JPS6323967Y2 - - Google Patents
Info
- Publication number
- JPS6323967Y2 JPS6323967Y2 JP191584U JP191584U JPS6323967Y2 JP S6323967 Y2 JPS6323967 Y2 JP S6323967Y2 JP 191584 U JP191584 U JP 191584U JP 191584 U JP191584 U JP 191584U JP S6323967 Y2 JPS6323967 Y2 JP S6323967Y2
- Authority
- JP
- Japan
- Prior art keywords
- separation chamber
- lower separation
- steam
- water
- inner cylinder
- 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
- 238000000926 separation method Methods 0.000 claims description 43
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 238000005192 partition Methods 0.000 claims description 6
- 238000007599 discharging Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
Landscapes
- Separating Particles In Gases By Inertia (AREA)
- Cyclones (AREA)
Description
【考案の詳細な説明】 本考案は蒸気の気水分離器に係るものである。[Detailed explanation of the idea] The present invention relates to a steam water separator.
サイクロンセパレーターや軸流セパレーターで
蒸気と水の分離を行うことは既に知られていると
ころである。しかし、サイクロンセパレーター及
び軸流セパレーターでは乾き度が90%を下がると
分離効率が極端に悪化し、水が伴流されてしまう
という欠点があつた。この欠点を補うためには、
セパレーターは、いきおい大型化してしまつてい
た。 It is already known that steam and water can be separated using a cyclone separator or an axial flow separator. However, cyclone separators and axial flow separators have the disadvantage that when the degree of dryness drops below 90%, the separation efficiency deteriorates extremely and water is swept away. To compensate for this shortcoming,
Separators were rapidly becoming larger.
本考案は上記の点に鑑み、乾き度の悪い場合に
も対応し、かつコンパクトな気水分離器を得るこ
とを目的とするものであつて、分離筒を仕切板に
て上部分離室と下部分離室に二分し、下部分離室
の側筒部に蒸気導入口を、下部分離室の底面に排
出管を、上部分離室に蒸気出口管を設け、仕切板
を貫通して上下分離室を連通する内筒を設け、前
記内筒内に軸流型の遠心分離器を設け、上下分離
室を連通し上部分離室の分離水を下部分離室に導
く降水管を設けた気水分離器である。 In view of the above points, the present invention aims to provide a compact steam/water separator that can be used even when the degree of dryness is poor. Divided into two separation chambers, with a steam inlet in the side cylinder of the lower separation chamber, a discharge pipe in the bottom of the lower separation chamber, and a steam outlet pipe in the upper separation chamber, the upper and lower separation chambers are communicated through the partition plate. The steam-water separator is provided with an inner cylinder, an axial flow type centrifugal separator inside the inner cylinder, and a downcomer pipe that connects the upper and lower separation chambers and guides the separated water in the upper separation chamber to the lower separation chamber. .
本考案を図面に従つて説明すると図1は本考案
における一実施例の縦断面図であり、図2は図1
の平面図である。図3は本考案における他の実施
例の縦断面図である。図中の1は分離筒であつて
仕切板2にて、上下分離室3,4に二分されてい
る。下部分離室4の側筒部には蒸気導入口5が設
けられている。本実施例においては蒸気導入口を
分離筒に直交させた場合を示しているが、分離筒
に対して接線方向に取付けてもよい。下部分離室
4の底面には分離水を排出する排出管6が設けら
れ、上部分離室には蒸気出口管7が設けられる。
この実施例では蒸気出口管7を上部分離室の上部
平面に取付けたものを示しているがこれに限定す
るわけではなく、蒸気導入口と同様に分離筒に対
して接線方向に取付けてもよい。上下分離室は仕
切板を貫通して設けられる内筒8にて連通せしめ
られている。この内筒8には、軸流型の遠心分離
器9が設けられている。さらに上下分離室は、上
部分離室で分離された水を下部分離室に導く降水
管10が設けられる。この上下分離室を連通する
降水管は図1のごとく分離筒内に設けてもよく、
図3のごとく分離筒外に設けてもよい。 To explain the present invention according to the drawings, FIG. 1 is a longitudinal sectional view of one embodiment of the present invention, and FIG.
FIG. FIG. 3 is a longitudinal sectional view of another embodiment of the present invention. Reference numeral 1 in the figure is a separation cylinder, which is divided into upper and lower separation chambers 3 and 4 by a partition plate 2. A steam inlet 5 is provided in the side tube portion of the lower separation chamber 4 . Although this embodiment shows a case in which the steam inlet is orthogonal to the separation tube, it may also be attached tangentially to the separation tube. A discharge pipe 6 for discharging separated water is provided at the bottom of the lower separation chamber 4, and a steam outlet pipe 7 is provided in the upper separation chamber.
In this embodiment, the steam outlet pipe 7 is shown attached to the upper plane of the upper separation chamber, but the invention is not limited to this, and it may be attached tangentially to the separation tube in the same way as the steam inlet. . The upper and lower separated chambers are communicated with each other by an inner cylinder 8 provided through a partition plate. This inner cylinder 8 is provided with an axial flow type centrifugal separator 9. Further, the upper and lower separation chambers are provided with a downcomer pipe 10 that guides the water separated in the upper separation chamber to the lower separation chamber. The downcomer pipe that communicates the upper and lower separation chambers may be provided inside the separation cylinder as shown in Figure 1.
It may also be provided outside the separation cylinder as shown in FIG.
次に作用について説明すると、蒸気導入口より
流入した気水は、下部分離室に突出した内筒に衝
突することによつて、一部分の水が分離される
(一段目)。次に内筒に設けた軸流型遠心分離器で
水滴を遠心分離する(二段目)。内筒を流出した
蒸気は良質な蒸気となつて蒸気出口管より系外に
移送される。なお、上部分離室で分離された分離
水は降水管により下部分離室に至り、下部分離室
で分離された分離水と一体となつて排出管から系
外に排出される。 Next, to explain the operation, the steam and water flowing in from the steam inlet collide with the inner cylinder protruding into the lower separation chamber, whereby a portion of the water is separated (first stage). Next, the water droplets are centrifuged using an axial flow centrifuge installed in the inner cylinder (second stage). The steam flowing out of the inner cylinder becomes high-quality steam and is transferred to the outside of the system through the steam outlet pipe. The separated water separated in the upper separation chamber reaches the lower separation chamber through the downcomer pipe, and is discharged from the system through the discharge pipe together with the separated water separated in the lower separation chamber.
本考案は以上のように構成されており、セパレ
ーター内で二段分離、すなわち重力落下で大粒の
水滴を分離し、二段目で微細な水滴を遠心分離さ
せるので、非常にコンパクトなセパレーターとす
ることができ、しかも乾き度の悪い蒸気に対して
も常に良質の蒸気を得ることができる。 The present invention is constructed as described above, and has two stages of separation within the separator. In other words, large water droplets are separated by gravity fall, and fine water droplets are centrifuged in the second stage, resulting in a very compact separator. Moreover, high-quality steam can always be obtained even from steam with poor dryness.
図1は本考案における一実施例の縦断面図、図
2は図1の平面図、図3は他の実施例の縦断面図
である。
1……分離筒、2……仕切板、3……上部分離
室、4……下部分離室、5……蒸気導入口、6…
…排出管、7……蒸気出口管、8……内筒、9…
…軸流型遠心分離器、10……降水管。
FIG. 1 is a longitudinal sectional view of one embodiment of the present invention, FIG. 2 is a plan view of FIG. 1, and FIG. 3 is a longitudinal sectional view of another embodiment. 1... Separation tube, 2... Partition plate, 3... Upper separation chamber, 4... Lower separation chamber, 5... Steam inlet, 6...
...Exhaust pipe, 7...Steam outlet pipe, 8...Inner cylinder, 9...
...Axial flow centrifuge, 10... Downcomer pipe.
Claims (1)
離室4に二分し、下部分離室4の側筒部に蒸気導
入口5を、下部分離室4の底面に排出管6を、上
部分離室3に蒸気出口管7を設け、仕切板2を貫
通して上下分離室3,4を連通する内筒8を設
け、前記内筒8内に軸流型の遠心分離器9を設
け、上下分離室3,4を連通し上部分離室3の分
離水を下部分離室4に導く降水管10を設けたこ
とを特徴とする気水分離器。 The separation tube 1 is divided into two by a partition plate 2 into an upper separation chamber 3 and a lower separation chamber 4, a steam inlet 5 is connected to the side cylinder part of the lower separation chamber 4, a discharge pipe 6 is connected to the bottom of the lower separation chamber 4, and a discharge pipe 6 is connected to the bottom of the lower separation chamber 4. A steam outlet pipe 7 is provided in the separation chamber 3, an inner cylinder 8 is provided that penetrates the partition plate 2 and communicates the upper and lower separation chambers 3 and 4, and an axial flow type centrifugal separator 9 is provided in the inner cylinder 8. A steam-water separator characterized in that a downcomer pipe 10 is provided for communicating the upper and lower separation chambers 3 and 4 and guiding the separated water in the upper separation chamber 3 to the lower separation chamber 4.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP191584U JPS60115565U (en) | 1984-01-10 | 1984-01-10 | steam water separator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP191584U JPS60115565U (en) | 1984-01-10 | 1984-01-10 | steam water separator |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS60115565U JPS60115565U (en) | 1985-08-05 |
JPS6323967Y2 true JPS6323967Y2 (en) | 1988-07-01 |
Family
ID=30475094
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP191584U Granted JPS60115565U (en) | 1984-01-10 | 1984-01-10 | steam water separator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS60115565U (en) |
Families Citing this family (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH0712666Y2 (en) * | 1988-04-22 | 1995-03-29 | 三菱重工業株式会社 | Engine cooling system |
US6941769B1 (en) * | 2004-04-08 | 2005-09-13 | York International Corporation | Flash tank economizer refrigeration systems |
JP7442169B2 (en) * | 2019-11-11 | 2024-03-04 | 株式会社ヒラカワ | Boiler steam and water separator |
-
1984
- 1984-01-10 JP JP191584U patent/JPS60115565U/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPS60115565U (en) | 1985-08-05 |
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