JPS631515B2 - - Google Patents
Info
- Publication number
- JPS631515B2 JPS631515B2 JP57066465A JP6646582A JPS631515B2 JP S631515 B2 JPS631515 B2 JP S631515B2 JP 57066465 A JP57066465 A JP 57066465A JP 6646582 A JP6646582 A JP 6646582A JP S631515 B2 JPS631515 B2 JP S631515B2
- Authority
- JP
- Japan
- Prior art keywords
- condenser
- steam
- tube
- cooling
- pipe
- 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
- 238000001816 cooling Methods 0.000 claims description 23
- 239000000498 cooling water Substances 0.000 claims description 4
- 239000007789 gas Substances 0.000 description 13
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 5
- 238000005192 partition Methods 0.000 description 5
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- OAKJQQAXSVQMHS-UHFFFAOYSA-N Hydrazine Chemical compound NN OAKJQQAXSVQMHS-UHFFFAOYSA-N 0.000 description 2
- 238000005260 corrosion Methods 0.000 description 2
- 230000007797 corrosion Effects 0.000 description 2
- 238000000605 extraction Methods 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28B—STEAM OR VAPOUR CONDENSERS
- F28B9/00—Auxiliary systems, arrangements, or devices
- F28B9/10—Auxiliary systems, arrangements, or devices for extracting, cooling, and removing non-condensable gases
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
【発明の詳細な説明】
本発明は、復水器に係り、特に蒸気タービン復
水器の空気冷却部冷却管群配置態様に関するもの
である。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a condenser, and particularly to an arrangement of cooling pipe groups in an air cooling section of a steam turbine condenser.
蒸気タービン復水器には通常、所謂空気冷却部
が設けられる。この空気冷却部の設置理由は下記
の通りである。蒸気タービンの低圧段から復水器
内にかけては負圧状態であり両者の連通蒸気管フ
ランジ等からの空気流入が避けられない。この混
入空気は高圧給水加熱器の給水中に注入された鋼
管の防食対策のヒドラジンがボイラ中で分解され
て発生するアンモニアガス等と共に復水器内に蓄
積される。これらの不凝縮ガスは、空気抽出器で
器外に抽出され、所定の復水気真空度の維持が計
られている。 Steam turbine condensers are usually provided with a so-called air cooling section. The reason for installing this air cooling section is as follows. There is a negative pressure state from the low pressure stage of the steam turbine to the inside of the condenser, and air inflow from the communicating steam pipe flanges between the two is unavoidable. This mixed air is accumulated in the condenser together with ammonia gas and other gas generated when hydrazine, which is injected into the water supply of the high-pressure feedwater heater to prevent corrosion of steel pipes, is decomposed in the boiler. These non-condensable gases are extracted to the outside of the vessel by an air extractor to maintain a predetermined degree of condensate vacuum.
一般にこれら非凝縮ガス中には蒸気が随伴して
おり、この随伴蒸気を再凝縮させ、ガス容積を減
少させ空気抽出器の負荷を軽減させるために空気
冷却部が設けられている。 Generally, these non-condensable gases are accompanied by steam, and an air cooling section is provided in order to recondense the entrained steam, reduce the gas volume, and reduce the load on the air extractor.
第1図乃至第3図に従来の復水器と空気冷却部
配置例を示す。ここでタービン蒸気14は冷却管
1の集合体である管巣6が配置された冷却室15
に周囲から流入し、殆んどの蒸気は復水器冷却管
1を流れる冷却水で凝縮されて復水する。また、
混入空気、アンモニアガスならびに一部の蒸気は
穴部10を通じて不凝縮ガス抽気管3に流れ込
み、空気冷却部7に導かれる。ここで蒸気の一部
は凝縮され、不凝縮ガスはさらに冷却されて空気
抽出管8を通つて空気抽出器9により排出され
る。 FIGS. 1 to 3 show examples of the arrangement of conventional condensers and air cooling units. Here, the turbine steam 14 is transferred to a cooling chamber 15 in which a tube nest 6, which is a collection of cooling tubes 1, is arranged.
Most of the steam flows into the condenser from the surroundings and is condensed by the cooling water flowing through the condenser cooling pipe 1. Also,
Entrained air, ammonia gas and some steam flow into the non-condensable gas bleed pipe 3 through the holes 10 and are guided to the air cooling section 7. Here, a part of the vapor is condensed, and the non-condensable gases are further cooled and discharged through the air extraction pipe 8 by the air extractor 9.
この空気冷却部7は、その上部および側面を仕
切板5で囲まれ、周りの管巣6からの未凝縮蒸気
が流れ込まないようにし、且つ冷却管1を保持し
ている支持板2間の管巣6では、未凝縮蒸気が不
凝縮ガス抽気管3に直接流れ込むのを防ぐために
第2図に示す仕切板11を設けている。4は管
板、12,13は水室、16はケーシング、17
は管巣中央空隙部、18は復水である。このよう
な空気冷却部の配置法は以下の欠点がある。 This air cooling section 7 is surrounded by a partition plate 5 on its top and side surfaces to prevent uncondensed steam from the surrounding tube nest 6 from flowing into the air cooling section 7, and to prevent uncondensed steam from flowing into the tube nest 6 between the support plates 2 holding the cooling tube 1. In the nest 6, a partition plate 11 shown in FIG. 2 is provided to prevent uncondensed steam from flowing directly into the uncondensed gas bleed pipe 3. 4 is a tube plate, 12 and 13 are water chambers, 16 is a casing, 17
18 is the central cavity of the tube nest, and 18 is the condensate. This method of arranging the air cooling section has the following drawbacks.
(ア) 管巣内に仕切板5,11を設けるために余分
のスペースが必要で、且つ製作面の難しさがあ
る。(A) Extra space is required to provide the partition plates 5 and 11 within the tube nest, and there are also manufacturing difficulties.
(イ) 管巣の一部を仕切板で仕切るため蒸気の流れ
が偏より蒸気速度の不均一さが助長されて圧力
損失が増す。(b) Part of the tube nest is partitioned with a partition plate, which causes uneven steam flow, which promotes uneven steam velocity and increases pressure loss.
本発明は上記の欠点を解決した性能の優れた復
水器を提供することを目的とする。 An object of the present invention is to provide a condenser with excellent performance that solves the above-mentioned drawbacks.
以下に本発明による復水器の一実施例を添付の
第4,5図に基づき説明する。 An embodiment of the condenser according to the present invention will be described below with reference to the attached FIGS. 4 and 5.
第4図及第5図(第5図は第4図のV―V矢
視)に於いて復水器は冷却室15及び水室12,
13からなり、冷却室15は冷却管1を管配列密
度を中央で密、周辺で疎とした管巣6が管板4及
び管支持板2で保持され、冷却室15に導かれた
タービン排気蒸気14が管巣6の中央部に導かれ
る。そして管巣中央空隙部17には外表面に穴部
10を設けた不凝縮ガス抽気管3が設置されてい
る。冷却水入口側の管板4ならびに管支持板2で
仕切られた空間部19では不凝縮ガス抽気管3は
なくその中間に管長手方向に直角に管巣中央空隙
部17の形状と相似で、且つやや大きなそらせ板
20が配されている。 In FIGS. 4 and 5 (FIG. 5 is taken from the V-V arrow in FIG. 4), the condenser includes a cooling chamber 15, a water chamber 12,
13, the cooling chamber 15 has a tube nest 6 in which the cooling tubes 1 are densely arranged in the center and sparsely arranged around the periphery, and is held by the tube plate 4 and the tube support plate 2, and the turbine exhaust gas guided to the cooling chamber 15. Steam 14 is guided into the center of the tube nest 6. A non-condensable gas bleed pipe 3 having a hole 10 on its outer surface is installed in the central cavity 17 of the tube nest. In the space 19 partitioned by the tube plate 4 and the tube support plate 2 on the cooling water inlet side, there is no non-condensable gas bleed pipe 3, and the shape is similar to that of the tube nest central cavity 17 at right angles to the longitudinal direction of the tubes. In addition, a somewhat large deflecting plate 20 is arranged.
以上の構造からなる復水器においてその作用を
以下に説明する。 The operation of the condenser having the above structure will be explained below.
蒸気14は管巣6の周囲から、最小の圧力損失
で流入する。この蒸気の殆んどは管巣6を構成す
る冷却管1中の水と熱交換し凝縮する。また、蒸
気中に混入している空気やアンモニアガス等は一
部の未蒸縮蒸気と共に穴部10を通して不凝縮ガ
ス抽気管3に導かれる。そして、このそらせ板2
0により、矢印21の如く冷却管1間を再び通
り、随伴蒸気は凝縮されて復水18となり、空気
等の不凝縮ガスは空気抽出管8を通じて空気抽出
器9で排出される。 Steam 14 flows from around the tube bundle 6 with minimal pressure loss. Most of this steam exchanges heat with water in the cooling pipes 1 constituting the tube nest 6 and condenses. In addition, air, ammonia gas, etc. mixed in the steam are guided to the non-condensable gas bleed pipe 3 through the hole 10 along with some unevaporated steam. And this deflector plate 2
0, it passes again between the cooling pipes 1 as indicated by the arrow 21, and the accompanying steam is condensed into condensate 18, and non-condensable gas such as air is discharged through the air extraction pipe 8 in the air extractor 9.
以上、説明したように本発明によれば、冷却管
間に仕切板5や11を設ける必要もなく、また特
別なスペースもとることなく空気冷却部が構成で
きる。したがつて蒸気の流れは良好で圧損も小さ
く、またアンモニアの滞留による管腐食も防げる
等優れた効果を奏する。 As described above, according to the present invention, the air cooling section can be configured without the need to provide the partition plates 5 and 11 between the cooling pipes, and without taking up any special space. Therefore, the flow of steam is good, pressure loss is small, and excellent effects such as prevention of pipe corrosion due to ammonia retention are achieved.
第1図は従来の復水器の構造を示す縦断面図、
第2図は第1図の―方向断面図、第3図は第
1図の―方向断面図、第4図は本発明による
復水器の縦断面図、第5図は第4図のV―V方向
断面図である。
6:管巣、3:不凝縮ガス抽気管、4:管板、
20:そらせ板。
Figure 1 is a vertical cross-sectional view showing the structure of a conventional condenser.
2 is a sectional view in the - direction of FIG. 1, FIG. 3 is a sectional view in the - direction of FIG. 1, FIG. 4 is a longitudinal sectional view of the condenser according to the present invention, and FIG. - It is a sectional view in the V direction. 6: tube nest, 3: non-condensable gas bleed pipe, 4: tube plate,
20: Deflection board.
Claims (1)
べく、冷却水を流通させる複数の冷却管群により
形成される管巣中に不凝縮ガス抽気管を備えた復
水器において、冷却水入口側管板とこれに対向す
る管支持板との間に管巣中の空隙部形状と相似で
且つやや大きいそらせ板を設けたことを特徴とす
る復水器。1 In a condenser equipped with a non-condensable gas bleed pipe in a pipe nest formed by a plurality of cooling pipe groups through which cooling water flows, in order to cool and condense the steam led into the condenser, the cooling water is A condenser characterized in that a deflecting plate similar in shape to the cavity in the tube nest and slightly larger in size is provided between an inlet side tube plate and a tube support plate opposing the same.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6646582A JPS58184488A (en) | 1982-04-21 | 1982-04-21 | Condenser |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6646582A JPS58184488A (en) | 1982-04-21 | 1982-04-21 | Condenser |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS58184488A JPS58184488A (en) | 1983-10-27 |
JPS631515B2 true JPS631515B2 (en) | 1988-01-13 |
Family
ID=13316553
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6646582A Granted JPS58184488A (en) | 1982-04-21 | 1982-04-21 | Condenser |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58184488A (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60232489A (en) * | 1984-05-04 | 1985-11-19 | Mitsubishi Heavy Ind Ltd | Condenser |
US20060045230A1 (en) * | 2004-08-31 | 2006-03-02 | Stephan Moen | Method and apparatus for mitigating pressure loss in a steam tunnel of a boiling water reactor |
JP5037050B2 (en) * | 2006-07-20 | 2012-09-26 | 株式会社タダノ | Telescopic boom in a working machine with a boom |
JP6262040B2 (en) * | 2014-03-19 | 2018-01-17 | 三菱日立パワーシステムズ株式会社 | Condenser and turbine equipment |
-
1982
- 1982-04-21 JP JP6646582A patent/JPS58184488A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS58184488A (en) | 1983-10-27 |
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