JPH1090484A - Hydrogen/oxygen injection system of boiling water reactor plant - Google Patents

Hydrogen/oxygen injection system of boiling water reactor plant

Info

Publication number
JPH1090484A
JPH1090484A JP8248108A JP24810896A JPH1090484A JP H1090484 A JPH1090484 A JP H1090484A JP 8248108 A JP8248108 A JP 8248108A JP 24810896 A JP24810896 A JP 24810896A JP H1090484 A JPH1090484 A JP H1090484A
Authority
JP
Japan
Prior art keywords
oxygen
hydrogen
treatment system
waste treatment
oxygen injection
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP8248108A
Other languages
Japanese (ja)
Inventor
Masamiki Ota
正幹 太田
Noriyuki Sasaki
規行 佐々木
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 Engineering Corp
Toshiba Corp
Original Assignee
Toshiba Engineering Corp
Toshiba 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 Toshiba Engineering Corp, Toshiba Corp filed Critical Toshiba Engineering Corp
Priority to JP8248108A priority Critical patent/JPH1090484A/en
Publication of JPH1090484A publication Critical patent/JPH1090484A/en
Pending legal-status Critical Current

Links

Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E30/00Energy generation of nuclear origin

Abstract

PROBLEM TO BE SOLVED: To stably maintain oxygen concentration at the outlet of recombiner of gas waste processing system by varying oxygen injection rate following the change of oxygen concentration and flowrate at the outlet. SOLUTION: In the case hydrogen temporarily stagnates and discharges in the main condenser 4, for example, the recombining amount of hydrogen and oxygen in a recombiner 8 of a gas waste processing system varies with it. The state can be known from the oxygen concentration at the outlet of the recombiner 8 of a gas waste processing system. Upon receiving the oxygen concentration change, oxygen concentration is detected without delay with an oxygen concentration detector 11 and an oxygen concentration measuring device 12, which is input in a hydrogen / oxygen injection rate controller 19. In the hydrogen / oxygen injection rate controller 19, control signal for varying the opening of an oxygen injection rate control valve 18 can be sent through a specific operation. Repeated operation of this, as the results, comes to stabilize oxygen concentration at the outlet of the recombiner 8 of a gas waste processing system.

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、原子炉一次冷却材
に水素を注入するとともに、主復水器で抽出された非凝
縮ガスに気体廃棄物処理系再結合器に至る前に気体廃棄
物処理系にて余剰となる水素を処理するための酸素を注
入する沸騰水型原子力発電所における水素・酸素注入運
転を行うシステムに係り、特に、気体廃棄物処理系再結
合器出口ガスの酸素濃度を安定に保つことで、水素爆発
濃度域への到達に対する危険性を回避し、原子力発電プ
ラントの安全性を確実のものとする沸騰水型原子力プラ
ントの水素・酸素注入システムに関する。
BACKGROUND OF THE INVENTION The present invention relates to a method for injecting hydrogen into a primary coolant of a nuclear reactor and converting the non-condensable gas extracted by a main condenser into a gas waste treatment system before reaching a gas waste treatment system recombiner. The present invention relates to a system for performing a hydrogen / oxygen injection operation in a boiling water nuclear power plant that injects oxygen for processing excess hydrogen in a processing system, and in particular, an oxygen concentration in a gaseous waste processing system recombiner outlet gas. The present invention relates to a hydrogen / oxygen injection system for a boiling water nuclear power plant, which can stabilize a fuel cell to avoid the danger of reaching a hydrogen explosion concentration range and ensure the safety of a nuclear power plant.

【0002】[0002]

【従来の技術】沸騰水型原子力発電所においては、原子
炉一次冷却材が原子炉にて蒸気となり、発生した蒸気は
タービンで仕事をした後、主復水器で凝縮される。凝縮
水は再び原子炉へ給水される一方、主復水器で抽出され
た非凝縮ガスは気体廃棄物処理系に導かれて処理され
る。この非凝縮ガスは、原子炉における一次冷却材、即
ち水の放射線分解で発生する水素と酸素が主なものであ
る。
2. Description of the Related Art In a boiling water nuclear power plant, the primary coolant of a reactor becomes steam in a reactor, and the generated steam works in a turbine and is condensed in a main condenser. The condensed water is supplied again to the reactor, while the non-condensed gas extracted in the main condenser is guided to a gaseous waste treatment system for treatment. This non-condensable gas is mainly composed of primary coolant in a nuclear reactor, that is, hydrogen and oxygen generated by radiolysis of water.

【0003】沸騰水型原子力発電プラントにおける水素
・酸素注入運転は、原子炉水の酸素濃度を低下させ炉内
構造材科の腐食抑制を図ることを目的とするものであっ
て、この原子炉一次冷却材に注入した水素は原子炉前で
注入した全量が蒸気側に移行し、主復水器を通じて非凝
縮ガスとして気体廃棄物処理系へ導かれる。この水素を
酸素と再結合させるため気体廃棄物処理系再結合器前に
おいて、注入した水素量が再結合するだけの量の酸素が
非凝縮ガス中に注入され、気体廃棄物処理系再結合器出
口においてその再結合の達成確認のため酸素濃度を監視
している。
[0003] The hydrogen / oxygen injection operation in the boiling water nuclear power plant is intended to reduce the oxygen concentration of the reactor water and to suppress the corrosion of structural materials in the reactor. All of the hydrogen injected into the coolant is transferred to the steam side before the reactor and is led to the gaseous waste treatment system as a non-condensable gas through the main condenser. In order to recombine this hydrogen with oxygen, just before the gas waste treatment system recombiner, enough oxygen is injected into the non-condensed gas to recombine the injected hydrogen, and the gas waste treatment system recombiner At the outlet, the oxygen concentration is monitored to confirm the achievement of the recombination.

【0004】このような従来の沸騰水型原子力プラント
の水素・酸素注入システム運転では、気体廃棄物処理系
再結合器出口のガス濃度は、主復水器内の圧力変化等の
際に、これに連動して酸素濃度の低下、ひいては水素濃
度の上昇が起こるという問題がある。これは、主復水器
内で圧力変化が生じる際に、非凝縮ガスの気体廃棄物処
理系の移行速度が過渡的に変動することで、再結合器に
到達する水素流量と酸素流量の比が変化することにより
生じるものであるが、水素濃度が上昇することがあって
も、爆発下限界(4%)以上となる状態は、原子力発電
プラントとしては必ず避けなくてはならない事態であ
る。
In the operation of the hydrogen / oxygen injection system of such a conventional boiling water nuclear power plant, the gas concentration at the outlet of the recombiner of the gaseous waste treatment system changes when the pressure in the main condenser changes. Therefore, there is a problem that the oxygen concentration is reduced and the hydrogen concentration is increased in conjunction therewith. This is because when the pressure changes in the main condenser, the transition speed of the non-condensable gas waste treatment system fluctuates transiently, and the ratio of the hydrogen flow rate and oxygen flow rate reaching the recombiner However, even if the hydrogen concentration rises, the state where the explosion level is lower than the lower limit (4%) must be avoided as a nuclear power plant.

【0005】このような、主復水器の圧力変化は、主復
水器の故障・事故時以外にも、主復水器の冷却水(海
水)温度の変化に伴う真空度調整や、主復水器の冷却水
管の洗浄など、日常的なプラント運転操作を行う際、一
時的な圧力変化として発生する。 この際、プラント運
転者は気体廃棄物処理系再結合器出口酸素濃度値変化に
注目して水素・酸素注入システムの運転操作の変更(酸
素注入流量のアップ)などを行うことになるが、この酸
素濃度値の表示は、実際の気体廃棄物処理系の酸素濃度
変化挙動に数分以上の時間遅れがあるという問題があっ
た。
[0005] Such a change in the pressure of the main condenser may be caused by a change in the degree of vacuum caused by a change in the temperature of the cooling water (seawater) of the main condenser or a change in the main condenser in addition to the failure or accident of the main condenser. Occurs as a temporary pressure change when performing routine plant operation, such as cleaning the condenser cooling water pipe. At this time, the plant operator changes the operation of the hydrogen / oxygen injection system (increases the oxygen injection flow rate) while paying attention to the change in the oxygen concentration value at the outlet of the gaseous waste treatment system recombiner. The display of the oxygen concentration value has a problem that there is a time delay of several minutes or more in the oxygen concentration change behavior of the actual gas waste treatment system.

【0006】すなわち、従来の気体廃棄物処理系再結合
器出口の酸素濃度計測装置は、酸素濃度検出器の校正時
の作業員被ばくや、耐圧面で堅牢な計器ではない等の諸
問題から、気体廃棄物処理系再結合器出口配管から配管
分岐し、遮へい壁で囲まれた気体廃棄物処理系室の外に
配管を導き、酸素濃度計測装置に導かれているが、気体
廃棄物処理系再結合器出口からこの計測装置位置までガ
スを導くのに時間がかかり、上述の数分以上の時間遅れ
の大半がこの計測装置位置までガスが導かれる時間とな
っていた。
In other words, the conventional oxygen concentration measuring device at the outlet of the gaseous waste treatment system recombiner has various problems such as exposure of workers at the time of calibrating the oxygen concentration detector and a device which is not robust in pressure resistance. The pipe is branched from the outlet pipe of the gas waste treatment system recombiner, and the pipe is led to the outside of the gas waste treatment system room surrounded by the shielding wall, and is led to the oxygen concentration measurement device. It takes time to introduce gas from the outlet of the recombiner to this measuring device position, and most of the above-described time delay of several minutes or more is time for introducing gas to this measuring device position.

【0007】このため、例えば、プラント運転員が酸素
濃度の低下を確認してから水素・酸素注入システムの運
転操作の変更を行ったとしても、気体廃棄物処理系での
同時刻の酸素濃度の低下事象(場合によっては水素濃度
の上昇)はそれまでの間にかなり進行していたり、ある
いは、酸素濃度が既に平常値以上に復帰し平常値以上の
系統流量になっている時であれば気体廃棄物処理系設計
流量を一時的に超過してしまうという問題があった。
For this reason, for example, even if the plant operator confirms a decrease in the oxygen concentration and then changes the operation of the hydrogen / oxygen injection system, the oxygen concentration in the gas waste treatment system at the same time is changed. If the decrease event (in some cases, the increase in hydrogen concentration) has progressed considerably before that, or if the oxygen concentration has already returned to a normal value or more and the system flow rate has exceeded the normal value, gas There is a problem that the design flow rate of the waste treatment system is temporarily exceeded.

【0008】[0008]

【発明が解決しようとする課題】上述のとおり、従来の
沸騰水型原子力プラントの水素・酸素注入システムで
は、気体廃棄物処理系再結合器出口の酸素濃度計測が、
気体廃棄物処理系再結合器出口配管から配管分岐し遮へ
い壁で囲まれた気体廃棄物処理系室の外に配管を導いて
設置された酸素濃度計測装置により行われていたため、
気体廃棄物処理系再結合器出口からこの計測装置位置ま
でガスを導くのに時間がかかり、実際の気体廃棄物処理
系の酸素濃度変化挙動に数分以上の時間遅れが生ずると
いう問題があった。
As described above, in the hydrogen / oxygen injection system of the conventional boiling water nuclear power plant, the oxygen concentration measurement at the outlet of the recombiner in the gaseous waste treatment system is performed as follows.
Because it was conducted by an oxygen concentration measurement device installed by guiding the pipe to the outside of the gas waste treatment system room that was branched from the gas waste treatment system recombiner outlet pipe and surrounded by a shielding wall,
There is a problem that it takes time to guide the gas from the gaseous waste treatment system recombiner outlet to this measuring device position, and a time delay of several minutes or more occurs in the oxygen concentration change behavior of the actual gaseous waste treatment system. .

【0009】本発明は、かかる従来の問題を解決すべく
なされたもので、プラントの運転条件の変更に伴い気体
廃棄物処理系再結合器出口の酸素が消費されて水素濃度
が上昇し始める可能性に対して、気体廃棄物処理系再結
合器出口の酸素濃度変化の検出から、その変化量に見合
った酸素注入流量の演算と、流量調節装置ヘ制御指令並
びに流量変更操作という一連の操作を自動でかつ連続的
に行うことにより、気体廃棄物処理系再結合器出口の酸
素濃度を安定にする沸騰水型原子力プラントの水素・酸
素注入システムを提供することにある。
The present invention has been made to solve such a conventional problem, and it is possible that the oxygen at the outlet of the gas waste treatment system recombiner is consumed and the hydrogen concentration starts to increase with a change in the operating conditions of the plant. To detect the change in oxygen concentration at the outlet of the gaseous waste treatment system recombiner, a series of operations such as calculating the oxygen injection flow rate commensurate with the change amount and controlling the flow rate control device and changing the flow rate are performed. An object of the present invention is to provide a hydrogen / oxygen injection system for a boiling water nuclear power plant, which stabilizes the oxygen concentration at the outlet of a gaseous waste treatment system recombiner by performing the operation automatically and continuously.

【0010】[0010]

【課題を解決するための手段】本発明は、以上の目的を
達成するために、 (1)原子炉一次冷却材に水素を注入するとともに、主
復水器で抽出された非凝縮ガスに気体廃棄物処理系再結
合器に至る前に気体廃棄物処理系にて余剰となる水素を
処理するための酸素を注入する沸騰水型原子力発電所に
おける水素・酸素注入運転を行うシステムにおいて、気
体廃棄物処理系再結合器通過後の非凝縮ガス中の酸素濃
度を気体廃棄物処理系再結合器出口配管に直接取付けら
れた酸素濃度検出器で計測する酸素濃度計測装置と、気
体廃棄物処理系への酸素注入流量をその酸素濃度値によ
り演算して変化させる酸素注入量制御装置と、この酸素
注入量制御装置の信号により調節弁の開度を自動で変化
させて酸素注入流量を制御する水素注入流量制御弁とを
有することを特徴とする沸騰水型原子力プラントの水素
・酸素注入システム。 (2)原子炉一次冷却材に水素を注入するとともに、主
復水器で抽出された非凝縮ガスに気体廃棄物処理系再結
合器に至る前に気体廃棄物処理系にて余剰となる水素を
処理するための酸素を注入する沸騰水型原子力発電所に
おける水素・酸素注入運転を行うシステムにおいて、気
体廃棄物処理系再結合器出口配管のガス流量を計測する
流量計測装置と、気体廃棄物処理系への酸素注入流量を
その流量値により演算して変化させる酸素注入量制御装
置と、この酸素注入量制御装置の信号により調節弁の開
度を自動で変化させて酸素注入流量を制御する酸素注入
流量制御弁とを有することを特徴とする沸騰水型原子力
プラントの水素・酸素注入システムとを提供する。
SUMMARY OF THE INVENTION In order to achieve the above objects, the present invention provides: (1) Injecting hydrogen into a primary coolant of a nuclear reactor and adding gas to a non-condensable gas extracted by a main condenser. In a system that performs hydrogen / oxygen injection operation at a boiling water nuclear power plant that injects oxygen to treat excess hydrogen in a gaseous waste treatment system before reaching a waste treatment system recombiner Oxygen concentration measurement device that measures the oxygen concentration in the non-condensed gas after passing through the waste treatment system recombiner with the oxygen concentration detector directly attached to the gas waste treatment system recombiner outlet pipe, and the gas waste treatment system Oxygen injection amount control device that calculates and changes the oxygen injection flow rate to oxygen based on the oxygen concentration value, and hydrogen that controls the oxygen injection flow rate by automatically changing the opening of the control valve according to a signal from the oxygen injection amount control device. Injection flow control valve and A hydrogen / oxygen injection system for a boiling water nuclear power plant. (2) Inject hydrogen into the primary coolant of the reactor, and add excess hydrogen to the non-condensed gas extracted by the main condenser in the gas waste treatment system before reaching the gas waste treatment system recombiner. In a system for performing hydrogen / oxygen injection operation at a boiling water nuclear power plant that injects oxygen for treating wastewater, a flow measurement device that measures the gas flow rate at the outlet pipe of a gaseous waste treatment system recombiner, and a gaseous waste An oxygen injection amount control device that calculates and changes the oxygen injection flow rate to the processing system based on the flow rate value, and automatically controls the oxygen injection flow rate by automatically changing the opening of the control valve according to a signal from the oxygen injection amount control device. A hydrogen / oxygen injection system for a boiling water nuclear power plant, comprising: an oxygen injection flow control valve.

【0011】[0011]

【発明の実施の形態】本発明の沸騰水型原子力プラント
の水素・酸素注入システムにおいては、プラントの運転
条件の変更等により、気体廃棄物処理系再結合器へ到達
する水素、酸素流量比が変化を起こす場合において、気
体廃棄物処理系再結合器出口の酸素濃度変化や流量変化
から酸素注入流量を追従させて変化させることで、原子
炉一次冷却材への水素注入量は維持した上で、気体廃棄
物処理系再結合器出口酸素濃度を安定に保つことが可能
となる。
BEST MODE FOR CARRYING OUT THE INVENTION In the hydrogen / oxygen injection system of a boiling water nuclear power plant according to the present invention, the ratio of the flow rate of hydrogen and oxygen reaching the gas waste treatment system recombiner is changed by changing the operating conditions of the plant. When a change occurs, the amount of hydrogen injected into the primary coolant of the reactor is maintained by following and changing the oxygen injection flow rate from the change in oxygen concentration and flow rate at the outlet of the gaseous waste treatment system recombiner. In addition, the oxygen concentration at the outlet of the gaseous waste treatment system recombiner can be kept stable.

【0012】[0012]

【実施例】以下、本発明の実施例を図1により説明す
る。
An embodiment of the present invention will be described below with reference to FIG.

【0013】図1は沸騰水型原子力プラントの水素・酸
素注入システムを模式的に示すもので、原子炉1で発生
した蒸気は主蒸気管2を経てタービン3を回転させ、仕
事を終えた蒸気は主復水器4で復水となり給水管5を経
て給水ポンプ6で加圧されて原子炉1へ給水される。
FIG. 1 schematically shows a hydrogen / oxygen injection system of a boiling water nuclear power plant, in which steam generated in a nuclear reactor 1 rotates a turbine 3 via a main steam pipe 2 to complete work. Is condensed by the main condenser 4, is pressurized by the water supply pump 6 through the water supply pipe 5, and is supplied to the reactor 1.

【0014】主復水器4には気体廃棄物処理系再結合器
入口配管7が接続され非凝縮ガスを気体廃棄物処理系再
結合器8へ導いている。気体廃棄物処理系再結合器出口
配管9は気体廃棄物処理系再結合器8で再結合しなかっ
た非凝縮ガスを流量計10、酸素濃度検出器11を備え
た酸素濃度測定装置12等を経て図示を省略した気体廃
棄物処理系へ導いている。
The main condenser 4 is connected to a gas waste treatment system recombiner inlet pipe 7 and guides non-condensed gas to the gas waste treatment system recombiner 8. The gaseous waste treatment system recombiner outlet pipe 9 is used to remove the non-condensed gas that has not been recombined by the gaseous waste treatment system recombiner 8 from a flow meter 10, an oxygen concentration measurement device 12 having an oxygen concentration detector 11, and the like. This leads to an unillustrated gaseous waste treatment system.

【0015】給水管5には水素供給管13が接続され、
水素供給設備14から水素注入流量制御弁15を介して
水素が注入される。また、気体廃棄物処理系再結合器入
口配管7には酸素供給管16が接続され、酸素供給設備
17から酸素注入流量制御弁18を介して酸素が注入さ
れる。
A hydrogen supply pipe 13 is connected to the water supply pipe 5,
Hydrogen is injected from the hydrogen supply facility 14 via the hydrogen injection flow control valve 15. Further, an oxygen supply pipe 16 is connected to the gas waste treatment system recombiner inlet pipe 7, and oxygen is injected from an oxygen supply facility 17 through an oxygen injection flow control valve 18.

【0016】水素・酸素注入量制御装置19は流量計1
0または酸素濃度測定装置12からの信号を受けて気体
廃棄物処理系で余剰となる水素を処理するための酸素量
を演算し酸素注入流量制御弁調節弁18に制御信号を供
給する。なお、水素・酸素注入量制御装置19は流量計
10または酸素濃度測定装置12からの信号を受けて、
必要に応じて水素注入流量制御弁15も自動で変化させ
水素注入流量を制御する。 プラント通常運転時、水素
及び酸素は、水素ガス供給設備14及び酸素ガス供給設
備17より供給され、水素・酸素注入量制御装置19か
らの制御信号により、水素注入流量制御弁15及び酸素
注入流量制御弁18によって、注入量が制御される。
The hydrogen / oxygen injection amount control device 19 includes the flow meter 1
In response to 0 or a signal from the oxygen concentration measuring device 12, the amount of oxygen for processing excess hydrogen in the gaseous waste treatment system is calculated, and a control signal is supplied to the oxygen injection flow control valve control valve 18. The hydrogen / oxygen injection amount control device 19 receives a signal from the flow meter 10 or the oxygen concentration measurement device 12,
If necessary, the hydrogen injection flow control valve 15 is also automatically changed to control the hydrogen injection flow. During normal operation of the plant, hydrogen and oxygen are supplied from the hydrogen gas supply equipment 14 and the oxygen gas supply equipment 17, and are controlled by a control signal from the hydrogen / oxygen injection quantity control device 19 to control the hydrogen injection flow control valve 15 and the oxygen injection flow rate. The valve 18 controls the injection volume.

【0017】この水素は、原子炉一次冷却材中に注入さ
れ、溶け込み、原子炉1に流入し、主蒸気管2を通じ
て、タービン3、主復水器4を経て、気体廃棄物処理系
再結合器8に導かれる。
This hydrogen is injected into the primary coolant of the reactor, melts, flows into the reactor 1, passes through the main steam pipe 2, passes through the turbine 3, the main condenser 4, and recombines with the gas waste treatment system. To the vessel 8.

【0018】また、酸素は気体廃棄物処理系再結合器8
前に注入され、注入した水素の再結合に寄与することと
なる。
Oxygen is supplied to the gaseous waste treatment system recombiner 8.
It is implanted before and contributes to the recombination of the implanted hydrogen.

【0019】ここで、例えば、主復水器4内で水素が一
時的に滞留、放出する様な場合において、気体廃棄物処
理系再結合器8における水素と酸素の再結合量は、これ
にともなって変化し、その状況は気体廃棄物処理系再結
合器8出口の酸素濃度変化により知ることができる。つ
まり、水素と酸素の注入体積流量比が2対1である場
合、気体廃棄物処理系再結合器8出口ガス組成は、気体
廃棄物処理系に流入する空気にほぼ等しくなり、理論的
に酸素濃度は約21%となる。しかし、気体廃棄物処理
系への酸素注入量が一定量で、気体廃棄物処理系への注
入した水素の到達量が少なくなる時、上記酸素濃度は上
昇することとなり、水素の到達量が多くなる時、酸素濃
度は低下し、酸素が欠乏した後は、それまで存在してい
なかった水素濃度が上昇し始める。
Here, for example, in the case where hydrogen temporarily stays and releases in the main condenser 4, the recombination amount of hydrogen and oxygen in the gas waste treatment system recombiner 8 is The situation can be known from the change in the oxygen concentration at the outlet of the gas waste treatment system recombiner 8. That is, when the injection volume flow ratio of hydrogen and oxygen is 2: 1, the gas composition at the outlet of the gas waste treatment system recombiner 8 is almost equal to the air flowing into the gas waste treatment system, and theoretically, the oxygen The concentration is about 21%. However, when the amount of oxygen injected into the gaseous waste treatment system is constant and the amount of hydrogen injected into the gaseous waste treatment system decreases, the oxygen concentration increases, and the amount of hydrogen reaches a large amount. Occasionally, the oxygen concentration decreases, and after oxygen depletion, the hydrogen concentration, which was not present before, begins to increase.

【0020】本発明の第1の実施形態は、この酸素濃度
変化を受け、直ちに酸素注入流量の変更させるシステム
であり、気体廃棄物処理系出口配管9に酸素濃度検出器
11を備えた酸素濃度計測装置12を直接取り付け、時
間遅れなく酸素濃度を検出し、水素・酸素注入量制御装
置19に入力する。
The first embodiment of the present invention is a system for immediately changing the oxygen injection flow rate in response to this change in oxygen concentration. The oxygen concentration detector 11 is provided in the gas waste treatment system outlet pipe 9 with the oxygen concentration detector 11. The measuring device 12 is directly attached, the oxygen concentration is detected without delay, and the detected oxygen concentration is input to the hydrogen / oxygen injection amount control device 19.

【0021】この酸素濃度入力値の演算、制御手法の例
を以下に示す。
An example of the calculation and control method of the oxygen concentration input value will be described below.

【0022】気体廃棄物処理系再結合器出口酸素濃度
(O2 )は、一般的に下式となる。
The oxygen concentration (O 2 ) at the outlet of the gaseous waste treatment system recombiner is generally expressed by the following equation.

【0023】(O2 )={(Air )×0.21+(O2in
−0.5 ×(H2in )}/{(Air )+(O2in )−0.5
×(H2in )} ただし、(Air )は気体廃棄物処理系流入空気流量、
(O2in )は注入酸素の到達流量(酸素注入流量)、
(H2in )は注入水素の到達流量、0.21は空気中の酸素
存在比を示す。
(O 2 ) = {(Air) × 0.21 + (O 2in )
−0.5 × (H 2in )} / {(Air) + (O 2in ) −0.5
× (H 2in )} where (Air) is the inflow air flow rate in the gaseous waste treatment system,
(O 2in ) is the attained flow rate of the injected oxygen (oxygen injection flow rate),
(H 2in ) indicates the reached flow rate of the injected hydrogen, and 0.21 indicates the oxygen abundance ratio in the air.

【0024】ここで、(Air )はプラント定格運転中変
動の少ないパラメータであるので定数と考えてよいの
で、水素・酸素注入定常運転下で、(O2 )の変化は
(H2in)の変化によることが示される。水素・酸素注
入量制御装置19では、(O2 )の値、或いは(O2
の変化巾がある一定の値となる様に、一定時刻毎に(O
2i n )の値を演算し、酸素注入流量制御弁18の開度を
変える制御信号を送ることができる。これを、繰り返し
行う動作は、結果として気体廃棄物処理系再結合器出口
の酸素濃度を安定させるものとなる。
Here, since (Air) is a parameter with little variation during the rated operation of the plant, it can be considered as a constant. Therefore, under steady operation of hydrogen / oxygen injection, the change of (O 2 ) is the change of (H 2in ). Is shown. In the hydrogen-oxygen injection rate control unit 19, the value of (O 2), or (O 2)
(O) at regular time intervals so that the range of change becomes a constant value.
Calculates the value of 2i n), it is possible to send a control signal for changing the opening degree of the oxygen injection flow control valve 18. The operation of repeating this operation stabilizes the oxygen concentration at the outlet of the gaseous waste treatment system recombiner as a result.

【0025】酸素濃度計測装置12は、図2に例を示す
ように、気体廃棄物処理系配管の異當昇圧時に酸素濃度
検出器11から系外漏洩を防ぐため、酸素濃度検出器1
1を覆う隔壁21と、気体廃棄物処理系の圧力変化によ
る酸素濃度値の変化影響を補正するため、圧力計22と
圧力補正演算器23とを備える。
As shown in the example of FIG. 2, the oxygen concentration measuring device 12 is provided to prevent the oxygen concentration detector 11 from leaking out of the system when the pressure of the gas waste treatment system piping is increased.
1 is provided, and a pressure gauge 22 and a pressure correction calculator 23 are provided to correct the influence of a change in the oxygen concentration value due to a change in pressure of the gaseous waste treatment system.

【0026】第2の実施形態では、気体廃棄物処理系再
結合器出口酸素濃度を検出するのではなく、水素到達量
が変化する場合、図1における気体廃棄物処理系再結合
器出口の流量計10の検出値が変化することを利用して
いる。
In the second embodiment, instead of detecting the oxygen concentration at the outlet of the gaseous waste treatment system recombiner, the flow rate at the outlet of the gaseous waste treatment system recombiner shown in FIG. The fact that the detection value of the total 10 changes is used.

【0027】これは、上式の分母が、気体廃棄物処理系
再結合器出口流量(Q)に相当することから、下式で表
されるので、第1の実施形態と同様に(Q)の変化は
(H2i n )の変化によることが示される。
Since the denominator of the above equation corresponds to the gaseous waste treatment system recombiner outlet flow rate (Q), it is expressed by the following equation, so that (Q) is the same as in the first embodiment. change in it is shown that due to a change in (H 2i n).

【0028】 (Q)=(Air )+(O2in )−0.5 ×(H2in ) ただし、(Air )は気体廃棄物処理系流入空気流量、
(O2in )は注入酸素の到達流量(酸素注入流量)、
(H2in )は注入水素の到達流量を示す。
(Q) = (Air) + (O 2in ) −0.5 × (H 2in ) where (Air) is the flow rate of air flowing into the gas waste treatment system,
(O 2in ) is the attained flow rate of the injected oxygen (oxygen injection flow rate),
(H 2in ) indicates the flow rate of the injected hydrogen.

【0029】水素・酸素注入量制御装置19では、
(Q)の値、或いは(Q)の変化巾がある一定の値とな
る様に、ー定時刻毎に(O2in )の値を演算し、酸素注
入流量制御弁18の開度を変える制御信号を送ることが
できる。これを、繰り返し行う動作は、結果として気体
廃棄物処理系再結合器出口の酸素濃度を安定させるもの
となる。
In the hydrogen / oxygen injection amount control device 19,
Control to change the opening of the oxygen injection flow control valve 18 by calculating the value of (O 2in ) at regular time intervals so that the value of (Q) or the range of change of (Q) becomes a certain value. You can send a signal. The operation of repeating this operation stabilizes the oxygen concentration at the outlet of the gaseous waste treatment system recombiner as a result.

【0030】[0030]

【発明の効果】本発明によれば、プラント側の運転条件
の変更等により、気体廃棄物処理系再結合器へ到達する
水素、酸素流量比が変化を起こす場合において、気体廃
棄物処理系再結合器出口の酸素濃度変化から酸素注入流
量を追従させて変化させることで、原子炉一次冷却材へ
の水素注入量は維持した上で、気体廃棄物処理系再結合
器出口酸素濃度を安定に保つ水素・酸素注入運転の実施
が可能となる。
According to the present invention, when the ratio of the flow rates of hydrogen and oxygen reaching the gas waste treatment system recombiner changes due to a change in the operating conditions of the plant, etc., the gas waste treatment system By changing the oxygen injection flow rate by following the change in the oxygen concentration at the outlet of the coupler, the amount of hydrogen injected into the primary coolant of the reactor is maintained, and the oxygen concentration at the outlet of the gaseous waste treatment system recombiner is stabilized. It is possible to carry out the hydrogen / oxygen injection operation in which the hydrogen and oxygen are maintained.

【0031】また、本発明によれば、プラント側の運転
条件の変更等により、気体廃棄物処理系再結合器へ到達
する水素、酸素流量比が変化を起こす場合において、気
体廃棄物処理系再結合器出口の流量変化から酸素注入流
量を追従させて変化させることで、原子炉一次冷却材ヘ
の水素注入量は維持した上で気体廃棄物処理系再結合器
出口酸素濃度を安定に保つ水素・酸素注入運転の実施も
可能となる。
Further, according to the present invention, when the ratio of the flow rate of hydrogen and oxygen reaching the gas waste treatment system recombiner changes due to a change in the operating conditions of the plant, etc., the gas waste treatment system By changing the flow rate of the oxygen injection from the change in the flow rate at the outlet of the coupler, the amount of hydrogen injected into the primary coolant of the reactor is maintained and the oxygen concentration at the outlet of the gaseous waste treatment system recombiner is kept stable.・ Oxygen injection operation can be performed.

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

【図1】本発明に関わる水素・酸素注入システムの概念
図。
FIG. 1 is a conceptual diagram of a hydrogen / oxygen injection system according to the present invention.

【図2】本発明の請求項2に関わる酸索濃度計測装置の
概念図。
FIG. 2 is a conceptual diagram of an apparatus for measuring the concentration of acid rope according to claim 2 of the present invention.

【符号の説明】[Explanation of symbols]

1…原子炉、2…主蒸気管、3…タービン、4…主復水
器、5…給水管、6…給水ポンプ、7…気体廃棄物処理
系再結合器入口配管、8…気体廃棄物処理系再結合器、
9…気体廃棄物処理系再結合器出口配管、10…流量
計、11…酸素濃度検出器、13…水素供給管、12…
酸素濃度計測装置、14…水素ガス供給設備、15…水
素注入流量制御弁、16…酸素供給管、17…酸素ガス
供給設備、18…酸素注入流量制御弁、19…水素・酸
素注入量制御装置、21…隔壁、22…圧力計、23…
圧力補正演算器。
DESCRIPTION OF SYMBOLS 1 ... Reactor, 2 ... Main steam pipe, 3 ... Turbine, 4 ... Main condenser, 5 ... Water supply pipe, 6 ... Water supply pump, 7 ... Gas waste treatment system recombiner inlet piping, 8 ... Gas waste Processing recombiner,
9: gas waste treatment system recombiner outlet pipe, 10: flow meter, 11: oxygen concentration detector, 13: hydrogen supply pipe, 12 ...
Oxygen concentration measuring device, 14: hydrogen gas supply equipment, 15: hydrogen injection flow control valve, 16: oxygen supply pipe, 17: oxygen gas supply equipment, 18: oxygen injection flow control valve, 19: hydrogen / oxygen injection amount control device , 21 ... partition wall, 22 ... pressure gauge, 23 ...
Pressure compensation calculator.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 原子炉一次冷却材に水素を注入するとと
もに、主復水器で抽出された非凝縮ガスに気体廃棄物処
理系再結合器に至る前に気体廃棄物処理系にて余剰とな
る水素を処理するための酸素を注入する沸騰水型原子力
発電所における水素・酸素注入運転を行うシステムにお
いて、 気体廃棄物処理系再結合器通過後の非凝縮ガス中の酸素
濃度を気体廃棄物処理系再結合器出口配管に直接取付け
られた酸素濃度検出器で計測する酸素濃度計測装置と、 気体廃棄物処理系への酸素注入流量をその酸素濃度値に
より演算して出力する酸素注入量制御装置と、 この酸素注入量制御装置の出力信号により調節弁の開度
を自動で変化させて酸素注入流量を制御する酸素注入流
量制御弁とを有することを特徴とする沸騰水型原子力プ
ラントの水素・酸素注入システム。
1. Injecting hydrogen into a primary coolant of a nuclear reactor and removing excess gas from a non-condensable gas extracted by a main condenser in a gas waste treatment system before reaching a gas waste treatment system recombiner. In a system for injecting hydrogen and oxygen at a boiling water nuclear power plant that injects oxygen to process hydrogen, the concentration of oxygen in non-condensed gas after passing through a gas waste treatment system An oxygen concentration measurement device that measures with an oxygen concentration detector directly attached to the treatment system recombiner outlet pipe, and an oxygen injection amount control that calculates and outputs the oxygen injection flow rate to the gaseous waste treatment system based on the oxygen concentration value Hydrogen in a boiling water nuclear power plant, comprising: an oxygen injection flow control valve for automatically changing an opening of a control valve by an output signal of the oxygen injection amount control device to control an oxygen injection flow rate. ·oxygen Injection system.
【請求項2】 原子炉一次冷却材に水素を注入するとと
もに、主復水器で抽出された非凝縮ガスに気体廃棄物処
理系再結合器に至る前に気体廃棄物処理系にて余剰とな
る水素を処理するための酸素を注入する沸騰水型原子力
発電所における水素・酸素注入運転を行うシステムにお
いて、 気体廃棄物処理系再結合器出口配管のガス流量を計測す
る流量計測装置と、 気体廃棄物処理系への酸素注入流量をその流量値により
演算して変化させる酸素注入量制御装置と、 この酸素注入量制御装置の信号により調節弁の開度を自
動で変化させて酸素注入流量を制御する酸素注入流量制
御弁とを有することを特徴とする沸騰水型原子力プラン
トの水素・酸素注入システム。
2. Injecting hydrogen into the primary coolant of the nuclear reactor and removing excess condensate from the non-condensed gas extracted by the main condenser in the gas waste treatment system before reaching the gas waste treatment system recombiner. A system for performing hydrogen / oxygen injection operation at a boiling water nuclear power plant that injects oxygen for treating hydrogen, comprising: a flow measuring device that measures a gas flow rate at an outlet pipe of a gas waste treatment system recombiner; and An oxygen injection amount control device that calculates and changes the oxygen injection flow rate to the waste treatment system based on the flow rate value, and automatically changes the opening of the control valve according to a signal from the oxygen injection amount control device to change the oxygen injection flow rate. A hydrogen / oxygen injection system for a boiling water nuclear power plant, comprising: an oxygen injection flow control valve for controlling.
JP8248108A 1996-09-19 1996-09-19 Hydrogen/oxygen injection system of boiling water reactor plant Pending JPH1090484A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8248108A JPH1090484A (en) 1996-09-19 1996-09-19 Hydrogen/oxygen injection system of boiling water reactor plant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8248108A JPH1090484A (en) 1996-09-19 1996-09-19 Hydrogen/oxygen injection system of boiling water reactor plant

Publications (1)

Publication Number Publication Date
JPH1090484A true JPH1090484A (en) 1998-04-10

Family

ID=17173354

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8248108A Pending JPH1090484A (en) 1996-09-19 1996-09-19 Hydrogen/oxygen injection system of boiling water reactor plant

Country Status (1)

Country Link
JP (1) JPH1090484A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001349983A (en) * 2000-06-12 2001-12-21 Toshiba Corp Method for operating boiling water nuclear power plant
JP2012021777A (en) * 2010-07-12 2012-02-02 Hitachi-Ge Nuclear Energy Ltd Device for predicting exit hydrogen concentration of exhaust gas recombination device and method of predicting exit hydrogen concentration

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001349983A (en) * 2000-06-12 2001-12-21 Toshiba Corp Method for operating boiling water nuclear power plant
JP2012021777A (en) * 2010-07-12 2012-02-02 Hitachi-Ge Nuclear Energy Ltd Device for predicting exit hydrogen concentration of exhaust gas recombination device and method of predicting exit hydrogen concentration

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