JPS6256401B2 - - Google Patents
Info
- Publication number
- JPS6256401B2 JPS6256401B2 JP55024896A JP2489680A JPS6256401B2 JP S6256401 B2 JPS6256401 B2 JP S6256401B2 JP 55024896 A JP55024896 A JP 55024896A JP 2489680 A JP2489680 A JP 2489680A JP S6256401 B2 JPS6256401 B2 JP S6256401B2
- Authority
- JP
- Japan
- Prior art keywords
- condensate
- condenser
- water
- storage tank
- water storage
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 59
- 238000000746 purification Methods 0.000 description 12
- 230000005856 abnormality Effects 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 230000007797 corrosion Effects 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000003628 erosive effect Effects 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 230000003139 buffering effect Effects 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 238000003908 quality control method Methods 0.000 description 1
- 239000008400 supply water Substances 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
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
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
Description
【発明の詳細な説明】
〔発明の目的〕
(産業上の利用分野)
本発明は蒸気原動所設備に係り、特に復水器よ
り抽出した復水を復水器に接続した貯水槽を介し
て蒸気発生装置に供給するようにした蒸気原動所
設備の改良に関する。[Detailed Description of the Invention] [Objective of the Invention] (Industrial Field of Application) The present invention relates to steam power plant equipment, and in particular, to a system for transferring condensate extracted from a condenser through a water storage tank connected to the condenser. This invention relates to improvements in steam power station equipment that supplies steam to steam generators.
(従来の技術および発明が解決しようとする問題
点)
一般に、原子力発電プラント等の蒸気原動所設
備における復水供給系は、高圧の原子炉等へ多量
の給水を送るため、数種類のポンプが直列に配設
されている。したがつて、単一のポンプの異常が
プラントの運転全体に与える影響が非常に大き
く、またプラント内の殆どの流体は復水器に回収
されるため、復水器には腐食生成物等が流入しや
すい。(Prior art and problems to be solved by the invention) In general, condensate supply systems in steam power plant equipment such as nuclear power plants have several types of pumps connected in series in order to send a large amount of water to high-pressure reactors, etc. It is located in Therefore, an abnormality in a single pump has a very large effect on the overall operation of the plant, and most of the fluid in the plant is collected in the condenser, so the condenser is prone to corrosion products, etc. Easy to flow in.
さらに、復水器の冷却水は主に海水が使用され
るため、海水の漏洩が発生すると原子炉内等に流
入する恐れがあり重大な問題となる。 Furthermore, since seawater is mainly used as cooling water for the condenser, if seawater leaks, it may flow into the reactor, which poses a serious problem.
そこで、復水器より抽出した復水を復水浄化装
置で浄化した後一時貯水槽に回収するとともに、
その貯水槽に復水器への戻しラインを設置するこ
とによつて、水量および水質管理の点で緩衝効果
をもたせることが提案されている。 Therefore, the condensate extracted from the condenser is purified by a condensate purification device and then collected in a temporary water tank.
It has been proposed to provide a buffering effect in terms of water quantity and water quality control by installing a return line to the condenser in the water storage tank.
すなわち、第1図は従来のこの種装置の概略系
統図であつて、タービン1から排出された排気蒸
気は復水器2で間接冷却され凝縮せしめられて復
水となり、ホツトウエル3に集められる。このホ
ツトウエル3に集められた復水は循環ポンプ4に
よつて抽出昇圧された後、復水浄化装置5,6に
送られ、そこで原子炉等(図示せず)に給水する
のに十分な水質に浄化した後、熱交換器7を経て
貯水槽8に送給される。そして、上記貯水槽8内
の復水が復水ポンプ9によつて再び昇圧され、図
示しない高圧熱交換器によつて加熱されて原子炉
等に供給される。 That is, FIG. 1 is a schematic system diagram of a conventional device of this kind, in which exhaust steam discharged from a turbine 1 is indirectly cooled and condensed in a condenser 2 to become condensed water, which is collected in a hot well 3. The condensate collected in this hot well 3 is extracted and pressurized by a circulation pump 4, and then sent to condensate purification devices 5 and 6, where the water quality is sufficient to supply water to a nuclear reactor etc. (not shown). After being purified, it is sent to a water storage tank 8 via a heat exchanger 7. Then, the condensate in the water storage tank 8 is again pressurized by the condensate pump 9, heated by a high-pressure heat exchanger (not shown), and supplied to a nuclear reactor or the like.
一方、上記貯水槽8は調節弁10を有する戻し
ライン11を介して前記復水器2に接続されてお
り、上記貯水槽8内の水位を検出する水位検出器
12からの信号によつて上記調節弁10を開閉制
御することにより、貯水槽8から戻しライン11
を経て復水器2へ戻される水量が調節される。 On the other hand, the water tank 8 is connected to the condenser 2 via a return line 11 having a control valve 10, and the water level in the water tank 8 is detected by a signal from a water level detector 12 that detects the water level in the water tank 8. By controlling the opening and closing of the control valve 10, the return line 11 is removed from the water tank 8.
The amount of water returned to the condenser 2 via the .
ところで、原子力発電プラントの場合、このよ
うに復水浄化装置5,6を含む系統と原子炉への
給水系統を各々独立にし、中間に貯水槽8を設け
た構成では、循環ポプ4等の復水浄化装置を含む
系統内の機器および装置に異常があつた場合に、
貯水槽8に貯えられた復水があるために瞬時に原
子炉側への給水に影響を及ぼすことがなく、その
間にすみやかな制御操作を行なうことによりプラ
ントの安全な停止または出力低下を行なうことが
できる。すなわち、復水浄化装置を含む系統の異
常が発生したことが検知されたら、直ちに原子炉
側への出力低下または停止の信号を出せば、貯水
槽8の貯水があるため、前面給水喪失に到る恐れ
は非常に少なくなる。また、復水浄化装置を含む
系統を単独に運転できるためにプラント起動前に
水浄化および系統内の配管および機器の洗浄を十
分に実施することができる。さらに、プラントの
出力変動と関係なく復水浄化装置を通過する復水
量を一定にすることができ、浄化能力を高く維持
することができる等の種々優れた点がある。 By the way, in the case of a nuclear power plant, in a configuration in which the system including the condensate purification devices 5 and 6 and the water supply system to the reactor are made independent, and the water storage tank 8 is provided in the middle, If there is an abnormality in the equipment or equipment in the system, including water purification equipment,
Because there is condensate stored in the water storage tank 8, there is no instantaneous effect on the water supply to the reactor side, and by performing prompt control operations during that time, the plant can be safely shut down or the output reduced. Can be done. In other words, if it is detected that an abnormality has occurred in the system including the condensate purification system, if a signal is immediately sent to the reactor to reduce the output or stop the reactor, water will be stored in the water tank 8, so the front water supply will be lost. The risk of this happening is greatly reduced. Furthermore, since the system including the condensate purification device can be operated independently, water purification and piping and equipment in the system can be sufficiently cleaned before starting the plant. Furthermore, it has various advantages such as being able to keep the amount of condensate passing through the condensate purification device constant regardless of fluctuations in the output of the plant, and maintaining a high purification capacity.
しかし、このような復水系統においては、貯水
槽8の上流と下流の流量の不一致によつて貯水槽
8の水位が変化すること、および大容量の循環ポ
ンプによつて抽出された飽和温度の復水が熱交換
器によつて加熱され、貯水槽8で一部気化するた
め、復水器2と貯水槽8とは互いにバランスさせ
ておく必要がある。そのため、従来装置において
も、第1図に示すように、貯水槽8と復水器2と
はバランス管13によつて互いに連通せしめられ
ている。しかして、貯水槽8内で気化した蒸気は
このバランス管13を経由して復水器2に流れる
が、復水器器内は真空域であるため、蒸気の比容
積が大きく、バランス管13の侵食や振動等を考
慮すると、バランス管13の口径は1000mmφを超
える程度の大口径となる。また、これは熱交換器
7で与えられた熱を逃がすことになり、プラント
の効率を低下させることとなる。さらに、復水器
2へ逃がした蒸気分だけ復水ポンプ9への送水が
減少することとなり、この減少分を補償するため
循環ポンプ4、復水浄化装置5,6、熱交換器7
等は容量を増加する必要があり、設備費が増大す
るとともに、循環ポンプ4の運転動力の損失をも
招く等の不都合がある。 However, in such a condensate system, the water level of the water tank 8 changes due to the mismatch between the flow rates upstream and downstream of the water tank 8, and the saturation temperature extracted by the large-capacity circulation pump changes. Since the condensate is heated by the heat exchanger and partially vaporized in the water tank 8, the condenser 2 and the water tank 8 need to be balanced with each other. Therefore, in the conventional device as well, the water storage tank 8 and the condenser 2 are communicated with each other through the balance pipe 13, as shown in FIG. The steam vaporized in the water storage tank 8 flows to the condenser 2 via the balance pipe 13, but since the inside of the condenser is a vacuum region, the specific volume of the steam is large, and the balance pipe 13 Considering corrosion, vibration, etc., the diameter of the balance tube 13 will be large, exceeding 1000 mmφ. Moreover, this causes the heat given by the heat exchanger 7 to escape, reducing the efficiency of the plant. Furthermore, the amount of water sent to the condensate pump 9 is reduced by the amount of steam released to the condenser 2, and in order to compensate for this decrease, the circulation pump 4, condensate purifiers 5 and 6, and heat exchanger 7 are used.
etc., it is necessary to increase the capacity, and there are disadvantages such as an increase in equipment costs and a loss of operating power for the circulation pump 4.
本発明はこのような点に鑑み、上述の如き不都
合がなく信頼性の高い蒸気原動所設備を提供する
ことを目的とする。 In view of these points, it is an object of the present invention to provide highly reliable steam power plant equipment that is free from the above-mentioned disadvantages.
本発明は復水器から抽出された復水を復水器に
接続した貯水槽を介して蒸気発生装置に供給する
ようにした蒸気原動所設備において、上記貯水槽
と復水器とを絞り装置を設けたバランス管路を介
して互いに連通せしめたことを特徴とするもので
ある。
The present invention provides a steam power station facility in which condensate extracted from a condenser is supplied to a steam generator via a water storage tank connected to the condenser, and a throttle device that connects the water storage tank and the condenser. This feature is characterized in that they are communicated with each other via a balanced conduit provided with.
(実施例)
以下、第2図を参照して本発明の一実施例につ
いて説明する。(Example) An example of the present invention will be described below with reference to FIG.
第2図において、循環ポンプ4によつて復水器
2より抽出昇圧された復水は、復水浄化装置5,
6および熱交換器7を経て貯水槽8へ送られる。 In FIG. 2, the condensate extracted and pressurized from the condenser 2 by the circulation pump 4 is transferred to the condensate purification device 5,
6 and a heat exchanger 7 before being sent to a water storage tank 8.
貯水槽8内の復水の一部は戻しライン11によ
つて復水器3へ戻され、残りの復水が復水ポンプ
9を経て原子炉等に供給される。また、貯水槽8
内で蒸発した蒸気はバランス管13を経て復水器
2へと返流される。 A portion of the condensate in the water storage tank 8 is returned to the condenser 3 via a return line 11, and the remaining condensate is supplied to a nuclear reactor or the like via a condensate pump 9. In addition, water tank 8
The steam evaporated inside is returned to the condenser 2 via the balance pipe 13.
以上は、第1図に示した従来装置と同一である
が、本発明においては上記バランス管13の途中
に絞り装置14が設けられている。 The above is the same as the conventional device shown in FIG. 1, but in the present invention, a throttle device 14 is provided in the middle of the balance tube 13.
ところで、上記絞り装置14は、貯水槽8内の
圧力を熱交換器7以降の復水温度の飽和圧力程度
に保つのに十分な絞りを与えるオリフイスの如き
ものであり、復水ポンプ等の復水系統の機器に異
常が発生し、貯水槽8内の復水のみによつて原子
炉等への給水が行なわれる場合、バランス管13
の絞り装置14によつて貯水槽8内の圧力が低下
し、それによつて復水ポンプ9の負荷が増大する
ような絞りを与えない程度であることが必要であ
る。また、バランス管13の口径の縮少化を考慮
した場合、バランス管13の振動、侵食などを防
止するには、最高でもバランス管13内の蒸気流
量を1/2程度におさえる必要があり、前記絞り装
置は少なくともこの条件を満す圧力を印加できる
程度のものとすることが望ましい。 By the way, the throttle device 14 is like an orifice that provides enough throttle to maintain the pressure in the water storage tank 8 at about the saturation pressure of the condensate temperature after the heat exchanger 7, and is used for condensate pumps etc. If an abnormality occurs in water system equipment and water is supplied to the reactor etc. only by condensed water in the water storage tank 8, the balance pipe 13
It is necessary that the throttle device 14 does not reduce the pressure in the water tank 8 and thereby increase the load on the condensate pump 9. In addition, when considering the reduction in the diameter of the balance tube 13, in order to prevent vibration and erosion of the balance tube 13, it is necessary to suppress the steam flow rate in the balance tube 13 to about 1/2 at the most. It is desirable that the expansion device is capable of applying at least a pressure that satisfies this condition.
しかして、貯水槽8内で発生した蒸気はバラン
ス管13によつて復水器2に返流されるが、この
場合上記バランス管13には絞り装置14が設け
られているので、貯水槽8内と復水器2との間に
圧力差が生じ、貯水槽8内圧力が高まり、復水の
蒸気発生量が抑制される。したがつて、これに伴
ないバランス管13の口径の縮少化を画ることが
でき、大口径バランス管内を多量の蒸気が流れる
ことによつて生じる振動や、管の侵食などの問題
を解消することができる。また、従来装置におい
ては貯水槽8内で発生した多量の蒸気を全て復水
器2へ逃がすため、復水ポンプ9への流量の減少
をもたらすと同時に、熱交換器7で与えられた熱
量をそのまま全て復水器2へ逃がしてしまうこと
となり、その分熱量の損失となるが、本発明にお
いてはバランス管13に絞り装置14が設けられ
ているので、貯水槽8内の圧力が高まり、復水の
蒸気発生量が減少せしめられ、それによつて復水
ポンプ9への流量の減少や熱量の損失が防止され
る。 Thus, the steam generated in the water storage tank 8 is returned to the condenser 2 through the balance pipe 13, but in this case, since the balance pipe 13 is equipped with a throttle device 14, the water storage tank 8 A pressure difference is generated between the inside and the condenser 2, the pressure inside the water storage tank 8 increases, and the amount of steam generated from the condensate is suppressed. Therefore, the diameter of the balance tube 13 can be reduced accordingly, and problems such as vibration and tube erosion caused by a large amount of steam flowing through the large-diameter balance tube can be solved. can do. In addition, in the conventional device, all of the large amount of steam generated in the water storage tank 8 is released to the condenser 2, which reduces the flow rate to the condensate pump 9, and at the same time reduces the amount of heat given by the heat exchanger 7. All of it will be released to the condenser 2, resulting in a loss of heat, but in the present invention, the balance pipe 13 is provided with a throttle device 14, so the pressure inside the water tank 8 increases and the condenser is lost. The amount of water vapor produced is reduced, thereby preventing a reduction in the flow rate to the condensate pump 9 and a loss of heat.
以上説明したように、本発明においては復水器
より抽出した復水を復水浄化装置で浄化した後の
系統に貯水槽および復水器への戻しラインを有す
る復水系統において、貯水槽と復水器とを接続す
るバランス管に貯水槽内圧力を復水の飽和圧力程
度に高めるような絞り装置を設けたので、貯水槽
内の復水の蒸発量を抑えることができ、それに伴
なつてバランス管の口径の縮少化、復水ポンプへ
の復水流量の減少の防止並びに復水の熱量の損失
防止等を画ることができる等の効果を奏する。
As explained above, in the present invention, in a condensate system that has a water storage tank and a return line to the condenser after the condensate extracted from the condenser is purified by the condensate purification device, the water storage tank and A throttling device is installed in the balance pipe that connects the condenser to increase the pressure inside the water storage tank to about the saturation pressure of the condensate, so it is possible to suppress the amount of evaporation of the condensate in the water storage tank. This has the effect of reducing the diameter of the balance pipe, preventing a decrease in the flow rate of condensate to the condensate pump, and preventing loss of heat in the condensate.
第1図は従来の蒸気原動所設備の概略系統図、
第2図は本発明における蒸気原動所設備の概略系
統図である。
1…タービン、2…復水器、4…循環ポンプ、
5,6…復水浄化装置、8…貯水槽、9…復水ポ
ンプ、10…調節弁、13…バランス管、14…
絞り装置。
Figure 1 is a schematic diagram of conventional steam power plant equipment.
FIG. 2 is a schematic system diagram of the steam power station equipment in the present invention. 1...Turbine, 2...Condenser, 4...Circulation pump,
5, 6...Condensate purification device, 8...Water tank, 9...Condensate pump, 10...Control valve, 13...Balance pipe, 14...
Squeezing device.
Claims (1)
た貯水槽を介して蒸気発生装置に供給するように
した蒸気原動所設備において、上記貯水槽と復水
器とを絞り装置を設けたバランス管路を介して互
いに連通せしめたことを特徴とする、蒸気原動所
設備。1. In steam power plant equipment in which condensate extracted from a condenser is supplied to a steam generator via a water storage tank connected to the condenser, a throttling device is installed to connect the water storage tank and the condenser. 1. Steam power station equipment, characterized in that the equipment is connected to each other via balanced pipelines.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2489680A JPS56120991A (en) | 1980-02-29 | 1980-02-29 | Steam generator facility |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2489680A JPS56120991A (en) | 1980-02-29 | 1980-02-29 | Steam generator facility |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56120991A JPS56120991A (en) | 1981-09-22 |
| JPS6256401B2 true JPS6256401B2 (en) | 1987-11-25 |
Family
ID=12150941
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2489680A Granted JPS56120991A (en) | 1980-02-29 | 1980-02-29 | Steam generator facility |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS56120991A (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015190719A (en) * | 2014-03-28 | 2015-11-02 | 三浦工業株式会社 | Boiler system |
-
1980
- 1980-02-29 JP JP2489680A patent/JPS56120991A/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2015190719A (en) * | 2014-03-28 | 2015-11-02 | 三浦工業株式会社 | Boiler system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56120991A (en) | 1981-09-22 |
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