JPS632202B2 - - Google Patents
Info
- Publication number
- JPS632202B2 JPS632202B2 JP58001590A JP159083A JPS632202B2 JP S632202 B2 JPS632202 B2 JP S632202B2 JP 58001590 A JP58001590 A JP 58001590A JP 159083 A JP159083 A JP 159083A JP S632202 B2 JPS632202 B2 JP S632202B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- stage
- weir
- collection
- waterway
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A20/00—Water conservation; Efficient water supply; Efficient water use
- Y02A20/124—Water desalination
Landscapes
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Description
【発明の詳細な説明】
この発明は、多段フラツシユ蒸発式の海水淡水
化造水装置における低水質生産水の戻し装置に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a return device for low-quality produced water in a multi-stage flash evaporation type seawater desalination water production system.
従来、この種の造水装置においては、多数の段
のうちある段で生産水の水質が低下すると、この
低水質水を除くために、造水装置全体の運転を停
止する必要があつた。したがつて造水装置の停止
および再稼動による運転費のロスが著しく、その
対策が望まれていた。 Conventionally, in this type of fresh water generating apparatus, when the quality of produced water deteriorates in one of the many stages, it has been necessary to stop the operation of the entire fresh water generating apparatus in order to remove the low quality water. Therefore, there is a significant loss in operating costs due to stopping and restarting the freshwater generating equipment, and countermeasures have been desired.
この発明は上記の要望にこたえるべくなされた
もので、造水装置の運転を停止することなく、低
水質水を抜取つて、循環ブラインに戻し、淡水の
生産を続行することのできる低水質生産水の戻し
装置を提供することを目的とする。 This invention was made in response to the above-mentioned needs, and it is possible to extract low-quality water and return it to the circulating brine without stopping the operation of the fresh water production equipment, allowing for continued production of fresh water. The purpose is to provide a return device for
この発明による低水質生産水の戻し装置は、降
水口を有する凝縮水受けトレーの下面に各段にわ
たつて降水口に通じる収集水路が設けられ、収集
水路内に路長方向に堰が設けられて、堰によつて
収集水路が、降水口からの流下水を受けて各段ご
とに溜める受水部と、受水部からの堰越え水を各
段の仕切壁にあけられた通水口を経て生産水取出
し口へ導く導水部とに区分せられ、各段において
受水部からブラインの蒸発ゾーンにバルブ付き低
水質水戻し管が配されているものである。 The low water quality produced water return device according to the present invention has a collection channel connected to the precipitation port provided at each stage on the bottom surface of the condensed water receiving tray having a precipitation port, and a weir is provided in the collection channel in the direction of the path length. The collection channel is constructed by a weir, with a water receiving section that receives the runoff from the rain outlet and collects it at each stage, and a water inlet in the partition wall of each stage that allows water to flow over the weir from the water receiving section. The brine is divided into a water guide section that leads the water to the produced water outlet, and a low-quality water return pipe with a valve is arranged from the water receiving section to the brine evaporation zone at each stage.
以下、この発明の実施例について具体的に説明
する。 Examples of the present invention will be described in detail below.
第1図から第3図において、ブライン循環式の
造水装置1は多数の垂直仕切壁2によつて長さ方
向に多段に区分されている。各仕切壁2の下端部
にはフラツシユ用のオリフイス3があけられてい
る。各段は凝縮水を受けるためのトレー4によつ
てそれぞれ下側の蒸発ゾーン5と上側の凝縮ゾー
ン6に区分され、両ゾーン5,6はミスト除去部
材7を有する蒸気上昇路8によつて連通されてい
る。造水装置1の一端部すなわち第1図における
同装置1の左端部には、一段目の蒸発ゾーン5a
に通じるブラインの供給口9が設けられ、同他端
部には最終段の蒸発ゾーン5bに通じる蒸発残ブ
ラインの排出口10が設けられている。そして蒸
発残ブラインは排出口10から装置外部を経て供
給口9に戻され、再び蒸発ゾーン5に循環され
る。濃縮ブラインは循環路から所要量抜取られ
る。排出口10には海水補給口11が設けられて
いる。各段の凝縮ゾーン6には、第3図に示すよ
うに、複数の支持板12で束ねられた凝縮用の伝
熱管束13が設けられている。各支持板12はト
レー4との間にそれぞれ通水用の小間隙14を有
する。 In FIGS. 1 to 3, a brine circulation type freshwater generator 1 is divided into multiple stages in the length direction by a large number of vertical partition walls 2. As shown in FIGS. An orifice 3 for flushing is provided at the lower end of each partition wall 2. Each stage is divided into a lower evaporation zone 5 and an upper condensation zone 6 by a tray 4 for receiving condensed water, and both zones 5, 6 are separated by a steam riser 8 having a mist removal member 7. It is communicated. At one end of the freshwater generating apparatus 1, that is, at the left end of the apparatus 1 in FIG.
A brine supply port 9 leading to the evaporation zone 5b is provided at the other end, and an evaporation residual brine discharge port 10 leading to the final stage evaporation zone 5b is provided at the other end. The evaporation residual brine is then returned to the supply port 9 from the discharge port 10 via the outside of the apparatus, and is again circulated to the evaporation zone 5. The required amount of concentrated brine is withdrawn from the circuit. A seawater replenishment port 11 is provided at the discharge port 10. As shown in FIG. 3, each condensation zone 6 is provided with a condensing heat transfer tube bundle 13 bound by a plurality of support plates 12. Each support plate 12 has a small gap 14 between it and the tray 4 for water passage.
造水装置1の一側部すなわち第3図における同
装置1の左端部において、トレー4に降水口15
があけられており、トレー4の下面にはその長さ
方向に各段の降水口15に通じる収集水路16が
設けられている。収集水路16内には路長方向に
堰17が設けられ、堰17によつて収集水路16
は受水部18と導水部19に区分されている。各
段において受水部18には降水口15が上から臨
み、受水部18は降水口15からの流下水を受け
て各段ごとに溜めている。各仕切壁2における導
水部19の部分にはそれぞれ通水口20があけら
れている。また造水装置1の他端一側部には導水
部19に通じる生産水取出し口21が設けられて
いる。そして導水部19は受水部18からの堰越
え水を生産水取出し口21へ導いている。造水装
置1の一側部には、受水部18から同装置の外部
を経て蒸発ゾーン5に至る低水質水戻し管22が
配されている。そして同管22の装置外部分にバ
ルブ23が設けられている。 At one side of the freshwater generating device 1, that is, at the left end of the device 1 in FIG.
A collection channel 16 is provided in the lower surface of the tray 4 in the length direction thereof, leading to a rain outlet 15 at each stage. A weir 17 is provided in the collection waterway 16 in the length direction, and the weir 17 allows the collection waterway 16 to
is divided into a water receiving section 18 and a water guiding section 19. A rain outlet 15 faces the water receiving part 18 from above in each stage, and the water receiving part 18 receives the flowing water from the rain mouth 15 and stores it in each stage. A water passage port 20 is provided in each of the partition walls 2 at the water guide portion 19 . Further, a produced water outlet 21 communicating with the water guide section 19 is provided at one side of the other end of the fresh water generator 1 . The water guide section 19 guides water from the water receiving section 18 over the weir to the produced water outlet 21. A low-quality water return pipe 22 is disposed on one side of the fresh water generator 1 and extends from the water receiving portion 18 to the evaporation zone 5 via the outside of the device. A valve 23 is provided on the outer part of the tube 22.
上記構成の造水装置1において、各段の圧力は
ブライン供給端から排出端に徐々に低下せられて
おり、また各段のバルブ23はすべて閉じられて
いる。スチーム・ヒータによつて加熱せられた熱
ブラインは、供給口9から蒸発ゾーン5に供給さ
れ、各段のオリフイス3を減圧下に順次通過する
たびにフラツシユ蒸発せられる。生じた水蒸気は
蒸気上昇路8のミスト除去部材7を経て凝縮ゾー
ン6に入り、凝縮される。凝縮水はトレー4に滴
下し、トレー10上を降水口15の方向に流れて
収集せられ、収集水は各段において降水口15か
ら収集水路16の受水部18に流下して溜まる。
各段において、受水部18を満した生産水は、堰
17を越えて導水部19に溢流し、通水口20を
通つて生産水取出し口21へ流れる。こうして取
出し口21から淡水生産水が取出される。 In the freshwater generator 1 having the above configuration, the pressure at each stage is gradually reduced from the brine supply end to the discharge end, and all valves 23 at each stage are closed. Thermal brine heated by the steam heater is supplied to the evaporation zone 5 from the supply port 9, and flash-evaporated each time it passes sequentially through the orifices 3 of each stage under reduced pressure. The generated water vapor enters the condensation zone 6 via the mist removal member 7 of the steam ascending path 8 and is condensed. The condensed water drips onto the tray 4, flows on the tray 10 in the direction of the rain outlet 15, and is collected, and the collected water flows down from the rain outlet 15 at each stage to the water receiving part 18 of the collection channel 16 and accumulates therein.
At each stage, the produced water that has filled the water receiving section 18 overflows over the weir 17 into the water guiding section 19 and flows to the produced water outlet 21 through the water inlet 20. In this way, produced fresh water is taken out from the take-out port 21.
多数の段のうちある段において生産水の水質が
低下した場合には、その段のバルブ23を開い
て、低水質水を戻し管22によつて蒸発ゾーン5
へ流下させて、循環ブラインに合流させる。その
他の段ではバルブ23は閉じたままである。 If the quality of the produced water deteriorates in a certain stage among the many stages, the valve 23 of that stage is opened and the low quality water is returned to the evaporation zone 5 through the return pipe 22.
and join the circulating brine. In the other stages, the valve 23 remains closed.
以上のとおりで、この発明によれば、トレー4
の下面に各段の降水口15に通じる収集水路16
が設けられ、収集水路16内にこれを受水部18
と導水部19に区分する堰17が設けられ、受水
部18から蒸発ゾーン5にバルブ23付き低水質
水戻し管22が配されているので、ある段におい
て生産水の水質が低下した場合には、その段のバ
ルブ23だけを開いて低水質水を戻し管22によ
つて蒸発ゾーン5へ流下させ、循環ブラインに合
流させることができる。したがつて生産水の水質
が低下していないその他の段では、バルブ23を
閉じないで、淡水の生産を続行することができ、
そのため造水装置1全体を停止する必要がなく
て、装置の停止および再稼動による運転費のロス
をなくすることができる。 As described above, according to the present invention, the tray 4
Collection waterway 16 leading to rain outlet 15 of each stage on the bottom surface of
is provided in the collection waterway 16 and the water receiving part 18
A weir 17 is provided to divide the water into the water conveyance section 19, and a low quality water return pipe 22 with a valve 23 is arranged from the water receiving section 18 to the evaporation zone 5. In this case, only the valve 23 of that stage can be opened to allow the low quality water to flow down to the evaporation zone 5 via the return pipe 22 and join the circulating brine. Therefore, in other stages where the quality of the produced water has not deteriorated, fresh water production can be continued without closing the valve 23.
Therefore, there is no need to stop the entire freshwater generating apparatus 1, and it is possible to eliminate operating cost losses due to stopping and restarting the apparatus.
図面はこの発明の実施例を示すもので、第1図
は造水装置の平面図、第2図は第1図中の−
線に沿う中間省略拡大断面図、第3図は第2図中
の−線に沿う断面図、第4図は第2図の要部
拡大図、第5図は第4図中のV−V線に沿う断面
図、第6図は第4図中の−線に沿う断面図で
ある。
1……造水装置、2……仕切壁、3……オリフ
イス、4……トレー、5……蒸発ゾーン、6……
凝縮ゾーン、7……ミスト除去部材、8……蒸気
上昇路、9……供給口、10……排水口、11…
…海水補給口、12……支持板、13……伝熱管
束、14……小間隙、15……降水口、16……
収集水路、17……堰、18……受水部、19…
…導水部、20……通水口、21……生産水取出
口、22……低水質水戻し管、23……バルブ。
The drawings show an embodiment of the present invention, and FIG. 1 is a plan view of a freshwater generator, and FIG.
3 is an enlarged cross-sectional view along the - line in FIG. 2, FIG. 4 is an enlarged view of the main part of FIG. 2, and FIG. 6 is a sectional view taken along the line - in FIG. 4. FIG. 1... Water generator, 2... Partition wall, 3... Orifice, 4... Tray, 5... Evaporation zone, 6...
Condensation zone, 7...Mist removal member, 8...Steam rising path, 9...Supply port, 10...Drain port, 11...
... Seawater supply port, 12 ... Support plate, 13 ... Heat exchanger tube bundle, 14 ... Small gap, 15 ... Downfall port, 16 ...
Collection channel, 17... Weir, 18... Water receiving part, 19...
...Water conduction section, 20...Water inlet, 21...Produced water outlet, 22...Low quality water return pipe, 23...Valve.
Claims (1)
面に各段にわたつて降水口15に通じる収集水路
16が設けられ、収集水路16内に路長方向に堰
17が設けられて、堰17によつて収集水路16
が、降水口15からの流下水を受けて各段ごとに
溜める受水部18と、受水部18からの堰越え水
を各段の仕切壁2にあけられた通水口20を経て
生産水取出し口21へ導く導水部19とに区分せ
られ、各段において受水部18からブラインの蒸
発ゾーン5にバルブ23付き低水質水戻し管22
が配されている、造水装置における低水質生産水
の戻し装置。1. A collection waterway 16 is provided at each level on the lower surface of the condensed water receiving tray 4 having a rainwater outlet 15 and is connected to the rainwater outlet 15. A weir 17 is provided in the collection waterway 16 in the direction of the road length, and a weir 17 is provided in the weir 17. Yotsute collection waterway 16
There is a water receiving part 18 which receives the flowing water from the rain outlet 15 and collects it in each stage, and the water flowing over the weir from the water receiving part 18 is passed through the water inlet 20 made in the partition wall 2 of each stage to produce water. A low water quality water return pipe 22 with a valve 23 is connected from the water receiving part 18 to the brine evaporation zone 5 at each stage.
A return device for low-quality produced water in a water production facility, where a water generator is installed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58001590A JPS59127687A (en) | 1983-01-07 | 1983-01-07 | Return device for low-quality produced water in water production equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58001590A JPS59127687A (en) | 1983-01-07 | 1983-01-07 | Return device for low-quality produced water in water production equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59127687A JPS59127687A (en) | 1984-07-23 |
| JPS632202B2 true JPS632202B2 (en) | 1988-01-18 |
Family
ID=11505721
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58001590A Granted JPS59127687A (en) | 1983-01-07 | 1983-01-07 | Return device for low-quality produced water in water production equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59127687A (en) |
-
1983
- 1983-01-07 JP JP58001590A patent/JPS59127687A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59127687A (en) | 1984-07-23 |
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