JPH094989A - Condensed water deaeration device - Google Patents
Condensed water deaeration deviceInfo
- Publication number
- JPH094989A JPH094989A JP15010495A JP15010495A JPH094989A JP H094989 A JPH094989 A JP H094989A JP 15010495 A JP15010495 A JP 15010495A JP 15010495 A JP15010495 A JP 15010495A JP H094989 A JPH094989 A JP H094989A
- Authority
- JP
- Japan
- Prior art keywords
- water
- valve
- condensate
- condenser
- storage tank
- 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.)
- Granted
Links
Landscapes
- Degasification And Air Bubble Elimination (AREA)
- Physical Water Treatments (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は蒸気プラントの起動時に
復水を脱気する設備に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to equipment for degassing condensate when starting a steam plant.
【0002】[0002]
【従来の技術】ボイラ給水中に酸素など非凝縮性のガス
が溶け込んでいると、ボイラや付属装置に電気的または
化学的腐食が生ずるので、これを除去しなければならな
い。ところが、プラント停止時に復水器の真空破壊を行
なった場合、復水器内の復水は空気と接触して酸素(O
2 )リッチとなる。したがって再起動時には、その復水
を十分に脱気してボイラ給水とする必要がある。2. Description of the Related Art If a non-condensable gas such as oxygen is dissolved in boiler feed water, electrical or chemical corrosion will occur in the boiler and auxiliary equipment, which must be removed. However, when the vacuum of the condenser is broken when the plant is stopped, the condensate in the condenser comes into contact with air and oxygen (O
2 ) Be rich. Therefore, at the time of restart, it is necessary to sufficiently degas the condensate and supply it to the boiler.
【0003】図3は従来の起動用復水脱気システムの一
例を示す系統図である。復水器(1)に起動用脱気器
(2)を一体に取付け、真空破壊後のホットウェル
(4)内の非脱気水を低圧給水ポンプ(5)によって起
動用脱気器(2)へ循環させ、復水を脱気する。なお図
3中(8)、(13)、(18)は復水弁、(11)は
脱気器水位調節弁、(17)は復水再循環管路である。FIG. 3 is a system diagram showing an example of a conventional condensate degassing system for startup. The deaerator (2) for start-up is integrally attached to the condenser (1), and the non-deaerated water in the hot well (4) after breaking the vacuum is removed by the low-pressure feed pump (5). ) To degas the condensate. In FIG. 3, (8), (13) and (18) are condensate valves, (11) is a deaerator water level control valve, and (17) is a condensate recirculation conduit.
【0004】[0004]
【発明が解決しようとする課題】DSS(Daily Start
& Stop)の行なわれるプラントの再起動時のように、プ
ラントを短時間で起動して通常運転に移行することが要
求される場合がある。しかし、プラント停止中に復水器
が真空破壊されていると、再起動時に脱気のため時間が
かかり要求される短時間の起動は困難であった。[Problems to be Solved by the Invention] DSS (Daily Start)
In some cases, it is required to start the plant in a short time and shift to normal operation, such as when the plant is restarted. However, if the condenser was vacuum-disrupted while the plant was stopped, it took time because of degassing at the time of restarting, and it was difficult to start it in the required short time.
【0005】[0005]
【課題を解決するための手段】本発明者は、前記従来の
課題を解決するために、復水器を有する蒸気プラントに
おいて、上記復水器のホットウェルとは別の気密の貯水
タンクと起動用脱気器とを上記復水器と一体に形成する
とともに、上記ホットウェルの底部から低圧給水ポンプ
へ至る管路に設けられた復水弁の出口に上記貯水タンク
の底部を連通させる復水弁付きの管路と、上記低圧給水
ポンプの出口からグランドコンデンサを経て上記起動用
脱気器の上部に至る復水弁付きの管路と、上記起動用脱
気器の底部から上記貯水タンクの上部に至る復水弁付き
の管路と、上記貯水タンクの上部に連通する空気抜き弁
とを設けたことを特徴とする復水脱気装置を提案するも
のである。In order to solve the above-mentioned conventional problems, the present inventor has found that in a steam plant having a condenser, an airtight water storage tank different from the hot well of the condenser and a start-up are provided. Condensate for forming a water vaporizer and a condenser together with the condenser, and for communicating the bottom of the water storage tank with the outlet of the condenser valve provided in the conduit from the bottom of the hot well to the low pressure feed pump. A conduit with a valve, a conduit with a condensate valve from the outlet of the low-pressure feed pump to the upper part of the starting deaerator through the ground condenser, and from the bottom of the starting deaerator to the water storage tank. The present invention proposes a condensate degassing device, which is provided with a pipe line with a condensate valve reaching the upper part and an air vent valve communicating with the upper part of the water storage tank.
【0006】[0006]
【作用】本発明は前記構成を有するので、プラント停止
時に起動用脱気器と貯水タンクの各空気抜き弁を閉じた
ままにしておけば、貯水タンク内の水は空気と接触しな
いから、脱気された状態に保たれる。Since the present invention has the above-described structure, if the deaerator for start-up and the air vent valves of the water storage tank are kept closed when the plant is stopped, the water in the water storage tank will not come into contact with the air, so Be kept in a good condition.
【0007】そこで再起動時は、ホットウェル・低圧給
水ポンプ間の復水弁を閉じ、貯水タンク・低圧給水ポン
プ間の復水弁と起動用脱気器・貯水タンク間の復水弁を
開いて、低圧給水ポンプを起動し、復水再循環運転をす
る。そうすると復水器内の真空度が上昇してゆく。真空
上昇完了後、グランドコンデンサ下流の復水弁を開いて
ボイラへ送水を開始し、給水系を全て運転状態としてプ
ラントを起動する。Therefore, at the time of restart, the condensate valve between the hot well and the low-pressure water supply pump is closed, and the condensate valve between the water storage tank and the low-pressure water supply pump and the condensate valve between the starting deaerator and the water storage tank are opened. Then, the low-pressure water supply pump is started and the condensate recirculation operation is performed. Then, the degree of vacuum in the condenser rises. After the vacuum rise is completed, the condensate valve downstream of the ground condenser is opened to start sending water to the boiler, and the plant is started with the entire water supply system in operation.
【0008】このように再起動時に貯水タンク内の脱気
水を再循環させて起動できるので、起動時間が短縮され
る。As described above, since the degassed water in the water storage tank can be recirculated and restarted at the time of restart, the startup time can be shortened.
【0009】[0009]
【実施例】図1は本発明の一実施例に係る復水脱気装置
を示す系統図である。FIG. 1 is a system diagram showing a condensate degassing apparatus according to an embodiment of the present invention.
【0010】復水器(1)には、起動用脱気器(2)
と、復水器のホットウェル(4)とは別の気密の貯水タ
ンク(3)とが、一体に取付けられている。復水器
(1)のホットウェル(4)と貯水タンク(3)とは、
同一レベルで復水を共有する構造になっている。貯水タ
ンク(3)の容量は定格給水量の約5分間分程度とす
る。The condenser (1) has a starter deaerator (2).
And an airtight water storage tank (3) separate from the hot well (4) of the condenser are integrally mounted. The hot well (4) of the condenser (1) and the water storage tank (3) are
It has a structure that shares condensate at the same level. The capacity of the water storage tank (3) should be about 5 minutes of the rated water supply.
【0011】ホットウェル(4)の底部から低圧給水ポ
ンプ(5)へ至る管路(6)に設けられた復水弁(8)
の出口に貯水タンク(3)の底部を連通させる管路
(7)が設けられ、この管路には復水弁(9)が設けら
れる。低圧給水ポンプ(5)の出口からグランドコンデ
ンサ(12)を経て起動用脱気器(2)の上部に至る復
水再循環管路(17)にも復水弁(18)が設けられ
る。また起動用脱気器(2)の底部から貯水タンク
(3)の上部に至る管路(10)にも、その起動用脱気
器(2)の水位を調節するため復水弁(11)が設けら
れている。更にグランドコンデンサ(12)の下流で復
水再循環管路(17)が分岐する分岐部の下流にも復水
弁(13)が設けられている。これら各弁の操作によ
り、脱気復水はそれぞれ隔離できる構造になっている。
また復水器(1)、起動用脱気器(2)、貯水タンク
(3)には、それぞれ、空気抜き弁(14a)、(14
b)、(14c)が設けられている。なお符号(15)
はレベル調節計、符号(16)はレベルスイッチをそれ
ぞれ示す。Condensate valve (8) provided in the conduit (6) from the bottom of the hot well (4) to the low pressure feed pump (5).
A conduit (7) for communicating the bottom of the water storage tank (3) is provided at the outlet of the conduit (7), and a condensate valve (9) is provided in this conduit. A condensate valve (18) is also provided in the condensate recirculation line (17) from the outlet of the low-pressure water supply pump (5) to the upper part of the starting deaerator (2) via the gland condenser (12). Further, in the conduit (10) from the bottom of the starting deaerator (2) to the upper part of the water storage tank (3), a condensate valve (11) for adjusting the water level of the starting deaerator (2). Is provided. Further, a condensate valve (13) is provided downstream of the branch portion where the condensate recirculation conduit (17) branches off downstream of the ground condenser (12). By operating each of these valves, the degassed condensate can be isolated.
Further, the condenser (1), the deaerator (2) for starting, and the water storage tank (3) are provided with air vent valves (14a) and (14), respectively.
b) and (14c) are provided. The reference numeral (15)
Is a level controller, and reference numeral (16) is a level switch.
【0012】図2は本実施例の復水器(1)の概略構造
を示す図であって、図2(a)は復水器の正面図、図2
(b)は同じく側面図、図2(c)は貯水タンク内の平
面図である。復水器(1)は起動用脱気器(2)および
貯水タンク(3)と一体の構造となっている。貯水タン
ク(3)内は仕切板によって仕切られている。FIG. 2 is a diagram showing a schematic structure of the condenser (1) of this embodiment, and FIG. 2 (a) is a front view of the condenser, and FIG.
2B is a side view of the same, and FIG. 2C is a plan view of the inside of the water storage tank. The condenser (1) has a structure integrated with the starting deaerator (2) and the water storage tank (3). The inside of the water storage tank (3) is partitioned by a partition plate.
【0013】プラント停止時には、空気抜き弁(14
a)を開いて復水器(1)内を真空破壊するが、空気抜
き弁(14b)、(14c)は閉じたままとする。した
がって、ホットウェル(4)内の水は空気と接触して酸
素等を溶け込ませることになるが、貯水タンク(3)内
の水は脱気された状態に保たれる。When the plant is stopped, the air vent valve (14
Although a) is opened and the inside of the condenser (1) is vacuum-disrupted, the air vent valves (14b) and (14c) are kept closed. Therefore, the water in the hot well (4) comes into contact with air to dissolve oxygen and the like, but the water in the water storage tank (3) is kept in a deaerated state.
【0014】再起動時は、ホットウェル(4)・低圧給
水ポンプ(5)間の復水弁(8)を閉じ、貯水タンク
(3)・低圧給水ポンプ(5)間の復水弁(9)と起動
用脱気器(2)・貯水タンク(3)間の調節弁(11)
を開いて、低圧給水ポンプ(5)を起動し、復水再循環
運転を行なう。そうすると、復水器(1)内の真空度が
上昇してゆく。真空上昇完了後、グランドコンデンサ
(12)下流の復水弁(13)を開いてボイラへ送水を
開始し、給水系を全て運転状態としてプラントを起動す
る。At the time of restart, the condensate valve (8) between the hot well (4) and the low pressure feed pump (5) is closed, and the condensate valve (9) between the water storage tank (3) and the low pressure feed pump (5) is closed. ) And the deaerator (2) for starting and the water storage tank (3) between the control valve (11)
Is opened, the low-pressure feed pump (5) is started, and the condensate recirculation operation is performed. Then, the degree of vacuum in the condenser (1) rises. After the vacuum rise is completed, the condensate valve (13) downstream of the ground condenser (12) is opened to start feeding water to the boiler, and the plant is started with all the water supply systems in operation.
【0015】このように、再起動時に貯水タンク(3)
内の水とホットウェル(4)内の水を共有している、す
なわち両者の圧力がバランスし、復水のレベルが一定に
保たれているので、貯水タンク(3)内の脱気水を再循
環させて起動でき、したがって起動時間が短縮される。Thus, at the time of restart, the water storage tank (3)
The water inside the hot well (4) is shared, that is, the pressures of the two are balanced and the condensate level is kept constant. It can be recirculated and activated, thus reducing activation time.
【0016】[0016]
【発明の効果】本発明の復水脱気装置によれば、再起動
時に貯水タンク内の脱気された水を再循環させて起動で
きるので、プラントの起動時間が短縮される。したがっ
てDSS停止時などに従来のように循環水ポンプを常時
運転して真空を保持する必要がなくなる。それに伴って
ポンプ動力費が節減でき、省エネルギープラントが実現
できる。According to the condensate degassing apparatus of the present invention, since the degassed water in the water storage tank can be recirculated and started at the time of restart, the start-up time of the plant can be shortened. Therefore, when the DSS is stopped, there is no need to constantly operate the circulating water pump to maintain the vacuum unlike the conventional case. As a result, the pump power cost can be reduced and an energy-saving plant can be realized.
【図1】図1は本発明の一実施例に係る復水脱気装置を
示す系統図である。FIG. 1 is a system diagram showing a condensate degassing apparatus according to an embodiment of the present invention.
【図2】図2は上記実施例の復水器の概略構造を示す図
であって、図2(a)は復水器の正面図、図2(b)は
同じく側面図、図2(c)は貯水タンク内の平面図であ
る。FIG. 2 is a view showing a schematic structure of the condenser of the above embodiment, FIG. 2 (a) is a front view of the condenser, FIG. 2 (b) is a side view thereof, and FIG. c) is a plan view of the inside of the water storage tank.
【図3】図3は従来の起動用復水脱気システムの一例を
示す系統図である。FIG. 3 is a system diagram showing an example of a conventional condensate degassing system for startup.
(1) 復水器 (2) 起動用脱気器 (3) 貯水タンク (4) ホットウェル (5) 低圧給水ポンプ (6)、(7) 管路 (8)、(9) 復水弁 (10) 管路 (11) 復水弁(脱気器水位調
節弁) (12) グランドコンデンサ (13) 復水弁 (14a)、(14b)、(14c) 空気抜き弁 (15) レベル調節計 (16) レベルスイッチ (17) 復水再循環管路 (18) 復水弁(1) Condenser (2) Deaerator for start-up (3) Water storage tank (4) Hot well (5) Low-pressure water supply pump (6), (7) Pipe line (8), (9) Condensate valve ( 10) Pipe line (11) Condensation valve (deaerator water level control valve) (12) Ground condenser (13) Condensation valve (14a), (14b), (14c) Air vent valve (15) Level controller (16) ) Level switch (17) Condensate recirculation line (18) Condensate valve
Claims (1)
上記復水器のホットウェルとは別の気密の貯水タンクと
起動用脱気器とを上記復水器と一体に形成するととも
に、上記ホットウェルの底部から低圧給水ポンプへ至る
管路に設けられた復水弁の出口に上記貯水タンクの底部
を連通させる復水弁付きの管路と、上記低圧給水ポンプ
の出口からグランドコンデンサを経て上記起動用脱気器
の上部に至る復水弁付きの管路と、上記起動用脱気器の
底部から上記貯水タンクの上部に至る復水弁付きの管路
と、上記貯水タンクの上部に連通する空気抜き弁とを設
けたことを特徴とする復水脱気装置。1. In a steam plant having a condenser,
An airtight water storage tank different from the hot well of the condenser and a deaerator for starting are integrally formed with the condenser, and are provided in a pipe line from the bottom of the hot well to the low pressure feed pump. A conduit with a condensate valve that connects the bottom of the water storage tank to the outlet of the condensate valve, and a condensate valve from the outlet of the low-pressure feed pump through the ground condenser to the top of the deaerator for start-up. Condensate characterized in that a conduit, a conduit with a condensate valve from the bottom of the starting deaerator to the upper part of the water storage tank, and an air vent valve communicating with the upper part of the water storage tank are provided. Degassing device.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15010495A JP3615831B2 (en) | 1995-06-16 | 1995-06-16 | Condensate deaerator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP15010495A JP3615831B2 (en) | 1995-06-16 | 1995-06-16 | Condensate deaerator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH094989A true JPH094989A (en) | 1997-01-10 |
JP3615831B2 JP3615831B2 (en) | 2005-02-02 |
Family
ID=15489597
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP15010495A Expired - Lifetime JP3615831B2 (en) | 1995-06-16 | 1995-06-16 | Condensate deaerator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3615831B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103573306A (en) * | 2013-11-12 | 2014-02-12 | 中国电力工程顾问集团西南电力设计院 | Starting system for thermal power plant adjacent machine auxiliary steam heating boiler |
-
1995
- 1995-06-16 JP JP15010495A patent/JP3615831B2/en not_active Expired - Lifetime
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN103573306A (en) * | 2013-11-12 | 2014-02-12 | 中国电力工程顾问集团西南电力设计院 | Starting system for thermal power plant adjacent machine auxiliary steam heating boiler |
Also Published As
Publication number | Publication date |
---|---|
JP3615831B2 (en) | 2005-02-02 |
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