JPH04298281A - Vacuum distillation method for fresh water - Google Patents
Vacuum distillation method for fresh waterInfo
- Publication number
- JPH04298281A JPH04298281A JP3084729A JP8472991A JPH04298281A JP H04298281 A JPH04298281 A JP H04298281A JP 3084729 A JP3084729 A JP 3084729A JP 8472991 A JP8472991 A JP 8472991A JP H04298281 A JPH04298281 A JP H04298281A
- Authority
- JP
- Japan
- Prior art keywords
- water
- steam
- vacuum
- polluted
- electric heating
- 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.)
- Pending
Links
- 239000013505 freshwater Substances 0.000 title claims abstract description 16
- 238000000034 method Methods 0.000 title claims description 5
- 238000005292 vacuum distillation Methods 0.000 title description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 42
- 239000013535 sea water Substances 0.000 claims abstract description 18
- 238000005485 electric heating Methods 0.000 claims abstract description 9
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000012535 impurity Substances 0.000 claims abstract description 7
- 239000003456 ion exchange resin Substances 0.000 claims abstract description 7
- 229920003303 ion-exchange polymer Polymers 0.000 claims abstract description 7
- 229910021642 ultra pure water Inorganic materials 0.000 claims abstract description 7
- 239000012498 ultrapure water Substances 0.000 claims abstract description 7
- 238000001816 cooling Methods 0.000 claims abstract description 4
- 238000010438 heat treatment Methods 0.000 claims abstract description 4
- 238000009835 boiling Methods 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 2
- 238000004140 cleaning Methods 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 239000008399 tap water Substances 0.000 description 1
- 235000020679 tap water Nutrition 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
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
- Y02A20/20—Controlling water pollution; Waste water treatment
- Y02A20/208—Off-grid powered water treatment
- Y02A20/212—Solar-powered wastewater sewage treatment, e.g. spray evaporation
Landscapes
- Treatment Of Water By Ion Exchange (AREA)
- Heat Treatment Of Water, Waste Water Or Sewage (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】海水、汚濁水を真水にするよう考
えた真水真空蒸留法である。[Industrial Application Field] This is a fresh water vacuum distillation method designed to turn seawater or polluted water into fresh water.
【0002】0002
【従来の技術】揚水手段(2)によって揚水された地下
水を通水し昇温するための日照エネルギー吸収パイプ(
9)と、該パイプ(9)から流出する昇温水を減圧下に
蒸発させる蒸発機(10)と、該蒸発機で発生した蒸気
を冷却し凝縮水として回収する凝縮回収機(15)とを
具備してなる造水装置。[Prior Art] A solar energy absorbing pipe (
9), an evaporator (10) that evaporates heated water flowing out from the pipe (9) under reduced pressure, and a condensation recovery machine (15) that cools the steam generated in the evaporator and recovers it as condensed water. A water production device equipped with
【0003】0003
【発明が解決しようとする課題】しかしながら「造水装
置」は発生水量が少なく小型であるが本発明は連続的に
水量を多く発生しうるようにしたもっと大規模なもので
井戸水ではなく海水、汚濁水を対象としたことに特色が
あり、真水真空蒸留法は大型にも小型にもでき、小型で
も水道水以上の量の水を生成しうる。太陽の当りにくい
所でも電熱板で水を生成しうる。特に寒冷地においては
その効果は大きい。真空近くになると水の沸点が急激に
下がるしなお高温にすると瞬間的に蒸発することを利用
し、海水、汚濁水を真水にするよう発明したものである
。[Problems to be Solved by the Invention] However, the "water generator" is small in size and generates a small amount of water, but the present invention is a larger scale device that can continuously generate a large amount of water, and uses seawater instead of well water. It is unique in that it targets polluted water, and the fresh water vacuum distillation method can be used in both large and small scales, and even small scales can produce more water than tap water. Water can be generated using electric heating plates even in places where sunlight is hard to reach. The effect is particularly great in cold regions. It was invented to turn seawater or polluted water into fresh water by taking advantage of the fact that the boiling point of water drops rapidly when the temperature is close to a vacuum, and when the temperature is raised it evaporates instantaneously.
【0004】0004
【課題を解決するための手段】給水ポンプより吸い上げ
た、海水、汚濁水を脱気器で海水、汚濁水に混入する空
気を除き、脱気した海水、汚濁水を胴内に入れ胴内を真
空近くし、太陽熱吸収板や電熱板により熱することによ
り、沸点が下がっているので瞬間的に水蒸気とすること
ができ、真空ポンプで吸い上げ、蒸気溜にて蒸気をため
そして冷却器で冷却し、水に混入した不純物をとり除く
ため、イオン交換樹脂を通して真水を得る。[Means for solving the problem] The seawater and polluted water sucked up by the water supply pump are removed by a deaerator to remove air mixed in the seawater and polluted water, and the deaerated seawater and polluted water are put into the shell and the inside of the shell is removed. By placing it near a vacuum and heating it with a solar heat absorbing plate or electric heating plate, the boiling point has been lowered, so it can be instantly turned into water vapor, which is sucked up with a vacuum pump, stored in a steam reservoir, and cooled with a cooler. In order to remove impurities mixed into the water, fresh water is obtained by passing it through an ion exchange resin.
【0005】[0005]
【作用】真空近く(0.042気圧)では海水は30℃
で沸騰するので、同じ気圧で60℃に設定すると、海水
、汚濁水は瞬間沸騰しその水蒸気を真空ポンプで吸収し
、蒸気溜で蒸気をため冷却器で10℃くらいまで下げ水
を得る。不純物を除くためイオン交換樹脂をとおすと真
水が得られる。利用法としては海水、汚濁水の真水化L
SIの洗浄工程で大量の超純水がいるがこれにも利用で
きる。[Effect] Seawater is 30℃ near vacuum (0.042 atm)
Therefore, if the temperature is set at 60°C at the same atmospheric pressure, seawater or polluted water will boil instantaneously, the water vapor will be absorbed by a vacuum pump, the steam will be stored in a steam reservoir, and the temperature will be lowered to about 10°C by a cooler to obtain water. Fresh water is obtained by passing it through an ion exchange resin to remove impurities. How to use it is to turn seawater and polluted water into fresh water.
The SI cleaning process requires a large amount of ultrapure water, which can also be used.
【0006】[0006]
【実施例】給水ポンプ1より吸い上げた海水、汚濁水を
脱気器2で海水、汚濁水に混入する空気を除き、脱気し
た海水、汚濁水を胴内に入れ真空近く(約0.042気
圧)近くにし太陽熱吸収板3や電熱板8により60℃に
熱することにより、沸点が下がっているので瞬間的に水
蒸気とすることができ、真空ポンプ4で吸い上げ連続的
に水を出すため蒸気溜5に蒸気をため、冷却器6で冷却
し(10℃)水に混入した不純物を取り除くためイオン
交換樹脂7を通すと真水(超純水)が得られる。なお海
水、汚濁水には不純物が混入して残留物が溜るのでドレ
ンコック10を設けてある。そして電熱板は温度を55
〜65℃にセットし自動制御する。[Example] The seawater and polluted water sucked up by the water supply pump 1 are removed by the deaerator 2, and the air mixed in the seawater and polluted water is removed. By heating it to 60°C using the solar heat absorbing plate 3 or electric heating plate 8 near the barometric pressure, the boiling point has been lowered, so it can be instantly converted to water vapor, which is then sucked up by the vacuum pump 4 and continuously released as steam. Fresh water (ultrapure water) is obtained by storing steam in a reservoir 5, cooling it with a cooler 6 (to 10° C.), and passing it through an ion exchange resin 7 to remove impurities mixed in the water. A drain cock 10 is provided since impurities are mixed into seawater and polluted water and residue accumulates therein. And the electric heating board has a temperature of 55
Set to ~65°C and automatically control.
【0007】[0007]
【発明の効果】本発明によって小型でも大型でも容易に
海水や汚濁水を多量に真水(超純水)化しうる点であり
、その他利用価値は多い。[Effects of the Invention] The present invention allows a large amount of seawater or polluted water to be easily converted into fresh water (ultra-pure water) regardless of whether it is small or large, and has many other utility values.
【図1】真横から見た断面図。FIG. 1 is a sectional view seen from the side.
【図2】真上から見た平面図。FIG. 2 is a plan view seen from directly above.
【図3】従来の海水から淡水生成装置断面図。FIG. 3 is a cross-sectional view of a conventional seawater to freshwater generator.
1 給水ポンプ 2 脱気器 3 太陽熱吸収板 4 真空ポンプ 5 蒸気溜 6 冷却器 7 イオン交換樹脂 8 電熱板 9 真水貯水槽 10 ドレンコック 11 温度計 12 真空圧力計 1 Water supply pump 2 Deaerator 3. Solar heat absorption plate 4 Vacuum pump 5 Steam reservoir 6 Cooler 7 Ion exchange resin 8 Electric heating board 9 Fresh water storage tank 10 Drain cock 11 Thermometer 12 Vacuum pressure gauge
Claims (1)
取り出す方法であるが、まず給水ポンプで水を吸いあげ
、脱気器で脱気した海水、又は汚濁水を胴内へいれ胴内
を真空近くにし、太陽熱吸収板及び電熱板により熱する
ことにより、高温にし、沸点が下がっているので瞬間的
に蒸発させることができ、その水蒸気を真空ポンプで吸
い取り蒸気溜に蒸気をため冷却器におくり冷却しイオン
交換樹脂で水に混入した不純物を取り除くと真水(超純
水)が得られる。海水、又は汚濁水は蒸発すると残留物
(ドレン)が残るが電熱板の桁を上げドレンの排出も出
来るようになっている。Claim 1: This is a method for extracting fresh water (ultra-pure water) from seawater or polluted water. By making the interior near a vacuum and heating it with a solar heat absorption plate and an electric heating plate, it becomes high temperature, and since the boiling point has been lowered, it can be evaporated instantly, and the water vapor is sucked up with a vacuum pump and stored in a steam reservoir for cooling. Fresh water (ultrapure water) can be obtained by cooling the water in a container and removing impurities mixed in with ion exchange resin. When seawater or polluted water evaporates, a residue (drainage) remains, but the electric heating plate can be raised to allow the drainage to be discharged.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3084729A JPH04298281A (en) | 1991-03-25 | 1991-03-25 | Vacuum distillation method for fresh water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3084729A JPH04298281A (en) | 1991-03-25 | 1991-03-25 | Vacuum distillation method for fresh water |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04298281A true JPH04298281A (en) | 1992-10-22 |
Family
ID=13838781
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3084729A Pending JPH04298281A (en) | 1991-03-25 | 1991-03-25 | Vacuum distillation method for fresh water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04298281A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011025119A (en) * | 2009-07-23 | 2011-02-10 | Michihiro Oe | Fresh water production device and fresh water production-power generation device |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60190298A (en) * | 1984-03-09 | 1985-09-27 | Ebara Infilco Co Ltd | Preparation of ultra-pure water |
JPS61291092A (en) * | 1985-06-15 | 1986-12-20 | Kyokuto Kikai Seisakusho:Kk | Apparatus for desalting sea water |
JPS62186983A (en) * | 1986-02-04 | 1987-08-15 | ヘンリ− シ−.ラサタ− | Water purifier |
-
1991
- 1991-03-25 JP JP3084729A patent/JPH04298281A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS60190298A (en) * | 1984-03-09 | 1985-09-27 | Ebara Infilco Co Ltd | Preparation of ultra-pure water |
JPS61291092A (en) * | 1985-06-15 | 1986-12-20 | Kyokuto Kikai Seisakusho:Kk | Apparatus for desalting sea water |
JPS62186983A (en) * | 1986-02-04 | 1987-08-15 | ヘンリ− シ−.ラサタ− | Water purifier |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011025119A (en) * | 2009-07-23 | 2011-02-10 | Michihiro Oe | Fresh water production device and fresh water production-power generation device |
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