JP3366817B2 - Condenser - Google Patents
CondenserInfo
- Publication number
- JP3366817B2 JP3366817B2 JP33186696A JP33186696A JP3366817B2 JP 3366817 B2 JP3366817 B2 JP 3366817B2 JP 33186696 A JP33186696 A JP 33186696A JP 33186696 A JP33186696 A JP 33186696A JP 3366817 B2 JP3366817 B2 JP 3366817B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- condenser
- tube nest
- water storage
- storage chamber
- 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 - Fee Related
Links
Landscapes
- Engine Equipment That Uses Special Cycles (AREA)
- Degasification And Air Bubble Elimination (AREA)
Description
【0001】[0001]
【発明の属する技術分野】本発明は復水器の改良に係わ
り、特に管巣部と凝縮水を貯水するホットウェル部とが
区画壁(天井板)を介して区分されている復水器に関する
ものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an improvement of a condenser, and more particularly to a condenser in which a tube nest portion and a hot well portion for storing condensed water are separated by a partition wall (ceiling plate). It is a thing.
【0002】[0002]
【従来の技術】火力発電プラントでは、プラント停止中
は、復水器の真空破壊を行うのが一般的である。この場
合、復水器ホットウェルに貯水されている復水が酸素を
吸収し、再起動時の復水の溶存酸素濃度は高くなり、こ
の復水をボイラに給水するとボイラに腐食などの不具合
を生じる恐れがある。このため、プラントの起動時には
必ず復水器のホットウェル部に貯水されている溶存酸素
濃度の高い復水を、復水器出口と連結された復水再循環
系統により再循環させると同時に脱気用加熱蒸気により
脱気運転を行う必要がある。2. Description of the Related Art In a thermal power plant, it is general that the condenser vacuum is broken while the plant is stopped. In this case, the condensate stored in the condenser hot well absorbs oxygen, and the dissolved oxygen concentration of the condensate at the time of restart becomes high.If this condensate is supplied to the boiler, corrosion such as corrosion to the boiler will occur. May occur. Therefore, when the plant is started, the condensate with high dissolved oxygen concentration, which is stored in the hot well of the condenser, is always recirculated by the condensate recirculation system connected to the condenser outlet and at the same time degassed. It is necessary to perform degassing operation with the heating steam for use.
【0003】ところで、ガスタービンと蒸気タービンを
用いた複合発電プラント等ではシステムの簡素化、機器
設備費の低減、熱効率の向上といった理由より、給水系
統に脱気器を設置しない場合があり、その場合には脱気
機能を有する脱気復水器が用いられる。By the way, in a combined power generation plant or the like using a gas turbine and a steam turbine, a deaerator may not be installed in the water supply system for the reason of system simplification, reduction of equipment cost, and improvement of thermal efficiency. In some cases, a deaeration condenser having a deaeration function is used.
【0004】従来一般に採用されているこの種の蒸気タ
ービン用復水器は、復水器ホットウェル内に貯水する復
水の脱気手段を備えており、脱気された復水と復水器ホ
ットウェルに貯水されている溶存酸素濃度の高い復水と
の直接混合を防止する区画壁,すなわち天井板が設置さ
れていて、天井板上に導入された復水は天井板を通り復
水器ホットウェルに送られる。The steam turbine condenser of this type that has been generally adopted in the past has a deaeration means for condensing the water stored in the condenser hot well. A partition wall that prevents direct mixing with condensate with a high dissolved oxygen concentration stored in the hot well, that is, a ceiling plate is installed, and the condensate introduced on the ceiling plate passes through the ceiling plate and the condenser. Sent to hotwell.
【0005】そしてホットウェルに送られた復水は、ホ
ットウェル内に流路を形成するように具備された仕切板
に沿って流動し、復水器出口に送られるように形成され
ているのが普通である。なお、この種の復水器に関連す
るものとしては、例えば特開平5−79776号公報が
挙げられる。The condensate sent to the hot well flows along a partition plate provided so as to form a flow path inside the hot well, and is sent to the condenser outlet. Is normal. In addition, as a thing related to this type of condenser, for example, Japanese Unexamined Patent Publication No. Hei 5-79776 can be cited.
【0006】[0006]
【発明が解決しようとする課題】このように形成されて
いる復水器,すなわち管巣部と復水器ホットウェル部と
を天井板等で区分する構造と復水器ホットウェル内に流
路を形成する仕切板を具備している復水器では、復水器
ホットウェルの復水を貯水する部分の水位は、プラント
運転時の復水流量と復水器の全体寸法により決められる
最適値に制御されている。The condenser thus formed, that is, the structure in which the tube nest portion and the condenser hot well portion are divided by a ceiling plate or the like, and the flow passage in the condenser hot well are provided. In a condenser equipped with a partition plate that forms a condenser, the water level of the condenser hotwell condensate is optimally determined by the condensate flow rate during plant operation and the overall condenser size. Controlled by.
【0007】通常の運転状態では、蒸気を凝縮する管巣
部の圧力と復水器ホットウェルの復水を貯水する部分の
圧力は均圧となっているが、プラントの運転状態、例え
ば、蒸気タービンの排気蒸気を凝縮する冷却管巣部の防
汚のために復水器の逆洗運転を行なう場合は、一時的に
冷却管巣を通過する冷却水量が零となり、復水器の真空
度が低下し、管巣部の圧力が上昇することになる。In a normal operating state, the pressure in the tube nest for condensing steam and the pressure in the portion for storing the condensate in the condenser hot well are equal, but in the operating state of the plant, for example, steam When backwashing the condenser to prevent fouling of the cooling tube nest that condenses the turbine exhaust steam, the amount of cooling water passing through the cooling tube nest temporarily becomes zero, and the degree of vacuum of the condenser is reduced. Will decrease and the pressure in the tube nest will rise.
【0008】このように、一時的に管巣部の圧力が上昇
する場合は、復水器ホットウェルの貯水部は、前述のよ
うに管巣部と分離されている構造となっているため、復
水器ホットウェルの貯水部は、管巣部の圧力からの圧力
伝幡の遅れにより、管巣部との間に圧力差を生じる。こ
の圧力差に起因して復水器ホットウェル内で水面波が起
こり、復水器ホットウェルの水位が変動するという課題
があり、この水位変動を小さくする有効な手段が望まれ
ていた。As described above, when the pressure at the tube nest portion temporarily rises, the water storage portion of the condenser hot well has a structure separated from the tube nest portion as described above. In the water reservoir of the condenser hot well, a pressure difference is generated between the reservoir and the tube nest due to the delay of pressure transfer from the pressure in the tube nest. There is a problem that a water surface wave occurs in the condenser hot well due to this pressure difference, and the water level of the condenser hot well fluctuates, and an effective means for reducing this water level fluctuation has been desired.
【0009】本発明はこれに鑑みなされたもので、その
目的とするところは、管巣部の圧力が一時的に上昇する
復水器逆洗運転等のプラントの運転状態においても、復
水ホットウェル部の水位変動を軽減することのでき、プ
ラントの運転に支障を来すことのないこの種の復水器を
提供するにある。The present invention has been made in view of the above, and an object thereof is to condensate hot even in an operating state of a plant such as a condenser backwashing operation in which the pressure in the tube nest temporarily rises. It is an object of the present invention to provide a condenser of this kind that can reduce fluctuations in the water level in the well and that does not hinder the operation of the plant.
【0010】[0010]
【課題を解決するための手段】本発明は、タービンより
流入する蒸気を凝縮する管巣部と、この管巣部で凝縮さ
れた凝縮水を脱気する脱気室と、前記脱気室との通水部
を有する隔離板によって前記脱気室と分割された貯水室
と、前記脱気室と前記管巣部の間に配置され、前記貯水
室と管巣部とを仕切り、前記管巣部から落下した凝縮水
を前記脱気室に流入させる区画壁を有する復水器におい
て、前記貯水室と管巣部との両室間に前記管巣部から落
下での圧力上昇による前記貯水室の水面波の発生を抑制
する無通水性で、かつ通気性を有する連通手段を備えた
ことである。 SUMMARY OF THE INVENTION
The tube nest that condenses the inflowing steam and the condensation inside this tube nest
A degassing chamber for degassing the condensed water collected, and a water passage between the degassing chamber
Reservoir separated from the deaeration chamber by a separator having a
And disposed between the deaeration chamber and the tube nest,
Condensed water that has separated from the chamber and the tube nest, and has fallen from the tube nest
In a condenser having a partition wall that allows air to flow into the deaeration chamber
Between the water storage chamber and the tube nest.
Suppressing the generation of surface waves in the water storage chamber due to pressure rise below
Equipped with a non-water-permeable and breathable communication means
That is.
【0011】またこの場合、前記連通手段を、前記ホッ
トウェル水面に対向した部分に、ほぼ平等間隔に複数個
設けるようにしたものである。また、前記連通手段の開
口面積を、前記ホットウェル水面の面積の0.2%以上
75%以下に形成するようにしたものである。Further, in this case, a plurality of the communication means are provided in the portion facing the water surface of the hot well at substantially equal intervals. Further, the opening area of the communication means is formed to be 0.2% or more and 75% or less of the area of the water surface of the hot well.
【0012】すなわちこのように形成された復水器であ
ると、復水ホットウェルの貯水部とタービンより流入す
る蒸気を凝縮する管巣部を区分する区画壁に無通水有通
気部が設けられていることから、脱気された復水と溶存
酸素濃度の高い復水との直接混合を防止しつつ、管巣部
と復水器ホットウェルの貯水部との圧力の伝幡がよくな
り、差圧に起因して生ずる復水器ホットウェルの水位変
動を防止することができ、したがって管巣部の圧力が一
時的に上昇する復水器逆洗運転等のプラントの運転状態
においても、復水ホットウェル部の水位変動を軽減する
ことのできるのである。That is, in the condenser thus formed, a water impervious section is provided on the partition wall for partitioning the water storage section of the condensing hot well and the tube nest section for condensing the steam flowing from the turbine. Therefore, while preventing direct mixing of degassed condensate and condensate with high dissolved oxygen concentration, the pressure transfer between the tube nest and the reservoir of the condenser hot well is improved. , It is possible to prevent the fluctuation of the water level of the condenser hot well caused by the differential pressure, and therefore, even in the operating state of the plant such as the condenser backwash operation in which the pressure in the tube nest temporarily rises, It is possible to reduce the fluctuation of the water level in the condensate hot well part.
【0013】[0013]
【発明の実施の形態】以下図示した実施例に基づいて本
発明を詳細に説明する。図1にはその復水器およびこれ
に連なる外部配管系が示されている。図中1が復水器で
あり、2がその管巣部、19が貯水室である。復水器1
は管巣2、隔離板15で分割された脱気室17および貯
水室19、天井板10、仕切板11等により構成されて
いる。なお、図2は、この復水器の構成を示す立体図で
あり、図3は図2のA−A断面図、図5は図2のB−B
断面図、図4は図3のA部分の詳細図を示している。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail based on the embodiments shown in the drawings. FIG. 1 shows the condenser and an external piping system connected to the condenser. In the figure, 1 is a condenser, 2 is its tube nest, and 19 is a water storage chamber. Condenser 1
Is composed of a tube nest 2, a deaeration chamber 17 divided by a separator 15, a water storage chamber 19, a ceiling plate 10, a partition plate 11 and the like. 2 is a three-dimensional view showing the structure of this condenser, FIG. 3 is a sectional view taken along line AA of FIG. 2, and FIG. 5 is taken along line BB of FIG.
FIG. 4 is a sectional view showing a detailed view of a portion A in FIG.
【0014】本発明の復水器1には、図3に示すような
天井板10上を流れる復水および管巣部2より落下した
復水が貯水室19に流入しない構造を持ち、かつ管巣部
2と貯水部19とが通気するように形成された通気装置
22が設けられている。The condenser 1 of the present invention has a structure in which the condensate flowing on the ceiling plate 10 and the condensate dropped from the tube nest 2 do not flow into the water storage chamber 19 as shown in FIG. A ventilation device 22 is provided so that the nest portion 2 and the water storage portion 19 are ventilated.
【0015】この通気装置22は、図4にその詳細が示
されているように、天井板10上を復水が流れる場合
に、復水が貯水室19に流れ込まない様に堰22aを持
っている。なお、この堰22aの高さbの寸法は、天井
板10上部の復水量と脱気室19へ流入する流路の断面
積により決定される。As shown in detail in FIG. 4, the ventilation device 22 has a weir 22a so that the condensed water does not flow into the water storage chamber 19 when the condensed water flows on the ceiling plate 10. There is. The height b of the weir 22a is determined by the amount of condensed water above the ceiling plate 10 and the cross-sectional area of the flow path flowing into the degassing chamber 19.
【0016】また、堤22aの上部にはカバー22bが
設けられ、管巣部2より落下する復水が貯水室19へ流
入しないように形成されている。堤22aとカバー22
bの結合部は通気口22cの開口部を備え、管巣部2と
貯水室19との通気性を確保する。この通気口22cの
所要面積は、管巣部2と貯水室19の最大圧力差、管巣
部容積、圧力変動の許容幅および圧力変動許容時間から
求められる。A cover 22b is provided on the upper part of the bank 22a so that the condensed water falling from the tube nest 2 does not flow into the water storage chamber 19. Bank 22a and cover 22
The connecting portion of b is provided with an opening of the vent hole 22c to ensure the air permeability between the tube nest portion 2 and the water storage chamber 19. The required area of the ventilation port 22c is obtained from the maximum pressure difference between the tube nest 2 and the water storage chamber 19, the tube nest volume, the allowable width of pressure fluctuation, and the allowable pressure fluctuation time.
【0017】本発明の復水器はこのように形成されてい
るわけであるが、次にこのように形成された復水器の運
転方法について述べる。プラントの起動に際してはま
ず、冷却水送水装置23により管巣2の管内に冷却水を
通水する。次に復水器1の真空を空気抽出装置24にて
上昇させる。この時貯水室19に蓄えている復水は、大
気との接触により溶存酸素濃度は飽和状態にあり、約1
0000ppb程度になっている。これに対し、復水器
送水装置3により送水される復水の溶存酸素濃度は、通
常運転中の基準値7ppb以下となっており、起動時に
ついても基準値(10ppb)以下とする必要がある。The condenser of the present invention is formed in this way. Next, a method of operating the condenser thus formed will be described. When the plant is started up, first, the cooling water supply device 23 allows the cooling water to flow into the pipe of the tube nest 2. Next, the vacuum of the condenser 1 is raised by the air extraction device 24. At this time, the condensate stored in the water storage chamber 19 has a dissolved oxygen concentration in a saturated state due to contact with the atmosphere,
It is about 0000 ppb. On the other hand, the dissolved oxygen concentration of the condensate sent by the condenser water supply device 3 is equal to or lower than the reference value of 7 ppb during the normal operation, and it is necessary to be equal to or lower than the reference value (10 ppb) at the time of startup. .
【0018】復水器1には起動時に脱気運転を行なうた
めの復水再循環系6が復水系5に接続され切替弁8を
開、切替弁7を閉とし、復水送水装置3により溶存酸素
濃度の高い再循環水は復水出口4よりグランド蒸気復水
器21を通りノズル9を介して、天井板10の上部に散
水導入される。この散水あるいは、復水器1で水となっ
た復水は脱気室17に集められる。In the condenser 1, a condensate recirculation system 6 for performing deaeration operation at startup is connected to the condensate system 5, the switching valve 8 is opened, the switching valve 7 is closed, and the condensate water feeding device 3 is used. The recirculated water having a high dissolved oxygen concentration is sprayed from the condensate outlet 4 through the gland steam condenser 21 and the nozzle 9 to the upper portion of the ceiling plate 10. The sprinkled water or the condensed water that has become water in the condenser 1 is collected in the deaeration chamber 17.
【0019】脱気室17には水面下に噴出口を有する蒸
気噴出管12が設けられ、蒸気供給系13から弁14を
介して加熱脱気蒸気が供給されて脱気を行なう。以上の
ように脱気を行ない、給水溶存酸素濃度が給水規定値に
達したら切替弁8を閉じ切替弁7を開けボイラに給水を
開始する。The deaeration chamber 17 is provided with a steam ejection pipe 12 having an ejection port below the water surface, and heated deaeration steam is supplied from a steam supply system 13 via a valve 14 for deaeration. The deaeration is performed as described above, and when the concentration of the dissolved oxygen in the water supply reaches the water supply regulation value, the switching valve 8 is closed and the switching valve 7 is opened to start supplying water to the boiler.
【0020】復水再循環系6より導入された溶存酸素濃
度の高い復水は、貯水室19の上部に設けられた天井板
10の上部で散水されさらに、隔離板15に設けられた
通水部16を通り脱気室17に落下する。脱気室17に
落下した復水は水面下で噴出するように設けられた蒸気
噴出管12により供給される加熱脱気蒸気により加熱脱
気され、通水部18より貯水室19に送られ、通路を形
成するように設けられた仕切板11に沿って復水出口4
に向かって流動する。Condensate having a high dissolved oxygen concentration introduced from the condensate recirculation system 6 is sprinkled at the upper part of the ceiling plate 10 provided at the upper part of the water storage chamber 19, and further the water flow provided at the separator plate 15 is carried out. It passes through the portion 16 and falls into the deaeration chamber 17. The condensed water that has fallen into the degassing chamber 17 is heated and degassed by the heated degassing steam supplied by the steam spouting pipe 12 provided so as to spout below the water surface, and is sent to the water storage chamber 19 from the water passing portion 18. Condensate outlet 4 along a partition plate 11 provided so as to form a passage
Flow toward.
【0021】貯水部19の天井板10は、前記通気装置
22が設置されていて、管巣部2と貯水室19とを連通
しており、通気性を確保している。そのため貯水室19
の天井板10上に散水導入される復水等は、貯水室19
に流入することなく、天井板10上に落下し、脱気室1
7に送られる。The ceiling plate 10 of the water storage portion 19 is provided with the ventilation device 22 and connects the tube nest portion 2 and the water storage chamber 19 to each other to ensure air permeability. Therefore, the water storage room 19
Condensate that is sprinkled on the ceiling plate 10 of the
Flow into the ceiling plate 10 without flowing into the deaeration chamber 1
Sent to 7.
【0022】このような運転中に復水器逆洗等によっ
て、管巣部2での一時的な圧力上昇があった場合は、前
記通気装置22により、通気性が確保されており、管巣
部2と貯水室19との圧力の伝幡がよいため、管巣部2
と貯水室19との差圧を小さくすることができ、このた
め、この差圧によるホットウェルの貯水室19の水位変
動が防止されるのである。If there is a temporary pressure increase in the tube nest 2 due to backwashing of the condenser during such operation, the ventilation is ensured by the ventilation device 22. Since the pressure transfer between the section 2 and the water storage chamber 19 is good, the tube nest 2
The pressure difference between the water storage chamber 19 and the water storage chamber 19 can be reduced, and therefore, the fluctuation of the water level in the water storage chamber 19 of the hot well due to this pressure difference can be prevented.
【0023】次に、本発明の他の実施例について説明す
る。図6に示す実施例は、図1に示す実施例に対し、管
巣部2と貯水室19を連通する通気装置が異なる点以外
は同一である。図7に図6の実施例による通気装置26
の構造図を示す。管巣部2と貯水室19は、図6の様な
連通管で接続される。この時のbの寸法は、前記図4の
実施例に示すb寸法と同一であり、連通管の流路断面積
も図4の通気口の断面積と同じであり、また、b<cで
ある。Next, another embodiment of the present invention will be described. The embodiment shown in FIG. 6 is the same as the embodiment shown in FIG. 1 except that the ventilation device that connects the tube nest 2 and the water storage chamber 19 is different. FIG. 7 shows a ventilation device 26 according to the embodiment of FIG.
The structural drawing of is shown. The tube nest portion 2 and the water storage chamber 19 are connected by a communication pipe as shown in FIG. The dimension of b at this time is the same as the dimension of b shown in the embodiment of FIG. 4, the flow passage cross-sectional area of the communicating pipe is also the same as the cross-sectional area of the vent of FIG. 4, and b <c is there.
【0024】このような構造を持つ通気装置26でも、
管巣部2と貯水室19の通気性を確保しつつ、管巣部2
から貯水室19への復水の流入を防止でき、圧力変化に
起因するレベル変動を防止することができる。Even in the ventilation device 26 having such a structure,
While ensuring the air permeability of the tube nest 2 and the water storage chamber 19, the tube nest 2
It is possible to prevent the condensate from flowing into the water storage chamber 19 and prevent the level fluctuation due to the pressure change.
【0025】図8に示す実施例はさらに他の実施例で、
図1の実施例に示す管巣部2と貯水部19を区分する天
井板10に通気性を備えた構造としたものである。10
a,10b,10c,10dは、天井板を示し、独立し
て構成され、それぞれの関係は、図9の通りである。The embodiment shown in FIG. 8 is still another embodiment.
The ceiling plate 10 for partitioning the tube nest portion 2 and the water storage portion 19 shown in the embodiment of FIG. 1 has a structure having air permeability. 10
Reference numerals a, 10b, 10c, and 10d denote ceiling plates, which are independently configured and their respective relationships are as shown in FIG.
【0026】この実施例の場合、天井板上に導入された
復水は、各天井板10a〜10dに落水し、天井板10
aに落水した復水は、天井板10aより、天井板10
b,10c,10dへと順番に送られた後、脱気室17
に送られる。各天井板10a〜10dには、高さが高い
方に堰が設けてあり、天井板上の復水がホットウェルの
貯水室19に直接流れ込むのを防いでいる。In the case of this embodiment, the condensate introduced on the ceiling plate 10 falls into each of the ceiling plates 10a to 10d, and
Condensed water that has fallen into a
b, 10c, 10d, and then the deaeration chamber 17
Sent to. Each ceiling plate 10a to 10d is provided with a weir at a higher height to prevent condensed water on the ceiling plate from directly flowing into the water storage chamber 19 of the hot well.
【0027】各天井板10a〜10dの間には、復水器
1の管巣部2と貯水室19との通気部がある。この時の
bの寸法は、図1の実施例と同一であり、10a,10
b,10c,10dそれぞれの間隔によって必要な通気
面積を確保している。この実施例でも、管巣部2と貯水
室19との通気性を確保しつつ、管巣部2から貯水室1
9への復水流入を防止でき、脱気性能を落すことなく、
管巣部2と貯水室19の圧力変動によるホットウェル貯
水室19の水位変動を防止できる。Between the ceiling plates 10a to 10d, there is a ventilation portion between the tube nest portion 2 of the condenser 1 and the water storage chamber 19. The dimension of b at this time is the same as that of the embodiment of FIG.
The required ventilation area is secured by the intervals of b, 10c, and 10d. Also in this embodiment, the air permeability between the tube nest portion 2 and the water storage chamber 19 is ensured while the tube nest portion 2 is moved to the water storage chamber 1.
It is possible to prevent the condensate from flowing into 9 and to reduce the degassing performance.
It is possible to prevent fluctuations in the water level in the hot well water storage chamber 19 due to pressure fluctuations in the tube nest 2 and the water storage chamber 19.
【0028】また、図9の実施例において、天井板10
aから10bに復水が落下する際、復水の流れによって
通気面積が確保できない可能性がある場合、図10に示
すように通気面積確保用の復水の流れを一部防止する仕
切板を通気必要面積相当分、部分的に設置することも可
能である。Further, in the embodiment of FIG. 9, the ceiling board 10
When the condensate falls from a to 10b, if there is a possibility that the ventilation area cannot be secured due to the condensate flow, a partition plate that partially prevents the condensate flow for securing the ventilation area as shown in FIG. It is also possible to install a part corresponding to the required ventilation area.
【0029】これまでの実施例では、脱気機能を有する
復水器について述べたが、復水器の逆洗運転による運転
状態において、管巣部の圧力が一時的に上昇し、ホット
ウェルの貯水室の水位が変動する事象は、前記脱気復水
器のみに限らず、蒸気を凝縮する管巣部とホットウェル
の貯水室とを天井板により区分している復水器において
必ず起こるものである。したがって、管巣、天井板付き
のホットウェル部等により構成されている復水器におい
ては、本発明は有効である。In the above-mentioned embodiments, the condenser having the deaeration function has been described. However, in the operating state of the condenser by the backwash operation, the pressure in the tube nest temporarily rises and the hot well The phenomenon in which the water level in the water storage chamber fluctuates is not limited to the degassing condenser, but it always occurs in the condenser that separates the tube nest for condensing steam from the hot well water storage chamber by the ceiling plate. Is. Therefore, the present invention is effective in a condenser configured by a tube nest, a hot well portion with a ceiling plate, and the like.
【0030】図11は天井板10に設けた通気性開口の
総面積をホットウェル貯水室の水面面積で除した比と逆
洗運転時の水位変動振幅の関係を示している。図より、
開口比が0.2%以上の領域では、振幅の値が開口のな
い場合の1/2以下になることがわかる。これより、通
気必要面積は、ホットウェル水面面積の0.2%以上と
すれば良く、また上限は天井板の強度の関係から75%
以下が良い。また、天井板上の開口はホットウェル流路
に沿って、偏らずまんべんなく設置することが望まし
い。FIG. 11 shows the relationship between the ratio of the total area of the ventilation openings provided on the ceiling plate 10 divided by the water surface area of the hot well water storage chamber and the water level fluctuation amplitude during backwash operation. From the figure,
It can be seen that in the region where the aperture ratio is 0.2% or more, the value of the amplitude is 1/2 or less of that when there is no aperture. From this, the required ventilation area should be 0.2% or more of the water surface area of the hot well, and the upper limit is 75% due to the strength of the ceiling plate.
The following is good. In addition, it is desirable that the openings on the ceiling plate should be installed evenly along the hot well channel.
【0031】なお、以上の説明では、両室を連通する連
通手段を両室を仕切る天井板に設けるように説明してき
たが、常にこの天井板に設けなければならないわけでは
なく、例えば復水器の外枠やホットウェル部の側壁を介
して両室を連通するようにしてもよいであろう。In the above description, it has been explained that the communication means for communicating both chambers is provided on the ceiling plate that separates both chambers, but it is not always necessary to provide this ceiling plate, and for example, a condenser. The two chambers may be communicated with each other through the outer frame of the above and the side wall of the hot well portion.
【0032】以上説明してきたようにこのように形成さ
れた復水器であると、復水ホットウェルの貯水部とター
ビンより流入する蒸気を凝縮する管巣部を区分する天井
板に通気部を設けることにより、管巣部と復水器ホット
ウェルの貯水部との圧力の伝幡がよくなり、差圧に起因
した復水器ホットウェルの水位変動を防止することがで
きるのである。As described above, in the condenser thus formed, the ventilation part is provided in the ceiling plate which separates the water storage part of the condensing hot well and the tube nest part for condensing the steam flowing from the turbine. By providing it, the pressure transfer between the tube nest part and the water storage part of the condenser hot well is improved, and the fluctuation of the water level of the condenser hot well due to the differential pressure can be prevented.
【0033】[0033]
【発明の効果】以上説明してきたように本発明によれ
ば、管巣部と復水器ホットウェルの貯水室との通気性が
良好となり、プラントの運転状態による管巣部の一時的
な圧力上昇による復水器ホットウェル貯水室との圧力差
の発生を防止でき、これに起因する水位の変動を防止す
ることが可能なこの種の復水器を得ることができる。As described above, according to the present invention, the air permeability between the tube nest portion and the water storage chamber of the condenser hot well becomes good, and the temporary pressure of the tube nest portion due to the operating state of the plant is improved. It is possible to obtain a condenser of this kind capable of preventing the occurrence of a pressure difference between the condenser and the hot well water storage chamber due to the rise, and preventing the fluctuation of the water level due to this.
【図1】本発明の復水器の一実施例を示す縦断側面図で
ある。FIG. 1 is a vertical sectional side view showing an embodiment of a condenser of the present invention.
【図2】本発明の復水器の一実施例を示す一部破断斜視
図である。FIG. 2 is a partially cutaway perspective view showing an embodiment of the condenser of the present invention.
【図3】本発明の復水器の一実施例を示す平面図(図2
のA−A線)である。FIG. 3 is a plan view showing one embodiment of the condenser of the present invention (FIG.
A-A line).
【図4】図3のA部分詳細図である。FIG. 4 is a detailed view of a portion A of FIG.
【図5】図2のB−B線に沿う断面図である。5 is a cross-sectional view taken along the line BB of FIG.
【図6】本発明の復水器の他の実施例を示す縦断側面図
である。FIG. 6 is a vertical sectional side view showing another embodiment of the condenser of the present invention.
【図7】図6の部分詳細図である。FIG. 7 is a partial detailed view of FIG.
【図8】本発明の復水器の他の実施例を示す縦断側面図
である。FIG. 8 is a vertical side view showing another embodiment of the condenser of the present invention.
【図9】図8の部分詳細図である。9 is a partial detailed view of FIG. 8. FIG.
【図10】本発明の他の実施例の部分詳細図である。FIG. 10 is a partial detailed view of another embodiment of the present invention.
【図11】開口比と水位変動振幅の大きさの関係を示す
特性図である。FIG. 11 is a characteristic diagram showing the relationship between the aperture ratio and the magnitude of the water level fluctuation amplitude.
1…復水器、2…管巣、3…復水送水装置、4…復水出
口、5…復水系、6…復水再循環系、7,8…切替弁、
9…ノズル、10,10a,10b,10c,10d…
天井板、11,27…仕切板、12…蒸気噴射管、13
…復水脱気系、14…制御弁、15…隔離板、16,1
8…通水口、17…脱気室、19…貯水室、20…水位
計、21…グランド蒸気復水器、22,26…通気装
置、22a…堰、22b…カバー、22c…通気口、2
3…冷却水送水装置、24…空気抽出装置、25…空気
抽出系。1 ... Condenser, 2 ... Tube nest, 3 ... Condensate water sending device, 4 ... Condensate outlet, 5 ... Condensate system, 6 ... Condensate recirculation system, 7, 8 ... Switching valve,
9 ... Nozzle, 10, 10a, 10b, 10c, 10d ...
Ceiling plates 11, 27 ... Partition plates, 12 ... Steam injection pipes, 13
… Condensate degassing system, 14… Control valve, 15… Separator, 16,1
8 ... Water inlet, 17 ... Deaeration chamber, 19 ... Water storage chamber, 20 ... Water level gauge, 21 ... Grand steam condenser, 22, 26 ... Ventilation device, 22a ... Weir, 22b ... Cover, 22c ... Vent port, 2
3 ... Cooling water supply device, 24 ... Air extraction device, 25 ... Air extraction system.
───────────────────────────────────────────────────── フロントページの続き (72)発明者 織田 繁夫 茨城県日立市幸町三丁目1番1号 株式 会社日立製作所日立工場内 (56)参考文献 特開 昭60−200086(JP,A) 特開 平5−79776(JP,A) 特公 昭63−12238(JP,B2) (58)調査した分野(Int.Cl.7,DB名) F28B 9/10 F28B 9/08 ─────────────────────────────────────────────────── ─── Continuation of the front page (72) Shigeo Oda Inventor Shigeo Oda 3-1-1, Saiwaicho, Hitachi, Ibaraki Hitachi Ltd. Hitachi factory (56) References JP-A-60-200086 (JP, A) Kaihei 5-79776 (JP, A) Japanese Patent Publication No. 63-12238 (JP, B2) (58) Fields investigated (Int.Cl. 7 , DB name) F28B 9/10 F28B 9/08
Claims (3)
巣部と、前記管巣部で凝縮された凝縮水を脱気する脱気
室と、隔離板によって前記脱気室と隔離され、通水部を
介して前記脱気室と連絡している貯水室と、前記脱気室
と前記管巣部との間に配置され、前記貯水室と管巣部と
を仕切り、前記管巣部から落下した凝縮水を前記脱気室
に流入させる区画壁を有する復水器において、前記貯水
室と管巣部との間に無通水性で、かつ、通気性を有する
連通手段を備え、前記管巣部での圧力上昇による前記貯
水室の水面波の発生を抑制することを特徴とする復水
器。1. A pipe nest for condensing steam flowing from a turbine, a degassing chamber for degassing condensed water condensed in the pipe nest, and a separator for separating the degassing chamber from the water passage. Is arranged between the deaeration chamber and the tube nest portion, which is in communication with the deaeration chamber via a portion, and partitions the water storage chamber and the tube nest portion and falls from the tube nest portion. In a condenser having a partition wall for allowing the condensed water to flow into the deaeration chamber, a water-impermeable and air-permeable communication means is provided between the water storage chamber and the tube nest portion, A condenser that suppresses the generation of a water surface wave in the water storage chamber due to an increase in pressure in the section.
巣部と、管巣部で凝縮された凝縮水を脱気する脱気室
と、隔離板によって前記脱気器と隔離され、通水部を介
して前記前記脱気室と連絡している貯水室と、前記脱気
室と前記管巣部の間に配置され、前記貯水室と管巣部と
を仕切り、前記管巣部から落下した凝縮水を前記脱気室
に流入させる天井板を有する復水器において、前記貯水
室と管巣部とを仕切る天井板に、通水性がなく、かつ、
通気性を有する連通手段を備え前記管巣部での圧力上昇
による前記貯水室の水面波の発生を抑制することを特徴
とする復水器。2. A tube nest portion for condensing steam flowing in from a turbine, a deaeration chamber for deaerating condensed water condensed in the tube nest portion, and a separator plate for separating the deaerator from the water passage portion. A water storage chamber that is in communication with the deaeration chamber via a, is arranged between the deaeration chamber and the tube nest portion, partitions the water storage chamber and the tube nest portion, and dropped from the tube nest portion In a condenser having a ceiling plate that allows condensed water to flow into the degassing chamber, the ceiling plate that separates the water storage chamber and the tube nest has no water permeability, and
A condenser, comprising a communicating means having air permeability, and suppressing generation of a water surface wave in the water storage chamber due to a pressure increase in the tube nest portion.
連通手段の開口面積が、前記貯水室のホットウエル水面
の面積の0.2%以上75%以下に形成されている請求
項1または2記載の復水器。3. The opening area of the communication means provided in the partition wall or the ceiling plate is formed to be 0.2% or more and 75% or less of the area of the hot well water surface of the water storage chamber. The condenser according to 1 or 2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33186696A JP3366817B2 (en) | 1996-12-12 | 1996-12-12 | Condenser |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP33186696A JP3366817B2 (en) | 1996-12-12 | 1996-12-12 | Condenser |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH10170170A JPH10170170A (en) | 1998-06-26 |
JP3366817B2 true JP3366817B2 (en) | 2003-01-14 |
Family
ID=18248528
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP33186696A Expired - Fee Related JP3366817B2 (en) | 1996-12-12 | 1996-12-12 | Condenser |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP3366817B2 (en) |
-
1996
- 1996-12-12 JP JP33186696A patent/JP3366817B2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH10170170A (en) | 1998-06-26 |
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