JPS59164999A - Liquid waste neutralization device - Google Patents
Liquid waste neutralization deviceInfo
- Publication number
- JPS59164999A JPS59164999A JP3901183A JP3901183A JPS59164999A JP S59164999 A JPS59164999 A JP S59164999A JP 3901183 A JP3901183 A JP 3901183A JP 3901183 A JP3901183 A JP 3901183A JP S59164999 A JPS59164999 A JP S59164999A
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- neutralized
- neutralization
- neutralizing
- waste 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.)
- Pending
Links
Landscapes
- Physical Or Chemical Processes And Apparatus (AREA)
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】
〔発明の利用分野〕
本発明は原子力発電所から発生する廃液の中和装置に係
り、特に高放射線量の廃液全中和するのに好適な廃液中
和装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a neutralization device for waste liquid generated from a nuclear power plant, and particularly to a waste liquid neutralization device suitable for completely neutralizing waste liquid with a high radiation dose.
従来は中和液全廃液混合タンクへポンプにより圧送して
いたが、高放射線量下に於いてポンプの保守が問題で、
予備機の設置もあり多大な保守時間と被爆が発生する。Previously, the neutralized liquid was pumped to a mixing tank, but maintenance of the pump was a problem under high radiation levels.
There is also a backup machine installed, which requires a lot of maintenance time and exposure to radiation.
本発明の目的はポンプのような摩耗品を全くなくシ、保
守及び故障発生部全少なくした原子力発電所に好適なる
廃液中和装置を提供することにちる。An object of the present invention is to provide a waste liquid neutralization device suitable for a nuclear power plant, which is free of wear parts such as pumps, and has fewer maintenance and failure-prone parts.
1)中和装置の計量全バルブ操作により自重(重力によ
゛る自由落下ンにより行い、又、廃液混合タンクへの注
入も自由落下により行う。1) Measurement of the neutralization device is carried out by free fall by gravity (gravity) by operating all valves, and injection into the waste liquid mixing tank is also carried out by free fall.
2)廃液混合タンクへの注入を廃液の一部により圧送す
る。2) Pumping the injection into the waste liquid mixing tank with a portion of the waste liquid.
3)廃液混合タンクへの注入を廃液の一部によるジェッ
トポンプにより移送する。3) Transfer the injection into the waste liquid mixing tank by a jet pump with a portion of the waste liquid.
以下本発明の一実施例全第1図により説明する。 An embodiment of the present invention will be explained below with reference to FIG.
先ず、被中和廃液がバルブ17全介し、廃液混合タンク
に移送され、レベルケージ8により一定量測定され、そ
の信号によりバルブ17を閉止する。First, the waste liquid to be neutralized is transferred to the waste liquid mixing tank through all the valves 17, a certain amount is measured by the level cage 8, and the valve 17 is closed in response to the signal.
このとき、ポンプ11は停止パルプ19は閉止となって
いるパルプ17閉止と同時にポンプ11奢駆動し、廃液
全循環させる。このときバルブ18は開となっており廃
液は10サンプリング装置によf)PH’を測定さnそ
の信号が、中和コントローラー6に送信されて中和液量
全演算し、レベル装定装置5の測定信号にマツチした値
に換算する。一方中和液は、中和源3より中和タンク1
に移送され、レベルゲージ2により一定量蓄えられてい
る。中和コントローラ6からの信号により、バルブ13
”i=開、次にパル’7’12が開となり、中和液タン
ク\
1から中和液が自重により、中和液計量器4に移動し、
その量がレベル測定装置により計測されながらその信号
が中和コントローラ6に送信され゛る。At this time, the pump 11 is driven at the same time as the pulp 17 is closed while the stopped pulp 19 is closed, thereby completely circulating the waste liquid. At this time, the valve 18 is open, and the waste liquid is measured for PH' by the sampling device 10. The signal is sent to the neutralization controller 6 to calculate the total amount of neutralized liquid, and the level setting device 5 Convert to a value that matches the measured signal. On the other hand, the neutralization liquid is supplied from the neutralization source 3 to the neutralization tank 1.
A certain amount is stored in the level gauge 2. The valve 13 is activated by the signal from the neutralization controller 6.
``i=open, then pal '7'12 opens, and the neutralizing liquid moves from the neutralizing liquid tank\1 to the neutralizing liquid measuring device 4 by its own weight,
While the amount is measured by the level measuring device, the signal is transmitted to the neutralization controller 6.
中和コントローラ6ではこの信号と前述のサンプリング
装置10からの信号全比較し、マツチし友所で、コント
ローラ9にバルブ12の閉止信号全速り、バルブ12奢
閉止し、中和液の流fl’に停止する。この時バルブ1
4,15.16は閉となっている。次にバルジ15全開
として中和液計量器内の中和液テ廃液混合タンクに自重
落下させる。The neutralization controller 6 compares this signal with all the signals from the sampling device 10 described above, and if a match is found, the controller 9 receives a full closing signal for the valve 12, closes the valve 12, and controls the flow of the neutralizing liquid fl'. Stop at. At this time valve 1
4, 15, and 16 are closed. Next, the bulge 15 is fully opened and the neutralized liquid in the neutralized liquid meter is allowed to fall by its own weight into the waste liquid mixing tank.
この自重による自由落下速度はバルブ13の開度又はバ
ルブ15の開度により任意に行われる。落下はレベル測
定装置5によって確認さn、この確認信号によりコント
ローラ9によりポンプ11を作動せしめて中和のための
混合を行う。すなわち、ポンプ11により、バルブ18
全介し廃液混合タンク間!廃液を循環させながら中和す
る。この中和効果はサンプリング装置10により測定さ
n、中和不足の場合は再度上述の順序で中和が行なわれ
る。中和が完了すると、バルブ18′に閉止し、バルブ
19を開とし、ポンプ11により図示さnない廃棄物処
理ラインで別途処理される。一方、過中和の場合は、図
示されないが、逆PHの液を同様のライン全役けて注入
することにより中和可能である。This free fall speed due to its own weight is arbitrarily determined by the opening degree of the valve 13 or the opening degree of the valve 15. The drop is confirmed by the level measuring device 5, and in response to this confirmation signal, the controller 9 operates the pump 11 to perform mixing for neutralization. That is, the pump 11 causes the valve 18 to
Between all the waste liquid mixing tanks! Neutralize while circulating the waste liquid. This neutralization effect is measured by the sampling device 10, and if neutralization is insufficient, neutralization is performed again in the above-mentioned order. When neutralization is completed, the valve 18' is closed, the valve 19 is opened, and the waste is treated separately by the pump 11 in a waste treatment line (not shown). On the other hand, in the case of over-neutralization, although not shown, neutralization can be achieved by injecting a liquid with a reverse PH through all the same lines.
一方、中和が完了すると同時にバルブ13.15が閉止
され、バルブ16.14が開となり図示されない洗浄水
源より洗浄水が中和液計量器4に流入し内部を洗浄する
。この洗浄層の廃液は図示さ扛ないドレンタンクへ自重
落下又は洗浄水、水圧により移送される。On the other hand, as soon as neutralization is completed, valve 13.15 is closed, valve 16.14 is opened, and cleaning water flows into the neutralizing liquid measuring device 4 from a cleaning water source (not shown) to clean the inside. The waste liquid from the cleaning layer is transferred to a drain tank (not shown) by falling under its own weight or by using cleaning water or water pressure.
以上にて中和の1ザイクルが完了する。この方法である
と従来の中和液の移送全ポンプによって行っていたもの
が不必要であり系統として非常に単純化する事が可能で
あり、回転体がないぶんだけ保守が不要であり、原子力
発電所特有問題である被爆の減少と、消耗品等の廃棄物
の減少の効果がある。With the above steps, one cycle of neutralization is completed. This method eliminates the need for the conventional transfer pump for neutralizing liquid, making it possible to greatly simplify the system, and since there is no rotating body, no maintenance is required, and nuclear power This has the effect of reducing radiation exposure, which is a problem unique to power plants, and reducing waste such as consumables.
第2図は、第1図に於ける中和液計量器4の上流側に循
環ラインからバイパスライン26t−設けた事全特徴と
するもので、洗浄時に洗浄水がバイパスライン26に流
入しないようチェック弁25奢有している。このバイパ
スライン26は、中和液全完全に中和のために有効使用
するために設けであるものでポンプ11により混合する
時、バイパスライン26にも被中和液が圧送されこの液
で中和液全完全に中和に使用するものである他の動作に
ついては第1図の実施例と同一につき省略する。Fig. 2 is characterized in that a bypass line 26t is provided from the circulation line to the upstream side of the neutralizing liquid measuring device 4 in Fig. 1, so that washing water does not flow into the bypass line 26 during washing. It has 25 check valves. This bypass line 26 is provided to effectively use all of the neutralizing liquid for complete neutralization, and when mixing is performed by the pump 11, the liquid to be neutralized is also pumped to the bypass line 26, and the liquid is neutralized with this liquid. The other operations used to completely neutralize the Japanese liquid are the same as those in the embodiment shown in FIG. 1, and will therefore be omitted.
第3図は輌1図に於ける中和液計量器4の下流、側にジ
エツ+ポンプ27全設けた事f:特徴とするもので、こ
のジェットポンプ27の駆動水は廃液循環ラインからバ
イパスしているバイパスライン28により廃液全使用す
る。この場合、中和液全強制的に移送できるので、中和
液計量器4は必ずしも廃液混合タンク7より上方に設置
する必要がなく、設置場所の選定が容易となるメリット
がある。Figure 3 is characterized in that the jet pump 27 is completely installed on the downstream side of the neutralizing liquid measuring device 4 in Figure 1, and the drive water for this jet pump 27 is bypassed from the waste liquid circulation line. All waste liquid is used by the bypass line 28. In this case, since all of the neutralized liquid can be forcibly transferred, the neutralized liquid measuring device 4 does not necessarily have to be installed above the waste liquid mixing tank 7, and there is an advantage that the installation location can be easily selected.
第4図は第1囚に於ける中和タンク1、レベルゲージ2
がない系統であり、中和液源3より直接中和液計量器4
へ中和液を移送する方法で他は第1交の方向と同一であ
るので説明全省略する。Figure 4 shows neutralization tank 1 and level gauge 2 in the first prisoner.
There is no system, and the neutralizing liquid measuring device 4 is directly connected to the neutralizing liquid source 3.
The rest of the method for transferring the neutralizing liquid to the first intersection is the same as the first intersection direction, so a complete explanation will be omitted.
本方式は中和液源3に他系統へも中和液全速る量的余裕
のある場合全示し、設備として簡素となりレベルスイッ
チ2の故障等考えた場合、保守要素の減少となり、原子
力に於ける被爆低減となる。In this system, if the neutralizing liquid source 3 has sufficient quantity to send the neutralizing liquid to other systems as well, it will be displayed completely, and the equipment will be simplified, and maintenance elements will be reduced in case of failure of the level switch 2. This will reduce exposure to radiation.
第5図は第2図に於ける、又第6図は第3図に於ける中
和液タンク1、レベルゲージ2のない方式で効果は第4
図の方式と同じであり、又機能も各々第2図、第3図と
同じであるため説明を省略する。Figure 5 shows the system in Figure 2, and Figure 6 shows the system in Figure 3 without the neutralizing liquid tank 1 and level gauge 2, and the effect is the same as in Figure 4.
The system is the same as that shown in the figure, and the functions are also the same as those in FIGS. 2 and 3, so a description thereof will be omitted.
尚第1.2.3図に於ける中和タンク1を設けるメリッ
トは、中和液源3に量的余裕のない場合本図に示す中和
操作ができなくなるの全防止するため予備量として蓄え
るために設けるものである。The advantage of providing the neutralization tank 1 in Figure 1.2.3 is that it can be used as a reserve amount to completely prevent the neutralization operation shown in this figure from becoming impossible if there is not enough volume in the neutralization liquid source 3. It is provided for storage.
以上説明したように、回転体等動く機能を中和液移送部
にないため故障率の減少、保守時間の減少、設備費の減
少、省エネ放射線被爆の減少等多くのメリットのある廃
液中和装置である。As explained above, the waste liquid neutralization device has many advantages such as reduced failure rate, reduced maintenance time, reduced equipment costs, energy saving, and reduced radiation exposure because the neutralizing liquid transfer part does not have any moving functions such as rotating bodies. It is.
本発明の効果は、(1)回転体(ポンプ)がないため高
放射線下に於ける作業時間が100Hr/年減少し被爆
減少につながる。(2)設備費用が2/3となる。(3
)故障の発生の多い回転体がないため運転効率が上る。The effects of the present invention are as follows: (1) Since there is no rotating body (pump), the working time under high radiation is reduced by 100 hours/year, leading to a reduction in radiation exposure. (2) Equipment costs will be reduced to 2/3. (3
) Operational efficiency is increased because there are no rotating parts that often fail.
第1図は本発明の一実施例の廃液中和装置の系統図、第
2図は第1図以外の廃液中和装置の系統図、第3図は第
1図、第2図以外の廃液中和@負の系統図、第4図は第
1図〜第3図以外の廃液中和装置の系統図、第5図は第
1図〜第4図以外の廃液中和装置の系統図、第6図は第
1図〜第5図以外の廃液中和装置の系統図である。Fig. 1 is a system diagram of a waste liquid neutralization device according to an embodiment of the present invention, Fig. 2 is a system diagram of a waste liquid neutralization device other than that shown in Fig. 1, and Fig. 3 is a system diagram of a waste liquid neutralization device other than those shown in Figs. 1 and 2. Neutralization @ negative system diagram, Figure 4 is a system diagram of waste liquid neutralization equipment other than Figures 1 to 3, Figure 5 is a system diagram of waste liquid neutralization equipment other than Figures 1 to 4, FIG. 6 is a system diagram of a waste liquid neutralization device other than those shown in FIGS. 1 to 5.
Claims (1)
液全中和する装置に於ける中和液の定量注入装置に於い
て、廃液混合タンク上方に設置される中和液タンク、中
和液計量器、中和液計量器の中和液のレベル測定装置、
計量操作用バルブ群、該バルブ群にコ、ントロールスル
コントローラー、中和中の液のPH’を測定するサンプ
リング装置、及び該サンプリング装置のPH倍信号ら必
要中和液量を演算し7、前記中和液のレベル測定装置か
らのレベル信号との比較により中和液量の調整信号全発
生する中和コントローラーから成ること”t%徴とする
廃液中和装置。 2、請求の範囲第1項に於いて、廃液混合中の液の一部
全中和液計量器の上方より任意の圧力で中和液全強制的
に廃液混合タンクへ流入せしめること?特徴とする廃液
中和装置。 3、請求の範囲第1項に於いて、廃液混合中の圧力液に
用いたジェットポンプを中和液計量器の下方に設置せし
めて、中和液計量器中の中和液を強制的に廃液混合タン
クへ流入せしめること?特徴とする廃液中和装置。[Scope of Claims] 1. A neutralizing liquid tank installed above a waste liquid mixing tank in a fixed quantity injection device for neutralizing liquid in a device for completely neutralizing acidic or alkaline waste liquid generated from a nuclear power plant. , neutralizing liquid measuring device, neutralizing liquid level measuring device of neutralizing liquid measuring device,
Calculate the required amount of neutralizing liquid from a metering operation valve group, a control controller for the valve group, a sampling device for measuring the pH' of the liquid being neutralized, and a PH multiplication signal of the sampling device 7, A waste liquid neutralization device comprising a neutralization controller that generates an adjustment signal for the amount of neutralized liquid by comparison with a level signal from a level measuring device for the neutralized liquid.2.Claim 1. A waste liquid neutralization device characterized by forcing all of the neutralized liquid to flow into the waste liquid mixing tank at an arbitrary pressure from above a neutralized liquid measuring device. 3. In claim 1, the jet pump used for the pressure liquid during waste liquid mixing is installed below the neutralized liquid measuring device, and the neutralized liquid in the neutralized liquid measuring device is forcibly mixed with the waste liquid. The waste liquid neutralization device is characterized by allowing it to flow into the tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3901183A JPS59164999A (en) | 1983-03-11 | 1983-03-11 | Liquid waste neutralization device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3901183A JPS59164999A (en) | 1983-03-11 | 1983-03-11 | Liquid waste neutralization device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59164999A true JPS59164999A (en) | 1984-09-18 |
Family
ID=12541158
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3901183A Pending JPS59164999A (en) | 1983-03-11 | 1983-03-11 | Liquid waste neutralization device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59164999A (en) |
-
1983
- 1983-03-11 JP JP3901183A patent/JPS59164999A/en active Pending
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