JP2001187307A - Horizontal steam separator for steam drum - Google Patents

Horizontal steam separator for steam drum

Info

Publication number
JP2001187307A
JP2001187307A JP37474199A JP37474199A JP2001187307A JP 2001187307 A JP2001187307 A JP 2001187307A JP 37474199 A JP37474199 A JP 37474199A JP 37474199 A JP37474199 A JP 37474199A JP 2001187307 A JP2001187307 A JP 2001187307A
Authority
JP
Japan
Prior art keywords
steam
horizontal
water
duct
drum
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
Application number
JP37474199A
Other languages
Japanese (ja)
Other versions
JP4415438B2 (en
Inventor
Kiichi Korekawa
紀一 是川
Masahiro Inoue
雅裕 井上
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
IHI Corp
Original Assignee
IHI Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by IHI Corp filed Critical IHI Corp
Priority to JP37474199A priority Critical patent/JP4415438B2/en
Publication of JP2001187307A publication Critical patent/JP2001187307A/en
Application granted granted Critical
Publication of JP4415438B2 publication Critical patent/JP4415438B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a horizontal steam separator for a steam drum capable of improving water separating performance at respective horizontal steam separators by equalizing the steam quantity introduced into respective horizontal steam separators, capable of preventing the generation of carry-over, capable of improving efficiency by suppressing a fall of steam temperature and also capable of avoiding undesirable influence on a turbine blade of a steam turbine. SOLUTION: A perforated plate 10 for controlling flow passage resistance is mounted at the inlet part of a steam inlet duct 8a of the horizontal steam separator 8.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、蒸気ドラム用横型
汽水分離装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a horizontal brackish water separator for a steam drum.

【0002】[0002]

【従来の技術】図3はボイラの一例を表わすものであっ
て、図中、1はボイラ本体、2はボイラ本体1内へ燃料
を噴射して燃焼させるバーナ、3は蒸気ドラムであり、
蒸気ドラム3内の水を図示していない降水管を介してボ
イラ本体1の炉壁管下部へ供給した状態で、バーナ2か
らボイラ本体1内へ燃料を噴射して燃焼させることによ
り、燃焼ガスを生成し、生成された燃焼ガスと、前記ボ
イラ本体1の炉壁管内を流れる水、並びに図示していな
い過熱器等の内部を流れる蒸気或いは水とを互いに熱交
換させ、熱交換により加熱された蒸気を多数の蒸気導入
管4を介して蒸気ドラム3へ導入し、該蒸気ドラム3内
において後述する横型汽水分離器8(図4〜図6参照)
により汽水分離を行った後、蒸気のみを蒸気導出管5か
ら図示していない蒸気タービンへ導き、該蒸気タービン
を駆動して発電機を駆動する一方、熱交換した後の排ガ
スは排ガスダクト6へ流出させるようになっている。
2. Description of the Related Art FIG. 3 shows an example of a boiler, in which 1 is a boiler main body, 2 is a burner for injecting fuel into a boiler main body 1 and burning it, 3 is a steam drum,
By injecting fuel from the burner 2 into the boiler main body 1 in a state where water in the steam drum 3 is supplied to a lower part of the furnace wall pipe of the boiler main body 1 via a downcomer (not shown), combustion gas is generated. The generated combustion gas and the water flowing through the furnace wall tube of the boiler main body 1 and the steam or water flowing inside the superheater (not shown) exchange heat with each other, and are heated by the heat exchange. The introduced steam is introduced into the steam drum 3 through a number of steam introduction pipes 4, and a horizontal brackish water separator 8 described later in the steam drum 3 (see FIGS. 4 to 6).
After steam separation is performed, only steam is guided from a steam outlet pipe 5 to a steam turbine (not shown), and the steam turbine is driven to drive a generator. It is designed to drain.

【0003】前記蒸気ドラム3は、図4に示される如
く、必要に応じて図示していない給水ラインから水が供
給され且つ図示していない降水管へ水を下降させる貯水
部3aと、該貯水部3aと仕切壁7を隔てて画成され且
つ蒸気導入管4(図3参照)から水を含む蒸気が導入さ
れる蒸気導入室3bと、該蒸気導入室3bの所要箇所か
ら蒸気ドラム3の中心部ヘ向け張り出すように配設され
た蒸気導入ダクト3cとを有しており、蒸気導入室3b
から蒸気導入ダクト3cへ導入された水を含む蒸気を、
該蒸気導入ダクト3c上に配置された複数の横型汽水分
離器8において水分を除去した後、内部に多数の波板が
配設されたV型ドライヤ9において更に水分を除去し、
蒸気導出管5(図3参照)から蒸気タービンへ導くよう
になっている。
As shown in FIG. 4, the steam drum 3 is provided with a water storage section 3a to which water is supplied from a water supply line (not shown) as required and which lowers the water to a downcomer (not shown). A steam introduction chamber 3b defined between the section 3a and the partition wall 7 and into which steam containing water is introduced from a steam introduction pipe 4 (see FIG. 3); A steam introduction duct 3c disposed so as to project toward the center, and a steam introduction chamber 3b.
Steam containing water introduced into the steam introduction duct 3c from
After removing moisture in a plurality of horizontal brackish water separators 8 arranged on the steam introduction duct 3c, moisture is further removed in a V-shaped dryer 9 in which a large number of corrugated plates are disposed.
The steam is led from the steam outlet pipe 5 (see FIG. 3) to the steam turbine.

【0004】前記各横型汽水分離器8は、図5及び図6
に示される如く、前記蒸気ドラム3の蒸気導入室3bに
連通するよう蒸気導入ダクト3c上に接続され且つ上下
方向へ延びる蒸気入口ダクト8aと、前記蒸気ドラム3
の蒸気導入室3bから蒸気導入ダクト3cへ導入された
水を含む蒸気が前記蒸気入口ダクト8aから接線方向へ
導かれ且つ軸線が前記蒸気ドラム3の軸線と略平行とな
るよう略水平に延びる円筒状の遠心分離ダクト8bと、
該遠心分離ダクト8bの下部所要位置に開口され且つ遠
心分離ダクト8bで分離された水をドレンとして前記貯
水部3aへ排出する一次ドレン出口部8cと、前記遠心
分離ダクト8bの下部所要位置から下方へ延設されたド
レンダクト8dと、該ドレンダクト8dの下端部に開口
され且つ前記遠心分離ダクト8bで分離された水をドレ
ンとして前記貯水部3aへ排出するドレン出口部8e
と、前記遠心分離ダクト8bの軸線方向両端部に開口さ
れ且つ水が分離された蒸気を蒸気ドラム3内上部へ排出
する蒸気出口部8fとを備えてなる構成を有している。
Each of the horizontal brackish water separators 8 is shown in FIGS.
, A steam inlet duct 8a connected to a steam inlet duct 3c so as to communicate with a steam inlet chamber 3b of the steam drum 3 and extending in a vertical direction;
The steam containing water introduced from the steam introduction chamber 3b into the steam introduction duct 3c is tangentially guided from the steam inlet duct 8a, and extends substantially horizontally so that the axis is substantially parallel to the axis of the steam drum 3. Centrifugal separation duct 8b,
A primary drain outlet 8c which is opened at a required position below the centrifugal separation duct 8b and discharges water separated by the centrifugal separation duct 8b as a drain to the water storage portion 3a; And a drain outlet 8e which is opened at the lower end of the drain duct 8d and drains the water separated by the centrifugal separation duct 8b as drain to the water storage 3a.
And a steam outlet 8f which is opened at both ends in the axial direction of the centrifugal separation duct 8b and discharges the steam from which water has been separated to the upper portion inside the steam drum 3.

【0005】前記各横型汽水分離器8においては、蒸気
ドラム3の蒸気導入室3bから蒸気導入ダクト3cへ導
入された水を含む蒸気は、蒸気入口ダクト8aから遠心
分離ダクト8bの接線方向へ導かれ、該遠心分離ダクト
8b内に沿って旋回する際の遠心力により、前記蒸気に
含まれる水が分離され、一次ドレン出口部8c及びドレ
ン出口部8eから蒸気ドラム3の貯水部3aへ排出され
ると共に、水が分離された蒸気は、遠心分離ダクト8b
の蒸気出口部8fから蒸気ドラム3内上部へ排出される
ようになっている。
In each of the horizontal steam separators 8, the steam containing water introduced from the steam introduction chamber 3b of the steam drum 3 into the steam introduction duct 3c is guided from the steam inlet duct 8a in the tangential direction of the centrifugal separation duct 8b. Then, the water contained in the steam is separated by the centrifugal force when swirling along the centrifugal separation duct 8b, and is discharged from the primary drain outlet 8c and the drain outlet 8e to the water reservoir 3a of the steam drum 3. And the steam from which the water has been separated is supplied to the centrifugal separation duct 8b.
From the steam outlet 8f to the upper portion of the steam drum 3.

【0006】尚、図4に示されるように、蒸気ドラム3
内における左側の蒸気導入ダクト3c上に横型汽水分離
器8を二列に配置すると共に、蒸気ドラム3内における
右側の蒸気導入ダクト3c上に横型汽水分離器8を三列
に配置してあるのは、蒸気導入管4から蒸気ドラム3の
蒸気導入室3bへ導入される蒸気量に左右で差があると
共に、設置スペース上の都合からである。
Incidentally, as shown in FIG.
The horizontal brackish water separators 8 are arranged in two rows on the left steam introducing duct 3c in the inside, and the horizontal brackish water separators 8 are arranged in three rows on the right steam introducing duct 3c in the steam drum 3. This is because there is a difference in the amount of steam introduced from the steam introduction pipe 4 into the steam introduction chamber 3b of the steam drum 3 on the right and left sides, and the installation space is limited.

【0007】[0007]

【発明が解決しようとする課題】前述の如き横型汽水分
離器8を蒸気ドラム3内に複数配置してなる蒸気ドラム
用横型汽水分離装置においては、各横型汽水分離器8に
導入される蒸気量は均等化を図る必要があるが、特に、
図4に示される如く、蒸気導入ダクト3c上に配置する
横型汽水分離器8の数を左右で違えたような場合には、
各横型汽水分離器8に導入される蒸気量にアンバランス
が生じて、各横型汽水分離器8における水の分離性能に
影響が出てしまい、水とシリカ等の固形分が蒸気と一緒
に蒸気出口部8fから排出されてしまう、いわゆるキャ
リーオーバーが発生し、蒸気温度が低下して効率が落ち
ると共に、シリカ等の固形分が蒸気タービンへ送り込ま
れると、該蒸気タービンのタービン翼に悪影響を及ぼす
という欠点があり、対策が望まれていた。
In the horizontal steam water separator for a steam drum in which a plurality of the horizontal steam separators 8 are arranged in the steam drum 3 as described above, the amount of steam introduced into each horizontal steam separator 8 is described. Needs to be equalized, but in particular,
As shown in FIG. 4, when the number of the horizontal brackish water separators 8 arranged on the steam introduction duct 3c is different between the left and right,
An imbalance occurs in the amount of steam introduced into each horizontal brackish water separator 8, which affects the water separation performance in each horizontal brackish water separator 8. When so-called carryover, which is discharged from the outlet portion 8f, occurs, the steam temperature decreases and the efficiency decreases, and when solids such as silica are fed into the steam turbine, the turbine blades of the steam turbine are adversely affected. There was a drawback that measures were desired.

【0008】本発明は、斯かる実情に鑑み、各横型汽水
分離器に導入される蒸気量を均等化して、各横型汽水分
離器における水の分離性能を向上し得、キャリーオーバ
ーの発生を防止することができ、蒸気温度の低下を抑制
して効率の向上を図り得ると共に、蒸気タービンのター
ビン翼への悪影響を回避し得る蒸気ドラム用横型汽水分
離装置を提供しようとするものである。
In view of such circumstances, the present invention can equalize the amount of steam introduced into each horizontal brackish water separator, improve the water separation performance in each horizontal brackish water separator, and prevent the occurrence of carryover. It is an object of the present invention to provide a steam drum horizontal brackish water separator capable of suppressing a decrease in steam temperature to improve efficiency and avoiding adverse effects on turbine blades of a steam turbine.

【0009】[0009]

【課題を解決するための手段】本発明は、貯水部と蒸気
導入室とを有する蒸気ドラム内に、該蒸気ドラムの蒸気
導入室と連通するよう配設された蒸気入口ダクトと、前
記蒸気ドラムの蒸気導入室へ導入された水を含む蒸気が
前記蒸気入口ダクトから接線方向へ導かれ且つ軸線が略
水平に延びる円筒状の遠心分離ダクトと、該遠心分離ダ
クトの下部所要位置に開口され且つ遠心分離ダクトで分
離された水をドレンとして前記貯水部へ排出するドレン
出口部と、前記遠心分離ダクトの軸線方向端部に開口さ
れる蒸気出口部とを備え、蒸気ドラムの蒸気導入室へ導
入された水を含む蒸気から水を除去する横型汽水分離器
を、前記蒸気ドラム内に複数配置してなる蒸気ドラム用
横型汽水分離装置において、横型汽水分離器の蒸気入口
ダクトの入口部に、流路抵抗調節用の多孔板を取り付け
たことを特徴とする蒸気ドラム用横型汽水分離装置にか
かるものである。
According to the present invention, there is provided a steam drum having a water storage section and a steam introduction chamber, a steam inlet duct disposed in communication with the steam introduction chamber of the steam drum, and the steam drum. A steam containing water introduced into the steam introduction chamber is tangentially guided from the steam inlet duct and has a cylindrical centrifugal separation duct whose axis extends substantially horizontally, and is opened at a required position below the centrifugal separation duct; and A drain outlet for discharging water separated by the centrifugal separation duct as a drain to the water storage unit, and a steam outlet opening at an axial end of the centrifugal separation duct, are introduced into a steam introduction chamber of a steam drum. A horizontal brackish water separator for removing water from steam containing water, in a steam drum horizontal brackish water separator that is arranged in the steam drum, in the inlet portion of the steam inlet duct of the horizontal brackish water separator In which according to the horizontal steam separator device for a steam drum, characterized in that fitted with perforated plates for adjusting the flow resistance.

【0010】上記手段によれば、以下のような作用が得
られる。
According to the above means, the following effects can be obtained.

【0011】横型汽水分離器の蒸気入口ダクトの入口部
に、流路抵抗調節用の多孔板を取り付けると、蒸気が導
入されやすい横型汽水分離器と蒸気が導入されにくい横
型汽水分離器との差が緩和され、各横型汽水分離器に導
入される蒸気量にアンバランスが生じなくなって、各横
型汽水分離器における水の分離性能に影響が出にくくな
り、水とシリカ等の固形分が蒸気と一緒に蒸気出口部か
ら排出されてしまう、いわゆるキャリーオーバーが発生
せず、蒸気温度が低下して効率が落ちることはなく、し
かも、シリカ等の固形分が蒸気タービンへ送り込まれな
くなり、該蒸気タービンのタービン翼に悪影響を及ぼす
心配もなくなる。
When a perforated plate for adjusting the flow path resistance is attached to the inlet of the steam inlet duct of the horizontal brackish water separator, the difference between the horizontal brackish water separator where steam is easily introduced and the horizontal brackish separator where steam is difficult to be introduced is provided. And the amount of steam introduced into each horizontal brackish water separator no longer becomes imbalanced, making it difficult to affect the water separation performance of each horizontal brackish water separator. The so-called carryover, which is discharged together with the steam from the steam outlet, does not occur, the efficiency of the steam does not decrease due to the decrease in the steam temperature, and solids such as silica are not fed into the steam turbine. There is no need to worry about adverse effects on the turbine blades.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施の形態を図示
例と共に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0013】図1及び図2は本発明を実施する形態の一
例であって、図中、図3〜図6と同一の符号を付した部
分は同一物を表わしており、基本的な構成は図3〜図6
に示す従来のものと同様であるが、本図示例の特徴とす
るところは、図1及び図2に示す如く、横型汽水分離器
8の蒸気入口ダクト8aの入口部に、流路抵抗調節用の
多孔板10を取り付けた点にある。
FIGS. 1 and 2 show an embodiment of the present invention. In the drawings, the portions denoted by the same reference numerals as those in FIGS. 3 to 6 represent the same components. 3 to 6
However, the present embodiment is characterized in that, as shown in FIGS. 1 and 2, the inlet of the steam inlet duct 8a of the horizontal brackish water separator 8 has In that the perforated plate 10 is attached.

【0014】前記多孔板10は、ステンレス等の金属板
11に、所要径を有する多数の孔12を横型汽水分離器
8の蒸気入口ダクト8aの入口部と対応させて穿設して
なり、蒸気導入ダクト3cの接続フランジ部13と横型
汽水分離器8の蒸気入口ダクト8aの接続フランジ部1
4との間にボルト・ナット15の締付により挟持される
ようにしてある。
The perforated plate 10 is formed by drilling a plurality of holes 12 having a required diameter in a metal plate 11 made of stainless steel or the like so as to correspond to the inlet of the steam inlet duct 8a of the horizontal brackish water separator 8. Connection flange 13 of introduction duct 3c and connection flange 1 of steam inlet duct 8a of horizontal brackish water separator 8
4 is clamped by tightening bolts and nuts 15.

【0015】図2には、図4に示されるように蒸気ドラ
ム3内における右側の蒸気導入ダクト3c上に三列に配
置した横型汽水分離器8の蒸気入口ダクト8aの入口部
に取り付けられる多孔板10を示してあるが、図4に示
されるように蒸気ドラム3内における左側の蒸気導入ダ
クト3c上に二列に配置した横型汽水分離器8の蒸気入
口ダクト8aの入口部に取り付けられる多孔板10は、
二列の横型汽水分離器8に対応するよう、図2中、仮想
線で示すように、横型汽水分離器8を一列分だけ削除し
て全長を略三分の二に縮小したものとなる。
FIG. 2 is a perspective view of the porous steam separator 8 arranged in three rows on the right steam introduction duct 3c in the steam drum 3 as shown in FIG. Although a plate 10 is shown, as shown in FIG. 4, a hole attached to the inlet of the steam inlet duct 8a of the horizontal brackish water separator 8 arranged in two rows on the left steam inlet duct 3c in the steam drum 3. The board 10
In order to correspond to the two rows of horizontal brackish water separators 8, the horizontal brackish water separators 8 are deleted by one row as shown by phantom lines in FIG.

【0016】尚、図2に示す如く、多孔板10を複数列
の横型汽水分離器8に跨るように長く形成する代りに、
各列の横型汽水分離器8毎に個別の多孔板10を取り付
けるようにしてもよいことは言うまでもない。
As shown in FIG. 2, instead of forming the perforated plate 10 so as to extend over a plurality of rows of the horizontal brackish water separators 8,
It goes without saying that an individual perforated plate 10 may be attached to each horizontal brackish water separator 8 in each row.

【0017】次に、上記図示例の作動を説明する。Next, the operation of the above illustrated example will be described.

【0018】横型汽水分離器8の蒸気入口ダクト8aの
入口部に、流路抵抗調節用の多孔板10を取り付ける
と、圧力損失が生じることで蒸気導入ダクト3c内部の
圧力が均一化され、蒸気が導入されやすい横型汽水分離
器8と蒸気が導入されにくい横型汽水分離器8との差が
緩和され、各横型汽水分離器8に導入される蒸気量にア
ンバランスが生じなくなって、各横型汽水分離器8にお
ける水の分離性能に影響が出にくくなり、水とシリカ等
の固形分が蒸気と一緒に蒸気出口部8fから排出されて
しまう、いわゆるキャリーオーバーが発生せず、蒸気温
度が低下して効率が落ちることはなく、しかも、シリカ
等の固形分が蒸気タービンへ送り込まれなくなり、該蒸
気タービンのタービン翼に悪影響を及ぼす心配もなくな
る。
If a perforated plate 10 for adjusting the flow path resistance is attached to the inlet of the steam inlet duct 8a of the horizontal brackish water separator 8, a pressure loss occurs, and the pressure inside the steam inlet duct 3c is made uniform, and The difference between the horizontal brackish water separator 8 in which steam is easily introduced and the horizontal brackish water separator 8 in which steam is hardly introduced is reduced, and the amount of steam introduced into each horizontal brackish water separator 8 does not become unbalanced. The separation performance of water in the separator 8 is hardly affected, and so-called carryover, in which water and solids such as silica are discharged from the steam outlet 8f together with the steam, does not occur, and the steam temperature decreases. As a result, the solid content such as silica is not fed into the steam turbine, and there is no fear of adversely affecting the turbine blades of the steam turbine.

【0019】尚、多孔板10は、蒸気導入ダクト3cの
接続フランジ部13と横型汽水分離器8の蒸気入口ダク
ト8aの接続フランジ部14との間にボルト・ナット1
5の締付により挟持されるようにしてあるため、必要に
応じて着脱調整を行うことにより、各横型汽水分離器8
に導入される蒸気量を確実に均等化させることが可能と
なる。
The perforated plate 10 is provided between the connection flange 13 of the steam introduction duct 3c and the connection flange 14 of the steam inlet duct 8a of the horizontal brackish water separator 8.
5 so that the horizontal brackish water separators 8 can be held by adjusting the attachment and detachment as necessary.
It is possible to reliably equalize the amount of steam introduced into the fuel cell.

【0020】こうして、各横型汽水分離器8に導入され
る蒸気量を均等化して、各横型汽水分離器8における水
の分離性能を向上し得、キャリーオーバーの発生を防止
することができ、蒸気温度の低下を抑制して効率の向上
を図り得ると共に、蒸気タービンのタービン翼への悪影
響を回避し得る。
In this way, the amount of steam introduced into each horizontal brackish water separator 8 can be equalized, the water separation performance in each horizontal brackish water separator 8 can be improved, and carryover can be prevented. The efficiency can be improved by suppressing a decrease in temperature, and adverse effects on turbine blades of the steam turbine can be avoided.

【0021】尚、本発明の蒸気ドラム用横型汽水分離装
置は、上述の図示例にのみ限定されるものではなく、本
発明の要旨を逸脱しない範囲内において種々変更を加え
得ることは勿論である。
It should be noted that the horizontal brackish water separator for a steam drum according to the present invention is not limited to the above illustrated example, and various changes can be made without departing from the gist of the present invention. .

【0022】[0022]

【発明の効果】以上、説明したように本発明の蒸気ドラ
ム用横型汽水分離装置によれば、各横型汽水分離器に導
入される蒸気量を均等化して、各横型汽水分離器におけ
る水の分離性能を向上し得、キャリーオーバーの発生を
防止することができ、蒸気温度の低下を抑制して効率の
向上を図り得ると共に、蒸気タービンのタービン翼への
悪影響を回避し得るという優れた効果を奏し得る。
As described above, according to the horizontal brackish water separator for a steam drum of the present invention, the amount of steam introduced into each horizontal brackish water separator is equalized to separate water in each horizontal brackish water separator. It is possible to improve the performance, prevent the occurrence of carryover, suppress the decrease in the steam temperature, improve the efficiency, and avoid the adverse effects on the turbine blades of the steam turbine. I can play.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明を実施する形態の一例の側断面図であっ
て、図4のV−V断面相当図である。
FIG. 1 is a side sectional view of an example of an embodiment of the present invention, and is a view corresponding to a section taken along line VV of FIG.

【図2】本発明を実施する形態の一例における多孔板の
平面図であって、図1のII−II矢視相当図である。
FIG. 2 is a plan view of a perforated plate according to an example of the embodiment of the present invention, and is a view corresponding to the view taken along the line II-II in FIG.

【図3】一般的なボイラの全体概要構成図である。FIG. 3 is an overall schematic configuration diagram of a general boiler.

【図4】従来の蒸気ドラムの一例を表わす断面図であ
る。
FIG. 4 is a cross-sectional view illustrating an example of a conventional steam drum.

【図5】従来の横型汽水分離器の一例を表わす側断面図
であって、図4のV−V断面相当図である。
5 is a side sectional view showing an example of a conventional horizontal brackish water separator, and is a view corresponding to a section taken along line VV of FIG. 4;

【図6】従来の横型汽水分離器の一例を表わす斜視図で
ある。
FIG. 6 is a perspective view illustrating an example of a conventional horizontal brackish water separator.

【符号の説明】[Explanation of symbols]

3 蒸気ドラム 3a 貯水部 3b 蒸気導入室 8 横型汽水分離器 8a 蒸気入口ダクト 8b 遠心分離ダクト 8c 一次ドレン出口部(ドレン出口部) 8d ドレンダクト 8e ドレン出口部 8f 蒸気出口部 9 V型ドライヤ 10 多孔板 Reference Signs List 3 steam drum 3a water storage section 3b steam introduction chamber 8 horizontal steam separator 8a steam inlet duct 8b centrifugal separation duct 8c primary drain outlet (drain outlet) 8d drain duct 8e drain outlet 8f steam outlet 9 V-type dryer 10 perforated plate

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 貯水部と蒸気導入室とを有する蒸気ドラ
ム内に、該蒸気ドラムの蒸気導入室と連通するよう配設
された蒸気入口ダクトと、前記蒸気ドラムの蒸気導入室
へ導入された水を含む蒸気が前記蒸気入口ダクトから接
線方向へ導かれ且つ軸線が略水平に延びる円筒状の遠心
分離ダクトと、該遠心分離ダクトの下部所要位置に開口
され且つ遠心分離ダクトで分離された水をドレンとして
前記貯水部へ排出するドレン出口部と、前記遠心分離ダ
クトの軸線方向端部に開口される蒸気出口部とを備え、
蒸気ドラムの蒸気導入室へ導入された水を含む蒸気から
水を除去する横型汽水分離器を、前記蒸気ドラム内に複
数配置してなる蒸気ドラム用横型汽水分離装置におい
て、 横型汽水分離器の蒸気入口ダクトの入口部に、流路抵抗
調節用の多孔板を取り付けたことを特徴とする蒸気ドラ
ム用横型汽水分離装置。
1. A steam inlet duct disposed in a steam drum having a water storage section and a steam introduction chamber so as to communicate with the steam introduction chamber of the steam drum, and introduced into the steam introduction chamber of the steam drum. Steam containing water is tangentially guided from the steam inlet duct and has a cylindrical centrifugal separation duct whose axis extends substantially horizontally; and water that is opened at a required position below the centrifugal separation duct and separated by the centrifugal separation duct. A drain outlet for discharging the water to the water storage unit as a drain, and a steam outlet that is opened at an axial end of the centrifugal separation duct,
A horizontal brackish water separator for a steam drum, comprising a plurality of horizontal brackish separators for removing water from the steam containing water introduced into the steam introduction chamber of the steam drum inside the steam drum. A horizontal brackish water separator for a steam drum, characterized in that a perforated plate for adjusting flow passage resistance is attached to the inlet of the inlet duct.
JP37474199A 1999-12-28 1999-12-28 Horizontal brackish water separator for steam drum Expired - Fee Related JP4415438B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP37474199A JP4415438B2 (en) 1999-12-28 1999-12-28 Horizontal brackish water separator for steam drum

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP37474199A JP4415438B2 (en) 1999-12-28 1999-12-28 Horizontal brackish water separator for steam drum

Publications (2)

Publication Number Publication Date
JP2001187307A true JP2001187307A (en) 2001-07-10
JP4415438B2 JP4415438B2 (en) 2010-02-17

Family

ID=18504357

Family Applications (1)

Application Number Title Priority Date Filing Date
JP37474199A Expired - Fee Related JP4415438B2 (en) 1999-12-28 1999-12-28 Horizontal brackish water separator for steam drum

Country Status (1)

Country Link
JP (1) JP4415438B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015075289A (en) * 2013-10-09 2015-04-20 日清食品ホールディングス株式会社 Drain generation and recovery apparatus and drain generation and recovery method

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2015075289A (en) * 2013-10-09 2015-04-20 日清食品ホールディングス株式会社 Drain generation and recovery apparatus and drain generation and recovery method

Also Published As

Publication number Publication date
JP4415438B2 (en) 2010-02-17

Similar Documents

Publication Publication Date Title
CN101952657B (en) Hybrid separator
KR20010014388A (en) Waste heat steam generator
US7842113B2 (en) Extended water level range steam/water conical cyclone separator
JP4848333B2 (en) Moisture separator heater
US3751886A (en) Vertical steam drum
KR20130143721A (en) Method and configuration to reduce fatigue in steam drums
US2763245A (en) Drum internal for low head boiler
CN101120207A (en) Continuous steam generator
KR20010052698A (en) Fossil fuel fired steam generator
JP2001187307A (en) Horizontal steam separator for steam drum
KR100685074B1 (en) Fossil fuel fired continuous-flow steam generator
US2402154A (en) Fluid separator
JPH09137905A (en) Steam separator
JP2007298245A (en) Economizer and exhaust heat recovery boiler provided therewith
JP2008144716A (en) Moisture separator
JPH10332105A (en) Horizontal type steam separator for steam drum
FI91558C (en) Pulse Combustion Boiler
RU2151341C1 (en) Deaerator
JPS5840081B2 (en) Blowdown equipment for steam generators
CN220892210U (en) Steam-water separation device in high-efficiency boiler and boiler thereof
CN110207086B (en) Circulation condensing boiler
KR880000051B1 (en) Boiler
KR200243138Y1 (en) Deaerator for water heating device of generating plant
KR840001508Y1 (en) Sheu and tube moisture separator reheater with outlet orificing
CN111780082A (en) Steam generator system

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20061025

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20091104

A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20091117

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20121204

Year of fee payment: 3

LAPS Cancellation because of no payment of annual fees