JPH0125638Y2 - - Google Patents
Info
- Publication number
- JPH0125638Y2 JPH0125638Y2 JP1984032580U JP3258084U JPH0125638Y2 JP H0125638 Y2 JPH0125638 Y2 JP H0125638Y2 JP 1984032580 U JP1984032580 U JP 1984032580U JP 3258084 U JP3258084 U JP 3258084U JP H0125638 Y2 JPH0125638 Y2 JP H0125638Y2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- gas
- drain
- buffer plate
- steam
- 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
- 239000007788 liquid Substances 0.000 claims description 33
- 239000012530 fluid Substances 0.000 claims description 15
- 238000007599 discharging Methods 0.000 claims description 4
- 238000009434 installation Methods 0.000 claims 1
- 238000000926 separation method Methods 0.000 description 17
- 230000000694 effects Effects 0.000 description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000010586 diagram Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は気液分離装置に係り、特に火力プラン
トのブローダウンタンクの如き気液混合流体を旋
回力により蒸気とドレンに分離して得たドレンの
旋回流動を拘束するに好適な気液分離装置に関す
る。[Detailed description of the invention] [Field of industrial application] The present invention relates to a gas-liquid separation device, in particular a gas-liquid separation device that separates a gas-liquid mixed fluid such as a blowdown tank of a thermal power plant into steam and condensate using swirling force. The present invention relates to a gas-liquid separation device suitable for restricting swirling flow of drain.
従来、火力プラント等に設置された圧力容器と
して、気液混合流体を導入し、気液に分離させる
タンクが知られている。例えば、火力プラントに
おけるブローダウンタンクは、第1〜2図に示す
ように、タンク胴1の側壁にその接線方向に沿わ
せて入口管2を取付けし、飽和蒸気とドレンから
なる気液混合流体を旋回導入させるようにしてい
る。そしてタンク内で、旋回力によつて蒸気とド
レンに分離させ、分離蒸気はタンク上部鏡3に取
付けた蒸気出口管4により、また分離ドレンはタ
ンク下部鏡5に取付けたドレン排出管6により、
それぞれタンク外に排出される。この場合、蒸気
出口管4からは蒸気のみを、ドレン排出管6から
はドレンのみを排出させる必要があり、このため
特にドレン排出管6はL字状に曲げて吸込口7を
タンク下部鏡板5の底面に臨ませるとともにドレ
ン水位が排出管6の中心となるようにして、蒸気
が混入排出されないようにしている。
BACKGROUND ART Conventionally, as a pressure vessel installed in a thermal power plant or the like, a tank is known that introduces a gas-liquid mixed fluid and separates it into gas and liquid. For example, in a blowdown tank in a thermal power plant, as shown in Figs. 1 and 2, an inlet pipe 2 is attached to the side wall of the tank body 1 along the tangential direction, and a gas-liquid mixture consisting of saturated steam and condensate is We are trying to introduce a rotation. In the tank, steam and drain are separated by swirling force, and the separated steam is passed through the steam outlet pipe 4 attached to the tank upper mirror 3, and the separated drain is passed through the drain discharge pipe 6 attached to the tank lower mirror 5.
Each is discharged outside the tank. In this case, it is necessary to discharge only steam from the steam outlet pipe 4 and only drain from the drain discharge pipe 6. For this reason, the drain discharge pipe 6 is particularly bent into an L shape and the suction port 7 is connected to the tank lower end plate 5. The drain water level is placed at the center of the discharge pipe 6 to prevent steam from being mixed in and discharged.
しかしながら、従来のタンク構造では、気液混
合流体が旋回導入されることによつて、内部に残
留している停滞ドレンおよび分離ドレンが旋回力
により持ち上げられ、第3図網目部Aで示すよう
なドレン分布となる。そして、その残部空間Bが
蒸気域となつてしまう。この結果、ドレン域Aが
入口管2の位置まで達するような事態の発生によ
り、流入流体とドレン域と混合してウオータハン
マ現像を起こし、タンクの破損原因となつてい
た。更に、蒸気域Bに排出管6の吸入口7が露呈
してしまい、ドレン排出管6から蒸気も排出さ
れ、気液分離機能が損われ、ドレン水位も一定に
保てない等の不都合を生じてしまうのである。 However, in the conventional tank structure, when the gas-liquid mixed fluid is introduced in a swirling manner, the stagnant drain and separated drain remaining inside are lifted by the swirling force, and as shown in the mesh section A in FIG. This results in drain distribution. Then, the remaining space B becomes a steam region. As a result, a situation occurs in which the drain region A reaches the position of the inlet pipe 2, and the inflow fluid mixes with the drain region, causing water hammer development, which causes damage to the tank. Furthermore, the suction port 7 of the discharge pipe 6 is exposed in the steam region B, and steam is also discharged from the drain discharge pipe 6, causing problems such as impairing the gas-liquid separation function and making it impossible to maintain a constant drain water level. That's what happens.
そこで、タンクの内部にバツフア板を設け、タ
ンク上部の旋回流とタンク下部の停滞ドレンの混
合を防止して、上述の不都合を解消するようにし
たものが、実公昭58−11364号公報および実開昭
55−28434号公報に記載されている。 Therefore, a buffer plate was installed inside the tank to prevent the swirling flow at the top of the tank from mixing with the stagnant drain at the bottom of the tank, thereby solving the above-mentioned problems. Kaisho
It is described in Publication No. 55-28434.
しかしながら、上記両公報の技術では、バツフ
ア板が平板状であるため、旋回流はこのバツフア
板上を整流となつて流れてしまい、良好な気液分
離能力を得るという点に関しては満足できるもの
ではない。
However, in the techniques disclosed in both of the above-mentioned publications, since the buffer plate is flat, the swirling flow flows on the buffer plate as a rectification, and is not satisfactory in terms of obtaining good gas-liquid separation ability. do not have.
本考案の目的は、旋回流による停滞ドレンの巻
き上げを防止しつつ、気液分離効率を向上させる
ことができる気液分離装置を提供することであ
る。 An object of the present invention is to provide a gas-liquid separation device that can improve gas-liquid separation efficiency while preventing stagnant drain from being rolled up due to swirling flow.
上記目的を達成するために、本考案は、気液混
合流体をタンク内に接線方向から導入する入口管
をタンク側壁に設けるとともに、分離蒸気を排出
する蒸気出口管を前記タンクの上部に、分離ドレ
ンを排出するドレン排出管を前記タンクの下部に
それぞれ配設した気液分離装置において、複数の
透孔を有するバツフア板を前記タンク内部に取付
けるとともに、該バツフア板の取付位置を前記入
口管とドレン排出管との間に設定したことを特徴
とする。
In order to achieve the above object, the present invention provides an inlet pipe on the side wall of the tank for introducing the gas-liquid mixed fluid into the tank from a tangential direction, and a vapor outlet pipe for discharging the separated vapor at the upper part of the tank. In a gas-liquid separation device in which drain discharge pipes for discharging condensate are arranged at the bottom of the tank, a buffer plate having a plurality of through holes is installed inside the tank, and the mounting position of the buffer plate is aligned with the inlet pipe. It is characterized by being set between the drain discharge pipe.
上記構成によれば、入口管からタンク内に気液
混合流体が導入されると、気液混合流体はタンク
内で旋回流となり、この旋回流はバツフア板の透
孔に衝突する。その結果、旋回流の旋回方向の速
度成分が極めて小さくなり、もつて旋回流による
停滞ドレンの巻き上げが防止され、かつ旋回流に
よる気液分離に加え、衝突による気液分離効果が
あるため、最終的な気液分離効率を大幅に向上さ
せることが可能となる。
According to the above configuration, when the gas-liquid mixed fluid is introduced into the tank from the inlet pipe, the gas-liquid mixed fluid becomes a swirling flow within the tank, and this swirling flow collides with the through hole of the buffer plate. As a result, the velocity component of the swirling flow in the swirling direction becomes extremely small, which prevents the stagnant drain from being rolled up by the swirling flow.In addition to the gas-liquid separation effect due to the swirling flow, there is a gas-liquid separation effect due to collision, so that the final This makes it possible to significantly improve gas-liquid separation efficiency.
以下に本考案の一実施例を図面に従つて説明す
る。
An embodiment of the present invention will be described below with reference to the drawings.
第4〜第5図は本考案に係る気液分離装置を示
している。図示の如く、タンク胴11のやや上部
に従来と同様に複数の気液混合流体の入口管12
を取付け、同じく上部鏡13に蒸気出口管14、
下部鏡15にドレン排出管16を設け、排出管1
6の吸込口17を下部鏡15の底面に近接させて
いる。 4 and 5 show a gas-liquid separation device according to the present invention. As shown in the figure, a plurality of gas-liquid mixed fluid inlet pipes 12 are installed slightly above the tank body 11 as in the past.
Attach the steam outlet pipe 14 to the upper mirror 13 as well.
A drain discharge pipe 16 is provided on the lower mirror 15, and the drain pipe 1
The suction port 17 of No. 6 is located close to the bottom surface of the lower mirror 15.
ここで、当該実施例では、気液混合流体の入口
管12とドレン排出管16の間に位置し、ドレン
排出管16の直上位置に気液分離機能を有するバ
ツフア板18を取付けている。このバツフア板1
8は気液混合流体の旋回流室19と、下部のドレ
ン室20とに区画するようにタンク胴11を横断
して取付けられる円板体とされている。そして、
このバツフア板18には複数の透孔21を穿設し
ており、上下の室19,20を通流可能ならしめ
ている。 In this embodiment, a buffer plate 18 having a gas-liquid separation function is installed between the gas-liquid mixed fluid inlet pipe 12 and the drain discharge pipe 16, and directly above the drain discharge pipe 16. This buffer board 1
Reference numeral 8 is a disc body attached across the tank body 11 so as to divide it into a swirling flow chamber 19 for gas-liquid mixed fluid and a drain chamber 20 at the lower part. and,
This buffer plate 18 is provided with a plurality of through holes 21 to allow the upper and lower chambers 19, 20 to pass through.
このような構成に係るタンク内停滞ドレンの巻
上げ防止装置の作用は次のようになる。入口管1
2から流入した流体は、タンク胴11の円周方向
に旋回しながら、旋回力によつて気液に分離され
るが、旋回流はバツフア板18の存在によつて、
下部のドレン室20へは作用せず、透孔21を通
じて整流され、停滞ドレンに対して旋回力を作用
させることがない。したがつて、気液混合流体の
旋回力によつては停滞ドレンを巻上げてしまうこ
とがなく、またこの巻上げが阻止されるのでドレ
ン排出管16の吸込口17が蒸気域に露呈される
ことも防止される。更に、気液混合流体の旋回流
はバツフア板18と直接接触するが、バツフア板
18が多孔板から形成されているために、透孔2
1に衝突することによつて当該透孔21での気液
分離作用が発揮され、分離機能を助長する効果を
奏する。 The function of the device for preventing the stagnant drain in the tank from rolling up, which has such a configuration, is as follows. Inlet pipe 1
The fluid flowing in from 2 is separated into gas and liquid by the swirling force while swirling in the circumferential direction of the tank body 11.
It does not act on the lower drain chamber 20, but is rectified through the through hole 21, and no turning force is applied to the stagnant drain. Therefore, the swirling force of the gas-liquid mixed fluid does not cause the stagnant drain to be rolled up, and since this lifting is prevented, the suction port 17 of the drain discharge pipe 16 is not exposed to the steam region. Prevented. Furthermore, the swirling flow of the gas-liquid mixed fluid comes into direct contact with the buffer plate 18, but since the buffer plate 18 is formed from a perforated plate, the through holes 2
By colliding with 1, the gas-liquid separation effect is exerted in the through hole 21, which has the effect of promoting the separation function.
以上説明したように、本考案によれば、複数の
透孔を有するバツフア板をタンク内に設けたの
で、停滞ドレンの巻き上げを防止することができ
るとともに、気液分離効率を大幅に向上させるこ
とが可能となる。
As explained above, according to the present invention, since a buffer plate having a plurality of through holes is provided in the tank, it is possible to prevent stagnant drain from being rolled up, and to significantly improve gas-liquid separation efficiency. becomes possible.
第1図は従来のブローダウンタンクの平面図、
第2図は同縦断面図、第3図はドレン旋回状態を
示す説明図、第4図は本考案に係る気液分離装置
の縦断面図、第5図は第4図の−線断面図で
ある。
11…タンク胴、12…気液混合流体入口管、
14…蒸気出口管、16…ドレン排出管、17…
吸込口、18…バツフア板、21…透孔。
Figure 1 is a plan view of a conventional blowdown tank.
FIG. 2 is a longitudinal sectional view of the same, FIG. 3 is an explanatory diagram showing the drain rotation state, FIG. 4 is a longitudinal sectional view of the gas-liquid separation device according to the present invention, and FIG. 5 is a sectional view taken along the line -- of FIG. 4. It is. 11... Tank body, 12... Gas-liquid mixed fluid inlet pipe,
14... Steam outlet pipe, 16... Drain discharge pipe, 17...
Suction port, 18...Buffer plate, 21...Through hole.
Claims (1)
る入口管をタンク側壁に設けるとともに、分離蒸
気を排出する蒸気出口管を前記タンクの上部に、
分離ドレンを排出するドレン排出管を前記タンク
の下部にそれぞれ配設した気液分離装置におい
て、 複数の透孔を有するバツフア板を前記タンク内
部に取付けるとともに、該バツフア板の取付位置
を前記入口管とドレン排出管との間に設定したこ
とを特徴とする気液分離装置。[Claims for Utility Model Registration] An inlet pipe for introducing the gas-liquid mixed fluid into the tank from a tangential direction is provided on the side wall of the tank, and a steam outlet pipe for discharging the separated steam is provided at the top of the tank,
In a gas-liquid separator in which drain discharge pipes for discharging separated drain are arranged at the lower part of the tank, a buffer plate having a plurality of through holes is installed inside the tank, and the installation position of the buffer plate is set to the inlet pipe. and a drain discharge pipe.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3258084U JPS60144950U (en) | 1984-03-07 | 1984-03-07 | Gas-liquid separation equipment |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3258084U JPS60144950U (en) | 1984-03-07 | 1984-03-07 | Gas-liquid separation equipment |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60144950U JPS60144950U (en) | 1985-09-26 |
JPH0125638Y2 true JPH0125638Y2 (en) | 1989-08-01 |
Family
ID=30534223
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3258084U Granted JPS60144950U (en) | 1984-03-07 | 1984-03-07 | Gas-liquid separation equipment |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60144950U (en) |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP4684398B2 (en) * | 2000-08-11 | 2011-05-18 | 株式会社テイエルブイ | Gas-liquid separator |
JP2002058932A (en) * | 2000-08-11 | 2002-02-26 | Tlv Co Ltd | Gas-liquid separator |
JP5267163B2 (en) * | 2008-12-04 | 2013-08-21 | 三浦工業株式会社 | Gas-solid liquid separator |
JP2010155229A (en) * | 2008-12-04 | 2010-07-15 | Miura Co Ltd | Gas-solid-liquid separator |
JP7388822B2 (en) * | 2019-03-27 | 2023-11-29 | 三菱重工サーマルシステムズ株式会社 | Oil separator and compressor |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5232177A (en) * | 1975-09-08 | 1977-03-11 | Hitachi Ltd | Gas-liquid separator |
JPS5528434B2 (en) * | 1974-01-29 | 1980-07-28 | ||
JPS5811364U (en) * | 1981-07-14 | 1983-01-25 | 柴山 繁 | Answering machine |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5528434U (en) * | 1978-08-11 | 1980-02-23 |
-
1984
- 1984-03-07 JP JP3258084U patent/JPS60144950U/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5528434B2 (en) * | 1974-01-29 | 1980-07-28 | ||
JPS5232177A (en) * | 1975-09-08 | 1977-03-11 | Hitachi Ltd | Gas-liquid separator |
JPS5811364U (en) * | 1981-07-14 | 1983-01-25 | 柴山 繁 | Answering machine |
Also Published As
Publication number | Publication date |
---|---|
JPS60144950U (en) | 1985-09-26 |
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