JP2003148702A - Steam attemper - Google Patents

Steam attemper

Info

Publication number
JP2003148702A
JP2003148702A JP2001349515A JP2001349515A JP2003148702A JP 2003148702 A JP2003148702 A JP 2003148702A JP 2001349515 A JP2001349515 A JP 2001349515A JP 2001349515 A JP2001349515 A JP 2001349515A JP 2003148702 A JP2003148702 A JP 2003148702A
Authority
JP
Japan
Prior art keywords
liquid
steam
reservoir
liquid reservoir
passage
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
JP2001349515A
Other languages
Japanese (ja)
Other versions
JP3836710B2 (en
Inventor
Kenichi Toda
賢一 戸田
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.)
TLV Co Ltd
Original Assignee
TLV Co Ltd
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 TLV Co Ltd filed Critical TLV Co Ltd
Priority to JP2001349515A priority Critical patent/JP3836710B2/en
Publication of JP2003148702A publication Critical patent/JP2003148702A/en
Application granted granted Critical
Publication of JP3836710B2 publication Critical patent/JP3836710B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To provide a steam attemper which has a simple mechanism and is inexpensive without using various kinds of sensors such as pressure sensors and flow rate sensors, control valves, and pumps for feeding coolant. SOLUTION: A liquid-vapor mixing and separating device 7 is connected with a steam pipe 1 in which an overheated steam flows. The first liquid reservoir 2 is connected at the bottom of the liquid-vapor mixing and separating device 7. The second liquid reservoir 3 is connected at the bottom of the first liquid reservoir 2. The reservoirs 2 and 3 are connected with a high-pressure liquid flow line 9. A connecting line 4 is connected with the bottom of the reservoir 3, and the upper edge of the connecting line 4 is connected with the inlet side of the mixing and separating device 7 of steam pipe 1. An in-line type heat exchanger 28 is installed in the connecting line 4. The overheated steam in the steam pipe 1 is cooled up to a predetermined temperature by a coolant fed to the steam pipe 1 from the first liquid reservoir 2 and the second liquid reservoir 3 through the connecting line 4.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】この発明は、飽和温度以上の
いわゆる過熱温度蒸気を、所定の温度例えば飽和温度ま
で減温することのできる蒸気減温装置に関する。 【0002】 【従来の技術】従来の蒸気減温装置としては例えば特開
昭62−141407号公報に示されているものが用い
られていた。これは、過熱蒸気配管に圧力調節弁と圧力
検出器と蒸気流量検出器と温度検出器、及び、過熱蒸気
中へ供給する水流量検出器をそれぞれ取り付けて、過熱
蒸気の圧力を検出して圧力調節弁を調節すると共に、過
熱蒸気の流量と温度を検出して水流量検出器から所定量
の水を過熱蒸気中へ供給することによって、過熱蒸気を
飽和温度の蒸気へ減温することができるものである。 【0003】 【発明が解決しようとする課題】上記従来の蒸気減温装
置では、圧力調節弁と、圧力や流量や温度等の各種検出
器及び検出器に対応した調節器が必要となり、減温装置
が高価で複雑な物となってしまう問題があった。 【0004】この実情に鑑み、本発明の主たる課題は、
各種の検出器や調節弁を用いることなく、過熱温度蒸気
を所定温度の蒸気へ減温することのできる安価でシンプ
ルな蒸気減温装置を得ることである。 【0005】 【課題を解決するための手段】上記の課題を解決するた
めに講じた本発明の手段は、蒸気通路を流下する過熱蒸
気に冷却流体を供給して、当該過熱蒸気を所定温度状態
の蒸気へ減温するものにおいて、液体を溜め置く第1の
液体溜容器を配置して、当該第1の液体溜容器の液体入
口を過熱蒸気の流下する蒸気通路と連通路で連通し、当
該第1の液体溜容器の液体出口を第2の液体溜容器と連
通路で連通して、当該第2の液体溜容器の液体出口に接
続通路を介して過熱蒸気の流下する蒸気通路と接続する
と共に、第1の液体溜容器と第2の液体溜容器に高圧流
体源と連通する高圧流体連通路を連通して、第1の液体
溜容器と高圧流体連通路の間に、第1の液体溜容器内へ
の高圧流体の流入と遮断を切り換える切換弁を取り付け
たものである。 【0006】 【発明の実施の形態】切換弁によって第1の液体溜容器
内への高圧流体が遮断されている時に、蒸気通路中の液
体が連通路と液体入口とを介して第1の液体溜容器内へ
流入する。第1の液体溜容器内へ流入して溜まった液体
は、切換弁によって高圧流体が第1の液体溜容器へ流入
されると連通路と液体出口とを介して第2の液体溜容器
内へ流入する。更に、第2の液体溜容器内へ流入した液
体は、高圧流体の流体圧力によって、接続通路と液体出
口とを介して蒸気通路へ供給されて過熱蒸気を減温す
る。 【0007】 【実施例】図1において、過熱蒸気の流下する蒸気通路
としての蒸気管1と、第1の液体溜容器2と第2の液体
溜容器3、及び、第2の液体溜容器3から蒸気管1中に
冷却液体を供給する接続通路4とで蒸気減温装置を構成
する。 【0008】蒸気管1にバルブ5と自動調節弁6と気液
の混合分離器7を順次取り付けて、管路8から所定温度
に減温された蒸気を、図示しない蒸気使用装置へ供給す
る。自動調節弁6は管路8から供給する蒸気の量又は圧
力又は温度を調節するものであり、気液の混合分離器7
は、蒸気管1中の過熱蒸気と接続通路4から供給される
冷却液体を混合して更に分離し、管路8へ液体が分離さ
れ所定温度まで減温された蒸気だけを供給する。 【0009】蒸気管1を分岐して高圧流体連通路9を連
通する。高圧流体連通路9にバルブ10を介して第1の
液体溜容器2の高圧流体入口11と接続すると共に、バ
ルブ12を介して第2の液体溜容器3の上部側方と接続
する。なお、図示はしていないが、高圧流体連通路9
に、その二次側の圧力を一定に維持する機能を有する減
圧弁を取り付けることによって、第1の液体溜容器2と
第2の液体溜容器3へ供給する高圧流体の圧力を一定に
保持することができる。 【0010】第1の液体溜容器2の液体入口13に、逆
止弁14と液体通路15を介して、気液の混合分離器7
の下端部と接続する。混合分離器7の下端部には蒸気ト
ラップ16と逆止弁17を接続する。蒸気トラップ16
は、気液の混合分離器7で分離された蒸気の凝縮水とし
ての復水や冷却液体だけを流下させ、蒸気は流下させる
ことがない自動弁の一種である。逆止弁17と14は、
蒸気トラップ16から液体入口13側への流体の通過を
許容し、反対側への流体の通過は許容しないものであ
る。 【0011】第1の液体溜容器2の上部の高圧流体入口
11の側方に、高圧流体出口18を設けて大気連通管1
9を接続する。第1の液体溜容器2の液体入口13の下
方には液体出口20を設けて、第2の液体溜容器3と連
通路21で連通する。連通路21には逆止弁22を取り
付ける。逆止弁22は、液体出口20から第2の液体溜
容器3側への流体の通過を許容し、反対側への通過は許
容しないものである。 【0012】第1の液体溜容器2は、液体入口13から
流入してきた復水等の液体が内部に溜まってその液位が
上昇すると内部の図示しないフロートを上昇させ、所定
位置に達するとスナップ移動して、高圧流体入口11に
取り付けた圧送弁を開弁すると共に、高圧流体出口18
に取り付けた排気弁を閉弁して、高圧流体連通路9から
高圧の蒸気を第1の液体溜容器2内部に供給し、溜まっ
ていた液体を液体出口20から逆止弁22と連通路21
を介して第2の液体溜容器3へ流下させるものである。 【0013】第1の液体溜容器2内の液体が第2の液体
溜容器3へ流下するに連れて、内部の図示しないフロー
トが降下して、所定の液位まで低下するとスナップ移動
して、高圧流体入口11の圧送弁を閉弁すると共に、高
圧流体出口18の排気弁が開弁して、第1の液体溜容器
2内の高圧蒸気が大気連通管19から外部に排出され、
再度、液体通路15から復水等の液体が第1の液体溜容
器2内へ流入してくるものである。 【0014】本実施例においては、高圧流体入口11に
取り付けた圧送弁と高圧流体出口18に取り付けた排気
弁とで、第1の液体溜容器2内への高圧流体の流入と遮
断を切り換える切換弁を構成する。 【0015】液体通路15の2つの逆止弁14,17の
間に、冷却液体補給管23を接続する。冷却液体補給管
23には自動弁24を取り付ける。冷却液体例えば冷却
水が不足した場合に、自動弁24から補給することがで
きるものである。 【0016】連通路21によって第1の液体溜容器2と
連通した第2の液体溜容器3は、密閉状のタンクで形成
して、上部側方に高圧流体連通路9を接続する。容器3
の上部には、容器3内の液位を検出する液位センサ25
を取り付ける。容器3の下部には接続通路4を接続す
る。 【0017】接続通路4には、自動弁26を介した余剰
液体排出管27を接続すると共に、インライン式の熱交
換器28を取り付ける。この熱交換器28は、エゼクタ
29と加熱又は冷却流体供給管30、及び、流体供給管
30に取り付けた自動調節弁31と逆止弁32とで構成
する。接続通路4の蒸気管1側に、接続通路4内の液体
温度を検出する温度センサ33を取り付ける。温度セン
サ33と自動調節弁31を図示しない温度コントローラ
を介して電気接続する。 【0018】温度センサ33で検出した冷却液体温度に
応じて、自動調節弁31の弁開度を調節することによっ
て、加熱又は冷却流体供給管30から、所定量の加熱又
は冷却流体を接続通路4内の液体に供給して、蒸気管1
内に供給する冷却液体温度を任意にコントロールするこ
とができる。接続通路4から蒸気管1内へ冷却液体を供
給する場合、図示はしていないが接続通路4の蒸気管1
内端部に、冷却液体を噴射するためのノズルを取り付け
ることが好ましい。 【0019】第2の液体溜容器3に取り付けた液位セン
サ25は、図示しないコントローラを介して自動弁2
4,26と電気接続する。液位センサ25の検出液位に
よって、自動弁24を開弁して冷却液体を補給したり、
あるいは、自動弁26を開弁して余剰冷却液体を系外へ
排除するものである。 【0020】蒸気管1内を初期立ち上げ時に蒸気が通過
すると冷却されて蒸気は復水となり、気液の混合分離器
7と蒸気トラップ16と逆止弁17,14を通って第1
の液体溜容器2内へ流入する。容器2内の液位が所定高
さに達すると、高圧流体入口11に取り付けた圧送弁が
開弁し、高圧流体出口18に取り付けた排気弁が閉弁す
ることによって、高圧流体連通路9から高圧蒸気が容器
2内へ供給され、第2の液体溜容器3内と同圧になるこ
とにより、容器2内の液体は容器3内へ水頭差によって
自然流下する。 【0021】第2の液体溜容器3内は絶えず高圧流体通
路9と連通しており、従って、容器3内の液体はその高
圧流体の圧力によって接続通路4から蒸気管1内へ圧送
され、蒸気管1内を流下する過熱蒸気中に注入される。
蒸気管1内へ注入された冷却液体は、気液の混合分離器
7で過熱蒸気と混合して過熱蒸気の温度を低下させる。
この場合、低下させる過熱蒸気の温度は、接続通路4か
ら供給する冷却液体の量とか温度を調節することによっ
て適宜制御することができる。 【0022】気液の混合分離器7で過熱蒸気と混合した
残余の冷却液体は、この混合分離器7で気液分離され、
下端部の蒸気トラップ16から第1の液体溜容器2内へ
流下する。一方、液体の分離された所定温度の蒸気は、
混合分離器7から管路8を通って蒸気使用箇所へと供給
される。 【0023】 【発明の効果】上記のように本発明によれば、第1の液
体溜容器と第2の液体溜容器とを介して連続的に冷却液
体を蒸気管へ供給することによって、蒸気管内の過熱蒸
気を任意の蒸気温度まで減温することができ、圧力や流
量等の各種検出器や、調節弁、あるいは、冷却液体を供
給するためのポンプ手段等を用いることなく、安価でシ
ンプルな蒸気減温装置とすることができる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a device for reducing the temperature of so-called superheated steam having a temperature higher than a saturation temperature to a predetermined temperature, for example, a saturation temperature. 2. Description of the Related Art As a conventional steam cooling device, for example, a device disclosed in Japanese Patent Application Laid-Open No. 62-141407 has been used. This is done by installing a pressure control valve, a pressure detector, a steam flow rate detector, a temperature detector, and a water flow rate detector to supply the superheated steam into the superheated steam pipe, and detecting the pressure of the superheated steam. By adjusting the control valve, detecting the flow rate and temperature of the superheated steam, and supplying a predetermined amount of water into the superheated steam from the water flow rate detector, the superheated steam can be reduced to the steam at the saturated temperature. Things. [0003] The above-mentioned conventional steam deheating apparatus requires a pressure control valve, various detectors for pressure, flow rate, temperature, etc. and a regulator corresponding to the detector. There is a problem that the device becomes expensive and complicated. [0004] In view of this situation, the main problems of the present invention are:
It is an object of the present invention to provide an inexpensive and simple steam deheater capable of reducing superheated steam to a predetermined temperature without using various detectors and control valves. Means for solving the above-mentioned problems According to the present invention, a cooling fluid is supplied to superheated steam flowing down a steam passage, and the superheated steam is cooled to a predetermined temperature. A first liquid storage container for storing a liquid is disposed, and a liquid inlet of the first liquid storage container is communicated with a vapor passage through which superheated steam flows, and The liquid outlet of the first liquid reservoir is communicated with the second liquid reservoir through a communication passage, and is connected to the liquid outlet of the second liquid reservoir via a connection passage with a vapor passage through which superheated steam flows. In addition, the first liquid reservoir and the second liquid reservoir communicate with a high-pressure fluid communication passage communicating with the high-pressure fluid source, and the first liquid reservoir and the high-pressure fluid communication passage communicate with each other between the first liquid reservoir and the high-pressure fluid communication passage. A switching valve that switches between inflow and shutoff of high-pressure fluid into the reservoir It is. DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS When a high-pressure fluid into a first liquid reservoir is shut off by a switching valve, liquid in a vapor passage passes through a first passage through a communication passage and a liquid inlet. It flows into the reservoir. The liquid that has flowed into and accumulated in the first liquid reservoir is transferred into the second liquid reservoir via the communication path and the liquid outlet when the high-pressure fluid flows into the first liquid reservoir by the switching valve. Inflow. Further, the liquid that has flowed into the second liquid reservoir is supplied to the vapor passage via the connection passage and the liquid outlet by the fluid pressure of the high-pressure fluid, and the temperature of the superheated steam is reduced. 1, a steam pipe 1 as a steam passage through which superheated steam flows, a first liquid reservoir 2 and a second liquid reservoir 3, and a second liquid reservoir 3 And a connection passage 4 for supplying the cooling liquid into the steam pipe 1 from above. A valve 5, an automatic control valve 6, and a gas-liquid mixing separator 7 are sequentially attached to the steam pipe 1, and steam reduced to a predetermined temperature is supplied from a pipe 8 to a steam using device (not shown). The automatic control valve 6 controls the amount, pressure, or temperature of the steam supplied from the pipe 8, and the gas-liquid mixing / separating device 7.
The superheated steam in the steam pipe 1 and the cooling liquid supplied from the connection passage 4 are mixed and further separated, and only the steam separated from the liquid and cooled to a predetermined temperature is supplied to the pipe 8. The steam pipe 1 is branched to communicate with the high-pressure fluid communication passage 9. The high-pressure fluid communication passage 9 is connected to the high-pressure fluid inlet 11 of the first liquid reservoir 2 via a valve 10 and to the upper side of the second liquid reservoir 3 via a valve 12. Although not shown, the high-pressure fluid communication passage 9
The pressure of the high-pressure fluid supplied to the first liquid reservoir 2 and the second liquid reservoir 3 is kept constant by attaching a pressure reducing valve having a function of keeping the pressure on the secondary side constant. be able to. A gas-liquid mixing / separating device 7 is connected to a liquid inlet 13 of the first liquid reservoir 2 via a check valve 14 and a liquid passage 15.
To the lower end of the A vapor trap 16 and a check valve 17 are connected to the lower end of the mixing separator 7. Steam trap 16
Is a type of automatic valve that allows only condensed water as a condensed water of the vapor separated by the gas-liquid mixing separator 7 or the cooling liquid to flow down, and does not cause the vapor to flow down. Check valves 17 and 14
The passage of the fluid from the vapor trap 16 to the liquid inlet 13 is allowed, and the passage of the fluid to the opposite side is not allowed. A high-pressure fluid outlet 18 is provided on the upper side of the first liquid reservoir 2 beside the high-pressure fluid inlet 11 so that the atmosphere communication pipe 1 is provided.
9 is connected. A liquid outlet 20 is provided below the liquid inlet 13 of the first liquid reservoir 2, and communicates with the second liquid reservoir 3 through a communication passage 21. A check valve 22 is attached to the communication passage 21. The check valve 22 allows the fluid to pass from the liquid outlet 20 to the second liquid reservoir 3 side, but does not allow the fluid to pass to the opposite side. The first liquid storage container 2 raises an internal float (not shown) when a liquid such as condensate flowing in from the liquid inlet 13 accumulates therein and the liquid level rises, and when the liquid reaches a predetermined position, it snaps. Moving to open the pressure delivery valve attached to the high pressure fluid inlet 11 and
The high-pressure fluid communication passage 9 supplies high-pressure vapor to the inside of the first liquid reservoir 2, and the accumulated liquid is discharged from the liquid outlet 20 to the check valve 22 and the communication passage 21.
Through the second liquid reservoir 3. As the liquid in the first liquid reservoir 2 flows down to the second liquid reservoir 3, the float (not shown) inside descends and snaps when it drops to a predetermined liquid level. The high-pressure fluid inlet 11 is closed, the high-pressure fluid outlet 18 is opened, and the high-pressure steam in the first liquid reservoir 2 is discharged from the atmosphere communication pipe 19 to the outside.
Again, liquid such as condensate flows into the first liquid reservoir 2 from the liquid passage 15. In the present embodiment, a pressure-feeding valve attached to the high-pressure fluid inlet 11 and an exhaust valve attached to the high-pressure fluid outlet 18 switch between inflow and cutoff of the high-pressure fluid into the first liquid reservoir 2. Configure the valve. A cooling liquid supply pipe 23 is connected between the two check valves 14 and 17 in the liquid passage 15. An automatic valve 24 is attached to the cooling liquid supply pipe 23. When the cooling liquid, for example, the cooling water is insufficient, the cooling liquid can be supplied from the automatic valve 24. The second liquid reservoir 3 communicated with the first liquid reservoir 2 by the communication passage 21 is formed by a closed tank, and the high pressure fluid communication passage 9 is connected to the upper side. Container 3
A liquid level sensor 25 for detecting the liquid level in the container 3
Attach. A connection passage 4 is connected to a lower portion of the container 3. The connection passage 4 is connected to a surplus liquid discharge pipe 27 via an automatic valve 26, and is fitted with an in-line heat exchanger 28. The heat exchanger 28 includes an ejector 29, a heating or cooling fluid supply pipe 30, and an automatic control valve 31 and a check valve 32 attached to the fluid supply pipe 30. A temperature sensor 33 for detecting a liquid temperature in the connection passage 4 is attached to the connection passage 4 on the side of the steam pipe 1. The temperature sensor 33 and the automatic control valve 31 are electrically connected via a temperature controller (not shown). A predetermined amount of heating or cooling fluid is supplied from the heating or cooling fluid supply pipe 30 by adjusting the valve opening of the automatic control valve 31 in accordance with the temperature of the cooling fluid detected by the temperature sensor 33. To the liquid in the steam pipe 1
The temperature of the cooling liquid supplied to the inside can be arbitrarily controlled. When the cooling liquid is supplied from the connection passage 4 into the steam pipe 1, the steam pipe 1
Preferably, a nozzle for injecting the cooling liquid is attached to the inner end. The liquid level sensor 25 attached to the second liquid reservoir 3 is connected to an automatic valve 2 via a controller (not shown).
4, 26 are electrically connected. Depending on the liquid level detected by the liquid level sensor 25, the automatic valve 24 is opened to supply the cooling liquid,
Alternatively, the automatic cooling valve 26 is opened to remove excess cooling liquid out of the system. When the steam passes through the inside of the steam pipe 1 at the time of initial startup, the steam is cooled and condensed, and the steam is condensed.
Flows into the liquid storage container 2. When the liquid level in the container 2 reaches a predetermined height, the pressure-feeding valve attached to the high-pressure fluid inlet 11 opens, and the exhaust valve attached to the high-pressure fluid outlet 18 closes. When the high-pressure steam is supplied into the container 2 and becomes the same pressure as that in the second liquid storage container 3, the liquid in the container 2 naturally flows down into the container 3 due to a difference in head. The inside of the second liquid reservoir 3 is constantly in communication with the high-pressure fluid passage 9, and the liquid in the container 3 is pumped from the connection passage 4 into the steam pipe 1 by the pressure of the high-pressure fluid, so that It is injected into superheated steam flowing down the pipe 1.
The cooling liquid injected into the steam pipe 1 is mixed with the superheated steam in the gas-liquid mixing / separator 7 to lower the temperature of the superheated steam.
In this case, the temperature of the superheated steam to be reduced can be appropriately controlled by adjusting the amount and temperature of the cooling liquid supplied from the connection passage 4. The remaining cooling liquid mixed with the superheated steam in the gas-liquid separator 7 is separated into gas and liquid in the separator 7.
It flows down from the vapor trap 16 at the lower end into the first liquid storage container 2. On the other hand, the vapor at a predetermined temperature from which the liquid is separated,
The water is supplied from the mixing separator 7 through the line 8 to the steam use point. As described above, according to the present invention, the cooling liquid is continuously supplied to the steam pipe through the first liquid storage container and the second liquid storage container, so that the steam is supplied. The superheated steam in the pipe can be reduced to an arbitrary steam temperature, and it is inexpensive and simple without using various sensors such as pressure and flow rate, control valves, or pump means for supplying cooling liquid. It is possible to provide a simple steam desuperheater.

【図面の簡単な説明】 【図1】本発明の蒸気減温装置の実施例を示す構成図。 【符号の説明】 1 蒸気管 2 第1の液体溜容器 3 第2の液体溜容器 4 接続通路 7 気液の混合分離器 9 高圧流体通路 11 高圧流体入口 13 液体入口 15 液体通路 18 高圧流体出口 19 大気連通管 20 液体出口 21 連通路 23 冷却液体補給管 25 液位センサ 28 熱交換器 33 温度センサ[Brief description of the drawings] FIG. 1 is a configuration diagram showing an embodiment of a steam deheater of the present invention. [Explanation of symbols] 1 steam pipe 2 First liquid reservoir 3 Second liquid reservoir 4 Connection passage 7 Gas-liquid mixing separator 9 High-pressure fluid passage 11 High-pressure fluid inlet 13 Liquid inlet 15 Liquid passage 18 High pressure fluid outlet 19 Atmospheric communication pipe 20 Liquid outlet 21 Connecting passage 23 Cooling liquid supply pipe 25 Liquid level sensor 28 heat exchanger 33 temperature sensor

Claims (1)

【特許請求の範囲】 【請求項1】 蒸気通路を流下する過熱蒸気に冷却流体
を供給して、当該過熱蒸気を所定温度状態の蒸気へ減温
するものにおいて、液体を溜め置く第1の液体溜容器を
配置して、当該第1の液体溜容器の液体入口を過熱蒸気
の流下する蒸気通路と連通路で連通し、当該第1の液体
溜容器の液体出口を第2の液体溜容器と連通路で連通し
て、当該第2の液体溜容器の液体出口に接続通路を介し
て過熱蒸気の流下する蒸気通路と接続すると共に、第1
の液体溜容器と第2の液体溜容器に高圧流体源と連通す
る高圧流体連通路を連通して、第1の液体溜容器と高圧
流体連通路の間に、第1の液体溜容器内への高圧流体の
流入と遮断を切り換える切換弁を取り付けたことを特徴
とする蒸気減温装置。
Claims: 1. A first liquid for storing a liquid, wherein a cooling fluid is supplied to superheated steam flowing down a steam passage to reduce the temperature of the superheated steam to steam at a predetermined temperature. A reservoir is disposed, the liquid inlet of the first liquid reservoir communicates with a vapor passage through which the superheated steam flows, and the liquid outlet of the first liquid reservoir communicates with the second liquid reservoir. The liquid passage of the second liquid reservoir is connected to the vapor outlet through which the superheated steam flows through the connection passage, and the first liquid reservoir is connected to the liquid outlet of the second liquid reservoir.
The high-pressure fluid communication passage communicating with the high-pressure fluid source communicates with the liquid storage container and the second liquid storage container, and between the first liquid storage container and the high-pressure fluid communication passage, into the first liquid storage container. And a switching valve for switching between inflow and shutoff of the high-pressure fluid.
JP2001349515A 2001-11-15 2001-11-15 Steam desuperheater Expired - Fee Related JP3836710B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001349515A JP3836710B2 (en) 2001-11-15 2001-11-15 Steam desuperheater

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001349515A JP3836710B2 (en) 2001-11-15 2001-11-15 Steam desuperheater

Publications (2)

Publication Number Publication Date
JP2003148702A true JP2003148702A (en) 2003-05-21
JP3836710B2 JP3836710B2 (en) 2006-10-25

Family

ID=19162170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001349515A Expired - Fee Related JP3836710B2 (en) 2001-11-15 2001-11-15 Steam desuperheater

Country Status (1)

Country Link
JP (1) JP3836710B2 (en)

Also Published As

Publication number Publication date
JP3836710B2 (en) 2006-10-25

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