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JPH0226757B2 - - Google Patents
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JPH0226757B2 - - Google Patents

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Publication number
JPH0226757B2
JPH0226757B2 JP4580282A JP4580282A JPH0226757B2 JP H0226757 B2 JPH0226757 B2 JP H0226757B2 JP 4580282 A JP4580282 A JP 4580282A JP 4580282 A JP4580282 A JP 4580282A JP H0226757 B2 JPH0226757 B2 JP H0226757B2
Authority
JP
Japan
Prior art keywords
temperature
radioactive waste
waste slurry
dry powder
heater
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
Application number
JP4580282A
Other languages
Japanese (ja)
Other versions
JPS58162898A (en
Inventor
Fumio Tajima
Mikio Wada
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.)
Toshiba Corp
Original Assignee
Tokyo Shibaura Electric 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 Tokyo Shibaura Electric Co Ltd filed Critical Tokyo Shibaura Electric Co Ltd
Priority to JP4580282A priority Critical patent/JPS58162898A/en
Publication of JPS58162898A publication Critical patent/JPS58162898A/en
Publication of JPH0226757B2 publication Critical patent/JPH0226757B2/ja
Granted legal-status Critical Current

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  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Heat Treatment Of Water, Waste Water Or Sewage (AREA)
  • Excavating Of Shafts Or Tunnels (AREA)

Description

【発明の詳細な説明】 〔発明の技術分野〕 本発明は原子力発電所から排出される使用済樹
脂および硫酸ナトリウムを主成分とする化学再生
廃液、洗濯廃液等の放射性廃液スラリーを乾燥さ
せて、その水分を蒸発させ固形分を乾燥粉体化さ
せる放射性廃棄物処理装置に関する。
[Detailed Description of the Invention] [Technical Field of the Invention] The present invention is a method of drying radioactive waste liquid slurry such as chemical regeneration waste liquid, laundry waste liquid, etc., which is mainly composed of spent resin and sodium sulfate discharged from a nuclear power plant, and The present invention relates to a radioactive waste processing apparatus that evaporates water and converts solid content into dry powder.

〔発明の技術的背景とその問題点〕[Technical background of the invention and its problems]

従来、放射性廃液スラリーを固化するためセメ
ント固化法が行なわれていた。
Conventionally, cement solidification methods have been used to solidify radioactive waste slurry.

ところが、このセメント固化法はドラム缶中に
放射性廃液スラリーとセメントとを一緒に充填し
て固化させるものであつたから、減容性が悪いと
いう不都合があつた。
However, this cement solidification method involved filling a drum with radioactive waste liquid slurry and cement and solidifying it, which had the disadvantage of poor volume reduction.

このため、特公昭55−33559号公報に示すよう
な放射性廃液スラリーを乾燥させ、その水分を蒸
発させ固形分を一定の含水率を有する乾燥粉体と
して得る処理方法が提案されている。
For this reason, a treatment method has been proposed, as disclosed in Japanese Patent Publication No. 55-33559, in which a radioactive waste slurry is dried, the water is evaporated, and the solid content is obtained as a dry powder having a constant moisture content.

ところが、前記公報記載の処理方法および処理
装置においては、乾燥粉体の含水率を知るために
乾燥粉体の温度を検知するのであるが、乾燥機の
加熱ジヤケツトおよびロータの間を加熱ジヤケツ
トにより加熱されつつ下降する放射性液体廃棄物
の温度を検知し、この検知温度を設定温度に一致
させるように処理するものであるから、次のよう
な欠点があつた。
However, in the processing method and processing apparatus described in the above publication, the temperature of the dry powder is detected in order to know the moisture content of the dry powder, but the temperature between the heating jacket and the rotor of the dryer is not heated by the heating jacket. The method detects the temperature of the radioactive liquid waste, which is decreasing as it is heated, and processes the detected temperature to match the set temperature, so it has the following drawbacks.

1 検知温度はまだ加熱ジヤケツトにより加熱さ
れている放射性液体廃棄物の温度であつて、乾
燥終了後の乾燥粉体の温度を検知したものでは
ない。
1. The detected temperature is the temperature of the radioactive liquid waste that is still being heated by the heating jacket, and is not the temperature of the dried powder after drying is completed.

また、加熱ジヤケツトへの供給蒸気の状態が
流量増大、温度上昇等のように変化した場合、
検知部位が加熱ジヤケツト部分でもあるため、
検知器が放射性液体廃棄物自身の温度ばかりで
なく外乱となる供給蒸気の状態変化をも検知し
てしまう。
Also, if the state of the steam supplied to the heating jacket changes, such as an increase in flow rate or a rise in temperature,
Since the detection part is also the heating jacket part,
The detector detects not only the temperature of the radioactive liquid waste itself, but also changes in the state of the supplied vapor that cause disturbances.

従つて、実際の放射性液体廃棄物の温度を検
知するものでないため、得られる乾燥粉体の状
態が所定の状態のものでなくなるおそれが大き
く、安定した処理を行なうことができず、更に
信頼性も劣るものであつた。
Therefore, since it does not detect the actual temperature of radioactive liquid waste, there is a high risk that the state of the dry powder obtained will not be the specified state, making it impossible to perform stable processing and further reducing reliability. It was also inferior.

2 加熱ジヤケツトとロータとの間を下降する放
射性液体廃棄物の温度を検知するためには、検
知器を極めて狭隘部に設けなければならず、し
かも正確に温度検知できるようにしなければな
らないので構造が複雑となる。また、検知器へ
加熱ジヤケツトから直接熱が伝わるので、検知
誤差の要因となる熱応力が検知器やその周辺の
構成部分に生じてしまう。
2. In order to detect the temperature of the radioactive liquid waste that descends between the heating jacket and the rotor, the detector must be installed in an extremely narrow space, and the structure must be designed so that it can accurately detect the temperature. becomes complicated. Furthermore, since heat is directly transmitted to the detector from the heating jacket, thermal stress, which causes detection errors, is generated in the detector and its surrounding components.

〔発明の目的〕[Purpose of the invention]

本発明はこのような点に鑑みてなされたもので
あり、乾燥終了後に得られた乾燥粉体自身の温度
を検知することができ、しかも加熱用の蒸気の状
態変化に影響を受けることなく正確に乾燥粉体自
身の温度を検出することができ、確実に検出温度
即ち乾燥粉体の温度を設定温度に一致させること
ができ、制御動作が安定され、信頼性が高く、更
に構造が簡単である放射性廃棄物処理装置を提供
することを目的とする。
The present invention has been made in view of these points, and is capable of detecting the temperature of the dried powder itself obtained after drying is completed, and moreover, is able to accurately detect the temperature of the dried powder itself without being affected by changes in the state of the heating steam. The temperature of the dry powder itself can be detected, and the detected temperature, that is, the temperature of the dry powder, can be reliably matched to the set temperature, and the control operation is stable and reliable, and the structure is simple. The purpose is to provide a certain radioactive waste treatment equipment.

〔発明の概要〕[Summary of the invention]

本発明は、乾燥終了後の乾燥粉体自身の温度を
加熱蒸気の状態に影響されることなく正確に検知
するために温度検知器を乾燥機の加熱器より下方
のコーン部分に設け、この温度検知器によつて正
確に測定された検知温度を設定温度に一致させる
制御装置を設けて形成されている。
In order to accurately detect the temperature of the dried powder itself after drying is completed without being affected by the state of the heating steam, the present invention provides a temperature sensor in the cone section below the heater of the dryer, and detects the temperature. A control device is provided to match the detected temperature accurately measured by the detector to the set temperature.

〔発明の実施例〕[Embodiments of the invention]

以下、図面により本発明の実施例を説明す。 Embodiments of the present invention will be described below with reference to the drawings.

第1図は本発明の放射性廃棄物処理装置の系統
図であり、図中、符号1は上下に長い乾燥機であ
る。この乾燥機1は、第2図に詳細が示されてお
り、その中間部内側に円筒状の加熱器2が設けら
れている。この加熱器2には熱源となる加熱蒸気
を供給するために、途中に加熱蒸気流量調整弁3
を有する加熱蒸気供給管4が接続されており、ま
た、加熱に供された加熱蒸気を排出する排出管5
が接続されている。この加熱器2の内側には乾燥
機1の頂部に設けられたモータ6によつて回転駆
動される回転ロータ7が設けられている。また、
乾燥機1には、加熱器2より上部に放射性廃液ス
ラリーが供給されて来る流入口8と、乾燥時に発
生する蒸気を排出する流出口9とが設けられてお
り、一方、その加熱器2より下方には加熱器2と
回転ロータ7との間から落下する乾燥粉体、即ち
放射性廃液スラリー中の固形分を集合して排出せ
しめる漏斗状のコーン部10が設けられている。
FIG. 1 is a system diagram of a radioactive waste treatment apparatus according to the present invention, and in the figure, reference numeral 1 indicates a vertically long dryer. The details of this dryer 1 are shown in FIG. 2, and a cylindrical heater 2 is provided inside the middle part. In order to supply heating steam as a heat source to this heater 2, there is a heating steam flow rate regulating valve 3 in the middle.
A heating steam supply pipe 4 is connected thereto, and a discharge pipe 5 for discharging the heated steam provided for heating
is connected. A rotating rotor 7 is provided inside the heater 2 and is driven to rotate by a motor 6 provided at the top of the dryer 1 . Also,
The dryer 1 is provided with an inlet 8 through which radioactive waste slurry is supplied above the heater 2 and an outlet 9 through which steam generated during drying is discharged. A funnel-shaped cone portion 10 is provided below to collect and discharge dry powder, that is, solid content in the radioactive waste slurry, that falls between the heater 2 and the rotating rotor 7.

前記流入口8を通して放射性廃液スラリーを乾
燥機1中へ供給する放射性廃液スラリー供給装置
11として、給液タンク12と、途中に給液ポン
プ13および放射性廃液スラリー供給量調整弁1
4とを有する供給路15とが設けられている。
A radioactive waste slurry supply device 11 that supplies radioactive waste slurry into the dryer 1 through the inlet 8 includes a liquid supply tank 12, a liquid supply pump 13 on the way, and a radioactive waste slurry supply amount adjustment valve 1.
A supply channel 15 having 4 is provided.

また、前記コーン部10には加熱器2と回転ロ
ータ7との間から落下して来る乾燥粉体の温度を
検出して検出温度信号16aを発する複数の温度
検出器16,16が設けられている。この温度検
出器16により乾燥粉体が流下する部分の雰囲気
温度を検出して乾燥粉体自身の温度を知ることに
より、その乾燥粉体の含水率を知ることができ
る。これは、乾燥粉体の検出温度と乾燥粉体の含
水率との関係をカールフイツシヤー法により測定
したところ、第3図に示す使用済樹脂および濃縮
廃液の場合の線図のように一定の関係があること
から求められた。従つて、乾燥粉体の含水率を一
定に保つには、乾燥粉体の温度検出器16による
検出温度を設定温度の範囲に保持させればよい。
Further, the cone portion 10 is provided with a plurality of temperature detectors 16, 16 for detecting the temperature of the dry powder falling from between the heater 2 and the rotating rotor 7 and emitting a detected temperature signal 16a. There is. The moisture content of the dry powder can be determined by detecting the atmospheric temperature of the part where the dry powder flows down using the temperature detector 16 and knowing the temperature of the dry powder itself. When the relationship between the detected temperature of the dry powder and the moisture content of the dry powder was measured using the Karl Fischer method, it was found that the relationship between the detected temperature of the dry powder and the moisture content of the dry powder was determined to be constant as shown in the diagram for used resin and concentrated waste liquid shown in Figure 3. It was requested because of the relationship. Therefore, in order to keep the moisture content of the dry powder constant, the temperature detected by the dry powder temperature detector 16 may be maintained within the set temperature range.

本発明は乾燥粉体の含水率を一定に保持するた
めに、乾燥粉体の温度を設定温度に保持させる制
御装置19を設けている。この制御装置19は、
温度検出器16から送られて来る検出温度信号1
6aと設定温度とを比較し、その差を零にして乾
燥粉体の温度を設定温度と一致させるように放射
性廃液スラリー供給量調整弁14および加熱蒸気
流量調整弁3を開閉させる開閉信号19aを発す
る。即ち、乾燥粉体の温度を制御するために、乾
燥機1への放射性廃液スラリーの供給量を制御す
るとともに、加熱器2による加熱温度を制御する
ため加熱蒸気流量を制御するようにしたものであ
る。
The present invention is provided with a control device 19 that maintains the temperature of the dry powder at a set temperature in order to maintain the moisture content of the dry powder constant. This control device 19 is
Detected temperature signal 1 sent from temperature detector 16
6a and the set temperature, and sends an opening/closing signal 19a to open and close the radioactive waste slurry supply amount adjustment valve 14 and the heating steam flow rate adjustment valve 3 so that the difference becomes zero and the temperature of the dry powder matches the set temperature. emanate. That is, in order to control the temperature of the dry powder, the amount of radioactive waste liquid slurry supplied to the dryer 1 is controlled, and the heating steam flow rate is controlled to control the heating temperature by the heater 2. be.

乾燥機1のコーン部10から排出された乾燥粉
体は、移送装置17によつて集積ホツパ18内に
貯められ、その後、放射性廃棄物の固化処理部お
よびドラム缶への充填処理部(共に図示せず)に
送られる。
The dry powder discharged from the cone section 10 of the dryer 1 is stored in a collection hopper 18 by a transfer device 17, and then transferred to a radioactive waste solidification processing section and a drum filling processing section (both not shown). sent to ).

また、上部の流出口9からは放射性廃液スラリ
ー中の水分が蒸気として排出流路20を経て排出
され、復水器21において復水せしめられる。
Further, from the upper outlet 9, the water in the radioactive waste slurry is discharged as steam through the discharge channel 20, and is condensed in the condenser 21.

次に、本実施例の作用を説明する。 Next, the operation of this embodiment will be explained.

給液タンク12内に貯留された放射性廃液スラ
リーは、放射性廃液スラリー供給量調整弁14を
開き、給液ポンプ13を駆動することにより、供
給路15を通り、流入口8を経て乾燥機1の上部
へ供給され得る。この際、乾燥機1においては加
熱蒸気流量調整弁3を開いて加熱蒸気供給管4か
ら加熱蒸気が加熱器2内に供給されており、また
回転ロータ7がモータ6により回転させられてい
る。よつて、乾燥機1内に供給された放射性廃液
スラリーは加熱器2と回転ロータ7との間を順に
流下して行く。その流下の間に放射性廃液スラリ
ーは加熱器2により加熱され、水分が蒸発され、
流出口9から排出流路20へ排出される。そし
て、その乾燥を受けつつ流下する放射性廃液スラ
リー中の固形分は徐々にその含水率が低くなり、
加熱器2と回転ロータ7との間の最下部ではほと
んど乾燥が終了し乾燥粉体となつている。
The radioactive waste liquid slurry stored in the liquid supply tank 12 is fed to the dryer 1 through the supply path 15 by opening the radioactive waste liquid slurry supply amount adjustment valve 14 and driving the liquid supply pump 13. Can be fed to the top. At this time, in the dryer 1, the heated steam flow rate adjustment valve 3 is opened to supply heated steam into the heater 2 from the heated steam supply pipe 4, and the rotating rotor 7 is rotated by the motor 6. Therefore, the radioactive waste liquid slurry supplied into the dryer 1 flows down between the heater 2 and the rotating rotor 7 in order. During the flow, the radioactive waste liquid slurry is heated by the heater 2, water is evaporated,
It is discharged from the outlet 9 to the discharge channel 20 . As the solid content in the radioactive waste slurry flows down as it dries, its moisture content gradually decreases.
At the lowest part between the heater 2 and the rotating rotor 7, drying is almost completed and the powder is a dry powder.

この乾燥粉体は加熱器2と回転ロータ7との間
から、コーン部10内に自由落下する。そして、
コーン部10内において温度検出器16,16に
より落下中の乾燥粉体の温度が検出される。この
際コーン部10は加熱器2と離れているので、温
度検出器16は加熱器2の温度状態によつて影響
されることなく真の乾燥粉体自身の温度を検出す
ることができる。また、コーン部10は加熱器2
より直径が小さいので、少ない個数の温度検出器
16によつて正確に乾燥粉体の温度を検出するこ
とができる。
This dry powder falls freely into the cone portion 10 from between the heater 2 and the rotating rotor 7. and,
Inside the cone section 10, temperature detectors 16 detect the temperature of the falling dry powder. At this time, since the cone portion 10 is separated from the heater 2, the temperature detector 16 can detect the true temperature of the dry powder itself without being affected by the temperature state of the heater 2. Further, the cone portion 10 is connected to the heater 2
Since the diameter is smaller, the temperature of the dry powder can be accurately detected using a smaller number of temperature detectors 16.

そして、制御装置19においては、温度検出器
16から送られて来る検出温度信号16aと設定
温度とを比較し、検出温度が低い場合には、含水
率が高過ぎるので加熱蒸気流量調整弁3に開度を
大きくする開閉信号19aを送つて加熱器2によ
る加熱能力を大きくするとともに、放射性廃液ス
ラリー供給量調整弁14へ開度を小さくする開閉
信号19aを送つて乾燥機1中への放射性廃液ス
ラリーの供給量を少なくする。これにより、乾燥
粉体の温度が、徐々に上昇し、検出温度が設定温
度に一致すると、制御装置19は、両調整弁3,
14の弁開度を現在の状態で保持する開閉信号1
9aをそれぞれ送る。一方、検出温度が設定温度
より高い場合には含水率が低過ぎるので、前記と
は逆に加熱蒸気流量調整弁3の弁開度を小さくす
る開閉信号19aを送るとともに、放射性廃液ス
ラリー供給量調整弁14の弁開度を大きくする開
閉信号を送る。
Then, the control device 19 compares the detected temperature signal 16a sent from the temperature detector 16 with the set temperature, and if the detected temperature is low, the water content is too high, so the heated steam flow rate regulating valve 3 is The opening/closing signal 19a that increases the opening degree is sent to increase the heating capacity of the heater 2, and the opening/closing signal 19a that decreases the opening degree is sent to the radioactive waste liquid slurry supply amount adjustment valve 14 to prevent the radioactive waste liquid from flowing into the dryer 1. Reduce the amount of slurry supplied. As a result, the temperature of the dry powder gradually rises, and when the detected temperature matches the set temperature, the control device 19 controls both the regulating valves 3,
Opening/closing signal 1 that maintains the valve opening degree of 14 in the current state
Send 9a each. On the other hand, if the detected temperature is higher than the set temperature, the water content is too low, so contrary to the above, an opening/closing signal 19a is sent to reduce the valve opening of the heated steam flow rate adjustment valve 3, and the supply amount of radioactive waste slurry is adjusted. An opening/closing signal is sent to increase the opening degree of the valve 14.

このように制御装置19の動作により一定の含
水率とされた乾燥粉体が得られる。
In this manner, dry powder having a constant moisture content is obtained by the operation of the control device 19.

この乾燥粉体はその後コーン部10を流出し、
移送装置17上に落下し、集積ホツパ18へ向け
て送られる。
This dry powder then flows out of the cone section 10,
It falls onto the transfer device 17 and is sent towards the collection hopper 18.

なお、上記の制御装置19による制御の一方法
として設定温度を125〜135℃にすれば、第3図に
示すように使用済樹脂の場合の含水率は5重量%
となり、濃縮廃液の場合の含水率は0.3重量%と
なり、十分な乾燥状態となることがわかる。
If the temperature is set to 125 to 135°C as a control method using the control device 19, the moisture content of the used resin will be 5% by weight as shown in Fig. 3.
Therefore, the water content in the case of concentrated waste liquid is 0.3% by weight, indicating that it is in a sufficiently dry state.

〔発明の効果〕〔Effect of the invention〕

このように本発明は構成されるから次のような
効果を奏する。
Since the present invention is configured in this manner, it produces the following effects.

1 温度検出器を乾燥機のコーン部に設けたの
で、加熱器と回転ロータとの間から落下して来
る乾燥粉体自身の温度を検出できる。従つて、
その検出温度は加熱器の温度等の外乱が入るこ
となく正確に乾燥粉体の温度となり、制御器に
より設定温度と比較され、確実に乾燥粉体を設
定温度に一致することができ、一定の含水率の
乾燥粉体を得ることができる。
1. Since the temperature sensor is installed in the cone of the dryer, it is possible to detect the temperature of the dry powder itself falling from between the heater and the rotating rotor. Therefore,
The detected temperature accurately becomes the temperature of the dry powder without disturbances such as the temperature of the heater, and is compared with the set temperature by the controller, ensuring that the dry powder temperature matches the set temperature and maintains a constant temperature. A dry powder with a high moisture content can be obtained.

2 加熱器への加熱蒸気の供給量が急変して、加
熱温度が急激に変化しても、その変化に影響さ
れることなく乾燥粉体自身の温度を検出するこ
とができるので、加熱蒸気供給量を変化させる
含水率制御を容易に行なうことができる。
2 Even if the heating temperature changes suddenly due to a sudden change in the amount of heating steam supplied to the heater, the temperature of the dry powder itself can be detected without being affected by the change, so the temperature of the dry powder itself can be detected without being affected by the change. Moisture content can be easily controlled by changing the amount.

3 温度制御による乾燥粉体の含水率制御を安定
的に行なうことができ、動作の信頼性が高くな
る。
3. Moisture content of dry powder can be stably controlled by temperature control, increasing operational reliability.

4 温度検出器を従来のように加熱器と回転ロー
タとの狭隘部に設けないで、広いコーン部に設
けるものであり、更に、その個数が少なくても
乾燥粉体の温度を正確に検出できるものである
から、構造が簡単であり、修理等も容易に行な
うことができる。
4 The temperature detector is not installed in the narrow area between the heater and rotating rotor as in the past, but is installed in the wide cone area, and furthermore, the temperature of the dry powder can be accurately detected even if the number of sensors is small. Since it is a product, it has a simple structure and can be easily repaired.

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

図面は本発明の放射性廃棄物処理装置の一実施
例を示し、第1図は系統図、第2図は乾燥機の縦
断側面図、第3図は乾燥粉体の検出温度と含水率
との関係を示す特性図である。 1……乾燥機、2……加熱器、3……加熱蒸気
流量調整弁、7……回転ロータ、8……流入口、
9……流出口、10……コーン部、11……放射
性廃液スラリー供給装置、14……放射性廃棄ス
ラリー供給量調整装置、16……温度検出器、1
9……制御装置。
The drawings show an embodiment of the radioactive waste processing apparatus of the present invention, in which Fig. 1 is a system diagram, Fig. 2 is a vertical side view of the dryer, and Fig. 3 is a graph showing the relationship between detected temperature and moisture content of dry powder. It is a characteristic diagram showing a relationship. 1... Dryer, 2... Heater, 3... Heated steam flow rate adjustment valve, 7... Rotating rotor, 8... Inflow port,
9... Outlet, 10... Cone part, 11... Radioactive waste slurry supply device, 14... Radioactive waste slurry supply amount adjustment device, 16... Temperature detector, 1
9...control device.

Claims (1)

【特許請求の範囲】 1 上部の流入口から供給された放射性廃液スラ
リーを中間部に設けられた加熱器および回転ロー
タの間を下方に通過せしめて乾燥させ、前記放射
性廃液スラリー中の水分を蒸気として上部の流出
口から排出させるとともに固形分を乾燥粉体とし
て前記加熱器より下方に設けられたコーン部を通
して流出させる乾燥機と、 この乾燥機の前記流入口へ前記放射性廃液スラ
リーを供給する放射性廃液スラリー供給装置と、 前記乾燥機のコーン部内に設けられて前記加熱
器から落下する前記乾燥粉体の温度を検出する温
度検出器と、 この温度検出器による検出温度と乾燥粉体の設
定温度とを比較して、その検出温度が設定温度と
一致するように前記加熱器による加熱状態および
前記放射性廃液スラリー供給装置による放射性廃
液スラリー供給量を調整する制御装置と、 を有する放射性廃棄物処理装置。 2 加熱器は加熱蒸気を熱源とするとともにその
加熱蒸気流量を調整する加熱蒸気流量調整弁を有
し、 放射性廃液スラリー供給装置は放射性廃液スラ
リー供給量を調整する放射性廃液スラリー供給量
調整弁を有し、 制御装置は検出温度と設定温度とを比較する比
較器と、双方の温度の差を零とさせる開閉信号を
前記加熱蒸気流量調整弁および放射性廃液スラリ
ー供給量調整弁へ送る指令器とを有する、ことを
特徴とする特許請求の範囲第1項記載の放射性廃
棄物処理装置。
[Claims] 1. The radioactive waste slurry supplied from the upper inlet is passed downward between a heater and a rotating rotor provided in the middle to dry it, and the moisture in the radioactive waste slurry is vaporized. a radioactive waste slurry for supplying the radioactive waste slurry to the inlet of the dryer; a waste liquid slurry supply device; a temperature detector provided in the cone of the dryer to detect the temperature of the dry powder falling from the heater; the temperature detected by the temperature detector and the set temperature of the dry powder. a control device that adjusts the heating state of the heater and the amount of radioactive waste slurry supplied by the radioactive waste slurry supply device so that the detected temperature matches the set temperature; . 2 The heater uses heated steam as a heat source and has a heated steam flow rate adjustment valve that adjusts the flow rate of the heated steam, and the radioactive waste slurry supply device has a radioactive waste slurry supply amount adjustment valve that adjusts the amount of radioactive waste slurry supplied. The control device includes a comparator that compares the detected temperature and a set temperature, and a command device that sends an opening/closing signal to the heated steam flow rate adjustment valve and the radioactive waste slurry supply amount adjustment valve to make the difference between the two temperatures zero. A radioactive waste treatment apparatus according to claim 1, characterized in that it comprises:
JP4580282A 1982-03-23 1982-03-23 Radioactive waste processing device Granted JPS58162898A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4580282A JPS58162898A (en) 1982-03-23 1982-03-23 Radioactive waste processing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4580282A JPS58162898A (en) 1982-03-23 1982-03-23 Radioactive waste processing device

Publications (2)

Publication Number Publication Date
JPS58162898A JPS58162898A (en) 1983-09-27
JPH0226757B2 true JPH0226757B2 (en) 1990-06-12

Family

ID=12729394

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4580282A Granted JPS58162898A (en) 1982-03-23 1982-03-23 Radioactive waste processing device

Country Status (1)

Country Link
JP (1) JPS58162898A (en)

Also Published As

Publication number Publication date
JPS58162898A (en) 1983-09-27

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