TWI788904B - Gas concentrator - Google Patents

Gas concentrator Download PDF

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TWI788904B
TWI788904B TW110124640A TW110124640A TWI788904B TW I788904 B TWI788904 B TW I788904B TW 110124640 A TW110124640 A TW 110124640A TW 110124640 A TW110124640 A TW 110124640A TW I788904 B TWI788904 B TW I788904B
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gas
outlet
inlet
molecular sieve
way solenoid
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TW110124640A
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TW202302202A (en
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王仁洲
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精俐有限公司
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Priority to CN202210741914.8A priority patent/CN115581992A/en
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/0407Constructional details of adsorbing systems
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • B01D53/047Pressure swing adsorption
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02Preparation of oxygen
    • C01B13/0229Purification or separation processes
    • C01B13/0248Physical processing only
    • C01B13/0259Physical processing only by adsorption on solids
    • C01B13/0262Physical processing only by adsorption on solids characterised by the adsorbent
    • C01B13/027Zeolites
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02Preparation of oxygen
    • C01B13/0229Purification or separation processes
    • C01B13/0248Physical processing only
    • C01B13/0259Physical processing only by adsorption on solids
    • C01B13/0262Physical processing only by adsorption on solids characterised by the adsorbent
    • C01B13/0274Other molecular sieve materials
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E60/00Enabling technologies; Technologies with a potential or indirect contribution to GHG emissions mitigation
    • Y02E60/30Hydrogen technology
    • Y02E60/36Hydrogen production from non-carbon containing sources, e.g. by water electrolysis

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  • Chemical & Material Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Organic Chemistry (AREA)
  • Engineering & Computer Science (AREA)
  • Inorganic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • General Chemical & Material Sciences (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • General Life Sciences & Earth Sciences (AREA)
  • Geology (AREA)
  • Materials Engineering (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Gas Separation By Absorption (AREA)
  • Separation Of Gases By Adsorption (AREA)

Abstract

A gas concentrator including at least one gas concentrating module is provided. The gas concentrating module includes a body filled with molecular sieve materials, a pipeline connector, and at least one control valve. The body has a first end and a second end opposite to each other, and the pipeline connector located at the first end has an inlet, a first outlet, and a second outlet. The control valve is located between the first end and the pipeline connector to open or close at least one of the inlet, the first outlet, and the second outlet. A first gas is injected into the body via the inlet, and is filtered with the molecular sieve materials to retain and separate a second gas and a third gas.

Description

氣體濃縮裝置Gas Concentrator

本發明是有關於一種氣體濃縮裝置。The invention relates to a gas enrichment device.

製氧機是一種常見的醫療設備,目前常規的醫用製氧設備按其原理可以分為兩類:其一是通過電解水製造氧氣,而另一則是利用分子篩吸附並分離空氣以汲取氧,也就是變壓吸附(Pressure Swing Adsorption,PSA)。前者以電解水製氧的方式具有成本低,噪音低,氧濃度高等優點,但卻容易產生安全性疑慮。後者雖然以分子篩過濾的理論最高濃度僅為96%,但其設備簡單,安全性高,同時製氧濃度已能滿足大多數醫學臨床的用氧需求,故而成為目前用於患者缺氧預防和治療的主要方式。Oxygen concentrator is a common medical equipment. At present, conventional medical oxygen concentrators can be divided into two categories according to their principles: one is to produce oxygen through electrolysis of water, and the other is to use molecular sieves to absorb and separate air to absorb oxygen. That is pressure swing adsorption (Pressure Swing Adsorption, PSA). The former method of electrolyzing water to produce oxygen has the advantages of low cost, low noise, and high oxygen concentration, but it is prone to safety concerns. Although the theoretical maximum concentration of the latter filtered by molecular sieve is only 96%, its equipment is simple and safe, and the concentration of oxygen production can meet the oxygen demand of most medical clinics, so it is currently used for the prevention and treatment of hypoxia in patients. main way.

雖然前述採用變壓吸附手段的製氧設備簡單而具備容易攜行的特性,但現有設備仍受限於構件組裝及管路配置,其中緣由即在於,習知之製氧機大多是採用現成之零組件加以組裝而成,因此造成結構鬆散且組裝空間龐大,如此反而導致攜行不易而有違前述特性,同時也造成使用者在進行更換或維修的不便與困難度。Although the aforementioned oxygen generators using pressure swing adsorption are simple and easy to carry, the existing equipment is still limited by component assembly and pipeline configuration. The components are assembled, so the structure is loose and the assembly space is huge, which makes it difficult to carry and violates the above-mentioned characteristics, and also causes inconvenience and difficulty for users to replace or maintain.

本發明提供一種氣體濃縮裝置,其以簡單結構配置而具備能毋須工具即能進行快速拆裝的特性。The invention provides a gas enrichment device, which is configured with a simple structure and has the characteristic of quick disassembly and assembly without tools.

本發明的氣體濃縮裝置,包括至少一氣體濃縮模組。氣體濃縮模組包括本體、管路接頭以及至少一控制閥。本體填充分子篩濾材,且本體具有彼此相對的第一端與第二端。管路接頭位於第一端。管路接頭具有入口、第一出口與第二出口。控制閥位於第一端與管路接頭之間並控制入口、第一出口與第二出口的至少其一的啟閉。第一氣體是於通過入口進入本體,並以分子篩濾材過濾第一氣體而分離出第二氣體與第三氣體。The gas enrichment device of the present invention includes at least one gas enrichment module. The gas enrichment module includes a body, a pipeline connector and at least one control valve. The body is filled with molecular sieve filter material, and the body has a first end and a second end opposite to each other. A tubing connector is located at the first end. The pipeline joint has an inlet, a first outlet and a second outlet. The control valve is located between the first end and the pipeline joint and controls opening and closing of at least one of the inlet, the first outlet and the second outlet. The first gas enters the body through the inlet, and the molecular sieve filter material is used to filter the first gas to separate the second gas and the third gas.

在本發明的一實施例中,上述的控制閥是二位三通電磁閥。氣體濃縮裝置還包括控制模組,電性連接二位三通電磁閥。第一氣體為空氣,第二氣體為氧氣,第三氣體為氮氣。控制模組驅動二位三通電磁閥以開啟入口以及控制第一出口與第二出口啟閉,以使第一氣體經由入口進入本體並被分子篩濾材過濾而分離出第二氣體與第三氣體,並經由該第一出口將第二氣體排出本體,其中控制模組驅動二位三通電磁閥關閉入口與第一出口且開啟第二出口,以經由第二出口將第三氣體排出本體。In an embodiment of the present invention, the above-mentioned control valve is a two-position three-way solenoid valve. The gas enrichment device also includes a control module, which is electrically connected to the two-position three-way solenoid valve. The first gas is air, the second gas is oxygen, and the third gas is nitrogen. The control module drives the two-position three-way solenoid valve to open the inlet and controls the opening and closing of the first outlet and the second outlet, so that the first gas enters the body through the inlet and is filtered by the molecular sieve filter material to separate the second gas and the third gas, And discharge the second gas out of the body through the first outlet, wherein the control module drives the two-position three-way solenoid valve to close the inlet and the first outlet and open the second outlet to discharge the third gas out of the body through the second outlet.

在本發明的一實施例中,上述的至少一控制閥包括二通電磁閥與開關。二通電磁閥連接並控制入口與第二出口的啟閉,開關連接並控制第一出口的啟閉。氣體濃縮裝置還包括控制模組,分別電性連接二通電磁閥與開關。第一氣體為空氣,第二氣體為氧氣,第三氣體為氮氣。控制模組驅動二通電磁閥開啟入口且關閉第二出口,且控制模組驅動開關開啟第一出口,以使第一氣體經由入口進入本體並被分子篩濾材過濾而分離出第二氣體與第三氣體,以經由第一出口將第二氣體排出本體。控制模組驅動二通電磁閥開啟第二出口,且關閉入口及第一出口,以經由第二出口將第三氣體排出本體。In an embodiment of the present invention, the above-mentioned at least one control valve includes a two-way solenoid valve and a switch. The two-way solenoid valve is connected and controls the opening and closing of the inlet and the second outlet, and the switch is connected and controls the opening and closing of the first outlet. The gas enrichment device also includes a control module, which is electrically connected to the two-way solenoid valve and the switch respectively. The first gas is air, the second gas is oxygen, and the third gas is nitrogen. The control module drives the two-way solenoid valve to open the inlet and close the second outlet, and the control module drives the switch to open the first outlet, so that the first gas enters the body through the inlet and is filtered by the molecular sieve filter material to separate the second gas and the third gas. gas to discharge the second gas out of the body through the first outlet. The control module drives the two-way solenoid valve to open the second outlet, and close the inlet and the first outlet, so as to discharge the third gas out of the body through the second outlet.

在本發明的一實施例中,上述經由第一出口將第二氣體排出本體,也經由第二出口將第三氣體排出本體。In an embodiment of the present invention, the above-mentioned second gas is discharged from the body through the first outlet, and the third gas is also discharged from the body through the second outlet.

在本發明的一實施例中,上述的氣體濃縮裝置還包括導管,設置於本體內。導管連接位於第一端的第一出口並延伸至第二端。第二氣體從第二端進入導管,並經由第一出口排出本體。In an embodiment of the present invention, the above-mentioned gas concentrator further includes a conduit disposed in the body. A conduit is connected to the first outlet at the first end and extends to the second end. The second gas enters the conduit from the second end and exits the body through the first outlet.

在本發明的一實施例中,上述的分子篩濾材包括依序從第一端層疊至第二端的多個網片,上述的導管穿過這些網片。In an embodiment of the present invention, the above-mentioned molecular sieve filter material includes a plurality of mesh sheets stacked sequentially from the first end to the second end, and the above-mentioned conduit passes through these mesh sheets.

在本發明的一實施例中,上述的氣體濃縮模組還包括彈性件,抵接在位於第二端的網片與本體之間,抵接彈性件的網片是這些網片的最末者。In an embodiment of the present invention, the above-mentioned gas concentration module further includes an elastic member abutting between the mesh at the second end and the body, and the mesh abutting the elastic member is the last of the meshes.

在本發明的一實施例中,上述的氣體濃縮裝置包括多個氣體濃縮模組,且這些氣體濃縮模組的多個管路接頭為一體式結構。In an embodiment of the present invention, the above-mentioned gas enrichment device includes a plurality of gas enrichment modules, and the plurality of pipeline joints of the gas enrichment modules are of an integrated structure.

在本發明的一實施例中,上述的氣體濃縮裝置還包括空壓機,連接至少一上述氣體濃縮模組的入口,以加壓並傳送第一氣體經由入口進入本體。In an embodiment of the present invention, the above-mentioned gas enrichment device further includes an air compressor connected to the inlet of at least one of the above-mentioned gas enrichment modules, so as to pressurize and deliver the first gas into the main body through the inlet.

在本發明的一實施例中,上述的氣體濃縮裝置還包括空壓機,連接至少一上述氣體濃縮模組的第二出口,以經由第二出口從本體抽出第三氣體。In an embodiment of the present invention, the above-mentioned gas enrichment device further includes an air compressor connected to the second outlet of at least one of the above-mentioned gas enrichment modules, so as to extract the third gas from the main body through the second outlet.

在本發明的一實施例中,上述的氧濃縮裝置還包括貯存罐,連接至少一上述氣體濃縮模組的第一出口,以收集第二氣體。In an embodiment of the present invention, the above-mentioned oxygen concentrator further includes a storage tank connected to the first outlet of at least one of the above-mentioned gas concentration modules to collect the second gas.

在本發明的一實施例中,上述的氧濃縮裝置還包括貯存罐,連接至少一上述氣體濃縮模組的第二出口,以收集第三氣體In an embodiment of the present invention, the above-mentioned oxygen enrichment device further includes a storage tank connected to the second outlet of at least one of the above-mentioned gas enrichment modules to collect the third gas

基於上述,本發明的氣體濃縮裝置包括至少一氣體濃縮模組,而氣體濃縮模組藉由在本體內填充分子篩濾材後,將管路接頭組裝於本體的第一端,以讓管路接頭的入口、第一出口與第二出口與本體的內部空間連通,進而將控制閥設置於第一端與管路接頭之間時,得以控制上述入口、第一出口與第二出口的至少其一的啟閉,其中第一氣體適於從管路接頭的入口進入本體,並以分子篩濾材過濾且分離出第二氣體與第三氣體。如此一來,氣體濃縮模組便能統一調控同位於第一端的管路接頭,以讓上述氣體皆是從本體的第一端進出,而據以達到結構簡化的效果。Based on the above, the gas concentrating device of the present invention includes at least one gas concentrating module, and the gas concentrating module assembles the pipeline joint on the first end of the main body after filling the molecular sieve filter material in the main body, so that the pipeline joint The inlet, the first outlet, and the second outlet communicate with the inner space of the body, and when the control valve is arranged between the first end and the pipe joint, at least one of the inlet, the first outlet, and the second outlet can be controlled. Opening and closing, wherein the first gas is suitable to enter the body from the inlet of the pipeline joint, and is filtered by molecular sieve filter material to separate the second gas and the third gas. In this way, the gas enrichment module can uniformly regulate the pipeline joints located at the first end, so that the above-mentioned gases all enter and exit from the first end of the main body, thereby achieving the effect of structural simplification.

圖1是依據本發明一實施例的氣體濃縮裝置的示意圖。圖2是圖1的氣體濃縮裝置的部分構件爆炸圖。請同時參考圖1與圖2,在本實施例中,氣體濃縮裝置100包括設置在殼體內的本體110A、110B、管路接頭120A、120B以及控制閥130A、130B。在此,本體110A、110B具有相同結構,管路接頭120A、120B具有相同結構,且控制閥130A、130B具有相同結構,因此後續(包含圖2所示)將以本體110A、管路結構120A與控制閥130A作為例示進行描述。也就是說,本實施例雖以兩組相同結構形成的氧濃縮裝置100作為例示,但因其作動原理相同,因此在另一未繪示的實施例中,僅以單一組件,例如本體110A、管路接頭120A與控制閥130A,也能達到相同效果。簡而言之,本實施例的氣體濃縮裝置100是由兩個氣體濃縮模組G1、G2組成,其中氣體濃縮模組G1包括本體110A、管路接頭120A與控制閥130A,氣體濃縮模組G2包括本體110B、管路接頭120B與控制閥130B,因氣體濃縮模組G1、G2各自具有相同的構件組成,故而具備同樣的氣體濃縮能力,後續會有進一步描述。FIG. 1 is a schematic diagram of a gas enrichment device according to an embodiment of the present invention. Fig. 2 is an exploded view of some components of the gas enrichment device in Fig. 1 . Please refer to FIG. 1 and FIG. 2 at the same time. In this embodiment, the gas concentrator 100 includes main bodies 110A, 110B, pipeline connectors 120A, 120B, and control valves 130A, 130B disposed in the housing. Here, the main bodies 110A and 110B have the same structure, the pipeline joints 120A and 120B have the same structure, and the control valves 130A and 130B have the same structure, so the following (including those shown in FIG. 2 ) will use the main body 110A, the pipeline structure 120A and The control valve 130A is described as an example. That is to say, although this embodiment takes two groups of oxygen concentrators 100 formed with the same structure as an example, but because of the same operating principle, in another unillustrated embodiment, only a single component, such as the main body 110A, The pipeline joint 120A and the control valve 130A can also achieve the same effect. In short, the gas enrichment device 100 of this embodiment is composed of two gas enrichment modules G1 and G2, wherein the gas enrichment module G1 includes a main body 110A, a pipeline connector 120A and a control valve 130A, and the gas enrichment module G2 Including the main body 110B, the pipeline connector 120B and the control valve 130B, the gas enrichment modules G1 and G2 have the same component composition and therefore have the same gas enrichment capability, which will be further described later.

如圖2所繪示本體110A的爆炸圖(本體110B的爆炸圖也是相同),本體110A包括頂蓋111、底蓋113、柱形壁112、導管114、以分子篩濾材115製成的多個網片(各網片具有如圖所示的多個篩孔)、彈性件116以及多個密封件117A、117B、117C與117D,其中頂蓋111組裝至柱形壁112並以密封件117B夾持其間,且形成本體110A的第一端N1,底蓋113組裝至柱形壁112並以密封件117A夾持其間,且形成本體110A的第二端N2。如此一來,由頂蓋111、柱形壁112、底蓋113以及密封件117A、117B便構成用以容置多個層疊網片的空間,相當於將分子篩濾材115填充於本體110A之內。為利於辨識,在此僅繪示部分分子篩濾材115。As shown in Figure 2, the exploded view of the main body 110A (the exploded view of the main body 110B is also the same), the main body 110A includes a top cover 111, a bottom cover 113, a cylindrical wall 112, a conduit 114, and a plurality of nets made of molecular sieve filter materials 115 sheet (each mesh sheet has a plurality of meshes as shown), an elastic member 116, and a plurality of seals 117A, 117B, 117C, and 117D, wherein the top cover 111 is assembled to the cylindrical wall 112 and clamped by the seal 117B In between, and form the first end N1 of the body 110A, the bottom cover 113 is assembled to the cylindrical wall 112 and sandwiched by the sealing member 117A, and forms the second end N2 of the body 110A. In this way, the top cover 111 , the cylindrical wall 112 , the bottom cover 113 and the seals 117A, 117B form a space for accommodating multiple laminated mesh sheets, which is equivalent to filling the molecular sieve filter material 115 in the main body 110A. For ease of identification, only part of the molecular sieve filter material 115 is shown here.

圖3是圖1的氣體濃縮裝置的部分構件剖視圖。請同時參考圖2與圖3,在本實施例中,導管114設置於本體110A內,且如圖3所示,導管114的一端連接頂蓋111,並以密封件117C密封其間,導管114的另一端延伸至本體110A的第二端N2。如圖3所示,頂蓋111與底蓋113分別螺接在柱形壁112的相對兩端而形成前述第一端N1與第二端N2。彈性件116抵接位於第二端N2的網片與本體110A之間,也就是抵接該彈性件116的網片是該些網片的最末者,進而在彈性件116的彈力驅使之下,使這些網片能彼此抵緊,同時,彈性件116還讓前述最末者的該網片與底蓋113之間存在空間,而前述導管114延伸至第二端N2的開口便位於所述空間中。Fig. 3 is a cross-sectional view of some components of the gas concentrator in Fig. 1 . Please refer to FIG. 2 and FIG. 3 at the same time. In this embodiment, the conduit 114 is arranged in the body 110A, and as shown in FIG. The other end extends to the second end N2 of the body 110A. As shown in FIG. 3 , the top cover 111 and the bottom cover 113 are respectively screwed to opposite ends of the cylindrical wall 112 to form the aforementioned first end N1 and second end N2 . The elastic member 116 abuts between the mesh at the second end N2 and the body 110A, that is, the mesh abutting the elastic member 116 is the last of the meshes, and driven by the elastic force of the elastic member 116 , so that these nets can be pressed against each other, and at the same time, the elastic member 116 also allows a space to exist between the aforementioned last net and the bottom cover 113, and the opening of the aforementioned conduit 114 extending to the second end N2 is located at the in space.

再者,管路接頭120A組裝於本體110A的第一端N1(管路接頭120B組裝於本體110B的第一端N1)。在本實施例中,管路接頭120A、120B各具有入口E1、第一出口E2與第二出口E3。在此,控制閥130A、130B例如是二位三通電磁閥,控制閥130A組裝於管路接頭120A(控制閥130B組裝於管路接頭120B)並控制入口E1、第一出口E2與第二出口E3的啟閉。第一氣體適於從入口E1進入本體110A後,經由分子篩濾材115過濾並分離出第二氣體與第三氣體。在此,第一氣體是空氣Air,第二氣體是氧氣O 2,第三氣體是氮氣N 2。同樣的氣體過濾分離動作也發生於另一氣體濃縮模組G2中。可預知地,在其他未繪示的實施例中,本領域的技術人員可通過不同種類的分子篩濾材而使本實施例的氣體過濾裝置對不同氣體進行過濾分離。 Furthermore, the pipeline connector 120A is assembled on the first end N1 of the body 110A (the pipeline connector 120B is assembled on the first end N1 of the body 110B). In this embodiment, each of the pipeline connectors 120A, 120B has an inlet E1 , a first outlet E2 and a second outlet E3 . Here, the control valves 130A and 130B are, for example, two-position three-way solenoid valves. The control valve 130A is assembled on the pipeline joint 120A (the control valve 130B is assembled on the pipeline joint 120B) and controls the inlet E1, the first outlet E2 and the second outlet. The opening and closing of E3. After the first gas enters the main body 110A from the inlet E1, it is filtered through the molecular sieve filter material 115 to separate the second gas and the third gas. Here, the first gas is air Air, the second gas is oxygen O 2 , and the third gas is nitrogen N 2 . The same gas filtration and separation action also occurs in another gas concentration module G2. Predictably, in other unillustrated embodiments, those skilled in the art can use different types of molecular sieve filter materials to make the gas filter device of this embodiment filter and separate different gases.

進一步地說,在製造氧氣(第二氣體)的過程中,入口E1與第一出口E2受控而被開啟,第二出口E3受控而被關閉,以讓第一氣體(空氣)流入本體110A(本體110B亦同,不再贅述),而讓分子篩濾材115將空氣篩離出的氧氣能從第一出口E2流出。在排氮過程中,與前述相反,也就是入口E1與第一出口E2受控而被關閉,第二出口E3受控而被開啟。Furthermore, during the process of producing oxygen (second gas), the inlet E1 and the first outlet E2 are controlled to be opened, and the second outlet E3 is controlled to be closed, so that the first gas (air) flows into the main body 110A (The same is true for the main body 110B, which will not be described again), and the oxygen sieved out by the molecular sieve filter material 115 can flow out from the first outlet E2. In the nitrogen exhaust process, contrary to the above, that is, the inlet E1 and the first outlet E2 are controlled to be closed, and the second outlet E3 is controlled to be opened.

請再參考圖1與圖3,在另一未繪示的實施例中,上述控制閥130A或130B也可改以二通電磁閥與開關替代,其中二通電磁閥連接並控制入口E1與第二出口E3的啟閉,而開關連接並控制第一出口E2的啟閉。換句話說,如圖3所示用以讓第二氣體(氧氣O 2)排出本體110A的管路接頭120A的獨立結構特徵,其可以開關作為獨立出口的啟閉之用。此舉讓本實施也能維持上述「氣體壓力需維持一定數值以上」的狀態,以利於第一氣體在本體110A內的過濾分離作用。還需提及的是,本實施例也因控制閥分置為二通電磁閥與開關,故而本體110A內的第一氣體完成被過濾分離出第二氣體與第三氣體後,能分別受二通電磁閥與開關的控制,經由第一出口E2將第二氣體排出本體110A的同時,也經由第二出口E3將第三氣體排出本體110A。 Please refer to FIG. 1 and FIG. 3 again. In another not-shown embodiment, the above-mentioned control valve 130A or 130B can also be replaced by a two-way solenoid valve and a switch, wherein the two-way solenoid valve is connected and controls the inlet E1 and the first The opening and closing of the second exit E3, and the switch is connected to and controls the opening and closing of the first exit E2. In other words, as shown in FIG. 3 , the independent structural feature of the pipeline connector 120A for allowing the second gas (oxygen O 2 ) to exit the main body 110A can be opened and closed as an independent outlet. This allows this implementation to maintain the above-mentioned state of "the gas pressure must be maintained above a certain value", so as to facilitate the filtration and separation of the first gas in the main body 110A. It should also be mentioned that in this embodiment, the control valve is divided into a two-way solenoid valve and a switch, so the first gas in the main body 110A is filtered and separated to separate the second gas and the third gas, which can be respectively subjected to the second gas and the third gas. Through the control of the solenoid valve and the switch, while the second gas is discharged from the main body 110A through the first outlet E2, the third gas is also discharged from the main body 110A through the second outlet E3.

此外,如圖1所示,氣體濃縮裝置100還包括貯存罐140與空壓機150,其中貯存罐140連接第一出口E2,以收集從本體110A、110B排出的第二氣體,而空壓機150連接入口E1與第二出口E3,其中空壓機150用以將外部環境的空氣予以壓縮並經由入口E1送入本體110A、110B,或空壓機150用以對本體110A、110B進行抽取第三氣體,以將殘留在分子篩濾材115的第三氣體從本體110A、110B抽出。在另一未繪示的實施例中,也可以另一貯存罐連接第二出口E3,以收集第三氣體。進一步地說,當進行前述製氧過程時,也就是入口E1與第一出口E2被開啟,第二出口E3被關閉時,從空壓機150提供的高壓空氣便能經由入口E1進入本體110A,氧氣被分子篩濾材115分離出並經由第一出口E2進入貯存罐140。在此,本實施例還包括調壓閥,用以限定氧氣需在特定壓力才能通過,因此能讓本體110A內形成正壓,以提高分子篩濾材115的分離效果。對應地,當入口E1與第一出口E2被關閉,而第二出口E3被開啟時,本體110A的壓力會降低,而讓氮氣得以經由第二出口E3離開,或以空壓機150強制從本體110A將氮氣抽出,同時此舉還能讓本體110A內形成負壓,而有利於下一次的製氧過程(因壓差而縮短氧氣製造時間,以提高製氧效率)。In addition, as shown in Figure 1, the gas enrichment device 100 also includes a storage tank 140 and an air compressor 150, wherein the storage tank 140 is connected to the first outlet E2 to collect the second gas discharged from the main body 110A, 110B, and the air compressor 150 connects the inlet E1 and the second outlet E3, wherein the air compressor 150 is used to compress the air in the external environment and send it into the main body 110A, 110B through the inlet E1, or the air compressor 150 is used to extract the main body 110A, 110B for the second time. Three gas, to extract the third gas remaining in the molecular sieve filter material 115 from the main body 110A, 110B. In another unillustrated embodiment, another storage tank can also be connected to the second outlet E3 to collect the third gas. Furthermore, when the aforementioned oxygen production process is performed, that is, when the inlet E1 and the first outlet E2 are opened, and the second outlet E3 is closed, the high-pressure air provided from the air compressor 150 can enter the main body 110A through the inlet E1, The oxygen is separated by the molecular sieve filter material 115 and enters the storage tank 140 through the first outlet E2. Here, this embodiment also includes a pressure regulating valve, which is used to limit the oxygen to pass through at a specific pressure, so that a positive pressure can be formed in the main body 110A to improve the separation effect of the molecular sieve filter material 115 . Correspondingly, when the inlet E1 and the first outlet E2 are closed, and the second outlet E3 is opened, the pressure of the main body 110A will decrease, allowing nitrogen to leave through the second outlet E3, or the air compressor 150 is used to force nitrogen gas from the main body 110A. 110A pumps out the nitrogen gas, and at the same time, it can also form a negative pressure in the body 110A, which is beneficial to the next oxygen production process (the oxygen production time is shortened due to the pressure difference, so as to improve the oxygen production efficiency).

圖4是圖1的氣體濃縮裝置電性關係圖。請同時參考圖2至圖4,氣體濃縮裝置100還包括控制模組160,其電性連接控制閥130A、130B(二位三通電磁閥)與空壓機150,也如上述另一實施例而電性連接二通電磁閥與開關,以利於進行相關作業,如後述。FIG. 4 is an electrical relationship diagram of the gas concentrator in FIG. 1 . Please refer to FIGS. 2 to 4 at the same time. The gas enrichment device 100 also includes a control module 160, which is electrically connected to the control valves 130A, 130B (two-position three-way solenoid valve) and the air compressor 150, as in the other embodiment described above. The two-way solenoid valve and the switch are electrically connected to facilitate related operations, as described later.

以例如是二位三通電磁閥的控制閥130A、130B為例,當控制閥130A、130B受控於控制模組160而開啟入口E1及第一出口E2,並關閉第二出口E3時,第一氣體(空氣Air)通過入口E1進入本體110A、110B(且如前述是經由空壓機150壓縮後的空氣),並以分子篩濾材115過濾而保留氧。如圖3所示,壓縮後的空氣從第一端N1進入本體110A、110B後,便會由上而下地依序通過這些由分子篩濾材115製成的網片,以讓這些網片逐層地將空氣中的氮吸附,故而空氣中的氧便會因此被壓制且傳送至本體110B的第二端N2,而在經過這些網片的最末者而進入導管114的開口所在的空間時,便能讓氧順利地進入導管114。此時由於第二出口E3保持關閉狀態,故能有效維持本體110A內的壓力而確保過濾分離過持的進行。當第二氣體(氧氣O 2)以通過導管114與第一出口E2排出本體110A、110B,且因此被傳送並收集至貯存罐140,這即是氣體濃縮裝置100的製氧模式。相對地,當控制閥130A、130B關閉入口E1、第一出口E2並開啟第二出口E3時,於前述製氧的過程中受分子篩濾材115吸附且阻滯的第三氣體(氮氣N 2)便能因空壓機150的抽取,而經由第二出口E3排出本體110A、110B,此即氣體濃縮裝置100的排氮模式。 Take the control valves 130A and 130B such as two-position three-way solenoid valves as an example. When the control valves 130A and 130B are controlled by the control module 160 to open the inlet E1 and the first outlet E2 and close the second outlet E3, the second A gas (air Air) enters the main body 110A, 110B through the inlet E1 (and is air compressed by the air compressor 150 as mentioned above), and is filtered by the molecular sieve filter material 115 to retain oxygen. As shown in Figure 3, after the compressed air enters the main body 110A, 110B from the first end N1, it will pass through these mesh sheets made of molecular sieve filter material 115 sequentially from top to bottom, so that these mesh sheets Adsorb the nitrogen in the air, so the oxygen in the air will be suppressed and sent to the second end N2 of the body 110B, and when entering the space where the opening of the conduit 114 passes through the last of these meshes, it will be Oxygen can enter the conduit 114 smoothly. At this time, since the second outlet E3 remains closed, the pressure in the main body 110A can be effectively maintained to ensure the filtration and separation. When the second gas (oxygen O 2 ) exits the bodies 110A, 110B through the conduit 114 and the first outlet E2 , and thus is sent and collected to the storage tank 140 , this is the oxygen production mode of the gas concentrator 100 . In contrast, when the control valves 130A and 130B close the inlet E1 and the first outlet E2 and open the second outlet E3, the third gas (nitrogen N 2 ) adsorbed and blocked by the molecular sieve filter material 115 during the aforementioned oxygen production process will be The main bodies 110A, 110B can be discharged through the second outlet E3 due to the suction of the air compressor 150 , which is the nitrogen exhaust mode of the gas concentrator 100 .

基於上述,由於管路接頭120A、120B的入口E1、第一出口E2與第二出口E3同位於本體110A、110B的第一端N1,因此能有效簡化氣體濃縮裝置100的結構組成,也就是相當於氣體的進出皆在第一端N1,故而本體110A、110B可從第二端N2進行維修拆裝而不致影響管路結構120A、120B與控制閥130A、130B。再者,由於頂蓋111與底蓋113皆是以螺接結構而與柱形壁112結合,此舉也便於使用者對於本體110A、110B的拆裝作業。換句話說,本發明有效地簡化氣體濃縮裝置100的拆裝機制,使用者毋須具備特殊工業技能即能順利地進行拆裝,也因此間接地提高養濃度裝置100在消費市場的應用程度。Based on the above, since the inlet E1, the first outlet E2 and the second outlet E3 of the pipeline joints 120A, 120B are located at the first end N1 of the main body 110A, 110B, the structure of the gas concentrator 100 can be effectively simplified, that is, the Since the gas enters and exits at the first end N1, the main bodies 110A, 110B can be maintained and disassembled from the second end N2 without affecting the pipeline structures 120A, 120B and the control valves 130A, 130B. Moreover, since the top cover 111 and the bottom cover 113 are combined with the cylindrical wall 112 by a screw connection structure, it is also convenient for the user to disassemble and assemble the main bodies 110A and 110B. In other words, the present invention effectively simplifies the assembly and disassembly mechanism of the gas concentration device 100 , and the user does not need to have special industrial skills to disassemble and assemble smoothly, thus indirectly improving the application degree of the nutrient concentration device 100 in the consumer market.

圖5是圖1的氣體濃縮裝置的作動關係示意圖。請參考圖5,在此要說明的作動狀態僅為例示。如本實施例在前述所示,氣體濃縮機構100的本體110A、110B,管路接頭120A、120B與控制閥130A、130B皆是具有相同結構,因此可依據需求而對應調整不同的模式。如圖5所示,氧濃縮裝置100可進一步分隔為兩個氣體濃縮模組G1、G2,使用者便能通過控制模組160而對氣體濃縮模組G1、G2下達相同或不同的指令。FIG. 5 is a schematic diagram of the operation relationship of the gas enrichment device in FIG. 1 . Please refer to FIG. 5 , the actuation state to be described here is only an example. As shown above in this embodiment, the main bodies 110A, 110B, the pipeline connectors 120A, 120B and the control valves 130A, 130B of the gas concentrating mechanism 100 all have the same structure, so different modes can be adjusted accordingly according to requirements. As shown in FIG. 5 , the oxygen enrichment device 100 can be further divided into two gas enrichment modules G1 and G2 , and the user can issue the same or different commands to the gas enrichment modules G1 and G2 through the control module 160 .

舉例來說,控制模組160傳送指令至控制閥130A而讓氣體濃縮模組G1處於製氧模式,同時,控制模組160傳送指令至控制閥130B而讓氣體濃縮模組G2處於排氮模式。據此,便能產生交替作動的狀態,且能隨時依據需求而加以改變(在製氧模式與排氮模式之間進行切換),進而提高氧濃縮裝置100的工作效率。類似地,當氧濃縮裝置包括多個氣體濃縮模組時,即能依據需求而提供使用者更有效率的製氧需求。如上述控制閥包括二通電磁閥與開關的實施例,除了在單一氣體濃縮模組G1或G2能使控制模組160分別對管路接頭控制而達到所需的啟閉效果外,也能如上述控制多個氣體濃縮模組,進而使氣體濃縮裝置能有多種驅動模式。For example, the control module 160 sends a command to the control valve 130A to make the gas enrichment module G1 in the oxygen generation mode, and at the same time, the control module 160 sends a command to the control valve 130B to make the gas enrichment module G2 in the nitrogen exhaust mode. Accordingly, the alternate operation state can be generated and can be changed according to the demand at any time (switching between the oxygen generating mode and the nitrogen exhausting mode), thereby improving the working efficiency of the oxygen concentrator 100 . Similarly, when the oxygen enrichment device includes multiple gas enrichment modules, it can provide users with more efficient oxygen production requirements according to their needs. As in the above-mentioned embodiment where the control valve includes a two-way solenoid valve and a switch, in addition to enabling the control module 160 to control the pipeline joints to achieve the required opening and closing effect in the single gas enrichment module G1 or G2, it can also be used as The above control of multiple gas enrichment modules enables the gas enrichment device to have multiple driving modes.

圖6是本發明另一實施例的氣體濃縮裝置的部分結構示意圖。請參考圖6,與前述實施例相同的是,氣體濃縮裝置同樣包括兩個氣體濃縮模組G1、G2,而不同的是,這兩個氣體濃縮模組G1、G2的管路接頭是採一體式結構,也就是分屬不同氣體濃縮模組G1、G2的入口E1、第一出口E2與第二出口E3是以整合結構體223而形成一體式結構,有利於提高結構強度,且也方便使用者拆裝本體110A、110B。Fig. 6 is a partial structural schematic diagram of a gas enrichment device according to another embodiment of the present invention. Please refer to Fig. 6, the same as the previous embodiment, the gas enrichment device also includes two gas enrichment modules G1, G2, but the difference is that the pipeline joints of the two gas enrichment modules G1, G2 are integrated In other words, the inlet E1, the first outlet E2, and the second outlet E3 belonging to different gas enrichment modules G1 and G2 form an integrated structure by integrating the structure 223, which is conducive to improving the structural strength and is also convenient to use. The user disassembles and assembles the main bodies 110A, 110B.

綜上所述,在本發明的上述實施例中,藉由在本體內填充分子篩濾材後,將管路接頭組裝於本體的第一端,以讓管路接頭的入口、第一出口與第二出口與本體的內部空間連通,進而在將控制閥組裝於管路接頭與第一端之間時,便得以控制上述入口、第一出口與第二出口的啟閉。如此一來,當入口開啟而第一出口、第二出口關閉時,第一氣體即能經由入口進入本體,以利於分子篩濾材將第一氣體分離為第二氣體與第三氣體,並在第一出口或第二出口開啟時,讓第二氣體經由第一出口排出本體,或讓第三氣體經由第二出口排出本體。To sum up, in the above-mentioned embodiment of the present invention, after filling the molecular sieve filter material in the main body, the pipeline joint is assembled on the first end of the main body, so that the inlet of the pipeline joint, the first outlet and the second The outlet communicates with the inner space of the body, and then when the control valve is assembled between the pipe joint and the first end, the opening and closing of the above-mentioned inlet, the first outlet and the second outlet can be controlled. In this way, when the inlet is opened and the first outlet and the second outlet are closed, the first gas can enter the body through the inlet, so that the molecular sieve filter material can separate the first gas into the second gas and the third gas, When the outlet or the second outlet is opened, the second gas is discharged from the body through the first outlet, or the third gas is discharged from the body through the second outlet.

再者,控制閥可依據管路接頭的結構型式而選用二位三通電磁閥對上述三個出入口(入口、第一出口與第二出口)進行啟閉控制,或以二通電磁閥搭配開關分別對上述三個出入口進行啟閉控制。無論選用何者,皆能確保在進行氣體過濾分離的過程中,以利於讓本體內的氣體壓力達一定值以上而得以使氣體過濾分離的過程順利進行。一旦完成氣體過濾分離後,即能分別開啟第一出口與第二出口,而將所需的第二氣體、第三氣體排出本體並進行收集。Furthermore, the control valve can use a two-position three-way solenoid valve to control the opening and closing of the above three inlets (inlet, first outlet, and second outlet) according to the structure of the pipe joint, or use a two-way solenoid valve with a switch Control the opening and closing of the above three entrances and exits respectively. No matter which one is selected, it can be ensured that in the process of gas filtration and separation, the gas pressure in the main body can reach a certain value, so that the process of gas filtration and separation can be carried out smoothly. Once the gas filtration and separation is completed, the first outlet and the second outlet can be respectively opened to discharge the required second gas and third gas out of the body and collect them.

上述設置有效簡化氣體濃縮裝置的結構組成,也就是相當於氣體的進出皆在第一端,故而本體可從第二端進行維修拆裝而不致影響管路結構與電磁閥。再者,由於頂蓋與底蓋皆是以螺接結構而與柱形壁結合,此舉也便於使用者對於本體的拆裝作業。 此外,氣體濃縮裝置還能藉由設置氣體濃縮模組,並藉由控制模組的調整而讓這些氣體濃縮模組各自依據需求而切換至不同工作模式,進而提高氣體濃縮裝置的作動效率。 The above arrangement effectively simplifies the structure of the gas concentrator, that is, the gas enters and exits at the first end, so the main body can be repaired and disassembled from the second end without affecting the pipeline structure and solenoid valve. Furthermore, since the top cover and the bottom cover are combined with the cylindrical wall through a screw connection structure, it is also convenient for the user to disassemble and assemble the main body. In addition, the gas enrichment device can also be equipped with gas enrichment modules, and through the adjustment of the control modules, these gas enrichment modules can be switched to different working modes according to requirements, thereby improving the operating efficiency of the gas enrichment device.

100:氣體濃縮裝置 110A、110B:本體 111:頂蓋 112:柱形壁 113:底蓋 114:導管 115:分子篩濾材 116:彈性件 117A、117B、117C、117D:密封件 120A、120B:管路接頭 130A、130B:控制閥 140:貯存罐 150:空壓機 160:控制模組 223:整合結構體 E1:入口 E2:第一出口 E3:第二出口 G1、G2:氣體濃縮模組 N1:第一端 N2:第二端 Air:空氣 O 2:氧氣 N 2:氮氣 100: Gas enrichment device 110A, 110B: Body 111: Top cover 112: Cylindrical wall 113: Bottom cover 114: Conduit 115: Molecular sieve filter material 116: Elastic parts 117A, 117B, 117C, 117D: Sealing parts 120A, 120B: Pipeline Joints 130A, 130B: control valve 140: storage tank 150: air compressor 160: control module 223: integrated structure E1: inlet E2: first outlet E3: second outlet G1, G2: gas concentration module N1: second One end N2: second end Air: air O 2 : oxygen N 2 : nitrogen

圖1是依據本發明一實施例的氣體濃縮裝置的示意圖。 圖2是圖1的氣體濃縮裝置的部分構件爆炸圖。 圖3是圖1的氣體濃縮裝置的部分構件剖視圖。 圖4是圖1的氣體濃縮裝置電性關係圖。 圖5是圖1的氣體濃縮裝置的作動關係示意圖。 圖6是本發明另一實施例的氣體濃縮裝置的部分結構示意圖。 FIG. 1 is a schematic diagram of a gas enrichment device according to an embodiment of the present invention. Fig. 2 is an exploded view of some components of the gas enrichment device in Fig. 1 . Fig. 3 is a cross-sectional view of some components of the gas concentrator in Fig. 1 . FIG. 4 is an electrical relationship diagram of the gas concentrator in FIG. 1 . FIG. 5 is a schematic diagram of the operation relationship of the gas enrichment device in FIG. 1 . Fig. 6 is a partial structural schematic diagram of a gas enrichment device according to another embodiment of the present invention.

100:氣體濃縮裝置 100: Gas enrichment device

110A、110B:本體 110A, 110B: body

120A、120B:管路接頭 120A, 120B: pipe joints

130A、130B:控制閥 130A, 130B: control valve

140:貯存罐 140: storage tank

150:空壓機 150: air compressor

E1:入口 E1: Entrance

E2:第一出口 E2: The first exit

E3:第二出口 E3: The second exit

G1、G2:氣體濃縮模組 G1, G2: Gas enrichment module

N1:第一端 N1: first end

N2:第二端 N2: the second end

Air:空氣 Air: air

O2:氧氣 O 2 : Oxygen

N2:氮氣 N 2 : Nitrogen

Claims (10)

一種氣體濃縮裝置,包括:多個氣體濃縮模組,各該氣體濃縮模組包括:一本體,填充分子篩濾材,該本體具有彼此相對的一第一端與一第二端;一管路接頭,位於該第一端,該管路接頭具有一入口、一第一出口與一第二出口,分別連通該本體;以及至少一控制閥,位於該第一端與該管路接頭之間並控制該入口、該第一出口與該第二出口的至少其一的啟閉,一第一氣體適於通過該入口進入該本體,並以該分子篩濾材過濾該第一氣體而分離出一第二氣體及一第三氣體,該些氣體濃縮模組的該些管路接頭為一體式結構。 A gas enrichment device, comprising: a plurality of gas enrichment modules, each of which includes: a body filled with molecular sieve filter material, the body has a first end and a second end opposite to each other; a pipeline joint, Located at the first end, the pipeline joint has an inlet, a first outlet, and a second outlet respectively communicating with the body; and at least one control valve located between the first end and the pipeline joint and controlling the Opening and closing of at least one of the inlet, the first outlet and the second outlet, a first gas is suitable to enter the body through the inlet, and the molecular sieve filter material is used to filter the first gas to separate a second gas and For a third gas, the pipeline joints of the gas enrichment modules are of an integrated structure. 一種氣體濃縮裝置,包括至少一氣體濃縮模組,該氣體濃縮模組包括一本體、一管路接頭以及至少一控制閥,該本體填充分子篩濾材,該本體具有彼此相對的一第一端與一第二端,該管路接頭位於該第一端,該管路接頭具有分別連通該本體的一入口、一第一出口與一第二出口,該控制閥位於該第一端與該管路接頭之間並控制該入口、該第一出口與該第二出口的至少其一的啟閉,一第一氣體適於通過該入口進入該本體,並以該分子篩濾材過濾該第一氣體而分離出一第二氣體與一第三氣體,其中該控制閥是二位三通電磁閥,而該氣體濃縮裝置還包括一控制模組,電性連接該二位三通電磁閥,該第一氣體為空氣,該第二氣體為氧氣,該第 三氣體為氮氣,其中該控制模組驅動該二位三通電磁閥以開啟該入口與控制第一出口與該第二出口啟閉,以使該空氣經由該入口進入該本體並被該分子篩濾材過濾而分離出該氧氣與該氮氣,並經由該第一出口將該氧氣排出該本體,其中該控制模組驅動該二位三通電磁閥關閉該入口與該第一出口且開啟該第二出口,以經由該第二出口將該氮氣排出該本體。 A gas concentration device, comprising at least one gas concentration module, the gas concentration module includes a body, a pipeline joint and at least one control valve, the body is filled with molecular sieve filter material, the body has a first end opposite to each other and a The second end, the pipeline connector is located at the first end, the pipeline connector has an inlet, a first outlet and a second outlet respectively connected to the body, the control valve is located at the first end and the pipeline connector and controlling the opening and closing of at least one of the inlet, the first outlet and the second outlet, a first gas is suitable to enter the body through the inlet, and the first gas is separated by filtering the first gas through the molecular sieve filter material A second gas and a third gas, wherein the control valve is a two-position three-way solenoid valve, and the gas enrichment device further includes a control module electrically connected to the two-position three-way solenoid valve, and the first gas is air, the second gas is oxygen, the first The third gas is nitrogen, wherein the control module drives the two-position three-way solenoid valve to open the inlet and control the opening and closing of the first outlet and the second outlet, so that the air enters the body through the inlet and is filtered by the molecular sieve filter to separate the oxygen and the nitrogen, and discharge the oxygen out of the body through the first outlet, wherein the control module drives the two-position three-way solenoid valve to close the inlet and the first outlet and open the second outlet , to discharge the nitrogen out of the body through the second outlet. 一種氣體濃縮裝置,包括至少一氣體濃縮模組,該氣體濃縮模組包括一本體、一管路接頭以及至少一控制閥,該本體填充分子篩濾材,該本體具有彼此相對的一第一端與一第二端,該管路接頭位於該第一端,該管路接頭具有分別連通該本體的一入口、一第一出口與一第二出口,該控制閥位於該第一端與該管路接頭之間並控制該入口、該第一出口與該第二出口的至少其一的啟閉,一第一氣體適於通過該入口進入該本體,並以該分子篩濾材過濾該第一氣體而分離出一第二氣體與一第三氣體,其中該至少一控制閥包括二通電磁閥與開關,該二通電磁閥連接並控制該入口與該第二出口的啟閉,該開關連接並控制該第一出口的啟閉,而該氣體濃縮裝置還包括一控制模組,分別電性連接該二通電磁閥與該開關,該第一氣體為空氣,該第二氣體為氧氣,該第三氣體為氮氣,其中該控制模組驅動該二通電磁閥開啟該入口且關閉該第二出口,且該控制模組驅動該開關開啟該第一出口,以使該空氣經由該入口進入該本體並被該分子篩濾材過濾而分離出該氧氣與該氮氣,以經由該第一出口將該氧氣排出該本體,其中該控制模組驅動 該二通電磁閥開啟該第二出口,且關閉該入口及該第一出口,以經由該第二出口將該氮氣排出該本體。 A gas concentration device, comprising at least one gas concentration module, the gas concentration module includes a body, a pipeline joint and at least one control valve, the body is filled with molecular sieve filter material, the body has a first end opposite to each other and a The second end, the pipeline connector is located at the first end, the pipeline connector has an inlet, a first outlet and a second outlet respectively connected to the body, the control valve is located at the first end and the pipeline connector and controlling the opening and closing of at least one of the inlet, the first outlet and the second outlet, a first gas is suitable to enter the body through the inlet, and the first gas is separated by filtering the first gas through the molecular sieve filter material A second gas and a third gas, wherein the at least one control valve includes a two-way solenoid valve and a switch, the two-way solenoid valve is connected and controls the opening and closing of the inlet and the second outlet, and the switch is connected and controls the first The opening and closing of an outlet, and the gas concentrator also includes a control module, which is electrically connected to the two-way solenoid valve and the switch, the first gas is air, the second gas is oxygen, and the third gas is Nitrogen, wherein the control module drives the two-way solenoid valve to open the inlet and close the second outlet, and the control module drives the switch to open the first outlet, so that the air enters the body through the inlet and is absorbed by the Molecular sieve filter material filters and separates the oxygen and the nitrogen, so that the oxygen is discharged from the body through the first outlet, wherein the control module drives The two-way solenoid valve opens the second outlet, and closes the inlet and the first outlet, so that the nitrogen gas is discharged from the body through the second outlet. 一種氣體濃縮裝置,包括至少一氣體濃縮模組,該氣體濃縮模組包括一本體、一管路接頭以及至少一控制閥,該本體填充分子篩濾材,該本體具有彼此相對的一第一端與一第二端,該管路接頭位於該第一端,該管路接頭具有分別連通該本體的一入口、一第一出口與一第二出口,該控制閥位於該第一端與該管路接頭之間並控制該入口、該第一出口與該第二出口的至少其一的啟閉,一第一氣體適於通過該入口進入該本體,並以該分子篩濾材過濾該第一氣體而分離出一第二氣體與一第三氣體,其中該氣體濃縮模組還包括一導管,設置於該本體內,該導管連接位於該第一端的該第一出口並延伸至該第二端,該第二氣體從該第二端進入該導管,並經由該第一出口排出該本體。 A gas concentration device, comprising at least one gas concentration module, the gas concentration module includes a body, a pipeline joint and at least one control valve, the body is filled with molecular sieve filter material, the body has a first end opposite to each other and a The second end, the pipeline connector is located at the first end, the pipeline connector has an inlet, a first outlet and a second outlet respectively connected to the body, the control valve is located at the first end and the pipeline connector and controlling the opening and closing of at least one of the inlet, the first outlet and the second outlet, a first gas is suitable to enter the body through the inlet, and the first gas is separated by filtering the molecular sieve filter material A second gas and a third gas, wherein the gas concentration module further includes a conduit disposed in the body, the conduit is connected to the first outlet at the first end and extends to the second end, the first Two gases enter the conduit from the second end and exit the body through the first outlet. 如請求項1、2、3或4所述的氣體濃縮裝置,其中經由該第一出口將該第二氣體排出該本體之後,也經由該第二出口將該第三氣體排出該本體。 The gas concentrator as claimed in claim 1, 2, 3 or 4, wherein after the second gas is discharged from the body through the first outlet, the third gas is also discharged from the body through the second outlet. 如請求項4所述的氣體濃縮裝置,其中該分子篩濾材包括從該第一端依序層疊至該第二端的多個網片,該導管穿過該些網片,而該氣體濃縮模組還包括一彈性件,抵接該第二端的該網片與該本體之間,且抵接該彈性件的該網片是該些網片的最末者。 The gas concentrator as claimed in item 4, wherein the molecular sieve filter material includes a plurality of mesh sheets sequentially stacked from the first end to the second end, the conduit passes through the mesh sheets, and the gas concentration module also An elastic member is included, the mesh abutting against the second end is between the body and the mesh abutting the elastic member is the last of the meshes. 如請求項1、2、3或4所述的氣體濃縮裝置,還包括一空壓機,連接該至少一氣體濃縮模組的該入口,以加壓並傳送該第一氣體經由該入口進入該本體。 The gas enrichment device as claimed in claim 1, 2, 3 or 4, further comprising an air compressor connected to the inlet of the at least one gas enrichment module to pressurize and deliver the first gas into the body through the inlet . 如請求項1、2、3或4所述的氣體濃縮裝置,還包括一空壓機,連接該至少一氣體濃縮模組的該第二出口,以經由該第二出口從該本體內抽出該第三氣體。 The gas concentrating device as claimed in claim 1, 2, 3 or 4, further comprising an air compressor connected to the second outlet of the at least one gas concentrating module, so as to extract the first gas from the main body through the second outlet Three gases. 如請求項1、2、3或4所述的氣體濃縮裝置,還包括一貯存罐,連接該至少一氣體濃縮模組的該第一出口,以收集該第二氣體或該第三氣體。 The gas enrichment device as claimed in claim 1, 2, 3 or 4 further comprises a storage tank connected to the first outlet of the at least one gas enrichment module to collect the second gas or the third gas. 如請求項1、3或4所述的氣體濃縮裝置,其中該控制閥是二位三通電磁閥,而該氣體濃縮裝置還包括一控制模組,電性連接該二位三通電磁閥,該第一氣體為空氣,該第二氣體為氧氣,該第三氣體為氮氣,其中該控制模組驅動該二位三通電磁閥以開啟該入口與該第二出口啟閉,以使該空氣經由該入口進入該本體並被該分子篩濾材過濾而分離出該氧氣與該氮氣,並經由該第一出口將該氧氣排出該本體,其中該控制模組驅動該二位三通電磁閥關閉該入口與該第一出口且開啟該第二出口,以經由該第二出口將該氮氣排出該本體。 The gas concentrating device as described in claim 1, 3 or 4, wherein the control valve is a two-position three-way solenoid valve, and the gas concentrating device further includes a control module electrically connected to the two-position three-way solenoid valve, The first gas is air, the second gas is oxygen, and the third gas is nitrogen, wherein the control module drives the two-position three-way solenoid valve to open and close the inlet and the second outlet so that the air Enter the body through the inlet and be filtered by the molecular sieve filter to separate the oxygen and the nitrogen, and discharge the oxygen out of the body through the first outlet, wherein the control module drives the two-position three-way solenoid valve to close the inlet connecting the first outlet and opening the second outlet, so that the nitrogen gas is discharged from the body through the second outlet.
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Citations (6)

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CN106456927A (en) * 2014-03-28 2017-02-22 开罗股份有限公司 Controlling oxygen concentrator timing cycle based on flow rate of oxygen output
CN112830456A (en) * 2021-02-08 2021-05-25 江苏鱼跃医疗设备股份有限公司 Oxygen concentrator casing and use oxygen concentrator of this casing

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1998057728A1 (en) * 1997-06-16 1998-12-23 Airsep Corporation Pressure swing adsorption apparatus and method
CN101534928A (en) * 2006-08-28 2009-09-16 Ric投资有限责任公司 Oxygen concentration system
TW200916134A (en) * 2007-05-07 2009-04-16 Teijin Pharma Ltd Oxygen enricher
CN106456927A (en) * 2014-03-28 2017-02-22 开罗股份有限公司 Controlling oxygen concentrator timing cycle based on flow rate of oxygen output
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CN112830456A (en) * 2021-02-08 2021-05-25 江苏鱼跃医疗设备股份有限公司 Oxygen concentrator casing and use oxygen concentrator of this casing

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