JPS6124837Y2 - - Google Patents

Info

Publication number
JPS6124837Y2
JPS6124837Y2 JP17063580U JP17063580U JPS6124837Y2 JP S6124837 Y2 JPS6124837 Y2 JP S6124837Y2 JP 17063580 U JP17063580 U JP 17063580U JP 17063580 U JP17063580 U JP 17063580U JP S6124837 Y2 JPS6124837 Y2 JP S6124837Y2
Authority
JP
Japan
Prior art keywords
drain
pipe
tank
steam
solution
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
Application number
JP17063580U
Other languages
Japanese (ja)
Other versions
JPS5793748U (en
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 filed Critical
Priority to JP17063580U priority Critical patent/JPS6124837Y2/ja
Publication of JPS5793748U publication Critical patent/JPS5793748U/ja
Application granted granted Critical
Publication of JPS6124837Y2 publication Critical patent/JPS6124837Y2/ja
Expired legal-status Critical Current

Links

Description

【考案の詳細な説明】 本考案は、スチーム加温設備のドレン回収装置
に関するものである。
[Detailed Description of the Invention] The present invention relates to a drain recovery device for steam heating equipment.

従来、スチーム加温設備では、熱交換後のスチ
ームはドレン化し、このドレンはトラツプを介し
て外部に排出されている。このため、排出される
ドレンはある程度の熱量(80゜〜90℃)をもつた
状態で捨てられており不経済であるとともに、し
かも排水系統での分離が難しいことから、排水処
理場の負荷増大の因をなしている。
Conventionally, in steam heating equipment, steam after heat exchange is converted into drain, and this drain is discharged to the outside via a trap. For this reason, the discharged condensate is discarded with a certain amount of heat (80° to 90°C), which is not only uneconomical, but also difficult to separate in the drainage system, which increases the load on wastewater treatment plants. It is the cause of

一方、加温設備であることから、槽内の加温さ
れるべき溶液、水または水溶液の蒸発減少分も多
く、また洗浄設備等として利用されている場合に
は、洗浄物の持ち出しもあるため、溶液の量が減
少するので、これを補うために通常は水の補給を
行なつている。
On the other hand, since it is a heating equipment, there is a large amount of evaporation loss of the solution, water, or aqueous solution to be heated in the tank, and if it is used as a cleaning equipment, cleaning items may be taken out. Since the amount of solution decreases, water is usually replenished to compensate for this.

また、スチームの有効利用ということで、熱交
換器を使用せずにスチームを直接溶液中に吹き込
む方法もあるが、この方法では液面制御ができ
る、オーバーフローした場合、溶液にアルカリと
か酸を使用していたときには公害面で大きな問題
となる。
Another method of effectively using steam is to blow steam directly into the solution without using a heat exchanger, but this method allows you to control the liquid level, and if an overflow occurs, use alkali or acid in the solution. When this happened, it became a big problem in terms of pollution.

本考案は、熱交換後のスチームドレンを、加温
槽中の溶液の補給のために使用するとともに、ス
チームドレンの有する熱量を有効に回収すること
を目的としたスチーム加温装置のドレン回収装置
を提供するものである。
The present invention is a drain recovery device for a steam heating device that uses the steam drain after heat exchange to replenish the solution in the heating tank, and also to effectively recover the heat contained in the steam drain. It provides:

本考案の装置は、加温されるべき水または水溶
液を収容している槽と、該槽内に配設されスチー
ム配管に接続されている熱交換器と、一端が該熱
交換器に接続され他端に排出口を有しかつ一部が
前記槽内の所定液面より高く配管されているドレ
ン配管と、一端が該ドレン配管の前記所定液面よ
り高く配管された部分に接続され他端が前記槽内
に開口しかつ途中にU字管部を有するリサイクル
管とからなることを特徴とする。
The device of the present invention includes a tank containing water or an aqueous solution to be heated, a heat exchanger disposed in the tank and connected to a steam pipe, and one end connected to the heat exchanger. A drain pipe having a discharge port at the other end and a part of which is piped higher than the predetermined liquid level in the tank, and one end of which is connected to the part of the drain pipe which is piped higher than the predetermined liquid level, and the other end and a recycle pipe opening into the tank and having a U-shaped pipe part in the middle.

以下、本考案の実施例を図面に従つてより詳細
に説明する。
Hereinafter, embodiments of the present invention will be described in more detail with reference to the drawings.

第1図は、本考案の一実施例の側断面図であ
る。図において、1は溶液aを収容している槽
で、従来のスチーム加温設備と同様に、槽1内に
熱交換器2を備えており、この熱交換器2は一端
がスチーム配管3に接続され、他端はトラツプ4
を備えたドレン配管5に接続されている。なお、
5′は開閉弁を備えたドレン配管5のバイパスで
ある。槽1の側壁には測温体6を設け、スチーム
配管3に設けた温調弁7と電気的に接続せしめス
チーム供給量を制御し得るようになつている。な
お、8は溶液aの供給管を示す。
Fig. 1 is a side cross-sectional view of one embodiment of the present invention. In the figure, 1 is a tank containing a solution a, and like conventional steam heating equipment, a heat exchanger 2 is provided in the tank 1. One end of the heat exchanger 2 is connected to a steam pipe 3 and the other end is connected to a trap 4.
It is connected to a drain pipe 5 equipped with
Reference numeral 5' denotes a bypass of the drain pipe 5 equipped with an on-off valve. A temperature sensor 6 is provided on the side wall of the tank 1 and is electrically connected to a temperature control valve 7 provided on the steam pipe 3 so that the amount of steam supplied can be controlled. Reference numeral 8 denotes a supply pipe for the solution a.

この加温設備に加えて、本考案ではドレン配管
5の一部を槽1内の所定液面よりも高くなるよう
に配管し、この高く配管したドレン配管5部分か
ら他端が槽1内に開口するリサイクル管9を設け
てある。しかも、このサイクル管9の途中には、
U字管部を形成させている。
In addition to this heating equipment, in the present invention, a part of the drain pipe 5 is piped so that it is higher than a predetermined liquid level in the tank 1, and the other end of the drain pipe 5 that is piped high is connected to the tank 1. An open recycling pipe 9 is provided. Moreover, in the middle of this cycle pipe 9,
A U-shaped tube portion is formed.

次に、この加温設備の作用について述べると、
まず溶液aの温度が所定温度以下となると、測定
温6からのフイードバツクで温調弁7が開き、ス
チームが熱交換器2中に供給される。この熱交換
器2でスチームは熱を放出し、凝縮してドレンb
となり、このドレンbは通常ドレン配管5を通つ
て排出口10から系外へ排出される。
Next, let's talk about the function of this heating equipment.
First, when the temperature of the solution a falls below a predetermined temperature, the temperature control valve 7 opens based on the feedback from the measured temperature 6, and steam is supplied into the heat exchanger 2. In this heat exchanger 2, the steam releases heat, condenses, and drains b.
The drain b is normally discharged from the drain port 10 through the drain pipe 5 to the outside of the system.

しかして、本考案ではリサイクル管9を設けて
あるため、ドレンbの一部が槽1内に供給される
のであるが、この供給機構を第2図および第3図
によりわかり易く説明する。この場合、ドレンb
はポツト9′に溜められ、余剰分だけが排出口1
0から排出される。
In the present invention, since a recycling pipe 9 is provided, a part of the drain b is supplied into the tank 1. This supply mechanism will be explained in an easy-to-understand manner with reference to FIGS. 2 and 3. In this case, drain b
is stored in pot 9', and only the excess is discharged to outlet 1.
Ejected from 0.

第2図は、槽1内が充分溶液aで満たされ液面
がほぼ所定の位置にあるときの状態を示す図であ
り、槽1内の溶液aの高さと開口部のリサイクル
管9中の溶液a面の高さとの差(H)と、U字管
部のドレン配管5側のドレンb面の高さとU字管
部の槽1側のドレンb面の高さとの差H′が一致
している。すなわち、リサイクル管9中に存在し
ている空気が、溶液aとドレンbから等しい圧力
を受けて移動しないため、ドレンbも槽1内に流
入しないのである。
FIG. 2 is a diagram showing the state when the tank 1 is sufficiently filled with solution a and the liquid level is approximately at a predetermined position. The difference (H) between the height of the solution a side and the difference H' between the height of the drain b side on the drain piping 5 side of the U-shaped pipe part and the height of the drain b side on the tank 1 side of the U-shaped pipe part is equal to We are doing so. That is, since the air existing in the recycle pipe 9 receives equal pressure from the solution a and the drain b and does not move, the drain b also does not flow into the tank 1.

一方、第3図は、槽1内の溶液aが減少し液面
が低下したときの状態を示す図であり、H<
H′となるために圧力差を生り、ドレンbが溶液
aに流入し、圧力が平衡となる所定の液面(点線
部)まで戻るのである。
On the other hand, FIG. 3 is a diagram showing the state when the solution a in the tank 1 decreases and the liquid level drops, and H<
H', a pressure difference is generated, drain b flows into solution a, and the pressure returns to a predetermined liquid level (dotted line) where it becomes equilibrium.

なお、図示した如くリサイクル管9の両端部の
管径を太くし、ポツト9′としたのは、管9内の
空気を逃さないため、また溶液aおよびドレンb
の液面変動を管9内で大きくとれるようにするた
めである。
As shown in the figure, the diameter of both ends of the recycle pipe 9 is increased to form pots 9' in order to prevent the air inside the pipe 9 from escaping, and also to prevent the solution a and the drain b from escaping.
This is to allow large fluctuations in the liquid level within the tube 9.

この結果、本考案では上記の如く給水をドレン
配管で自動的に行なうため、液面制御等のメンテ
ナンスが不要となるほか、補給用水を手動バルブ
で投入した場合の閉め忘れやボールタツプ給水の
洩れによるオーバーフロー等を防止できる。
As a result, with this invention, water is automatically supplied through the drain piping as described above, which eliminates the need for maintenance such as liquid level control, and eliminates the need for maintenance such as liquid level control. Overflow etc. can be prevented.

以上の如く、本考案の装置によれば、溶液の補
給を工業用水等でなく、熱をもつドレンによつて
行なうため、補給用水を必要としないことは勿
論、加温に使用していたスチーム量を10%程度削
減できる。また、公害面での総量規制が適用され
ている現在、水量を大幅に減らすことができる等
多くの利点を有する。
As described above, according to the device of the present invention, the solution is replenished not with industrial water but with a heated drain, so there is no need for replenishment water, and the steam used for heating can be removed. The amount can be reduced by about 10%. In addition, it has many advantages such as being able to significantly reduce the amount of water used in the current situation where total water pollution regulations are being applied.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は、本考案の一実施例を示す側断面図、
第2図および第3図は、上記実施例のリサイクル
管の機構を示す側断面図を表わす。 図中、1……槽、2……熱交換器、3……スチ
ーム配管、5……ドレン配管、9……リサイクル
管、10……排出口、a……溶液(水、水溶
液)、b……ドレン。
FIG. 1 is a side sectional view showing an embodiment of the present invention;
2 and 3 are side sectional views showing the mechanism of the recycling pipe of the above embodiment. In the figure, 1...tank, 2...heat exchanger, 3...steam pipe, 5...drain pipe, 9...recycle pipe, 10...discharge port, a...solution (water, aqueous solution), b ...Drain.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 加温されるべき水または水溶液を収容している
槽と、該槽内に配設されスチーム配管に接続され
ている熱交換器と、一端が該熱交換器に接続され
他端に排出口を有しかつ一部が前記槽内の所定液
面より高く配管されているドレン配管と、一端が
該ドレン配管の前記所定液面より高く配管された
部分に接続され他端が前記槽内に開口しかつ途中
にU字管部を有するリサイクル管とからなること
を特徴とするスチーム加温設備のドレン回収装
置。
A tank containing water or an aqueous solution to be heated, a heat exchanger disposed in the tank and connected to a steam pipe, and one end connected to the heat exchanger and an outlet at the other end. a drain pipe with a part of the drain pipe installed above a predetermined liquid level in the tank, and one end connected to a part of the drain pipe connected above the predetermined liquid level and the other end opened into the tank. A drain recovery device for a steam heating facility, comprising a recycling pipe having a U-shaped pipe section in the middle.
JP17063580U 1980-11-28 1980-11-28 Expired JPS6124837Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17063580U JPS6124837Y2 (en) 1980-11-28 1980-11-28

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17063580U JPS6124837Y2 (en) 1980-11-28 1980-11-28

Publications (2)

Publication Number Publication Date
JPS5793748U JPS5793748U (en) 1982-06-09
JPS6124837Y2 true JPS6124837Y2 (en) 1986-07-25

Family

ID=29529062

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17063580U Expired JPS6124837Y2 (en) 1980-11-28 1980-11-28

Country Status (1)

Country Link
JP (1) JPS6124837Y2 (en)

Also Published As

Publication number Publication date
JPS5793748U (en) 1982-06-09

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