Claims (1)
合したのち気化させる気化部、該気化部からの気
化ガスを燃焼させる燃焼室、該燃焼室から排出さ
れる燃焼ガスの通路に位置して設け、該燃焼ガス
中の不完全燃焼成分を完全燃焼させるための触媒
体、とからなる気化燃焼部と、炉体の中央部に位
置し、かつ前記気化燃焼部の触媒体に連接して設
け、内板によつて形成される前記気化燃焼部から
の燃焼ガスを通過させる通路を備える一方、前記
内板とその外周を囲む外板との間で形成される前
記燃焼室に連通する空気導入路を備えた熱交換部
と、炉体の下部に配置し、かつ前記熱交換部の燃
焼ガスを通過させる通路に連接して設け、前記熱
交換部からの燃焼ガスを冷却液化する冷却機構を
備える液化部とから構成した放射性物質を含む廃
液の処理装置において、前記気化燃焼部における
気化部は、外周部に補助ヒーターを付設した耐熱
性を有する多孔性物質で形成した気化部材と、前
記気化部材の内部に配置し、周面に任意数個の透
孔を穿設した混合筒とを備え、該混合筒内には、
前記被処理液を送り込むための被処理液の送入管
と、前記被処理液中で気泡を生じさせるべく空気
を送り込むための供給管との開口端をそれぞれ配
置して構成したことを特徴とする放射性物質を含
む廃液の処理装置。1. A vaporization section located in the upper part of the furnace body to vaporize the liquid to be treated after mixing it with air, a combustion chamber that combusts the vaporized gas from the vaporization section, and a passageway for the combustion gas discharged from the combustion chamber. a catalytic combustion section for completely combusting incompletely burned components in the combustion gas; The combustion chamber is provided with a passage through which combustion gas from the vaporization combustion section formed by the inner plate passes, and communicates with the combustion chamber formed between the inner plate and an outer plate surrounding the outer periphery thereof. A heat exchange section provided with an air introduction passage, and a cooling device disposed at the lower part of the furnace body and connected to a passage through which the combustion gas of the heat exchange section passes, cooling and liquefying the combustion gas from the heat exchange section. In an apparatus for treating waste liquid containing radioactive materials, the vaporization section in the vaporization combustion section includes a vaporization member formed of a heat-resistant porous material with an auxiliary heater attached to the outer circumference; a mixing cylinder disposed inside the vaporizing member and having an arbitrary number of through holes bored in the circumferential surface, and inside the mixing cylinder,
A feed tube for the liquid to be treated for feeding the liquid to be treated and a supply tube for feeding air to generate bubbles in the liquid to be treated are configured so that their open ends are respectively arranged. Equipment for treating waste liquid containing radioactive materials.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10730681A JPS589099A (en) | 1981-07-09 | 1981-07-09 | Processing device for liquid waste having radioactive material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP10730681A JPS589099A (en) | 1981-07-09 | 1981-07-09 | Processing device for liquid waste having radioactive material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS589099A JPS589099A (en) | 1983-01-19 |
| JPS6127720B2 true JPS6127720B2 (en) | 1986-06-26 |
Family
ID=14455736
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP10730681A Granted JPS589099A (en) | 1981-07-09 | 1981-07-09 | Processing device for liquid waste having radioactive material |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS589099A (en) |
-
1981
- 1981-07-09 JP JP10730681A patent/JPS589099A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS589099A (en) | 1983-01-19 |
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