JP2000237317A - Pressure fluctuation adsorption type oxygen thickener - Google Patents

Pressure fluctuation adsorption type oxygen thickener

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Publication number
JP2000237317A
JP2000237317A JP11041483A JP4148399A JP2000237317A JP 2000237317 A JP2000237317 A JP 2000237317A JP 11041483 A JP11041483 A JP 11041483A JP 4148399 A JP4148399 A JP 4148399A JP 2000237317 A JP2000237317 A JP 2000237317A
Authority
JP
Japan
Prior art keywords
oxygen
air
membrane
humidification
hollow fiber
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
Application number
JP11041483A
Other languages
Japanese (ja)
Inventor
Kenji Takemasa
賢治 武政
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.)
Teijin Ltd
Original Assignee
Teijin Ltd
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 Teijin Ltd filed Critical Teijin Ltd
Priority to JP11041483A priority Critical patent/JP2000237317A/en
Publication of JP2000237317A publication Critical patent/JP2000237317A/en
Pending legal-status Critical Current

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  • Separation Of Gases By Adsorption (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)

Abstract

PROBLEM TO BE SOLVED: To adequately humidify an oxygen thickening gas by utilizing outdoor air of the atmosphere pressure by providing the apparatus with a module for humidification which humidifies the oxygen thickening gas and is composed of a hollow fiber-like moisture permeable membrane, passing the oxygen thickening gas on the inner side of the hollow membrane and bringing the atmospheric air into contact with the outer side. SOLUTION: This apparatus has an adsorption column packed with a zeolite-base adsorbent as the adsorbent for selectively adsorbing nitrogen. The pressurized air from a compressor is supplied to the column to form the thickened oxygen. The thickened oxygen is stored in a surge tank and is humidified when passing a humidifying device having the steam selective permeable hollow fiber membrane (moisture permeable membrane) and thereafter, the thickened oxygen is supplied to a patient. A nonporous fluororesin-base dissolved diffusion membrane allowing the permeation of moisture by utilizing a steam partial pressure difference is used for the moisture permeable membrane. The thickened oxygen is humidified by the outdoor air of the atmospheric pressure, by which a need for separate moisture replenishment is eliminated and the humidification to approximately the same humidification degree as that of the air in the atmosphere without a flow rate control system for regulation of the humidification rate is made possible.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、大気中から酸素濃
縮気体(酸素富化空気を含む)を分離して使用するための
酸素濃縮装置に関する。更に詳細には、圧力変動吸着型
酸素濃縮装置の加湿器に関し、空気中の水分を利用して
加湿された酸素濃縮気体を使用者に供給できるようにし
た、改善された酸素濃縮装置を提供するものである。
The present invention relates to an oxygen concentrator for separating and using oxygen-enriched gas (including oxygen-enriched air) from the atmosphere. More specifically, the present invention relates to a humidifier for a pressure fluctuation adsorption-type oxygen concentrator, and provides an improved oxygen concentrator capable of supplying a user with a humidified oxygen-enriched gas utilizing moisture in the air. Things.

【0002】[0002]

【従来の技術】近年、喘息、肺気腫症、慢性気管支炎等
の呼吸器系疾患に苦しむ患者が増加する傾向にある。そ
の最も効果的な治療法の一つとして酸素吸入療法があ
り、空気中から酸素濃縮気体を直接分離する酸素濃縮装
置が開発され、使用時の利便性、保守管理の容易さから
酸素吸入療法のための治療装置として次第に普及するよ
うになって来ている。
2. Description of the Related Art In recent years, the number of patients suffering from respiratory diseases such as asthma, emphysema and chronic bronchitis has been increasing. One of the most effective treatments is oxygen inhalation therapy, and an oxygen concentrator that separates oxygen-enriched gas directly from the air has been developed.Oxygen inhalation therapy has been developed for its convenience and ease of maintenance. It is becoming more and more popular as a medical treatment device.

【0003】かかる酸素濃縮装置としては、酸素選択透
過膜を用いた膜分離型酸素濃縮装置や、窒素又は酸素を
選択的に吸着し得る吸着剤を用いた吸着型酸素濃縮装置
が知られている。更には、酸素イオンを選択的に透過す
る固体電解質膜を利用し、電気化学的に酸素を生成する
装置なども有る。吸着型酸素濃縮装置としては、コンプ
レッサーを用いた圧力変動吸着型酸素濃縮装置があり、
通常、窒素を選択的に吸着し得る吸着剤を充填した吸着
床に、コンプレッサーで圧縮空気を導入して加圧状態で
窒素を吸着させることにより酸素濃縮気体を得る吸着工
程と、吸着床の内圧を減少させて窒素を脱着させ吸着剤
の再生を行う脱着工程とを交互に行うことにより酸素濃
縮気体を得る装置である。
As such an oxygen concentrator, a membrane separation type oxygen concentrator using an oxygen selective permeable membrane and an adsorption type oxygen concentrator using an adsorbent capable of selectively adsorbing nitrogen or oxygen are known. . Further, there is an apparatus that electrochemically generates oxygen using a solid electrolyte membrane that selectively transmits oxygen ions. As the adsorption type oxygen concentrator, there is a pressure fluctuation adsorption type oxygen concentrator using a compressor,
Usually, an adsorption step in which compressed air is introduced by a compressor into an adsorption bed filled with an adsorbent capable of selectively adsorbing nitrogen to adsorb nitrogen in a pressurized state to obtain an oxygen-enriched gas, and an internal pressure of the adsorption bed. This is an apparatus for obtaining an oxygen-enriched gas by alternately performing a desorption step in which nitrogen is desorbed to reduce nitrogen and the adsorbent is regenerated.

【0004】かかる圧力変動吸着法により生成された酸
素濃縮気体は、ほぼ絶乾に近い乾燥状態を示す。このよ
うな気体を使用者が呼吸用として吸入すると、呼吸器、
特に鼻孔や喉の内部が乾燥し不快感を覚えたり、肺に直
接届いた場合粘膜を傷つけ体調を害するなどの問題点が
あり、別途加湿器を用いて水分補給する必要がある。
[0004] The oxygen-enriched gas produced by such a pressure fluctuation adsorption method shows a dry state which is almost completely dry. When the user inhales such a gas for respiration,
In particular, there is a problem that the inside of the nostrils and throat is dry and uncomfortable, and when it reaches the lungs directly, it damages the mucous membrane and impairs the physical condition. Therefore, it is necessary to separately supply water using a humidifier.

【0005】かかる加湿器としては、密閉された器の中
に水を入れて、その水中に酸素濃縮気体をくぐらせるバ
ブリング加湿器や、酸素濃縮気体を加湿水表面上を通過
させ、蒸発した水分で加湿する蒸発式加湿器がある。こ
れらは、何れも水を使用し、使用者は常に加湿器内の水
の補充や交換、雑菌の発生を防ぐための洗浄と言った加
湿水の管理が必要となり、手間がかかると同時に、水交
換後の加湿器着脱部からの酸素濃縮気体洩れなど新たな
問題を引き起こす結果となっている。
[0005] As such a humidifier, a bubbling humidifier in which water is poured into a sealed container and oxygen-enriched gas is passed through the water, or the oxygen-enriched gas is passed over the surface of the humidified water to evaporate water There is an evaporative humidifier that humidifies with. All of these use water, and the user always needs to manage the humidifying water, such as replenishing or replacing the water in the humidifier, and cleaning to prevent the generation of various bacteria. This results in a new problem such as leakage of oxygen-enriched gas from the humidifier attachment / detachment section after replacement.

【0006】これらの不具合を解消する方法として、特
開平2−99113号公報に記載の水蒸気透過性中空糸
膜を利用し、酸素濃縮気体を加湿する膜式加湿器を備え
た酸素濃縮装置が考えられた。かかる酸素濃縮装置は原
料加圧空気中の水分、或いは吸着塔の再生ガス中の水分
の何れか使用して、酸素濃縮気体を加湿するものであ
る。
As a method for solving these problems, an oxygen concentrating apparatus provided with a membrane humidifier for humidifying an oxygen-enriched gas using a water vapor permeable hollow fiber membrane described in Japanese Patent Application Laid-Open No. 2-99113 is considered. Was done. Such an oxygen concentrator humidifies the oxygen-enriched gas by using either the moisture in the raw material pressurized air or the moisture in the regeneration gas of the adsorption tower.

【0007】かかる装置においては、全原料加圧空気を
水蒸気透過性中空糸を装填したモジュールに供給した
後、吸着塔に空気を供給するため、加湿度の調整が困難
であり、特に、製品酸素流量が少ない場合には、水分が
過剰になりドレンの発生が起こるという問題点がある。
In such an apparatus, since all the raw material pressurized air is supplied to the module loaded with the water vapor permeable hollow fiber, and then the air is supplied to the adsorption tower, it is difficult to adjust the humidification. When the flow rate is small, there is a problem that moisture is excessive and drain is generated.

【0008】これに対して特開平5−49697号公報
に記載のように過剰の水分を別の膜式加湿(除湿)器を
用いて除湿し、ドレンとして廃棄する方法や、特開平8
−196635号公報に記載のように製品酸素ガスを加
湿するルートにバイパスルートを設け加湿度を調節する
方法が見出されている。しかし、いずれの方法も、必要
とする加湿度の制御が難しく、複数の膜式加湿(除湿)
モジュールや複雑な配管系流量制御系が必要など、問題
点が多い。
On the other hand, as described in JP-A-5-49697, a method of dehumidifying excess moisture by using another film-type humidifying (dehumidifying) device and disposing it as drain is disclosed in JP-A-5-49697.
As described in JP-A-196635, a method of adjusting a humidification by providing a bypass route in a route for humidifying product oxygen gas has been found. However, it is difficult to control the required humidification by any of the methods, and a plurality of film-type humidification (dehumidification) is required.
There are many problems, such as the need for modules and complicated piping flow control systems.

【0009】更には、該中空糸を直接加湿水と接触さ
せ、水分を中空糸内部を流通する酸素に供給する方法と
して、特開平9−276408号公報に記載の酸素濃縮
装置が考えられた。しかし、本方式においても加湿水分
が過剰になりドレンの発生や、加湿度調整が困難である
ことや、加湿水交換といった取扱性の悪さなどの問題点
がある。
Further, as a method of bringing the hollow fiber into direct contact with humidified water and supplying the water to oxygen flowing inside the hollow fiber, an oxygen concentrating device described in Japanese Patent Application Laid-Open No. 9-276408 has been considered. However, this method also has problems such as excessive humidification moisture, drainage, difficulty in adjusting humidification, and poor handling such as humidification water exchange.

【0010】[0010]

【発明が解決しようとする課題】本発明は、従来の膜式
加湿器を備えた酸素濃縮装置で生じる種々の問題点を解
消し、水の補充や交換を必要とせずに使用可能であり、
且つ大気圧空気の相対湿度と略同じレベルに加湿するこ
とが可能な呼吸用気体の加湿器を備えた酸素濃縮装置を
提供することを目的とする。
SUMMARY OF THE INVENTION The present invention solves various problems that occur in a conventional oxygen concentrator equipped with a membrane humidifier, and can be used without the need for refilling or replacing water.
It is another object of the present invention to provide an oxygen concentrator provided with a humidifier for breathing gas capable of humidifying to a level substantially equal to the relative humidity of atmospheric pressure air.

【0011】[0011]

【課題を解決するための手段】本出願人はかかる課題に
対して、鋭意検討した結果、中空糸膜式の加湿器の水分
供給源として原料加圧空気ではなく、大気圧の外気空気
を利用して酸素濃縮気体を加湿する装置を見出したもの
である。
Means for Solving the Problems As a result of intensive studies on such a problem, the applicant of the present invention has found that as a water supply source of a hollow fiber membrane humidifier, outside air at atmospheric pressure is used instead of pressurized air as raw material. To humidify the oxygen-enriched gas.

【0012】即ち、本発明は、酸素よりも窒素を選択的
に吸着し得る吸着剤を充填した少なくとも1つの吸着床
と、該吸着床へ空気を供給する空気供給手段と、該吸着
床からの酸素濃縮気体を使用者に供給する酸素供給手段
を備えた圧力変動吸着型酸素濃縮装置において、該酸素
濃縮気体を加湿する中空糸状水分透過膜で構成される加
湿用モジュールを備え、該中空糸膜内側を該酸素濃縮気
体が流通し、外側が大気圧空気に接触していることを特
徴とする圧力変動吸着型酸素濃縮装置を提供するもので
ある。
That is, the present invention provides at least one adsorption bed filled with an adsorbent capable of selectively adsorbing nitrogen rather than oxygen, air supply means for supplying air to the adsorption bed, A pressure fluctuation adsorption type oxygen concentrator equipped with an oxygen supply means for supplying an oxygen-enriched gas to a user, comprising: a humidifying module comprising a hollow fiber-shaped moisture permeable membrane for humidifying the oxygen-enriched gas; It is an object of the present invention to provide a pressure fluctuation adsorption type oxygen concentrator characterized in that the oxygen-concentrated gas flows inside and the outside is in contact with atmospheric pressure air.

【0013】また、本発明はかかる水分透過膜が、内径
1.0mm〜5.0mmの中空糸であることを特徴とす
る圧力変動吸着型酸素濃縮装置を提供するものである。
The present invention also provides a pressure fluctuation adsorption type oxygen concentrator characterized in that the moisture permeable membrane is a hollow fiber having an inner diameter of 1.0 mm to 5.0 mm.

【0014】[0014]

【発明の実施の形態】以下に本発明の酸素濃縮装置の好
適な具体的実施例について必要に応じて図面を用いなが
ら説明する。本発明の酸素濃縮装置に使用する膜式加湿
器の種類は、特に限定されるものではないが、膜の水蒸
気透過原理として、大別して水蒸気分圧差を利用して水
分を透過する非多孔質の溶解拡散膜と、分子篩作用を原
理として水蒸気分子を選択透過する微多孔質膜とが有
る。材質としてはフッ素系の樹脂膜を使用することが好
ましい。特に旭硝子(株)製のSUN SEP−W、デ
ュポン社製NAFION、宇部興産(株)製メンブレン
等が好ましい。但し、本物性を示す樹脂系材料である限
りフッ素系樹脂に限定されるものではない。又、本材質
は抗菌性樹脂として使用される場合も多く、医療用途に
は適している。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Preferred embodiments of the oxygen concentrator according to the present invention will be described below with reference to the drawings as necessary. The type of the membrane humidifier used in the oxygen concentrator of the present invention is not particularly limited. There are a dissolution-diffusion membrane and a microporous membrane that selectively permeates water vapor molecules based on the principle of molecular sieve action. It is preferable to use a fluorine resin film as a material. In particular, SUN SEP-W manufactured by Asahi Glass Co., Ltd., NAFION manufactured by DuPont, and a membrane manufactured by Ube Industries, Ltd. are preferable. However, the material is not limited to a fluorine-based resin as long as it is a resin-based material having the physical properties. In addition, this material is often used as an antibacterial resin, and is suitable for medical use.

【0015】中空糸の径は内径数μm〜数mmのものが
使用されるが、あまり細いと目詰まりの原因となり易
く、特に本発明の1.0〜5.0mmのものを使用する
のが好ましい。かかる口径は医療用酸素を流すのに必要
なチューブサイズとも一致し、使い易いものになってい
る。
The hollow fiber having a diameter of several μm to several mm is used. However, if the diameter is too small, clogging is likely to occur. Particularly, the fiber having a diameter of 1.0 to 5.0 mm of the present invention is preferably used. preferable. Such a diameter matches the tube size necessary for flowing medical oxygen, and is easy to use.

【0016】中空糸の長さとしては、少なくとも10c
m以上であることが好ましく、医療用酸素濃縮装置とし
て用いる場合は、10〜100cmであるものが好まし
い。100cm以上のものを使用することも可能である
が、圧力損出が発生するので使用流量を制限するなどの
考慮が必要であり、100cm以下の中空糸を複数本並
列で用いる方が圧損低減、小型化の面で有利である。
The length of the hollow fiber is at least 10 c
m or more, and preferably 10 to 100 cm when used as a medical oxygen concentrator. Although it is possible to use those having a diameter of 100 cm or more, it is necessary to consider the use flow rate because pressure loss occurs, and it is better to use a plurality of hollow fibers of 100 cm or less in parallel to reduce the pressure loss. This is advantageous in terms of miniaturization.

【0017】本発明に用いる加湿器は、かかる中空糸を
用いたモジュールであって、中空糸の内側を乾燥状態の
酸素濃縮気体を通過させ、外側は大気に開放された状態
に置く。中空糸自体には強度確保の為にメッシュ構造の
補強材を備えるものが好ましい。また乾燥酸素濃縮気体
の導入部、加湿酸素濃縮気体の導出部は樹脂製の酸素濃
縮器本体とワンタッチで取付け、取外しが可能なものが
好ましい。
The humidifier used in the present invention is a module using such a hollow fiber, in which the inside of the hollow fiber is made to pass oxygen-enriched gas in a dry state, and the outside is kept open to the atmosphere. The hollow fiber itself is preferably provided with a reinforcing material having a mesh structure in order to secure strength. Further, it is preferable that the introduction portion of the dry oxygen concentrated gas and the outlet portion of the humidified oxygen concentrated gas can be attached to and detached from the resin oxygen concentrator body with one touch.

【0018】また、本願発明の酸素濃縮装置に用いられ
る該空気供給手段が、吸着工程においては該吸着床に原
料空気を供給するためのコンプレッサー手段として機能
する酸素濃縮装置が用いられる。
Further, the air supply means used in the oxygen concentrator of the present invention uses an oxygen concentrator which functions as a compressor means for supplying raw air to the adsorption bed in the adsorption step.

【0019】又、本願発明に利用する水分透過膜の特徴
として、水分透過速度には温度依存性が有り、使用環境
温度を高めることにより瞬時に目標の加湿度を得ること
が可能となる。更には、本特性を利用することにより水
分透過膜の使用本数や長さを縮小でき、比較的高価な本
水分透過膜のコストダウンにもつながる。また、コンプ
レッサーや吸着床など装置内の温度を一定にする為、冷
却ファンが使用されているが、かかる冷却風を本発明の
装置の膜式加湿器の大気側に当てるように構成すること
や、吸着床の脱着工程で発生する水分リッチな脱着空気
を本発明の装置の膜式加湿器の大気側に当てるように構
成することも加湿度を得る為には好ましい。
Further, as a feature of the moisture permeable membrane used in the present invention, the moisture permeation rate has a temperature dependency, and a target humidification can be obtained instantaneously by increasing the use environment temperature. Furthermore, by utilizing this characteristic, the number and length of the water permeable membrane used can be reduced, which leads to a reduction in the cost of the relatively expensive water permeable membrane. Further, a cooling fan is used to keep the temperature inside the device such as a compressor or an adsorption bed constant.However, it is possible to configure such that the cooling air is blown to the atmosphere side of the membrane humidifier of the device of the present invention. In order to obtain humidification, it is also preferable that moisture-rich desorption air generated in the desorption step of the adsorption bed be applied to the atmosphere side of the membrane humidifier of the apparatus of the present invention.

【0020】本発明は、膜式加湿器を備えた圧力変動吸
着型酸素濃縮装置であるが、乾燥気体である酸素ボンベ
を供給源とする酸素供給装置、固体電解質膜を酸素供給
源とする酸素供給装置に対しても応用することは可能で
ある。
The present invention relates to a pressure fluctuation adsorption-type oxygen concentrator equipped with a membrane humidifier. The oxygen supply device uses a dry gas oxygen cylinder as a supply source, and the oxygen supply device uses a solid electrolyte membrane as an oxygen supply source. It is also possible to apply to a supply device.

【0021】[0021]

【実施例】以下、図面を用いて更に詳細に説明する。図
1に本願発明の好ましい態様を示す。即ち、窒素を選択
的に吸着する吸着剤としてゼオライト系吸着剤を充填し
た1個の吸着塔2に加圧空気を供給するコンプレッサー
1を備え、非吸着の濃縮酸素をサージタンク3に貯留
後、水蒸気選択透過性中空糸膜4を備えた加湿器5を通
って、患者に濃縮酸素が供給される。かかる水蒸気透過
性中空糸膜は、水蒸気分圧差を利用して水分を透過する
非多孔質のフッ素樹脂系溶解拡散膜(デュポン社製NA
FION膜)を用いた。内径が1.5mm、長さ60c
mの中空糸6本を並列状態にして用いた。加湿ボックス
には外気空気と接触している。
BRIEF DESCRIPTION OF THE DRAWINGS FIG. FIG. 1 shows a preferred embodiment of the present invention. That is, a compressor 1 for supplying pressurized air to one adsorption tower 2 filled with a zeolite-based adsorbent as an adsorbent for selectively adsorbing nitrogen is provided. After storing non-adsorbed concentrated oxygen in a surge tank 3, The concentrated oxygen is supplied to the patient through the humidifier 5 having the water vapor selectively permeable hollow fiber membrane 4. Such a water-vapor-permeable hollow fiber membrane is a non-porous fluororesin-based dissolution-diffusion membrane (NA manufactured by DuPont) that transmits moisture by utilizing a partial pressure difference of water vapor.
FION film). Inner diameter 1.5mm, length 60c
6 m hollow fibers were used in parallel. The humidification box is in contact with outside air.

【0022】図2は、本発明の酸素濃縮装置の概観図、
図3は加湿器3部分の概観図を示す。
FIG. 2 is a schematic view of an oxygen concentrator according to the present invention.
FIG. 3 shows a schematic view of the humidifier 3 part.

【0023】温度25℃、湿度60%RHの環境下でか
かる酸素濃縮装置を起動し、発生した酸素濃縮気体湿度
を図4に示す。結果、酸素濃縮気体の取出し流量が1L
/分の場合、環境湿度の90%、3L/分の場合、環境
湿度の85%の湿度を有する酸素濃縮気体を得ることが
出来た。
FIG. 4 shows the generated oxygen-enriched gas humidity when the oxygen concentrator is activated under an environment of a temperature of 25 ° C. and a humidity of 60% RH. As a result, the removal flow rate of the oxygen-enriched gas is 1 L
/ Min, 90% of the environmental humidity, and 3 L / min, an oxygen-enriched gas having a humidity of 85% of the environmental humidity could be obtained.

【0024】[0024]

【発明の効果】本発明の酸素濃縮装置においては、中空
糸膜式加湿器を用い、水分補給する必要なく医療用酸素
濃縮空気を加湿することができる。更に、本願発明の酸
素濃縮装置の加湿器においては、特別に加湿量調整のた
めの流量制御系なしに、患者に供給される酸素濃縮空気
は大気中の空気とほぼ同じ加湿度を示すことができる。
According to the oxygen concentrating apparatus of the present invention, the oxygen enriched air for medical use can be humidified without using a hollow fiber membrane type humidifier. Further, in the humidifier of the oxygen concentrator according to the present invention, the oxygen-concentrated air supplied to the patient exhibits almost the same humidification as the air in the atmosphere without a flow control system for adjusting the humidification amount. it can.

【0025】かかる酸素濃縮空気は、外気の湿度の変化
によって当然に酸素濃縮空気の湿度も変化するが、通常
の人が呼吸している空気と同じレベルの加湿度を維持す
ることができる。但し、酸素濃縮空気の流れによる乾燥
効果もあることから、酸素濃縮装置の酸素濃縮空気供給
流量としては、5L/分以下で用いることが好ましい。
The oxygen-enriched air naturally changes its humidity due to a change in the humidity of the outside air, but can maintain the same level of humidification as the air breathed by a normal person. However, since there is also a drying effect by the flow of the oxygen-enriched air, it is preferable to use the oxygen-enriched air supply flow rate of 5 L / min or less as the oxygen-enriched air supply flow rate.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の圧力変動吸着型酸素濃縮装置のフロ
ー。
FIG. 1 is a flow chart of a pressure fluctuation adsorption type oxygen concentrator according to the present invention.

【図2】本発明の実施例である圧力変動吸着型酸素濃縮
装置の外観概略図。
FIG. 2 is a schematic external view of a pressure fluctuation adsorption type oxygen concentrator according to an embodiment of the present invention.

【図3】本発明の実施例である圧力変動吸着型酸素濃縮
装置の加湿器の外観概略図。
FIG. 3 is a schematic external view of a humidifier of the pressure fluctuation adsorption type oxygen concentrator according to the embodiment of the present invention.

【図4】本発明の圧力変動吸着型酸素濃縮装置の酸素濃
縮気体湿度。
FIG. 4 shows the oxygen concentration gas humidity of the pressure fluctuation adsorption type oxygen concentrator of the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 酸素よりも窒素を選択的に吸着し得る吸
着剤を充填した少なくとも1つの吸着床と、該吸着床へ
空気を供給する空気供給手段と、該吸着床からの酸素濃
縮気体を使用者に供給する酸素供給手段を備えた圧力変
動吸着型酸素濃縮装置において、該酸素濃縮気体を加湿
する中空糸状水分透過膜で構成される加湿用モジュール
を備え、該中空糸膜内側を該酸素濃縮気体が流通し、外
側が大気圧空気に接触していることを特徴とする圧力変
動吸着型酸素濃縮装置。
1. At least one adsorption bed filled with an adsorbent capable of selectively adsorbing nitrogen over oxygen, air supply means for supplying air to the adsorption bed, and oxygen-enriched gas from the adsorption bed. A pressure fluctuation adsorption-type oxygen concentrator provided with an oxygen supply means for supplying a user with a humidifying module comprising a hollow fiber-shaped moisture permeable membrane for humidifying the oxygen-enriched gas, wherein the inside of the hollow fiber membrane is provided with the oxygen. A pressure fluctuation adsorption type oxygen concentrator characterized in that a concentrated gas flows and the outside is in contact with atmospheric pressure air.
【請求項2】 該水分透過膜が、内径1.0mm〜5.
0mmの中空糸であることを特徴とする請求項1に記載
の圧力変動吸着型酸素濃縮装置。
2. The water permeable membrane according to claim 1, wherein the inner diameter is from 1.0 mm to 5.0 mm.
The pressure fluctuation adsorption type oxygen concentrator according to claim 1, wherein the apparatus is a 0 mm hollow fiber.
JP11041483A 1999-02-19 1999-02-19 Pressure fluctuation adsorption type oxygen thickener Pending JP2000237317A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11041483A JP2000237317A (en) 1999-02-19 1999-02-19 Pressure fluctuation adsorption type oxygen thickener

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11041483A JP2000237317A (en) 1999-02-19 1999-02-19 Pressure fluctuation adsorption type oxygen thickener

Publications (1)

Publication Number Publication Date
JP2000237317A true JP2000237317A (en) 2000-09-05

Family

ID=12609604

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11041483A Pending JP2000237317A (en) 1999-02-19 1999-02-19 Pressure fluctuation adsorption type oxygen thickener

Country Status (1)

Country Link
JP (1) JP2000237317A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003010630A (en) * 2001-07-03 2003-01-14 Kofurotsuku Kk Nitrogen concentration gas humidifying device
JP2004008620A (en) * 2002-06-10 2004-01-15 Teijin Ltd Humidifier
JP2007530157A (en) * 2004-03-26 2007-11-01 ベイポサーム,インコーポレイティド Apparatus and method for supplying water vapor to gas
AU2004296144B2 (en) * 2003-12-15 2011-06-16 Teijin Limited Humidifying device and oxygen concentrating system

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2003010630A (en) * 2001-07-03 2003-01-14 Kofurotsuku Kk Nitrogen concentration gas humidifying device
JP2004008620A (en) * 2002-06-10 2004-01-15 Teijin Ltd Humidifier
AU2004296144B2 (en) * 2003-12-15 2011-06-16 Teijin Limited Humidifying device and oxygen concentrating system
JP2007530157A (en) * 2004-03-26 2007-11-01 ベイポサーム,インコーポレイティド Apparatus and method for supplying water vapor to gas

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