JPH11137946A - Dehumidifier - Google Patents
DehumidifierInfo
- Publication number
- JPH11137946A JPH11137946A JP9310082A JP31008297A JPH11137946A JP H11137946 A JPH11137946 A JP H11137946A JP 9310082 A JP9310082 A JP 9310082A JP 31008297 A JP31008297 A JP 31008297A JP H11137946 A JPH11137946 A JP H11137946A
- Authority
- JP
- Japan
- Prior art keywords
- anode
- membrane
- oxygen
- space
- dehumidified
- 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.)
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- Separation Using Semi-Permeable Membranes (AREA)
- Drying Of Gases (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、電気化学素子を用
いた除湿装置に関する。TECHNICAL FIELD The present invention relates to a dehumidifier using an electrochemical device.
【0002】[0002]
【従来の技術】この種の除湿装置は、例えば図4に示す
ように、水を電気分解して酸素を発生する陽極1と、水
素イオンと酸素を反応させて水もしくは水蒸気を発生す
る陰極2との間に、水素イオン交換膜となる固体高分子
電解質膜3が挟持された積層構造の電気化学素子Eを用
いるのが一般的であり、当該素子Eは、その周辺部を陽
極1と陰極2の各電極面1a,2aに積層して装着され
る一対の給電体4及び4により挟持した状態で、その周
辺部が絶縁性樹脂フレーム5で締め付けられると共に、
当該樹脂フレーム5の周辺部を接着剤で固定してガスシ
ールされている。そして、陽極1と陰極2は、それぞれ
の電極面1a,2aに積層して装着された給電体4及び
4を介して所定の直流電圧を印加する外部電源6に接続
されるようになっている。2. Description of the Related Art As shown in FIG. 4, for example, a dehumidifier of this type comprises an anode 1 for electrolyzing water to generate oxygen, and a cathode 2 for reacting hydrogen ions with oxygen to generate water or water vapor. It is common to use an electrochemical element E having a laminated structure in which a solid polymer electrolyte membrane 3 serving as a hydrogen ion exchange membrane is sandwiched between the anode 1 and the cathode 1. In the state of being sandwiched between a pair of power supply bodies 4 and 4 stacked and mounted on the respective electrode surfaces 1a and 2a, the periphery thereof is tightened by an insulating resin frame 5, and
The periphery of the resin frame 5 is fixed with an adhesive and gas-sealed. The anode 1 and the cathode 2 are connected to an external power supply 6 for applying a predetermined DC voltage via feeders 4 and 4 mounted on and stacked on the respective electrode surfaces 1a and 2a. .
【0003】 また、陽極1と陰極2は、いずれも多孔
質基材で形成されると共に、それぞれその一部が固体高
分子電解質膜3の表面に食い込んだ状態になっており、
両電極1及び2間に外部電源6から直流電圧を印加する
と、陽極1では、水を電気分解する次式(1)の反応が
起こって、陽極1側に形成した被除湿空間7内の雰囲気
が除湿されると同時に、酸素が富化される。 2H2 O → O2 +4H+ +4e- ・・・・・(1)The anode 1 and the cathode 2 are both formed of a porous base material, and a part of each of the anode 1 and the cathode 2 is cut into the surface of the solid polymer electrolyte membrane 3.
When a DC voltage is applied between the electrodes 1 and 2 from the external power supply 6, a reaction of the following formula (1) for electrolyzing water occurs at the anode 1, and the atmosphere in the dehumidified space 7 formed on the anode 1 side is formed. Is dehumidified and oxygen is enriched at the same time. 2H 2 O → O 2 + 4H + + 4e - ····· (1)
【0004】 そして、このとき発生する水素イオン
(H+ )が、陽極1側から固体高分子電解質膜3を通じ
て陰極2側へ移行すると共に、電子(e- )が、外部電
源6の回路を通じて陰極2へ達し、その陰極2では、水
素イオンと酸素が反応して水もしくは水蒸気を発生する
次式(2)の反応が起こって、陰極2側に形成した被加
湿空間8内の雰囲気が加湿されると同時に、酸素が除去
される。 O2 +4H+ +4e- → 2H2 O ・・・・・(2)Then, hydrogen ions (H + ) generated at this time move from the anode 1 side to the cathode 2 side through the solid polymer electrolyte membrane 3, and electrons (e − ) are passed through the circuit of the external power supply 6. 2 at the cathode 2, a reaction of the following formula (2) occurs in which hydrogen ions and oxygen react with each other to generate water or steam, and the atmosphere in the humidified space 8 formed on the cathode 2 side is humidified. At the same time, oxygen is removed. O 2 + 4H + + 4e − → 2H 2 O (2)
【0005】[0005]
【発明が解決しようとする課題】しかし、上記のような
除湿装置にあっては、被除湿空間7と被加湿空間8との
間における湿度差が大きすぎると、被加湿空間8内の空
気中に含まれる水蒸気が陰極2側から固体高分子電解質
膜3を透過して陽極1側へ浸透してくるため、陽極1で
は水を電気分解する前記(1)式の反応が絶え間なく起
こり、その結果として、被除湿空間7では酸素が異常に
増え続ける。However, in the above dehumidifying apparatus, if the humidity difference between the space 7 to be dehumidified and the space 8 to be humidified is too large, the air in the space 8 The water vapor contained permeates through the solid polymer electrolyte membrane 3 from the cathode 2 side and penetrates into the anode 1 side, so that the reaction of the above formula (1) for electrolyzing water occurs continuously at the anode 1, As a result, oxygen in the dehumidified space 7 continues to increase abnormally.
【0006】 このため、被除湿空間7が食品その他の
保管物を収容する保管庫の庫内である場合は、その庫内
に酸素ガスが高濃度で充満して、陽極1から発生する活
性な酸素や副次的に発生するオゾン等で食品等の酸化が
促進され、また、庫内が気密構造になっている場合は、
酸素ガスの蓄積により庫内の内圧が上昇して保管庫の一
部を破損に至らしめるおそれがあると共に、支燃性の酸
素ガスの増加に伴って保管物の引火性ないし発火性を増
大させる危険がある。For this reason, when the space 7 to be dehumidified is in the storage of a storage for storing foods and other storage items, the storage is filled with oxygen gas at a high concentration, and the active gas generated from the anode 1 is activated. Oxidation of foods and the like is promoted by oxygen and ozone generated as a by-product, and when the inside of the refrigerator has an airtight structure,
The accumulation of oxygen gas may cause an increase in the internal pressure of the storage, which may cause damage to a part of the storage, and increase the flammability or the ignitability of the storage with the increase of the oxygen-supporting gas. There is danger.
【0007】 そこで本発明は、除湿装置の除湿性能を
損なうことなく、被除湿空間内における酸素富化を抑制
することを技術的課題としている。Therefore, an object of the present invention is to suppress oxygen enrichment in a space to be dehumidified without impairing the dehumidifying performance of the dehumidifying device.
【0008】[0008]
【課題を解決するための手段】上記課題を解決するため
に、本発明は、水を電気分解して酸素を発生する陽極
と、水素イオンと酸素を反応させて水もしくは水蒸気を
発生する陰極との間に、水素イオン交換膜となる固体高
分子電解質膜が挟持された積層構造の電気化学素子を用
いる除湿装置において、被除湿空間に向けて配される前
記電気化学素子の陽極側に、水蒸気は透過するが酸素は
透過しない膜体によって前記陽極と被除湿空間との間を
隔絶する遮蔽室が形成されると共に、当該遮蔽室の周辺
部に、前記陽極から発生した酸素を外部に放出する微細
孔が形成されていることを特徴とする。SUMMARY OF THE INVENTION In order to solve the above-mentioned problems, the present invention relates to an anode for electrolyzing water to generate oxygen, and a cathode for reacting hydrogen ions with oxygen to generate water or water vapor. In a dehumidifier using a laminated electrochemical element in which a solid polymer electrolyte membrane serving as a hydrogen ion exchange membrane is sandwiched, a water vapor is provided on the anode side of the electrochemical element disposed toward the dehumidified space. Is formed by a film body that transmits but does not transmit oxygen, and a shielding chamber that separates the anode from the space to be dehumidified is formed, and oxygen generated from the anode is released to the outside around the shielding chamber. It is characterized in that micropores are formed.
【0009】 本発明によれば、電気化学素子の陽極で
水を電気分解して発生した酸素が、陽極の電極面と被除
湿空間との間を酸素を透過しない膜体で隔絶した遮蔽室
内に封じられ、その遮蔽室の周辺部に形成された微細孔
を通じて外部に放出されるので、被除湿空間内での酸素
富化が抑制される。また、陽極の電極面と被除湿空間と
の間を隔絶する膜体は、酸素を透過しないが水蒸気は透
過するので、被除湿空間内の水蒸気が遮蔽室内へ移行し
て陽極で電気分解され、被除湿空間内の雰囲気が除湿さ
れる。According to the present invention, oxygen generated by electrolyzing water at the anode of the electrochemical element is placed in a shielded room in which the oxygen-permeable membrane separates the electrode surface of the anode from the space to be dehumidified. It is sealed and released to the outside through the fine holes formed in the periphery of the shielding room, so that oxygen enrichment in the space to be dehumidified is suppressed. In addition, since the membrane that separates the electrode surface of the anode from the space to be dehumidified does not transmit oxygen but does transmit water vapor, the water vapor in the space to be dehumidified moves to the shielding room and is electrolyzed by the anode. The atmosphere in the space to be dehumidified is dehumidified.
【0010】[0010]
【発明の実施の形態】以下、本発明の実施形態を図面に
よって具体的に説明する。図1〜図3は、それぞれ本発
明による除湿装置の一例を示す断面図である。なお、図
4に示す従来装置との対応部分については同一符号を付
して詳細説明は省略する。Embodiments of the present invention will be specifically described below with reference to the drawings. 1 to 3 are cross-sectional views each showing an example of a dehumidifier according to the present invention. The parts corresponding to those of the conventional apparatus shown in FIG.
【0011】 図1及び図2に示す本発明の除湿装置
は、電気化学素子Eの陽極1と陰極2が、それぞれ厚さ
0.06mm 、有効膜面積 100×100mm のチタンメッシュシ
ートに、厚さ1μmの白金メッキを施した多孔質基材で
構成されている。In the dehumidifier of the present invention shown in FIGS. 1 and 2, the anode 1 and the cathode 2 of the electrochemical element E
It is composed of a titanium substrate having a thickness of 0.06 mm and an effective film area of 100 × 100 mm, and a 1 μm-thick platinum-plated porous substrate.
【0012】 また、陽極1と陰極2との間に挟持され
る固体高分子電解質膜3は、厚さ 170μmのナフィオン
膜(Nafion:デュポン社の商品名)が用いられ、予めナ
フィオン溶液(5重量%水アルコール溶液)に白金黒を
混合した溶液を塗布、乾燥して、単位面積当たり 0.5mg
/cm2 の白金黒が陽極及び陰極面に担持させてある。As the solid polymer electrolyte membrane 3 sandwiched between the anode 1 and the cathode 2, a 170 μm-thick Nafion membrane (Nafion: trade name of DuPont) is used, and a Nafion solution (5 wt. % Aqueous alcohol solution) mixed with platinum black and dried, and 0.5mg / unit area
/ Cm 2 of platinum black is carried on the anode and cathode surfaces.
【0013】 そして、陽極1と陰極2との間に固体高
分子電解質膜3を挟み、それらを温度 170℃、50kg/cm
2 の圧力でホットプレスして接合した後、陽極1と陰極
2の電極面1a,2aの周辺部にそれぞれ外部電源6に
接続される給電体4,4を装着させて、絶縁性樹脂フレ
ーム5に嵌め付け、当該樹脂フレーム5の周辺部をガス
シールして固定することにより、電気化学素子Eが形成
される。[0013] A solid polymer electrolyte membrane 3 is sandwiched between the anode 1 and the cathode 2, and they are heated at a temperature of 170 ° C and 50 kg / cm.
After hot-pressing and joining at a pressure of 2 , feeders 4, 4 connected to an external power supply 6 are mounted around the electrode surfaces 1 a, 2 a of the anode 1 and the cathode 2, respectively. , And the periphery of the resin frame 5 is gas-sealed and fixed, whereby the electrochemical element E is formed.
【0014】 次に、その電気化学素子Eが、陽極1を
被除湿空間7に向けて配設されると共に、その陽極1側
に、水蒸気は透過するが酸素は殆ど透過しない膜体10
によって陽極1の電極面1aと被除湿空間7との間を隔
絶する遮蔽室9が形成されている。Next, the electrochemical element E is disposed so that the anode 1 faces the space 7 to be dehumidified, and a film 10 that transmits water vapor but hardly transmits oxygen is provided on the anode 1 side.
Thereby, a shielding chamber 9 for isolating between the electrode surface 1a of the anode 1 and the space 7 to be dehumidified is formed.
【0015】 図1の遮蔽室9は、膜体10の周辺部を
ガスシールして接合した樹脂フレーム11を電気化学素
子Eの周辺部である絶縁性樹脂フレーム5の周辺部に沿
って接着剤で固定して形成されると共に、樹脂フレーム
11の一部に電気化学素子Eの陽極1から発生した酸素
を外部に放出する微細孔12が形成されている。The shielding chamber 9 shown in FIG. 1 is formed by bonding a resin frame 11 joined by sealing the periphery of the film body 10 by gas sealing along the periphery of the insulating resin frame 5 which is the periphery of the electrochemical element E. In addition, a fine hole 12 for releasing oxygen generated from the anode 1 of the electrochemical element E to the outside is formed in a part of the resin frame 11.
【0016】 膜体10は、厚さ 0.05mm のナフィオン
膜が用いられ、そのナフィオン膜が電気化学素子Eの陽
極1の電極面1aと一定の間隔を保って平行に対峙する
ように配されている。また、微細孔12は、遮蔽室9の
周辺部を成す樹脂フレーム11に穿設した直径1mm程度
の貫通孔で形成されている。電気化学素子Eの陽極1の
電極面1aと膜体10との間の間隔は、通常2〜10mm程
度に選定されるが、膜体10の有効膜面積に応じて適宜
に変更される。As the film body 10, a Nafion film having a thickness of 0.05 mm is used, and the Nafion film is disposed so as to face the electrode surface 1 a of the anode 1 of the electrochemical element E in parallel at a constant interval. I have. The fine hole 12 is formed as a through hole having a diameter of about 1 mm and formed in the resin frame 11 which forms a peripheral portion of the shielding chamber 9. The distance between the electrode surface 1a of the anode 1 of the electrochemical element E and the film body 10 is usually selected to be about 2 to 10 mm, but is appropriately changed according to the effective film area of the film body 10.
【0017】 なお、図2の遮蔽室9は、その周辺部が
酸素やオゾン等のガスを透過する多数の微細孔13を有
した多孔質膜体14で形成されている点において図1の
遮蔽室9と相違し、多孔質膜体14としては、例えば孔
径 0.6μmの微細孔13を有する発水性のテフロン膜
(PTFE膜)等が用いられている。また、図1に示す
遮蔽室9の周辺部を成す貫通孔を形成した樹脂フレーム
に替えて、たとえば 0.2〜 0.6mmの狭隙を有する金属フ
レームを使用することもできる。The shielding chamber 9 shown in FIG. 2 is formed by a porous film body 14 having a large number of fine holes 13 through which a gas such as oxygen or ozone is transmitted. Unlike the chamber 9, as the porous film body 14, for example, a water-repellent Teflon film (PTFE film) having the micropores 13 having a pore diameter of 0.6 μm is used. Further, instead of the resin frame having the through-holes forming the peripheral portion of the shielding chamber 9 shown in FIG. 1, a metal frame having a narrow gap of, for example, 0.2 to 0.6 mm can be used.
【0018】 以上が、図1及び図2に示す本発明装置
の構成であり、次に、その作用効果について説明する。
図4に示す従来装置に、図1及び図2の本発明装置に係
る電気化学素子Eと同一の素子Eを適用して、当該素子
Eに直流電圧3Vを印加する除湿実験を行ったところ、
その従来装置によれば、周辺環境が室温20℃、湿度90%
の条件下で、被除湿空間7内における酸素ガス増加量は
0.4リットル/hrであった。これに対し、図1及び図2
の本発明装置によれば、電気化学素子Eの陽極1から発
生する酸素が、遮蔽室9の内部から微細孔12又は13
を通じて外部に放出されると共に、酸素を透過しない膜
体10によって被除湿空間7内への侵入を阻止されるの
で、被除湿空間7内における酸素ガスの増加は略0に抑
制された。The above is the configuration of the device of the present invention shown in FIG. 1 and FIG. 2. Next, the operation and effect will be described.
When the same device E as the electrochemical device E according to the device of the present invention shown in FIGS. 1 and 2 was applied to the conventional device shown in FIG. 4, a dehumidification experiment was performed in which a DC voltage of 3 V was applied to the device E.
According to the conventional device, the surrounding environment is room temperature 20 ° C and humidity 90%.
Under the conditions described above, the amount of increase in oxygen gas in the space 7 to be dehumidified is
It was 0.4 liter / hr. In contrast, FIGS. 1 and 2
According to the device of the present invention, oxygen generated from the anode 1 of the electrochemical element E is supplied from the inside of the shielding chamber 9 to the fine holes 12 or 13.
Is released to the outside, and is prevented from entering the dehumidification space 7 by the film body 10 that does not transmit oxygen. Therefore, the increase of oxygen gas in the dehumidification space 7 is suppressed to substantially zero.
【0019】 一方、除湿性能に関しては、図1及び図
2の本発明装置は、被除湿空間7内の水蒸気が、その被
除湿空間7内と水蒸気を透過させる膜体10を挟んで隣
接する遮蔽室9内との間に生ずる湿度勾配によって、絶
え間なく被除湿空間7内から遮蔽室9内へ移行して来る
ため、前記除湿実験に供した図4の従来装置と略同じく
7.0cc/hrの除湿性能(相対湿度90%から10%に低下さ
せる除湿能力)が得られ、陽極1の電極面1aと被除湿
空間7との間を膜体10で隔絶しても、電気化学素子E
の除湿性能は損なわれないことが確認された。On the other hand, with respect to the dehumidifying performance, in the apparatus of the present invention shown in FIGS. 1 and 2, the water vapor in the dehumidified space 7 is shielded from the dehumidified space 7 by the film body 10 that allows the water vapor to pass therethrough. Due to the humidity gradient generated between the inside of the room 9 and the inside of the room 7 to be continuously transferred from the space 7 to be dehumidified to the inside of the shielded room 9, substantially the same as the conventional apparatus of FIG.
A dehumidifying performance of 7.0 cc / hr (a dehumidifying ability to reduce the relative humidity from 90% to 10%) is obtained, and even if the film surface 10 separates the space 1 between the electrode surface 1a of the anode 1 and the space 7 to be dehumidified. Chemical element E
It was confirmed that the dehumidifying performance of was not impaired.
【0020】 また、図1及び図2に示す本発明装置の
ように、電気化学素子Eの陽極1と被除湿空間7との間
に、陽極1から発生する酸素ガスによって陽圧状態とな
る遮蔽室9の空間が形成されていると、その陽圧空間の
圧力差による作用により、被加湿空間8内の水蒸気が遮
蔽室9の一部に配置された微細孔12又は13から侵入
する作用も抑制されるため、電気化学素子Eの除湿性能
が損なわれない。Further, as in the apparatus of the present invention shown in FIGS. 1 and 2, between the anode 1 of the electrochemical element E and the space 7 to be dehumidified, a shield is brought into a positive pressure state by the oxygen gas generated from the anode 1. When the space of the chamber 9 is formed, the action of the water vapor in the humidified space 8 from the fine holes 12 or 13 arranged in a part of the shielding chamber 9 is also caused by the action due to the pressure difference of the positive pressure space. Since it is suppressed, the dehumidifying performance of the electrochemical element E is not impaired.
【0021】 なお、電気化学素子Eの陽極1及び陰極
2を構成する多孔質基材は、上記チタンメッシュシート
に限るものではなく、ニッケル、タンタル、ステンレ
ス、カーボン等を繊維シート状に成形したものや、多孔
性を保ちながらシート状に形成したものを用いることも
できる。The porous substrate constituting the anode 1 and the cathode 2 of the electrochemical element E is not limited to the above-mentioned titanium mesh sheet, but is formed by forming nickel, tantalum, stainless steel, carbon or the like into a fiber sheet. Alternatively, a sheet formed while maintaining the porosity can be used.
【0022】 また、図2に示す多孔質膜体14として
は、テフロン、ポリプロピレン又はポリエステル等の有
機高分子材料、若しくはガラス繊維、アルミナ繊維、シ
リカ繊維又はムライト繊維等のセラミックス材料で成形
されたもの等が用いられる。The porous membrane 14 shown in FIG. 2 is formed of an organic polymer material such as Teflon, polypropylene or polyester, or a ceramic material such as glass fiber, alumina fiber, silica fiber or mullite fiber. Are used.
【0023】 また、図示は省略するが、図1及び図2
の膜体10を成す固体高分子電解質膜は、吸湿性に富む
ため高湿度環境では膨潤して著しく変形するので、その
片面,両面若しくは内部に、前記多孔質膜体14と同様
に水蒸気を透過させる多数の微細孔を有した補強用多孔
質膜体を添着すると、膜体10の機械的強度が補強され
て、その膜体10が破損するおそれもなくなる。機械的
な補強効果の高い補強用多孔質膜体としては吸湿性がな
く、固体高分子電解質膜が膨潤しても殆ど変形しないテ
フロンの多孔質膜体が適している。Although not shown, FIGS. 1 and 2
Since the solid polymer electrolyte membrane constituting the membrane body 10 is rich in hygroscopicity, it swells and is significantly deformed in a high humidity environment. When the reinforcing porous membrane having a large number of micropores to be attached is attached, the mechanical strength of the membrane 10 is reinforced, and the membrane 10 is not likely to be damaged. As a reinforcing porous membrane having a high mechanical reinforcing effect, a Teflon porous membrane that has no hygroscopicity and hardly deforms even when the solid polymer electrolyte membrane swells is suitable.
【0024】 次に、図3に示す本発明の除湿装置は、
被除湿空間7とその空間に向けて配される電気化学素子
Eの陽極1との間が、水蒸気は透過するが酸素は透過し
ない膜体10によって隔絶される点において、図1及び
図2の除湿装置と共通するが、その膜体10と陽極1と
の間に、遮蔽室9及びその空間が形成されずに、水蒸気
と酸素を透過する多数の微細孔15を有した多孔質膜体
(16) が挟装されている点において、図1及び図2の除
湿装置と相違する。Next, the dehumidifier of the present invention shown in FIG.
1 and 2 in that the space between the space 7 to be dehumidified and the anode 1 of the electrochemical element E disposed toward the space is separated by a film body 10 that transmits water vapor but does not transmit oxygen. Although it is common to the dehumidifier, a porous film body having a large number of micropores 15 permeable to water vapor and oxygen without forming a shielding chamber 9 and a space between the film body 10 and the anode 1 ( 16) is different from the dehumidifier of FIG. 1 and FIG.
【0025】 この図3の装置は、膜体10と電気化学
素子Eの陽極1との間に挟装された多孔質膜体16が、
膜体10の破損を防止する補強材として機能すると同時
に、その多孔質膜体16が有する微細孔15の空隙が、
図1及び図2に示す遮蔽室9の空間と同様に、被加湿空
間8内の水蒸気が陰極2側から固体高分子電解質膜3を
透過して陽極1側へ浸透することを抑制する作用を奏
し、更に、その多孔質膜体16の周縁部側の微細孔15
が、図1の微細孔12や図2の微細孔13と同様に、陽
極1から発生する酸素を外部へ放出する作用を奏する。In the apparatus shown in FIG. 3, the porous membrane 16 sandwiched between the membrane 10 and the anode 1 of the electrochemical element E comprises:
At the same time as functioning as a reinforcing material for preventing damage to the membrane 10, the pores of the micropores 15 of the porous membrane 16 are
As in the case of the shielded chamber 9 shown in FIGS. 1 and 2, the water vapor in the humidified space 8 has an effect of suppressing the permeation of the water vapor from the cathode 2 side through the solid polymer electrolyte membrane 3 and into the anode 1 side. And further, the fine holes 15 on the peripheral edge side of the porous film body 16.
However, as in the case of the micropores 12 of FIG. 1 and the micropores 13 of FIG. 2, it has an effect of releasing oxygen generated from the anode 1 to the outside.
【0026】 なお、多孔質膜体16は、テフロン、ポ
リプロピレン又はポリエステル等の有機高分子材料、若
しくはガラス繊維、アルミナ繊維、シリカ繊維又はムラ
イト繊維等のセラミックス材料で成形され、微細孔15
の孔径は、10μm程度に選定されている。The porous membrane 16 is formed of an organic polymer material such as Teflon, polypropylene or polyester, or a ceramic material such as glass fiber, alumina fiber, silica fiber or mullite fiber,
Is selected to be about 10 μm.
【0027】[0027]
【発明の効果】本発明による除湿装置は、被除湿空間内
の雰囲気を除湿する際に電気化学素子の陽極から発生し
た酸素が被除湿空間内に蓄積充満することがないから、
従来装置のように被除湿空間内の酸素ガス濃度が高まっ
てその空間内に保管された各種保管物の発火性や引火性
が増大するという危険が解消されると同時に、陽極から
発生する活性な酸素や副次的に発生するオゾン等によっ
て保管物が酸化したり変質するおそれも解消されるとい
う大変優れた効果がある。According to the dehumidifying device of the present invention, oxygen generated from the anode of the electrochemical element does not accumulate and fill the space to be dehumidified when the atmosphere in the space to be dehumidified is dehumidified.
As with the conventional device, the danger that the oxygen gas concentration in the space to be dehumidified is increased and the ignitability and flammability of various storage items stored in the space is increased is eliminated, and at the same time, the active gas generated from the anode is removed. There is a very excellent effect that the danger of oxidizing or deteriorating the stored material due to oxygen or ozone generated by the side is eliminated.
【図1】本発明による除湿装置の一例を示す断面図。FIG. 1 is a cross-sectional view showing an example of a dehumidifier according to the present invention.
【図2】本発明による除湿装置の一例を示す断面図。FIG. 2 is a sectional view showing an example of a dehumidifying device according to the present invention.
【図3】本発明による除湿装置の一例を示す断面図。FIG. 3 is a sectional view showing an example of a dehumidifier according to the present invention.
【図4】従来の除湿装置を示す断面図。FIG. 4 is a sectional view showing a conventional dehumidifier.
E・・・・・電気化学素子 1・・・・・陽極 2・・・・・陰極 3・・・・・固体高分子電解質膜 7・・・・・被除湿空間 9・・・・・遮蔽室 10・・・・・膜体 12・・・・・微細孔 13・・・・・微細孔 14・・・・・多孔質膜体 15・・・・・微細孔 16・・・・・多孔質膜体 E ... Electrochemical element 1 ... Anode 2 ... Cathode 3 ... Solid polymer electrolyte membrane 7 ... Dehumidified space 9 ... Shield Chamber 10 ··· Membrane 12 ··· Micropores 13 ··· Micropores 14 ··· Porous membrane 15 ··· Micropores 16 ··· Porous Membrane
フロントページの続き (72)発明者 中 村 光 宏 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 塚 本 秀 幸 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 今 泉 三 之 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 生田目 輝 昭 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 佐 藤 誠 一 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 横 松 得 滋 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 永 井 英 男 静岡県小笠郡大東町浜川新田1933−1 株 式会社オプテックディディ・メルコ・ラボ ラトリー内 (72)発明者 光 田 憲 朗 東京都千代田区丸の内二丁目2番3号 三 菱電機株式会社内 (72)発明者 山 内 四 郎 東京都千代田区丸の内二丁目2番3号 三 菱電機株式会社内Continued on the front page (72) Inventor Mitsuhiro Nakamura 193-1 Hamakawa Nitta, Oto-cho, Ogasa-gun, Shizuoka Prefecture Inside Optec Didi Melco Laboratory (72) Inventor Hideyuki Tsukamoto Ogasa-gun, Shizuoka Prefecture 193-1 Higashicho Hamakawa Nitta Inside Optec Didi Melco Laboratory Co., Ltd. (72) Inventor Miyuki Imaizumi 193-13-1 Hamakawa Nitta Ohitomachi Ogasa-gun Shizuoka Prefecture Inside Optec Didi Melco Laboratories (72) Inventor Teruaki Ikutame 193-1-1, Hamakawa Nitta, Daito-cho, Ogasa-gun, Shizuoka Prefecture Inside the Optec Didi Melco Laboratory (72) Inventor Seiichi Sato 1933, Hamakawa Nitta, Oto-cho, Ogasa-gun, Shizuoka Prefecture -1 Inside Optec Didi Melco Laboratory, Inc. (72) Inventor Takeshi Yokomatsu 193-1-1, Hamakawa Shinda, Oto-gun, Ogasa-gun, Shizuoka Prefecture Inside Optitech Didi Melco Laboratories, Inc. (72) Inventor Eternity Hideo Ii 193-1 Hamakawa Nitta, Daito-cho, Ogasa-gun, Shizuoka Prefecture Inside the Optec Didi Melco Laboratory (72) Inventor Kenro Mitsuda 2-3-2 Marunouchi 2-chome, Chiyoda-ku, Tokyo Mitsui Electric Co., Ltd. In-company (72) Inventor Shiro Yamauchi 2-3-2 Marunouchi, Chiyoda-ku, Tokyo Mitsubishi Electric Corporation
Claims (10)
と、水素イオンと酸素を反応させて水もしくは水蒸気を
発生する陰極との間に、水素イオン交換膜となる固体高
分子電解質膜が挟持された積層構造の電気化学素子を用
いる除湿装置において、被除湿空間(7)に向けて配さ
れる前記電気化学素子(E)の陽極(1)側に、水蒸気
は透過するが酸素は透過しない膜体(10)によって前記
陽極(1)と被除湿空間(7)との間を隔絶する遮蔽室
(9)が形成されると共に、当該遮蔽室(9)の周辺部
に、前記陽極(1)から発生した酸素を外部に放出する
微細孔(12,13)が形成されていることを特徴とする除
湿装置。A solid polymer electrolyte membrane serving as a hydrogen ion exchange membrane is provided between an anode for generating oxygen by electrolyzing water and a cathode for reacting hydrogen ions with oxygen to generate water or water vapor. In the dehumidifier using the sandwiched electrochemical element having a laminated structure, water vapor permeates oxygen but permeates the anode (1) side of the electrochemical element (E) disposed toward the space to be dehumidified (7). A shield chamber (9) is formed between the anode (1) and the space to be dehumidified (7) by the membrane (10) not to be formed, and the anode ( A dehumidifier characterized in that micropores (12, 13) for releasing oxygen generated from 1) to the outside are formed.
である請求項1記載の除湿装置。2. The dehumidifier according to claim 1, wherein the membrane is a solid polymer electrolyte membrane.
(10)の片面,両面若しくは内部に、水蒸気を透過させ
る多数の微細孔を有した補強用多孔質膜体が添着されて
いる請求項2記載の除湿装置。3. A reinforcing porous membrane having a large number of fine pores for allowing water vapor to pass therethrough is provided on one side, both sides or inside of the membrane (10) comprising a solid polymer electrolyte membrane. 2. The dehumidifier according to 2.
を有するテフロンシートである請求項3記載の除湿装
置。4. The dehumidifier according to claim 3, wherein the reinforcing porous membrane is a Teflon sheet having a large number of fine holes.
の周辺部を成す樹脂フレーム(11)に穿設された貫通孔
である請求項1記載の除湿装置。5. The shielding chamber (9), wherein the micro holes (12) are provided.
2. The dehumidifier according to claim 1, wherein the through hole is formed in a resin frame (11) forming a peripheral portion of the dehumidifier.
部を成す金属フレームが有する狭隙である請求項1記載
の除湿装置。6. The dehumidifier according to claim 1, wherein the fine hole is a narrow gap of a metal frame forming a peripheral portion of the shielding chamber (9).
の周辺部を成す多孔質膜体(14)が有する微細孔である
請求項1記載の除湿装置。7. The shielding chamber (9), wherein the micro holes (13) are provided.
2. The dehumidifier according to claim 1, wherein the porous membrane (14) constituting the peripheral portion has fine pores.
リプロピレン又はポリエステル等の有機高分子材料、若
しくはガラス繊維、アルミナ繊維、シリカ繊維又はムラ
イト繊維等のセラミックス材料で成形されている請求項
5記載の除湿装置。8. The porous membrane (14) is formed of an organic polymer material such as Teflon, polypropylene or polyester, or a ceramic material such as glass fiber, alumina fiber, silica fiber or mullite fiber. 5. The dehumidifying device according to 5.
と、水素イオンと酸素を反応させて水もしくは水蒸気を
発生する陰極との間に、水素イオン交換膜となる固体高
分子電解質膜が挟持された積層構造の電気化学素子を用
いる除湿装置において、被除湿空間(7)とその空間に
向けて配される前記電気化学素子(E)の陽極(1)と
の間が、水蒸気は透過するが酸素は透過しない膜体(1
0)によって隔絶されると共に、当該膜体(10)と前記
陽極(1)との間に、酸素やオゾン等のガスを透過する
多数の微細孔(15)を有した多孔質膜体(16) が挟装さ
れていることを特徴とする除湿装置。9. A solid polymer electrolyte membrane serving as a hydrogen ion exchange membrane is provided between an anode which electrolyzes water to generate oxygen and a cathode which reacts hydrogen ions with oxygen to generate water or water vapor. In the dehumidifier using the sandwiched electrochemical element having a laminated structure, water vapor permeates between the space (7) to be dehumidified and the anode (1) of the electrochemical element (E) arranged toward the space. Membrane that does not transmit oxygen (1
0) and a porous membrane (16) between the membrane (10) and the anode (1) having a number of micropores (15) permeable to gases such as oxygen and ozone. ) Is sandwiched between them.
リプロピレン又はポリエステル等の有機高分子材料、若
しくはガラス繊維、アルミナ繊維、シリカ繊維又はムラ
イト繊維等のセラミックス材料で成形されている請求項
7記載の除湿装置。10. The porous membrane (16) is formed of an organic polymer material such as Teflon, polypropylene or polyester, or a ceramic material such as glass fiber, alumina fiber, silica fiber or mullite fiber. 7. The dehumidifier according to 7.
Priority Applications (1)
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JP31008297A JP3844859B2 (en) | 1997-11-12 | 1997-11-12 | Dehumidifier |
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JP31008297A JP3844859B2 (en) | 1997-11-12 | 1997-11-12 | Dehumidifier |
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Cited By (13)
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---|---|---|---|---|
EP1120816A1 (en) * | 2000-01-28 | 2001-08-01 | Ebara Corporation | Substrate container and method of dehumidifying substrate container |
JP2014037620A (en) * | 2012-06-29 | 2014-02-27 | Toshiba Corp | Device for reducing oxygen, chamber for reducing oxygen and refrigerator |
CN103808106A (en) * | 2012-11-12 | 2014-05-21 | 株式会社东芝 | Food preservation device |
US8985474B2 (en) | 2011-01-17 | 2015-03-24 | Paragon Space Development Corporation | Space humidity control systems |
US9132439B2 (en) | 2009-06-15 | 2015-09-15 | Mitsubishi Electric Corporation | Electrostatic atomizer and air conditioner |
TWI551838B (en) * | 2012-11-08 | 2016-10-01 | Toshiba Lifestyle Products & Services Corp | Oxygen reduction equipment and cold storage |
WO2017091785A1 (en) * | 2015-11-23 | 2017-06-01 | Xergy Inc. | Environment control system utilizing an electrochemical cell |
US20190192806A1 (en) * | 2015-11-23 | 2019-06-27 | Xergy Inc | Environment control system utilizing an electrochemical cell |
US20190264341A1 (en) * | 2016-11-01 | 2019-08-29 | Xergy Inc. | Electrolysis cell assembly utilizing an anion exchange membrane |
JP2020535001A (en) * | 2017-09-22 | 2020-12-03 | スカイア・インコーポレイテッドSkyre, Inc. | Air-water extraction system |
US10890344B2 (en) | 2015-11-23 | 2021-01-12 | Xergy Inc. | Environment control system utilizing an electrochemical cell |
GB2612222A (en) * | 2018-03-04 | 2023-04-26 | Ffi Ionix Ip Inc | Environment control system utilizing an electrochemical cell |
US11717788B2 (en) * | 2015-11-23 | 2023-08-08 | Ffi Ionix Ip, Inc. | Environment control system utilizing an electrochemical cell |
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Cited By (24)
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EP1120816A1 (en) * | 2000-01-28 | 2001-08-01 | Ebara Corporation | Substrate container and method of dehumidifying substrate container |
US6547953B2 (en) | 2000-01-28 | 2003-04-15 | Ebara Corporation | Substrate container and method of dehumidifying substrate container |
US9132439B2 (en) | 2009-06-15 | 2015-09-15 | Mitsubishi Electric Corporation | Electrostatic atomizer and air conditioner |
US8985474B2 (en) | 2011-01-17 | 2015-03-24 | Paragon Space Development Corporation | Space humidity control systems |
JP2014037620A (en) * | 2012-06-29 | 2014-02-27 | Toshiba Corp | Device for reducing oxygen, chamber for reducing oxygen and refrigerator |
TWI551838B (en) * | 2012-11-08 | 2016-10-01 | Toshiba Lifestyle Products & Services Corp | Oxygen reduction equipment and cold storage |
CN103808106A (en) * | 2012-11-12 | 2014-05-21 | 株式会社东芝 | Food preservation device |
CN103808106B (en) * | 2012-11-12 | 2016-11-02 | 东芝生活电器株式会社 | Food preservation storehouse |
TWI580917B (en) * | 2012-11-12 | 2017-05-01 | 東芝生活電器股份有限公司 | Food storage reservoir |
US20190192806A1 (en) * | 2015-11-23 | 2019-06-27 | Xergy Inc | Environment control system utilizing an electrochemical cell |
US11717788B2 (en) * | 2015-11-23 | 2023-08-08 | Ffi Ionix Ip, Inc. | Environment control system utilizing an electrochemical cell |
GB2558847A (en) * | 2015-11-23 | 2018-07-18 | Xergy Incorporated | Environment control system utilizing an electrochemical cell |
WO2017091785A1 (en) * | 2015-11-23 | 2017-06-01 | Xergy Inc. | Environment control system utilizing an electrochemical cell |
US10890344B2 (en) | 2015-11-23 | 2021-01-12 | Xergy Inc. | Environment control system utilizing an electrochemical cell |
CN108291317A (en) * | 2015-11-23 | 2018-07-17 | 艾克塞基股份有限公司 | Utilize the environmental control system of electrochemical cell |
US11504494B2 (en) * | 2015-11-23 | 2022-11-22 | Ffi Ionix Ip, Inc. | Environment control system utilizing an electrochemical cell |
GB2558847B (en) * | 2015-11-23 | 2023-03-01 | Ffi Ionix Ip Inc | Environment control system utilizing an electrochemical cell |
US20190264341A1 (en) * | 2016-11-01 | 2019-08-29 | Xergy Inc. | Electrolysis cell assembly utilizing an anion exchange membrane |
US11725291B2 (en) * | 2016-11-01 | 2023-08-15 | Ffi Ionix Ip, Inc. | Electrolysis cell assembly utilizing an anion exchange membrane |
US11353222B2 (en) | 2017-09-22 | 2022-06-07 | Skyre, Inc. | Air-water extraction system |
JP2020535001A (en) * | 2017-09-22 | 2020-12-03 | スカイア・インコーポレイテッドSkyre, Inc. | Air-water extraction system |
EP3669128B1 (en) * | 2017-09-22 | 2023-08-30 | Skyre, Inc. | Air-water extraction system |
GB2612222B (en) * | 2018-03-04 | 2023-08-02 | Ffi Ionix Ip Inc | Environment control system utilizing an electrochemical cell |
GB2612222A (en) * | 2018-03-04 | 2023-04-26 | Ffi Ionix Ip Inc | Environment control system utilizing an electrochemical cell |
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