JP2008272350A - Oxygen concentrator - Google Patents
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- JP2008272350A JP2008272350A JP2007122327A JP2007122327A JP2008272350A JP 2008272350 A JP2008272350 A JP 2008272350A JP 2007122327 A JP2007122327 A JP 2007122327A JP 2007122327 A JP2007122327 A JP 2007122327A JP 2008272350 A JP2008272350 A JP 2008272350A
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- 239000001301 oxygen Substances 0.000 title claims abstract description 63
- 229910052760 oxygen Inorganic materials 0.000 title claims abstract description 63
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 title claims abstract description 62
- 238000001816 cooling Methods 0.000 claims abstract description 55
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 32
- 238000001179 sorption measurement Methods 0.000 claims abstract description 25
- 238000007664 blowing Methods 0.000 claims abstract description 15
- 230000006835 compression Effects 0.000 claims abstract description 15
- 238000007906 compression Methods 0.000 claims abstract description 15
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 15
- 239000003463 adsorbent Substances 0.000 claims abstract description 13
- 238000001514 detection method Methods 0.000 claims abstract description 11
- 239000007789 gas Substances 0.000 claims abstract description 7
- 150000002926 oxygen Chemical class 0.000 abstract 1
- 238000000034 method Methods 0.000 description 6
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 description 5
- 229910001882 dioxygen Inorganic materials 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- 230000003584 silencer Effects 0.000 description 4
- 238000002664 inhalation therapy Methods 0.000 description 3
- 238000003795 desorption Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 238000009434 installation Methods 0.000 description 2
- 239000012528 membrane Substances 0.000 description 2
- 238000012544 monitoring process Methods 0.000 description 2
- 239000010457 zeolite Substances 0.000 description 2
- 206010006458 Bronchitis chronic Diseases 0.000 description 1
- 208000014085 Chronic respiratory disease Diseases 0.000 description 1
- 206010014561 Emphysema Diseases 0.000 description 1
- 229910021536 Zeolite Inorganic materials 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
- 238000010586 diagram Methods 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
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 230000020169 heat generation Effects 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 210000000056 organ Anatomy 0.000 description 1
- 238000002640 oxygen therapy Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 230000000241 respiratory effect Effects 0.000 description 1
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
本発明は、酸素よりも窒素を優先的に吸着する吸着剤を用いた圧力変動吸着型の酸素濃縮装置に関するものである。 The present invention relates to a pressure fluctuation adsorption type oxygen concentrator using an adsorbent that preferentially adsorbs nitrogen over oxygen.
近年、喘息、肺気腫症、慢性気管支炎等の呼吸器系器官の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ひとつに酸素吸入療法がある。かかる酸素吸入療法とは、酸素ガスあるいは酸素富化空気を患者に吸入させるものである。その供給源として、酸素濃縮装置、液体酸素、酸素ガスボンベ等が知られているが、使用時の便利さや保守管理の容易さから、在宅酸素療法においては酸素濃縮装置が主流で用いられている。 In recent years, the number of patients suffering from respiratory organ diseases such as asthma, emphysema, and chronic bronchitis has been increasing. One of the most effective treatment methods is oxygen inhalation therapy. Such oxygen inhalation therapy is to allow a patient to inhale oxygen gas or oxygen-enriched air. Oxygen concentrators, liquid oxygen, oxygen gas cylinders, and the like are known as supply sources, but oxygen concentrators are mainly used in home oxygen therapy because of convenience during use and ease of maintenance.
酸素濃縮装置は、空気中に存在する約21%の酸素を濃縮して使用者に供給する装置であり、それには酸素を選択的に透過する膜を用いた膜式酸素濃縮装置と、窒素または酸素を優先的に吸着しうる吸着剤を用いた圧力変動吸着型酸素濃縮装置があるが、得られる酸素濃度の点から圧力変動吸着型酸素濃縮装置が主流になっている。 The oxygen concentrator is a device for concentrating and supplying about 21% oxygen present in the air to the user, and includes a membrane oxygen concentrator using a membrane that selectively permeates oxygen, nitrogen or There is a pressure fluctuation adsorption type oxygen concentrator using an adsorbent capable of preferentially adsorbing oxygen, but the pressure fluctuation adsorption type oxygen concentrator is the mainstream in terms of the obtained oxygen concentration.
かかる圧力変動吸着型酸素濃縮装置として、窒素又は酸素を選択的に吸着し得るゼオライトなどの吸着剤を1個或いは、複数の吸着筒に充填した酸素濃縮装置が知られている。通常、窒素を選択的に吸着し得る吸着剤を充填した1個或いは複数の吸着筒にコンプレッサで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、吸着筒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、更には脱着工程終了直前に既に生成した乾燥酸素濃縮気体を一部逆流させ再生効率の向上と昇圧を目的とする均圧工程を、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。 As such a pressure fluctuation adsorption type oxygen concentrator, an oxygen concentrator in which one or a plurality of adsorbents such as zeolite capable of selectively adsorbing nitrogen or oxygen is filled is known. Usually, an adsorption process, adsorption, in which oxygen-concentrated gas is obtained by supplying compressed air to one or more adsorption cylinders filled with an adsorbent capable of selectively adsorbing nitrogen and adsorbing nitrogen in a pressurized state. A desorption process in which nitrogen is desorbed by reducing the internal pressure of the cylinder to regenerate the adsorbent, and a portion of the dry oxygen-concentrated gas that has already been generated just before the desorption process is backflowed to improve the regeneration efficiency and increase the pressure. This is an apparatus for obtaining an oxygen-enriched gas by sequentially performing the pressure step in a constant cycle.
かかる酸素濃縮装置は在宅用、医療用途として使用する為には、装置の小型化、長期寿命、装置安定化が必須であり、装置内における熱発生の大部分を占めるコンプレッサの冷却は必須要件となる。
かかる酸素濃縮気体を得る装置におけるコンプレッサを冷却する方法としては、特開2001-278606号公報に示されるように、ファンまたはブロアなどの冷却ファン(送風手段)によりコンプレッサボックスの上方から冷却空気を強制対流させ、下方の排気口から排気するのが一般的である。
In order to use such oxygen concentrators for home use and medical applications, it is essential to reduce the size of the device, extend its life, and stabilize the device. Cooling the compressor, which accounts for the majority of heat generation in the device, is an essential requirement. Become.
As a method for cooling the compressor in the apparatus for obtaining the oxygen-enriched gas, as shown in Japanese Patent Laid-Open No. 2001-278606, cooling air is forced from above the compressor box by a cooling fan (blower means) such as a fan or a blower. It is common to convect and exhaust from the lower exhaust port.
さらに特に酸素濃縮装置に使用されるコンプレッサボックスに収納された揺動型、往復型コンプレッサを均一かつ効率よく冷却する方法として、特開2003-246607号公報には、コンプレッサボックス上部に冷却ファンを備えると共に、冷却ファンによる空気の流れが、該ボックス下部に配置された吸気開口部より吸入され、コンプレッサ下面で回折したのち、ボックス上部に配置された排気開口部より排出されることを特徴とする酸素濃縮装置が記載されている。 Furthermore, as a method for uniformly and efficiently cooling an oscillating and reciprocating compressor housed in a compressor box used in an oxygen concentrator, JP 2003-246607 A includes a cooling fan at the top of the compressor box. The oxygen flow is characterized in that the air flow by the cooling fan is sucked from the intake opening disposed at the lower part of the box, diffracted at the lower surface of the compressor, and then discharged from the exhaust opening disposed at the upper part of the box. A concentrator is described.
また、特開2004-18313号公報には、冬季等の低温環境下で所定の酸素濃度を簡易に確保することができる在宅医療用の酸素濃縮装置として、設置環境温度及び/または圧縮空気温度を検出する温度検出手段を備え、検出された該設置環境温度または圧縮空気温度のいずれかに基づいて圧縮空気が酸素濃度条件と対応する所定の目標温度となるように冷却送風手段の駆動を制御する駆動制御手段を備えた装置が記載されている。 Japanese Patent Laid-Open No. 2004-18313 discloses an installation environment temperature and / or a compressed air temperature as an oxygen concentrator for home medical care that can easily secure a predetermined oxygen concentration in a low temperature environment such as winter. Temperature detecting means for detecting is provided, and the driving of the cooling air blowing means is controlled based on either the detected installation environment temperature or the compressed air temperature so that the compressed air becomes a predetermined target temperature corresponding to the oxygen concentration condition. An apparatus with drive control means is described.
酸素濃縮装置の筐体内の冷却、特に発生熱源の大部分を占めるコンプレッサの冷却は、装置の長期耐久性を維持するためには必須要素であり、いずれの装置のおいても、品質保証期間の間は、運転保証条件下で必要な装置の冷却能力を有する冷却ファンを搭載している。大型の冷却ファンは消費電力が大きく、更に発生する騒音も大きくなる。
本発明は、かかる装置のコンプレッサの温度を測定し、状況に応じ送風手段を制御することにより過剰冷却を無くし、騒音低減・消費電力低減を実現した装置を提供することを目的とする。
Cooling of the oxygen concentrator housing, especially the compressor that accounts for the majority of the heat source, is an essential element for maintaining the long-term durability of the equipment. In the meantime, it is equipped with a cooling fan that has the required equipment cooling capacity under guaranteed operating conditions. Large cooling fans consume more power and generate more noise.
It is an object of the present invention to provide an apparatus that reduces noise and power consumption by measuring the temperature of the compressor of such an apparatus and controlling the blowing means according to the situation to eliminate excessive cooling.
本発明は、かかる課題を解決する手段として以下の記する酸素濃縮装置を提供する。すなわち本発明は、酸素よりも窒素を優先的に吸着する吸着剤を充填した少なくとも1個の吸着床と、該吸着床に圧縮空気を供給して窒素を吸着させることにより酸素濃縮気体を生成するための空気圧縮手段、該空気圧縮手段の温度を検出する温度検出手段、該空気圧縮手段を冷却する送風手段を備えた酸素濃縮装置において、該温度検出手段により得られた温度に基づいて送風手段の駆動を制御する制御手段を備え、該温度検出手段が予め設定した上限温度値以上の値を検知した場合に、該送風手段の送風量を増加させる制御を、下限温度値以下の値を検知した場合に、該送風手段の送風量を減少させる制御を行う手段であることを特徴とする酸素濃縮装置を提供する。 The present invention provides an oxygen concentrator as described below as means for solving such problems. That is, the present invention generates at least one adsorbent bed filled with an adsorbent that preferentially adsorbs nitrogen over oxygen, and generates oxygen-enriched gas by supplying compressed air to the adsorbent bed to adsorb nitrogen. In the oxygen concentrating apparatus provided with the air compression means for detecting the temperature, the temperature detection means for detecting the temperature of the air compression means, and the air blowing means for cooling the air compression means, the air blowing means based on the temperature obtained by the temperature detection means Control means for controlling the driving of the air supply, and when the temperature detection means detects a value equal to or higher than a preset upper limit temperature value, the control for increasing the air flow rate of the blower means detects a value lower than the lower limit temperature value. In such a case, an oxygen concentrating device is provided which is a means for performing control to reduce the amount of air blown by the air blowing means.
また本発明は、かかる送風手段がPWM制御で駆動する冷却ファン、または印加電圧を切替えて駆動する冷却ファンであることを特徴とする酸素濃縮装置を提供する。 The present invention also provides an oxygen concentrator characterized in that the air blowing means is a cooling fan driven by PWM control or a cooling fan driven by switching an applied voltage.
本発明の酸素濃縮装置は、慢性呼吸器疾患患者などに対して行われる酸素吸入療法に使用する医療用酸素濃縮装置に適用することができ、装置の使用環境状況に応じて、冷却手段である送風手段の運転を制御することにより、騒音の低減および消費電力の低減を実現することができる。 The oxygen concentrator of the present invention can be applied to a medical oxygen concentrator used for oxygen inhalation therapy performed for patients with chronic respiratory diseases and the like, and is a cooling means according to the use environment of the device. By controlling the operation of the blowing means, it is possible to reduce noise and power consumption.
本発明の実施態様例である圧力変動吸着型の酸素濃縮装置は、原料空気を圧縮し供給する空気圧縮手段、該空気圧縮手段を冷却するための送風手段、該空気圧縮手段の温度を検出する温度検出手段を備え、該温度検出手段に基づき該空気圧縮手段の状態を監視し、該送風手段の駆動を制御する駆動制御手段を備えたことを特徴とする。詳細には、該空気圧縮手段があらかじめ定めた切替温度に達すると該送風手段の駆動状態を制御することを特徴とする。 An oxygen concentration apparatus of pressure fluctuation adsorption type as an embodiment of the present invention detects an air compression means for compressing and supplying raw material air, a blowing means for cooling the air compression means, and a temperature of the air compression means. A temperature detection unit is provided, and a drive control unit that monitors the state of the air compression unit based on the temperature detection unit and controls the driving of the blower unit is provided. Specifically, the driving state of the air blowing means is controlled when the air compression means reaches a predetermined switching temperature.
かかる構成の圧力変動吸着型酸素濃縮装置は、吸入空気を空気圧縮手段によって圧縮し、この圧縮空気を吸着床に送ることによって窒素を吸着し濃縮酸素を送出する。このとき検出された空気圧縮手段の温度により送風手段が空気圧縮手段を過剰に冷却していないか判断し制御することから、騒音低減・消費電力低減を図ることができる。 The pressure fluctuation adsorption type oxygen concentrator having such a configuration compresses intake air by an air compression means, and sends the compressed air to an adsorption bed to adsorb nitrogen and send out concentrated oxygen. Since the air blowing means determines whether or not the air compressing means is excessively cooled based on the temperature of the air compressing means detected at this time and controls it, noise and power consumption can be reduced.
本発明の酸素濃縮装置の実施形態について図面を用いて説明する。
圧力変動吸着型酸素濃縮装置のシステム構成図を図1に示す。酸素濃縮装置1は、空気を吸入して圧縮するコンプレッサ2、その圧縮空気から選択的に窒素を吸着する吸着剤を充填した吸着筒3,3を介し生成された濃縮酸素を一時保管する製品タンク4、製品酸素の圧力を調整する圧力調整器5等で構成され、カニューラ6により利用者に濃縮酸素を供給する。
An embodiment of the oxygen concentrator of the present invention will be described with reference to the drawings.
A system configuration diagram of the pressure fluctuation adsorption type oxygen concentrator is shown in FIG. Oxygen concentrator 1 is a product tank for temporarily storing concentrated oxygen generated through a compressor 2 that sucks and compresses air, and adsorption cylinders 3 and 3 filled with an adsorbent that selectively adsorbs nitrogen from the compressed air. 4. Consists of a pressure regulator 5 that adjusts the pressure of product oxygen, and the cannula 6 supplies concentrated oxygen to the user.
この酸素ガスの取り出しは、原料空気を酸素ガス分子よりも窒素ガス分子を選択的に吸着する5A型、13X型やLi-X型、MD-X型などのゼオライトなどからなる吸着剤が充填された吸着筒に対して、切換弁によって対象とする吸着筒を順次切り換えながら、原料空気をコンプレッサにより加圧して供給し、吸着筒内で原料空気中に含まれる約77%の窒素ガスを選択的に吸着除去する。 This oxygen gas is extracted by filling the material air with adsorbents such as zeolites such as 5A, 13X, Li-X, and MD-X that selectively adsorb nitrogen gas molecules over oxygen gas molecules. While the target adsorption cylinder is sequentially switched by the switching valve to the adsorption cylinder, the raw material air is pressurized and supplied by the compressor, and approximately 77% nitrogen gas contained in the raw air is selectively contained in the adsorption cylinder. Remove by adsorption.
前記の吸着筒3としては、前記吸着剤を充填した円筒状容器で形成され、通常、1筒式、2筒式の他に3筒以上の多筒式が用いられるが、連続的かつ効率的に原料空気から酸素富化空気を製造するためには、2筒式や多筒式の吸着筒を使用することが好ましい。 The adsorbing cylinder 3 is formed of a cylindrical container filled with the adsorbent, and usually a multi-cylinder type of 3 or more cylinders is used in addition to the 1-cylinder type and the 2-cylinder type. In order to produce oxygen-enriched air from raw material air, it is preferable to use a two-cylinder or multi-cylinder type adsorption cylinder.
また、前記のコンプレッサ2としては、圧縮機能及び真空機能を有するコンプレッサとして2ヘッドのタイプの揺動型空気圧縮機が用いられるほか、スクリュー式、ロータリー式、スクロール式などの回転型空気圧縮機が用いられる場合もある。また、このコンプレッサ2を駆動するモータの電源は、交流であっても直流であってもよい。 As the compressor 2, a two-head type oscillating air compressor is used as a compressor having a compression function and a vacuum function, and a rotary air compressor such as a screw type, a rotary type, a scroll type, or the like is used. Sometimes used. The power source of the motor that drives the compressor 2 may be alternating current or direct current.
詳細には、コンプレッサ2は冷却ファン7、モータ温度を検出する温度センサ8、冷却ファン制御回路9を備えており、温度センサ8の検出値に応じ決められた動作をするよう制御回路9にて冷却ファン7の送風量を制御する。更にコンプレッサ2のみを冷却する冷却ファン7以外にも、外気を装置内に取り込み、電装部品などを含め、筐体内全体を冷却する冷却ファン7’を備え、冷却ファン制御回路9により両者のファンモータ回転数を制御することで装置全体の冷却効率の最適化を図る。冷却ファン7や冷却ファン7’には軸流ファンやシロッコファンなどを用いることができ、各冷却ファンのモータ回転数はPWM制御による連続運転制御や、例えば24V、12V、0Vなど印加電圧の切替制御による回転数制御を採用することができる。 Specifically, the compressor 2 includes a cooling fan 7, a temperature sensor 8 that detects the motor temperature, and a cooling fan control circuit 9. The control circuit 9 performs an operation determined according to the detection value of the temperature sensor 8. The air flow rate of the cooling fan 7 is controlled. In addition to the cooling fan 7 that cools only the compressor 2, it also has a cooling fan 7 ′ that takes outside air into the device and cools the entire interior including the electrical components. By controlling the number of revolutions, the cooling efficiency of the entire device is optimized. The cooling fan 7 and the cooling fan 7 'can be an axial fan, a sirocco fan, etc., and the motor rotation speed of each cooling fan can be controlled continuously by PWM control or switching of applied voltage such as 24V, 12V, 0V, etc. Rotational speed control by control can be employed.
また、コンプレッサ2の吸気管10には、インテイクフィルタ11、吸気フィルタ12、消音器13等を備えている。吐出側には熱交換器14を介して送気管15を接続する。排気管16には消音器17を接続する。
二本の吸着筒3,3は、それぞれ圧縮空気の出入りを制御するための切り替え弁18,18、送出側を均圧弁20で両筒を繋ぐと共にそれぞれ逆止弁21,21を備え、濃縮酸素を一時保管する製品タンク4へ接続される。
その先、カニューラ6までには、圧力調整器5、酸素濃度センサ19、流量調整器22、パーティクルフィルタ13を備える。
Further, the intake pipe 10 of the compressor 2 includes an intake filter 11, an intake filter 12, a silencer 13, and the like. An air supply pipe 15 is connected to the discharge side via a heat exchanger 14. A silencer 17 is connected to the exhaust pipe 16.
The two adsorbing cylinders 3 and 3 are respectively provided with switching valves 18 and 18 for controlling the flow of compressed air, the pressure-feeding valve 20 on the delivery side, and the check valves 21 and 21 respectively. Is connected to the product tank 4 for temporary storage.
Further up to the cannula 6, a pressure regulator 5, an oxygen concentration sensor 19, a flow rate regulator 22, and a particle filter 13 are provided.
上記構成の圧力変動型酸素濃縮装置は、原料空気を圧縮し窒素吸着部に送ることで濃縮酸素が送出される。冷却ファン制御部はコンプレッサのモータ温度を監視することから、コンプレッサの温度状態を把握し冷却ファンを動作させる。例えばコンプレッサの温度を0.5秒間隔で測定し、その温度により低温、通常、高温を判断して冷却ファンの駆動状態を制御する。温度制御を設けない場合、冷却ファンを常に駆動させることとなり、コンプレッサの過剰冷却及び無駄な電力消費を招いてしまうが、コンプレッサの温度を監視することによりコンプレッサの過剰冷却を無くし、騒音低減・消費電力低減を実現する。 In the pressure fluctuation type oxygen concentrator having the above-described configuration, the concentrated oxygen is delivered by compressing the raw material air and sending it to the nitrogen adsorption section. Since the cooling fan controller monitors the motor temperature of the compressor, it grasps the temperature state of the compressor and operates the cooling fan. For example, the temperature of the compressor is measured at intervals of 0.5 seconds, and the driving state of the cooling fan is controlled by determining whether the temperature is low, usually high. Without temperature control, the cooling fan is always driven, which causes overcooling of the compressor and unnecessary power consumption. However, monitoring the temperature of the compressor eliminates overcooling of the compressor and reduces noise and consumption. Realize power reduction.
近年如何なる電子機器も低消費電力化が求められている。特に本装置のような在宅医療機器において消費電力低下は利用者の負担の低減することに繋がりQOL向上の観点からも重要である。従来の冷却ファン連続運転に比べ、コンプレッサの温度監視による冷却ファンの過冷却防止は、冷却が不要な場合冷却ファンを停止させることが可能であり消費電力は確実に低下する。 In recent years, any electronic device is required to have low power consumption. In particular, in home medical equipment such as this device, a reduction in power consumption leads to a reduction in the burden on the user, which is important from the viewpoint of improving QOL. Compared to conventional continuous cooling fan operation, overcooling prevention of the cooling fan by monitoring the temperature of the compressor can stop the cooling fan when cooling is unnecessary, and power consumption is reliably reduced.
本装置は、在宅および病院で利用することが多く騒音低減は、利用者にとって低消費電力と共に重要な項目である。従来行われていたファン連続運転では、ファンによる風切り音が大きく、騒音低減が望まれていた。本装置によれば冷却が不要な場合において冷却ファンを停止させるので冷却ファンが発する風切り音がなく低騒音化が実現できる。 This device is often used at home and in hospitals, and noise reduction is an important item for users as well as low power consumption. In conventional fan continuous operation, wind noise from the fan is large, and noise reduction has been desired. According to this apparatus, since the cooling fan is stopped when cooling is unnecessary, there is no wind noise generated by the cooling fan, and low noise can be realized.
図1に記載の2L/分の最大酸素生成能力を有する圧力変動吸着型酸素濃縮装置を用い、コンプレッサ温度の検知結果に基いて冷却ファンの回転を制御することによる消費電力への効果、騒音低減への効果を確認した。かかる装置には冷却ファンとして装置全体を冷却するシロッコファン7’および2ヘッド型レシプロコンプレッサ2のシリンダ部を直接冷却する2個の軸流ファン7,7を備える。 Effect on power consumption and noise reduction by controlling the rotation of the cooling fan based on the detection result of the compressor temperature using the pressure fluctuation adsorption type oxygen concentrator having the maximum oxygen production capacity of 2 L / min shown in FIG. Confirmed the effect. Such a device includes a sirocco fan 7 'for cooling the entire device and two axial fans 7 and 7 for directly cooling the cylinder portion of the two-head type reciprocating compressor 2 as cooling fans.
コンプレッサを一定回転数で運転させた状態で外部の環境温度を−5℃、25℃、35℃に変化させることによりコンプレッサの温度を変化させ、冷却ファンの作動状態を遷移させた。 The operating temperature of the cooling fan was changed by changing the temperature of the compressor by changing the external environmental temperature to −5 ° C., 25 ° C., and 35 ° C. while operating the compressor at a constant rotational speed.
冷却ファンの回転数制御は、シロッコファン7’について、コンプレッサ温度が30℃未満でOFF、30℃以上で連続運転とし、軸流ファン7については、コンプレッサ温度が30℃未満で0V、30℃以上65℃未満で12V、65℃以上で24Vの電圧で駆動させる制御を行なった。 The number of rotations of the cooling fan is controlled for the sirocco fan 7 'when the compressor temperature is less than 30 ° C, and is continuously operated when the compressor temperature is less than 30 ° C. For the axial fan 7, the compressor temperature is less than 30 ° C and 0V, 30 ° C or more Control was performed to drive at a voltage of 12V below 65 ° C and 24V above 65 ° C.
環境温度−5℃では、コンプレッサの温度tは30℃以下となり冷却ファン7,7’は共にOFFの状態、環境温度25℃では、コンプレッサの温度tは30℃以上、65℃未満となりシロッコファン7’を12Vで駆動、軸流ファン7は連続運転した。さらに環境温度35℃では、コンプレッサの温度は65℃以上となり、シロッコファン7’を24Vで駆動した。 At an ambient temperature of -5 ° C, the compressor temperature t is 30 ° C or less and the cooling fans 7 and 7 'are both OFF. At an ambient temperature of 25 ° C, the compressor temperature t is 30 ° C or more and less than 65 ° C, and the sirocco fan 7 'Was driven at 12V, and the axial fan 7 was operated continuously. Furthermore, at an environmental temperature of 35 ° C., the compressor temperature was 65 ° C. or higher, and the sirocco fan 7 ′ was driven at 24V.
その結果を表1及び表2に示す。比較対照として冷却ファン制御を行わない(OFF)の状態での消費電力及び騒音測定の結果を示す。冷却ファンの運転制御有無により最大で5.39[W](環境温度-5℃の時の平均消費電力)、最小で3.18[W](環境温度35℃の時の平均消費電力)消費電力を抑えることができた。騒音に関しては、0.2[dBA]〜3.2[dBA]の騒音を低減している。装置の前後左右で騒音を測定した結果、特に排気口が設けてある機台を正面に見て右後方の騒音は冷却ファンの制御有無による効果が大きいことが明らかになった。 The results are shown in Tables 1 and 2. As a comparison, the results of power consumption and noise measurement when the cooling fan control is not performed (OFF) are shown. Reduce power consumption by a maximum of 5.39 [W] (average power consumption at an ambient temperature of -5 ° C) and a minimum of 3.18 [W] (average power consumption at an ambient temperature of 35 ° C), depending on whether the cooling fan is controlled or not. I was able to. Regarding noise, the noise is reduced from 0.2 [dBA] to 3.2 [dBA]. As a result of measuring the noise at the front, rear, left and right of the device, it became clear that the noise on the right rear side, especially when looking at the machine base with the exhaust vent in front, is greatly influenced by the presence or absence of control of the cooling fan.
1. 酸素濃縮器
2. コンプレッサ(空気圧縮手段)
3. 吸着筒(吸着床)
4. 製品タンク
5. 圧力調整器
6. カニューラ
7. 冷却ファン
8. 温度センサ
9. 冷却ファン制御回路
10. 吸気管
11. インテイクフィルタ
12. 吸気フィルタ
13. 消音器
14. 熱交換器
15. 送気管
16. 排気管
17. 消音器
18. 切り替え弁
19. 酸素濃度センサ
20. 均圧弁
21. 逆止弁
22. 流量調整器
1. 1. oxygen concentrator Compressor (Air compression means)
3. Adsorption cylinder (adsorption bed)
4). Product tank 5. Pressure regulator 6. Cannula 7. Cooling fan 8. Temperature sensor 9. 9. Cooling fan control circuit Intake pipe 11. Intake filter 12. Intake filter 13. Silencer 14. Heat exchanger 15. Air pipe 16. Exhaust pipe 17. Silencer 18. Switching valve 19. Oxygen concentration sensor 20. Equalizing valve 21. Check valve 22. Flow regulator
Claims (3)
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JP2007122327A JP2008272350A (en) | 2007-05-07 | 2007-05-07 | Oxygen concentrator |
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JP2007122327A JP2008272350A (en) | 2007-05-07 | 2007-05-07 | Oxygen concentrator |
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Cited By (2)
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JP2021122774A (en) * | 2020-02-04 | 2021-08-30 | 株式会社日立産機システム | Gas separation system and gas separation method |
JP7530282B2 (en) | 2020-12-16 | 2024-08-07 | 株式会社クラレ | Nitrogen gas separation method and nitrogen gas separation device |
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