JP2005066072A - Medical oxygen concentrator - Google Patents

Medical oxygen concentrator Download PDF

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JP2005066072A
JP2005066072A JP2003301020A JP2003301020A JP2005066072A JP 2005066072 A JP2005066072 A JP 2005066072A JP 2003301020 A JP2003301020 A JP 2003301020A JP 2003301020 A JP2003301020 A JP 2003301020A JP 2005066072 A JP2005066072 A JP 2005066072A
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air compressor
oxygen concentrator
oxygen
adsorption
air
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JP4426232B2 (en
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Kenji Nishimura
謙史 西村
Taizo Magari
泰三 間狩
Shigenori Hirano
茂徳 平野
Hideki Kobayashi
英樹 小林
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Teijin Ltd
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<P>PROBLEM TO BE SOLVED: To provide a pressure swing adsorption oxygen concentrator used for a home oxygen therapy, which is quiet, and has a low power consumption. <P>SOLUTION: This pressure swing type oxygen concentrator is equipped with at least one adsorption cylinder which is filled with an adsorbent selectively adsorbing nitrogen more than oxygen, an air compressor for pressure pump and/or vacuum pump of air to/from the adsorption cylinder, and a switching valve which switches adsorption/desorption channels. In the pressure swing type oxygen concentrator, a motor which drives the air compressor is a brushless motor which is equipped with an inverter and is driven by a DC power source. Also, a buffer tank of which the tank capacity (V) to a discharging amount q(L/min) per unit time which is converted into 25°C-1atm of the air compressor satisfies V≥q/600(L) is provided between the air compressor and the switching valve. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

本発明は空気中から酸素を分離濃縮する酸素濃縮器、特に医療用として在宅で行なわれる酸素吸入療法に使用する圧力変動吸着型の酸素濃縮器に関する。   The present invention relates to an oxygen concentrator for separating and concentrating oxygen from the air, and more particularly to a pressure fluctuation adsorption type oxygen concentrator used for oxygen inhalation therapy performed at home for medical use.

在宅酸素療法に使用する医療用の酸素濃縮器は、空気を原料としてその中に含まれる約21%の酸素を40%や90%前後に濃縮して使用するものである。その方法としては、酸素を選択的に透過する酸素富化膜を使用する膜型の酸素濃縮器と、ゼオライト等の窒素を選択的に吸着する吸着剤を用い、これを充填した吸着筒に原料である空気を加えて窒素を吸着分離する圧力変動吸着型の酸素濃縮器がある。前者の酸素濃縮器で濃縮される酸素濃度は約40%で後者が約90%である。現在では,後者が主流となっており、本発明は、後者に関するものである。   A medical oxygen concentrator used for home oxygen therapy uses air as a raw material and concentrates about 21% oxygen contained therein to about 40% or 90%. The method uses a membrane-type oxygen concentrator that uses an oxygen-enriched membrane that selectively permeates oxygen, and an adsorbent that selectively adsorbs nitrogen, such as zeolite, and a raw material in an adsorption cylinder filled with this. There is a pressure fluctuation adsorption type oxygen concentrator that adsorbs and separates nitrogen by adding air. The concentration of oxygen concentrated by the former oxygen concentrator is about 40% and the latter is about 90%. At present, the latter is mainstream, and the present invention relates to the latter.

かかる圧力変動吸着型酸素濃縮器は、5A型ゼオライトや13X型ゼオライト、或はSiO/Al比が2.0〜3.0であるX型ゼオライトでそのAlO四面体単位の少なくとも88%以上がLiカチオンと会合している高性能のLiゼオライト等を1筒、2筒、或は更に多数の吸着筒に充填し、コンプレッサを用いて大気を加圧供給し窒素を吸着させ、酸素を分離すると共に、流路を切換え、大気圧迄で圧力を減圧して吸着した窒素を脱着させるPSA方式、或は吸着筒を真空状態まで減圧することで脱着再生効率を上げたVPSA方式の各種装置が市場に供給されている。 Such a pressure fluctuation adsorption type oxygen concentrator is a 5A type zeolite, a 13X type zeolite, or an X type zeolite having a SiO 2 / Al 2 O 3 ratio of 2.0 to 3.0, and at least 88% of the AlO 4 tetrahedral unit is more than 88%. High-performance Li zeolite associated with Li cations is packed in one, two, or many adsorption cylinders, and the atmosphere is pressurized with a compressor to adsorb nitrogen and separate oxygen. At the same time, there are various PSA systems that change the flow path and reduce the pressure up to atmospheric pressure to desorb the adsorbed nitrogen, or VPSA systems that increase the desorption regeneration efficiency by reducing the adsorption cylinder to a vacuum state. Has been supplied to.

特開2000−176019号公報JP 2000-176019 A 特開昭63−242901号公報JP-A-63-242901 特開昭60−200804号公報JP-A-60-200804 特開昭59−274654号公報JP 59-274654 A

在宅酸素療法に用いられる酸素濃縮器に求められる基本性能は、酸素濃縮性能の他に、特に在宅医療用として求められる要件として、静寂性、省エネ性他がある。これは、次の理由によるものである。   The basic performance required for an oxygen concentrator used for home oxygen therapy includes quietness, energy saving, and the like as requirements required for home medical use in addition to the oxygen concentration performance. This is due to the following reason.

在宅酸素療法で使用する酸素濃縮器は、装置自体の費用の大部分は健康保険負担となり患者負担は少ないものの、運転費用は患者負担であり、患者は一日24時間連続運転して使用するため、電気代は大きな負担となり、消費電力の小さい装置が必須要件となっている。また、在宅酸素療法で使用する酸素濃縮器は、一日24時間使用する場合が多く、夜間は装置の動作音が家族を含め患者の睡眠を妨げない静かな装置であることが要求される。   Oxygen concentrators used in home oxygen therapy are mostly covered by health insurance and less burdened by the patient, but the operating expenses are burdened by the patient, and the patient operates continuously for 24 hours a day. The electricity bill is a heavy burden, and a device with low power consumption is an essential requirement. In addition, oxygen concentrators used in home oxygen therapy are often used 24 hours a day, and at night, it is required that the operation sound of the device be a quiet device that does not disturb the sleep of patients including family members.

次にこれらの酸素濃縮器に求められている2つの要件について従来技術では、以下のような態様となっている。
(1)低消費電力性について
酸素濃縮器における主たる電力消費部は、空気圧縮機であるので、この部分の効率化が低消費電力化を実現する為に、多大な効果がある。特に高効率を実現する為の装置構成として、従来から一般的に使用されている往復動型ピストン方式の代わりに、効率の高い回転型スクロール方式やヘリカル方式の空気圧縮機を使用し、駆動する為の電動機に対しては、交流用誘導電動機よりも効率の高い直流電動機を使用することが一般的になりつつある。特開2000−176019号公報の如く、スクロール方式の圧縮機と直流用ブラッシュレス電動機を使用する装置構成が、公知の技術である。
Next, regarding the two requirements required for these oxygen concentrators, the prior art has the following aspects.
(1) About low power consumption Since the main power consumption part in an oxygen concentrator is an air compressor, since the efficiency improvement of this part implement | achieves low power consumption, there exists a great effect. In particular, as a device configuration for realizing high efficiency, instead of the reciprocating piston type that has been generally used, a highly efficient rotary scroll type or helical type air compressor is used for driving. For this purpose, it is becoming common to use a DC motor having higher efficiency than an AC induction motor. As in Japanese Patent Application Laid-Open No. 2000-176019, a device configuration using a scroll compressor and a DC brushless motor is a known technique.

(2)静粛性について
従来、交流用誘導電動機を使用した装置構成が主流であった時は、装置における動作音の発生源は原料である空気を取り入れて圧縮する空気圧縮機の動作音と圧力変動吸着型酸素濃縮器の吸着筒の圧力切り替えと排気に伴って発生する排気音が主なものであった。
(2) Quietness Conventionally, when the equipment configuration using an AC induction motor has been the mainstream, the operating noise and pressure of the air compressor that takes in the air as raw material and compresses it is the source of the operating noise in the equipment. Exhaust noise generated by pressure switching and exhaust of the adsorption cylinder of the variable adsorption type oxygen concentrator was the main one.

排気音は高性能のサイレンサを取り付けることにより、比較的良く消音することができる。しかし、空気圧縮機の動作音は振動を伴った低周波音を多く含んでおり容易には下げにくい。現在、医療用酸素濃縮気に使用されている空気圧縮機はピストン方式、ベーン方式、スクロール方式のものがある。ベーン方式のものは使用されているカーボンが摩耗し、二次側に黒いカーボンが出てくるし、これを取り除く為のフィルタが必要になってくる。更にこのフィルタも度々交換しなければならない。加えてカーボンベーンの摩耗寿命が2000〜4000Hであり、保守が頻繁に発生する為ピストン方式のものが主に使用されている。   Exhaust noise can be silenced relatively well by installing a high-performance silencer. However, the operation sound of the air compressor contains a lot of low-frequency sound accompanied by vibrations and is not easily lowered. Currently, there are piston type, vane type and scroll type air compressors used for oxygen enrichment for medical use. In the vane type, the carbon used is worn out, black carbon comes out on the secondary side, and a filter is required to remove it. In addition, this filter must be replaced frequently. In addition, the wear life of the carbon vane is 2000 to 4000H, and maintenance frequently occurs, so that the piston type is mainly used.

ピストン方式の空気圧縮機の騒音は、通常上記の種類の酸素濃縮器に使用するクラスの空気圧縮機単体での騒音レベルは80〜60dBAの範囲にあり、これは、ピストンの動作に伴って生じる空気圧縮機の振動と電動機のトルク変動に伴う低周波動作音が原因である。振動の他への伝播を防ぐ為の手段としては特開昭63−242901号公報に示される如くスプリングや防振ゴムにより浮かせる手段をとりかつ、特開昭60−200804号公報、特開昭59−274654号公報などに示されるように二重の防音ボックスにより音を封じ込めている。しかし、完全に密閉することはできず、駆動電動機や空気圧縮に伴う発熱を冷却する必要があり、ファンを取り付けている。しかし、この冷却風の取り込み口、排出口を経由して騒音が外部に漏出するので屈曲した通路を設けてこれを防いでいる。このようにいろいろな防音手段を講じているので装置が大きく、重くなっており40〜60kgであり、保守員1人では抱えて建物の階段を上り降りすることが困難である。   The noise level of a piston type air compressor is usually in the range of 80 to 60 dBA in the class of air compressor of the class used for the above-mentioned type of oxygen concentrator, and this is caused by the operation of the piston. This is due to the low-frequency operating noise associated with vibrations in the air compressor and torque fluctuations in the motor. As means for preventing the propagation of vibrations to the other, a means for floating by a spring or an anti-vibration rubber as shown in JP-A-63-242901, and JP-A-60-200804 and JP-A-59. As shown in Japanese Patent Publication No. 274654 / etc., Sound is contained by a double soundproof box. However, it cannot be completely sealed, and it is necessary to cool the heat generated by the drive motor and air compression, and a fan is attached. However, since noise leaks to the outside through the intake and discharge ports for cooling air, a bent passage is provided to prevent this. Since various soundproofing measures are taken in this way, the apparatus is large and heavy, weighing 40-60 kg, and it is difficult for one maintenance person to carry it up and down the stairs of the building.

回転型のスクロール方式やヘリカル方式の空気圧縮機は、バルブレス構造で、バルブの開閉音がなく、騒音面で有利である為、近年、医療用酸素濃縮器への適応が増加している。   The rotary scroll type and helical type air compressors have a valveless structure, have no valve opening / closing noise, and are advantageous in terms of noise, and thus have recently been increasingly applied to medical oxygen concentrators.

しかしながら、近年、省エネ技術として直流用ブラッシュレス電動機が使用されるようになって、モータから発生する騒音が新たな課題となっている。元来、吸着筒内の圧力変動を利用し、窒素成分を吸脱着することを基本原理とするPSAおよびVPSA方式の酸素濃縮器は、本質的に、周期的な負荷変動を伴うプロセスであり、空気圧縮機を駆動する為の電動機は、該負荷変動に応じた仕事が要求される。従来型の交流用誘導電動機と直流用ブラッシュレス電動機を比較した場合、その回転数−トルク特性の差異により、必要トルクが変化した場合の回転数変動は、直流用ブラッシュレス電動機の方が格段に大きい。該回転数変動の周期は、うなり音の周期と一致し、該回転数変動の回転数変動幅は、うなり音の大きさに比例するため、該回転数変動は、大きな問題となっている。   However, in recent years, brushless electric motors for direct current have been used as energy-saving technologies, and noise generated from motors has become a new issue. Originally, the PSA and VPSA type oxygen concentrators based on the basic principle of adsorbing and desorbing nitrogen components using pressure fluctuations in the adsorption cylinder are essentially processes with periodic load fluctuations. An electric motor for driving an air compressor is required to perform work in accordance with the load fluctuation. When comparing a conventional AC induction motor and a DC brushless motor, the fluctuation in the rotational speed when the required torque changes due to the difference in the rotational speed-torque characteristics of the direct current brushless motor. large. Since the cycle of the rotational speed coincides with the period of the roaring sound, and the rotational speed fluctuation range of the rotational speed fluctuation is proportional to the size of the roaring sound, the rotational speed fluctuation is a big problem.

具体例をあげれば、吸着プロセス圧が150kPa±20kPaで、必要流量が70L/minで運転される2筒式酸素濃縮器に、ピストン方式の空気圧縮機を組み合わせた場合、交流用誘導電動機では、回転数変動は、1680±20rpmであることに対して、直流用ブラッシュレス電動機では、回転数変動は、1680±200rpmである。上記、直流用ブラッシュレス電動機の回転数変動対策としては、駆動用インバータで、フィードバック制御の制御速度を高め、回転数制御の精度を上げることも有効であるが、この場合、CPUの負荷増大に伴う消費電力の悪化や、各負荷条件に対し、個別の制御時定数の設定が必要という欠点がある。   As a specific example, when a piston type air compressor is combined with a two-cylinder oxygen concentrator operated at an adsorption process pressure of 150 kPa ± 20 kPa and a required flow rate of 70 L / min, The rotational speed fluctuation is 1680 ± 20 rpm, whereas in the direct current brushless motor, the rotational speed fluctuation is 1680 ± 200 rpm. As a countermeasure against fluctuations in the rotational speed of the brushless motor for direct current, it is effective to increase the control speed of feedback control and increase the precision of rotational speed control with a drive inverter. In this case, however, the load on the CPU is increased. There is a drawback that the power consumption is accompanied and the control time constant needs to be set individually for each load condition.

本発明は、上記のように在宅酸素療法に使用する静粛でかつ低消費電力の圧力変動吸着型の酸素濃縮器を提供するものである。そこで本発明者は、かかる課題に対して鋭意検討した結果、以下の酸素濃縮器を見出した。   The present invention provides a pressure fluctuation adsorption type oxygen concentrator that is quiet and has low power consumption used for home oxygen therapy as described above. Therefore, as a result of intensive studies on the problem, the present inventor has found the following oxygen concentrator.

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少なくとも1個の吸着筒と該吸着筒に空気を加圧供給及び/または減圧排気する為の空気圧縮機を有する圧力変動型の酸素濃縮器において、該空気圧縮機を駆動する電動機が、直流電源で駆動するブラッシュレス電動機であり、且つインバータを備え、該空気圧縮機と該吸着筒の間に圧縮空気を保持する為のバッファタンクを有し、該バッファタンクの容量V(L)が、該空気圧縮機の25℃−1atmに換算した単位時間辺りの吐出量q(L/min)に対し、V>=q/600(L)であることを特徴とする酸素濃縮器を提供するものである。   That is, the present invention has at least one adsorption cylinder filled with an adsorbent capable of selectively adsorbing nitrogen rather than oxygen, and an air compressor for pressurizing and / or evacuating air to the adsorption cylinder. In the pressure fluctuation type oxygen concentrator, the electric motor that drives the air compressor is a brushless electric motor that is driven by a DC power source, and includes an inverter, and holds compressed air between the air compressor and the adsorption cylinder. The buffer tank capacity V (L) is V> = with respect to the discharge amount q (L / min) per unit time converted to 25 ° C.-1 atm of the air compressor. The oxygen concentrator is characterized by being q / 600 (L).

直流用ブラッシュレス電動機にて駆動する空気圧縮機と切り替えバルブ間にバッファタンクを設置するとにより、静粛かつ低消費電力の圧力変動吸着型の酸素濃縮器を提供することができる。   By installing a buffer tank between the air compressor driven by the DC brushless motor and the switching valve, it is possible to provide a quiet and low power consumption pressure fluctuation adsorption type oxygen concentrator.

本発明の医療用酸素濃縮装置の概略図を図1に示す。かかる酸素濃縮装置は、酸素よりも窒素を選択的に吸着する吸着剤として5A型ゼオライトを充填した吸着筒にコンプレッサにより加圧空気を供給し、酸素濃度90%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2筒式の圧力変動吸着型酸素濃縮装置である。   A schematic diagram of the medical oxygen concentrator of the present invention is shown in FIG. Such an oxygen concentrator supplies pressurized air to an adsorption cylinder filled with 5A-type zeolite as an adsorbent that selectively adsorbs nitrogen rather than oxygen, takes out an oxygen-concentrated gas having an oxygen concentration of 90%, and a humidifier This is a two-cylinder pressure fluctuation adsorption type oxygen concentrator that supplies a respiratory disease patient, who is a user, via, for example, at a flow rate of 3 L / min.

空気圧縮機は圧縮比が1.5〜3.0の範囲にあり、かつ、排除容積が50cc/rev以下の範囲を有するヘリカルブレード型の空気圧縮機である。該空気圧縮機を駆動する電動機が5000rpm以下で運転することができる能力を有するブラッシュレスDC電動機であり、これをインバータにより制御することにより、任意に回転数を変更できるようになっている。   The air compressor is a helical blade type air compressor having a compression ratio in a range of 1.5 to 3.0 and an excluded volume in a range of 50 cc / rev or less. The electric motor that drives the air compressor is a brushless DC electric motor that has the capability of being operated at 5000 rpm or less, and the rotational speed can be arbitrarily changed by controlling the electric motor with an inverter.

空気圧縮機と切り替えバルブの間には、容量V(L)が、該空気圧縮機の単位時間辺りの25℃−1atmに換算した吐出量q(L/min)に対し、V≧q/600(L)となるサイズのバッファタンクが挿入されている。バッファタンクの容量については、鋭意検討した結果、空気圧縮機の排除容積をD(L)とし、圧縮比をrとした場合、V≧200D/r×0.1(L)で効果を発現することを見出した。しかし、空気圧縮機の設計仕様であるD(L)やrの値は、開示されていない値であることが多い為、医療用酸素濃縮器として適用可能な空気圧縮機を検討した結果、V≧q/600(L)であることを見出した。   Between the air compressor and the switching valve, the capacity V (L) is V ≧ q / 600 with respect to the discharge amount q (L / min) converted to 25 ° C.-1 atm per unit time of the air compressor. A buffer tank having a size of (L) is inserted. As a result of intensive investigations on the capacity of the buffer tank, when the displacement volume of the air compressor is D (L) and the compression ratio is r, the effect is manifested when V ≧ 200 D / r × 0.1 (L). I found out. However, since the values of D (L) and r, which are design specifications of the air compressor, are often undisclosed values, as a result of studying an air compressor applicable as a medical oxygen concentrator, V It was found that ≧ q / 600 (L).

上限は規定していないが、性能的には大きい方が圧力変動幅を小さくすることが出来るのは明らかである。しかしながら、装置仕様から求められる要件としては、バッファタンクの性能を維持しつつ可能な限り小さくすることである為、濃縮器筐体内に設置可能なレベルを上限とする。   Although the upper limit is not specified, it is clear that the larger the performance, the smaller the pressure fluctuation range. However, since the requirement required from the apparatus specification is to make it as small as possible while maintaining the performance of the buffer tank, the upper limit is the level that can be installed in the concentrator housing.

本発明においては、かかるバッファタンクを空気圧縮機と切り替えバルブ間に設置した構成を、酸素濃縮器に採用した。従来の構成の様に、直流用ブラッシュレス電動機にて駆動する空気圧縮機と切り替えバルブ間を配管で直接接続した構成では、バルブ切り替えによる空気圧縮機出側での圧力変動が大きく、その負荷変動周期に併せて電動機の回転数も変動する為、周期的なうなり音が発生する。しかしながら、本発明における構成では、空気圧縮機と切り替えバルブ間に設置されたバッファタンクが圧力変動を吸収する為のアキュムレータとして作用し、負荷変動が大幅に軽減する為、その結果、電動機の回転数変動が抑制され、うなり音は解消されることを見出した。また、負荷変動を緩和することにより、モータ自身の効率を高めることができ結果として消費電力低減効果も発生すると同時に、モータ寿命を延長し、機器信頼性の高い酸素濃縮器を提供することが可能となる。   In the present invention, a configuration in which such a buffer tank is installed between the air compressor and the switching valve is employed in the oxygen concentrator. In the configuration in which the air compressor driven by the DC brushless motor and the switching valve are directly connected by piping as in the conventional configuration, the pressure fluctuation on the outlet side of the air compressor due to valve switching is large, and the load fluctuation Since the rotation speed of the electric motor fluctuates in accordance with the cycle, a periodic beat sound is generated. However, in the configuration of the present invention, the buffer tank installed between the air compressor and the switching valve acts as an accumulator for absorbing pressure fluctuations, and the load fluctuations are greatly reduced. It was found that the fluctuation was suppressed and the beat sound was eliminated. Also, by mitigating load fluctuations, the efficiency of the motor itself can be increased, resulting in a reduction in power consumption. At the same time, it is possible to extend the motor life and provide a highly reliable oxygen concentrator. It becomes.

以下、91%の酸素濃度で、5L/分の流量を実現する酸素濃縮器の実施例及び比較例について説明する。   Hereinafter, examples and comparative examples of an oxygen concentrator realizing a flow rate of 5 L / min with an oxygen concentration of 91% will be described.

[実施例1]
直径70mm、長さ400mmの吸着筒に5A型ゼオライトを密度0.8で充填したものを2本と、流量70L/分が得られる性能を有するヘリカル型のコンプレッサと切り替え弁の間に、直径60mm、長さ400mmの円筒型バッファタンクを図1のフローシートのように接続し、動作させる。ヘリカルコンプレッサは、直流用ブラッシュレス電動機によりインバータにて一定回転数指令で運転し、実回転数をタコメータにて測定する。
[Example 1]
A diameter of 60 mm is provided between two helical cylinders filled with a density of 0.8 in an adsorption cylinder having a diameter of 70 mm and a length of 400 mm, and a helical compressor capable of obtaining a flow rate of 70 L / min and a switching valve. A cylindrical buffer tank having a length of 400 mm is connected and operated as in the flow sheet of FIG. The helical compressor is operated at a constant rotational speed command by an inverter with a brushless motor for direct current, and the actual rotational speed is measured by a tachometer.

[比較例1]
直径70mm、長さ400mmの吸着筒に5A型ゼオライトを密度0.8で充填したものを2本と、流量70L/分が得られる性能を有するヘリカル型のコンプレッサを内径8mmの配管で直接きり替え弁まで接続し、動作させる。その他の条件は、実施例1と同じ条件である。
[Comparative Example 1]
Two helical cylinders with a density of 0.8 packed in an adsorption cylinder with a diameter of 70mm and a length of 400mm, and a helical compressor with a performance of 70L / min. Connect to the valve and operate. Other conditions are the same as those in the first embodiment.

上記実施例と比較例の結果を表1に示す。回転数の変動幅が±20rpmと、比較例の10分の1に収まり、騒音の変動レベルもΔ0.9dBAと、比較例の29%のレベルに収束した。酸素濃度及び収率には影響なく、消費電力も5W低減した。このように実施例1と比較例1との性能差は、非常に大きく、直流用ブラッシュレス電動機にて駆動する空気圧縮機と切り替えバルブ間にバッファタンクを設置するとにより、周期的なうなり音の原因となる電動機の回転数変動は、大幅に改善されていることがわかる。また、消費電力も改善されていることが分かる。   Table 1 shows the results of the above examples and comparative examples. The fluctuation range of the rotational speed was ± 20 rpm, which was 1/10 of that of the comparative example, and the noise fluctuation level was also converged to Δ0.9 dBA, which was 29% of the comparative example. The power consumption was reduced by 5 W without affecting the oxygen concentration and yield. Thus, the performance difference between Example 1 and Comparative Example 1 is very large. By installing a buffer tank between the air compressor driven by the DC brushless motor and the switching valve, periodic beat noise is generated. It turns out that the rotation speed fluctuation | variation of the motor which becomes a cause is improved significantly. It can also be seen that power consumption is improved.

Figure 2005066072
Figure 2005066072

本発明の2筒式酸素濃縮器の概略構成図。The schematic block diagram of the 2 cylinder type oxygen concentrator of this invention.

Claims (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個の吸着筒と、該吸着筒に空気を加圧供給及び/または減圧排気する為の空気圧縮機と、吸脱着流路を切り替える切り替えバルブとを備えた圧力変動型の酸素濃縮器において、該空気圧縮機を駆動する電動機が、インバータを備えた直流電源で駆動するブラッシュレス電動機であり、且つ、該空気圧縮機と該切り替えバルブの間に、タンク容量(V)が該空気圧縮機の25℃−1atmに換算した単位時間辺りの吐出量q(L/min)に対し、V≧q/600(L)であるバッファタンクを有することを特徴とする酸素濃縮器。   At least one adsorption cylinder filled with an adsorbent capable of selectively adsorbing nitrogen rather than oxygen, an air compressor for pressurizing and / or evacuating air to the adsorption cylinder, and an adsorption / desorption flow path In the pressure fluctuation type oxygen concentrator provided with a switching valve for switching, the electric motor that drives the air compressor is a brushless electric motor that is driven by a DC power source that includes an inverter, and the air compressor and the air compressor Between the switching valves, a buffer whose tank capacity (V) is V ≧ q / 600 (L) with respect to the discharge amount q (L / min) per unit time converted to 25 ° C.-1 atm of the air compressor An oxygen concentrator comprising a tank.
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JP2013536705A (en) * 2010-09-06 2013-09-26 レスメド・リミテッド Method and apparatus for preventing rainout
CN113277478A (en) * 2021-06-15 2021-08-20 成都联帮医疗科技股份有限公司 Oxygen generation system with single reversing valve and double functions and oxygen generation method thereof

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JP2013536705A (en) * 2010-09-06 2013-09-26 レスメド・リミテッド Method and apparatus for preventing rainout
US10076628B2 (en) 2010-09-06 2018-09-18 Resmed Limited Methods and apparatus for preventing rainout
US11273278B2 (en) 2010-09-06 2022-03-15 ResMed Pty Ltd Methods and apparatus for preventing rainout
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