JP2008298309A - Steam separator - Google Patents

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JP2008298309A
JP2008298309A JP2007141666A JP2007141666A JP2008298309A JP 2008298309 A JP2008298309 A JP 2008298309A JP 2007141666 A JP2007141666 A JP 2007141666A JP 2007141666 A JP2007141666 A JP 2007141666A JP 2008298309 A JP2008298309 A JP 2008298309A
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steam
water
separator
pipe
steam separator
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Hiroshi Takashima
博史 高島
Kengo Shigetaka
健吾 重高
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SAMSON CO Ltd
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SAMSON CO Ltd
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a steam separator capable of keeping high separating capacity of boiled water. <P>SOLUTION: In this steam separator 7 for a boiler with a vertically long cylindrical barrel 4 portion, having a steam taking-out pipe 1 connected with an upper portion of the steam separator 7 and a return water pipe 2 connected with a bottom portion of the steam separator 7, and circulating the gas-liquid two-phase flow composed of the steam and the boiled water inside of the steam separator 7, so that the steam and the boiler water are separated by action of centrifugal force, a collection space 5 having a diameter smaller than an inner diameter of the steam separator barrel 4 portion and larger than an inner diameter of the water return pipe 2 is defined at a lower portion in the steam separator, and the return water pipe 2 is connected with a lower portion of the collection space 5. Further the collection space 5 has the shape of which cross-section is reduced downward. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、遠心作用によって蒸気と缶水を分離するボイラ用の気水分離器に関するものである。   The present invention relates to a steam / water separator for a boiler that separates steam and can water by centrifugal action.

一般に水を加熱して蒸気を発生する蒸気ボイラでは、沸騰した缶水が蒸気とともに取り出され、蒸気質が低下するということを防ぐために、蒸気と缶水を分離する気水分離器を設ける。気水分離器には、縦型円筒形の胴内部で内壁面に沿って気液2相流を旋回させ、遠心力の作用によって蒸気と缶水を分離する遠心分離式の気水分離器が広く使用されている。遠心式気水分離器は、気水分離器胴の接線方向に蒸気連絡管を接続しておき、気水分離器内に流入した気液2相流を気水分離器内で旋回させると、比重の重い缶水は遠心力で分離されて胴内壁にそって旋回しながら落下し、比重の軽い蒸気は胴の上方部に集合するために、蒸気と缶水を分離することができる。気水分離器で分離した蒸気は、気水分離器の上部に接続している蒸気取り出し管を通して取り出し、気水分離器で分離した缶水は、気水分離器の底部に接続している還水管を通してボイラの缶体下部へ戻される。   In general, in a steam boiler that generates steam by heating water, a steam / water separator for separating steam and can water is provided in order to prevent boiling can water from being taken out together with the steam and lowering the steam quality. The steam-water separator has a centrifugal-type steam-water separator that swirls a gas-liquid two-phase flow along the inner wall surface inside a vertical cylindrical body and separates steam and can water by the action of centrifugal force. Widely used. The centrifugal steam-water separator has a steam communication pipe connected in the tangential direction of the steam-water separator body, and when the gas-liquid two-phase flow flowing into the steam-water separator is swirled in the steam-water separator, The can water having a high specific gravity is separated by centrifugal force and falls while swirling along the inner wall of the cylinder, and the steam having a low specific gravity collects in the upper part of the cylinder, so that the steam and the can water can be separated. The steam separated by the steam separator is taken out through a steam outlet pipe connected to the top of the steam separator, and the can water separated by the steam separator is returned to the bottom of the steam separator. It returns to the bottom of the boiler body through the water pipe.

ボイラでは、運転条件によって気水分離器内に流入する缶水量が変化する。気水分離器へ入る缶水量が多くなり、気水分離器内から還水管への缶水排出が間に合わなくなると、気水分離器内の下部にたまる缶水の水量が多くなり、水位も高くなる。気水分離器内での水位が高くなると、蒸気と缶水を分離するための空間容積が小さくなるため、分離能力が低下することになる。缶水の分離能力が低下すると、缶水が蒸気とともに取り出され、蒸気の質(乾き度)が低下するという問題が発生することになる。
特開2002−48303号公報
In the boiler, the amount of canned water flowing into the steam separator varies depending on the operating conditions. If the amount of canned water entering the steam separator becomes large and the canned water discharge from the steam separator to the return pipe cannot be made in time, the amount of canned water that accumulates in the lower part of the steam separator increases and the water level increases. Become. When the water level in the steam / water separator becomes high, the space capacity for separating the steam and the can water becomes small, so that the separation ability is lowered. If the separation capacity of can water is reduced, the problem is that the can water is taken out together with the steam and the quality (dryness) of the steam is lowered.
JP 2002-48303 A

本発明が解決しようとする課題は、缶水の分離能力を高く維持することのできる気水分離器を提供することにある。   The problem to be solved by the present invention is to provide a steam separator capable of maintaining a high separation capacity of can water.

請求項1に記載の発明は、縦長円筒状の胴部を持った気水分離器であって、気水分離器の上部に接続した蒸気取り出し管、気水分離器の底部に接続した還水管を持ち、気水分離器の内部で蒸気と缶水からなる気液2相流を旋回させ、遠心力の作用によって蒸気と缶水に分離するボイラ用の気水分離器において、気水分離器内の下部に、気水分離器胴部の内径よりは小さく、還水管の内径よりは大きな径を持った集合空間を設け、集合空間の下部に前記還水管を接続するようにしたことを特徴とする。   The invention according to claim 1 is a steam / water separator having a vertically long cylindrical body, a steam take-out pipe connected to the top of the steam / water separator, and a return water pipe connected to the bottom of the steam / water separator. In a steam / water separator for a boiler, the steam / water two-phase flow consisting of steam and can water is swirled inside the steam / water separator and separated into steam and can water by the action of centrifugal force. In the lower part of the inside, a collecting space having a diameter smaller than the inner diameter of the steam-water separator body and larger than the inner diameter of the returning water pipe is provided, and the returning water pipe is connected to the lower part of the collecting space. And

請求項2に記載の発明は、前記の気水分離器において、前記集合空間は下方へ向けて断面積を縮小していく形状としているものであることを特徴とする。   The invention according to claim 2 is characterized in that, in the steam-water separator, the collective space has a shape in which a cross-sectional area is reduced downward.

気水分離器から還水管へ向かって、断面積を段階的に縮小していくと、缶水による旋回流は徐々に旋回径を小さくして中心軸方向へ集合していくため、気水分離器から還水管へ缶水が抜ける際に発生する圧力損失は小さくなる。気水分離器底部での圧力損失が小さくなると、気水分離器底部から還水管へ抜ける缶水の流れがスムーズとなり、気水分離器内で滞留する缶水量が少なくなるため、気水分離器での缶水分離能力を高く保つことができる。気水分離の能力が高まることで気水分離器をコンパクト化することができ、同容積のものであれば気水分離器から取り出される蒸気の乾き度を高めることができる。   When the cross-sectional area is gradually reduced from the steam separator to the return water pipe, the swirling flow from the can water gradually gathers in the direction of the central axis with the swirling diameter gradually reduced. The pressure loss that occurs when the can water is drained from the vessel to the return pipe is reduced. When the pressure loss at the bottom of the steam / water separator is reduced, the flow of canned water flowing from the bottom of the steam / water separator to the return water pipe becomes smooth, and the amount of canned water remaining in the steam / water separator is reduced. Can keep the water separation capacity high. The steam / water separator can be made compact by increasing the steam / water separation capability, and if it has the same volume, the dryness of the steam taken out from the steam / water separator can be increased.

本発明の一実施例を図面を用いて説明する。図1は本発明を実施しているボイラの概要図、図2は本発明を実施している気水分離器における缶水旋回流の説明図、図3は従来の気水分離器における缶水旋回流の説明図である。   An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a schematic diagram of a boiler embodying the present invention, FIG. 2 is an explanatory diagram of a swirling water flow in a steam separator implementing the present invention, and FIG. 3 is a can water in a conventional steam separator. It is explanatory drawing of a swirl flow.

ボイラは蒸気発生部6で缶水を加熱することで蒸気を発生する。蒸気発生部6から取り出す蒸気には、沸騰によって持ち上がる缶水を含んでいるため、蒸気から缶水を分離する気水分離器7を設ける。気水分離器7は缶水を含んだ蒸気を内部で旋回させ、遠心力を利用して蒸気と缶水を分離するものであり、分離した蒸気は気水分離器の上部から取り出して蒸気使用箇所へ送り、缶水は気水分離器の下部から取り出して蒸気発生部6の下部へ戻すようにしている。   The boiler generates steam by heating the can water in the steam generating section 6. Since the steam taken out from the steam generation unit 6 contains canned water that is lifted by boiling, a steam separator 7 is provided for separating the canned water from the steam. The steam separator 7 swirls steam containing can water inside and separates steam and can water using centrifugal force. The separated steam is taken out from the top of the steam separator and used as steam. The can water is taken out from the lower part of the steam separator and returned to the lower part of the steam generating unit 6.

気水分離器7は、上下を鏡板でふさいでいる縦型円筒形の胴4を持った容器であり、上部に蒸気取り出し管1、下部に還水管2、側部に蒸気連絡管3をそれぞれ接続する。蒸気取り出し管1と還水管2は、胴4と同心になるように接続する。蒸気連絡管3は、胴4内に蒸気を導入したときに蒸気流が胴の内壁に沿って旋回するように、胴部壁面の接線方向に接続する。   The steam / water separator 7 is a container having a vertical cylindrical barrel 4 whose upper and lower sides are covered with end panels, each having a steam extraction pipe 1 at the top, a return water pipe 2 at the bottom, and a steam communication pipe 3 at the side. Connecting. The steam extraction pipe 1 and the return water pipe 2 are connected so as to be concentric with the trunk 4. The steam communication pipe 3 is connected in the tangential direction of the body wall surface so that the steam flow swirls along the inner wall of the body when the steam is introduced into the body 4.

気水分離器の下部には、気水分離器胴部の内径よりは小さく、還水管2の内径よりは大きな径を持った集合空間5を設けておく。集合空間5も胴4及び還水管2と同心の円筒形としておき、還水管2は集合空間5の下部に接続する。集合空間5は、気水分離器内径と還水管内径の中間的なものとし、気水分離器断面積>集合空間断面積>還水管断面積となるように、流路断面積が段階的に小さくなっていくようにしておく。また、集合空間5でも気水分離器につながっている上部から還水管につながっている下部にかけて、徐々に流路断面積を小さくなるように傾斜を設けた形状とした方がより好ましい。集合空間5の傾斜は、断面を直線とした形状で径を縮小していくものであってもよく、断面を曲線とした形状で径を縮小していくものであってもよい。   A collecting space 5 having a diameter smaller than the inner diameter of the steam-water separator body and larger than the inner diameter of the return water pipe 2 is provided below the steam-water separator. The collective space 5 is also concentric with the trunk 4 and the return water pipe 2, and the return water pipe 2 is connected to the lower part of the collective space 5. The collective space 5 is intermediate between the inner diameter of the steam-water separator and the inner diameter of the return water pipe, and the cross-sectional area of the flow path is stepwise so that the cross-sectional area of the steam-water separator> the cross-sectional area of the gather space> the cross-sectional area of the return water pipe Keep it getting smaller. Further, it is more preferable that the collecting space 5 has an inclined shape so that the cross-sectional area of the flow path gradually decreases from the upper part connected to the steam separator to the lower part connected to the return water pipe. The inclination of the collective space 5 may be one in which the diameter is reduced with a shape having a straight section, or may be one in which the diameter is reduced with a shape having a curved section.

蒸気連絡管3は、蒸気発生部6と気水分離器7を接続したものであり、蒸気発生部6で発生した蒸気を気水分離器7内へ導入する。蒸気発生部6で缶水を加熱して蒸気を発生する際には、蒸気の発生と同時に缶水の沸き上がりが発生する。そのため、蒸気連絡管3内の蒸気には多くの缶水が含まれていることになる。特にボイラ内の圧力が低い状態の時には、沸き上がりが大きくなるために気水分離器内へ入る缶水量も多くなる。   The steam communication pipe 3 connects the steam generator 6 and the steam / water separator 7, and introduces steam generated by the steam generator 6 into the steam / water separator 7. When the steam is generated by heating the can water by the steam generating unit 6, the boiling of the can water is generated simultaneously with the generation of the steam. For this reason, the steam in the steam communication pipe 3 contains a large amount of can water. In particular, when the pressure in the boiler is low, the amount of water that enters the steam separator increases because boiling increases.

蒸気と缶水からなる気液2相流を気水分離器7の胴4内へ導入すると、気液2相流は胴内壁面に沿って旋回する。2相流を旋回させると、液体である缶水は単位容積当たりの重量が重いため、遠心力の作用によって胴の内壁面に沿って旋回し続け、重力の作用によって下方へ落ちていくらせん状の流れとなる。しかし、気体である蒸気は単位容積当たりの重量は軽く、遠心力や重力の影響をほとんど受けないため、最初は胴の内壁面に沿って流れていても徐々に気水分離器7の中央部に集まり、気水分離器7の上部に接続している蒸気取り出し管1を通って出ていくことになる。   When a gas-liquid two-phase flow composed of steam and can water is introduced into the shell 4 of the steam-water separator 7, the gas-liquid two-phase flow swirls along the inner wall surface. When the two-phase flow is swirled, the liquid canned water has a heavy weight per unit volume, so it keeps swirling along the inner wall surface of the trunk by the action of centrifugal force and falls downward by the action of gravity. It becomes the flow of. However, since the vapor, which is a gas, is light in weight per unit volume and hardly affected by centrifugal force or gravity, even if it initially flows along the inner wall surface of the trunk, the central portion of the steam separator 7 is gradually And go out through the steam extraction pipe 1 connected to the upper part of the steam separator 7.

胴内でらせん状の流れとなった缶水は、重力の影響を受けて下方に向かい、集合空間5内へ入る。胴4の内壁面に沿って旋回していた缶水は、集合空間5の内壁面に沿って旋回することになり、集合空間5は、胴4の内径よりも少し小さな径を持った空間であるため、缶水の旋回流は気水分離器7の中心軸方向へ集まっていくことになる。   The can water that has a spiral flow in the trunk is moved downward under the influence of gravity and enters the assembly space 5. The can water swirling along the inner wall surface of the trunk 4 swirls along the inner wall surface of the collective space 5, and the collective space 5 is a space having a slightly smaller diameter than the inner diameter of the trunk 4. Therefore, the swirl flow of the can water gathers in the direction of the central axis of the steam separator 7.

内径の大きな気水分離器7と内径の小さな還水管2を直接接続しており、流路面積が急激に小さくなる従来の気水分離器では、缶水が還水管2に入る際に発生する圧力損失が大きくなり、気水分離器7から還水管2への缶水の排出が悪くなっていた。そこで、気水分離器の胴部と還水管の中間的な径を持った集合空間5を設け、集合空間5を通じて還水管2に入るようにする。このようにすると気水分離器から還水管へ向かって、断面積は段階的に縮小していくことになり、缶水による旋回流は徐々に旋回径を小さくして中心軸方向へ集合していく。缶水の旋回流を段階的に中心軸方向へ集合するようにすると、還水管接続部での圧力損失は大幅に低減し、気水分離器から還水管へ缶水が抜けやすくなる。気水分離器の下部に滞留する缶水の量が少なくなると、気水分離器内での分離空間容積を大きく確保できるため、缶水の分離能力が向上するという作用が得られる。このように気水分離器内にある缶水の水位を低く保つことができれば、気水分離器をコンパクト化することができるようになり、同容積の気水分離器であれば蒸気の乾き度を0.5%程度アップできる結果が得られた。   In the conventional steam / water separator in which the steam / water separator 7 having a large inner diameter and the return water pipe 2 having a small inner diameter are directly connected and the flow path area is drastically reduced, the can water is generated when entering the return water pipe 2. Pressure loss increased, and the discharge of canned water from the steam separator 7 to the return water pipe 2 was worsened. Therefore, a collective space 5 having an intermediate diameter between the body portion of the steam separator and the return water pipe is provided so as to enter the return water pipe 2 through the collective space 5. In this way, the cross-sectional area gradually decreases from the steam separator to the return water pipe, and the swirling flow due to the can water gradually decreases the swirling diameter and gathers in the direction of the central axis. Go. If the swirling flow of the can water is gathered stepwise in the direction of the central axis, the pressure loss at the return water pipe connecting portion is greatly reduced, and the can water easily escapes from the steam separator to the return water pipe. If the amount of canned water staying in the lower part of the steam separator is reduced, a large separation space volume in the steam separator can be ensured, so that the ability to separate canned water is improved. Thus, if the water level of the can water in the steam separator can be kept low, the steam separator can be made compact. If the steam separator has the same volume, the dryness of the steam As a result, an increase of about 0.5% was obtained.

本発明を実施しているボイラの概要図Outline diagram of boiler implementing the present invention 本発明を実施している気水分離器における缶水旋回流の説明図Explanatory drawing of can water swirl flow in the steam separator which is carrying out the present invention 従来の気水分離器における缶水旋回流の説明図Explanatory drawing of canned water swirl flow in conventional steam separator

符号の説明Explanation of symbols

1 蒸気取り出し管
2 還水管
3 蒸気連絡管
4 胴
5 集合空間
6 蒸気発生部
7 気水分離器
DESCRIPTION OF SYMBOLS 1 Steam extraction pipe 2 Return water pipe 3 Steam communication pipe 4 Body 5 Collecting space 6 Steam generation part 7 Steam-water separator

Claims (2)

縦長円筒状の胴部を持った気水分離器であって、気水分離器の上部に接続した蒸気取り出し管、気水分離器の底部に接続した還水管を持ち、気水分離器の内部で蒸気と缶水からなる気液2相流を旋回させ、遠心力の作用によって蒸気と缶水に分離するボイラ用の気水分離器において、気水分離器内の下部に、気水分離器胴部の内径よりは小さく、還水管の内径よりは大きな径を持った集合空間を設け、集合空間の下部に前記還水管を接続するようにしたことを特徴とする気水分離器。 A steam / water separator having a vertically long cylindrical body with a steam take-out pipe connected to the top of the steam / water separator and a return water pipe connected to the bottom of the steam / water separator. In a steam / water separator for boilers that swirls a gas / liquid two-phase flow consisting of steam and can water and separates it into steam and can water by the action of centrifugal force, a steam / water separator is installed at the bottom of the steam / water separator. An air / water separator, characterized in that a collecting space having a diameter smaller than the inner diameter of the body portion and larger than the inner diameter of the return water pipe is provided, and the return water pipe is connected to a lower portion of the collecting space. 請求項1に記載の気水分離器において、前記集合空間は下方へ向けて断面積を縮小していく形状としているものであることを特徴とする気水分離器。   The steam-water separator according to claim 1, wherein the collective space has a shape in which a cross-sectional area is reduced downward.
JP2007141666A 2007-05-29 2007-05-29 Steam separator Pending JP2008298309A (en)

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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103216817A (en) * 2013-01-30 2013-07-24 珠海新市节能环保科技有限公司 Steam-water isolator for boiler
JP2014031891A (en) * 2012-08-01 2014-02-20 Samson Co Ltd Multitubular through flow boiler
EP2881660A1 (en) * 2013-12-09 2015-06-10 Gorenje d.d. Centrifugal separator of fluid and vapour with a household apparatus

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002028421A (en) * 2000-07-18 2002-01-29 Samson Co Ltd Centrifugal gas/liquid separator using separation by baffle plate in combination
JP2003230850A (en) * 2002-02-08 2003-08-19 Aisan Ind Co Ltd Trapping device
JP2004105822A (en) * 2002-09-17 2004-04-08 Sango Co Ltd Gas-liquid separator

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002028421A (en) * 2000-07-18 2002-01-29 Samson Co Ltd Centrifugal gas/liquid separator using separation by baffle plate in combination
JP2003230850A (en) * 2002-02-08 2003-08-19 Aisan Ind Co Ltd Trapping device
JP2004105822A (en) * 2002-09-17 2004-04-08 Sango Co Ltd Gas-liquid separator

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014031891A (en) * 2012-08-01 2014-02-20 Samson Co Ltd Multitubular through flow boiler
CN103216817A (en) * 2013-01-30 2013-07-24 珠海新市节能环保科技有限公司 Steam-water isolator for boiler
EP2881660A1 (en) * 2013-12-09 2015-06-10 Gorenje d.d. Centrifugal separator of fluid and vapour with a household apparatus

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