JPH05172304A - Clean superheated steam generator - Google Patents

Clean superheated steam generator

Info

Publication number
JPH05172304A
JPH05172304A JP35483091A JP35483091A JPH05172304A JP H05172304 A JPH05172304 A JP H05172304A JP 35483091 A JP35483091 A JP 35483091A JP 35483091 A JP35483091 A JP 35483091A JP H05172304 A JPH05172304 A JP H05172304A
Authority
JP
Japan
Prior art keywords
water
steam
pipe
water pipe
supply header
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.)
Pending
Application number
JP35483091A
Other languages
Japanese (ja)
Inventor
Makoto Sanmi
誠 三美
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.)
Miura Co Ltd
Original Assignee
Miura 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 Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP35483091A priority Critical patent/JPH05172304A/en
Publication of JPH05172304A publication Critical patent/JPH05172304A/en
Pending legal-status Critical Current

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  • Cleaning By Liquid Or Steam (AREA)

Abstract

PURPOSE:To obtain a clean superheated steam generator integrated with a steam generator and a steam superheater. CONSTITUTION:A water supply header part 2, a heat exchange port 3 and a steam header part 4 are successively provided in a container 1 and a plurality of water pipes 6 piercing the heat exchange part 3 to allow the water supply header part 2 and the steam header part 4 to communicate with each other are provided and a steam generating part 8a is formed between the end parts 6a on the side of the water supply header part 2 of the water pipes 6 and the water level WL at the time of operation of the water supplied into the water pipes 6 and a steam superheating part 8b is formed between the water level WL and the end parts 6b on the side of the steam header part 4 of the water pipes 6. A conc. water discharge chamber 10 is provided to be adjacent to the water supply header part 2 and conc. water discharge pipes 11 each having an outer diameter smaller than the inner diameter of each of the water pipes 6 and piercing the water supply header part 2 to allow the concn. water discharge chamber 10 and the water pipes 6 to communicate with each other are provided and the end parts on the side of the water pipes 6 of the conc. water discharge pipes 11 are positioned between the end parts 6a and the water level WL within the water pipes 6.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、半導体、精密部品等の
洗浄に使用されるクリーン過熱蒸気を製造するクリーン
過熱蒸気発生器に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a clean superheated steam generator for producing clean superheated steam used for cleaning semiconductors, precision parts and the like.

【0002】[0002]

【従来の技術】半導体や精密部品等の洗浄剤としてフロ
ンが使用されているのは周知の通りである。しかし、近
年、フロンによるオゾン層の破壊が大きな環境問題にな
っており、フロンの代替品として、純水の過熱蒸気(以
下、クリーン過熱蒸気という)の使用が検討されてい
る。クリーン過熱蒸気を製造する装置としては、例えば
図3に示すようなものが提案されている。該装置は、給
水ライン33を介して供給された水を加熱して蒸気にす
るための蒸気発生器34と、蒸気発生器34に接続さ
れ、蒸気発生器34から供給された蒸気を過熱して過熱
蒸気にするための蒸気過熱器35と、この装置全体を制
御する制御ユニット36と、蒸気発生器34内に設けら
れ、蒸気から液滴分を除去するためのセパレータ37と
からなる。
2. Description of the Related Art It is well known that CFC is used as a cleaning agent for semiconductors and precision parts. However, in recent years, the destruction of the ozone layer by CFCs has become a major environmental problem, and the use of superheated steam of pure water (hereinafter referred to as clean superheated steam) as a substitute for CFCs is being considered. As a device for producing clean superheated steam, for example, a device as shown in FIG. 3 has been proposed. The apparatus is connected to the steam generator 34 for heating the water supplied through the water supply line 33 to form steam, and superheats the steam supplied from the steam generator 34. It comprises a steam superheater 35 for converting to superheated steam, a control unit 36 for controlling the entire apparatus, and a separator 37 provided in the steam generator 34 for removing droplets from the steam.

【0003】図4に示すように、蒸気発生器34は、容
器38内に順に給水ヘッダ部39、熱交換部40、蒸気
ヘッダ部41を有し、図3に示すように、給水ヘッダ部
39には給水ライン33が接続され、給水ライン33を
介して水が供給される。供給される水は原水に精密濾
過、脱イオン処理、脱気処理等を施して実質上純水とし
たものである。図4に示すように、熱交換部40は熱交
換部40を貫通して給水ヘッダ部39と蒸気ヘッダ部4
1とを連通する複数の水管42を有し、図3に示すよう
に、熱交換部40には蒸気ライン43が接続され、蒸気
ライン43を介して加熱用蒸気が供給される。水管42
の外周と容器38の内周との間の空間は蒸気ジャケット
として機能し、水管42内の水を加熱するようになって
いる。また、蒸気ヘッダ部41は、その中心部に、旋回
流による遠心力によって蒸気から液滴分を除去するセパ
レータ37を有し、蒸気ヘッダ部41にはドレンライン
44が接続され、セパレータ37によって除去された液
滴分はドレンライン44を介して排出される。
As shown in FIG. 4, the steam generator 34 has a water supply header section 39, a heat exchange section 40, and a steam header section 41 in order inside a container 38, and as shown in FIG. 3, the water supply header section 39. A water supply line 33 is connected to, and water is supplied through the water supply line 33. The supplied water is substantially pure water obtained by subjecting raw water to microfiltration, deionization, deaeration, and the like. As shown in FIG. 4, the heat exchange part 40 penetrates the heat exchange part 40 and the water supply header part 39 and the steam header part 4
1 has a plurality of water pipes 42 communicating with each other. As shown in FIG. 3, a steam line 43 is connected to the heat exchange section 40, and heating steam is supplied through the steam line 43. Water pipe 42
The space between the outer circumference of the water container and the inner circumference of the container 38 functions as a steam jacket and heats the water in the water pipe 42. Further, the steam header portion 41 has a separator 37 at the center thereof, which removes droplets from the steam by centrifugal force due to the swirling flow, and a drain line 44 is connected to the steam header portion 41 and removed by the separator 37. The formed droplets are discharged through the drain line 44.

【0004】図5に示すように、蒸気過熱器35は、容
器45内に順に蒸気ヘッダ部46、熱交換部47、過熱
蒸気ヘッダ部48を有し、図3に示すように、蒸気ヘッ
ダ部46は蒸気ライン49によって蒸気発生器34の蒸
気ヘッダ部41に接続されている。図5に示すように、
熱交換部47は、熱交換部47を貫通して蒸気ヘッダ部
46と過熱蒸気ヘッダ部48とを連通する複数本の伝導
管50を有し、図3に示すように、熱交換部47には蒸
気ライン51が接続され、蒸気ライン51を介して加熱
用蒸気が供給される。伝導管50の外周と容器45の内
周との間の空間は蒸気ジャケットとして機能し、伝導管
50内の蒸気を過熱するようになっている。また、過熱
蒸気ヘッダ部48には過熱蒸気供給ライン52が接続さ
れ、過熱蒸気供給ライン52を介して過熱蒸気が洗浄ユ
ニット等の負荷に供給される。
As shown in FIG. 5, the steam superheater 35 has a steam header section 46, a heat exchanging section 47, and a superheated steam header section 48 in a container 45 in order, and as shown in FIG. 46 is connected to the steam header portion 41 of the steam generator 34 by a steam line 49. As shown in FIG.
The heat exchanging part 47 has a plurality of conduction pipes 50 penetrating the heat exchanging part 47 and communicating the steam header part 46 and the superheated steam header part 48. As shown in FIG. Is connected to a steam line 51, and heating steam is supplied through the steam line 51. The space between the outer circumference of the conduction pipe 50 and the inner circumference of the container 45 functions as a steam jacket, and superheats the steam in the conduction pipe 50. Further, an overheated steam supply line 52 is connected to the overheated steam header section 48, and the overheated steam is supplied to a load such as a cleaning unit via the overheated steam supply line 52.

【0005】制御ユニット36は、蒸気発生器34、蒸
気過熱器35に各々供給される加熱用蒸気の圧力、蒸気
発生器34の蒸気ヘッダ部41内の蒸気圧力、蒸気過熱
器35の前後における蒸気温度、蒸気発生器34の熱交
換部40の水管42の水位を検出することによって、蒸
気ライン43、49、51の制御弁V1〜V3の開度を
調整し、蒸気過熱器35に接続された負荷に応じた過熱
蒸気を供給するようになっている。また、図3におい
て、参照番号53は蒸気発生器34に取り付けられた水
位制御筒で、この水位制御筒53は熱交換部40の水管
42の水位を検出するとともに、この検出値をもとに蒸
気発生器34への給水量を制御するようになっている。
The control unit 36 controls the pressure of the heating steam supplied to the steam generator 34 and the steam superheater 35, the steam pressure in the steam header portion 41 of the steam generator 34, the steam before and after the steam superheater 35. By detecting the temperature and the water level of the water pipe 42 of the heat exchange section 40 of the steam generator 34, the openings of the control valves V1 to V3 of the steam lines 43, 49, and 51 were adjusted and connected to the steam superheater 35. Superheated steam is supplied according to the load. Further, in FIG. 3, reference numeral 53 is a water level control cylinder attached to the steam generator 34. The water level control cylinder 53 detects the water level of the water pipe 42 of the heat exchange section 40, and based on the detected value. The amount of water supplied to the steam generator 34 is controlled.

【0006】上記の構成のクリーン過熱蒸気製造装置を
起動すると、水が給水ライン33から蒸気発生器34の
給水ヘッダ部39に供給され、水管42の設定水位まで
満たされる。次に、蒸気ライン43、51から加熱用蒸
気が蒸気発生器34ならびに蒸気過熱器35の熱交換部
40、47に供給される。水管42内の水が加熱され、
水管42の下部の内面から蒸気泡が発生し、水管42内
の水を押し上げ、水管42の上端付近まで達する。そし
て、水管42の上端付近で水と蒸気が分離し、蒸気は蒸
気ヘッダ部41内に流入し、セパレータ37によって蒸
気内に含まれている液滴分が除去され、乾き度の高い飽
和蒸気になる。そして、蒸気は蒸気ライン49を介して
蒸気過熱器35の蒸気ヘッダ部46に供給され、熱交換
部47の伝導管50内に流入し、更に飽和温度以上に過
熱されて過熱蒸気になり、過熱蒸気ヘッダ部48に流入
する。そして、過熱蒸気は過熱蒸気供給ライン52を介
して洗浄ユニット等の負荷に供給される。
When the clean superheated steam producing apparatus having the above-mentioned structure is started, water is supplied from the water supply line 33 to the water supply header section 39 of the steam generator 34 and is filled up to the set water level of the water pipe 42. Next, the heating steam is supplied from the steam lines 43 and 51 to the steam generator 34 and the heat exchange sections 40 and 47 of the steam superheater 35. The water in the water pipe 42 is heated,
Steam bubbles are generated from the inner surface of the lower portion of the water pipe 42, push up the water in the water pipe 42, and reach the vicinity of the upper end of the water pipe 42. Then, the water and the steam are separated near the upper end of the water pipe 42, the steam flows into the steam header portion 41, the droplets contained in the steam are removed by the separator 37, and a saturated dry steam is obtained. Become. Then, the steam is supplied to the steam header section 46 of the steam superheater 35 through the steam line 49, flows into the conduction pipe 50 of the heat exchange section 47, and is further superheated to a temperature equal to or higher than the saturation temperature to become superheated steam. It flows into the steam header portion 48. Then, the superheated steam is supplied to the load such as the cleaning unit via the superheated steam supply line 52.

【0007】ところで、上記のクリーン過熱蒸気製造装
置では、蒸気発生器34と蒸気過熱器35が独立して設
けられているので、装置全体が大きくなると共に、装置
を構成する部品の数が多かった。
By the way, in the above-mentioned clean superheated steam manufacturing apparatus, since the steam generator 34 and the steam superheater 35 are provided independently, the entire apparatus becomes large and the number of parts constituting the apparatus is large. ..

【0008】[0008]

【発明が解決しようとする課題】そこで、本発明は、ク
リーン過熱蒸気発生器において、蒸気発生器と蒸気過熱
器を一体化することを課題とする。
Therefore, an object of the present invention is to integrate a steam generator and a steam superheater in a clean superheated steam generator.

【0009】[0009]

【発明の構成】本発明のクリーン過熱蒸気発生器は、容
器1内に順に給水ヘッダ部2、熱交換部3、蒸気ヘッダ
部4を設け、熱交換部3を貫通して給水ヘッダ部2と蒸
気ヘッダ部4とを連通する複数の水管6を設け、給水ヘ
ッダ部2に水を供給し、熱交換部3に加熱用蒸気を供給
し、給水ヘッダ部2を介して水管6内に供給される水を
加熱して蒸気を発生させるようにした蒸気発生器におい
て、水管6内に供給される水の稼動時の水位WLが水管
6内に位置し、水管6の給水ヘッダ部2側の端部6aと
水位WLとの間に蒸気発生部8aを形成し、水位WLと
水管6の蒸気ヘッダ部4側の端部6bとの間に蒸気過熱
部8bを形成してなり、蒸気発生部8aにおいて発生し
た蒸気を蒸気過熱部8bにおいて過熱し、給水ヘッダ部
2に隣接して濃縮水排出室10を設け、水管6の内径よ
り小さい外径を有していて、給水ヘッダ部2を貫通して
濃縮水排出室10と水管6とを連通する濃縮水排出管1
1を設け、濃縮水排出管11の水管6側の端部を水管6
内において端部6aと水位WLとの間に位置させ、水管
6内の水を濃縮水排出管11を介して濃縮水排出室10
内に排出するようにしたことを特徴とするものである。
The clean superheated steam generator of the present invention is provided with a water supply header part 2, a heat exchange part 3 and a steam header part 4 in this order in a container 1, and penetrates the heat exchange part 3 to form a water supply header part 2. A plurality of water pipes 6 communicating with the steam header portion 4 are provided, water is supplied to the water supply header portion 2, heating steam is supplied to the heat exchange portion 3, and water is supplied into the water pipe 6 via the water supply header portion 2. In a steam generator that heats water to generate steam, the water level WL of the water supplied into the water pipe 6 during operation is located inside the water pipe 6, and the end of the water pipe 6 on the side of the water supply header 2 The steam generating portion 8a is formed between the portion 6a and the water level WL, and the steam superheating portion 8b is formed between the water level WL and the end portion 6b of the water pipe 6 on the steam header portion 4 side. The steam generated in the above is superheated in the steam superheating section 8b and concentrated adjacent to the water supply header section 2. The discharge chamber 10 is provided, have an outside diameter smaller than the inside diameter of the water pipe 6, the water supply header 2 through the concentrated water discharge chamber 10 and the concentrated water discharge pipe 1 that communicates the water pipe 6
1 is provided, and the end of the concentrated water discharge pipe 11 on the water pipe 6 side is connected to the water pipe 6
Located in the interior between the end 6a and the water level WL, and the water in the water pipe 6 is passed through the concentrated water discharge pipe 11 to the concentrated water discharge chamber 10
It is characterized by being discharged inside.

【0010】[0010]

【作用】水管6内の水が加熱されると、水管6の内面か
ら蒸気泡が発生し、蒸気泡が水管6内の水をほぼ水位W
Lの位置まで押し上げ、水位WL付近で水と蒸気が分離
し、蒸気は蒸気過熱部8bにおいて更に飽和温度以上に
過熱されて過熱蒸気になる。蒸気と分離された水は濃縮
水排出管11の上端の開口部に流入して濃縮水排出室1
0内に排出される。このため、水管6内には給水ヘッダ
部2から新しい水が補充され、水管6内の水が薄められ
るので、水管6内の水が濃縮されるのを防止することが
できる。
When the water in the water pipe 6 is heated, steam bubbles are generated from the inner surface of the water pipe 6, and the steam bubbles cause the water in the water pipe 6 to be almost at the water level W.
It is pushed up to the position of L, water and steam are separated in the vicinity of the water level WL, and the steam is further heated to the saturation temperature or higher in the steam superheating section 8b and becomes superheated steam. The water separated from the steam flows into the opening at the upper end of the concentrated water discharge pipe 11 and flows into the concentrated water discharge chamber 1
It is discharged into 0. Therefore, new water is replenished in the water pipe 6 from the water supply header portion 2 and the water in the water pipe 6 is diluted, so that the water in the water pipe 6 can be prevented from being concentrated.

【0011】[0011]

【実施例】以下、本発明の実施例について説明する。図
1は本発明のクリーン過熱蒸気発生器の縦断面図であ
り、容器1内に順に給水ヘッダ部2、熱交換部3、過熱
蒸気ヘッダ部4が設けられている。給水ヘッダ部2には
給水ライン5が接続され、給水ライン5を介して実質上
純水である水が供給される。熱交換部3は、熱交換部3
を貫通して給水ヘッダ部2と過熱蒸気ヘッダ部4とを連
通する複数の水管6を有する。また、熱交換部3には蒸
気ライン7が接続され、蒸気ライン7を介して加熱用蒸
気が熱交換部3に供給される。熱交換部3内の水管6の
外周と容器1の内周との間の空間は蒸気ジャケットとし
て機能し、水管6内の水を加熱するようになっている。
また、この装置では、水管6内に供給される水の稼動時
の水位WLが水管6の中間点付近に位置し、水管6の給
水ヘッダ部2側の端部6aと水位WLとの間が蒸気発生
部8aとして機能し、水位WLと水管6の過熱蒸気ヘッ
ダ部4側の端部6bとの間が蒸気過熱部8bとして機能
するようになっている。過熱蒸気ヘッダ部4には過熱蒸
気供給ライン9が接続され、過熱蒸気供給ライン9は洗
浄ユニット等の負荷に接続されている。そして、給水ヘ
ッダ部2に隣接して濃縮水排出室10が設けられ、水管
6の内径より小さい外径を有する濃縮水排出管11が給
水ヘッダ部2を貫通して設けられ、その一端は水管6内
に挿入され、水位WLの少し下に位置し、他端は濃縮水
排出室10内に突出している。濃縮水排出室10には水
を排出するためのドレンライン12が接続されている。
また、容器1には水位制御筒13が取り付けられてお
り、水位制御筒13は水管6内の水位を検出するととも
に、この検出値をもとに給水ライン5から給水ヘッダ部
2に供給される水の量を制御するようになっている。
EXAMPLES Examples of the present invention will be described below. FIG. 1 is a vertical cross-sectional view of the clean superheated steam generator of the present invention, in which a water supply header portion 2, a heat exchange portion 3, and a superheated steam header portion 4 are sequentially provided in a container 1. A water supply line 5 is connected to the water supply header portion 2, and water that is substantially pure water is supplied through the water supply line 5. The heat exchange section 3 is a heat exchange section 3
Has a plurality of water pipes 6 penetrating therethrough to connect the water supply header portion 2 and the superheated steam header portion 4 to each other. A steam line 7 is connected to the heat exchange section 3, and heating steam is supplied to the heat exchange section 3 via the steam line 7. The space between the outer circumference of the water pipe 6 in the heat exchange section 3 and the inner circumference of the container 1 functions as a steam jacket to heat the water in the water pipe 6.
In addition, in this device, the water level WL of the water supplied into the water pipe 6 during operation is located near the midpoint of the water pipe 6, and the water level WL between the end 6a of the water pipe 6 on the side of the water supply header 2 and the water level WL. It functions as a steam generating portion 8a, and a portion between the water level WL and the end portion 6b of the water pipe 6 on the side of the superheated steam header portion 4 functions as a steam superheating portion 8b. An overheated steam supply line 9 is connected to the overheated steam header portion 4, and the overheated steam supply line 9 is connected to a load such as a cleaning unit. Then, a concentrated water discharge chamber 10 is provided adjacent to the water supply header part 2, and a concentrated water discharge pipe 11 having an outer diameter smaller than the inner diameter of the water pipe 6 is provided so as to penetrate the water supply header part 2, and one end thereof is a water pipe. 6 is located in the concentrated water discharge chamber 10, and the other end projects into the concentrated water discharge chamber 10. A drain line 12 for discharging water is connected to the concentrated water discharge chamber 10.
A water level control cylinder 13 is attached to the container 1, and the water level control cylinder 13 detects the water level in the water pipe 6 and is supplied to the water supply header section 2 from the water supply line 5 based on the detected value. It is designed to control the amount of water.

【0012】上記のような構成のクリーン過熱蒸気発生
器を駆動すると、水が給水ライン5から給水ヘッダ部2
に供給され、水管6内に所定の水位まで満たされる。そ
して、加熱用蒸気が蒸気ライン7から熱交換部3に供給
され、水管6内の水が加熱され、水温が飽和温度に達す
ると水管6の内面から蒸気泡が発生し始め、これが上方
へ流れていくのに伴って合体し、気泡塊となって水を押
し上げ、水がほぼ水位WLの位置に達する。水位WL付
近で蒸気と水が分離し、蒸気は蒸気過熱部8bにおいて
更に飽和温度以上に過熱されて過熱蒸気となり、過熱蒸
気ヘッダ部4に流入する。そして、過熱蒸気は過熱蒸気
供給ライン9を介して洗浄ユニット等の負荷に供給され
る。
When the clean superheated steam generator having the above structure is driven, water is supplied from the water supply line 5 to the water supply header section 2.
And the water pipe 6 is filled up to a predetermined water level. Then, the heating steam is supplied from the steam line 7 to the heat exchange unit 3, the water in the water pipe 6 is heated, and when the water temperature reaches the saturation temperature, steam bubbles start to be generated from the inner surface of the water pipe 6, and this flows upward. As they move, they coalesce and form bubbles, pushing up the water, and the water almost reaches the water level WL. Steam and water are separated in the vicinity of the water level WL, and the steam is further heated in the steam superheating section 8b to a temperature equal to or higher than the saturation temperature to become superheated steam, which then flows into the superheated steam header section 4. Then, the superheated steam is supplied to the load such as the cleaning unit via the superheated steam supply line 9.

【0013】一方、水位WL付近で蒸気と分離された水
は濃縮水排出管11の上端の開口部に流入し、濃縮水排
出管11を通って濃縮水排出室10内に排出される。水
管6内の水の水位が下がると水位制御筒13によって検
出され、給水ライン5から給水ヘッダ部2に水が供給さ
れ、水管6内に水が補充され、水管6内の水の水位が一
定に保たれる。したがって、水管6内の水が薄められ、
水管6内の水が濃縮されるのを防止することができる。
そして、濃縮水排出室10内の濃縮水はドレンライン1
2を介して外部に排出される。
On the other hand, the water separated from the steam near the water level WL flows into the opening at the upper end of the concentrated water discharge pipe 11 and is discharged into the concentrated water discharge chamber 10 through the concentrated water discharge pipe 11. When the water level in the water pipe 6 is lowered, it is detected by the water level control cylinder 13, water is supplied from the water supply line 5 to the water supply header portion 2, the water pipe 6 is replenished with water, and the water level in the water pipe 6 is constant. Kept in. Therefore, the water in the water pipe 6 is diluted,
It is possible to prevent the water in the water pipe 6 from being concentrated.
The concentrated water in the concentrated water discharge chamber 10 is drain line 1
It is discharged to the outside via 2.

【0014】このクリーン過熱蒸気発生器は、同一水管
内で蒸気の発生と過熱を行うことによって、従来の装置
で独立して設けられていた蒸気発生器と蒸気過熱器が一
体化されており、従来の装置に比べて大幅に小型化され
ると共に、装置を構成する部品の数が大幅に低減され
る。また、同一水管内で蒸気の発生と過熱を行うことに
より、過熱される前の蒸気の熱を損失することがなく、
効率良く過熱蒸気を製造することができる。
In this clean superheated steam generator, the steam generator and the steam superheater, which are independently provided in the conventional device, are integrated by generating and superheating steam in the same water pipe. The size is greatly reduced as compared with the conventional device, and the number of parts constituting the device is significantly reduced. Also, by generating steam and heating in the same water pipe, without losing the heat of steam before overheating,
Superheated steam can be efficiently produced.

【0015】なお、水位WLの位置は本実施例の位置に
限定されることはなく、水管内に蒸気発生部と蒸気過熱
部が形成されるように任意の位置に設定することができ
る。
The position of the water level WL is not limited to the position of this embodiment, and can be set at any position so that the steam generating part and the steam superheating part are formed in the water pipe.

【0016】また、装置を小型化する別の方法として、
図2に示すように、蒸気発生器と蒸気過熱器を一つに結
合することも考えられる。この装置は蒸気発生器14と
蒸気過熱器15とが分離可能に結合されたものである。
蒸気発生器14は図4に示す蒸気発生器34とほぼ同様
の構造を有し、容器16内に順に給水ヘッダ部17、熱
交換部18、蒸気ヘッダ部19が設けられ、熱交換部1
8を貫通して給水ヘッダ部17と蒸気ヘッダ部19とを
連通する複数の水管20を有し、給水ヘッダ部17に給
水ライン21が接続され、熱交換部18に加熱用蒸気を
供給する蒸気ライン22が接続され、容器16に水管2
0内の水位を検出し、給水ヘッダ部17に供給される水
の量を制御する水位制御筒23が接続され、蒸気ヘッダ
部19内に蒸気から液滴分を除去するためのセパレータ
24が設けられ、蒸気ヘッダ部19に蒸気から除去した
液滴分を排出するためのドレンライン25が接続されて
いる。蒸気過熱器15は図5に示す蒸気過熱器35と同
様の構造を有し、容器26内に順に蒸気ヘッダ部27、
熱交換部28、過熱蒸気ヘッダ部29が設けられ、熱交
換部28を貫通して蒸気ヘッダ部27と過熱蒸気ヘッダ
部29とを連通する伝導管30を有し、熱交換部28に
加熱用蒸気を供給する蒸気ライン31が接続され、過熱
蒸気ヘッダ部29に過熱蒸気を洗浄ユニット等に供給す
るための過熱蒸気ライン32が接続されている。
As another method for downsizing the device,
It is also conceivable to combine the steam generator and the steam superheater into one, as shown in FIG. In this device, a steam generator 14 and a steam superheater 15 are detachably connected.
The steam generator 14 has substantially the same structure as the steam generator 34 shown in FIG. 4, and a water supply header portion 17, a heat exchange portion 18, and a steam header portion 19 are sequentially provided in the container 16, and the heat exchange portion 1 is provided.
8 has a plurality of water pipes 20 penetrating 8 to connect the water supply header section 17 and the steam header section 19 to each other, the water supply line 21 is connected to the water supply header section 17, and the steam for supplying heating steam to the heat exchange section 18 The line 22 is connected to the water pipe 2 in the container 16.
A water level control cylinder 23 that detects the water level in 0 and controls the amount of water supplied to the water supply header section 17 is connected, and a separator 24 for removing droplets from the steam is provided in the steam header section 19. A drain line 25 for discharging the liquid droplets removed from the steam is connected to the steam header section 19. The steam superheater 15 has a structure similar to that of the steam superheater 35 shown in FIG.
The heat exchange section 28 and the superheated steam header section 29 are provided, and the heat exchange section 28 has a conduction pipe 30 which penetrates the heat exchange section 28 and communicates the steam header section 27 with the superheated steam header section 29. A steam line 31 for supplying steam is connected, and a superheated steam line 32 for supplying superheated steam to a cleaning unit or the like is connected to the superheated steam header portion 29.

【0017】上記の装置を駆動すると、給水ライン21
から蒸気発生器14の給水ヘッダ部17に水が供給さ
れ、水管20の所定水位まで水が満たされ、蒸気ライン
22から熱交換部18に加熱用蒸気が供給され、水管2
0内の水が加熱されて蒸気泡が発生し、水が水管20の
上端付近まで押し上げられ、水管20の上端で水と蒸気
が分離する。蒸気は蒸気ヘッダ部19に流入し、セパレ
ータ24によって液滴分が除去され、蒸気過熱器15の
蒸気ヘッダ部27に流入する。蒸気は熱交換部28の伝
導管30内に流入し、加熱用蒸気が蒸気ライン31から
熱交換部28に供給され、伝導管30内の蒸気は飽和温
度以上に過熱され、過熱蒸気になり、過熱蒸気ヘッダ部
29に流入する。過熱蒸気は過熱蒸気ライン32を介し
て洗浄ユニット等に供給される。
When the above device is driven, the water supply line 21
From the steam generator 14 to the water supply header portion 17 of the water, the water pipe 20 is filled with water to a predetermined water level, the steam line 22 to the heat exchange portion 18 to supply heating steam, the water pipe 2
The water in 0 is heated to generate steam bubbles, the water is pushed up to near the upper end of the water pipe 20, and the water and steam are separated at the upper end of the water pipe 20. The steam flows into the steam header section 19, the droplets are removed by the separator 24, and the steam flows into the steam header section 27 of the steam superheater 15. The steam flows into the conduction pipe 30 of the heat exchange unit 28, the heating steam is supplied from the steam line 31 to the heat exchange unit 28, the vapor in the conduction pipe 30 is superheated to the saturation temperature or higher, and becomes superheated steam. It flows into the superheated steam header section 29. The superheated steam is supplied to the cleaning unit or the like via the superheated steam line 32.

【0018】この装置は、蒸気発生器14と蒸気過熱器
15を分離して使用することもできる。その場合、蒸気
発生器14の蒸気ヘッダ部19と蒸気過熱器15の蒸気
ヘッダ部27がチューブ状の蒸気ラインによって接続さ
れる。
In this apparatus, the steam generator 14 and the steam superheater 15 can be used separately. In that case, the steam header portion 19 of the steam generator 14 and the steam header portion 27 of the steam superheater 15 are connected by a tubular steam line.

【0019】[0019]

【発明の効果】以上説明したように、この発明のクリー
ン過熱蒸気発生器によれば、蒸気発生器と蒸気過熱器が
一体化されているので、従来の装置に比べて大幅に小型
化することができると共に、装置を構成する部品の数を
大幅に低減することができる。また、蒸気の熱の損失を
防ぎ、過熱蒸気を製造する効率を向上させることもでき
る。したがって、所期の目的を達成することができるも
のである。
As described above, according to the clean superheated steam generator of the present invention, since the steam generator and the steam superheater are integrated, the size can be greatly reduced as compared with the conventional device. In addition, the number of parts constituting the device can be significantly reduced. It is also possible to prevent heat loss of steam and improve the efficiency of producing superheated steam. Therefore, the intended purpose can be achieved.

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

【図1】この発明のクリーン過熱蒸気発生器の縦断面図
である。
FIG. 1 is a vertical sectional view of a clean superheated steam generator of the present invention.

【図2】蒸気発生器と蒸気過熱器を分離可能に結合した
クリーン過熱蒸気発生器の縦断面図である。
FIG. 2 is a vertical cross-sectional view of a clean superheated steam generator in which a steam generator and a steam superheater are detachably connected.

【図3】従来のクリーン過熱蒸気発生器の概略図であ
る。
FIG. 3 is a schematic view of a conventional clean superheated steam generator.

【図4】従来の蒸気発生器の一部を破断した側面図であ
る。
FIG. 4 is a side view in which a part of a conventional steam generator is cut away.

【図5】従来の蒸気過熱器の一部を破断した側面図であ
る。
FIG. 5 is a side view in which a part of a conventional steam superheater is cut away.

【符号の説明】[Explanation of symbols]

1 容器 2 給水ヘッダ部 3 熱交換部 4 蒸気ヘッダ部 6 水管 6a 水管6の給水ヘッダ部2側の端部 6b 水管6の蒸気ヘッダ部4側の端部 8a 蒸気発生部 8b 蒸気過熱部 10 濃縮水排出室 11 濃縮水排出管 WL 水位 1 Container 2 Water Supply Header Section 3 Heat Exchange Section 4 Steam Header Section 6 Water Pipe 6a Water Pipe 6 Water Supply Header Section 2 Side End 6b Water Tube 6 Steam Header Section 4 Side End 8a Steam Generation Section 8b Steam Overheating Section 10 Concentration Water discharge chamber 11 Concentrated water discharge pipe WL Water level

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 容器1内に順に給水ヘッダ部2、熱交換
部3、蒸気ヘッダ部4を設け、前記熱交換部3を貫通し
て前記給水ヘッダ部2と前記蒸気ヘッダ部4とを連通す
る複数の水管6を設け、前記給水ヘッダ部2に水を供給
し、前記熱交換部3に加熱用蒸気を供給し、前記給水ヘ
ッダ部2を介して前記水管6内に供給される水を加熱し
て蒸気を発生させるようにした蒸気発生器において、前
記水管6内に供給される水の稼動時の水位WLが前記水
管6内に位置し、前記水管6の前記給水ヘッダ部2側の
端部6aと前記水位WLとの間に蒸気発生部8aを形成
し、前記水位WLと前記水管6の前記蒸気ヘッダ部4側
の端部6bとの間に蒸気過熱部8bを形成してなり、前
記蒸気発生部8aにおいて発生した蒸気を前記蒸気過熱
部8bにおいて過熱し、前記給水ヘッダ部2に隣接して
濃縮水排出室10を設け、前記水管6の内径より小さい
外径を有していて、前記給水ヘッダ部2を貫通して前記
濃縮水排出室10と前記水管6とを連通する濃縮水排出
管11を設け、前記濃縮水排出管11の前記水管6側の
端部を前記水管6内において前記端部6aと前記水位W
Lとの間に位置させ、前記水管6内の水を前記濃縮水排
出管11を介して前記濃縮水排出室10内に排出するよ
うにしたことを特徴とするクリーン過熱蒸気発生器。
1. A water supply header portion 2, a heat exchange portion 3, and a steam header portion 4 are sequentially provided in a container 1, and the water supply header portion 2 and the steam header portion 4 are communicated with each other through the heat exchange portion 3. A plurality of water pipes 6 are provided, water is supplied to the water supply header portion 2, heating steam is supplied to the heat exchange portion 3, and water supplied into the water pipe 6 via the water supply header portion 2 is supplied. In the steam generator that is heated to generate steam, the water level WL of the water supplied into the water pipe 6 during operation is located inside the water pipe 6, and the water pipe 6 on the side of the water supply header portion 2 of the water pipe 6 is located. A steam generating portion 8a is formed between the end portion 6a and the water level WL, and a steam superheating portion 8b is formed between the water level WL and the end portion 6b of the water pipe 6 on the steam header portion 4 side. , Superheat the steam generated in the steam generating section 8a in the steam superheating section 8b. Then, a concentrated water discharge chamber 10 is provided adjacent to the water supply header part 2, has an outer diameter smaller than the inner diameter of the water pipe 6, and penetrates the water supply header part 2 to form the concentrated water discharge chamber 10. A concentrated water discharge pipe 11 that communicates with the water pipe 6 is provided, and an end portion of the concentrated water discharge pipe 11 on the side of the water pipe 6 is connected to the end portion 6a and the water level W in the water pipe 6.
A clean superheated steam generator characterized in that the water in the water pipe (6) is discharged into the concentrated water discharge chamber (10) through the concentrated water discharge pipe (11).
JP35483091A 1991-12-18 1991-12-18 Clean superheated steam generator Pending JPH05172304A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP35483091A JPH05172304A (en) 1991-12-18 1991-12-18 Clean superheated steam generator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP35483091A JPH05172304A (en) 1991-12-18 1991-12-18 Clean superheated steam generator

Publications (1)

Publication Number Publication Date
JPH05172304A true JPH05172304A (en) 1993-07-09

Family

ID=18440193

Family Applications (1)

Application Number Title Priority Date Filing Date
JP35483091A Pending JPH05172304A (en) 1991-12-18 1991-12-18 Clean superheated steam generator

Country Status (1)

Country Link
JP (1) JPH05172304A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11149940B2 (en) 2010-09-03 2021-10-19 Greg Naterer Heat exchanger using non-pure water for steam generation

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US11149940B2 (en) 2010-09-03 2021-10-19 Greg Naterer Heat exchanger using non-pure water for steam generation

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