JP2002345964A - Medical pressure variable oxygen condensing device - Google Patents
Medical pressure variable oxygen condensing deviceInfo
- Publication number
- JP2002345964A JP2002345964A JP2001158400A JP2001158400A JP2002345964A JP 2002345964 A JP2002345964 A JP 2002345964A JP 2001158400 A JP2001158400 A JP 2001158400A JP 2001158400 A JP2001158400 A JP 2001158400A JP 2002345964 A JP2002345964 A JP 2002345964A
- Authority
- JP
- Japan
- Prior art keywords
- adsorption
- heat pipe
- pipe radiator
- oxygen concentrator
- oxygen
- 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)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、大気中から酸素濃
縮空気を分離して使用するための酸素濃縮装置に関す
る。さらに詳細には、圧力変動吸着型酸素濃縮装置に関
し、プロセスの均熱化により酸素分離効率の向上を可能
とした、改善された酸素濃縮装置に関するものである。The present invention relates to an oxygen concentrator for separating and using oxygen-enriched air from the atmosphere. More specifically, the present invention relates to a pressure fluctuation adsorption type oxygen concentrator, and more particularly, to an improved oxygen concentrator capable of improving oxygen separation efficiency by soaking a process.
【0002】[0002]
【従来の技術】近年、喘息、肺気腫、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が、そ
の治療法として最も効果的なものの1つに酸素吸入療法
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
うになってきている。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. Oxygen concentrators for directly separating oxygen-enriched gas from inside have been developed, and are becoming increasingly popular as therapeutic devices for oxygen inhalation therapy because of their convenience in use and ease of maintenance.
【0003】かかる酸素濃縮装置として、窒素を選択的
に吸着し得る吸着剤を1筒あるいは複数の吸着床に充填
し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酸素濃縮
装置が多用されている。かかる装置は、通常、窒素を選
択的に吸着し得る吸着剤を充填した1筒或いは複数の吸
着床にコンプレッサーから圧縮空気を供給して加圧状態
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を一定サイクルで繰り返し行
い、さらに必要に応じて、両工程の間に、既に生成した
乾燥酸素濃縮空気を一部逆流させるなどして再生効率の
向上と昇圧を目的とする均圧工程を加えて、順次一定サ
イクルで行うことにより酸素濃縮気体を得る装置であ
る。[0003] As such an oxygen concentrator, an adsorbent oxygen concentrator in which an adsorbent capable of selectively adsorbing nitrogen is filled in one tube or a plurality of adsorbent beds is known. Among them, pressure fluctuation using a compressor as an air supply means is known. Adsorption type oxygen concentrators are frequently used. Such an apparatus generally obtains oxygen-enriched gas by supplying compressed air from a compressor to one or more adsorption beds filled with an adsorbent capable of selectively adsorbing nitrogen and adsorbing nitrogen in a pressurized state. The adsorption step and the desorption step of reducing the internal pressure of the adsorption bed to desorb nitrogen to regenerate the adsorbent are repeated in a fixed cycle, and if necessary, between the two steps, dry oxygen-enriched air already generated This is an apparatus for obtaining an oxygen-enriched gas by adding a pressure equalization step for improving the regeneration efficiency and increasing the pressure by partially backflowing the gas, and sequentially performing the same in a constant cycle.
【0004】該酸素濃縮装置の吸着床に使用されるゼオ
ライト系吸着剤は、酸素よりも窒素を選択的に吸着し得
る吸着剤であり、例えばモレキュラーシーブゼオライト
5A、13X、或はリチウム系ゼオライトなどが使用され
る。The zeolite adsorbent used in the adsorption bed of the oxygen concentrator is an adsorbent capable of selectively adsorbing nitrogen over oxygen, such as molecular sieve zeolite 5A, 13X, or lithium zeolite. Is used.
【0005】[0005]
【発明が解決しようとする課題】かかる吸着剤は、一定
の使用条件下では、吸着剤の温度により吸着剤に対する
窒素の吸着量が変化し、それに伴い酸素の回収率が大き
く左右されるという問題点を有している。該酸素濃縮装
置の温度による性能低下への影響を解消する手段とし
て、コンプレッサー等の空気供給手段の冷却排熱を利用
し、排気を直接吸着床表面に吹き付ける方法や、ヒート
パイプ等の熱移動手段を用いて回収し、吸着床表面の加
熱に用いる方法があるが、配置上の制約が大きく、また
小型軽量化の妨げともなる。The problem with such an adsorbent is that, under certain conditions of use, the amount of nitrogen adsorbed on the adsorbent changes depending on the temperature of the adsorbent, and the recovery rate of oxygen is greatly affected accordingly. Have a point. As a means for eliminating the influence of the temperature of the oxygen concentrator on performance degradation, a method of utilizing the cooling and exhaust heat of an air supply means such as a compressor to blow exhaust gas directly to the surface of an adsorption bed, or a heat transfer means such as a heat pipe There is a method of recovering the adsorbent bed and using it for heating the surface of the adsorbent bed. However, this method has a large restriction on the arrangement and hinders reduction in size and weight.
【0006】吸着現象は発熱反応であり、一方脱着現象
は吸熱反応であることが知られている。吸着、脱着を繰
り返す圧力変動吸着型酸素濃縮装置では、吸着剤は時間
的、空間的に温度分布が存在し、一般に圧力変動吸着型
酸素濃縮装置では、圧縮空気が吸着床に流入する部分で
急激な温度変化が起こる。吸着時には流入空気による急
激な窒素吸着に伴う発熱反応のために急激な温度上昇が
起こる。この温度上昇は、酸素濃縮効率の低下の原因と
なる。It is known that the adsorption phenomenon is an exothermic reaction, while the desorption phenomenon is an endothermic reaction. In a pressure fluctuation adsorption type oxygen concentrator that repeats adsorption and desorption, the adsorbent has a temporal and spatial temperature distribution, and in general, in a pressure fluctuation adsorption type oxygen concentrator, abruptly occurs at the part where compressed air flows into the adsorption bed. Temperature changes occur. At the time of adsorption, a rapid temperature rise occurs due to an exothermic reaction accompanying rapid nitrogen adsorption by the inflowing air. This increase in temperature causes a decrease in oxygen concentration efficiency.
【0007】本発明は、これらのプロセスでの温度不均
一を解消し、酸素回収率などの性能の向上を目的とする
ものであり、装着位置の自由度が高く熱交換性の優れた
熱交換器を装着することでプロセス均熱化し、酸素分離
効率の高い医療用酸素濃縮装置を提供するものである。An object of the present invention is to eliminate the temperature non-uniformity in these processes and improve the performance such as the oxygen recovery rate. The present invention provides a medical oxygen concentrator having a high level of oxygen separation efficiency by equilibrating a process by attaching a vessel.
【0008】[0008]
【課題を解決するための手段】かかる課題に対して本発
明者は鋭意検討した結果、以下の酸素濃縮装置を見出し
た。すなわち本発明は、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吸着筒と、該吸着筒へ空気を供
給する空気供給手段と、生成した酸素濃縮空気を使用者
に供給するための酸素供給手段を備えた圧力変動型酸素
濃縮装置において、該吸着筒にヒートパイプ放熱器を備
え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。Means for Solving the Problems The inventors of the present invention have made intensive studies on such problems and found the following oxygen concentrator. That is, the present invention provides an adsorption column filled with an adsorbent capable of selectively adsorbing nitrogen over oxygen, an air supply means for supplying air to the adsorption column, and a device for supplying the generated oxygen-enriched air to a user. A pressure fluctuation type oxygen concentrator provided with a heat pipe radiator in the adsorption column.
【0009】また本発明は、特にかかるヒートパイプ放
熱器が蛇行細管ヒートパイプ放熱器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 in which the heat pipe radiator is a meandering thin tube heat pipe radiator.
【0010】また本発明は、かかる蛇行細管ヒートパイ
プ放熱器を吸着筒内部に備えること、該吸着筒の筒体自
体が蛇行細管ヒートパイプ放熱器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。[0010] The present invention also provides a pressure fluctuation adsorption type oxygen concentrator characterized in that the meandering thin tube heat pipe radiator is provided inside the adsorption tube, and the tube itself of the suction tube is a meandering thin tube heat pipe radiator. An apparatus is provided.
【0011】さらに本発明は、複数の該吸着筒を備え、
吸着工程の吸着筒と脱着工程の吸着筒間に蛇行細管ヒー
トパイプ放熱器を備え、接続す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。Further, the present invention comprises a plurality of the adsorption cylinders,
It is an object of the present invention to provide a pressure fluctuation adsorption type oxygen concentrator characterized in that a meandering thin tube heat pipe radiator is provided and connected between an adsorption column in an adsorption step and an adsorption column in a desorption step.
【0012】[0012]
【発明の実施の形態】本発明の医療用圧力変動吸着型酸
素濃縮装置は、図4に示すように、酸素よりも窒素を選
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
した吸着筒にコンプレッサーにより加圧空気を供給し、
酸素濃度90%以上の酸素濃縮ガスを取り出し、加湿器
を経由して使用者である呼吸器疾患患者に、例えば3L/
minの流量で供給する1つ或いは複数の吸着筒を有する
圧力変動吸着型酸素濃縮装置である。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As shown in FIG. 4, a medical pressure fluctuation adsorption type oxygen concentrator according to the present invention has an adsorption column filled with a zeolite adsorbent as an adsorbent for selectively adsorbing nitrogen over oxygen. Pressurized air by a compressor
An oxygen-enriched gas having an oxygen concentration of 90% or more is taken out, and passed through a humidifier to a user, a respiratory disease patient, for example, 3 L /
This is a pressure fluctuation adsorption type oxygen concentrator having one or a plurality of adsorption cylinders supplied at a flow rate of min.
【0013】吸着筒は、酸素濃縮装置の筐体内に1つ或
いは複数設置され、内部に吸着剤を充填しており、一般
的には切替弁を通じて吸気、排気のためのコンプレッサ
ー及び製品空気貯蔵のための製品タンクに接続される。
また、コンプレッサーからの吸気、排気により吸着筒内
の圧力が変動し、吸着、脱着を繰り返す。[0013] One or more adsorption cylinders are installed in the housing of the oxygen concentrator and are filled with an adsorbent. In general, a compressor for intake and exhaust and a compressor for storing product air are provided through a switching valve. Connected to the product tank.
Further, the pressure in the adsorption cylinder fluctuates due to intake and exhaust from the compressor, and adsorption and desorption are repeated.
【0014】蛇行細管ヒートパイプは、図1に示すよう
に、熱伝導性の良好なアルミニウム鋼や銅鋼板等ででき
たコンテナ本体1の内部に受熱部と放熱部との間を往復
蛇行する内径約3mm以下の密閉蛇行細管を形成する構造
2を有し、その蛇行細管中に水などの冷媒作動液を充填
したものを基本要素とするものである。熱吸収により作
動液が相変化し、蒸気は受熱部の高圧側から放熱側の低
圧側へと移動することで潜熱輸送するものであり、蒸気
泡の移動と同時に液相部も受熱部から放熱部へと移動し
て顕熱をも輸送するものである。この為、蛇行細管ヒー
トパイプは、従来型のヒートパイプとことなり、放熱部
を受熱部よりも下方に設置することが可能である。ま
た、任意の形状に折り曲げたり、フィンを取り付けたり
して使用することも可能である。As shown in FIG. 1, the meandering thin tube heat pipe has an inner diameter reciprocating between a heat receiving portion and a heat radiating portion inside a container body 1 made of aluminum steel or copper steel plate having good heat conductivity. It has a structure 2 for forming a closed meandering thin tube of about 3 mm or less, and the meandering thin tube is filled with a refrigerant working liquid such as water as a basic element. The working fluid undergoes a phase change due to heat absorption, and the vapor moves from the high-pressure side of the heat-receiving part to the low-pressure side of the heat-dissipating part to transport latent heat. And transports sensible heat as well. For this reason, the meandering thin tube heat pipe is different from the conventional heat pipe, and the heat radiating portion can be installed below the heat receiving portion. Further, it can be used by bending it into an arbitrary shape or attaching a fin.
【0015】吸着筒及び蛇行細管ヒートパイプ放熱器の
構成について、更に詳細に示す。図2は本発明の医療用
圧力変動吸着型酸素濃縮装置に使用する吸着筒の実施態
様例を示すものである。吸着筒3には吸着剤4が充填さ
れ、吸着筒3の上下には、配管6aおよび6bが接続さ
れており、配管6aにより吸気のためのコンプレッサー
または排気口に接続され、配管6bにより酸素濃縮気体
を製品タンクに貯留とともに、吸着床の再加圧や脱着の
ためのリンス効果のため貯留した酸素濃縮気体を逆流さ
せる機構となっていることが多い。The structures of the adsorption cylinder and the meandering thin tube heat pipe radiator will be described in more detail. FIG. 2 shows an embodiment of an adsorption cylinder used in the medical pressure fluctuation adsorption type oxygen concentrator according to the present invention. The adsorption cylinder 3 is filled with an adsorbent 4, and pipes 6a and 6b are connected above and below the adsorption cylinder 3, and are connected to a compressor or an exhaust port for intake by the pipe 6a, and oxygen is concentrated by a pipe 6b. In many cases, the gas is stored in the product tank, and the stored oxygen-enriched gas is back-flowed due to a rinsing effect for re-pressurizing and desorbing the adsorption bed.
【0016】5は蛇行細管ヒートパイプ放熱器であり、
吸着剤4に直接接触させる構造とすることにより、吸着
熱、脱着熱により温度分布が生じる吸着剤4を均熱化す
ることが可能となる。尚、かかる蛇行細管ヒートパイプ
放熱器として、ティーエスヒートロニクス社製ヒートレ
ーンTMを使用した。5 is a meandering thin tube heat pipe radiator,
By adopting a structure in which the adsorbent 4 is brought into direct contact with the adsorbent 4, it is possible to equalize the temperature of the adsorbent 4, which has a temperature distribution due to heat of adsorption and heat of desorption. In addition, as such a meandering thin tube heat pipe radiator, Heat Lane ™ manufactured by TS Heatronics Co., Ltd. was used.
【0017】本発明者は、リチウム系ゼオライトを充填
した内径60mm、高さ320mmの1本の吸着筒を有
する圧力変動吸着型酸素濃縮装置において、その内部に
該蛇行細管ヒートパイプ放熱器を鉛直方向に装填した吸
着筒を使用したもの及び蛇行細管ヒートパイプ放熱器な
しの吸着筒を使用した場合の、性能の比較(実施例1/
比較例1)を実施した。90%以上の酸素濃縮ガス発生
する運転条件下での吸着筒出側(サージタンク側)の温
度変化を計測し、これらの結果を表1に示す。The inventor of the present invention has disclosed a pressure fluctuation adsorption type oxygen concentrator having a single adsorber having an inner diameter of 60 mm and a height of 320 mm filled with a lithium zeolite, and having the meandering thin-tube heat pipe radiator installed therein in a vertical direction. Of the performance between the case using the adsorption tube loaded in the tube and the case using the adsorption tube without the meandering thin tube heat pipe radiator (Example 1 /
Comparative Example 1) was performed. Temperature changes on the outlet side (surge tank side) of the adsorption cylinder under operating conditions in which oxygen-enriched gas of 90% or more was generated were measured.
【0018】本装置には、伝熱効率を考慮して蛇行細管
ヒートパイプ放熱器にフィンを有するものを用いること
もできる。また、図2に示す吸着筒内部に蛇行細管ヒー
トパイプ放熱器を備えるものの他、別の態様例として、
該吸着筒の筒体自体を蛇行細管ヒートパイプ放熱器を使
用して作製する(図示せず)ことも効果的であり、温度
分布を生じた吸着剤の均熱化を行うことが可能である。In the present device, a meandering thin tube heat pipe radiator having fins may be used in consideration of heat transfer efficiency. Further, in addition to the meandering thin tube heat pipe radiator provided inside the adsorption cylinder shown in FIG.
It is also effective to fabricate the adsorption tube itself using a meandering thin tube heat pipe radiator (not shown), and it is possible to equalize the temperature of the adsorbent having a temperature distribution. .
【0019】本発明の医療用圧力変動吸着型酸素濃縮装
置の吸着筒の構成の別の実施態様例を図3に示す。かか
る態様例は、複数の吸着筒を有する圧力変動吸着型酸素
濃縮装置であり、例えば一方が吸着工程の時に他方が脱
着工程となるようにシーケンス制御された2つの吸着剤
4が充填された吸着筒3を蛇行細管ヒートパイプ放熱器
5により接続する。吸着工程で加圧および気体の吸着に
より温度が上昇した吸着剤と、脱着工程で減圧および気
体の脱着により温度が低下した吸着剤の温度差を、蛇行
細管ヒートパイプ放熱器により均熱し、酸素分離効率を
向上させることができる。FIG. 3 shows another embodiment of the configuration of the adsorption column of the medical pressure fluctuation adsorption type oxygen concentrator of the present invention. An example of such an embodiment is a pressure fluctuation adsorption type oxygen concentrator having a plurality of adsorption cylinders, for example, an adsorption apparatus in which two adsorbents 4 are sequence-controlled so that one is an adsorption step and the other is a desorption step. The tube 3 is connected by a meandering thin tube heat pipe radiator 5. The temperature difference between the adsorbent whose temperature has risen due to pressurization and gas adsorption in the adsorption process and the adsorbent whose temperature has dropped due to decompression and gas desorption in the desorption process is equalized by a meandering thin tube heat pipe radiator to separate oxygen. Efficiency can be improved.
【0020】本発明者は、リチウム系ゼオライトを使用
し、内径60mm、高さ320mmの2本の吸着筒を有
する2筒式の圧力変動吸着型酸素濃縮装置において、該
蛇行細管ヒートパイプ放熱器による吸着筒同士の接続の
有無による性能の比較(実施例2/比較例2)を実施例
1と同様に実施した。これらの結果を表1に示す。The inventor of the present invention has proposed a two-tube pressure fluctuation adsorption-type oxygen concentrator using lithium zeolite and having two adsorption cylinders having an inner diameter of 60 mm and a height of 320 mm. A comparison of performance (Example 2 / Comparative Example 2) depending on the presence or absence of connection between the adsorption cylinders was performed in the same manner as in Example 1. Table 1 shows the results.
【0021】[0021]
【表1】 [Table 1]
【0022】表1に示す結果から明らかなように、蛇行
細管ヒートパイプ放熱器を応用することにより、プロセ
スにおける最高温度および温度差は減少していることが
分かる。上記、実施様態例は医療用圧力変動吸着型酸素
濃縮装置を例に述べたが、かかる発明は医療用圧力変動
吸着型酸素濃縮装置だけでなく、装置内のプロセスにお
いて、発熱、吸熱現象が発生する医療機器に適用できる
ものである。As is clear from the results shown in Table 1, the maximum temperature and the temperature difference in the process are reduced by applying the meandering thin-tube heat pipe radiator. In the above embodiment, the medical pressure fluctuation adsorption type oxygen concentrator has been described as an example, but the present invention is not limited to the medical pressure fluctuation adsorption type oxygen concentrator, and heat generation and endothermic phenomenon occur in the process in the device. It can be applied to medical equipment that performs
【0023】[0023]
【発明の効果】装着位置の自由度が高く熱交換性の優れ
た蛇行細管ヒートパイプ放熱器を応用し、プロセスを均
熱化することにより、酸素分離効率を向上させた酸素濃
縮装置を提供することが可能となる。その結果、装置の
小型化、低電力化を実現された医療用圧力変動型酸素濃
縮装置が提供可能となる。According to the present invention, there is provided an oxygen concentrator having an improved oxygen separation efficiency by applying a meandering thin-tube heat pipe radiator having a high degree of freedom in a mounting position and an excellent heat exchange property and equalizing the process. It becomes possible. As a result, it is possible to provide a medical pressure fluctuation type oxygen concentrator which has realized a reduction in size and power consumption of the device.
【図1】蛇行細管ヒートパイプ放熱器の概略構成図であ
る。FIG. 1 is a schematic configuration diagram of a meandering thin tube heat pipe radiator.
【図2】本発明の医療用圧力変動吸着型酸素濃縮装置の
吸着筒の概略構成図である。FIG. 2 is a schematic configuration diagram of an adsorption column of the medical pressure fluctuation adsorption type oxygen concentrator according to the present invention.
【図3】本発明の医療用圧力変動吸着型酸素濃縮装置の
吸着筒の別の態様例の概略構成図である。FIG. 3 is a schematic configuration diagram of another embodiment of the adsorption cylinder of the medical pressure fluctuation adsorption type oxygen concentrator according to the present invention.
【図4】本発明の圧力変動吸着型酸素濃縮装置の概略構
成図である。FIG. 4 is a schematic configuration diagram of a pressure fluctuation adsorption type oxygen concentrator according to the present invention.
1 蛇行細管ヒートパイプ放熱器本体 2 蛇行細管構造 3 吸着筒 4 吸着剤 5 蛇行細管ヒートパイプ放熱器 6a 吸気または排気用配管 6b 酸素濃縮空気用配管 DESCRIPTION OF SYMBOLS 1 Meandering thin tube heat pipe radiator main body 2 Meandering thin tube structure 3 Adsorption tube 4 Adsorbent 5 Meandering thin tube heat pipe radiator 6a Intake or exhaust piping 6b Oxygen-enriched air piping
フロントページの続き (72)発明者 西村 謙史 大阪府茨木市耳原3丁目4番1号 帝人株 式会社大阪研究センター内 (72)発明者 間狩 泰三 大阪府茨木市耳原3丁目4番1号 帝人株 式会社大阪研究センター内 (72)発明者 早坂 浩人 東京都狛江市岩戸北3丁目11番4号 ティ ーエス ヒートロニクス 株式会社内 Fターム(参考) 4D012 CA05 CB16 CD07 CK02 CK10 4G042 BA15 BB02 BC04 Continued on the front page (72) Inventor Kenshi Nishimura 3-4-1 Amihara, Ibaraki-shi, Osaka Teijin Limited Inside Osaka Research Center (72) Inventor Taizo Makari 3-4-1 Amihara, Ibaraki-shi, Osaka Teijin Inside Osaka Research Center Co., Ltd. (72) Inventor Hiroto Hayasaka 3-11-4 Iwatokita, Komae-shi, Tokyo TS Heatronics Co., Ltd. F-term (reference) 4D012 CA05 CB16 CD07 CK02 CK10 4G042 BA15 BB02 BC04
Claims (5)
着剤を充填した吸着筒と、該吸着筒へ空気を供給する空
気供給手段と、生成した酸素濃縮空気を使用者に供給す
るための酸素供給手段を備えた圧力変動型酸素濃縮装置
において、該吸着筒にヒートパイプ放熱器を備えること
を特徴とする圧力変動吸着型酸素濃縮装置。1. An adsorption column filled with an adsorbent capable of selectively adsorbing nitrogen rather than oxygen, an air supply means for supplying air to the adsorption column, and a device for supplying the generated oxygen-enriched air to a user. A pressure-variation-type oxygen concentrator comprising the oxygen supply means of claim 1, wherein said adsorption column is provided with a heat pipe radiator.
パイプ放熱器であることを特徴とする請求項1記載の圧
力変動吸着型酸素濃縮装置。2. The pressure fluctuation adsorption type oxygen concentrator according to claim 1, wherein said heat pipe radiator is a meandering thin tube heat pipe radiator.
内部に備えることを特徴とする請求項2記載の圧力変動
吸着型酸素濃縮装置。3. The pressure fluctuation adsorption type oxygen concentrator according to claim 2, wherein said meandering thin tube heat pipe radiator is provided inside the adsorption cylinder.
であることを特徴とする請求項2記載の圧力変動吸着型
酸素濃縮装置。4. The pressure fluctuation adsorption type oxygen concentrator according to claim 2, wherein said adsorption cylinder is a meandering thin tube heat pipe radiator.
筒と脱着工程の吸着筒間に蛇行細管ヒートパイプ放熱器
を備え、接続することを特徴とする請求項2記載の圧力
変動吸着型酸素濃縮装置。5. The pressure fluctuation adsorption according to claim 2, further comprising a plurality of said adsorption cylinders, wherein a meandering thin tube heat pipe radiator is provided and connected between the adsorption cylinder in the adsorption step and the adsorption cylinder in the desorption step. Type oxygen concentrator.
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JP2001158400A JP2002345964A (en) | 2001-05-28 | 2001-05-28 | Medical pressure variable oxygen condensing device |
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JP2001158400A JP2002345964A (en) | 2001-05-28 | 2001-05-28 | Medical pressure variable oxygen condensing device |
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Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2006075456A1 (en) * | 2005-01-11 | 2006-07-20 | Go Hirabayashi | Heat-conducting member, reaction vessel and method for reacting carbon dioxide absorbing agent |
JP2011177638A (en) * | 2010-02-27 | 2011-09-15 | Jfe Steel Corp | Gas separation method and apparatus using pressure swing adsorption process |
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