JP2001252360A - Oxygen concentrating device - Google Patents

Oxygen concentrating device

Info

Publication number
JP2001252360A
JP2001252360A JP2000068583A JP2000068583A JP2001252360A JP 2001252360 A JP2001252360 A JP 2001252360A JP 2000068583 A JP2000068583 A JP 2000068583A JP 2000068583 A JP2000068583 A JP 2000068583A JP 2001252360 A JP2001252360 A JP 2001252360A
Authority
JP
Japan
Prior art keywords
oxygen
adsorbent
adsorption
beds
concentrating device
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
JP2000068583A
Other languages
Japanese (ja)
Inventor
Tomio Sasaki
利美雄 佐々木
Hideyuki Sakurai
秀行 櫻井
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.)
Sumitomo Bakelite Co Ltd
Original Assignee
Sumitomo Bakelite Co 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 Sumitomo Bakelite Co Ltd filed Critical Sumitomo Bakelite Co Ltd
Priority to JP2000068583A priority Critical patent/JP2001252360A/en
Publication of JP2001252360A publication Critical patent/JP2001252360A/en
Pending legal-status Critical Current

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  • Oxygen, Ozone, And Oxides In General (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide an oxygen concentrating device which is capable of drastically shortening the waiting time before the start of the supply of high- concentration oxygen in starting operation. SOLUTION: The medical oxygen concentrating device which is a pressure swing adsorption type for concentrating the oxygen in air and has >=2 adsorption beds includes a stop valve for passing the oxygen for regenerating purging to an oxygen replacement side of a whole volume buffer tank without passing the same to another adsorption bed side in starting the operation in a flow passage installed with a flow rate regulator.

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、大気より酸素濃縮
気体を分離して使用するための酸素濃縮装置に関するも
のであり、更に詳しくは呼吸器系疾患の患者が療養目的
で使用する圧力変動方式の医療用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 an oxygen concentrator for separating and using an oxygen-enriched gas from the atmosphere, and more particularly, to a pressure fluctuation system used by a patient with a respiratory disease for medical treatment. The present invention relates to a medical oxygen concentrator.

【0002】[0002]

【従来の技術】酸素濃縮装置は、空気中の酸素を分離濃
縮する装置であり、その分離濃縮方法としては主に酸素
透過膜を用いて酸素富化気体を得る分離膜方式と、窒素
と酸素に関して選択的吸着性能を有する吸着剤を用いた
吸着方式の2種類があるが、得られる酸素濃度の点から
吸着方式酸素濃縮装置が主流になりつつある。
2. Description of the Related Art An oxygen concentrator is a device for separating and concentrating oxygen in air. The separation and concentrating method is mainly a separation membrane system for obtaining an oxygen-enriched gas by using an oxygen permeable membrane, a nitrogen and oxygen system. There are two types of adsorption methods using an adsorbent having selective adsorption performance, but the adsorption type oxygen concentrator is becoming mainstream in view of the obtained oxygen concentration.

【0003】吸着方式の酸素濃縮装置は、コンプレッサ
ーと、コンプレッサーから発生する熱を冷却するための
ファンと、吸着剤の酸素と窒素の吸着性能の差を利用し
て酸素濃縮気体を得るための少なくとも1個以上の吸着
床と、吸着剤を再生するための再生手段と、2個以上の
吸着床より交互に発生する酸素の脈動を除去し安定供給
するためのバッファータンクからなる。
[0003] The oxygen concentrator of the adsorption system is composed of a compressor, a fan for cooling the heat generated from the compressor, and at least an oxygen-concentrated gas for obtaining an oxygen-enriched gas by utilizing the difference between the adsorbents' oxygen and nitrogen adsorption performance. It comprises one or more adsorbent beds, a regenerating means for regenerating the adsorbent, and a buffer tank for removing and stably supplying oxygen pulsations alternately generated from the two or more adsorbent beds.

【0004】吸着床が2個以上の酸素濃縮装置において
は、一方の吸着床で窒素を吸着し酸素の濃縮を行うとと
もに、作り出した酸素の一部を他の吸着床へ流通回路を
経由して流通させ、更に該吸着床の吸着工程時の方向と
は逆の方向へ流通させること(以下パージとよぶ)で吸
着剤に付着した窒素を脱着させ吸着剤の再生を同時に並
行して行っている。
In an oxygen concentrator having two or more adsorbent beds, one of the adsorbent beds adsorbs nitrogen to concentrate oxygen, and a part of the produced oxygen is transferred to another adsorbent bed via a circulation circuit. Nitrogen adhering to the adsorbent is desorbed by allowing the adsorbent to flow in the direction opposite to the direction of the adsorption step during the adsorption step (hereinafter referred to as purge), and the adsorbent is regenerated at the same time. .

【0005】2個以上の吸着床をもつ酸素濃縮装置での
吸着剤の再生において、再生のための流通回路に流通量
制御手段のみの設置の場合、吐出側への酸素量と吸着剤
の再生側への酸素量をバランス良く調整することはでき
るが、常時吸着側より再生側へ酸素を流通させることに
なり、運転スタート時は再生パージ分バッファータンク
の酸素置換が遅れることになり、その分高濃度酸素を供
給開始できるまでの時間が遅れることとなる。
In the regeneration of an adsorbent in an oxygen concentrator having two or more adsorbent beds, if only a flow control means is provided in a flow circuit for regeneration, the amount of oxygen on the discharge side and the regeneration of the adsorbent Although it is possible to adjust the amount of oxygen to the recovery side in a well-balanced manner, oxygen is always circulated from the adsorption side to the regeneration side, and at the start of operation, the oxygen purge in the buffer tank is delayed by the amount of regeneration purge. The time required to start supplying high-concentration oxygen is delayed.

【0006】[0006]

【発明が解決しようとする課題】本発明は、2個以上の
吸着床をもつ酸素濃縮装置において、運転スタート時の
高濃度酸素供給開始までの立ち上がり時間の遅れを、可
能な限り最小限とした酸素濃縮装置を提供することを目
的とする。
SUMMARY OF THE INVENTION According to the present invention, in an oxygen concentrator having two or more adsorbent beds, a delay in a rise time until the start of high-concentration oxygen supply at the start of operation is minimized. An object of the present invention is to provide an oxygen concentrator.

【0007】[0007]

【課題を解決するための手段】本発明者は、かかる問題
を解決することを目的として鋭意研究した結果、圧力変
動吸着型で2個以上の吸着床をもつ酸素濃縮装置におい
て、運転スタート時より次の吸着床に吸着工程が切り換
えられるまでの間、該開閉弁により該吸着床間のパージ
用流通路を閉じておくことで、可能な限り速やかにバッ
ファータンクの酸素置換を行うことができ、高濃縮酸素
の供給を最短時間で立ち上げられることを見い出し、本
発明に到達した。
Means for Solving the Problems The present inventor has conducted intensive studies with the aim of solving such a problem. As a result, the oxygen concentrator having a pressure fluctuation adsorption type having two or more adsorption beds has been used since the start of operation. Until the adsorption step is switched to the next adsorption bed, by closing the purge flow passage between the adsorption beds by the on-off valve, oxygen exchange of the buffer tank can be performed as quickly as possible, The inventors have found that the supply of highly concentrated oxygen can be started in the shortest time, and arrived at the present invention.

【0008】即ち本発明は、酸素よりも窒素をより優先
的に吸着する吸着剤を充填した2個以上の吸着床と、該
吸着床に空気を供給するための空気供給手段を有した圧
力変動吸着式の酸素濃縮装置において、該吸着床間で一
方の吸着床より他方の吸着床へ酸素濃縮気体を流通させ
る経路を1回路有し、且つその1回路に流通量を制御す
る手段と流通を開閉制御できる開閉手段を合わせ持つこ
とを特徴とする酸素濃縮装置である。
[0008] That is, the present invention provides a pressure fluctuation apparatus comprising two or more adsorption beds filled with an adsorbent for adsorbing nitrogen more preferentially than oxygen, and air supply means for supplying air to the adsorption beds. In an adsorption-type oxygen concentrator, there is one circuit for flowing the oxygen-enriched gas from one adsorbent bed to the other adsorbent bed between the adsorbent beds. An oxygen concentrator characterized by having an opening / closing means capable of opening / closing control.

【0009】[0009]

【発明の実施の形態】以下本発明について詳細に説明す
る。本発明の酸素濃縮装置は、選択的吸着性能をもつ吸
着剤を用いて空気中より酸素濃縮気体を得るものである
が、その原料となる空気の供給手段としてコンプレッサ
ーを用いるものである。また、コンプレッサーは、その
運転時に熱を発生するため、その熱を冷却するためのフ
ァンが備えられている。コンプレッサーで加圧供給され
た原料空気は、吸着床で窒素成分を選択的に吸着せしめ
た後、得られた酸素の一部を他吸着床にパージし脱着を
行い吸着剤の再生を並行して行いながら、濃度の高い酸
素気体を連続して得ることのできる装置である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below in detail. The oxygen concentrating device of the present invention obtains oxygen-enriched gas from the air using an adsorbent having selective adsorption performance, and uses a compressor as a means for supplying air as a raw material. Further, the compressor generates heat during its operation, and thus is provided with a fan for cooling the heat. The raw material air pressurized and supplied by the compressor, after selectively adsorbing nitrogen components in the adsorbent bed, purging a part of the obtained oxygen to other adsorbent beds and desorbing, and regenerating the adsorbent in parallel This is an apparatus that can continuously obtain oxygen gas with high concentration while performing.

【0010】かかる本発明の装置において、吸着床は、
2個以上のいずれでもよいが、医療用で在宅治療も考慮
した小型の酸素濃縮装置の場合には2個が望ましい。ま
た、コンプレッサーは、一般的に様々な形式のコンプレ
ッサーが市販されているが、原料空気を所定の圧力と流
量で供給できるものであれば、いずれの形式も使用する
ことができる。ただし、オイル潤滑タイプのコンプレッ
サーは、圧縮空気中にオイルが含まれることがあり、後
処理が必要となるため、オイルフリータイプのコンプレ
ッサーであることが望ましい。ファンとしては、コンプ
レッサーの動力軸に取り付けられた一体型のファンや別
に装着されたものなど種々あるが、冷却能力が十分であ
れば問題はなく、装置としては騒音の少ない低消費電力
のタイプが望ましい。
[0010] In the apparatus of the present invention, the adsorption bed comprises:
Any number of two or more may be used, but two are desirable in the case of a small-sized oxygen concentrator for medical use and also considering home treatment. In general, various types of compressors are commercially available, but any type can be used as long as it can supply raw material air at a predetermined pressure and flow rate. However, an oil-lubricated compressor is preferably an oil-free compressor because compressed air sometimes contains oil and requires post-treatment. There are various types of fans, such as an integrated fan attached to the power shaft of the compressor and a fan attached separately, but there is no problem if the cooling capacity is sufficient, and a low power consumption type with low noise is used as the device. desirable.

【0011】本発明の酸素濃縮装置の特徴は、吸着剤再
生パージ用流量調整器のほか、運転スタート時バッファ
ータンクの酸素置換並びに高濃度酸素供給の開始時間を
最短とするための流通路開閉弁を具備していることであ
る。パージ用流通路は吸着剤の再生に必要な流量を圧力
変化を生じることなく通過させることのできる太さ以上
であれば良く、流量調整器は必要な流量を設定できる構
造であれば良い。設定値ズレを防止するためにも所定の
流量に固定する方式であるオリフィスによる方が望まし
い。流通路開閉弁は簡単な構造の二方向弁で良く、弁口
径は吸着剤再生用パージの流量に支障の起こらない太さ
であれば良い。電気信号により簡単に開閉を制御できる
電磁弁が望ましい。
The oxygen concentrator of the present invention is characterized in that, in addition to the flow regulator for purifying the adsorbent regeneration, a flow passage opening / closing valve for minimizing the start time of oxygen replacement of the buffer tank and supply of high-concentration oxygen at the start of operation. Is provided. The purging flow passage may have a thickness that allows the flow rate required for regeneration of the adsorbent to pass without causing a pressure change, and the flow regulator may have any structure that can set the required flow rate. In order to prevent a set value deviation, it is more preferable to use an orifice which is a method of fixing the flow rate at a predetermined value. The flow passage opening / closing valve may be a two-way valve having a simple structure, and the valve diameter may be any thickness that does not interfere with the flow rate of the adsorbent regeneration purge. It is desirable to use an electromagnetic valve whose opening and closing can be easily controlled by an electric signal.

【0012】[0012]

【実施例】以下、本発明の実施例について図を参照して
詳しく説明する。図1は酸素濃縮装置の系統図の一例で
ある。この図において、1は吸気フィルター、2はコン
プレッサー、3は冷却ファン、4と5は三方弁、6は消
音器、7は圧力計、8と9は吸着床、10は再生パージ
用流通路、11は流量調整器、12は二方弁、13と1
4は逆止弁、15がバッファータンクである。従来の酸
素濃縮器と比較して、再生パージ用流通路10と流量調
整器11に加え、運転スタート時の高濃度酸素供給の開
始までの時間を最短とするための開閉弁12を具備する
ことが本発明での大きな特徴である。
DESCRIPTION OF THE PREFERRED EMBODIMENTS Embodiments of the present invention will be described below in detail with reference to the drawings. FIG. 1 is an example of a system diagram of the oxygen concentrator. In this figure, 1 is an intake filter, 2 is a compressor, 3 is a cooling fan, 4 and 5 are three-way valves, 6 is a silencer, 7 is a pressure gauge, 8 and 9 are adsorption beds, 10 is a flow path for regeneration purge, 11 is a flow regulator, 12 is a two-way valve, 13 and 1
4 is a check valve and 15 is a buffer tank. Compared with a conventional oxygen concentrator, an on-off valve 12 for minimizing the time until the start of high-concentration oxygen supply at the start of operation is provided in addition to the regeneration purge flow passage 10 and the flow regulator 11. Is a major feature of the present invention.

【0013】2個以上の吸着床をもつ酸素濃縮装置での
吸着剤の再生において、再生パージ量としては吸着床の
吸脱工程切り換え時間内に十分再生できる量が設定され
ており、通常装置の酸素供給能力の半分から同等レベル
の量がパージされている。従って運転スタート時は、こ
の再生パージ用酸素が全量バッファータンクの置換側へ
供給されることになり、高濃度酸素の供給開始までの時
間が大幅に短縮されることになる。
In the regeneration of an adsorbent in an oxygen concentrator having two or more adsorption beds, the regeneration purge amount is set to an amount that can be sufficiently regenerated within the time for switching the adsorption / desorption step of the adsorption bed. An equivalent level of volume is purged from half of the oxygen supply capacity. Therefore, when the operation is started, the regeneration purge oxygen is supplied to the replacement side of the entire buffer tank, and the time until the start of the supply of the high-concentration oxygen is greatly reduced.

【0014】[0014]

【発明の効果】本発明により、運転スタート時の高濃度
酸素供給開始までの待ち時間を、大幅に短縮することが
できる。
According to the present invention, the waiting time until the start of the supply of high-concentration oxygen at the start of operation can be greatly reduced.

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

【図1】酸素濃縮装置の系統図の一例である。FIG. 1 is an example of a system diagram of an oxygen concentrator.

【符号の説明】[Explanation of symbols]

1 吸気フィルター 2 コンプレッサー 3 冷却ファン 4 三方弁 5 三方弁 6 消音器 7 圧力計 8 吸着床 9 吸着床 10 再生パージ用流通路 11 流量調整器 12 二方弁 13 逆止弁 14 逆止弁 15 バッファータンク DESCRIPTION OF SYMBOLS 1 Intake filter 2 Compressor 3 Cooling fan 4 Three-way valve 5 Three-way valve 6 Silencer 7 Pressure gauge 8 Adsorption bed 9 Adsorption bed 10 Regeneration purge flow path 11 Flow regulator 12 Two-way valve 13 Check valve 14 Check valve 15 Buffer tank

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 酸素よりも窒素をより優先的に吸着する
吸着剤を充填した2個以上の吸着床と、該吸着床に空気
を供給するための空気供給手段を有した圧力変動吸着式
の酸素濃縮装置において、該吸着床間で一方の吸着床よ
り他方の吸着床へ酸素濃縮気体を流通させる経路を1回
路有し、且つその1回路に流通量を制御する手段と流通
を開閉制御できる開閉手段を合わせ持つことを特徴とす
る酸素濃縮装置。
1. A pressure fluctuation adsorption type having two or more adsorption beds filled with an adsorbent for adsorbing nitrogen more preferentially than oxygen and an air supply means for supplying air to the adsorption beds. In the oxygen concentrator, there is one circuit for flowing the oxygen-enriched gas from one adsorbent bed to the other adsorbent bed between the adsorbent beds, and the means for controlling the flow rate and the open / close control of the flow can be controlled in the one adsorbent bed. An oxygen concentrator characterized by having an opening and closing means.
JP2000068583A 2000-03-13 2000-03-13 Oxygen concentrating device Pending JP2001252360A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2000068583A JP2001252360A (en) 2000-03-13 2000-03-13 Oxygen concentrating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2000068583A JP2001252360A (en) 2000-03-13 2000-03-13 Oxygen concentrating device

Publications (1)

Publication Number Publication Date
JP2001252360A true JP2001252360A (en) 2001-09-18

Family

ID=18587617

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2000068583A Pending JP2001252360A (en) 2000-03-13 2000-03-13 Oxygen concentrating device

Country Status (1)

Country Link
JP (1) JP2001252360A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009006256A (en) * 2007-06-27 2009-01-15 Ihi Corp Oxygen enricher
JP2009006255A (en) * 2007-06-27 2009-01-15 Ihi Corp Method of uniforming pressure of oxygen concentrator

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009006256A (en) * 2007-06-27 2009-01-15 Ihi Corp Oxygen enricher
JP2009006255A (en) * 2007-06-27 2009-01-15 Ihi Corp Method of uniforming pressure of oxygen concentrator

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