JPH0250439B2 - - Google Patents
Info
- Publication number
- JPH0250439B2 JPH0250439B2 JP56198575A JP19857581A JPH0250439B2 JP H0250439 B2 JPH0250439 B2 JP H0250439B2 JP 56198575 A JP56198575 A JP 56198575A JP 19857581 A JP19857581 A JP 19857581A JP H0250439 B2 JPH0250439 B2 JP H0250439B2
- Authority
- JP
- Japan
- Prior art keywords
- heavy water
- moderator
- poison
- purification device
- cooler
- 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 - Lifetime
Links
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E30/00—Energy generation of nuclear origin
- Y02E30/30—Nuclear fission reactors
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
- Road Signs Or Road Markings (AREA)
- Cleaning In General (AREA)
- Treatment Of Water By Oxidation Or Reduction (AREA)
Description
【発明の詳細な説明】
本発明は、重水炉の減速材浄化系に係り、特に
液体ポイズンを減速材系に使用し、浄化塔樹脂に
ポイズン飽和系樹脂を使用する減速材浄化系に適
用するに好適な重水炉の減速材浄化系に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a moderator purification system for a heavy water reactor, and is particularly applicable to a moderator purification system that uses liquid poison in the moderator system and uses a poison-saturated resin as the purification tower resin. The present invention relates to a moderator purification system for heavy water reactors suitable for use in heavy water reactors.
重水炉の減速材系統の従来例を第1図に示す。
カランドリアタンク2内に減速材である重水を供
給する減速材系統は、オーバフロータンク6、オ
ーバフローポンプ7、重水循環ポンプ4、重水冷
却器8、D2O2分解装置9、重水浄化装置11、
ポイズン濃度制御系12、及び重水配分管13等
の配管類より構成される。重水出口管3は、カラ
ンドリアタンク2と重水冷却器8を連絡し、重水
循環ポンプ4を有している。重水供給管19は、
重水冷却器8と重水配分管13を連絡している。
オーバフロー管5は、カランドリアタンク2と重
水冷却器8とを連絡し、オーバフロータンク6と
オーバフローポンプ7を有している。浄化配管2
0はD2O2分解装置9、重水浄化装置11および
ポイズン濃度制御系12を連絡し、両端は重水供
給管19に取付けられる。1は鉄体しやへい体、
10はバイパス配管である。制御棒案内管15の
下部からカランドリアタンク2内に流出した重水
の大部分は、重水出口管3を経て、またその一部
はオーバフロー管5を経て重水冷却器8に入る。
ここで冷却された重水の大部分は、重水供給管1
9を通つて重水配分管13内に達し、さらに多数
の重水入口管14を経て、制御棒案内管15より
カランドリアタンク2内に戻る。しかし、重水冷
却器8から吐出される一部の重水は、D2O2分解
装置9及び重水浄化装置11、ポイズン濃度制御
系12を経由する。ここでは、重水中のポイズン
濃度制御系及び不純物除去が行なわれる。ポイズ
ン濃度制御系12は、高濃度のポイズン溶液を貯
え減速材系へ供給するポイズン供給装置と、系統
内のポイズン濃度を下げるポイズン除去装置より
成り、ポイズン除去装置には強塩基性イオン交換
樹脂が使用されている。減速材である重水中に
は、中性子吸収材としてのポイズン、例えばボロ
ンが溶解している。 A conventional example of a moderator system for a heavy water reactor is shown in Figure 1.
The moderator system that supplies heavy water, which is a moderator, into the calandria tank 2 includes an overflow tank 6, an overflow pump 7, a heavy water circulation pump 4, a heavy water cooler 8, a D 2 O 2 decomposition device 9, a heavy water purification device 11,
It is composed of a poison concentration control system 12 and piping such as a heavy water distribution pipe 13. The heavy water outlet pipe 3 connects the calandria tank 2 and the heavy water cooler 8, and has a heavy water circulation pump 4. The heavy water supply pipe 19 is
The heavy water cooler 8 and the heavy water distribution pipe 13 are connected.
The overflow pipe 5 communicates the calandria tank 2 and the heavy water cooler 8, and has an overflow tank 6 and an overflow pump 7. Purification piping 2
0 connects the D 2 O 2 decomposition device 9, the heavy water purification device 11 and the poison concentration control system 12, and both ends are attached to the heavy water supply pipe 19. 1 is an iron body,
10 is a bypass pipe. Most of the heavy water flowing out into the calandria tank 2 from the lower part of the control rod guide pipe 15 passes through the heavy water outlet pipe 3, and a part of it passes through the overflow pipe 5 and enters the heavy water cooler 8.
Most of the heavy water cooled here is from the heavy water supply pipe 1
9 and reaches the inside of the heavy water distribution pipe 13 , further passes through a large number of heavy water inlet pipes 14 , and returns to the calandria tank 2 through the control rod guide pipe 15 . However, some of the heavy water discharged from the heavy water cooler 8 passes through the D 2 O 2 decomposition device 9 , the heavy water purification device 11 , and the poison concentration control system 12 . Here, a poison concentration control system and impurity removal in heavy water are performed. The poison concentration control system 12 consists of a poison supply device that stores a highly concentrated poison solution and supplies it to the moderator system, and a poison removal device that reduces the poison concentration in the system.The poison removal device includes a strong basic ion exchange resin. It is used. Poison, such as boron, as a neutron absorber is dissolved in heavy water, which is a moderator.
重水浄化装置11には、ポイズンを除去するこ
となく、不純物を除去する為に、従来弱塩基性イ
オン交換樹脂が充填されていた。しかし、弱塩基
性イオン交換樹脂は、重水の放射線分解により生
じる過酸化重水素によつて劣化されやすいため、
劣化しにくい強塩基性イオン交換樹脂を使用する
計画が進められている。 The heavy water purification device 11 has conventionally been filled with a weakly basic ion exchange resin in order to remove impurities without removing poisons. However, weakly basic ion exchange resins are easily degraded by deuterium peroxide produced by radiolysis of heavy water.
Plans are underway to use strongly basic ion exchange resins that do not easily deteriorate.
強塩基性イオン交換樹脂を使用する場合は、ポ
イズン飽和型にする必要があるので、プラントの
起動及び停止時等、重水浄化装置入口温度が変化
した場合、樹脂のポイズン吸脱着現象により減速
材中のポイズン濃度が変化するという問題点があ
る。 When using a strongly basic ion exchange resin, it must be a poison-saturated type, so if the inlet temperature of the heavy water purification equipment changes, such as when starting or stopping the plant, the resin will absorb and desorb poisons, causing damage to the moderator. There is a problem that the concentration of poison changes.
本発明の目的は、重水浄化装置に起因する減速
材重水中ポイズン濃度変化を減少しうる重水炉の
減速材浄化系を提供するにある。 An object of the present invention is to provide a moderator purification system for a heavy water reactor that can reduce changes in the concentration of poison in heavy water moderator water caused by a heavy water purification device.
本発明の特徴は、重水浄化装置入口温度を、重
水冷却器出口温度から減速材系最低温度までの間
でのある一定温度に保つようにしたものである。 A feature of the present invention is that the heavy water purification device inlet temperature is maintained at a certain constant temperature between the heavy water cooler outlet temperature and the moderator system minimum temperature.
以下本発明の一実施例を第2図によつて説明す
る。重水浄化装置11には、ポイズン飽和型強塩
基性イオン交換樹脂が充填されている。本実施例
は、重水浄化装置11に流入する重水を、通常時
にも減速材系の最低温度10℃(浄化装置室の最低
温度)に保持するため、浄化装置の上流側へ、再
生熱交換器16、冷凍装置18を有する非再生の
冷却器17を設けたものである。運転経費を低減
するために、再生熱交換器を使用している。重水
冷却器8から吐出された重水の一部は、D2O2分
解装置9を通つて再生熱交換器16および冷却器
17で10℃まで冷却された後、重水浄化装置11
に導かれ、再生熱交換器16で加熱されてポイズ
ン濃度制御系12へと送られる。60MWeクラス
の重水炉において、浄化流量は20m3/h程度であ
るから、49℃の重水を10℃まで冷却するに要する
冷凍機電動機容量は、約120KW程度であり、特
に問題とはならない。 An embodiment of the present invention will be described below with reference to FIG. The heavy water purification device 11 is filled with a poison saturated strong basic ion exchange resin. In this embodiment, in order to maintain the heavy water flowing into the heavy water purification device 11 at the minimum temperature of the moderator system of 10°C (minimum temperature of the purification device room) even under normal conditions, a regenerative heat exchanger is installed on the upstream side of the purification device. 16, a non-regenerative cooler 17 having a refrigeration device 18 is provided. Regenerative heat exchangers are used to reduce operating costs. A portion of the heavy water discharged from the heavy water cooler 8 passes through the D 2 O 2 decomposition device 9 and is cooled to 10° C. in the regenerative heat exchanger 16 and cooler 17, and then is transferred to the heavy water purification device 11.
It is heated by the regenerative heat exchanger 16 and sent to the poison concentration control system 12. In a 60 MWe class heavy water reactor, the purification flow rate is about 20 m 3 /h, so the refrigerator motor capacity required to cool heavy water at 49° C. to 10° C. is about 120 KW, which is not a particular problem.
本実施例では、10℃保持装置に故障が発生した
場合においても、重水温度は上昇しポイズンは、
ポイズン飽和型強塩基性イオン交換樹脂から減速
材中に放出されるので原子炉を安全に停止できる
効果がある。 In this example, even if a failure occurs in the 10°C holding device, the heavy water temperature will rise and the poison will be
Since it is released into the moderator from the poison saturated strong basic ion exchange resin, it has the effect of safely shutting down the nuclear reactor.
なお、第2図では、一定保持温度を減速材最低
温度としたため、常に冷却が必要となつたが、一
定保持温度を原子炉の通常運転時の温度とするこ
とにより、冷却または加熱量を減らし、熱効率を
高めることができる。すなわち、重水浄化装置1
1の上流側において重水温度を測定し、重水温度
が所定値、例えば、原子炉の通常運転時の重水温
度を越えた時に冷凍装置18を作動して冷却器1
7で重水を冷却する。これにより原子炉の起動時
および停止時にのみ冷却器17を作動させるので
熱効率が上昇する。本実施例では、原子炉の通常
運転時には重水冷却器8による冷却のみが行なわ
れる。 In addition, in Figure 2, the constant holding temperature was set as the lowest moderator temperature, which required constant cooling, but by setting the constant holding temperature as the temperature during normal operation of the reactor, the amount of cooling or heating could be reduced. , thermal efficiency can be increased. That is, heavy water purification device 1
The heavy water temperature is measured on the upstream side of the cooler 1, and when the heavy water temperature exceeds a predetermined value, for example, the heavy water temperature during normal operation of the reactor, the refrigeration device 18 is activated to
Cool the heavy water in step 7. As a result, the cooler 17 is operated only when the reactor is started and stopped, thereby increasing thermal efficiency. In this embodiment, only cooling by the heavy water cooler 8 is performed during normal operation of the nuclear reactor.
本発明によれば、減速材中ポイズン濃度変化に
伴う浄化装置からのポイズン吸脱着量を最小にで
きるのでポイズン濃度制御性を向上させ、出力調
整用制御棒駆動回数を低減することができるとい
う効果がある。 According to the present invention, the amount of poison adsorbed and desorbed from the purification device due to changes in the poison concentration in the moderator can be minimized, thereby improving poison concentration controllability and reducing the number of times the control rod for output adjustment is driven. There is.
第1図は、重水炉の従来の減速材系統の系統
図、第2図は、本発明の一実施例である重水炉の
減速材系統の系統図である。
2……カランドリアタンク、3……重水出口
管、8……重水冷却器、11……重水浄化装置、
14……重水入口管、16……再生熱交換器、1
7……冷却器、19……重水供給管。
FIG. 1 is a system diagram of a conventional moderator system for a heavy water reactor, and FIG. 2 is a system diagram of a moderator system for a heavy water reactor according to an embodiment of the present invention. 2...Calandria tank, 3...Heavy water outlet pipe, 8...Heavy water cooler, 11...Heavy water purification device,
14...Heavy water inlet pipe, 16...Regeneration heat exchanger, 1
7...Cooler, 19...Heavy water supply pipe.
Claims (1)
たカランドリアタンクに両端が接続されて内部に
重水が流れる配管と、前記配管に設けられた浄化
装置とからなる重水炉の減速材浄化系において、
前記浄化装置内に強塩基性樹脂を充填し、前記浄
化装置の上流側で前記配管に冷却器を設けること
を特徴とする重水炉の減速材浄化系。1. A moderator purification system for a heavy water reactor consisting of a pipe whose both ends are connected to a calandria tank filled with heavy water, which is a moderator containing poison, and into which heavy water flows, and a purification device installed in the pipe.
A moderator purification system for a heavy water reactor, characterized in that the purification device is filled with a strong basic resin, and a cooler is provided in the piping upstream of the purification device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56198575A JPS58100791A (en) | 1981-12-11 | 1981-12-11 | Moderator cleaning system of heavy water reactor |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56198575A JPS58100791A (en) | 1981-12-11 | 1981-12-11 | Moderator cleaning system of heavy water reactor |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS58100791A JPS58100791A (en) | 1983-06-15 |
| JPH0250439B2 true JPH0250439B2 (en) | 1990-11-02 |
Family
ID=16393450
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56198575A Granted JPS58100791A (en) | 1981-12-11 | 1981-12-11 | Moderator cleaning system of heavy water reactor |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS58100791A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0795107B2 (en) * | 1989-04-27 | 1995-10-11 | 動力炉・核燃料開発事業団 | Power Control Method for Heavy Water Moderated Light Water Cooled Pressure Tube Reactor |
-
1981
- 1981-12-11 JP JP56198575A patent/JPS58100791A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS58100791A (en) | 1983-06-15 |
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