JP2012037175A - Deaerator - Google Patents

Deaerator Download PDF

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JP2012037175A
JP2012037175A JP2010179257A JP2010179257A JP2012037175A JP 2012037175 A JP2012037175 A JP 2012037175A JP 2010179257 A JP2010179257 A JP 2010179257A JP 2010179257 A JP2010179257 A JP 2010179257A JP 2012037175 A JP2012037175 A JP 2012037175A
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water supply
water
steam
axial direction
fuselage
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JP5645538B2 (en
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Kazusaku Fujita
一作 藤田
Naomiki Hasegawa
直幹 長谷川
Jiro Kasahara
二郎 笠原
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Mitsubishi Heavy Industries Ltd
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Mitsubishi Heavy Industries Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a deaerator of single barrel type capable of subjecting feed water and steam to rectangular contact and enhancing deaeration efficiency even when being disposed on the under side of a feed water supply part which supplies feed water from the above side to a water storage part in a barrel.SOLUTION: The feed water supply part 3 includes: a feed water ejector 31 which ejects feed water from the above side to the water storage part 6; and a regulator which directs the feed water ejected from the feed water ejector 31 to a horizontal direction center part perpendicular to the axial direction of the barrel, a steam supply part 4 is configured to have a plurality of steam jetting unit groups 43 in the axial direction of the barrel 2, each steam jetting unit group 43 includes a plurality of steam jetting units which jet steam into the water storage part, in the horizontal direction perpendicular to the axial direction of the barrel 2 and the ejection means constituting the ejector group is arranged by setting a distance of a gap from the lower end position of each ejector to a barrel inner peripheral surface of the vertical direction lower side into the distance where the feed water can flow, and the ejector is prevented from being located on the horizontal direction center part vertical to the axial direction of the barrel 2.

Description

本発明は、給水中に含まれている溶存酸素を取り除き、ボイラ等の蒸気発生器に供給するための脱気器に関するものである。   The present invention relates to a deaerator for removing dissolved oxygen contained in feed water and supplying it to a steam generator such as a boiler.

火力発電プラントや原子力発電プラント等においては、給水中の溶存酸素によってプラントの構成機器が腐食することを抑制するために、給水中の溶存酸素を除去する脱気器が使用されている。   In a thermal power plant, a nuclear power plant, and the like, a deaerator that removes dissolved oxygen in the feed water is used in order to suppress corrosion of the components of the plant due to dissolved oxygen in the feed water.

脱気器として、双胴式脱気器と称されるものと、単胴式脱気器と称されるものとの2種類が知られている。前記双胴式脱気器は、脱気部と貯水部とを別々に備え、脱気部で霧状にした給水に蒸気を加えて溶存酸素を取り除き、脱気した給水を貯水部に溜めるものである。また、前記単胴式脱気器は、一つの胴体内に脱気部と貯水部とが併存し、貯水部に溜められた給水に気泡状にした蒸気を加え、給水中の溶存酸素を取り除くものである。   Two types of deaerators are known: a so-called twin-bottle type deaerator and a so-called single-cylinder type deaerator. The twin-bottle type deaerator has a deaeration part and a water storage part separately, and steam is added to the water supply made into a mist in the deaeration part to remove dissolved oxygen, and the deaerated water supply is stored in the water storage part. It is. In addition, the single cylinder type deaerator has a deaeration part and a water storage part coexisting in one body, and adds bubbled steam to the water supply stored in the water storage part to remove dissolved oxygen in the water supply. Is.

従来の単胴式脱気器の一例について図6を用いて説明する。
単胴式脱気器101は、横長筒状の胴体102を有し、胴体102の頭部側に給水供給部103と蒸気供給部104とを備え、胴体102の底部側に給水出口部105を備えている。
An example of a conventional single cylinder deaerator will be described with reference to FIG.
The single-body deaerator 101 has a horizontally long cylindrical body 102, and includes a water supply supply unit 103 and a steam supply unit 104 on the head side of the body 102, and a water supply outlet 105 on the bottom side of the body 102. I have.

給水供給部103は、スプレーノズル131と該スプレーノズル131に給水を導入する導入口132から構成され、導入口132から導入された給水をスプレーノズル131で霧状にして胴体102に形成される貯水部106に噴霧して供給するものである。   The water supply unit 103 includes a spray nozzle 131 and an introduction port 132 that introduces water to the spray nozzle 131, and water storage that is formed in the body 102 by spraying the water introduced from the introduction port 132 with the spray nozzle 131. It sprays and supplies to the part 106.

また、蒸気供給部104は、蒸気を導入する蒸気入口管141と、蒸気入口管141に接続されて胴体102の軸方向に延びる蒸気ヘッダー142と、蒸気ヘッダー142から貯水部106に向って延びて貯水部106内で多数の開孔部を有するスプレーパイプ143とから構成され、蒸気タービン(不図示)などの外部機器からの蒸気を蒸気入口管141、蒸気ヘッダー142、スプレーパイプ143を介して貯水部106内に供給するものである。   The steam supply unit 104 also includes a steam inlet pipe 141 that introduces steam, a steam header 142 that is connected to the steam inlet pipe 141 and extends in the axial direction of the body 102, and extends from the steam header 142 toward the water storage unit 106. The water storage unit 106 includes a spray pipe 143 having a large number of openings, and stores steam from an external device such as a steam turbine (not shown) through the steam inlet pipe 141, the steam header 142, and the spray pipe 143. It supplies in the part 106. FIG.

このような構成の脱気器101において、スプレーパイプ143の前記開孔部からの蒸気は、気泡となって貯水部106の給水(貯水)中に噴出され、気泡の持つ広い接触面積で給水(貯水)と直接接触し、給水(貯水)に含まれる酸素を加熱脱気させる。給水(貯水)から酸素を加熱脱気させた気泡としての蒸気は、貯水部106中を上昇して胴体102内上部の蒸気空間部107に達すると、ここで給水供給部103のスプレーノズル131から噴霧される霧状の給水と直接接触し、給水に含まれる酸素を加熱脱気させる。脱気により給水から分離された酸素及び随伴蒸気は胴体2の上部に設けた空気出口(不図示)より外部に排出される。また、脱気された給水は給水出口部105より排出され、脱気水の必要なプラント内の機器に送られる。   In the deaerator 101 having such a configuration, the steam from the opening portion of the spray pipe 143 is jetted into the water supply (water storage) of the water storage unit 106 as water bubbles, and the water is supplied with a wide contact area of the bubbles ( It comes into direct contact with water storage) and heats and degass oxygen contained in the water supply (storage water). Steam as air bubbles obtained by heating and degassing oxygen from the water supply (storage water) rises in the water storage section 106 and reaches the steam space section 107 in the upper part of the fuselage 102. Here, the steam from the spray nozzle 131 of the water supply supply section 103 Direct contact with sprayed mist-like water supply, and oxygen contained in the water supply is heated and degassed. Oxygen and accompanying steam separated from the feed water by deaeration are discharged to the outside through an air outlet (not shown) provided in the upper part of the body 2. In addition, the deaerated water supply is discharged from the water supply outlet 105 and sent to equipment in the plant that requires deaerated water.

このようにして、従来の単胴式脱気器は、給水に含まれる酸素を加熱脱気させ、溶存酸素によるプラントの構成機器が腐食を防止するものである。このような従来の単胴式脱気器は、例えば特許文献1、特許文献2に開示されている。   In this way, the conventional single-cylinder deaerator heats and degass oxygen contained in the feed water, and the plant components caused by dissolved oxygen prevent corrosion. Such conventional single cylinder type deaerators are disclosed in Patent Document 1 and Patent Document 2, for example.

さらに、図7に示したように、貯水部106に仕切板108を設け、貯水部106を対向流領域161と対向流領域162とに分割した単胴式脱気器も知られている。図7に示した単胴式脱気器においては、仕切板を設けた以外の構成は図6に示した単胴式脱気器と同様である。なお、仕切板108は下方に間隙109が形成されるように設けられており、該間隙109によって対向流領域161と対向流領域162とは連通している。   Furthermore, as shown in FIG. 7, there is also known a single cylinder type deaerator in which a partition plate 108 is provided in the water storage unit 106 and the water storage unit 106 is divided into a counter flow region 161 and a counter flow region 162. The single cylinder deaerator shown in FIG. 7 is the same as the single cylinder deaerator shown in FIG. 6 except that a partition plate is provided. The partition plate 108 is provided so that a gap 109 is formed below, and the counterflow region 161 and the counterflow region 162 communicate with each other through the gap 109.

図7に示した単胴式脱気器においては、仕切板108を設けることで、対向流領域161では、スプレーノズル131から貯水部106に供給された給水は、該噴霧の勢いによって下向きに流れ、上昇する気泡としての蒸気と対向接触する。また、前記給水は、仕切板108の下方の間隙109を通過してから、対向流領域162では胴体102の軸方向に流れ、上昇する気泡としての蒸気と直交接触する。   In the single-cylinder deaerator shown in FIG. 7, by providing the partition plate 108, the water supply supplied from the spray nozzle 131 to the water storage section 106 flows downward in the counterflow region 161 due to the force of the spray. , Facing the vapor as rising bubbles. Further, after the water supply passes through the gap 109 below the partition plate 108, it flows in the counterflow region 162 in the axial direction of the body 102, and is in orthogonal contact with the vapor as rising bubbles.

給水と蒸気は、対向接触する場合よりも、直交接触する方が、接触によって水の乱流が生じやすく、該乱流により気泡としての蒸気と給水との接触頻度が上がり脱気効率が上昇する。即ち、図7に示した単胴式脱気器においては、仕切板108を設けることで給水と蒸気が直交接触する直交接触領域162を作り出し、脱気効率の向上を図ったものである。   Water supply and steam are more likely to cause turbulent flow of water when they are in orthogonal contact than when they face each other, and the turbulent flow increases the frequency of contact between steam and water as bubbles and increases deaeration efficiency. . That is, in the single cylinder type deaerator shown in FIG. 7, by providing the partition plate 108, an orthogonal contact region 162 where the water supply and the steam are orthogonally contacted is created to improve the deaeration efficiency.

特開平11−351507号公報Japanese Patent Laid-Open No. 11-351507 特許第3684192号公報Japanese Patent No. 3684192

しかしながら、図6、図7に示した従来技術における単胴式脱気器においては、何れもスプレーノズル131下方では、スプレーノズル131から貯水部106に噴霧された給水の流れは下向き方向である。そのため、スプレーノズル131下方では下向きに流れる給水と、上昇する前記気泡としての蒸気は対向接触する。そのため、スプレーノズル131の下方では脱気効率が充分ではなく、例えば大型プラントで脱気器を使用する場合には脱気能力を上げるために胴体を非常に長いものとする必要があり、脱気器の設置場所の制約や脱気器の製作コストの面で問題が生じる。   However, in the single cylinder type deaerator in the prior art shown in FIGS. 6 and 7, the flow of the water supply sprayed from the spray nozzle 131 to the water storage unit 106 is downward in the downward direction of the spray nozzle 131. For this reason, the water supply flowing downward and the vapor as the rising bubbles are opposed to each other below the spray nozzle 131. Therefore, the deaeration efficiency is not sufficient below the spray nozzle 131. For example, when a deaerator is used in a large plant, the body needs to be very long in order to increase the deaeration capability. Problems arise in terms of the installation location of the vessel and the production cost of the deaerator.

従って、胴体内の貯水部に上方より給水を供給する給水供給部の下方であっても、給水と蒸気とを直交接触させることができ、脱気効率の向上が可能である単胴式の脱気器を提供することを目的とする。   Therefore, even in the lower part of the water supply part that supplies water to the water storage part in the fuselage from above, the water supply and the steam can be brought into orthogonal contact with each other, so that the degassing efficiency can be improved. The purpose is to provide a ventilator.

上記の課題を解決するために、本発明においては、内部に給水を貯留する貯水部を有する胴体と、前記胴体の上部に設けられ前記貯水部に給水を噴出する給水供給部と、前記胴体の貯水部に蒸気を供給する蒸気供給部と、前記胴体の底部に設けられ前記給水を排出するための給水出口部とを有する脱気器において、前記給水供給部は、前記貯水部に上方より給水を噴出する給水噴出手段と、前記噴出手段より噴出された給水を前記胴体の軸方向と直交する水平方向の中心部に向ける規制手段とを有し、前記蒸気供給部は、前記貯水部中に蒸気を噴出させる蒸気噴出手段を前記胴体の軸方向と直交する水平方向に複数備えた蒸気噴出手段群を、前記胴体の軸方向に複数群有して構成され、前記噴出手段群を構成する前記噴出手段は、それぞれの噴出手段の下端位置からその鉛直方向下方の胴体内周面までの間隙の距離を、前記給水が流通可能な距離に設定して配置されるとともに、前記噴出手段を前記胴体の軸方向と直交する水平方向中心部に位置しないことを特徴とする。   In order to solve the above-described problems, in the present invention, a fuselage having a water storage part for storing water supply therein, a water supply supply part that is provided on the upper part of the fuselage and that jets water supply to the water storage part, and In the deaerator having a steam supply unit for supplying steam to the water storage unit and a water supply outlet unit for discharging the water supply provided at the bottom of the body, the water supply unit supplies water to the water storage unit from above. Water supply jetting means, and regulating means for directing the water supplied from the jetting means to a central portion in the horizontal direction perpendicular to the axial direction of the fuselage, and the steam supply part is in the water storage part The steam jetting means group is configured to have a plurality of steam jetting means groups in the axial direction of the fuselage provided with a plurality of steam jetting means for jetting steam in a horizontal direction perpendicular to the axial direction of the fuselage, and constitute the jetting means group Each jet means The gap between the lower end position of the outlet means and the circumferential surface of the fuselage in the lower vertical direction is set to a distance through which the water supply can flow, and the jetting means is orthogonal to the axial direction of the trunk. It is not located in the center in the horizontal direction.

これにより、前記給水噴出手段によって噴出された給水は前記既成手段によってその噴霧方向を規制されて前記胴体の軸方向と直交する方向の中心付近に噴霧され、その後、胴体中心付近をそのまま下降し、下端まで達すると、胴体の内周面に沿って上昇していく。なお、このとき、前記胴体の軸方向と直交する水平方向の中心付近には前記蒸気噴出手段が設けられていないので、蒸気噴出手段が給水噴出手段から噴出された給水が胴体2の軸方向と直交する方向の中心付近を下降することを前記蒸気噴出手段が妨害することはなく、さらに、前記間隙の存在により、給水が前記胴体の内周面に沿って上昇することを、前記蒸気噴出手段が妨害することはない。   Thereby, the water supply sprayed by the water supply spraying means is sprayed in the vicinity of the center in the direction orthogonal to the axial direction of the fuselage, the spraying direction of which is regulated by the pre-made means, and then descends in the vicinity of the fuselage center, When it reaches the lower end, it rises along the inner peripheral surface of the fuselage. At this time, since the steam jetting means is not provided near the center in the horizontal direction orthogonal to the axial direction of the fuselage, the water supplied from the steam jetting means by the steam jetting means is the axial direction of the fuselage 2. The steam jetting means does not prevent the steam jetting means from descending in the vicinity of the center in the orthogonal direction, and the steam jetting means indicates that the water supply rises along the inner peripheral surface of the fuselage due to the presence of the gap. Will not interfere.

つまり、蒸気噴出手段の下方では給水は胴体の内周面に沿って流れており、即ち略水平に流れている。従って、蒸気噴出手段の下方では蒸気と給水は略直交して接触するため、高効率で給水に含まれる酸素を加熱脱気することができる。さらに、前記蒸気噴出手段群は、胴体の軸方向と直交する方向、即ち給水の流れに沿って複数設けているため、給水はその流れの中で蒸気と高効率で接触し、脱気効率を高めることができる。   That is, below the steam jetting means, the water supply flows along the inner peripheral surface of the fuselage, that is, flows substantially horizontally. Accordingly, since the steam and the water supply are in contact with each other substantially orthogonally below the steam jetting means, the oxygen contained in the water supply can be heated and degassed with high efficiency. Furthermore, since a plurality of the steam ejection means groups are provided in the direction orthogonal to the axial direction of the body, that is, along the flow of the feed water, the feed water contacts the steam with high efficiency in the flow, and the deaeration efficiency is improved. Can be increased.

また、前記噴出手段群を構成する各噴出手段の下端位置からその鉛直方向下方の胴体内周面までの間隙の距離を同一に設定するとよい。
これにより、前記間隙を、前記給水が胴体の内周面に沿って流れることを促進できる。
Moreover, it is preferable to set the distance of the gap from the lower end position of each of the jetting means constituting the jetting means group to the circumferential surface of the fuselage in the vertical direction below the same.
Thereby, it can accelerate | stimulate that the said water supply flows along the internal peripheral surface of a trunk | drum through the said clearance gap.

また、前記噴出手段群を構成する複数の噴出手段は、前記胴体の軸方向と直交する水平方向中心線を軸線とした線対称に配置されているとよい。
これにより、どのように流れた給水も均等に蒸気と接触することができ、脱気のムラを無くすことができる。
Further, the plurality of jetting means constituting the jetting means group may be arranged in line symmetry with a horizontal center line orthogonal to the axial direction of the body as an axis.
Thereby, the water supply which flowed how can contact with a vapor | steam equally, and the nonuniformity of deaeration can be eliminated.

また、前記貯水部を、前記胴体の軸線方向に2つの領域に分割する仕切板を有し、該仕切板は下部に間隙を設けて配置されて、該間隙を介して前記2つの領域は連通されており、前記給水供給部は、前記2つの領域の一方にのみ給水を供給するように配されるとともに、前記給水出口部は、前記給水供給部から給水が供給される領域と別の領域に配されるとよい。   In addition, the water storage section includes a partition plate that divides the water storage portion into two regions in the axial direction of the body, and the partition plate is disposed with a gap in the lower portion, and the two regions communicate with each other through the gap. The water supply supply unit is arranged to supply water supply to only one of the two regions, and the water supply outlet unit is a region different from the region where water supply is supplied from the water supply supply unit. It is good to be arranged.

本発明によれば、胴体内の貯水部に上方より給水を供給する給水供給部の下方であっても、給水と蒸気とを直交接触させることができ、脱気効率の向上が可能である単胴式の脱気器を提供することができる。   According to the present invention, water supply and steam can be brought into orthogonal contact with each other even below the water supply supply unit that supplies water to the water storage unit in the fuselage from above, and the deaeration efficiency can be improved. A torso type deaerator can be provided.

実施例における単胴式脱気器を示す概略横断面図である。It is a schematic cross-sectional view which shows the single cylinder type deaerator in an Example. 図1におけるA−A断面図である。It is AA sectional drawing in FIG. 給水供給部の別の例の胴体の軸方向と直交する方向の断面図である。It is sectional drawing of the direction orthogonal to the axial direction of the trunk | drum of another example of a water supply part. 図3におけるB方向矢視図である。It is a B direction arrow line view in FIG. 図4におけるC方向矢視図である。It is a C direction arrow directional view in FIG. 従来の単胴式脱気器の一例を示す概略横断面図である。It is a schematic cross-sectional view showing an example of a conventional single-cylinder deaerator. 従来の単胴式脱気器の別の例を示す概略横断面図である。It is a schematic cross-sectional view which shows another example of the conventional single cylinder type deaerator.

以下、図面を参照して本発明の好適な実施例を例示的に詳しく説明する。但しこの実施例に記載されている構成部品の寸法、材質、形状、その相対的配置等は特に特定的な記載がない限りは、この発明の範囲をそれに限定する趣旨ではなく、単なる説明例に過ぎない。   Hereinafter, exemplary embodiments of the present invention will be described in detail with reference to the drawings. However, the dimensions, materials, shapes, relative arrangements, and the like of the components described in this embodiment are not intended to limit the scope of the present invention unless otherwise specified, but are merely illustrative examples. Not too much.

まず、図1及び図2を用いて本発明の脱気器の構成について説明する。
図1は、実施例における単胴式脱気器を示す概略横断面図であり、図2は、図1におけるA−A断面図である。
First, the structure of the deaerator of this invention is demonstrated using FIG.1 and FIG.2.
FIG. 1 is a schematic cross-sectional view showing a single cylinder type deaerator in the embodiment, and FIG. 2 is a cross-sectional view taken along line AA in FIG.

本発明の単胴式脱気器1は、横長筒状の胴体2を有し、胴体2の頭部側に給水供給部3と蒸気供給部4とを備え、胴体2の底部側でかつ給水供給部3から胴体2の軸方向に離れる方向の位置に給水出口部5を備えている。   A single-body deaerator 1 of the present invention has a horizontally long cylindrical body 2, and includes a water supply supply unit 3 and a steam supply unit 4 on the head side of the body 2, and a water supply on the bottom side of the body 2. A water supply outlet portion 5 is provided at a position away from the supply portion 3 in the axial direction of the body 2.

給水供給部3は、多数のスプレーノズル31が取り付けられた板状部材33と、該板状部材33の上部空間36に給水を導入する導入口32と、ガイド35から構成されている。板状部材33は、胴体2の軸方向両端は仕切板34で仕切られ、胴体2の軸方向と直交する方向の両端は図2に示すように胴体2の内壁に取り付けられており、板状部材33の上部空間36は閉じた空間となっている。また、スプレーノズル31は、上部空間36に導入口32から供給された給水を霧状にして胴体2に形成される貯水部6に噴霧して供給するものである。また、ガイド35はスプレーノズル31によって噴霧される給水の噴霧方向を規制するものであって、ガイド35によってスプレーノズル31から噴霧された給水は、胴体2の軸方向と直交する方向の胴体中心付近に噴霧される。   The water supply unit 3 includes a plate-like member 33 to which a large number of spray nozzles 31 are attached, an introduction port 32 for introducing water supply into the upper space 36 of the plate-like member 33, and a guide 35. The plate-like member 33 is partitioned at both ends in the axial direction of the body 2 by a partition plate 34, and both ends in the direction orthogonal to the axial direction of the body 2 are attached to the inner wall of the body 2 as shown in FIG. The upper space 36 of the member 33 is a closed space. Moreover, the spray nozzle 31 sprays and supplies the water supply supplied from the inlet 32 to the upper space 36 to the water storage section 6 formed in the body 2 in the form of a mist. The guide 35 regulates the spraying direction of the feed water sprayed by the spray nozzle 31, and the feed water sprayed from the spray nozzle 31 by the guide 35 is near the trunk center in the direction orthogonal to the axial direction of the trunk 2. Sprayed on.

また、蒸気供給部4は、蒸気を導入する蒸気入口管41と、蒸気入口管41に接続されて胴体2の軸方向に延びる蒸気ヘッダー42と、蒸気ヘッダー42から貯水部6に向って延びて、前記胴体の軸方向に複数配設されるスプレーパイプ群43とから構成される。スプレーパイプ群43は、貯水部6内で多数の開孔部を有する複数(本実施例においては6つ)のスプレーパイプ43a、43b・・・43fから構成されている。即ち、蒸気供給部4は、蒸気タービン(不図示)などの外部機器からの蒸気を蒸気入口管41、蒸気ヘッダ42、スプレーパイプ群43を介して貯水部6内に供給するものである。   The steam supply unit 4 includes a steam inlet pipe 41 for introducing steam, a steam header 42 connected to the steam inlet pipe 41 and extending in the axial direction of the body 2, and extending from the steam header 42 toward the water storage unit 6. And a plurality of spray pipe groups 43 arranged in the axial direction of the body. The spray pipe group 43 is composed of a plurality (six in this embodiment) of spray pipes 43a, 43b,. That is, the steam supply unit 4 supplies steam from an external device such as a steam turbine (not shown) into the water storage unit 6 through the steam inlet pipe 41, the steam header 42, and the spray pipe group 43.

スプレーパイプ群43は、図2に示すように、胴体2の軸方向と直交する方向に複数本(図2に示した本実施例においては6本)のスプレーパイプ43a、43b・・・43fから構成されており、各スプレーパイプ43a、43b・・・43fの下端とその鉛直方向下側の胴体2の内表面との距離dが全て同じになるように各スプレーパイプ43a、43b・・・43fは設けられている。また、胴体2の軸方向と直交する方向の中心付近(図2においてaで表す範囲/スプレーパイプより噴出した蒸気泡が、隣接するスプレーパイプから噴出した蒸気泡とぶつかり、合体し、気泡サイズが大きくならない範囲及び当該範囲と下降流の幅fを加えた間隔が設けられた範囲)にはスプレーパイプは配設されていない。 As shown in FIG. 2, the spray pipe group 43 includes a plurality of spray pipes 43a, 43b,... 43f in a direction orthogonal to the axial direction of the body 2 (six in the present embodiment shown in FIG. 2). Each of the spray pipes 43a, 43b,... 43f is configured so that the distances d between the lower ends of the spray pipes 43a, 43b,... 43f and the inner surface of the body 2 on the lower side in the vertical direction are all the same. Is provided. Further, near the center of the direction perpendicular to the axial direction of the fuselage 2 (the range represented by a in FIG. 2 / the vapor bubbles ejected from the spray pipe collide with the vapor bubbles ejected from the adjacent spray pipe, coalesce, and the bubble size is spray pipe largely become not scope and range interval plus the width f 1 of the range and downflow is provided) is not provided.

また、貯水部6には仕切板8が設けられており、仕切板8によって貯水部6は対向流領域61と、対向流領域62とに分割されている。なお、仕切板8は、下方に間隙9が形成されるように設けられており、間隙9によって対向流領域61と対向流領域62とは連通している。   Further, the water storage section 6 is provided with a partition plate 8, and the water storage section 6 is divided into a counter flow region 61 and a counter flow region 62 by the partition plate 8. The partition plate 8 is provided so that a gap 9 is formed below, and the counterflow region 61 and the counterflow region 62 communicate with each other through the gap 9.

このような脱気器1において、対向流領域61では、スプレーノズル31から噴霧された給水は、ガイド35によってその噴霧方向を規制されて胴体2の軸方向と直交する方向の胴体中心付近に噴霧される。そして、該給水は図2にfで示したように前記胴体中心付近をそのまま下降する。該給水は、胴体2の下端まで達すると、そこで図2にf→fで示したように胴体2の内周面に沿って上昇していく。 In such a deaerator 1, in the counterflow region 61, the water supplied from the spray nozzle 31 is sprayed in the vicinity of the fuselage center in the direction orthogonal to the axial direction of the fuselage 2 with the spraying direction regulated by the guide 35. Is done. Then, water supply as it is lowered to the body around the center as shown in f 1 in FIG. When the water supply reaches the lower end of the fuselage 2, it rises along the inner peripheral surface of the fuselage 2 as indicated by f 2 → f 3 in FIG.

このとき、スプレーパイプ群43を構成するスプレーパイプは、図2にaで示す胴体2の軸方向と直交する方向の中心付近の範囲には設けられていないので、スプレーパイプ43がスプレーノズル31から噴霧された給水が胴体2の軸方向と直交する方向の中心付近を下降すること(図2に示したfの流れ)を妨害することはない。 At this time, the spray pipes constituting the spray pipe group 43 are not provided in the vicinity of the center in the direction orthogonal to the axial direction of the body 2 shown by a in FIG. The sprayed water supply does not interfere with the lowering of the vicinity of the center in the direction orthogonal to the axial direction of the body 2 (flow of f 1 shown in FIG. 2).

また、各スプレーパイプ43の下端とその鉛直方向下側の胴体2の内表面との距離dが全て同じになるように複数本のスプレーパイプ43は設けられているので、スプレーパイプ43が胴体2の内周面に沿って流れることを妨害することもなく、前記距離dを均一にすることで給水の内周面に沿った流れの形成を促進している。   Further, since the plurality of spray pipes 43 are provided so that the distances d between the lower ends of the spray pipes 43 and the inner surface of the body 2 on the lower side in the vertical direction are all the same, the spray pipes 43 are formed of the body 2. The formation of the flow along the inner peripheral surface of the water supply is promoted by making the distance d uniform without obstructing the flow along the inner peripheral surface of the water supply.

一方、スプレーパイプ群43を形成する各スプレーパイプ43a、43b・・・43fの前記開口部からの蒸気は、気泡となって貯水部6の給水(貯水)中に噴出され、気泡の持つ広い接触面積で給水(貯水)と直接接触し、給水(貯水)に含まれる酸素を加熱脱気させる。このとき、蒸気は各スプレーパイプ43a、43b・・・43fから下向きに噴出され、その後上昇するため、上下方向の流れを形成する。一方、各スプレーパイプ43a、43b・・・43fの下側では給水は図2に示したようにスプレーパイプの下方を胴体2の内周面に沿って流れており、即ち略水平に流れている。   On the other hand, the steam from the opening of each of the spray pipes 43a, 43b,... 43f forming the spray pipe group 43 is bubbled into the water supply (water storage) of the water storage unit 6, and the wide contact of the bubbles. In direct contact with the water supply (storage water) by area, the oxygen contained in the water supply (storage water) is heated and degassed. At this time, the steam is ejected downward from each of the spray pipes 43a, 43b,... 43f and then rises, so that a vertical flow is formed. On the other hand, below each spray pipe 43a, 43b,... 43f, the water supply flows along the inner peripheral surface of the body 2 below the spray pipe as shown in FIG. .

従って、スプレーパイプ43a、43b・・・43fの下方では蒸気と給水は略直交して接触するため、高効率で給水に含まれる酸素を加熱脱気することができる。さらに、スプレーパイプ43a、43b・・・43fを胴体2の軸方向と直交する方向、即ち給水の流れに沿って複数本(図2の例においては6本)設けているため、給水はその流れの中で蒸気と高効率で接触し、脱気効率を高めることができる。   Therefore, since the steam and the water supply are in contact with each other substantially orthogonally below the spray pipes 43a, 43b,... 43f, the oxygen contained in the water supply can be heated and degassed with high efficiency. Furthermore, since a plurality of spray pipes 43a, 43b,... 43f are provided in the direction perpendicular to the axial direction of the body 2, that is, along the flow of the water supply (six in the example of FIG. 2), the water supply flows. It is possible to contact the steam with high efficiency and improve the deaeration efficiency.

なお、給水(貯水)から酸素を加熱脱気させた気泡としての蒸気は、貯水部6中を上昇して胴体2内上部の蒸気空間部7に達すると、ここで給水供給部3のスプレーノズル31から噴霧される霧状の給水と直接接触し、給水に含まれる酸素を加熱脱気させる。脱気により給水から分離された酸素及び随伴蒸気は胴体2の上部に設けた空気出口(不図示)より外部に排出される。   In addition, when the steam as bubbles obtained by heating and degassing oxygen from the water supply (storage water) rises in the water storage section 6 and reaches the steam space section 7 in the upper part of the body 2, the spray nozzle of the water supply supply section 3 here The mist-like water sprayed from 31 is directly contacted, and oxygen contained in the water is heated and deaerated. Oxygen and accompanying steam separated from the feed water by deaeration are discharged to the outside through an air outlet (not shown) provided in the upper part of the body 2.

即ち、本実施例によれば、対向流領域61においても蒸気と給水を直交に近い状態で接触させることができ、高効率での脱気が可能である。   That is, according to the present embodiment, the steam and the water supply can be brought into contact with each other even in the counterflow region 61 in a nearly orthogonal state, and deaeration with high efficiency is possible.

また、対向流領域においては、前記給水が、仕切板8の下方の間隙9を通過することで、胴体2の軸方向に流れ、上昇する気泡としての蒸気と直交接触して加熱脱気される。対向流領域では蒸気と給水が直交接触するため高効率での脱気が可能である。
対交流領域及び対向流領域で脱気された給水は給水出口部5より外部に排出され、脱気された水を必要とする他機器に送られて使用される。
Further, in the counterflow region, the water supply passes through the gap 9 below the partition plate 8 and flows in the axial direction of the body 2, and is heated and deaerated while being orthogonally contacted with the vapor as rising bubbles. . In the counterflow region, steam and feed water are in orthogonal contact with each other, so high efficiency degassing is possible.
The water supply deaerated in the counter-current region and the counterflow region is discharged to the outside from the water supply outlet 5 and sent to other equipment that requires the degassed water for use.

本発明においては、給水を霧化して噴霧するスプレーノズル31の下方であっても蒸気と給水を直交に近い状態で接触させることができるため、脱気効率の向上が可能である。   In the present invention, even under the spray nozzle 31 that atomizes and sprays the feed water, the steam and the feed water can be brought into contact with each other in a nearly orthogonal state, so that the deaeration efficiency can be improved.

なお、給水供給部103は、図6、図7に示した形態に限られず、他の形態とすることもできる。給水供給部103の他の形態の一例について図3〜図4を用いて説明する。図3〜図4は、給水供給部の別の形態を示す図であり、図3は胴体2の軸方向と直交する方向の断面図であって図2の上部に相当するもの、図4は図3におけるB方向矢視図、図5は図4におけるC方向矢視図である。   In addition, the water supply part 103 is not restricted to the form shown in FIG. 6, FIG. 7, It can also be set as another form. An example of another form of the water supply unit 103 will be described with reference to FIGS. 3-4 is a figure which shows another form of a water supply part, FIG. 3 is sectional drawing of the direction orthogonal to the axial direction of the fuselage | body 2, and corresponds to the upper part of FIG. 2, FIG. FIG. 5 is a view in the direction of arrow B in FIG. 3, and FIG. 5 is a view in the direction of arrow C in FIG.

給水供給部3’は、6本のスプレーノズル31’が取り付けられた胴体2と、給水を貯留しスプレーノズル31’に供給するヘッダー36’と、該ヘッダー36’に給水を導入する導入口32’と、ガイド35’から構成されている。図4〜図3に示したような給水供給部3’では、導入口32’から導入された給水は、ヘッダー36’に一旦貯留され、各スプレーノズル31’より胴体2内の貯水部6へ向けて噴霧される。この際、ガイド35’によって胴体2の軸方向と直交する方向の胴体中心付近に噴霧されるように規制される。
図4〜図3に示したような給水供給部3’の形態は大量の給水を供給する場合に適しており、給水の供給量即ち脱気器1の処理量に応じて適切な給水供給部の形態を選択するとよい。
The water supply unit 3 ′ includes a body 2 to which six spray nozzles 31 ′ are attached, a header 36 ′ for storing water supply and supplying the spray nozzle 31 ′, and an inlet 32 for introducing water supply to the header 36 ′. 'And a guide 35'. In the water supply unit 3 ′ as shown in FIGS. 4 to 3, the water supplied from the introduction port 32 ′ is temporarily stored in the header 36 ′, and is supplied to the water storage unit 6 in the body 2 from each spray nozzle 31 ′. Sprayed toward. At this time, the guide 35 ′ is regulated so that it is sprayed in the vicinity of the center of the body in the direction orthogonal to the axial direction of the body 2.
The form of the water supply unit 3 ′ as shown in FIGS. 4 to 3 is suitable for supplying a large amount of water supply, and is suitable for the supply amount of the water supply, that is, the processing amount of the deaerator 1. It is good to select the form.

胴体内の貯水部に上方より給水を供給する給水供給部の下方であっても、給水と蒸気とを直交接触させることができ、脱気効率の向上が可能である単胴式の脱気器として利用することができる。   A single-cylinder type deaerator that can make the feed water and steam orthogonally contact with each other even below the feed water supply unit that supplies feed water to the water storage unit in the fuselage from above. Can be used as

1 脱気器
2 胴体
3 給水供給部
4 蒸気供給部
5 給水出口部
6 貯水部
8 仕切板
9 間隙
31 スプレーノズル(給水噴出手段)
35 ガイド(規制手段)
43 スプレーパイプ群(蒸気噴出手段群)
43a〜43f スプレーパイプ(蒸気噴出手段)
DESCRIPTION OF SYMBOLS 1 Deaerator 2 Body 3 Water supply part 4 Steam supply part 5 Water supply outlet part 6 Water storage part 8 Partition plate 9 Gap 31 Spray nozzle (water supply ejection means)
35 Guide (regulatory means)
43 Spray pipe group (steam jetting means group)
43a-43f spray pipe (steam ejection means)

Claims (4)

内部に給水を貯留する貯水部を有する胴体と、前記胴体の上部に設けられ前記貯水部に給水を噴出する給水供給部と、前記胴体の貯水部に蒸気を供給する蒸気供給部と、前記胴体の底部に設けられ前記給水を排出するための給水出口部とを有する脱気器において、
前記給水供給部は、前記貯水部に上方より給水を噴出する給水噴出手段と、前記給水噴出手段より噴出された給水を前記胴体の軸方向と直交する水平方向中心部に向ける規制手段とを有し、
前記蒸気供給部は、前記貯水部中に蒸気を噴出させる蒸気噴出手段を前記胴体の軸方向と直交する水平方向に複数備えた蒸気噴出手段群を、前記胴体の軸方向に複数群有して構成され、
前記噴出手段群を構成する前記噴出手段は、それぞれの噴出手段の下端位置からその鉛直方向下方の胴体内周面までの間隙の距離を、前記給水が流通可能な距離に設定して配置されるとともに、前記噴出手段を前記胴体の軸方向と直交する水平方向中心部に位置しないことを特徴とする脱気器。
A fuselage having a water storage part for storing water supply therein, a water supply supply part provided at an upper part of the fuselage for ejecting water supply to the water storage part, a steam supply part for supplying steam to the water storage part of the fuselage, and the fuselage A deaerator having a water supply outlet provided at the bottom of the water supply for discharging the water supply,
The water supply unit has water supply jetting means for jetting water from above into the water storage part, and regulating means for directing the water jetted from the water supply jetting means toward a horizontal central portion orthogonal to the axial direction of the fuselage. And
The steam supply section has a plurality of steam ejection means groups, each having a plurality of steam ejection means for ejecting steam into the water storage section in a horizontal direction orthogonal to the axial direction of the fuselage, in the axial direction of the fuselage. Configured,
The jetting means constituting the jetting means group are arranged by setting the distance of the gap from the lower end position of each jetting means to the body circumferential surface below the vertical direction to the distance through which the water supply can flow. In addition, the deaerator is characterized in that the jetting means is not located in a horizontal central portion orthogonal to the axial direction of the body.
前記噴出手段群を構成する各噴出手段の下端位置からその鉛直方向下方の胴体内周面までの間隙の距離を同一に設定したことを特徴とする請求項1記載の脱気器。   The deaerator according to claim 1, wherein a distance between a lower end position of each of the jetting means constituting the jetting means group and a peripheral surface of the trunk in the vertical direction is set to be the same. 前記噴出手段群を構成する複数の噴出手段は、前記胴体の軸方向と直交する水平方向中心線を軸線とした線対称に配置されていることを特徴とする請求項1又は2記載の脱気器。   3. The deaeration according to claim 1, wherein the plurality of ejection means constituting the ejection means group are arranged symmetrically with respect to a horizontal center line orthogonal to the axial direction of the body. vessel. 前記貯水部を、前記胴体の軸線方向に2つの領域に分割する仕切板を有し、
該仕切板は下部に間隙を設けて配置されて、該間隙を介して前記2つの領域は連通されており、
前記給水供給部は、前記2つの領域の一方にのみ給水を供給するように配されるとともに、
前記給水出口部は、前記給水供給部から給水が供給される領域と別の領域に配されることを特徴とする請求項1〜3何れかに記載の脱気器。
A partition plate that divides the water reservoir into two regions in the axial direction of the body;
The partition plate is arranged with a gap in the lower part, and the two regions communicate with each other through the gap.
The water supply unit is arranged to supply water to only one of the two regions,
The deaerator according to any one of claims 1 to 3, wherein the water supply outlet is arranged in a region different from a region where water is supplied from the water supply unit.
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* Cited by examiner, † Cited by third party
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EP3153792A1 (en) * 2015-09-01 2017-04-12 Doosan Heavy Industries & Construction Co., Ltd. Deaerator
US10605533B2 (en) 2015-09-01 2020-03-31 DOOSAN Heavy Industries Construction Co., LTD Deaerator
KR101785787B1 (en) 2015-09-02 2017-10-16 두산중공업 주식회사 Deaerator
KR101761090B1 (en) 2017-03-30 2017-07-24 두산중공업 주식회사 Deaerator

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