JP2003180838A - Medical oxygen concentration device - Google Patents
Medical oxygen concentration deviceInfo
- Publication number
- JP2003180838A JP2003180838A JP2001389371A JP2001389371A JP2003180838A JP 2003180838 A JP2003180838 A JP 2003180838A JP 2001389371 A JP2001389371 A JP 2001389371A JP 2001389371 A JP2001389371 A JP 2001389371A JP 2003180838 A JP2003180838 A JP 2003180838A
- Authority
- JP
- Japan
- Prior art keywords
- oxygen
- adsorption
- adsorbed
- adsorbent
- adsorption bed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Separation Of Gases By Adsorption (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
- Solid-Sorbent Or Filter-Aiding Compositions (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、窒素より酸素を選
択的に吸着する吸着剤を用いた圧力変動吸着方法によ
り、空気中から酸素を濃縮して使用者に供給する医療用
圧力変動吸着型酸素濃縮装置に関する。更に詳細には、
大気中の酸素と水分子を同時に吸着させ、該酸素と該水
分子を同時に回収、使用者に提供する事により、濃縮酸
素を加湿するため加湿手段が省略された圧力変動吸着型
酸素濃縮装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a pressure fluctuation adsorption type for medical use which concentrates oxygen from the air and supplies it to a user by a pressure fluctuation adsorption method using an adsorbent that selectively adsorbs oxygen from nitrogen. The present invention relates to an oxygen concentrator. More specifically,
The present invention relates to a pressure fluctuation adsorption type oxygen concentrator in which a humidifying means is omitted to humidify concentrated oxygen by simultaneously adsorbing oxygen and water molecules in the atmosphere, recovering the oxygen and water molecules at the same time, and providing the oxygen to the user. It is a thing.
【0002】[0002]
【従来の技術】近年、喘息、肺気腫症、慢性気管支炎な
どの呼吸器系疾患に苦しむ患者が増加する傾向がある
が、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
から酸素吸入療法用の治療装置として、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 tends to increase. One of the most effective treatment methods is oxygen inhalation therapy, Oxygen concentrators that directly separate oxygen-enriched gas from the inside have been developed, and are becoming increasingly popular as therapeutic devices for oxygen inhalation therapy because of convenience in use and ease of maintenance.
【0003】かかる酸素濃縮装置として、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1個或いは複
数の吸着床を備えた吸着型酸素濃縮装置が知られ、中で
も空気供給手段としてコンプレッサーを用いた圧力変動
吸着型の酸素濃縮装置が、在宅酸素吸入療法の治療装置
として用いられている。As such an oxygen concentrator, there is known an adsorption type oxygen concentrator having one or a plurality of adsorbent beds filled with an adsorbent capable of selectively adsorbing nitrogen rather than oxygen. Among them, a compressor is used as an air supply means. A pressure fluctuation adsorption type oxygen concentrating device using is used as a therapeutic device for home oxygen inhalation therapy.
【0004】通常、圧力変動吸着型酸素濃縮装置は、空
気圧縮手段で吸着床に空気を供給し、床内を加圧状態に
することにより空気中の窒素や水を吸着させ、未吸着の
酸素を取出す吸着工程と、吸着工程が終了した後、該吸
着床を大気開放して減圧し、吸着されている窒素や水を
脱着させ吸着剤を再生する脱着工程を繰り返すPSA
(Pressure Swing Adsorption)、または空気圧縮手段
を逆に用いて吸着床内が負圧になるまで排気を行い、吸
着されている窒素や水を脱着させ吸着剤を再生する脱着
工程を繰り返し実施するVPSA(Vacuum Pressure Sw
ing Adsorption)により酸素濃縮空気を生成している。Normally, the pressure fluctuation adsorption type oxygen concentrator supplies air to the adsorption bed by means of an air compression means to bring the inside of the bed into a pressurized state so as to adsorb nitrogen and water in the air, and to absorb unadsorbed oxygen. PSA for repeating the adsorption step for extracting and the desorption step for desorbing adsorbed nitrogen and water to regenerate the adsorbent after repeating the adsorption step and decompressing the adsorption bed to the atmosphere
(Pressure Swing Adsorption), or reversely using air compression means, exhausting until the pressure inside the adsorption bed becomes negative pressure, and repeating the desorption process of desorbing adsorbed nitrogen and water to regenerate the adsorbent (Vacuum Pressure Sw
ing Adsorption) to generate oxygen-enriched air.
【0005】かかる吸着型酸素濃縮装置には、酸素分離
のため吸着剤として酸素より窒素を選択的に吸着するゼ
オライト5Aや13X、さらに近年では13X型ゼオラ
イトを基にしてカチオン種がLiに交換されたもの、元
素の構成比率を変化させカチオンを多く含むゼオライト
が用いられ、かかる吸着剤に吸着され難い酸素を回収
し、使用者に提供する方式が採用されている。In the adsorption type oxygen concentrator, zeolite 5A or 13X which selectively adsorbs nitrogen rather than oxygen as an adsorbent for oxygen separation, and more recently, a cation species is exchanged with Li based on a 13X type zeolite. In addition, a zeolite containing a large amount of cations by changing the composition ratio of elements is used, and a method is adopted in which oxygen that is difficult to be adsorbed by such an adsorbent is recovered and provided to the user.
【0006】[0006]
【発明が解決しようとする課題】かかる酸素濃縮装置に
より生成される酸素ガスは、呼吸器系疾患を患う患者に
使用されることから、その安全性はもちろんのこと、酸
素濃度など装置性能の安定性、さらには供給されるガス
は適度な湿度に加湿されていることが望まれている。し
かし、従来の酸素濃縮装置に使用される吸着剤は、窒素
を吸着する際に水分子を同時に吸着除去するため、生成
される酸素ガスは非常に乾燥している。Oxygen gas produced by such an oxygen concentrator is used for patients suffering from respiratory diseases, so that not only the safety but also the stability of the device performance such as oxygen concentration is stable. In addition, it is desired that the supplied gas is humidified to an appropriate humidity. However, since the adsorbent used in the conventional oxygen concentrator simultaneously adsorbs and removes water molecules when adsorbing nitrogen, the oxygen gas produced is very dry.
【0007】この乾燥状態の酸素を使用者である呼吸系
疾患の患者へ供給すると、鼻の痛みや喉の渇きなどを訴
え、治療行為に障害を及ぼす。よって、かかる医療用酸
素濃縮装置には酸素ガスの加湿手段として、容器に水を
充填してその中を酸素ガスでバブリング、或いは水表面
を通過させる水接触式加湿器が搭載されている。When this dry oxygen is supplied to a user who has a respiratory disease, he or she complains of nasal pain or thirst, and impairs the treatment. Therefore, such a medical oxygen concentrator is equipped with a water contact type humidifier as a means for humidifying oxygen gas, in which water is filled in a container and oxygen gas is bubbled through the container or passed through the water surface.
【0008】しかし、かかる酸素濃縮装置では、水接触
式加湿器の接続不良などに起因する酸素ガス漏れによ
り、患者は酸素不足状態を引き起こし、呼吸困難に至る
ことが極稀に発生している。この水接触式加湿器による
事故を回避するため、水接触式加湿器の酸素濃縮装置へ
の接続容易化や接続不良検知技術などが検討されてお
り、加湿器接続不良を改善する方策としては、特許2773
100号公報に記載のような加湿器接続部位の構造改善
や、リミットスイッチなどを用いた接続不良の検出、更
には高分子加湿膜を装置に組み込み、空気中の水分子を
加湿膜に接触させることにより、水分子に膜を透過させ
乾燥酸素を加湿するなど様々な公知の手段が検討されて
いる。However, in such an oxygen concentrator, an oxygen deficiency is caused in the patient due to oxygen gas leakage due to a poor connection of the water contact type humidifier, and it is extremely rare that the patient has respiratory distress. In order to avoid accidents due to this water contact type humidifier, facilitation of connection of the water contact type humidifier to the oxygen concentrator and connection failure detection technology are being studied, and as a measure to improve the connection failure of the humidifier, Patent 2773
Improvement of the structure of the humidifier connection part as described in Japanese Patent No. 100, detection of connection failure using a limit switch, etc., and further incorporation of a polymer humidifying film into the device to bring water molecules in the air into contact with the humidifying film. Therefore, various known means such as permeation of water molecules through the membrane to humidify dry oxygen have been investigated.
【0009】しかし、高分子加湿膜は非常に高価である
ことや、酸素ガスの加湿度が外気湿度に支配され、加湿
度調整が困難であるなど未だ課題は多く、完全な改善が
講じられたとは言い難い。However, there are still many problems such as the fact that the polymer humidifying membrane is very expensive and that the humidity of oxygen gas is dominated by the humidity of the outside air, making it difficult to adjust the humidity. Is hard to say.
【0010】本発明は、上記課題を解決するものであ
り、在宅で長期使用する医療機器である吸着型酸素濃縮
装置の使用時の安全性と快適性を向上し、患者の精神的
負担を低減するものである。The present invention solves the above problems and improves the safety and comfort when using an adsorption type oxygen concentrator, which is a medical device used at home for a long period of time, and reduces the mental burden on the patient. To do.
【0011】[0011]
【課題を解決するための手段】本発明者はかかる課題に
対して鋭意検討した結果、吸着剤に酸素と水を吸着さ
せ、これを脱離、回収する事により、加湿された酸素を
生成することができることを見出したものである。Means for Solving the Problems As a result of diligent studies on the above problems, the present inventor adsorbed oxygen and water to the adsorbent, and desorbed and recovered the adsorbent to generate humidified oxygen. I found that I could do it.
【0012】即ち本発明は、窒素より酸素を選択的に吸
着し得る吸着剤を充填した少なくとも1本の吸着床、該
吸着床に加圧空気を供給する空気供給手段、該吸着床の
加圧空気供給の反対側に窒素を排出するポートを備える
ともに、該吸着床に吸着された酸素を回収する酸素回収
手段、回収された酸素ガス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の医療用酸素濃縮装置にお
いて、該酸素回収手段が該吸着床の加圧空気供給側から
吸着ガスを回収する手段であり、回収初期の吸着ガスを
系外に排気するポートを備えるとともに、回収した吸着
ガスをタンク手段に加圧貯留させる手段を備えることを
特徴とする医療用酸素濃縮装置を提供するものである。That is, according to the present invention, at least one adsorbent bed filled with an adsorbent capable of selectively adsorbing oxygen over nitrogen, air supply means for supplying pressurized air to the adsorbent bed, and pressurization of the adsorbent bed Pressure fluctuation adsorption equipped with a port for discharging nitrogen on the opposite side of the air supply, an oxygen recovery means for recovering the oxygen adsorbed in the adsorption bed, and an oxygen supply means for supplying the recovered oxygen gas to the user. Type medical oxygen concentrator, the oxygen recovery means is means for recovering the adsorbed gas from the pressurized air supply side of the adsorption bed, and is equipped with a port for exhausting the adsorbed gas at the initial stage of recovery to the outside of the system, The present invention provides a medical oxygen concentrating device comprising means for pressurizing and storing the adsorbed gas in a tank means.
【0013】また本発明は、かかる吸着剤が4A型ゼオ
ライト、或いは分子篩い活性炭であることを特徴とする
医療用酸素濃縮装置を提供するものである。The present invention also provides a medical oxygen concentrator, wherein the adsorbent is 4A type zeolite or molecular sieve activated carbon.
【0014】[0014]
【発明の実施の形態】本発明の医療用酸素濃縮装置は、
窒素より酸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本の吸着床と、該吸着床に空気を供給する空
気供給手段と、該吸着床に吸着された酸素を回収する酸
素回収手段と、回収されたガス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の医療用酸素濃縮装置
であり、大気中の酸素と水分子を同時に吸着させ、該酸
素と該水分子を同時に回収する機能を備える。かかる装
置により加湿された酸素が生成され、使用者たる患者は
水接触式加湿器の水補給や着脱の手間から開放され、日
常手入れの精神的負担から解放され、かつ加湿器の取り
付け不良にともなう体調悪化の危険性低減を実現する装
置である。BEST MODE FOR CARRYING OUT THE INVENTION The medical oxygen concentrator of the present invention comprises:
At least one adsorption bed filled with an adsorbent capable of selectively adsorbing oxygen from nitrogen, air supply means for supplying air to the adsorption bed, and oxygen recovery means for recovering oxygen adsorbed in the adsorption bed And a pressure fluctuation adsorption type medical oxygen concentrator equipped with an oxygen supply means for supplying the recovered gas to the user, wherein oxygen and water molecules in the atmosphere are adsorbed at the same time, and the oxygen and water molecules are absorbed. Equipped with a function to collect at the same time. Humidified oxygen is generated by such a device, the user as a user can be freed from the trouble of replenishing and attaching and detaching the water contact type humidifier, is freed from the mental burden of daily maintenance, and is attached to the humidifier poorly. It is a device that reduces the risk of physical condition deterioration.
【0015】本件発明で提供する医療用酸素濃縮装置に
おいては、吸着床として4A型ゼオライトを充填した吸
着筒を用いる事により、吸着床に導入された空気中の酸
素と水分子を吸着し、吸着され難い窒素は吸着床の加圧
空気供給側の反対側に設けた排気ポートから系外に排気
される。そして吸着剤中に吸着された酸素と水分子は、
脱着工程で吸着剤から脱離、回収され、使用者たる患者
に供給される。この時、回収ガス中には酸素と水分子と
が同時に回収されるため、この時点で加湿されており、
特別な加湿手段を必要とせず、患者は水接触式加湿器へ
の水補給を必要とせず、加湿器そのものが不要となるた
めに加湿器取付け不良などの問題も解消する。In the medical oxygen concentrator provided by the present invention, by using an adsorption column filled with 4A type zeolite as an adsorption bed, oxygen and water molecules in the air introduced into the adsorption bed are adsorbed and adsorbed. Nitrogen which is difficult to be discharged is exhausted out of the system through an exhaust port provided on the opposite side of the adsorption bed to the pressurized air supply side. And the oxygen and water molecules adsorbed in the adsorbent,
In the desorption process, it is desorbed from the adsorbent, collected, and supplied to the patient as a user. At this time, since oxygen and water molecules are simultaneously recovered in the recovered gas, it is humidified at this point,
No special humidifying means is required, the patient does not need to replenish water to the water contact type humidifier, and the humidifier itself is not required. Therefore, problems such as improper mounting of the humidifier are eliminated.
【0016】使用可能な吸着剤としては4A型ゼオライ
トの他、分子篩い活性炭を用いることも可能である。As the adsorbent that can be used, in addition to 4A type zeolite, it is also possible to use molecular sieve activated carbon.
【0017】吸着床にコンプレッサーで加圧空気を導入
すると、拡散速度に勝る水分子、酸素分子の順で吸着が
行われる。未吸着の窒素は吸着床の排気ポートから排気
されるが、吸着床内の吸着圧が高くなると窒素分子の吸
着が開始されるため、窒素分子の吸着が始まる前に脱着
回収工程に移行する。When compressed air is introduced into the adsorption bed by a compressor, adsorption is carried out in the order of water molecules and oxygen molecules, which have higher diffusion rates. The non-adsorbed nitrogen is exhausted from the exhaust port of the adsorption bed, but when the adsorption pressure in the adsorption bed becomes high, the adsorption of nitrogen molecules is started, and therefore the process proceeds to the desorption recovery step before the adsorption of nitrogen molecules is started.
【0018】脱着回収工程は、吸着床の加圧空気供給端
側からコンプレッサーで減圧回収することで実施する。
水分子は加圧空気供給端側の吸着剤に主に吸着するた
め、水分回収のためには加圧空気供給端側から吸着ガス
を回収する必要がある。回収初期のガス中には吸着床内
に残留する窒素ガスが含まれるため、かかる回収ガスの
初期画分は三方弁などの流路切替バルブから系外に排気
し、酸素および水分画分を製品タンクに貯留する。The desorption / recovery step is carried out by pressure-recovering with a compressor from the pressurized air supply end side of the adsorption bed.
Since water molecules are mainly adsorbed by the adsorbent on the pressurized air supply end side, it is necessary to recover the adsorbed gas from the pressurized air supply end side for water recovery. Since the nitrogen gas remaining in the adsorption bed is contained in the gas at the initial stage of recovery, the initial fraction of the recovered gas is exhausted outside the system from the flow path switching valve such as the three-way valve, and the oxygen and moisture fractions are Store in a tank.
【0019】図1に、本発明の医療用酸素濃縮装置の一
例を示す。かかる装置は窒素より酸素を選択的に吸着す
る吸着剤である4A型ゼオライトを充填した1本の吸着
筒を備えた圧力変動吸着型酸素濃縮装置であり、コンプ
レッサーにポペット弁を備えることで加圧、減圧双方の
機能を持たせたものである。FIG. 1 shows an example of the medical oxygen concentrator of the present invention. Such a device is a pressure fluctuation adsorption type oxygen concentrator equipped with one adsorption cylinder filled with a 4A type zeolite which is an adsorbent that selectively adsorbs oxygen from nitrogen, and a compressor is equipped with a poppet valve to pressurize. It has both the function of reducing pressure.
【0020】外気から原料空気を取り入れ、コンプレッ
サーからポペット弁を介して吸着筒に加圧空気を供給す
る。吸着筒内では水分子および酸素が吸着剤に吸着し、
未吸着の窒素は吸着筒の反対側端部に設けられた排気ポ
ートからオリフィス、逆止弁を介して大気中に排気され
る。一方、脱着、回収工程はポペット弁の流路を切り替
えることにより開始される。即ち、吸着筒からコンプレ
ッサーを介して吸着した水分子および酸素を貯留タンク
へ回収する。その際、回収ガスの初期画分は窒素を含有
するため、三方弁から排気し、酸素リッチ画分のみを回
収する。貯留タンクの酸素は空気中の水分も同時に回収
するため、加湿されており、そのまま調圧弁、流量設定
器を経由して患者に供給される。Raw material air is taken from the outside air, and pressurized air is supplied from the compressor to the adsorption cylinder through the poppet valve. In the adsorption column, water molecules and oxygen are adsorbed on the adsorbent,
The unadsorbed nitrogen is exhausted into the atmosphere from an exhaust port provided at the opposite end of the adsorption cylinder through an orifice and a check valve. On the other hand, the desorption / recovery process is started by switching the flow path of the poppet valve. That is, water molecules and oxygen adsorbed from the adsorption column via the compressor are collected in the storage tank. At that time, since the initial fraction of the recovered gas contains nitrogen, it is exhausted from the three-way valve and only the oxygen-rich fraction is recovered. Oxygen in the storage tank is humidified because water in the air is also collected at the same time and is supplied to the patient as it is via the pressure regulating valve and the flow rate setting device.
【0021】このように弁の開閉制御により、拡散速度
差にともなう吸着分離を行い、水、酸素を吸着、窒素を
ガス中に残留させ、ついで脱着工程に入る事により、吸
着されている酸素分子と水分子を脱離、回収し、貯留タ
ンクに送り込む。かかる工程を順次切り替えることによ
り酸素を連続的に供給することが可能となる。By controlling the opening and closing of the valve in this way, adsorption separation according to the diffusion rate difference is carried out, water and oxygen are adsorbed, nitrogen is left in the gas, and then the desorption step is carried out, whereby the adsorbed oxygen molecules are adsorbed. Water molecules are desorbed, collected, and sent to a storage tank. By sequentially switching such steps, it becomes possible to continuously supply oxygen.
【0022】図2には、本発明の別の態様として、2本
の吸着筒を備えた医療用酸素濃縮装置の例を示す。窒素
より酸素を選択的に吸着する吸着剤である4A型ゼオラ
イトを充填した2本の吸着筒を備えた圧力変動吸着型酸
素濃縮装置であり、加圧用コンプレッサー、減圧用コン
プレッサーを組合せ、さらに流路切替手段として回転式
流路切替手段を搭載した酸素濃縮装置の例を示す。基本
的な装置構成要素の機能は図1の装置と同じであり、加
圧用コンプレッサーを用いて拡散速度差にともなう吸着
分離を行い、窒素をガス中に残留させ排気し、ついで脱
着工程に入り、減圧用コンプレッサーを用いて吸着され
ている酸素分子と水分離を脱離、回収し、貯留タンクに
送り込む。この時、流路の切替は回転式流路切替手段に
より吸着床は脱着工程から吸着工程に移行し、再度、酸
素の濃縮が開始される。FIG. 2 shows an example of a medical oxygen concentrator equipped with two adsorption cylinders as another embodiment of the present invention. A pressure fluctuation adsorption type oxygen concentrator equipped with two adsorption cylinders filled with 4A type zeolite, which is an adsorbent that selectively adsorbs oxygen from nitrogen, a pressurizing compressor and a depressurizing compressor are combined, and a flow path is further provided. An example of an oxygen concentrator equipped with a rotary flow path switching means as the switching means will be shown. The functions of the basic components of the apparatus are the same as those of the apparatus shown in FIG. 1. Adsorption separation is performed using a compression compressor due to the difference in diffusion rate, nitrogen is left in the gas and exhausted, and then the desorption process is started. A decompression compressor is used to desorb and collect adsorbed oxygen molecules and water separation, and send them to a storage tank. At this time, the flow passage is switched from the desorption process to the adsorption process by the rotary flow passage switching means, and the concentration of oxygen is started again.
【0023】流路切替手段として回転式開閉弁手段を用
いる場合には、弁の回転速度が開閉時間に反比例し、通
常、回転式開閉弁の回転はモーターを用いて電気的に制
御する。この電気的制御はコンプレッサーも同様で搭載
されているモーターの種類により異なる。交流電源用モ
ーターであれば通電する電源周波数制御、直流電源用モ
ーターであれば電圧制御により達成される。更にステッ
ピングモーターについては、通電のオン/オフの周波数
によりその回転数を制御する事が可能である。更に回転
計などに代表される回転数監視手段を有し、該回転数監
視手段の検出結果に基づき回転数を調整、安定化するフ
ィードバック回路などの回転数安定化手段により、装置
の安定性は更に向上する。When the rotary on-off valve means is used as the flow path switching means, the rotational speed of the valve is inversely proportional to the opening / closing time, and the rotation of the rotary on-off valve is usually electrically controlled by using a motor. This electrical control is the same for compressors and depends on the type of motor installed. This is achieved by controlling the frequency of the power supply for energizing AC motors and voltage control for DC power motors. Further, with respect to the stepping motor, it is possible to control the rotation speed of the stepping motor depending on the frequency of turning on / off the power. Further, it has a rotation speed monitoring means represented by a tachometer, etc., and the stability of the device is improved by a rotation speed stabilizing means such as a feedback circuit for adjusting and stabilizing the rotation speed based on the detection result of the rotation speed monitoring means Further improve.
【0024】流路切替手段として開閉式電磁弁を用いた
場合には、制御回路からの信号により開閉時間の制御が
可能である。When an opening / closing solenoid valve is used as the flow path switching means, the opening / closing time can be controlled by a signal from the control circuit.
【0025】また本発明の吸着型酸素濃縮装置に用いら
れる該コンプレッサー手段は、特に限定するものではな
く、レシプロタイプ、スクロールタイプ等のコンプレッ
サーを使用することが出来る。Further, the compressor means used in the adsorption type oxygen concentrator of the present invention is not particularly limited, and a reciprocating type compressor, a scroll type compressor or the like can be used.
【0026】[0026]
【発明の効果】本発明の吸着型酸素濃縮装置は、50H
z,60Hzの両周波数電源において異常なく運転を
し、40%程度の加湿酸素が得られ、患者の安全性、快
適性の向上を図ることが出来る。The adsorption-type oxygen concentrator of the present invention has a capacity of 50H.
It operates without abnormality in both z and 60 Hz power supplies, humidified oxygen of about 40% is obtained, and the safety and comfort of the patient can be improved.
【図1】本発明の医療用酸素濃縮装置である一筒式酸素
濃縮装置の概略構成図。FIG. 1 is a schematic configuration diagram of a one-cylinder oxygen concentrator that is a medical oxygen concentrator of the present invention.
【図2】本発明の医療用酸素濃縮装置である二筒式酸素
濃縮装置の概略構成図。FIG. 2 is a schematic configuration diagram of a two-cylinder oxygen concentrator that is a medical oxygen concentrator of the present invention.
1.コンプレッサー 2.吸着筒 3.オリフィス 4.逆止弁 5.三方弁 6.貯留タンク 7.調圧弁 8.流量設定器 9.切替制御手段 10.回転式開閉弁 11.減圧用コンプレッサー 1. compressor 2. Adsorption cylinder 3. Orifice 4. Check valve 5. Three-way valve 6. Storage tank 7. Regulator valve 8. Flow rate setting device 9. Switching control means 10. Rotary on-off valve 11. Decompression compressor
Claims (2)
剤を充填した少なくとも1本の吸着床、該吸着床に加圧
空気を供給する空気供給手段、該吸着床の加圧空気供給
の反対側に窒素を排出するポートを備えるともに、該吸
着床に吸着された酸素を回収する酸素回収手段、回収さ
れた酸素ガスを使用者に供給する酸素供給手段を備えた
圧力変動吸着型の医療用酸素濃縮装置において、該酸素
回収手段が該吸着床の加圧空気供給側から吸着ガスを回
収する手段であり、回収初期の吸着ガスを系外に排気す
るポートを備えるとともに、回収した吸着ガスをタンク
手段に加圧貯留させる手段を備えることを特徴とする医
療用酸素濃縮装置。1. At least one adsorbent bed filled with an adsorbent capable of selectively adsorbing oxygen from nitrogen, air supply means for supplying pressurized air to the adsorbent bed, and pressurized air supply for the adsorbent bed. A pressure fluctuation adsorption type medical device equipped with a port for discharging nitrogen on the opposite side, an oxygen recovery means for recovering oxygen adsorbed in the adsorption bed, and an oxygen supply means for supplying the recovered oxygen gas to a user. In the oxygen concentrating apparatus for use, the oxygen recovery means is a means for recovering the adsorbed gas from the pressurized air supply side of the adsorption bed, and is provided with a port for exhausting the adsorbed gas at the initial stage of recovery to the outside of the system, and the recovered adsorbed gas An oxygen concentrating device for medical use, comprising means for pressurizing and storing in a tank means.
子篩い活性炭であることを特徴とする請求項1に記載の
医療用酸素濃縮装置。2. The medical oxygen concentrator according to claim 1, wherein the adsorbent is 4A type zeolite or molecular sieve activated carbon.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001389371A JP2003180838A (en) | 2001-12-21 | 2001-12-21 | Medical oxygen concentration device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001389371A JP2003180838A (en) | 2001-12-21 | 2001-12-21 | Medical oxygen concentration device |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003180838A true JP2003180838A (en) | 2003-07-02 |
Family
ID=27597606
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001389371A Pending JP2003180838A (en) | 2001-12-21 | 2001-12-21 | Medical oxygen concentration device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003180838A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011110521A (en) * | 2009-11-30 | 2011-06-09 | Sumitomo Seika Chem Co Ltd | Method and device for acquiring purified gas-pressurized gas |
CN102494515A (en) * | 2011-12-05 | 2012-06-13 | 无锡威克亨盛机械制造有限公司 | Process for preparing high-pressure medical oxygen |
US10603626B2 (en) | 2016-09-01 | 2020-03-31 | Exxonmobil Upstream Research Company | Swing adsorption processes using zeolite structures |
US11433346B2 (en) | 2019-10-16 | 2022-09-06 | Exxonmobil Upstream Research Company | Dehydration processes utilizing cationic zeolite RHO |
-
2001
- 2001-12-21 JP JP2001389371A patent/JP2003180838A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011110521A (en) * | 2009-11-30 | 2011-06-09 | Sumitomo Seika Chem Co Ltd | Method and device for acquiring purified gas-pressurized gas |
CN102494515A (en) * | 2011-12-05 | 2012-06-13 | 无锡威克亨盛机械制造有限公司 | Process for preparing high-pressure medical oxygen |
US10603626B2 (en) | 2016-09-01 | 2020-03-31 | Exxonmobil Upstream Research Company | Swing adsorption processes using zeolite structures |
US11318413B2 (en) | 2016-09-01 | 2022-05-03 | Exxonmobil Upstream Research Company | Swing adsorption processes using zeolite structures |
US11433346B2 (en) | 2019-10-16 | 2022-09-06 | Exxonmobil Upstream Research Company | Dehydration processes utilizing cationic zeolite RHO |
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