JPH04250231A - Fresh water generator - Google Patents

Fresh water generator

Info

Publication number
JPH04250231A
JPH04250231A JP3006445A JP644591A JPH04250231A JP H04250231 A JPH04250231 A JP H04250231A JP 3006445 A JP3006445 A JP 3006445A JP 644591 A JP644591 A JP 644591A JP H04250231 A JPH04250231 A JP H04250231A
Authority
JP
Japan
Prior art keywords
water
atmospheric
air
taken
atmospheric pressure
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
Application number
JP3006445A
Other languages
Japanese (ja)
Other versions
JPH0711151B2 (en
Inventor
Toshio Hanya
半谷 利夫
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
DAIKA SANGYO YUGEN
Original Assignee
DAIKA SANGYO YUGEN
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by DAIKA SANGYO YUGEN filed Critical DAIKA SANGYO YUGEN
Priority to JP3006445A priority Critical patent/JPH0711151B2/en
Publication of JPH04250231A publication Critical patent/JPH04250231A/en
Publication of JPH0711151B2 publication Critical patent/JPH0711151B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To provide water easily and surely at a low cost at any place though the constitution is simple. CONSTITUTION:A fresh water generator is provided with an air suction device 2 and a mechanism 4 for decreasing the atmospheric pressure of air taken by the air suction device 2. An air humidity converter 1 incorporates a cooling portion 5 which takes out humidity by cooling the air taken. The water obtained by the air humidity converter 1 is taken out from an intake pipe 7.

Description

【発明の詳細な説明】[Detailed description of the invention]

【0001】0001

【産業上の利用分野】本発明は造水装置に関し、詳しく
は大気中の湿分を採取する造水装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water generator, and more particularly to a water generator that extracts moisture from the atmosphere.

【0002】0002

【従来の技術】近年における水利用の増大から、種々の
造水装置が開発されてきた。例えば、海水淡水化といっ
た目的には、古くからある蒸留法に代わって、より効率
の高い、逆浸透膜を利用した装置や限外濾過法を利用し
た装置等が開発されてきた。なかでも、エネルギー的に
有利な面が多いことから逆浸透膜を利用した装置が注目
され、実用機の開発がなされるに至っている。
BACKGROUND OF THE INVENTION Due to the increased use of water in recent years, various water generating devices have been developed. For example, for purposes such as seawater desalination, more efficient devices using reverse osmosis membranes and ultrafiltration methods have been developed to replace the old distillation method. Among these, devices using reverse osmosis membranes have attracted attention because of their many energy advantages, and practical devices have been developed.

【0003】0003

【発明が解決しようとする課題】しかしながら、上記従
来の装置、例えば逆浸透膜を利用した装置では、膜自体
が高価であることと、膜の寿命がそれほど長くないこと
と相まって装置全体のコストが高いという問題があった
。しかも、膜の劣化を直接的に感知する方法がなく、生
成される淡水の水質を常時検査する必要があった。そこ
で、上記従来技術の有する問題点を解決するため、本発
明は、高価な逆浸透膜を利用することなく、従って、安
価で簡易に水、特に淡水を製造することの可能な造水装
置を提供することを目的とする。
[Problems to be Solved by the Invention] However, in the above-mentioned conventional devices, such as devices using reverse osmosis membranes, the cost of the entire device is high due to the fact that the membrane itself is expensive and the lifespan of the membrane is not very long. The problem was that it was expensive. Moreover, there was no way to directly detect membrane deterioration, and the quality of the fresh water produced had to be constantly tested. Therefore, in order to solve the problems of the above-mentioned conventional technology, the present invention provides a water generation device that can easily produce water, especially fresh water, at low cost without using an expensive reverse osmosis membrane. The purpose is to provide.

【0004】0004

【課題を解決するための手段】上記目的を達成するため
、本発明の造水装置の特徴構成は、大気吸引装置と、こ
の大気吸引装置によって取入れられる大気圧力を低減す
る機構を備えると共に取入れられた大気を冷却して湿分
を取出す冷却部を内蔵した大気湿度変換機と、この大気
湿度変換機によって得られる水を取出す取水口とからな
る点にある。加えて、前記大気圧力低減機構が大気取入
れ口に設けられた多孔質通気体で構成されていると好ま
しい。更に、前記大気湿度変換機と取水口との間に殺菌
装置を備えると飲料水採取用として使用できて好ましい
[Means for Solving the Problems] In order to achieve the above object, the characteristic configuration of the fresh water generation device of the present invention includes an atmospheric suction device and a mechanism for reducing the atmospheric pressure taken in by the atmospheric suction device. It consists of an atmospheric humidity converter that has a built-in cooling unit that cools the atmospheric air and extracts moisture, and a water intake that takes out the water obtained by the atmospheric humidity converter. In addition, it is preferable that the atmospheric pressure reduction mechanism is constituted by a porous vent provided in the atmospheric air intake. Furthermore, it is preferable to provide a sterilizer between the atmospheric humidity converter and the water intake, since it can be used for collecting drinking water.

【0005】[0005]

【作用】次に、本発明にかかる造水装置の作用・効果を
説明する。本発明の造水装置が上記構成となっているの
で、大気吸引装置を駆動することにより、大量の大気を
装置内部に取入れ、その時の大気の湿分に応じた量の水
を凝縮させて取出すことができる。従って、高価な逆浸
透膜を用いることがないので、装置コストが安く、かつ
水質検査を行う必要もない。しかも、得られる水は比較
的純度が高く、利用するのに好ましいので、利用範囲は
極めて広いものとなる。
[Function] Next, the function and effect of the freshwater generating device according to the present invention will be explained. Since the water generating device of the present invention has the above configuration, by driving the atmospheric suction device, a large amount of atmospheric air is taken into the device, and an amount of water corresponding to the humidity of the atmospheric air at that time is condensed and taken out. be able to. Therefore, since there is no need to use an expensive reverse osmosis membrane, the equipment cost is low and there is no need to conduct a water quality test. Moreover, the obtained water has relatively high purity and is preferable for use, so the range of use is extremely wide.

【0006】更に、大気圧力低減機構を大気取入れ口に
設けられた多孔質通気体で構成するようにすると、低コ
ストで効果的に目的を達成できて一層好ましい。この場
合、大気中の塵芥を除くこともできるので、より清浄な
水が得られると共に、装置自体の耐久性が向上する利点
がある。尚、大気圧力は6kgf/cm2以下、より好
ましくは3kgf/cm2以下に低減することが取水効
率を高める上で好ましい。つまり、単位時間当り得られ
る水量を多くするためには、取入れる大気量を出来るだ
け多くすることが好ましいが、取入れる大気量が多くな
れば大気圧力も大きくならざるを得ず、大気圧力が大き
くなれば、図2に示すように、残留する湿分は少なくな
り、得られる湿分も少なくなって効率的でなくなるから
である。因に、図2は、100m3の飽和大気を760
mmHgより圧縮したときの、等温圧縮された飽和大気
中に残留する湿分を表す図である。そこで、本発明者は
、大気吸引装置で大量の大気を取入れるものでありなが
ら、効率よく造水するために大気圧力を低減する装置を
備える構成とすることが効果的であることを見出して、
本発明を完成したものである。大気湿度変換機と取水口
との間に殺菌装置を備えると、得られた水を飲料水に使
用できるのみならず、精密部品の洗浄水等とくに清浄な
水が要求される用途に使用できる。
[0006] Furthermore, it is more preferable that the atmospheric pressure reduction mechanism is constituted by a porous ventilation body provided at the air intake, since the purpose can be effectively achieved at low cost. In this case, since dust in the atmosphere can be removed, cleaner water can be obtained and the durability of the device itself can be improved. Note that it is preferable to reduce the atmospheric pressure to 6 kgf/cm2 or less, more preferably 3 kgf/cm2 or less, in order to increase water intake efficiency. In other words, in order to increase the amount of water obtained per unit time, it is preferable to take in as much air as possible, but as the amount of air taken in increases, the atmospheric pressure must also increase. This is because if the size increases, as shown in FIG. 2, the amount of remaining moisture will decrease, and the amount of moisture obtained will also decrease, making it less efficient. Incidentally, Figure 2 shows that 100 m3 of saturated air is
It is a figure showing the moisture remaining in the isothermally compressed saturated atmosphere when compressed from mmHg. Therefore, the inventors of the present invention have found that it is effective to adopt a configuration in which an atmospheric suction device takes in a large amount of atmospheric air, but also includes a device that reduces atmospheric pressure in order to efficiently produce water. ,
This completes the present invention. If a sterilizer is provided between the atmospheric humidity converter and the water intake, the obtained water can not only be used for drinking, but also for applications that require particularly clean water, such as water for washing precision parts.

【0007】[0007]

【発明の効果】以上のように、本発明によれば、簡単な
構成であるにも拘らず、場所を選ぶことなく安価に、か
つ容易確実に水を得ることのできる造水装置を提供する
ことができた。
[Effects of the Invention] As described above, according to the present invention, there is provided a water generating device that can obtain water easily and reliably at a low cost, regardless of the location, despite its simple configuration. I was able to do that.

【0008】[0008]

【実施例】本発明にかかる造水装置の実施例を、図面を
参照して詳細に説明する。図1は、飲料水を得るための
造水装置の全体構造を示し、この装置は、大気湿度変換
機1に大量の大気を取入れるための大気吸引装置たる吸
引ポンプ2と、取入れた大気中の湿分を取出すための大
気湿度変換機1と、この大気湿度変換機1に取入れられ
た大気を冷却する冷媒を送込む冷却機構3とからなって
いる。この内、大気湿度変換機1は、吸引ポンプ2から
取入れられた大量の大気から効率よく湿分を取出すため
に大気圧力を低減するための大気圧力低減機構たる多孔
質通気体4と、冷却機構3からの冷却部5と、冷却され
凝縮された水を殺菌する殺菌装置6と、殺菌された水を
採取するための取水口7と、取入れた空気を排出する空
気排出口8とから構成されている。  又、冷却機構3
は、一般に用いられている冷却装置をそのまま使用する
ことができ、例えば、冷媒を圧縮する圧縮器9と凝縮器
10と減圧機構(図示せず)と冷熱を蓄熱する蓄熱槽(
図示せず)等とからなっていて、冷熱を有する冷媒を、
配管11を介して大気湿度変換機1の冷却部5に搬送す
るようになっている。これによって、取入れられた大量
の大気を効果的に凝縮して、水を得ることができるので
ある。尚、冷媒としては、フレオン、水等種々のものを
使用することができる。得られた水は飲料用に供するた
め、更に、殺菌装置6に送られて、殺菌され取水される
こととなる。もっとも、得られた水を飲料用に供するの
でなければ、必ずしも殺菌装置6を設けておく必要はな
い。要は、目的に応じて必要設備を組合せるようにすれ
ばよい。
[Embodiment] An embodiment of the freshwater generating apparatus according to the present invention will be described in detail with reference to the drawings. Figure 1 shows the overall structure of a water production system for obtaining drinking water. The air humidity converter 1 consists of an atmospheric humidity converter 1 for extracting moisture, and a cooling mechanism 3 for feeding a refrigerant to cool the air taken into the atmospheric humidity converter 1. Among these, the atmospheric humidity converter 1 includes a porous ventilation body 4 which is an atmospheric pressure reduction mechanism for reducing atmospheric pressure in order to efficiently extract moisture from a large amount of atmospheric air taken in from a suction pump 2, and a cooling mechanism. 3, a sterilizer 6 for sterilizing the cooled and condensed water, a water intake 7 for collecting the sterilized water, and an air outlet 8 for discharging the taken air. ing. Also, the cooling mechanism 3
A commonly used cooling device can be used as is, for example, a compressor 9 that compresses the refrigerant, a condenser 10, a pressure reduction mechanism (not shown), and a heat storage tank (not shown) that stores cold heat.
(not shown), etc., and the refrigerant has cold energy.
It is conveyed to the cooling section 5 of the atmospheric humidity converter 1 via a pipe 11. This allows the large amount of air taken in to be effectively condensed to yield water. Note that various refrigerants such as freon and water can be used as the refrigerant. Since the obtained water is to be used for drinking, it is further sent to a sterilizer 6, where it is sterilized and taken. However, unless the obtained water is to be used for drinking, it is not necessarily necessary to provide the sterilizer 6. The key is to combine the necessary equipment according to the purpose.

【0009】次に、本発明装置によって得られた結果を
示す。 (実験例)室温が30℃で相対湿度90%の大気中にお
いて、大気吸引ポンプ(吸引能:1時間当り0.1m3
)を長時間運転した。尚、このときの大気圧縮比は2k
gf/cm2であった。その結果、平均9.5cc/m
3の水が得られた。この値は、ほぼ理論値に近いもので
あった。因に、上記条件下での理論値は、第2図を参照
して30℃で相対湿度100%の場合、大気圧縮比2k
gf/cm2中の湿分は約11cc/m3であるから、
同温度で相対湿度90%の水蒸気量は、11×0.9=
9.9cc/m3となる。上記実施例では、飲料用水を
得るように構成したが、得られた水を各種冷却水等の工
業用水として使用することは自由である。又、大気圧力
を低減するための多孔質通気体4としては、市販の各種
エアフィルター等を用いることができる。多孔質通気体
の代わりに、大気取入れ通路に邪魔板を多数配置するよ
うに構成してもよく、オリフィスのような構成としても
よい。 要は、取入れる大気圧力を低減するために、圧損を大き
くできる構成であればよい。前記多孔質通気体が多孔質
焼結材のようなものでもよいし、繊維を密に絡めた集合
体のようなもので構成されていてもよい。大気圧力低減
機構が、取入れた大気をらせん管のような細長い通路を
通過させた後、体積の大きな室に導入することにより大
気圧力を低減させるようにしたものであってもよい。 又、取入れられた大量の大気を効果的に凝縮させるため
、露結を容易にさせる触媒作用を備えた凝縮剤のような
ものを添加してもよい。更に、大気を冷却して取水した
後は外部に逃がす大気中の湿分をできるだけ少なくする
ために、出口部分の大気圧力を高めるように出口の大き
さを小さく絞るようにしてもよい。
Next, the results obtained using the apparatus of the present invention will be shown. (Experiment example) In an atmosphere with a room temperature of 30°C and a relative humidity of 90%, an atmospheric suction pump (suction capacity: 0.1 m3 per hour)
) was driven for a long time. In addition, the atmospheric compression ratio at this time is 2k
gf/cm2. As a result, the average was 9.5cc/m
3 of water was obtained. This value was almost close to the theoretical value. Incidentally, the theoretical value under the above conditions is, as shown in Figure 2, at 30°C and 100% relative humidity, the atmospheric compression ratio is 2k.
Since the moisture content in gf/cm2 is approximately 11cc/m3,
The amount of water vapor at the same temperature and relative humidity of 90% is 11 x 0.9 =
It becomes 9.9cc/m3. Although the above embodiment is configured to obtain drinking water, the obtained water can be freely used as industrial water such as various types of cooling water. Moreover, as the porous ventilation body 4 for reducing atmospheric pressure, various commercially available air filters and the like can be used. Instead of the porous ventilation body, a large number of baffle plates may be arranged in the air intake passage, or an orifice-like structure may be used. In short, any configuration that can increase pressure loss is sufficient in order to reduce the atmospheric pressure taken in. The porous ventilation body may be made of a porous sintered material or may be made of an aggregate of tightly entangled fibers. The atmospheric pressure reduction mechanism may reduce the atmospheric pressure by passing the taken-in atmospheric air through an elongated passage such as a spiral tube and then introducing it into a large-volume chamber. Also, in order to effectively condense the large amount of air that is taken in, a condensing agent with a catalytic action that facilitates dew condensation may be added. Further, in order to minimize the amount of moisture in the atmosphere that escapes to the outside after cooling the atmosphere and taking water, the size of the outlet may be reduced to increase the atmospheric pressure at the outlet.

【0010】尚、特許請求の範囲の項に図面との対照を
便利にするために符号を記すが、該記入により本発明は
添付図面の構成に限定されるものではない。
[0010]Although reference numerals are written in the claims for convenience of comparison with the drawings, the present invention is not limited to the structure shown in the accompanying drawings.

【図面の簡単な説明】[Brief explanation of the drawing]

【図1】本発明にかかる造水装置の実施例を表す全体概
念図
[Fig. 1] Overall conceptual diagram showing an embodiment of a fresh water generation device according to the present invention.

【図2】自由大気中の湿分と大気圧力との関係図[Figure 2] Relationship diagram between moisture in free air and atmospheric pressure

【符号の説明】[Explanation of symbols]

1  大気湿度変換機 2  大気吸引装置 4  大気圧力低減機構 5  冷却部 6  殺菌装置 7  取水口 1 Atmospheric humidity converter 2 Atmospheric suction device 4 Atmospheric pressure reduction mechanism 5 Cooling section 6 Sterilizer 7 Water intake

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】  大気吸引装置(2)と、この大気吸引
装置(2)によって取入れられる大気圧力を低減する機
構(4)を備えると共に取入れられた大気を冷却して湿
分を取出す冷却部(5)を内蔵した大気湿度変換機(1
)と、この大気湿度変換機(1)によって得られる水を
取出す取水口(7)とからなる造水装置。
1. A cooling unit (1) comprising an atmospheric suction device (2) and a mechanism (4) for reducing the atmospheric pressure taken in by the atmospheric suction device (2), and a cooling unit (4) for cooling the taken atmospheric air and extracting moisture. Atmospheric humidity converter (1) with built-in
) and a water intake (7) for taking out the water obtained by the atmospheric humidity converter (1).
【請求項2】  前記大気圧力低減機構(4)が大気取
入口に設けられた多孔質通気体である請求項1記載の造
水装置。
2. The fresh water generating apparatus according to claim 1, wherein the atmospheric pressure reduction mechanism (4) is a porous ventilation body provided at an atmospheric intake port.
【請求項3】  前記大気湿度変換機(1)と取水口(
7)との間に殺菌装置(6)を備える請求項1または2
記載の造水装置。
[Claim 3] The atmospheric humidity converter (1) and the water intake (
7) Claim 1 or 2 further comprising a sterilizer (6) between the
The water production device described.
JP3006445A 1991-01-23 1991-01-23 Desalination equipment Expired - Lifetime JPH0711151B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3006445A JPH0711151B2 (en) 1991-01-23 1991-01-23 Desalination equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3006445A JPH0711151B2 (en) 1991-01-23 1991-01-23 Desalination equipment

Publications (2)

Publication Number Publication Date
JPH04250231A true JPH04250231A (en) 1992-09-07
JPH0711151B2 JPH0711151B2 (en) 1995-02-08

Family

ID=11638612

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3006445A Expired - Lifetime JPH0711151B2 (en) 1991-01-23 1991-01-23 Desalination equipment

Country Status (1)

Country Link
JP (1) JPH0711151B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014185402A1 (en) * 2013-05-16 2014-11-20 株式会社廣林 Filter device and water-purification device
JP2014224399A (en) * 2013-05-16 2014-12-04 株式会社廣林 Water intake device
JP2014224398A (en) * 2013-05-16 2014-12-04 株式会社廣林 Water intake device

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2014185402A1 (en) * 2013-05-16 2014-11-20 株式会社廣林 Filter device and water-purification device
JP2014223589A (en) * 2013-05-16 2014-12-04 株式会社廣林 Filter device and water purifier
JP2014224399A (en) * 2013-05-16 2014-12-04 株式会社廣林 Water intake device
JP2014224398A (en) * 2013-05-16 2014-12-04 株式会社廣林 Water intake device

Also Published As

Publication number Publication date
JPH0711151B2 (en) 1995-02-08

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