The present invention relates to an oxygen concentrator, and more particularly to a medical oxygen concentrator that is capable of supplying oxygen by compressing suctioned raw air and supplying the compressed air to an adsorbent.
An oxygen concentrator is configured to acquire oxygen by using a pressure swing adsorbing method that generates oxygen by using zeolite selectively adsorbing nitrogen by transmitting oxygen in raw air, as an adsorbent.
According to the oxygen concentrator using the method, introduced raw air is compressed by a compressor to generate compressed air and the compressed air is supplied to an adsorption column containing the adsorbent to separate oxygen by adsorbing nitrogen to the adsorbent. While the generated oxygen is stored in a tank, a predetermined flow of oxygen can be supplied from the tank through a pressure reducing valve or a flow setter to allow a patient to inhale oxygen by using a mechanism such as a nasal cannula, and the like.
When the oxygen concentrator is installed at a place where an AC power supply (utility AC power supply) can be used, for example, a domiciliary oxygen therapy patient having a deteriorated lung function can safely inhale oxygen even while sleeping to have a good sleep. In particular, when the domiciliary oxygen therapy patient uses the oxygen concentrator even while sleeping, the oxygen concentrator preferably operates very quietly. For example, noise of the oxygen concentrator is preferably equal to or less than a noise level generated from an indoor air-conditioning facility.
The oxygen concentrator used for a long-term oxygen inhalation therapy which is effective as a therapeutic method for a patient who suffers from respiratory disease, such as chronic bronchitis and the like, is generally not transportable and is not configured for the patient to take with them to go outside.
When the patient is forced to go outside, for example, the patient inhales concentrated oxygen from an oxygen bomb while pushing a cart mounted with the oxygen bomb in which oxygen is charged in a predetermined receiving reservoir. Oxygen needs to be charged in the oxygen bomb by using an exclusive facility. Therefore, a transportable or movable oxygen concentrator is proposed, and the transportable or movable oxygen concentrator includes a compressor that introduces raw air to generate compressed air and decompressed air (see Patent Literature 1).
Patent Literature 1: Japanese Patent Application Laid-Open No. 2005-111016
However, in a conventional oxygen concentrator, as illustrated in
However, when the raw air is transported from the conduit 401 to the branch conduits 404 and 405 in order to increase the amount of suctioned raw air, pressure loss is increased, and as a result, the actual amount of suctioned raw air is decreased.
Accordingly, an object of the present invention is to provide an oxygen concentrator that can reduce pressure loss when suctioning raw air and increase an amount of suctioned raw air by an amount of reduction in the pressure loss without significantly changing a basic structure of a compressor.
An oxygen concentrator according to the present invention includes: a compressor that has a plurality of suction ports suctioning raw air and that generates compressed air by compressing the suctioned raw air; and a silencer installed at a stage preceding the compressor to reduce noise from the suction ports, in which the plurality of suction ports of the compressor are individually connected with the silencer.
According to the configuration, by directly connecting the plurality of raw air suction ports of the compressor to the silencer by using respective connection conduits, the amount of sent raw air per one connection conduit can be reduced and the raw air can be introduced into the compressor without loss by reducing pressure loss.
In the oxygen concentrator of the present invention, the compressor may include a first pump unit and a second pump unit that respectively generate the compressed air by compressing the raw air by reciprocatively moving a piston in a sleeve, and the suction ports may be formed in the first pump and the second pump unit, respectively.
According to the configuration, since a raw air suction port of the first pump unit and the raw air suction port of the second pump can be directly connected by using the respective connection conduits, the influence of the pressure loss can be reduced by reducing the amount of sent raw air per one connection conduit.
In the oxygen concentrator of the present invention, the silencer may have a filter removing dust in the compressed air.
According to the configuration, after the filter removes the dust in the compressed air, the compressed air can be sent to the plurality of connection conduits and the influence of the pressure loss can be reduced by reducing the amount of sent raw air per one connection conduit.
According to the present invention, it is possible to provide an oxygen concentrator that can reduce pressure loss when suctioning raw air and increase an amount of suctioned raw air by an amount of reduction in the pressure loss without significantly changing a basic structure of a compressor.
Hereinafter, an exemplary embodiment of the present invention will be described in detail with reference to the accompanying drawings.
The oxygen concentrator 1 illustrated in
The oxygen concentrator 1 illustrated in
The main case 2 includes a front panel 2F, left and right side panels 2S, and a rear panel 2R, a top 2D, and a bottom 2B. In an inner surface of the main case 2, as a soundproof material, a non-woven fabric, which consists of a polyolefin based fiber (preferably, a polypropylene fiber) having a fiber diameter in the range of 1 to 4 μm and a polyolefin based fiber (preferably, a polypropylene fiber) having a fiber diameter in the range of 20 to 30 μm, may be used. By using the non-woven fabric, a light weight and a soundproof effect are achieved. As illustrated in
Referring to
As illustrated in
As illustrated in
As illustrated in
As illustrated in
As illustrated in
An end 37B of the conduit 37 is connected to a suction side end 38A of the noise buffer 38 also serving as the intake filter, and a first end 40A of the first connection conduit 40 and a first end 41A of the second connection conduit 41 are connected to a discharge side end 38B of the noise buffer 38 also serving as the intake filter. A second end 40B of the first connection conduit 40 is connected to a suction port 11P of the case section 11F and a second end 41B of the second connection conduit 41 is connected to a suction port 12P of the case section 12F.
An introduction path of the raw air between the noise buffer 38 also serving as the intake filter and the compressor 10 is divided into a plurality of paths, and the first connection conduit 40 and the second connection conduit 41 are connected in parallel between the noise buffer 38 also serving as the intake filter and the compressor 10. In other words, the first connection conduit 40 and the second connection conduit 41 directly connect the suction ports 11P and 12P of the noise buffer 38 also serving as the intake filter and the compressor 10.
As a result, as the raw air introduced from the conduit 37 into the noise buffer 38 also serving as the intake filter passes through the noise buffer 38 also serving as the intake filter, dust is removed by the intake filter, and after noise is reduced, the raw air flows dividedly into the first connection conduit 40 and the second connection conduit 41 and may be introduced into the case section 11F through the suction port 11P of the case section 11F and further, may be introduced into the case section 12F through the suction port 12P of the case section 12F.
The head covers 11H and 12H are commonly connected to the conduit 15 and the generated compressed air is sent through the conduit 15. A heat-dissipating radiator 13 is placed at midstream of the conduit 15.
Herein, as the connection conduits, two conduits, that is, the first connection conduit 40 and the second connection conduit 41, are installed in the embodiment, but the connection conduits are installed as many as sleeves (cylinders) and when the number of the sleeves increases, individually connected connection conduits are also correspondingly increased as many.
Herein, referring to
A double line illustrated in
As illustrated in
As such, the raw air is introduced into the compressor 10 to become the compressed air, but heat is generated when the raw air is compressed. As a result, the compressor 10, in particular, the sleeves 11 and 12 are cooled by blowing from the first fan 34 and the second fan 36 for cooling. The compressed air sent from the compressor 10 through the conduit 15 is cooled by the radiator 13.
By cooling the compressed air, the temperature of zeolite as an adsorbent of which a function deteriorates at high temperature may be prevented from being increased. As a result, zeolite may sufficiently serve as the adsorbent for generating oxygen by adsorption of nitrogen and oxygen may be concentrated up to approximately 90% or more.
The first adsorption column body 31 and the second adsorption column body 32 as examples of adsorption members placed in line are placed in parallel vertically. The 3-way switching valves 14B and 14C are connected to the first adsorption column body 31 and the second adsorption column body 32, respectively. One end of one 3-way switching valve 14B is connected to the conduit 15. One 3-way switching valve 14B and the other 3-way switching valve 14C are connected to each other and one end of the other 3-way switching valve 14C is connected to a conduit 15R. An end of the conduit 15R reaches the exhaust port 6.
The 3-way switching valves 14B and 14C are connected to correspond to the first adsorption column body 31 and the second adsorption column body 32, respectively. The compressed air generated from the compressor 10 are alternately supplied to the first adsorption column body 31 and the second adsorption column body 32 through the conduit 15, and the 3-way switching valves 14B and 14C.
Zeolite as a catalyst adsorbent is stored in each of the first adsorption column body 31 and the second adsorption column body 32. The zeolite is X-type zeolite in which for example, a ratio of Si2O3/Al2O3 is in the range of 2.0 to 3.0, and zeolite in which at least 88% of a tetrahedral unit of Al2O3 is combined with lithium cation is used to increase an adsorption amount of nitrogen per unit weight. The zeolite has particularly, a granule measurement value which is less than 1 mm and at least 88% of the tetrahedral unit is preferably fused with lithium cation. By using zeolite, the amount of used raw air required to separate oxygen may be reduced as compared with a case of using other adsorbent. As a result, the compressor 10 for generating the compressed air may be further miniaturized and low noise of the compressor 10 may be achieved.
As illustrated in
As illustrated in
As illustrated in
A coupler socket 71 of a nasal cannula 70 is removably connected to the oxygen outlet 100. The coupler socket 71 is connected to the nasal cannula 70 through a tube 72. A patient may inhale for example, oxygen having a flow corresponding to a maximum flow of 5 L/min. and concentrated at approximately 90% or more, through the nasal cannula 70.
Subsequently, a power system will be described with reference to
A connector 203 of an AC (utility AC) power supply illustrated in
As a result, the central control unit 200 of
The central control unit 200 of
A read only memory (ROM) storing a predetermined operation program is built in the central control unit 200 and a circuit constituted by an external storage device, a volatile memory, a temporary storage device, and a real-time clock is electrically connected to the central control unit 200. The central control unit 200 is accessible by connecting with an external communication line, and the like through a communication connector 205.
By on/off-controlling the 3-way switching valves 14B and 14C and the uniform-pressure valve 107 illustrated in
The oxygen flow setting button 102 may set the flow of oxygen whenever for example, operating oxygen concentrated at approximately 90% or more from 0.25 L (liter) to the maximum 5 L by 0.25 L per minute. As the display unit 128, for example, a display device such as a liquid crystal monitor displaying 7 segments, and the like is used. For example, display items including the oxygen flow, an oxygen lamp, warning icons (tube bending, separation of the humidifier, decrease in oxygen concentration, stoppage of power supplying, a residual quantity of the battery, battery in operation, and a charging lamp), an accumulation time, and the like may be displayed in the display unit 128.
The compressor 10 illustrated in
Subsequently, an operation example of the oxygen concentrator 1 will be described.
The central control unit 200 illustrated in
When the compressor 10 operates, the raw air is introduced from the air introduction port 5 illustrated in
The first connection conduit 40 and the second connection conduit 41 divide an introduction path of the raw air between the noise buffer 38 also serving as the intake filter and the compressor 10 into a plurality of systems to be parallel and directly connect the noise buffer 38 also serving as the intake filter and the suction ports 11P and 12P of the compressor 10 to each other. As a result, the amount of raw air which should be sent per one of the first connection conduit 40 and the second connection conduit 41 maybe reduced. In other words, although the diameters of the first conduit 40 and the second conduit 41 are set to be small, the pressure loss is not increased.
The compressed air generated by the compressor 10 illustrated in
Meanwhile, the central control unit 200 illustrated in
The oxygen concentration sensor 66 of
In a connection structure of branch conduits 404 and 405 of the compressor 400 in the related art, which is illustrated in
However, the present invention is not limited to the embodiment and various modifications and changes of the present invention can be made and various transformations can be made within the scope of the appended claims.
The illustrated compressor 10 includes the first pump unit 51 and the second pump unit 52, but is not limited thereto and may include one pump unit or three or more pump units. Fans that cool the compressor 10 may be placed such that the number of fans corresponds to the number of pumps. The driving motor of the illustrated compressor 10 is for example, the 5 L-class motor, but is not limited thereto and may adopt for example, a motor suitable for 3 L class and the like. The type of the compressor is not particularly limited and may adopt a predetermined type.
1: Oxygen concentrator
2: Main case
2F: Front panel
2S: Side panel
2R: Rear panel
2D: Top
2B: Bottom
5: Air introduction port
6: Exhaust port
10: Compressor
11: One sleeve
12: The other sleeve
11P, 12P: Piston
13: Radiator
15: conduit
31: First adsorption column body
32: Second adsorption column body
34: First fan
36: Second fan
38: Noise buffer (silencer) also serving as intake filter
40: First connection conduit
42: Second connection conduit
51: First pump unit
52: Second pump unit
Number | Date | Country | Kind |
---|---|---|---|
2009-288266 | Dec 2009 | JP | national |
Filing Document | Filing Date | Country | Kind | 371c Date |
---|---|---|---|---|
PCT/JP2010/006946 | 11/29/2010 | WO | 00 | 8/27/2012 |
Publishing Document | Publishing Date | Country | Kind |
---|---|---|---|
WO2011/074192 | 6/23/2011 | WO | A |
Number | Name | Date | Kind |
---|---|---|---|
4418788 | Gorchev et al. | Dec 1983 | A |
4450933 | Fukuoka et al. | May 1984 | A |
4681099 | Sato et al. | Jul 1987 | A |
5370728 | LaSala et al. | Dec 1994 | A |
5656068 | Smolarek et al. | Aug 1997 | A |
5658371 | Smolarek et al. | Aug 1997 | A |
5858062 | McCulloh et al. | Jan 1999 | A |
6702880 | Roberts et al. | Mar 2004 | B2 |
7279029 | Occhialini et al. | Oct 2007 | B2 |
7455717 | Sprinkle | Nov 2008 | B2 |
7510601 | Whitley et al. | Mar 2009 | B2 |
20090025564 | Kuwabara | Jan 2009 | A1 |
20130008438 | Sugawara et al. | Jan 2013 | A1 |
Number | Date | Country |
---|---|---|
07-310651 | Nov 1995 | JP |
2003-235982 | Aug 2003 | JP |
2005-111016 | Apr 2005 | JP |
2008-144714 | Jun 2008 | JP |
2009-183489 | Aug 2009 | JP |
Entry |
---|
International Search Report (PCT/ISA/210) issued on Feb. 8, 2011, by the Japanese Patent Office as the International Searching Authority for International Application No. PCT/JP2010/006946. |
Office Action dated May 31, 2013, issued by the Taiwanese Patent Office in the corresponding Taiwanese Patent Application No. 099144387. (4 pages). |
Number | Date | Country | |
---|---|---|---|
20120304867 A1 | Dec 2012 | US |