JPH025201Y2 - - Google Patents
Info
- Publication number
- JPH025201Y2 JPH025201Y2 JP9617582U JP9617582U JPH025201Y2 JP H025201 Y2 JPH025201 Y2 JP H025201Y2 JP 9617582 U JP9617582 U JP 9617582U JP 9617582 U JP9617582 U JP 9617582U JP H025201 Y2 JPH025201 Y2 JP H025201Y2
- Authority
- JP
- Japan
- Prior art keywords
- water
- boiler
- separated
- separator
- deaerator
- 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
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 44
- 239000000203 mixture Substances 0.000 claims 1
- 230000000694 effects Effects 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
Landscapes
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
- Pipeline Systems (AREA)
Description
【考案の詳細な説明】
本考案は上下の管寄の間に多数の水管を接続す
る構造の多管式貫流ボイラの改良に関するもので
ある。[Detailed Description of the Invention] The present invention relates to an improvement of a multi-tube once-through boiler having a structure in which a large number of water pipes are connected between upper and lower headers.
このような構造の多管式貫流ボイラでは上部管
寄から取出した蒸気をセパレータ(気水分離器)
に流入せしめ、該セパレータにおいて蒸気と水と
に分離する構成をとるのが通例であり、その場
合、従来は、セパレータ内に貯留された分離水は
その一部がブロー水として放出されるものの、残
余の分離水についてはそのままボイラ本体側へ環
流させることが可能となるような構造となつてい
た。 In a multi-tubular once-through boiler with this type of structure, the steam taken out from the upper header is passed through a separator (steam water separator).
It is customary to have a structure in which steam and water are separated into steam and water in the separator, and in this case, conventionally, part of the separated water stored in the separator is released as blow water. The structure was such that the remaining separated water could be directly returned to the boiler body.
ところがこの従来構造の多管式貫流ボイラを、
分離水を多量にボイラ本体側へ環流させるように
して使用されると貫流式ボイラでありながら循環
ボイラに近似するようになり、場合によつては貫
流ボイラの規格に合致しない方法で使用されるお
それが生じる。 However, this conventional multi-tubular once-through boiler
If a large amount of separated water is recirculated to the boiler body, it becomes similar to a circulation boiler even though it is a once-through boiler, and in some cases it is used in a manner that does not meet the once-through boiler standards. There is a risk that this may occur.
本考案は従来構造の多管式貫流ボイラにおける
上記の如き問題に鑑みてなされたもので、セパレ
ータで分離された分離水を脱気器へ導き、該脱気
器において給水と混合した後ボイラ本体へ環流さ
せるようにし、もつて分離水が直接ボイラ本体へ
環流することのないようにしたことを特徴とする
ものである。 The present invention was developed in view of the above-mentioned problems in multi-tube once-through boilers of conventional structure. Separated water separated by a separator is led to a deaerator, where it is mixed with feed water, and then the boiler body This feature is characterized in that the separated water is allowed to flow back to the boiler, thereby preventing the separated water from flowing directly back to the boiler body.
以下、本考案の多管式水管ボイラを第1図に示
す第1実施例及び第2図に示す第2実施例につい
て説明すると、第1図に示す第1実施例において
符号1は上部管寄2と下部管寄3の間に多数の水
管4を接続してなるボイラ本体を示し、符号5は
バーナを示している。 Hereinafter, the first embodiment shown in FIG. 1 and the second embodiment shown in FIG. 2 of the multi-tube water tube boiler of the present invention will be explained. In the first embodiment shown in FIG. 2 and a lower header 3, the boiler main body is formed by connecting a large number of water pipes 4, and the reference numeral 5 indicates a burner.
ボイラ本体1で発生せしめられた蒸気は蒸気管
19を通つてサイクロン式のセパレータ6に導か
れ、該セパレータ6において蒸気S(乾き度98%
以上)と分離水Xとに分離される。 Steam generated in the boiler body 1 is led to a cyclone-type separator 6 through a steam pipe 19, and in the separator 6 steam S (dryness 98%
above) and separated water X.
この分離水Xはその一部がブロー水として管2
5及び弁26を通つて連続的又は間欠的に排出さ
れるとともに残りの分離水Xは管21、トラツプ
22及びコントロール弁23を通つて直接脱気器
7に送られる。 A part of this separated water X is used as blow water in the pipe 2.
5 and valve 26, and the remaining separated water X is sent directly to deaerator 7 through pipe 21, trap 22 and control valve 23.
一方、給水管10を通つて供給される給水Yは
軟化器9を通過後、熱交換器8においてブロー水
から熱を回収した後散水器12によつて脱気器7
内で散水せしめられ、そこで溶存酸素及びCO1等
を分離する。この給水Yは脱気器7内の熱交換コ
イル11を通るときに予熱されて空気分離効果が
高められる。脱気器7内で分離されたガスAは脱
気管30から放出される。 On the other hand, the water supply Y supplied through the water supply pipe 10 passes through the softener 9, recovers heat from the blow water in the heat exchanger 8, and is then transferred to the deaerator 7 by the water sprinkler 12.
Water is sprinkled inside the tank, and dissolved oxygen, CO 1 , etc. are separated there. This feed water Y is preheated when passing through the heat exchange coil 11 in the deaerator 7, thereby enhancing the air separation effect. Gas A separated in the deaerator 7 is released from the deaerator pipe 30.
脱気器7内で分離水Xと給水Yとを混合してで
きた混合水Zは管13及びストレーナ14を通つ
て給水ポンプ15に吸入され、さらにコントロー
ル弁16を経て連続的は間欠的にボイラ本体1に
供給される。ボイラ本体1の下部管寄3には管1
7により水面計18が取付けられている。コント
ロール弁16はこの水面計18からの信号によつ
て開閉制御され、ボイラ本体1内での水位を常に
一定に保持する如く作用する。又、セパレータ6
にも水面計24が取付けられているが、この水面
計24はセパレータ6内の水位にしたがつてコン
トロール弁23を開閉制御し、セパレータ6内の
水位を一定に保持する作用をする。 Mixed water Z, which is created by mixing separated water It is supplied to the boiler main body 1. Pipe 1 is installed in the lower header 3 of the boiler body 1.
7, a water level gauge 18 is attached. The control valve 16 is controlled to open and close by a signal from the water level gauge 18, and acts to maintain the water level within the boiler body 1 at a constant level. Also, separator 6
A water level gauge 24 is also attached to the separator 6, and this water level gauge 24 controls the opening and closing of the control valve 23 according to the water level in the separator 6, and functions to maintain the water level in the separator 6 at a constant level.
第2図に示す第2実施例のものは、エジエクタ
ーポンプ29を使用して分離水Xと給水Yとを混
合する点が第1実施例の場合と異なつているだけ
で他の構成は第1実施例のものと同様である。 The second embodiment shown in FIG. 2 differs from the first embodiment only in that an ejector pump 29 is used to mix separated water X and feed water Y. This is similar to that of the first embodiment.
本考案は多管式貫流ボイラは上記各実施例にも
示されているように、セパレータ6内の分離水X
を直接ボイラ本体1へ環流させることなく、脱気
器7において給水Yと混合した後にボイラ本体1
へ供給するようにしているから、従来構造の貫流
ボイラの場合のように貫流ボイラに近似した方法
で誤使用されるおそれがなく、いづれの使用現場
においても確実に貫流ボイラの規格に合致した方
法で使用されるという効果がある。 In the present invention, the multi-tubular once-through boiler has separated water in the separator 6, as shown in each of the above embodiments.
The boiler body 1 is mixed with the feed water Y in the deaerator 7 without being directly circulated to the boiler body 1.
Because once-through boilers with a conventional structure are used, there is no risk of misuse in a method that approximates a once-through boiler, and the method ensures that once-through boiler standards are met at any site where it is used. It has the effect of being used in
第1図及び第2図はそれぞれ本考案の実施例に
かかる多管式貫流ボイラの構造図である。
1……ボイラ本体、2……上部管寄、3……下
部管寄、4……水管、6……セパレータ、7……
脱気器。
1 and 2 are structural diagrams of a multi-tubular once-through boiler according to an embodiment of the present invention, respectively. 1...Boiler body, 2...Upper header, 3...Lower header, 4...Water pipe, 6...Separator, 7...
Deaerator.
Claims (1)
連通せしめてボイラ本体1を構成し、該ボイラ本
体1に対して脱気器7を経由して給水を供給する
如くする一方、前記ボイラ本体1で発生した蒸気
をセパレータ6へ導き該セパレータ6において蒸
気と分離水とに分離させる如くした多管式貫流ボ
イラであつて、前記分離水を前記脱気器7におい
て前記給水と混合して前記ボイラ本体1へ還流さ
せるようにしたことを特徴とする多管式貫流ボイ
ラ。 A boiler main body 1 is constructed by connecting the upper and lower headers 2 and 3 with a large number of water pipes 4, 4, etc., and water is supplied to the boiler main body 1 via a deaerator 7. On the other hand, it is a multi-tube once-through boiler in which steam generated in the boiler main body 1 is guided to a separator 6 and separated into steam and separated water in the separator 6, and the separated water is passed through the deaerator 7 to the feed water. A multi-tube once-through boiler, characterized in that the mixture is mixed with the water and then refluxed to the boiler body 1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9617582U JPS593102U (en) | 1982-06-25 | 1982-06-25 | Multi-tubular once-through boiler |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9617582U JPS593102U (en) | 1982-06-25 | 1982-06-25 | Multi-tubular once-through boiler |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS593102U JPS593102U (en) | 1984-01-10 |
| JPH025201Y2 true JPH025201Y2 (en) | 1990-02-08 |
Family
ID=30229323
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9617582U Granted JPS593102U (en) | 1982-06-25 | 1982-06-25 | Multi-tubular once-through boiler |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS593102U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016148304A (en) * | 2015-02-13 | 2016-08-18 | 株式会社タクマ | Power generation system and power generation method |
-
1982
- 1982-06-25 JP JP9617582U patent/JPS593102U/en active Granted
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2016148304A (en) * | 2015-02-13 | 2016-08-18 | 株式会社タクマ | Power generation system and power generation method |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS593102U (en) | 1984-01-10 |
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