JPH0361096B2 - - Google Patents
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- Publication number
- JPH0361096B2 JPH0361096B2 JP60091556A JP9155685A JPH0361096B2 JP H0361096 B2 JPH0361096 B2 JP H0361096B2 JP 60091556 A JP60091556 A JP 60091556A JP 9155685 A JP9155685 A JP 9155685A JP H0361096 B2 JPH0361096 B2 JP H0361096B2
- Authority
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- Japan
- Prior art keywords
- porous sheet
- water
- hollow structure
- humidifier
- moisture
- 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 - Lifetime
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Description
【発明の詳細な説明】
〔産業上の利用分野〕
この発明は温風等による自然蒸発方式でありな
がら、加湿能力を大巾に向上させた加湿器に関す
るものである。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a humidifier that uses a natural evaporation method using hot air or the like, but has significantly improved humidification ability.
省エネルギーの観点から最近の居住空間は断熱
化、気密化が進んでおり、より高度の空調が要求
されている。空調の要素として、温度コントロー
ル、湿度コントロールおよび有害空気成分のコン
トロールが挙げられる。温度コントロールに関し
ては、種々の加熱方式および冷却方式が実用化さ
れ、満足のいく状況にある。しかし、温度コント
ロールおよび有害空気成分のコントロールに関し
ては未だ十分に満足のいく物がない状況にある。
From the perspective of energy conservation, modern living spaces are becoming more insulated and airtight, and more advanced air conditioning is required. Air conditioning elements include temperature control, humidity control, and control of harmful air components. Regarding temperature control, various heating and cooling methods have been put into practical use and are in a satisfactory state. However, there is still nothing completely satisfactory in terms of temperature control and control of harmful air components.
加湿器に関しては、自然蒸発方式、電熱方式、
水スプレー方式および超音波方式等があるが、自
然蒸発方式は加湿能力が小さい、電熱方式ではラ
ンニングコストが高い、水スプレー方式では加湿
効率が低く、大型化する。また、超音波方式はイ
ニシヤルコストが高い、寿命が短い等の欠点があ
る。 Regarding humidifiers, natural evaporation method, electric heating method,
There are water spray methods and ultrasonic methods, but the natural evaporation method has a small humidifying capacity, the electric heating method has high running costs, and the water spray method has low humidification efficiency and is bulky. Further, the ultrasonic method has drawbacks such as high initial cost and short life.
そこで、イニシヤルコストおよびランニングコ
ストが低く、最も実用性の高い自然蒸発方式の加
湿器で加湿能力を大巾に向上させる方法について
検討を重ねた。 Therefore, we have repeatedly investigated ways to greatly improve the humidification capacity of a natural evaporation type humidifier, which has the lowest initial cost and running cost and is the most practical.
自然蒸発方式では水の蒸発面積を極力広くとる
ために、開口部の大きいバツト状の容器を用いた
り、親水性繊維の織布の下端を水中に浸して毛細
力により水の表面積を増やす努力をしている。こ
こで仮りに、水を厚さ数mmにスライスし、これを
縦などに多層並べることができれば、水の蒸発面
積を大巾に増加させることができる。そこでスラ
イスされた厚さ数mmの水を縦に保持する方法につ
いて研究を重ねた結果、疎水性高分子を素材とす
る多孔質シートを用いて内部の厚さが数mmの中空
構造体を形成し、この中空部に上記スライスされ
た水をおさめることにより任意の空間に水を保持
することができ、しかも水は自由に蒸発できるこ
とを先に見い出した。(特願昭59−026741号明細
書)
以上のように自然蒸発方式でありながら加湿能
力の大きい加湿器を先に見い出したが(特願昭59
−026741号明細書)、例えば小型化するためには、
さらに大巾に加湿能力が向上した高性能なものが
要求された。 In the natural evaporation method, in order to maximize the area for water evaporation, efforts are made to use a bucket-shaped container with a large opening or to soak the bottom end of a woven hydrophilic fiber in water to increase the surface area of water using capillary force. are doing. If water were to be sliced into slices several millimeters thick and arranged in multiple layers vertically, the area for water evaporation could be greatly increased. As a result of repeated research on how to hold sliced water vertically several millimeters thick, we created a hollow structure with an internal thickness of several millimeters using a porous sheet made of hydrophobic polymer. However, it was previously discovered that by storing the sliced water in this hollow part, water can be held in any space, and moreover, the water can freely evaporate. (Specification of Japanese Patent Application No. 59-026741) As mentioned above, we have discovered a humidifier that uses natural evaporation but has a large humidifying capacity (Japanese Patent Application No. 59-026741).
-026741 specification), for example, in order to downsize,
Furthermore, a high-performance product with significantly improved humidification capacity was required.
そこで水の通過を防止し、水蒸気を通過させ得
る疎水性高分子の多孔質シート(以下透湿膜と略
記する。)を用いる自然蒸発式加湿器(以下透湿
膜方式加湿器と略記する。)を高性能化するため
に、上記透湿膜が水蒸気の透過に対して示す物質
抵抗(以下透湿抵抗と略記する。)を測定すると
ともに、透湿膜の複雑な形状をした空孔構造を屈
曲した毛細管の集合でモデル化し、透湿膜方式加
湿器の加湿能力と透湿膜の透湿抵抗および空孔構
造との関係を明らかにし、最適な透湿抵抗と空孔
構造を有する透湿膜を先に見い出した。(特願昭
60−026824号明細書)
〔発明が解決しようとする問題点〕
上記の透湿膜方式加湿器を高性能化できる透湿
膜は透湿抵抗の小さいものであり、その空孔構造
は空孔率が高く、空孔が膜全体に高密度に分布し
ているため、機械的強度に劣るという問題点があ
つた。また機械的強度を向上させるために膜厚を
厚くすると透湿抵抗が膜厚に比例して高くなると
いうジレンマに陥るという問題点があつた。 Therefore, a natural evaporation type humidifier (hereinafter abbreviated as a moisture permeable membrane humidifier) uses a porous sheet of hydrophobic polymer (hereinafter abbreviated as a moisture permeable membrane) that prevents the passage of water and allows water vapor to pass through. ) In order to improve the performance of the moisture permeable membrane, we measured the material resistance (hereinafter abbreviated as moisture permeation resistance) that the moisture permeable membrane exhibits against the permeation of water vapor, and also investigated the complex-shaped pore structure of the moisture permeable membrane. was modeled as a set of bent capillaries, and the relationship between the humidifying capacity of a permeable membrane type humidifier and the permeation resistance and pore structure of the permeable membrane was clarified. We found the wet film first. (Tokugansho
60-026824 specification) [Problems to be solved by the invention] The moisture permeable membrane that can improve the performance of the moisture permeable membrane type humidifier described above has a low moisture permeation resistance, and its pore structure is composed of pores. The problem was that the mechanical strength was poor because the pores were densely distributed throughout the membrane. Another problem was that when the film thickness was increased to improve mechanical strength, the moisture permeation resistance increased in proportion to the film thickness.
この発明は上記のような問題点を解消するため
になされたもので、小さい透湿抵抗と、その小さ
い透湿抵抗を実現するための空孔構造を保持する
とともに、機械的強度にも優れた透湿膜を見い出
し、加湿能力が大巾に向上した高性能な透湿膜方
式加湿器を提供することを目的とする。 This invention was made to solve the above problems, and it has a low moisture permeation resistance and a porous structure to achieve the low moisture permeation resistance, and also has excellent mechanical strength. The purpose of the present invention is to discover a moisture-permeable membrane and provide a high-performance moisture-permeable membrane type humidifier with greatly improved humidification capacity.
この発明の加湿器は、水蒸気を通過させ得る中
空構造体の中空部に水を供給し、上記中空構造体
に送風した空気に上記中空構造体を通過した水蒸
気を含ませて加湿するものにおいて、上記中空構
造体の素材として、水の通過を防止し、水蒸気を
通過させ得る疎水性高分子の多孔質シートと、水
と水蒸気を通過させる通気性布を重ね合わせた複
合多孔質シートを用いたものである。
The humidifier of the present invention supplies water to a hollow part of a hollow structure through which water vapor can pass, and humidifies the air blown into the hollow structure by impregnating the water vapor that has passed through the hollow structure. As the material for the hollow structure, we used a composite porous sheet in which a porous sheet of hydrophobic polymer that prevents water from passing through and allows water vapor to pass through, and a breathable cloth that allows water and vapor to pass through. It is something.
この発明においては、水及び水蒸気を通過させ
る通気性布が複合多孔質シートの機械強度を担う
ので、疎水性高分子の多孔質シートが水の通過を
防止する撥水性と水蒸気を通過させる透湿性の2
つの機能を担えばよいので、多孔質シートの空孔
率が高く、高密度に空孔が分布していても、その
膜厚を薄くできるので、複合多孔質シートの透湿
抵抗を小くできる。その結果、加湿能力の向上し
た高性能な加湿器が得られる。
In this invention, the breathable fabric that allows water and water vapor to pass through is responsible for the mechanical strength of the composite porous sheet, so the porous sheet of hydrophobic polymer has water repellency that prevents water from passing through, and moisture permeability that allows water vapor to pass through. 2
Therefore, even if the porous sheet has a high porosity and pores are distributed in a high density, the film thickness can be made thinner, so the moisture permeation resistance of the composite porous sheet can be reduced. . As a result, a high-performance humidifier with improved humidification capacity can be obtained.
以下、この発明を図に基づいて説明する。第1
図はこの発明に係わる中空構造体の一実施例を一
部切欠いて表わす斜視図で、図中、1は疎水性高
分子の多孔質シートと通気性布を重ね合わせた複
合多孔質シート(透湿膜)、2はスペーサ、3は
水の供給口、4は水の排出口、5は空孔構造体
で、矢印イは水の供給方向、ロは水の排出方向を
表わす。
Hereinafter, this invention will be explained based on the drawings. 1st
The figure is a partially cutaway perspective view of an embodiment of the hollow structure according to the present invention. In the figure, 1 is a composite porous sheet (transparent (wet film), 2 is a spacer, 3 is a water supply port, 4 is a water discharge port, 5 is a porous structure, arrow A indicates the water supply direction, and arrow B indicates the water discharge direction.
この発明に係わる疎水性高分子の多孔質シート
素材としては、例えばポリエチレン、ポリプロピ
レン、ポリスチレン、ポリ塩化ビニル、ポリ塩化
ビニリデン、ポリカーボネート、ポリエステル及
びフツ素樹脂等が用いられ、水の通過を防止し、
水蒸気を通過させ得るものである。 Examples of the hydrophobic polymer porous sheet material used in this invention include polyethylene, polypropylene, polystyrene, polyvinyl chloride, polyvinylidene chloride, polycarbonate, polyester, and fluorine resin, which prevent water from passing through,
It allows water vapor to pass through.
この発明に係わる通気性布としては水と水蒸気
を自由に通過させるものであれば何でも良く、植
物繊維、化学繊維、及び金属繊維等の織布あるい
は不織布が用いられる。多孔質シートの補強とい
う機械的強度を担う面から厚みは200μm以上が望
ましく、実用的には500μm以下が適当である加工
性面からは、例えばポリエステル等の化織布が使
用しやすい。 The breathable fabric according to the present invention may be any fabric as long as it allows water and steam to pass through freely, and woven or nonwoven fabrics such as vegetable fibers, chemical fibers, and metal fibers are used. The thickness is desirably 200 μm or more from the viewpoint of providing mechanical strength for reinforcing the porous sheet, and 500 μm or less is practically appropriate. From the viewpoint of processability, for example, a chemically woven fabric such as polyester is easily used.
複合多孔質シートは上記の多孔質シートと布を
部分的に点接合して重ねあわせている。全面を接
合した場合孔が閉じてしまうので、透湿抵抗があ
り減少しないように、例えば5mmとか10mm間隔で
部分的に点接合している。 The composite porous sheet is made by overlapping the above-mentioned porous sheet and cloth by partially point-joining them. If the entire surface is bonded, the holes will be closed, so to prevent moisture permeation resistance from decreasing, point bonding is done in spots at intervals of, for example, 5 mm or 10 mm.
この実施例においては、厚さ数mmの目の粗い布
(織布及び不織布)をスペーサ2として用い、こ
の布の両面を複合多孔質シート1で被い、水の供
給口3及び排出口4を除いて端部を接着あるいは
熱融着することにより中空構造体5を構成した。
なお、中空構造体5の内側が複合多孔質シート1
の通気性布になるように構成した場合、この布が
スペーサの機能を果たし、水を供給しやすくし、
スペーサの代用となる。 In this embodiment, a coarse cloth (woven fabric or non-woven fabric) with a thickness of several mm is used as a spacer 2, both sides of this cloth are covered with a composite porous sheet 1, and a water supply port 3 and a water discharge port 4 are used. The hollow structure 5 was constructed by gluing or heat-sealing the ends except for the ends.
Note that the inside of the hollow structure 5 is the composite porous sheet 1.
When configured to be a breathable fabric, this fabric acts as a spacer and facilitates water supply.
Substitute for spacer.
この発明に係わる複合多孔質シートは透湿抵抗
が4h・cmHg/Kg以下のものが、後述するように
加湿量が大きく増大するので適当であり、2h・
cmHg/Kg以下の範囲のものがより望ましい。 It is appropriate for the composite porous sheet according to the present invention to have a moisture permeation resistance of 4 h.cmHg/Kg or less, as this greatly increases the amount of humidification as will be described later.
A range of cmHg/Kg or less is more desirable.
孔のない高分子膜に対する水蒸気の透過性を評
価する方法として、JIS−Z0208で規定された透
湿カツプ法であるが、透湿膜のように水蒸気の透
過性の大きい多孔質シートでは多孔質シートの持
つ透湿抵抗よりも多孔質シートの両面に接する空
気層の透湿抵抗の方が大きくなり、上記透湿カツ
プ法では正確な透湿抵抗を測定することができな
い。そこで、発明者らは先に多孔質シートの透湿
抵抗を測定する方法を提案した。〔文献:高橋、
他;化学工学論文集vol.3No.5P.510〜513(1977)〕
また、多孔質シートの複雑な形状をした空孔構造
を第2図に示すような屈曲した毛細管の集合でモ
デル化し、空孔構造を定量化する方法も提案し
た。〔文献:高橋、他;化学工学論文集vol.5No.
4P.391〜396(1979)〕
上記方法により種々の透湿膜の透湿抗と空孔の
平均孔径(c)、平均屈曲率(≡c/l)
および単位面積当りの孔数(nc)を測定すると
共に、これらの透湿膜を用いて後述の膜面積が
1.0m2の加湿器を試作して、その加湿量を測定し、
これらの相関性を詳細に検討した。その結果、加
湿量と透湿抵抗の間には第3図の特性図に示すよ
うな明確な相関関係が存在することを明らかにし
た。但し、加湿器の加湿量は送風空気の風速、温
度および湿度に依存する。第3図の測定値は風速
2m/s、温度約40℃、相対湿度約20%の時の値
で、加湿器として使用する場合の、暖房時ヒータ
から出てくる温風を想定したものであり、縦軸は
加湿量(c.c./h)を、横軸は透湿抵抗(h・cm
Hg/Kg)を表わしている。なお、この加湿量と
透湿抵抗の関係を示す特性曲線は風速あるいは温
度を上げると加湿量は増えるので、上方にシフト
し、相対湿度を上げると加湿量が減るので、下方
にシフトする。図から判るように、透湿抵抗が
4h・cmHg/Kg以下になると大巾に加湿量が増大
するので好ましい。透湿膜方式加湿器の中空構造
体は膜面積に比例する。従つて、この値は例えば
加湿器を薄型コンパクト化するために好ましい膜
面積が1.0m2程度のものに適し、6〜8畳の標準
的な部屋の加湿量として好ましい500c.c./h以上
を確保できる。 The moisture-permeable cup method specified in JIS-Z0208 is a method for evaluating the water vapor permeability of a non-porous polymer membrane. The moisture permeability resistance of the air layer in contact with both surfaces of the porous sheet is greater than the moisture permeation resistance of the sheet, and the above-mentioned moisture permeation cup method cannot accurately measure the moisture permeation resistance. Therefore, the inventors previously proposed a method for measuring the moisture permeation resistance of a porous sheet. [Reference: Takahashi,
etc.; Chemical Engineering Papers Vol.3No.5P.510-513 (1977)]
We also proposed a method for quantifying the pore structure by modeling the complex-shaped pore structure of a porous sheet as a collection of bent capillaries as shown in Figure 2. [Reference: Takahashi, et al.; Chemical Engineering Papers Vol. 5 No.
4P.391-396 (1979)] By the above method, the average pore size (c) and average curvature (≡c/l) of various moisture permeable membranes were determined.
In addition to measuring the number of pores per unit area (nc), using these moisture permeable membranes, the membrane area as described below was calculated.
We prototyped a 1.0m 2 humidifier and measured the amount of humidification.
We examined these correlations in detail. As a result, it was revealed that there is a clear correlation between the amount of humidification and the moisture permeation resistance as shown in the characteristic diagram of FIG. However, the amount of humidification by a humidifier depends on the wind speed, temperature, and humidity of the blown air. The measured values in Figure 3 are wind speed
2 m/s, temperature of approximately 40°C, and relative humidity of approximately 20%. This value assumes warm air coming out of the heater when used as a humidifier, and the vertical axis represents the amount of humidification ( cc/h), and the horizontal axis is the moisture permeability resistance (h・cm
Hg/Kg). Note that the characteristic curve showing the relationship between the amount of humidification and moisture permeation resistance shifts upward because the amount of humidification increases when the wind speed or temperature increases, and shifts downward because the amount of humidification decreases when the relative humidity increases. As can be seen from the figure, the moisture permeation resistance
It is preferable that the amount of humidification is 4 h·cmHg/Kg or less because the amount of humidification increases significantly. The hollow structure of a moisture-permeable membrane humidifier is proportional to the membrane area. Therefore, this value is suitable, for example, for a humidifier with a membrane area of about 1.0 m2 in order to make it thin and compact, and is preferably 500 c.c./h or more as a humidification amount for a standard room of 6 to 8 tatami mats. can be secured.
ここで、単位面積当りの透湿抵抗(RH20)は次
式のように透湿膜の膜厚(l)透湿係数(PH20)で割
つた値として定義される。 Here, the moisture permeability resistance per unit area (R H20 ) is defined as the value obtained by dividing the thickness (l) of the moisture permeable membrane by the moisture permeability coefficient (P H20 ) as shown in the following equation.
PH20≡l/PH20 (1)
透湿係数(PH20)は多孔膜の空孔構造により決
まるため同一空孔構造を有する多孔質膜では透湿
抵抗(PH20)は膜厚に比例する。 P H20 ≡l/P H20 (1) The moisture permeability coefficient (P H20 ) is determined by the pore structure of the porous membrane, so for porous membranes with the same pore structure, the moisture permeation resistance (P H20 ) is proportional to the membrane thickness. .
例えば透湿膜方式加湿器を商品化するためには
透湿膜に対する信頼性が重要であり必要最少限の
機械強度を得るためには膜厚として200μm以上が
要求される。膜厚200μm以上で透湿抵抗を4h・cm
Hg/Kg以下にするためには透湿係数を5×10-5
Kg/m.h.cmHg以上にする必要がある。 For example, in order to commercialize a moisture-permeable membrane type humidifier, reliability of the moisture-permeable membrane is important, and in order to obtain the minimum necessary mechanical strength, a membrane thickness of 200 μm or more is required. Moisture permeability resistance of 4h・cm when film thickness is 200μm or more
To reduce the moisture permeability to Hg/Kg or less, set the moisture permeability coefficient to 5×10 -5
Must be at least Kg/mhcmHg.
疎水性高分子の多孔質シートの透湿係数は一般
に10-6〜10-6Kg/m.h.cmHgの範囲にあり、上記
値を満足するものも存在するが、そのような多孔
質シートは空孔率が高く、空孔が膜全体に高密度
に分布するため機械強度に劣る。 The moisture permeability coefficient of porous sheets of hydrophobic polymers is generally in the range of 10 -6 to 10 -6 Kg/mhcmHg, and there are some sheets that satisfy the above value, but such porous sheets have a high porosity. The mechanical strength is poor because the pores are densely distributed throughout the membrane.
一方、膜厚I1、透湿係数PH20(1)の多孔質シート
と膜厚I2、透湿係数PH20の多孔質シートを重ね合
わせた複合多孔質シートの単位面積当りの透湿抵
抗PH20は次式で与えられる。 On the other hand, the moisture permeability resistance per unit area of a composite porous sheet in which a porous sheet with a membrane thickness of I 1 and a moisture permeability coefficient of P H20 (1) and a porous sheet with a membrane thickness of I 2 and a moisture permeability coefficient of P H20 are superimposed. P H20 is given by the following formula.
PH20=I1/PH20(1)+I2/PH20(2) (2)
例えば前者を水の通過を防止し、水蒸気を通過
させ得る(撥水性と透湿性を兼ね備えた)多孔質
シート、後者を水と水蒸気を通過させる通気性の
布と考えると、PH20(1)は10-6〜10-4Kg/m.h.cmHg
の範囲にあり、PH20(2)は10-4〜10-3Kg/m.h.cmHg
の範囲にある。従つてPH20の大きい布に機械強度
を持たせ、PH20の小さい多孔質シートのI1を小さ
くすることにより全体の透湿抵抗PH20を小さくす
ることが可能である。その結果第3図に示すよう
に加湿器の加湿器を大巾に増大させながら透湿膜
の信頼性を向上させることができる。多孔質シー
トのI1としては薄い程好ましく、その効果を発現
するためには100μm以下にすることが好ましい。
従つて、多孔質シートの厚みは実用上10μm以上
で、加湿性能を向上させ、透湿抵抗を小さくする
ため100μm以下が望ましい。 P H20 = I 1 /P H20 (1) + I 2 /P H20 (2) (2) For example, the former is a porous sheet that can prevent water from passing through but allow water vapor to pass (combined with water repellency and moisture permeability). , considering the latter as a breathable cloth that allows water and steam to pass through, P H20 (1) is 10 -6 ~ 10 -4 Kg/mhcmHg
P H20 (2) is in the range of 10 -4 to 10 -3 Kg/mhcmHg
within the range of Therefore, it is possible to reduce the overall moisture permeation resistance P H20 by imparting mechanical strength to a fabric with a large P H20 and by reducing I 1 of a porous sheet with a small P H20 . As a result, as shown in FIG. 3, the reliability of the moisture permeable membrane can be improved while greatly increasing the number of humidifiers. The thinner the I 1 of the porous sheet, the more preferable it is, and in order to achieve this effect, it is preferably 100 μm or less.
Therefore, the thickness of the porous sheet is practically 10 μm or more, and desirably 100 μm or less in order to improve humidification performance and reduce moisture permeation resistance.
第4図はこの発明の一実施例であるプレート型
加湿器を示す構成図で、図中、6は中空構造体5
より上部に位置し、蒸発分の水を供給する水タン
クで、矢印ハは空気の導入方向、ニは空気の導出
方向を表わす。この実施例においては透湿膜の透
湿抵抗を4h・cmHg/Kg以下にして、加湿量を大
巾に増加させているうえに、中空構造体5を乾燥
空気の通路となる空間をあけて折りたたみ多層積
層して直方体形状にし、小さい容積でありなが
ら、水の蒸発面積を大巾に増大させているので、
加湿能力が飛躍的に向上した。なお、図中に示し
ていないが、中空構造体5は形状を保つため積層
された中空構造体の空間には波状の間隔材、例え
ばプラスチツクで形成されたものが挿入されて補
強されている。 FIG. 4 is a configuration diagram showing a plate type humidifier which is an embodiment of the present invention, and in the figure, 6 is a hollow structure 5.
The water tank is located higher up and supplies evaporated water. Arrow C indicates the direction in which air is introduced, and arrow D indicates the direction in which air is discharged. In this embodiment, the moisture permeability resistance of the moisture permeable membrane is set to 4 h·cmHg/Kg or less, and the amount of humidification is greatly increased. It is folded and laminated in multiple layers to form a rectangular parallelepiped shape, which greatly increases the water evaporation area despite its small volume.
Humidification ability has improved dramatically. Although not shown in the figure, in order to maintain the shape of the hollow structure 5, a corrugated spacer, for example made of plastic, is inserted into the space of the stacked hollow structures to reinforce it.
なお、中空構造体5の外側が複合多孔質シート
1の通気性布になるように構成した場合、この布
が中空構造体5表面の補護、補強をするため、間
隔材の代用となる。 Note that when the outside of the hollow structure 5 is configured to be the breathable cloth of the composite porous sheet 1, this cloth protects and reinforces the surface of the hollow structure 5, and thus serves as a spacing material.
加湿運転時には、水の排出口4は閉じられてお
り、水タンク6より水の供給口3を経て中空構造
体5の中空部に水が供給され保持される。中空構
造体5の空間に乾燥空気をハ方向より送風するこ
とにより複合多孔質シート(透湿膜)を通過して
水蒸気が蒸気して空気に含まれ、加湿された空気
がニ方向へ出て行く。蒸発分の水はタンク6より
随時補給される。なお、水の排出口4は長期間使
用しない時に開けて水抜きをしたり、水を流通さ
せて水垢を除去したりするのに用いる。 During humidification operation, the water discharge port 4 is closed, and water is supplied from the water tank 6 to the hollow part of the hollow structure 5 through the water supply port 3 and held therein. By blowing dry air into the space of the hollow structure 5 from the direction C, water vapor passes through the composite porous sheet (moisture permeable membrane) and is contained in the air, and the humidified air exits in the two directions. go. Evaporated water is replenished from the tank 6 as needed. The water outlet 4 is used to drain water by opening it when not in use for a long period of time, or to remove limescale by circulating water.
第5図はこの発明の他の実施例であるスパイラ
ル型加湿器をす構成図で、図中、7は波状の間隔
材、例えばプラスチツクで形成されたものを表わ
し、中空構造体5を波状の間隔材7を介して巻き
込んでハニカム状円柱形状にし、第4図に示すも
のと同様、複合多孔質シートの加湿能力の増加に
加え、小さい容積でありながら、水の蒸発面積を
大巾に増大しており、飛躍的に加湿能力が向上し
た。水タンク6より水を供給しながら乾燥空気を
送風することにより加湿された空気が得られる。
中空構造体5と間隔材7は接着しても良いが、接
着しなくても構わない。図に示していないが、中
心部にパイプを通すことにより水の排出口を設け
ることが出来る。 FIG. 5 is a block diagram showing a spiral type humidifier according to another embodiment of the present invention. In the figure, 7 represents a wavy spacer, for example, one made of plastic, and the hollow structure 5 is formed of a wavy spacer. It is wound into a honeycomb-like columnar shape through the spacing material 7, and in addition to increasing the humidifying capacity of the composite porous sheet as shown in Fig. 4, the evaporation area of water is greatly increased despite its small volume. The humidifying ability has improved dramatically. Humidified air is obtained by blowing dry air while supplying water from the water tank 6.
The hollow structure 5 and the spacer 7 may be bonded together, but they do not need to be bonded together. Although not shown in the figure, a water outlet can be provided by passing a pipe through the center.
実施例 1
膜厚が100μm、透湿係数が5×10-5Kg/m.h.cm
Hgのポリエチレン製多孔質シートと膜厚が
200μm、透湿係数が4×10-4Kg/m.h.cmHgのポ
リエチレン製不織布を重ね合わせ、1cm間隔で点
融着を行つた。できた複合多孔質シートの透湿抵
抗を測定したとこの2.8h.cmHg/Kgであつた。こ
の複合多孔質シートを透湿膜として用い、巾22
cm、長さ5.1mの帯状に裁断した。Example 1 Film thickness is 100μm, moisture permeability coefficient is 5×10 -5 Kg/mhcm
Hg polyethylene porous sheet and film thickness
Polyethylene nonwoven fabrics of 200 μm and a moisture permeability coefficient of 4×10 -4 Kg/mhcmHg were overlapped and point-fused at 1 cm intervals. The moisture permeability resistance of the resulting composite porous sheet was measured to be 2.8h.cmHg/Kg. This composite porous sheet is used as a moisture permeable membrane with a width of 22 mm.
It was cut into strips with a length of 5.1 m.
次に厚さ4mm、巾10cm、長さ5.0mの不織布を
カツトし、これをスペーサとして上記多孔質膜で
覆い、2枚の多孔質膜が重なつた側をヒートシー
ラーを用いて熱融着した。次に両端に直径6mm、
長さ5cmのポリエチレンチユーブを挿入しながら
多孔質膜を熱融着して、第1図のように中空構造
体を作製した。ポリエチレンチユーブと多孔質シ
ートの界面よりの水洩れを防ぐため必要に応じて
接着剤を用いて封止した。 Next, cut a piece of nonwoven fabric with a thickness of 4 mm, width of 10 cm, and length of 5.0 m, cover it with the above porous membrane as a spacer, and heat seal the side where the two porous membranes overlap using a heat sealer. did. Next, 6mm in diameter on both ends,
A polyethylene tube with a length of 5 cm was inserted and the porous membrane was heat-sealed to produce a hollow structure as shown in FIG. 1. In order to prevent water leakage from the interface between the polyethylene tube and the porous sheet, adhesive was used to seal as necessary.
次にポリエチレン製の波状間隔材を用いて第4
図のようなプレート型加湿器を作製した。通風時
の圧損を小さくするために波状間隔材の波の高さ
を6mm、ピツチを9mmとした。加湿器の膜面積は
約1.0m2となつた。 Next, a wavy spacer made of polyethylene was used to create a fourth
A plate-type humidifier as shown in the figure was created. In order to reduce pressure loss during ventilation, the wave height of the wavy spacing material was set to 6 mm, and the pitch was set to 9 mm. The membrane area of the humidifier was approximately 1.0 m 2 .
次に上記加湿器を50℃の温水を流したフアンコ
イルユニツトの熱交換器の前面に取り付け、約40
℃の温度を送風した。加湿量は風速に依存し、風
1m/sの時の加湿量は560c.c./hであり、風速を
2m/sに上げると加湿量は650c.c./hに増加し
た。 Next, attach the above humidifier to the front of the heat exchanger of the fan coil unit, which has 50℃ hot water flowing through it.
The temperature of ℃ was blown. The amount of humidification depends on the wind speed.
The humidification amount at 1 m/s is 560 c.c./h, and the
When the speed was increased to 2 m/s, the humidification amount increased to 650 c.c./h.
実施例 2
膜厚が50μm、透湿係数が5×10-5Kg/m.h.cm
Hgのポリエチレン製多孔質シートと膜厚が
200μm、透湿係数が4×10-4Kg/m.h.cmHgのポ
リエチレン製不織布を重ね合わせ、1cm間隔で点
融着を行つた。できた複合多孔質シートの透湿抵
抗を測定したとこの1.8h.cmHg/Kgであつた。こ
の複合多孔質シートを透湿膜として用い、巾22
cm、長さ5.1mの帯状に裁断した。Example 2 Film thickness is 50μm, moisture permeability coefficient is 5×10 -5 Kg/mhcm
Hg polyethylene porous sheet and film thickness
Polyethylene nonwoven fabrics of 200 μm and a moisture permeability coefficient of 4×10 -4 Kg/mhcmHg were overlapped and point-fused at 1 cm intervals. The moisture permeation resistance of the resulting composite porous sheet was measured to be 1.8h.cmHg/Kg. This composite porous sheet is used as a moisture permeable membrane with a width of 22 mm.
It was cut into strips with a length of 5.1 m.
実施例1と同様にして中空構造体を作製した。 A hollow structure was produced in the same manner as in Example 1.
次にポリエチレン製の波状間隔材を用いて第4
図のようなプレート型加湿器を作製した。加湿器
の膜面積は約1.0m2となつた。 Next, a wavy spacer made of polyethylene was used to create a fourth
A plate-type humidifier as shown in the figure was created. The membrane area of the humidifier was approximately 1.0 m 2 .
次に上記加湿器を50℃の温水を流したフアンコ
イルユニツトの熱交換器の前面に取り付け、約40
℃の温度を送風した。加湿量は風速1m/sで710
c.c./h、2m/sで820c.c./hであつた。 Next, attach the above humidifier to the front of the heat exchanger of the fan coil unit, which has 50℃ hot water flowing through it.
The temperature of ℃ was blown. The amount of humidification is 710 at a wind speed of 1m/s
cc/h, 2m/s was 820c.c./h.
実施例 3
実施例2と同じ複合多孔質シートの透湿膜を用
い、巾12cm、長さ10.1mの帯状にカツトし、実施
例1と同様にして中空構造体を作成した。Example 3 A hollow structure was prepared in the same manner as in Example 1 by using the same composite porous sheet moisture permeable membrane as in Example 2 and cutting it into a strip having a width of 12 cm and a length of 10.1 m.
次に波の高さ6mm、ピツチ9mmのポリエチレン
製の波状間隔材を用いて第5図のようなスパイラ
ル型加湿器を作成した。 Next, a spiral type humidifier as shown in Fig. 5 was made using polyethylene wavy spacing material with a wave height of 6 mm and a pitch of 9 mm.
加湿器の膜面積は約1.0m2、なつた。 The membrane area of the humidifier is approximately 1.0m 2 .
次に上記加湿を50℃の温水を流したフアンコイ
ルユニツトの熱交換器の前面に取り付け、約40℃
の温度を送風した。加湿量は風速1m/sで720
c.c./h、2m/sで830c.c./hであつた。膜面積が
等しい場合にはプレート型加湿器とスパイラル型
加湿器の加湿量はほぼ一致した。 Next, attach the above humidifier to the front of the heat exchanger of the fan coil unit, which has hot water of 50℃ flowing, and
The temperature of the air was blown. Humidification amount is 720 at wind speed 1m/s
cc/h, 2m/s was 830c.c./h. When the membrane area was the same, the humidification amount of the plate type humidifier and the spiral type humidifier was almost the same.
実施例 4
膜厚が50μm、透湿係数が8×10-5Kg/m.h.cm
Hgのポリ塩化ビニルの多孔質シートと膜厚が
150μm、透湿係数が5×10-4Kg/m.h.cmHgのポ
リエチレン製の織布を重ね合わせ、接着剤を用い
て1cm間隔で点融着した。できた複合多孔質シー
トの透湿抵抗を測定したところ1.0h.cmHg/Kgで
あつた。この複合多孔質シートを透湿膜として用
い、巾12cm、長さ10.1mの帯状に裁断し、実施例
1と同様にして中空構造体を作製した。Example 4 Film thickness is 50μm, moisture permeability coefficient is 8×10 -5 Kg/mhcm
Hg polyvinyl chloride porous sheet and film thickness
Polyethylene woven fabrics of 150 μm and a moisture permeability coefficient of 5×10 −4 Kg/mhcmHg were overlapped and bonded at 1 cm intervals using an adhesive. The moisture permeation resistance of the resulting composite porous sheet was measured to be 1.0h.cmHg/Kg. This composite porous sheet was used as a moisture permeable membrane and cut into strips with a width of 12 cm and a length of 10.1 m to produce a hollow structure in the same manner as in Example 1.
次に実施例3と同様にしてスパイラル型加湿器
を作製した。 Next, a spiral humidifier was produced in the same manner as in Example 3.
加湿器の膜面積は約1.0m2、となつた。 The membrane area of the humidifier was approximately 1.0 m 2 .
次に上記加湿器を50℃の温水を流したフアンコ
イルユニツトの熱交換器の前面に取り付け、約40
℃の温度を送風した。加湿量は風速1msで1000
c.c./h、2m/sで1200c.c./hであつた。多孔質
膜の空孔特性および透湿特性が等しい場合には膜
材料が異つても加湿量はほぼ一致した。 Next, attach the above humidifier to the front of the heat exchanger of the fan coil unit, which has 50℃ hot water flowing through it.
The temperature of ℃ was blown. The amount of humidification is 1000 at a wind speed of 1ms.
cc/h, 2m/s was 1200c.c./h. When the pore characteristics and moisture permeability characteristics of porous membranes were the same, the humidification amount was almost the same even if the membrane materials were different.
上記実施例に用いた透湿膜は織布あるいは不織
布で裏打ちされているため機械強度に優れ、加工
性も向上した。 The moisture permeable membrane used in the above examples was lined with a woven or nonwoven fabric, so it had excellent mechanical strength and improved workability.
また、この発明による加湿器は第4図あるいは
第5図の構造の加湿器をケーシングに納め、エア
コンやヒーター等の乾燥空気の出口に取り付けて
使用するが、加湿器として独立に使用する場合に
はフアンやブロアー等の送風器と組み合わせて使
用することもできる。 In addition, the humidifier according to the present invention has the structure shown in Fig. 4 or 5 and is housed in a casing and is used by being attached to the dry air outlet of an air conditioner or heater, but when used independently as a humidifier. It can also be used in combination with a blower such as a fan or blower.
以上のように、この発明によれば、水蒸気を通
過させ得る中空構造体の中空部に水を供給し、上
記中空構造体に送風した空気上記中空構造体を通
過した水蒸気を含ませて加湿するものにおいて、
上記中空構造体の素材として、水の通過を防止
し、水蒸気を通過させ得る疎水性高分子の多孔質
シートと、水と水蒸気を通過させる通気性布を重
ね合わせた複合多孔質シートを用いることによ
り、複合多孔質シートを機械的強度にも優れた透
湿抵抗の小さいものにできるので、加湿能力が大
巾に向上した高性能な加湿器が得られる効果があ
る。
As described above, according to the present invention, water is supplied to the hollow part of a hollow structure through which water vapor can pass, and the air blown to the hollow structure is humidified by being impregnated with the water vapor that has passed through the hollow structure. In things,
As a material for the hollow structure, a composite porous sheet is used, which is a composite porous sheet made by laminating a hydrophobic polymer porous sheet that prevents water from passing through and allows water vapor to pass through, and a breathable cloth that allows water and water vapor to pass through. As a result, the composite porous sheet can be made to have excellent mechanical strength and low moisture permeation resistance, resulting in the effect of obtaining a high-performance humidifier with greatly improved humidification capacity.
第1図はこの発明に係わる中空構造体の一実施
例を一部切欠いて表わす斜視図、第2図はこの発
明に係わる多孔質シートの空孔の形状モデルを示
す説明図、第3図はこの発明に係わる多孔質シー
トの透湿抵抗と加湿量との相関関係を示す特性
図、第4図はこの発明の一実施例の、第5図は他
の実施例の感湿器を示す構成図である。
図において、1は疎水性高分子の多孔質シート
と通気性布を重ね合わせた複合多孔質シート(透
湿膜)、2はスペーサ、3は水の供給口、4は水
の排出口、5は中空構造体、6は水タンク、7は
波の間隔材、イは水の供給方向、ロは水の排出方
向、ハは空気の導入方向、ニは空気の導出方向を
表わす。なお、図中、同一符号は同一又は相当部
分を示す。
FIG. 1 is a partially cutaway perspective view of an embodiment of a hollow structure according to the present invention, FIG. 2 is an explanatory diagram showing a model of the shape of pores in a porous sheet according to the present invention, and FIG. A characteristic diagram showing the correlation between the moisture permeation resistance and the amount of humidification of the porous sheet according to the present invention, FIG. 4 shows the structure of a humidity sensor according to one embodiment of the present invention, and FIG. 5 shows the structure of a humidity sensor according to another embodiment. It is a diagram. In the figure, 1 is a composite porous sheet (moisture permeable membrane) made by laminating a porous sheet of hydrophobic polymer and a breathable cloth, 2 is a spacer, 3 is a water supply port, 4 is a water discharge port, and 5 6 is a hollow structure, 6 is a water tank, 7 is a wave spacing member, A is a water supply direction, B is a water discharge direction, C is an air introduction direction, and D is an air discharge direction. In addition, in the figures, the same reference numerals indicate the same or corresponding parts.
Claims (1)
水を供給し、上記中空構造体に送風した空気に上
記中空構造体を通過した水蒸気を含ませて加湿す
るものにおいて、上記中空構造体の素材として、
水の通過を防止し、水蒸気を通過させ得る疎水性
高分子の多孔質シートと、水と水蒸気を通過させ
る通気性布を重ね合わせた複合多孔質シートを用
いたことを特徴とする加湿器。 2 複合多孔質シートは多孔質シートと通気性布
を部分的に点接合して重ね合わせたものであるこ
とを特徴とする特許請求の範囲第1項記載の加湿
器。 3 多孔質シートの厚みが10〜100μmであること
を特徴とする特許請求の範囲第1項又は第2項記
載の加湿器。 4 中空構造体の内側が多孔質シートで、外側が
通気性布で構成されていることを特徴とする特許
請求の範囲第1項ないし第3項のいずれかに記載
の加湿器。 5 中空構造体の内側が通気性布で、外側が多孔
質シートで構成されていることを特徴とする特許
請求の範囲第1項ないし第3項のいずれかに記載
の加湿器。 6 多孔質シートの素材の疎水性高分子がポリエ
チレン、ポリプロピレン、ポリスチレン、ポリ塩
化ビニル、ポリ塩化ビニリデン、ポリカーボネー
ト、ポリエステル、及びフツ素樹脂のいずれか一
種であることを特徴とする特許請求の範囲第1項
ないし第5項のいずれかに記載の加湿器。[Scope of Claims] 1. A humidifier that supplies water to a hollow part of a hollow structure through which water vapor can pass, and humidifies the air blown into the hollow structure by impregnating the water vapor that passed through the hollow structure, As the material for the hollow structure mentioned above,
A humidifier characterized by using a composite porous sheet made by laminating a hydrophobic polymer porous sheet that prevents water from passing through and allows water vapor to pass through, and a breathable cloth that allows water and water vapor to pass through. 2. The humidifier according to claim 1, wherein the composite porous sheet is a porous sheet and a breathable cloth partially bonded and overlapped at points. 3. The humidifier according to claim 1 or 2, wherein the porous sheet has a thickness of 10 to 100 μm. 4. The humidifier according to any one of claims 1 to 3, wherein the inside of the hollow structure is made of a porous sheet and the outside is made of breathable cloth. 5. The humidifier according to any one of claims 1 to 3, wherein the inside of the hollow structure is made of breathable cloth and the outside is made of a porous sheet. 6. Claim No. 6, characterized in that the hydrophobic polymer of the material of the porous sheet is any one of polyethylene, polypropylene, polystyrene, polyvinyl chloride, polyvinylidene chloride, polycarbonate, polyester, and fluororesin. The humidifier according to any one of items 1 to 5.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9155685A JPS61250429A (en) | 1985-04-25 | 1985-04-25 | Humidifier |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9155685A JPS61250429A (en) | 1985-04-25 | 1985-04-25 | Humidifier |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS61250429A JPS61250429A (en) | 1986-11-07 |
| JPH0361096B2 true JPH0361096B2 (en) | 1991-09-18 |
Family
ID=14029779
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9155685A Granted JPS61250429A (en) | 1985-04-25 | 1985-04-25 | Humidifier |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS61250429A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08100934A (en) * | 1994-09-30 | 1996-04-16 | Japan Gore Tex Inc | Humidification membrane and its manufacturing method |
| JPH08110071A (en) * | 1994-10-13 | 1996-04-30 | Japan Gore Tex Inc | Humidification sheet and humidification unit |
| JPH08145420A (en) * | 1994-11-24 | 1996-06-07 | Japan Gore Tex Inc | humidifier |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7380774B2 (en) | 2004-05-17 | 2008-06-03 | Mitsubishi Heavy Industries, Ltd. | Humidifier |
| EP4542126A1 (en) * | 2022-06-15 | 2025-04-23 | Daicel Corporation | Humidification element and humidifier |
Family Cites Families (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5058852A (en) * | 1973-09-26 | 1975-05-21 | ||
| JPS59158252A (en) * | 1983-03-01 | 1984-09-07 | ジヤパンゴアテツクス株式会社 | Waterproof material of excellent moisture permeability |
| JPS6127434A (en) * | 1984-07-18 | 1986-02-06 | P S Kankyo Giken Kk | Humidifier |
-
1985
- 1985-04-25 JP JP9155685A patent/JPS61250429A/en active Granted
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH08100934A (en) * | 1994-09-30 | 1996-04-16 | Japan Gore Tex Inc | Humidification membrane and its manufacturing method |
| JPH08110071A (en) * | 1994-10-13 | 1996-04-30 | Japan Gore Tex Inc | Humidification sheet and humidification unit |
| JPH08145420A (en) * | 1994-11-24 | 1996-06-07 | Japan Gore Tex Inc | humidifier |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS61250429A (en) | 1986-11-07 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| EXPY | Cancellation because of completion of term |