JP2002253676A - Adsorbing type oxygen concentrating device - Google Patents
Adsorbing type oxygen concentrating deviceInfo
- Publication number
- JP2002253676A JP2002253676A JP2001061483A JP2001061483A JP2002253676A JP 2002253676 A JP2002253676 A JP 2002253676A JP 2001061483 A JP2001061483 A JP 2001061483A JP 2001061483 A JP2001061483 A JP 2001061483A JP 2002253676 A JP2002253676 A JP 2002253676A
- Authority
- JP
- Japan
- Prior art keywords
- adsorption
- compressor
- adsorbing
- type oxygen
- 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
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 64
- 239000001301 oxygen Substances 0.000 title claims abstract description 64
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 64
- 238000001179 sorption measurement Methods 0.000 claims abstract description 30
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 18
- 238000000034 method Methods 0.000 claims abstract description 9
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 9
- 238000003795 desorption Methods 0.000 claims abstract description 7
- 239000007789 gas Substances 0.000 claims abstract description 6
- 239000003463 adsorbent Substances 0.000 claims description 14
- 230000008929 regeneration Effects 0.000 claims description 5
- 238000011069 regeneration method Methods 0.000 claims description 5
- 238000011282 treatment Methods 0.000 abstract description 2
- 239000003795 chemical substances by application Substances 0.000 abstract 1
- 238000010586 diagram Methods 0.000 description 4
- 230000000087 stabilizing effect Effects 0.000 description 4
- 238000001514 detection method Methods 0.000 description 3
- 238000002664 inhalation therapy Methods 0.000 description 3
- 230000003340 mental effect Effects 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 206010006458 Bronchitis chronic Diseases 0.000 description 1
- 206010014561 Emphysema Diseases 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
- 230000005856 abnormality Effects 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 208000006673 asthma Diseases 0.000 description 1
- 206010006451 bronchitis Diseases 0.000 description 1
- 208000007451 chronic bronchitis Diseases 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000008094 contradictory effect Effects 0.000 description 1
- 230000006837 decompression Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000003203 everyday effect Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 208000023504 respiratory system disease Diseases 0.000 description 1
- 238000002336 sorption--desorption measurement Methods 0.000 description 1
- 230000001225 therapeutic effect Effects 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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、酸素又は窒素を選
択的に吸着する吸着剤を用い、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酸素濃縮装
置に関する。更に詳細には、吸着床に加圧空気を供給す
るコンプレッサー手段の起動時にかかる負荷を軽減させ
るように制御することにより、起動性を向上させた圧力
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 an oxygen concentrating apparatus which uses an adsorbent for selectively adsorbing oxygen or nitrogen and condenses oxygen from air by a pressure fluctuation adsorption method and supplies the oxygen to a user. More specifically, the present invention relates to a pressure-variation adsorption-type oxygen concentrator with improved start-up performance by controlling a load applied when starting up a compressor means for supplying pressurized air to an adsorption bed.
【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 tends to increase. One of the most effective treatments is oxygen inhalation therapy. Oxygen concentrators for directly separating oxygen-enriched gas from the 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個或いは、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の酸素濃
縮装置が、在宅酸素吸入療法の装置として用いられてい
る。[0003] As such an oxygen concentrator, an adsorbent oxygen concentrator in which one or more adsorbents capable of selectively adsorbing nitrogen are filled in an adsorbent bed is known. Among them, a pressure using a compressor as an air supply means is known. A variable adsorption type oxygen concentrator is used as a home oxygen inhalation therapy device.
【0004】圧力変動吸着型酸素濃縮装置においては、
一般に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窒素を脱着させ
吸着剤を再生する、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、吸着窒素を脱着さ
せ吸着剤を再生する脱着工程を繰り返し実施することに
より酸素濃縮空気を生成している。In a pressure fluctuation adsorption type oxygen concentrator,
In general, air is supplied to the adsorption bed by an air compression means, and the inside of the bed is pressurized to adsorb nitrogen in the air to take out oxygen that has not been adsorbed. The adsorbent is released to the atmosphere and decompressed to desorb adsorbed nitrogen to regenerate the adsorbent. Oxygen-enriched air is generated by repeatedly performing the desorption process for regeneration.
【0005】[0005]
【発明が解決しようとする課題】かかる酸素濃縮装置
は、在宅で使用されることから安全性や安定性はもちろ
んのこと、一般家庭で毎日使用されることから、確実に
起動することが望まれている。かかる酸素濃縮装置に
は、通常、使用温度などが規定されているが、冬場に必
ずしも使用下限温度が守られるとは限らず、極低温下で
起動されることがある。このような場合、コンプレッサ
ーの機械的抵抗が増加しており、装置の起動不良にいた
る事が極稀に発生する。この起動不良を回避するため、
種々の起動性能改善技術の開発が行われている。しか
し、未だ起動不良は散見される。Since such an oxygen concentrator is used not only at home but also for safety and stability because it is used at home, and it is used every day in ordinary households, it is desired to start it reliably. ing. In such an oxygen concentrator, a use temperature and the like are usually specified, but the minimum use temperature is not always kept in winter, and the device may be started at an extremely low temperature. In such a case, the mechanical resistance of the compressor has increased, and the start-up of the device rarely occurs. To avoid this startup failure,
Various startup performance improvement techniques have been developed. However, start-up failures are still seen.
【0006】起動性能を向上する方策としては、搭載す
るコンプレッサー能力の最適化の他、起動時の短時間に
通常コンプレッサーにかける電流値より高い電流を通じ
ることにより、短期的にコンプレッサーの回転トルクを
高めるなど様々な公知の手段がとられている。しかし、
前述の手段は短時間とはいえ、モーターコイルに大電流
を流す事から、モーター寿命に影響を及ぼす可能性があ
るなど、何れの方法も極低温時の起動性向上が認められ
るものの、完全な改善が講じられたとは言い難い。As a measure for improving the start-up performance, in addition to optimizing the capacity of the mounted compressor, in addition to passing the current higher than the current applied to the normal compressor in a short time at the time of start-up, the rotational torque of the compressor is reduced in a short term. Various known measures such as enhancement are taken. But,
Although the above-mentioned means has a short time, a large current flows through the motor coil, which may affect the life of the motor. It is hard to say that improvements have been made.
【0007】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
装置の起動性を向上し、患者の精神的負担を低減するも
のである。SUMMARY OF THE INVENTION The present invention has been made to solve the above-mentioned problems, and it is an object of the present invention to improve the startability of an adsorption-type oxygen concentrator, which is a medical device used at home for a long period of time, and to reduce the mental burden on a patient.
【0008】[0008]
【課題を解決する為の手段】本発明者はかかる課題に対
して鋭意検討した結果、酸素濃縮装置の起動時における
コンプレッサー2次側圧力の急上昇を制御することによ
り、起動性能を向上させ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 intensive studies on the above problem, the present inventor has found that the start-up performance can be improved by controlling a sudden increase in the compressor secondary pressure when the oxygen concentrator is started. They found what they could do.
【0009】すなわち本発明は、酸素又は窒素を選択的
に吸着す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コンプレッサー手段、該
吸着床の吸着、脱着再生工程を切り替える流路切替手
段、および該吸着床から得られた酸素濃縮気体を使用者
に供給する酸素供給手段を備えた吸着型酸素濃縮装置に
おいて、該コンプレッサー手段の2次側圧力を制御する
制御手段を備え、該制御手段が吸着型酸素濃縮装置の起
動時の2次側圧力上昇を抑制する手段であることを特徴
とする吸着型酸素濃縮装置を提供するものである。That is, the present invention provides at least one adsorbent bed filled with an adsorbent for selectively adsorbing oxygen or nitrogen,
Compressor means for supplying pressurized air to the adsorption bed, flow path switching means for switching the adsorption and desorption regeneration steps of the adsorption bed, and oxygen supply means for supplying a user with oxygen-enriched gas obtained from the adsorption bed. The adsorption-type oxygen concentrator provided with control means for controlling the secondary pressure of the compressor means, wherein the control means is means for suppressing an increase in the secondary-side pressure when the adsorption-type oxygen concentrator is activated. The present invention provides an adsorption-type oxygen concentrator characterized by the following.
【0010】また本発明は、かかる制御手段が、該コン
プレッサー手段の起動時の回転数を制限すると共に、所
定時間後に定格回転数まで上昇させる制御手段であるこ
とを特徴とする吸着型酸素濃縮装置を提供するものであ
る。[0010] The present invention is also an adsorption-type oxygen concentrator, wherein the control means is a control means for limiting the number of revolutions at the time of starting the compressor means and increasing the number of revolutions to a rated number of revolutions after a predetermined time. Is provided.
【0011】また本発明は、かかる制御手段が、起動時
の時間当たりの該流路切替手段の切り替え回数を定常運
転時よりも高めに設定すると共に、所定時間後に切り替
え回数を定常値に戻す制御を行う手段であることを特徴
とする吸着型酸素濃縮装置を提供するものである。Further, according to the present invention, the control means sets the number of times of switching of the flow path switching means per time at the time of startup to be higher than that in the normal operation, and returns the number of times of switching to a steady value after a predetermined time. The present invention is to provide an adsorption-type oxygen concentrator characterized in that it is a means for carrying out.
【0012】[0012]
【発明の実施の形態】本発明の吸着型酸素濃縮装置は、
酸素又は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本の吸着床、該吸着床に加圧空気を供給する
コンプレッサー手段、該吸着床の吸着、脱着再生工程を
切り替える流路切替手段、および該吸着床から得られた
酸素濃縮気体を使用者に供給する酸素供給手段を備えた
吸着型酸素濃縮装置において、該酸素濃縮装置起動時の
該コンプレッサー手段の2次側圧力の上昇を抑制する制
御手段を備えた事を特徴とする吸着型酸素濃縮装置であ
り、かかる制御手段により装置の起動性を向上し、患者
の精神的負担低減を実現する装置である。BEST MODE FOR CARRYING OUT THE INVENTION The adsorption type oxygen concentrator of the present invention
At least one adsorption bed filled with an adsorbent capable of selectively adsorbing oxygen or nitrogen, a compressor means for supplying pressurized air to the adsorption bed, and a flow path switching means for switching the adsorption and desorption regeneration steps of the adsorption bed And an adsorption-type oxygen concentrator provided with an oxygen supply means for supplying a user with an oxygen-enriched gas obtained from the adsorption bed, wherein an increase in the secondary pressure of the compressor means when the oxygen concentrator is started is suppressed. This is an adsorption-type oxygen concentrator characterized by having a control means for performing the above-mentioned control, and the control means improves the startability of the apparatus and reduces the mental burden on the patient.
【0013】かかる装置には、装置の起動時に該コンプ
レッサー手段の2次側圧力が急激に上昇しないように制
御手段を備えているが、その態様例としては、供給空気
量の制御によるコンプレッサー手段の2次圧側の制御、
言い換えれば該コンプレッサー手段の回転数を抑制する
制御手段を備えることにより達成される。該コンプレッ
サーの回転数は、搭載されているモーターの回転数制御
に他ならず、電気的に制御される。この電気的制御は搭
載されているモーターの種類により異なり、交流電源用
モーターであれば、インバーター等による通電する電源
周波数制御、直流電源用モーターであればDCインバータ
ー等による電圧制御により達成される。更に直流電源用
モーターの中でもステッピングモーターと言われるモー
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り、本発明に適用する事
が可能である。[0013] Such a device is provided with control means for preventing the secondary pressure of the compressor means from suddenly increasing when the apparatus is started. As an embodiment, the control means controls the amount of air supplied to the compressor means. Control of the secondary pressure side,
In other words, this is achieved by providing control means for suppressing the number of revolutions of the compressor means. The number of revolutions of the compressor is electrically controlled, as is the control of the number of revolutions of the mounted motor. This electrical control differs depending on the type of motor mounted, and is achieved by controlling the power supply frequency by an inverter or the like for an AC power supply motor, or by controlling the voltage by a DC inverter or the like for a DC power supply motor. Further, among the DC power supply motors, a motor called a stepping motor can control the number of rotations by the frequency of ON / OFF of energization, and can be applied to the present invention.
【0014】制御方法は、装置の起動時に該コンプレッ
サーが回転するため必要な最低限度の電源条件を供給
し、コンプレッサーの回転を確保する。その後、予め定
められた条件に従い回転数を制御する。[0014] The control method supplies the minimum power condition required for the compressor to rotate when the apparatus is started up, and ensures the rotation of the compressor. After that, the rotation speed is controlled according to a predetermined condition.
【0015】たとえば図1に、酸素よりを窒素を選択的
に吸着する吸着剤である5A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におい
て、交流モーターを搭載したコンプレッサーを搭載した
例を示す。制御手段により、図2に示すようにコンプレ
ッサーの回転数を制御手段により、定格回転数より低く
抑えることにより、回転軸の軸トルクを高く維持し、か
つ2次側圧力が上昇し難くなっている事で、極低温条件
下においてもコンプレッサーの起動が容易になる。予め
定められた条件を満たした後、コンプレッサーは別に定
められた定常運転条件へと制御され、酸素の濃縮が開始
される。For example, FIG. 1 shows a sample filled with 5A zeolite, which is an adsorbent for selectively adsorbing nitrogen over oxygen.
An example in which a compressor equipped with an AC motor is mounted in a pressure fluctuation adsorption type oxygen concentrator equipped with this adsorption column is shown. As shown in FIG. 2, the control means keeps the rotation speed of the compressor lower than the rated rotation speed by the control means, so that the shaft torque of the rotating shaft is kept high and the secondary side pressure is hardly increased. This makes it easy to start the compressor even under extremely low temperature conditions. After satisfying the predetermined condition, the compressor is controlled to a separately determined steady-state operating condition, and oxygen concentration is started.
【0016】図1では交流モータ(100V/60Hz)を搭載
したTHOMAS社製コンプレッサーを使用したが、イ
ンバーターを介し、起動時に50Hzの周波数でモーター
を起動し、モーター特性(トルク曲線)やコンプレッサ
ーの機械的な抵抗などを考慮し、表2に示す制御曲線で
コンプレッサー回転数を制御する。In FIG. 1, a compressor manufactured by THOMAS equipped with an AC motor (100 V / 60 Hz) is used. The motor is started at a frequency of 50 Hz at the time of starting via an inverter, and the motor characteristics (torque curve) and the machine of the compressor are used. The rotational speed of the compressor is controlled by the control curve shown in Table 2 in consideration of the electrical resistance and the like.
【0017】起動時の回転数は予め定められた条件通り
に運転するため、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、起動性は更に向上する。In order to operate according to a predetermined condition at the time of start-up, it has a speed monitor such as a tachometer, and adjusts the speed based on the detection result of the speed monitor. Startability is further improved by a rotational speed stabilizing means such as a stabilizing feedback circuit.
【0018】このような制御を用いないで済むよう、予
め回転トルクの大きいモーターを選択し起動性を確保す
るという方法もあるが、回転トルクの高いモーターは消
費電力量が高いため酸素濃縮装置自体の電力量悪化を導
く。かかる装置は在宅で用いられるため、使用者の経済
的負担を軽減するという見地から、低消費電力型のコン
プレッサーを採用する必要があり、その際に発生する起
動性の低下を防ぐ意味で本発明は有効である。In order to avoid such a control, there is a method of selecting a motor having a large rotation torque in advance and securing startability. However, since a motor having a high rotation torque consumes a large amount of power, the oxygen concentrator itself is not used. Leads to the deterioration of the electric energy. Since such a device is used at home, it is necessary to employ a low-power-consumption type compressor from the viewpoint of reducing the economic burden on the user. Is valid.
【0019】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。The compressor means used in the adsorption-type oxygen concentrator of the present invention is not particularly limited.
Compressors such as reciprocating type and scroll type can be used.
【0020】起動時のコンプレッサー手段の2次側圧力
の急上昇を制御する別の態様としては、図3に示すよう
に、該吸着床の吸着、脱着再生工程を切り替える流路切
替手段の切替タイミングを、起動時の時間当たりの該流
路切替手段の切り替え回数を定常運転時よりも高めに設
定すると共に、所定時間後に切り替え回数を定常値に戻
す制御を行うことによりコンプレッサー手段の2次圧を
制御する装置が含まれる。かかる装置は、市販の交流モ
ーターを接続した回転式開閉弁をインバータにより制御
する装置を示し、図4は回転式開閉弁の起動から定格回
転数までの変更状態を示している。As another mode for controlling the sudden rise in the secondary pressure of the compressor means at the time of startup, as shown in FIG. 3, the switching timing of the flow path switching means for switching the adsorption and desorption regeneration steps of the adsorption bed is controlled. The secondary pressure of the compressor means is controlled by setting the number of times of switching of the flow path switching means per time at the time of startup to be higher than that in the normal operation, and performing control to return the number of times of switching to a steady value after a predetermined time. Device. Such a device is a device for controlling a rotary on-off valve connected to a commercially available AC motor by an inverter, and FIG. 4 shows a state where the rotary on-off valve is changed from activation to a rated rotation speed.
【0021】該流路切替手段は、ガス流れ方向とタイミ
ングを制御する事が可能な手段であり、開閉式電磁弁手
段や回転式開閉弁手段などが用いられる。The flow path switching means is a means capable of controlling the direction and timing of gas flow, and may be an open / close solenoid valve or a rotary open / close valve.
【0022】起動時の吸着床の加圧(吸着工程)、減圧
(脱着工程)の切替は、予め定められた起動時の時間当
たりの該流路切替手段の切り替え回数を定常運転時より
も高めに設定すると共に、所定時間後に切り替え回数を
定常値に戻すという条件で運転する。The switching between pressurization (adsorption step) and depressurization (desorption step) of the adsorbent bed at the time of start-up is performed by increasing the number of times of switching of the flow path switching means per predetermined start-up time as compared with the time of normal operation. , And the number of times of switching is returned to a steady value after a predetermined time.
【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。この電気的制御は前述のコンプレッサーの場合
と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、起動性は更に向上する。When a rotary on-off valve is used as the passage switching means, the rotation 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 using a motor. This electric control is the same as in the case of the above-described compressor, and differs depending on the type of the mounted motor.
If the motor is for AC power supply, power supply frequency control to energize,
A DC power supply motor is achieved by voltage control. Further, the rotation speed of the stepping motor can be controlled by the ON / OFF frequency of energization. Furthermore, it has a rotation speed monitoring means typified by a tachometer and the like, and the startability is further 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. I do.
【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 a control circuit.
【0025】流路切替手段の制御による装置の起動性向
上の基本方法としては、例えば回転式開閉弁手段をもち
いた酸素濃縮装置の場合、装置起動時に、図4に示すよ
うな条件に従い、該吸着床の加減圧を制御する。流路の
切替、即ち、吸着床の加減圧の切替を迅速に行う事によ
り、該吸着床の圧力上昇幅は小さく抑制され、コンプレ
ッサー2次側圧力の上昇を押えることで、極低温条件下
においてもコンプレッサーの起動が容易になる。一定時
間後には、別に定められた定常運転条件へと制御され、
酸素濃縮が開始される。As a basic method of improving the startability of the apparatus by controlling the flow path switching means, for example, in the case of an oxygen concentrator using a rotary on-off valve means, at the time of starting the apparatus, the conditions shown in FIG. The pressure in the adsorption bed is controlled. By rapidly switching the flow path, that is, switching the pressurization and decompression of the adsorbent bed, the pressure rise of the adsorbent bed is suppressed to a small extent, and by suppressing the rise of the secondary pressure of the compressor, under cryogenic conditions. This also makes it easier to start the compressor. After a certain period of time, it is controlled to a separately determined steady-state operating condition,
Oxygen concentration is started.
【0026】さらに、かかる装置は前述のようにコンプ
レッサー手段の回転制御と流路切替手段の制御の併用が
可能であり、組み合わせて使用することにより個々の技
術を単一で用いた場合より極低温条件下においても高い
起動性向上効果が得られる。Further, as described above, such a device can use both the rotation control of the compressor means and the control of the flow path switching means. Under the conditions, a high startability improvement effect can be obtained.
【0027】流路切替手段が回転式開閉弁手段の場合、
高回転用のモーターを採用し起動時の回転数を高く保つ
事は、消費電力の面からは前述のコンプレッサーの起動
とは相反する考え方となる。しかし、回転式開閉弁用モ
ーターの消費電力はコンプレッサーに比較して2桁低
く、かつ、回転抵抗が極めて小さいので、起動時に加減
圧切替高速化のためモーター自体を高速で回転させても
起動性、電力共に支障はなく、該モーターの起動不良は
発生しない。When the flow path switching means is a rotary on-off valve means,
Adopting a high-speed motor and keeping the number of revolutions at the start high is a contradictory idea to the above-mentioned compressor start in terms of power consumption. However, the power consumption of the rotary on-off valve motor is two orders of magnitude lower than that of the compressor, and the rotation resistance is extremely small. There is no problem with the electric power, and no starting failure of the motor occurs.
【0028】本発明の装置では、起動時の予め定められ
た条件でコンプレッサー手段や流路切替手段を制御する
場合、吸着床の温度を検知する温度検知手段、或はコン
プレッサーの温度を検知する温度検知手段等を備え、か
かる吸着床の温度が15℃以上、またはコンプレッサー
の温度が10℃以上の状態が確保された時点で装置の運
転を起動モードから定常運転モードに切り替えるような
条件とした制御を行うことが好ましい。In the apparatus of the present invention, when the compressor means and the flow path switching means are controlled under predetermined conditions at the time of starting, the temperature detecting means for detecting the temperature of the adsorption bed or the temperature for detecting the temperature of the compressor. Control that includes detection means and the like and switches the operation of the apparatus from the start-up mode to the steady-state operation mode when the temperature of the adsorption bed is 15 ° C. or more or the temperature of the compressor is 10 ° C. or more is secured. Is preferably performed.
【0029】また、タイマー手段を備え、一定時間運転
後に自動的に起動モードから定常運転モードへ制御する
装置とすることが出来るように条件付けすることも可能
であり、タイマー手段により一定時間経過後に該コンプ
レッサー手段の回転数や流路切替速度を変更する制御手
段を備えた装置、或いはカウンター手段を備え、一定回
数の吸脱着工程経過後に該コンプレッサー手段の回転数
や流路切替手段の切替速度を変更する制御手段を備えた
装置であることが好ましい。It is also possible to provide a condition that a timer means is provided to automatically control the operation mode from the start mode to the steady operation mode after the operation for a certain period of time. A device equipped with a control means for changing the rotation speed of the compressor means and the flow switching speed, or a counter means, and changing the rotation speed of the compressor means and the switching speed of the flow switching means after a certain number of adsorption / desorption steps. It is preferable that the apparatus is provided with a control unit that performs the control.
【0030】[0030]
【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0℃の環境下にお
いても、異常なく起動をし、起動不良機台は認められ
ず、極低温環境下における起動性能向上を図ることが出
来る。The adsorption type oxygen concentrator according to the present invention has a capacity of 50H.
Even under the environment of 0 ° C. in the both frequency power supply of z and 60 Hz, the start-up is performed without any abnormality, and the start-up failure machine is not recognized, and the start-up performance under the extremely low temperature environment can be improved.
【図1】本発明の吸着型酸素濃縮装置の概略構成図。FIG. 1 is a schematic configuration diagram of an adsorption-type oxygen concentrator according to the present invention.
【図2】本発明の吸着型酸素濃縮装置のコンプレッサー
の回転数制御図。FIG. 2 is a control diagram of a rotation speed of a compressor of the adsorption-type oxygen concentrator according to the present invention.
【図3】本発明の吸着型酸素濃縮装置の概略構成図。FIG. 3 is a schematic configuration diagram of an adsorption-type oxygen concentrator according to the present invention.
【図4】本発明の吸着型酸素濃縮装置の回転式開閉弁
(流路切替手段)の回転制御図。FIG. 4 is a rotation control diagram of a rotary on-off valve (flow path switching means) of the adsorption-type oxygen concentrator of the present invention.
Claims (3)
を充填した少なくとも1本の吸着床、該吸着床に加圧空
気を供給するコンプレッサー手段、該吸着床の吸着、脱
着再生工程を切り替える流路切替手段、および該吸着床
から得られた酸素濃縮気体を使用者に供給する酸素供給
手段を備えた吸着型酸素濃縮装置において、該コンプレ
ッサー手段の2次側圧力を制御する制御手段を備え、該
制御手段が吸着型酸素濃縮装置の起動時の2次側圧力上
昇を抑制する手段であることを特徴とする吸着型酸素濃
縮装置。1. At least one adsorption bed filled with an adsorbent for selectively adsorbing oxygen or nitrogen, compressor means for supplying pressurized air to the adsorption bed, and switching between adsorption and desorption regeneration steps of the adsorption bed In an adsorption-type oxygen concentrator provided with a flow path switching means and an oxygen supply means for supplying a user with oxygen-enriched gas obtained from the adsorption bed, a control means for controlling a secondary pressure of the compressor means is provided. An adsorption-type oxygen concentrator characterized in that the control means is means for suppressing a rise in secondary pressure when the adsorption-type oxygen concentrator is activated.
起動時の回転数を制限すると共に、所定時間後に定格回
転数まで上昇させる制御手段であることを特徴とする請
求項1記載の吸着型酸素濃縮装置。2. The adsorption-type oxygen according to claim 1, wherein said control means is a control means for limiting the number of revolutions of said compressor means at the time of starting and increasing the number of revolutions to a rated number of revolutions after a predetermined time. Concentrator.
流路切替手段の切り替え回数を定常運転時よりも高めに
設定すると共に、所定時間後に切り替え回数を定常値に
戻す制御を行う手段であることを特徴とする請求項1、
2に記載の吸着型酸素濃縮装置。3. The control means sets the number of times of switching of the flow path switching means per time at the start-up time to be higher than that in the steady operation, and performs control for returning the number of times of switching to a steady value after a predetermined time. The method according to claim 1, wherein
3. The adsorption-type oxygen concentrator according to 2.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001061483A JP2002253676A (en) | 2001-03-06 | 2001-03-06 | Adsorbing type oxygen concentrating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001061483A JP2002253676A (en) | 2001-03-06 | 2001-03-06 | Adsorbing type oxygen concentrating device |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2002253676A true JP2002253676A (en) | 2002-09-10 |
Family
ID=18920770
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001061483A Pending JP2002253676A (en) | 2001-03-06 | 2001-03-06 | Adsorbing type oxygen concentrating device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006263441A (en) * | 2005-02-24 | 2006-10-05 | Ngk Spark Plug Co Ltd | Oxygen enricher |
US7306657B2 (en) | 2003-10-28 | 2007-12-11 | Ngk Spark Plug Co., Ltd. | Oxygen concentrating apparatus |
JP2008214151A (en) * | 2007-03-06 | 2008-09-18 | Teijin Pharma Ltd | Oxygen concentrator |
US8337599B2 (en) | 2007-05-07 | 2012-12-25 | Teijin Pharma Limited | Oxygen concentrator |
-
2001
- 2001-03-06 JP JP2001061483A patent/JP2002253676A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7306657B2 (en) | 2003-10-28 | 2007-12-11 | Ngk Spark Plug Co., Ltd. | Oxygen concentrating apparatus |
JP2006263441A (en) * | 2005-02-24 | 2006-10-05 | Ngk Spark Plug Co Ltd | Oxygen enricher |
JP2008214151A (en) * | 2007-03-06 | 2008-09-18 | Teijin Pharma Ltd | Oxygen concentrator |
US8337599B2 (en) | 2007-05-07 | 2012-12-25 | Teijin Pharma Limited | Oxygen concentrator |
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