JPS6038081A - Flash evaporation type water distilling apparatus - Google Patents
Flash evaporation type water distilling apparatusInfo
- Publication number
- JPS6038081A JPS6038081A JP14598983A JP14598983A JPS6038081A JP S6038081 A JPS6038081 A JP S6038081A JP 14598983 A JP14598983 A JP 14598983A JP 14598983 A JP14598983 A JP 14598983A JP S6038081 A JPS6038081 A JP S6038081A
- Authority
- JP
- Japan
- Prior art keywords
- demister
- splash
- flash
- folded plates
- chamber
- 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.)
- Granted
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/06—Flash distillation
- B01D3/065—Multiple-effect flash distillation (more than two traps)
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
【発明の詳細な説明】 本発明はフラッシュ蒸発型造水装置に関し。[Detailed description of the invention] The present invention relates to a flash evaporation type water generator.
特に該装置におけるスプラ・νソユの防止を図る技術の
改良に関する。In particular, the present invention relates to improvements in techniques for preventing splatter and v-soil in the apparatus.
第1図は従来の多段フラッシュ蒸発型造水装置の1部所
面図を示す。FIG. 1 shows a partial plan view of a conventional multi-stage flash evaporation type fresh water generator.
第1図において、1はオリフィス、2は堰。In Figure 1, 1 is an orifice and 2 is a weir.
3はフラッシュ室、4はワイヤメツシュ型のデミスタ、
5はコンデンサ室、qはトレイ、7番オスプラッシュ防
止板、9は隔壁、10は底板、11は伝熱管、12はオ
リフィス調整板を示す。しかして、オリフィス1より導
入されたブラインは噴出し、フラッシュ室3内にてフラ
ッシュ蒸発し、蒸発したフラッシュ蒸気(矢印)はデミ
スタ4を経て、コンデンサ室5内にて凝縮されて淡水と
なりトレイ6に集められ外部に取り出さ′れる。3 is a flash chamber, 4 is a wire mesh type demister,
5 is a condenser chamber, q is a tray, 7 is a male splash prevention plate, 9 is a partition, 10 is a bottom plate, 11 is a heat exchanger tube, and 12 is an orifice adjustment plate. As a result, the brine introduced from the orifice 1 is ejected and flash-evaporated in the flash chamber 3, and the evaporated flash vapor (arrow) passes through the demister 4 and is condensed in the condenser chamber 5 to become fresh water in the tray 6. is collected and taken out to the outside.
しかし、上述した従来の多段フラッシュ蒸発型遣水装置
では、ブラインがオリフィス1より噴出した時に発生す
るスプラッシュ(飛散ミスト)がフラッシュ蒸気流に同
伴され、スプラツシユかデミスタ4に到達してデミスタ
4に付着し、デミスタ4の蒸気流通効率を低下せしめる
とともに、さらにコンデンサ室5にいたり、製造淡水の
水質低下をまねく等の欠点があった。However, in the above-mentioned conventional multi-stage flash evaporation type water supply system, the splash (dispersed mist) generated when the brine is ejected from the orifice 1 is entrained in the flash steam flow, reaches the demister 4, and adheres to the demister 4. This has drawbacks such as lowering the efficiency of steam flow through the demister 4, and further causing the steam to flow into the condenser chamber 5, leading to a deterioration in the quality of the produced fresh water.
そこで、従来はフラッシュ室3の股間絞りオリフィス1
部とデミスタ4の間に、スプラッシュを遮断するための
スプラツシユ防止板7を設けてこれらの不具合を解消す
るように図っていた。しかし従来のスプラッシュ防止板
7では。Therefore, conventionally, the crotch throttle orifice 1 of the flash chamber 3
In order to solve these problems, a splash prevention plate 7 was provided between the demister 4 and the demister 4 to block the splash. However, with the conventional splash prevention plate 7.
衝突したミストの一部が再飛散して蒸気の流れに同伴さ
れ、デミスタ4に到達することかありスプラッシュの遮
断がまだ十分に行なえず従来装置の不具合は依然として
残っていた。Part of the collided mist may be re-splattered and carried along with the steam flow, reaching the demister 4, so that the splash cannot be blocked sufficiently, and the problems of the conventional device still remain.
本発明は、上述した従来装置の不具合を解消すべく、ス
プラッシュ防止板に衝突し、その後再飛散したスプラッ
シュを捕捉してその重力落下を促がして、スプラッシュ
のデミスタへの付着およびコンデンサ室への混入を防止
することを提案するものである。In order to solve the above-mentioned problems of the conventional device, the present invention captures the splash that collides with the splash prevention plate and is then re-splattered, and accelerates its fall due to gravity, so that the splash adheres to the demister and flows into the condenser chamber. This is a proposal to prevent the contamination of
以下1本発明を第2図ないし第5図に基づき説明する。The present invention will be explained below with reference to FIGS. 2 to 5.
第2図ないし第4図において、8は本発明の1実施例で
ある折板を示し、折板8はデミスタ4の下部に相互に間
隔をおいて平行に並設されている。In FIGS. 2 to 4, reference numeral 8 indicates a folded plate according to an embodiment of the present invention, and the folded plates 8 are arranged in parallel at a distance from each other below the demister 4.
なお、第2図中において第1図と同様の符号で示すもの
は同じ構造であることを示し、折板しかして、オリフィ
ス1を通過して減圧されたフラッシュ室3内に流入した
高温ブラインはフラッシュ蒸発する。この時発生したス
プラッシュは、高温段はど激しく、約500〜1000
μmの大粒径の液滴がデミスタ4取伺位置まで到達する
。このスプラッシュ量が多い場合、一旦デミスタ4に捕
捉されたスプラッシュ(液M)が十分滴下回収されずに
再び蒸気に同伴されてコンデンサ室5に持ち込まれ、そ
の結果製造水の純度を低下させるという好ましくない状
態となる。Note that in FIG. 2, the same symbols as in FIG. Flash evaporates. The splash that occurred at this time was very violent on the high temperature stage, and the splash was approximately 500 to 1000.
The droplets with a large particle diameter of μm reach the demister 4 pick-up position. If the amount of this splash is large, the splash (liquid M) once captured by the demister 4 will not be sufficiently dripped and collected and will be carried into the condenser chamber 5 again along with the steam, resulting in a decrease in the purity of the produced water. There will be no.
ところが1本発明の構造の場合、飛来したスプラッシュ
は一旦折板8に衝突し、折板8壁面上で凝集して更に大
粒径の液滴となり、下方から上昇する蒸気流れに打勝っ
てフラッシュ室3内下部の蒸発液面へ自然落下する。However, in the case of the structure of the present invention, the flying splash once collides with the folded plate 8, aggregates on the wall surface of the folded plate 8, becomes larger droplets, overcomes the vapor flow rising from below, and flashes. It naturally falls to the evaporated liquid level in the lower part of chamber 3.
第2図に示すように、スプラッシュの発生はオリフィス
1と堰2の間で大半が生じ、水平面とスプラッシュの飛
散方向とのなす角度αが約20〜90度のものが一般に
デミスタ4へ到達する。As shown in Fig. 2, most of the splash occurs between the orifice 1 and the weir 2, and the splash that forms an angle α between the horizontal plane and the scattering direction of approximately 20 to 90 degrees generally reaches the demister 4. .
従って、折板8が単に平板の場合には、平板間を通過す
るスプラッシュか生じる。従って、折板の角度βは90
度以下が好ましい。Therefore, if the folded plates 8 are simply flat plates, splashes will occur that pass between the flat plates. Therefore, the angle β of the folded plate is 90
degree or less is preferable.
また、隣接する折板8の間隔が広い場合には。Moreover, when the interval between adjacent folded plates 8 is wide.
折板8の間隔をぬって飛散するスプラッシ−75(生じ
る。そこで、折板8の下端と折板8の凸部との間隔d
(第4図参照)は大きい方が良いが。Splash 75 (generates) that scatters across the intervals between the folded plates 8. Therefore, the distance d between the lower end of the folded plates 8 and the convex portion of the folded plates 8
(See Figure 4) The larger the value, the better.
あまり大きすぎると折板8の枚数が多くなってコストア
ップとなり、更に折板8間を通過する蒸気の圧損を大き
くする不具合を生じる。If it is too large, the number of folded plates 8 will increase, resulting in an increase in cost, and will also cause problems such as increasing the pressure loss of steam passing between the folded plates 8.
第1図及び第2図の構造の装置を使用して。Using an apparatus of the structure of FIGS. 1 and 2.
本発明の効果を確認した結果を第5図に示す。The results of confirming the effects of the present invention are shown in FIG.
(1)実施条件
(al ブライン温度 55℃
(bl 蒸気温度 52.2℃
Ic) 圧力 0.14 kg/ C#LA+dl デ
ミスタ通過ガス流速 9.4 m / 5(2)結 果
デミスタ通過後の蒸気中の重量平均ミスト粒径が減小し
ている仁とが明確であり2本発明の効果が確認できた。(1) Implementation conditions (al Brine temperature 55℃ (bl Steam temperature 52.2℃ Ic) Pressure 0.14 kg/C#LA+dl Gas flow rate passing through demister 9.4 m/5 (2) Results Steam after passing through demister It was clear that the weight-average mist particle size was decreasing, confirming the effects of the present invention.
以上、実施例で説明したように、デミスタを有するフラ
ッシュ蒸発型造水装置において、デミスタ下部に多数の
折板を配置することにより。As described above in the embodiments, in a flash evaporation type fresh water generating apparatus having a demister, a large number of folded plates are arranged below the demister.
フラッシュ蒸発で生じるスプラッシュの大半をデミスタ
通過蒸気中から分離除去でき、製造水品質を大幅に向上
することができる。Most of the splash generated by flash evaporation can be separated and removed from the vapor passing through the demister, significantly improving the quality of produced water.
また2本発明の効果はコンデンサ室形状が丸型の場合に
特に大きい。Further, the effects of the present invention are particularly large when the shape of the condenser chamber is round.
第1図は丸型形状のコンデンサ室を有する従来の遣水装
置の1部所面図、第2図は本発明を説明する断面図、第
3図は折板の斜視図、第4図は折板の正面図、第5図は
従来と本発明の装置を使用した運転の実施側番と基づく
スプラッシュ粒径のグラフである。
3、フラッシュ室、9.隔壁、2:堰、10:底板、4
.デミスタ、1ニオリフイス、8:折板。
第1図
勇2園
第5図
スプラッシュ(ミズト)粒イ昼明筑〕Fig. 1 is a partial plan view of a conventional water supply device having a round-shaped condenser chamber, Fig. 2 is a sectional view illustrating the present invention, Fig. 3 is a perspective view of a folded plate, and Fig. 4 is a folded plate. FIG. 5, a front view of the plate, is a graph of splash particle size based on run number of runs using conventional and inventive apparatus. 3. Flash chamber, 9. Partition wall, 2: Weir, 10: Bottom plate, 4
.. Demister, 1 niorifice, 8: folded plate. Figure 1 Yuu 2 Garden Figure 5 Splash (Mizuto) grains Hiruakichiku]
Claims (1)
サ室とを連通ずる蒸気流路に設けたデミスタの下部に、
多数の折板を相互に間隔をおいて平行に並設したことを
特徴とするフラ・ンンユ蒸発型造水装置。At the bottom of the demister installed in the steam flow path that communicates the flash chamber and condenser chamber of the flash evaporation type fresh water generator,
A Hula Nyu evaporative water generation device characterized by a large number of folded plates arranged in parallel at intervals.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14598983A JPS6038081A (en) | 1983-08-10 | 1983-08-10 | Flash evaporation type water distilling apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP14598983A JPS6038081A (en) | 1983-08-10 | 1983-08-10 | Flash evaporation type water distilling apparatus |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6038081A true JPS6038081A (en) | 1985-02-27 |
JPH0225673B2 JPH0225673B2 (en) | 1990-06-05 |
Family
ID=15397602
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP14598983A Granted JPS6038081A (en) | 1983-08-10 | 1983-08-10 | Flash evaporation type water distilling apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6038081A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61150001U (en) * | 1985-03-06 | 1986-09-17 | ||
JPS6364031U (en) * | 1986-10-16 | 1988-04-27 |
-
1983
- 1983-08-10 JP JP14598983A patent/JPS6038081A/en active Granted
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61150001U (en) * | 1985-03-06 | 1986-09-17 | ||
JPS6364031U (en) * | 1986-10-16 | 1988-04-27 |
Also Published As
Publication number | Publication date |
---|---|
JPH0225673B2 (en) | 1990-06-05 |
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