JPS5987019A - Oxygen enriching apparatus - Google Patents
Oxygen enriching apparatusInfo
- Publication number
- JPS5987019A JPS5987019A JP19629882A JP19629882A JPS5987019A JP S5987019 A JPS5987019 A JP S5987019A JP 19629882 A JP19629882 A JP 19629882A JP 19629882 A JP19629882 A JP 19629882A JP S5987019 A JPS5987019 A JP S5987019A
- Authority
- JP
- Japan
- Prior art keywords
- filter
- oxygen
- air
- section
- blower
- 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 Using Semi-Permeable Membranes (AREA)
Abstract
Description
【発明の詳細な説明】
産業上の利用分野
;に:発明は窒素より大きい速度で酸素を透過させる選
択性気体透過膜を用いることにより、大気空気から酸素
濃度の向上した空気を得る医療用酸素富化装置に関する
ものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application: The invention relates to medical oxygen, which obtains air with an improved oxygen concentration from atmospheric air by using a selective gas permeable membrane that allows oxygen to pass through at a rate greater than that of nitrogen. This relates to an enrichment device.
従来例の構成とその問題点
従来よりぜんそくや慢性気管支炎などの呼吸気系疾患治
療に酸素を投与する場合が多い。Conventional Structure and Problems Conventionally, oxygen has often been administered to treat respiratory diseases such as asthma and chronic bronchitis.
酸素の供給源として深冷分離法から製造された純酸素を
ボンベなどに詰めて供給する方法や、ゼオライトなどの
吸着剤を用いて大気中の酸素濃度を高める手段、そして
極薄膜の選択性気体透過膜により大気空気を酸素富化す
る方法などが現在考えられている。As an oxygen supply source, there are methods to supply pure oxygen produced by cryogenic separation in cylinders, methods to increase the oxygen concentration in the atmosphere using adsorbents such as zeolite, and selective gas using ultra-thin membranes. Currently, methods are being considered to enrich atmospheric air with oxygen using a permeable membrane.
その−例を第1図〜第2図に基づいて説明する。An example thereof will be explained based on FIGS. 1 and 2.
図において、1は吸気室2と排気室3を仕切板4により
仕切形成した酸素富化装置の本体である。In the figure, 1 is the main body of an oxygen enrichment device in which an intake chamber 2 and an exhaust chamber 3 are partitioned by a partition plate 4.
5は吸気室2に連通ずるように本体1に設けられた大気
の吸気口、6は吸気口5に設けられたフィルター、7は
排気室3から連通ずる排気口、8は膜モジュールであり
、9は吸気口5から膜モジエール8間を通過し、排気ロ
アに同う空気流を形成させる送風機である。Reference numeral 5 indicates an air intake port provided in the main body 1 so as to communicate with the intake chamber 2, 6 indicates a filter provided in the intake port 5, 7 indicates an exhaust port that communicates with the exhaust chamber 3, and 8 indicates a membrane module. Reference numeral 9 denotes a blower that passes between the air intake port 5 and the membrane module 8 to form a similar air flow at the exhaust lower.
膜モジュール8は第2図に示さ几るごとく、それぞれの
孔が連通ずる多孔質の膜支持体ioの表面に選択性気体
透過膜11を形成し、補強板12で強化さ九ている。膜
支持体10と補強板12の間には膜透過空気の流量を容
易にするためにネット材13が存在し、また透過空気を
補集するノズル14がセットされている。そしてノズル
14と集約管15は連結されている。16は集i−勺管
15に接続された真空ポンプであり送風機9により空冷
される位置に構成される。17は冷却管であり真空ポン
プ16により昇温した気体はここで冷却される。As shown in FIG. 2, the membrane module 8 has a selective gas permeable membrane 11 formed on the surface of a porous membrane support io with which the respective pores communicate, and is reinforced with a reinforcing plate 12. A net material 13 is present between the membrane support 10 and the reinforcing plate 12 in order to facilitate the flow rate of the membrane-permeating air, and a nozzle 14 is set to collect the permeating air. The nozzle 14 and the collecting pipe 15 are connected. Reference numeral 16 denotes a vacuum pump connected to the collector pipe 15, and is located at a position where it is air-cooled by the blower 9. 17 is a cooling pipe in which the gas heated by the vacuum pump 16 is cooled.
冷却によって生じた凝縮水は水分離器18によって分離
され、水分吸収材19((導かれる。20はレリーフ弁
、21は流量計、22は活性炭、23はバクテリアフィ
ルター、24は酸素富化空気吐出口である。The condensed water produced by cooling is separated by a water separator 18 and guided to a moisture absorbing material 19 (20 is a relief valve, 21 is a flow meter, 22 is activated carbon, 23 is a bacterial filter, 24 is an oxygen enriched air outlet) It is the exit.
上記構成において、送風機9並びに真空ポンプ16を運
転すると送風機9により本体1の吸込口6から大気空気
がフィルター6を介して吸気され、吸気された大気は膜
モジユール8間に流入する。In the above configuration, when the blower 9 and the vacuum pump 16 are operated, the blower 9 sucks atmospheric air from the suction port 6 of the main body 1 through the filter 6, and the sucked atmosphere flows between the membrane modules 8.
このとき真空ポンプ16によシ膜モジュール8内が減圧
となるため、膜モジユール9間を通過する大気空気の一
部は選択性気体透過膜11を透過し、酸素富化空気にな
る。At this time, the pressure inside the membrane module 8 is reduced by the vacuum pump 16, so that part of the atmospheric air passing between the membrane modules 9 passes through the selective gas permeable membrane 11 and becomes oxygen-enriched air.
酸素富化空気は膜モジユール8内の多孔質膜支持体゛1
o、ネット材13.ノズル14を通り集約%i 15へ
導かれる。Oxygen-enriched air is supplied to the porous membrane support 1 within the membrane module 8.
o, net material 13. It is directed through nozzle 14 to aggregate %i 15.
真空ポンプ16内を通ることにより昇温した酸素富化空
気:/i冷却管17のところで゛冷却され、水分か凝縮
する。The oxygen-enriched air heated by passing through the vacuum pump 16 is cooled in the cooling pipe 17, and moisture is condensed.
凝縮水を分離した酸素富化空気は流量調整のだめのレリ
ーフ弁20、そして流量計21、脱臭するだめの活性炭
22、およびバクテリアフィルター23で浄化された後
、e素富化空気吐出口24に送られる。The oxygen-enriched air from which the condensed water has been separated is purified by a relief valve 20 for flow rate adjustment, a flow meter 21, activated carbon 22 for deodorizing the reservoir, and a bacteria filter 23, and then sent to an e-enriched air outlet 24. It will be done.
一方選択性気体透過膜11を透過しなかった大気空気は
送風機9により排気室3へ送られる。そして真空ポンプ
16を冷却しながら排気ロアより排出される。On the other hand, atmospheric air that has not passed through the selective gas permeable membrane 11 is sent to the exhaust chamber 3 by the blower 9. The vacuum pump 16 is then discharged from the exhaust lower while being cooled.
この際、水分吸収材19に吸収された、凝縮水は装置か
ら排出される空気より蒸発する。At this time, the condensed water absorbed by the moisture absorbing material 19 evaporates from the air discharged from the device.
上記構成における装置において、患者に対し人体に有害
な亜硫酸ガスや窒素酸化物なども選択性透過膜11は透
過してしまうことや、長時間稼動していた場合、フィル
ター6のみでは膜表面に微粒子が吸着し、透過した酸素
富化空気量か減夕して来る欠点を有していた。In the device having the above configuration, the selective permeable membrane 11 may pass through the selectively permeable membrane 11 even sulfur dioxide gas and nitrogen oxides that are harmful to the human body, and if the filter 6 alone is used for a long time, fine particles may be deposited on the membrane surface. It has the disadvantage that the amount of oxygen-enriched air that permeates is reduced.
そしてまた選択性気体透過膜11を透過しなかった空気
は患者の居る部屋に排出されるため、微粒子や臭気を除
去しなければならない欠点を有していた。Furthermore, since the air that has not passed through the selective gas permeable membrane 11 is discharged into the room where the patient is, there is a drawback that fine particles and odors must be removed.
発明の目的
本発明は上記従来の欠点を解消するとともに、酸素富化
空気供給機能と空気清浄の機能を有し、また空気清浄の
機能単独でも使用できる装置にすることを目的とする。OBJECTS OF THE INVENTION It is an object of the present invention to eliminate the above-mentioned conventional drawbacks, and to provide an apparatus that has an oxygen-enriched air supply function and an air cleaning function, and can also be used solely for the air cleaning function.
発明の構成
本発明は酸素富化装置の吸気口に上ヒ較的大きなほこり
から煙草の煙のような微細な粒子を除去する防塵部、そ
して人体に有害な亜硫酸ガスなどを除去する有害ガス吸
着部、そして排出口に至る前に臭気などを除去する脱臭
部を構成する。Structure of the Invention The present invention has a dust-proofing part that removes fine particles such as cigarette smoke from relatively large dust at the intake port of an oxygen enrichment device, and a harmful gas adsorption part that removes sulfur dioxide gas that is harmful to the human body. and a deodorizing section that removes odors before reaching the discharge port.
上記構成・、・こより酸素富化空気供給機能旨を有しな
から排出空気をも浄化し、そして酸素富化空気供給機能
を作動させなくても室内の空気を浄イヒさせる機能を有
する装置にしたものである。From the above structure, the device has the function of supplying oxygen-enriched air, purifies the exhaust air, and purifies the indoor air without activating the function of supplying oxygen-enriched air. This is what I did.
実施例の説明 本発明の一実例を第3図に基づいて説明する。Description of examples An example of the present invention will be explained based on FIG.
なお往来ケと同一部材については同一番号を付けて説明
する。It should be noted that the same members as those used in the forward and backward directions will be described using the same numbers.
吸気口5に大きなほこりなどを除去するブ1ノフィルタ
ー25.そして微粒子を除去するメインフィルター26
の防塵部を設ける。メインフィルり=26の次に亜硫酸
ガスや窒素酸化物などの有害ガスを除去するガス吸着フ
ィルター27の有害ガス吸着部を、そして排気ロアに至
る前に活IE炭フィルター28の脱臭部を設ける。1 filter to remove large dust etc. from the intake port 5 25. And the main filter 26 that removes particulates
Provide a dustproof section. Next to the main filter 26, a harmful gas adsorption part of a gas adsorption filter 27 for removing harmful gases such as sulfur dioxide gas and nitrogen oxides is provided, and before reaching the exhaust lower, a deodorizing part of an activated carbon filter 28 is provided.
上記構成において、送風機9と真空ポンプ16とは連動
して始動するよう構成され装置内に供給される大気空気
はプリフィルター25、メインフィルター26.ガス吸
着フィルター27を通過することにより、選択性気体透
過膜11の手前で微粒子や有害ガスが除去される。In the above configuration, the blower 9 and the vacuum pump 16 are configured to start in conjunction with each other, and the atmospheric air supplied into the device is filtered through the prefilter 25, the main filter 26. By passing through the gas adsorption filter 27, particulates and harmful gases are removed before the selective gas permeable membrane 11.
上記各フィルターを通過した空気の一部は真空ポンプ1
6により選択性気体透過膜11を透過し酸素富化空気と
して吐出口24より吐出される。A portion of the air that has passed through each of the above filters is pumped to the vacuum pump 1.
6, the air passes through the selective gas permeable membrane 11 and is discharged from the discharge port 24 as oxygen-enriched air.
他方透過しなかった空気は送風機9により膜モジユール
8間を通り、脱臭部の活性炭フィルター28で浄化され
排出される。On the other hand, the air that has not permeated is passed between the membrane modules 8 by the blower 9, purified by the activated carbon filter 28 of the deodorizing section, and discharged.
次に酸素富化空気を必要とし々いて部屋の空気のみを浄
化したい場合、真空ポンプ1eのみを独立して作動停止
可能としこれを停止させて送風機9のみ作動させる。Next, when oxygen-enriched air is required and only the air in the room is desired to be purified, only the vacuum pump 1e can be independently stopped, and only the blower 9 is operated.
送風機9により装置内に供給された全量の大気空気は防
塵部、有害ガス吸着部および脱臭部を通過処理されて排
出ロアより排出される。The entire amount of atmospheric air supplied into the apparatus by the blower 9 passes through a dustproof section, a harmful gas adsorption section, and a deodorization section, and is discharged from the discharge lower.
尚、上記実施例では微粒子を除去するためにメインフィ
ルター26を使用したが、このフィルタ一式以外に電極
板方式あるいは静電フィルタ一方式でもよく、要は微粒
子が除去できnばよい。In the above embodiment, the main filter 26 was used to remove particulates, but in addition to this set of filters, an electrode plate type or one type of electrostatic filter may be used, as long as it can remove particulates.
発明の効果
このように本発明によれば酸素富化装置の吸気口に微細
な粒子を除去する防塵部と、人体に有害な亜硫酸ガスな
どを除去する有害ガス吸着部を設け、排出口に至る間に
臭気などを除去する防臭部を設けているため、有害な亜
硫酸ガスや窒素酸化物なども除去された清浄な酸素を患
者に供給することか出来ると共に酸素富化装置の透過膜
を透過せず1″で患者の居る部屋に排出される空気も浄
化出来るなどの効果が発揮されるものである。Effects of the Invention As described above, according to the present invention, a dust prevention section for removing fine particles and a harmful gas adsorption section for removing sulfur dioxide gas, etc., which are harmful to the human body, are provided at the intake port of the oxygen enrichment device, and the oxygen enrichment device is provided with a dust prevention section that removes fine particles and a harmful gas adsorption section that removes sulfur dioxide gas that is harmful to the human body. Since there is a deodorizing section in between that removes odors, it is possible to supply clean oxygen to the patient from which harmful sulfur dioxide gas and nitrogen oxides have been removed, and it is also able to pass through the permeable membrane of the oxygen enrichment device. It is effective in that it can also purify the air discharged into the room where the patient is.
第1図は従来例の酸素富化装置の断面図、第2図は膜モ
ジュールの断面図、第3図は本発明の一実施例における
酸素富化装置の断面図である。
1・・・・・・酸素富化装置本体、5・・・・・・吸気
口、7・・・・・・排気口、8・・・・・・膜モジュー
ル、9・・・・・・送風機、11・・・・・選択性気体
透過膜、16・・・・・Jlポンフ;24・・・・・・
酸素富化空気吐出口、2815・・・・・・防塵部のブ
リフィルター、26・・・・・・防塵部のメインフィル
ター、27・・・・・・有害ガス吸着部のガス吸着フィ
ルター、28・・・・・脱臭部の活性炭フィルター。FIG. 1 is a sectional view of a conventional oxygen enrichment device, FIG. 2 is a sectional view of a membrane module, and FIG. 3 is a sectional view of an oxygen enrichment device in an embodiment of the present invention. 1... Oxygen enrichment device main body, 5... Intake port, 7... Exhaust port, 8... Membrane module, 9... Blower, 11... Selective gas permeable membrane, 16... Jl pump; 24...
Oxygen-enriched air discharge port, 2815... Buri filter of dustproof section, 26... Main filter of dustproof section, 27... Gas adsorption filter of harmful gas adsorption section, 28 ...Activated carbon filter in the deodorizing section.
Claims (3)
向上させる装置内へ供給される大気空気が防塵部・有害
ガス吸着部および脱臭部を通過処理される流路と、防塵
部と有害ガス吸着部を通過した後、一部空気が選択性気
体透過膜を透通ずることにより酸素富化空気となる流路
を有し、前記防塵部・有害ガス吸着部・脱臭部を通過す
る流路には送風機を、そして酸素富化空気流路にはポン
プを設けた酸素富化装置。(1) A flow path through which the atmospheric air supplied to the device that improves the oxygen concentration of atmospheric air using a selective gas permeable membrane passes through a dustproof section, a harmful gas adsorption section, and a deodorizing section, and a dustproof section. After passing through the harmful gas adsorption section, a portion of the air passes through a selective gas permeable membrane to become oxygen-enriched air, and the flow passes through the dust prevention section, harmful gas adsorption section, and deodorization section. An oxygen enrichment device with a blower in the channel and a pump in the oxygen enriched air flow channel.
て行えるよう構成した特許請求の範囲第1項記載の酸素
富化装置。(2) The oxygen enrichment device according to claim 1, which is configured so that the operation of the blower and the pump can be controlled independently.
特許請求の範囲第1項記載の酸素富化装置。(3) The oxygen enrichment device according to claim 1, wherein the operation of the blower is automatically linked with the operation of the pump.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19629882A JPS5987019A (en) | 1982-11-08 | 1982-11-08 | Oxygen enriching apparatus |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP19629882A JPS5987019A (en) | 1982-11-08 | 1982-11-08 | Oxygen enriching apparatus |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5987019A true JPS5987019A (en) | 1984-05-19 |
Family
ID=16355476
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP19629882A Pending JPS5987019A (en) | 1982-11-08 | 1982-11-08 | Oxygen enriching apparatus |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5987019A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61280870A (en) * | 1985-06-07 | 1986-12-11 | 井上 理文 | Oxygen enriching device of oxygen inhaler |
JPH01147821U (en) * | 1988-03-31 | 1989-10-12 | ||
KR20040021793A (en) * | 2002-09-04 | 2004-03-11 | 웅진코웨이주식회사 | Oxygen generator |
KR100469657B1 (en) * | 2002-05-29 | 2005-02-02 | 삼성전자주식회사 | Air conditioner having oxygen generator |
KR100476094B1 (en) * | 2002-08-28 | 2005-03-10 | 웅진코웨이주식회사 | Apparatus for Generating Oxygen using clean Filter and Plate type membrane |
KR100492723B1 (en) * | 2002-05-04 | 2005-06-10 | 디지털오토모빌(주) | Air cleaning method using oxygen concentrator |
-
1982
- 1982-11-08 JP JP19629882A patent/JPS5987019A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61280870A (en) * | 1985-06-07 | 1986-12-11 | 井上 理文 | Oxygen enriching device of oxygen inhaler |
JPH0519424B2 (en) * | 1985-06-07 | 1993-03-16 | Masafumi Inoe | |
JPH01147821U (en) * | 1988-03-31 | 1989-10-12 | ||
KR100492723B1 (en) * | 2002-05-04 | 2005-06-10 | 디지털오토모빌(주) | Air cleaning method using oxygen concentrator |
KR100469657B1 (en) * | 2002-05-29 | 2005-02-02 | 삼성전자주식회사 | Air conditioner having oxygen generator |
KR100476094B1 (en) * | 2002-08-28 | 2005-03-10 | 웅진코웨이주식회사 | Apparatus for Generating Oxygen using clean Filter and Plate type membrane |
KR20040021793A (en) * | 2002-09-04 | 2004-03-11 | 웅진코웨이주식회사 | Oxygen generator |
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