JPH0365213A - Nitrogen concentrating apparatus - Google Patents
Nitrogen concentrating apparatusInfo
- Publication number
- JPH0365213A JPH0365213A JP1200552A JP20055289A JPH0365213A JP H0365213 A JPH0365213 A JP H0365213A JP 1200552 A JP1200552 A JP 1200552A JP 20055289 A JP20055289 A JP 20055289A JP H0365213 A JPH0365213 A JP H0365213A
- Authority
- JP
- Japan
- Prior art keywords
- nitrogen
- oxygen
- gas separation
- separation membrane
- air
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
- Oxygen, Ozone, And Oxides In General (AREA)
Abstract
(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.
Description
【発明の詳細な説明】
産業上の利用分野
本発明は、気体分離膜を用いて室内の窒素濃度を高くす
る窒素濃縮装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION Field of Industrial Application The present invention relates to a nitrogen concentrator that uses a gas separation membrane to increase the nitrogen concentration in a room.
従来の技術 従来から、窒素は不活性気体として化学工業。Conventional technology Traditionally, nitrogen has been used in the chemical industry as an inert gas.
食品貯蔵、電子工業等の分野で広く利用されている。窒
素の供給源としては液体窒素や圧縮窒素を充填したボン
ベを用いるのが一般的である。ところがこれらの方法で
は低温の液体窒素や高圧ガス容器を取シ扱う危険が伴な
う上、容器の交換、流量調節等の取シ扱いが煩雑である
という課題を有していた。このため高純度の窒素を必要
としない用途には気体分離膜を用いて室内の窒素を濃縮
する方法が提案されている(例えば特開昭6〇−149
24号公報)。Widely used in food storage, electronic industry, etc. As a nitrogen supply source, a cylinder filled with liquid nitrogen or compressed nitrogen is generally used. However, these methods involve the risk of handling low-temperature liquid nitrogen or high-pressure gas containers, and have the problem that handling such as container replacement and flow rate adjustment is complicated. For this reason, methods have been proposed for concentrating indoor nitrogen using a gas separation membrane for applications that do not require high-purity nitrogen (for example, Japanese Patent Application Laid-Open No. 60-149
Publication No. 24).
以下図面を参照しながら、従来の窒素濃縮装置について
説明する。A conventional nitrogen concentrator will be described below with reference to the drawings.
第3図は従来の窒素濃縮装置の構成を示す模式図である
。図にかいて1は窒素濃度を高めようとする窒素富化室
、2は窒素富化室1内の空気をダクト3及び気体分離膜
エミツト4に供給するファン、5は前記気体分離膜ユニ
ット4を介して窒素富化室1内の酸素を分離するための
真空ポンプ、6は分離された酸素濃度が高い空気の排出
径路、7は窒素濃縮空気の供給径路、8は外気供給ファ
ン、10は酸素除去装置である。FIG. 3 is a schematic diagram showing the configuration of a conventional nitrogen concentrator. In the figure, 1 is a nitrogen enrichment chamber for increasing the nitrogen concentration, 2 is a fan that supplies air in the nitrogen enrichment chamber 1 to a duct 3 and a gas separation membrane emitter 4, and 5 is a gas separation membrane unit 4. a vacuum pump for separating oxygen in the nitrogen enrichment chamber 1; 6 is a discharge path for the separated air with high oxygen concentration; 7 is a supply path for nitrogen-enriched air; 8 is an outside air supply fan; 10 is a It is an oxygen removal device.
以上のように構成された窒素濃縮装置について以下その
動作について説明する。The operation of the nitrogen concentrator configured as described above will be explained below.
筐ずファン2によって窒素富化室1内の空気が気体分離
膜ユニット4に供給される。同時に真空ポンプ6を運転
すると気体分離膜ユニソト4内で酸素が分離され、排出
径路6より室外に排出される。酸素がとり除かれ、窒素
濃度が高くなった空気は窒素濃縮空気供給径路アから窒
素富化室1内へ供給される。また外気供給ファン8によ
って、気体分離膜ユニットから排出される酸素富化空気
と同等程度の空気を供給している。Air inside the nitrogen enrichment chamber 1 is supplied to the gas separation membrane unit 4 by the housing fan 2 . When the vacuum pump 6 is operated at the same time, oxygen is separated within the gas separation membrane Unisoto 4 and is discharged to the outside through the discharge path 6. The air from which oxygen has been removed and whose nitrogen concentration has been increased is supplied into the nitrogen enrichment chamber 1 from the nitrogen enriched air supply path A. Furthermore, the outside air supply fan 8 supplies air equivalent to the oxygen-enriched air discharged from the gas separation membrane unit.
発明が解決しようとする課題
しかしながら上記窒素濃縮装置では除去された酸素量の
空気を外気から補給して釦り、気体分離膜ユニットで濃
縮された窒素濃縮空気に大気を混合することにより、効
率が悪くなる上、高濃度の窒素濃縮雰囲気が得られない
という課題を有していた。Problems to be Solved by the Invention However, in the above nitrogen concentrator, the efficiency is improved by replenishing the removed oxygen amount from outside air and mixing the atmospheric air with the nitrogen-enriched air concentrated in the gas separation membrane unit. In addition, there were problems in that a highly concentrated nitrogen atmosphere could not be obtained.
本発明は、上記課題に鑑み、より効率よく高濃度の窒素
濃縮雰囲気が得られる窒素濃縮装置を提供するものであ
る。In view of the above-mentioned problems, the present invention provides a nitrogen concentrator that can more efficiently obtain a highly concentrated nitrogen atmosphere.
課題を解決するための手段
この目的を遠戚するために本発明の窒素濃縮装置は、気
体分離膜を備えた酸素除去手段、釦よび窒素濃縮手段に
よ夕室内から酸素を除去すると同時に室内に窒素濃縮空
気を供給する構成を有している。Means for Solving the Problem In order to achieve this object distantly, the nitrogen concentrator of the present invention uses an oxygen removing means equipped with a gas separation membrane, a button, and a nitrogen concentrating means to remove oxygen from the evening room and at the same time remove oxygen from the room. It has a configuration that supplies nitrogen-enriched air.
作 用
との構成によって酸素除去手段により室内の空気から酸
素をとり除き、同時に窒素濃縮手段によシ室外の空気か
ら酸素をと9除くことによシ得られた窒素濃縮空気を室
内に供給し、室内の窒素濃度は高められる。このとき窒
素濃縮手段から室内へ供給する窒素濃縮空気の濃度を必
要とする室内窒素濃度以上に設定すると、酸素除去手段
はもともと室内に存在する酸素を除去するだけですみ、
室外空気をそのまま導入する場合に比べて短時間に窒素
濃度を高めることができる。また供給する窒素富化空気
の濃度が必要とする室内窒素濃度以下の場合でも酸素除
去手段によって取り除く酸素量は大気を導入する場合よ
りも少なく、よシ短時間に窒素濃度を高められるのはい
うまでもない。According to the configuration, the oxygen removing means removes oxygen from indoor air, and at the same time, the nitrogen concentrating means removes oxygen from the outdoor air, thereby supplying nitrogen-enriched air into the room. , the indoor nitrogen concentration is increased. At this time, if the concentration of the nitrogen-enriched air supplied from the nitrogen concentrator into the room is set to a level higher than the required indoor nitrogen concentration, the oxygen remover only needs to remove the oxygen that originally exists in the room.
Nitrogen concentration can be increased in a shorter time than when outdoor air is directly introduced. Furthermore, even if the concentration of nitrogen-enriched air supplied is below the required indoor nitrogen concentration, the amount of oxygen removed by the oxygen removal means is less than when introducing atmospheric air, and the nitrogen concentration can be increased in a much shorter time. Not even.
実施例
以下本発明の一実施例について図面を参照しながら説明
する。第1図は本発明の一実施例における窒素濃縮装置
の模式図である。101は窒素濃度を高めようとする窒
素富化容器で、10/の容積をもち、気密にフタができ
るようになっている。EXAMPLE An example of the present invention will be described below with reference to the drawings. FIG. 1 is a schematic diagram of a nitrogen concentrator in one embodiment of the present invention. Reference numeral 101 is a nitrogen enrichment container intended to increase the nitrogen concentration, and has a volume of 10/1, and is designed to have an airtight lid.
104は酸素除去装置で、気体分離膜モジュール105
(以下、モジュー/L/105という)と真空ポンプ1
06からなっている。モジュー/L/105に備えられ
た気体分離膜107はポリプロピレン不織布上にポリエ
ーテルスルホンの多孔質体を形成した支持体上にジメチ
ルシリコーンを主体とした高分子膜をコートしたもので
ある。111は窒素濃縮空気供給装置で、気体分離膜モ
ジュール112(jは下、モジュール112という)と
真空ポンプ113とからなっている。モジュール112
に備えられた気体分離膜114は気体分離膜107と同
じものを用いる。104 is an oxygen removal device, and a gas separation membrane module 105
(hereinafter referred to as module/L/105) and vacuum pump 1
It consists of 06. The gas separation membrane 107 provided in MODU/L/105 is a support made of a polyethersulfone porous material formed on a polypropylene nonwoven fabric and coated with a polymer membrane mainly composed of dimethyl silicone. Reference numeral 111 denotes a nitrogen-concentrated air supply device, which consists of a gas separation membrane module 112 (j is below, referred to as module 112) and a vacuum pump 113. module 112
The same gas separation membrane 114 as the gas separation membrane 107 is used.
以上の様な構成による窒素濃縮装置について以下その動
作を説明する。まず酸素除去装置104の真空ポンプ1
06を運転するとモジュー/l/10E5に備えられた
気体分離膜1o了によって窒素富化容器101内の酸素
が選択的に分離され酸素富化空気として容器外へ排出さ
れる。同時に排出された酸素富化空気と同量の空気が、
容器外から窒素濃縮空気供給装置111の外気導入口1
16からモジュール112に導入され、容器内の窒素濃
度を高くする。The operation of the nitrogen concentrator configured as described above will be explained below. First, the vacuum pump 1 of the oxygen removal device 104
When the module 06 is operated, oxygen in the nitrogen enriched container 101 is selectively separated by the gas separation membrane 10 provided in the module 10E5, and is discharged as oxygen enriched air to the outside of the container. At the same time, the same amount of oxygen-enriched air is exhausted.
Outside air inlet 1 of nitrogen enriched air supply device 111 from outside the container
16 into module 112 to increase the nitrogen concentration in the container.
以上の様な構成で酸素除去装置の気体分離膜10了の面
積が41.5d、窒素濃縮空気供給装置の気体分離膜1
07の面積が208d、真空ポンプ106,113によ
って減圧されるモジニーμm05,112内部の真空度
−480snHg で運転したところ窒素富化容器10
1内の窒素濃度は20分後に86.6%、60分後に8
9.5%になった。な釦第2図にその結果を示した。With the above configuration, the area of the gas separation membrane 10 of the oxygen removal device is 41.5 d, and the area of the gas separation membrane 1 of the nitrogen concentrated air supply device is 41.5 d.
The area of 07 is 208d, and the vacuum inside Moginy μm05,112 is reduced by vacuum pumps 106,113.When operating at -480snHg, the nitrogen enrichment vessel 10
The nitrogen concentration in 1 was 86.6% after 20 minutes and 8 after 60 minutes.
It became 9.5%. The results are shown in Figure 2.
以上の様に本実施例によれば、窒素富化容器内の酸素を
除去するための気体分離膜を用いた酸素除去装置と、窒
素富化容器内に窒素濃縮空気を供給するための気体分離
膜による窒素濃縮空気供給装置を用いることによシ、容
器内の窒素濃度を短時間のうちに高めることができる。As described above, according to this embodiment, there is provided an oxygen removal device using a gas separation membrane for removing oxygen in a nitrogen enrichment container, and a gas separation device for supplying nitrogen enriched air into the nitrogen enrichment container. By using a membrane-based nitrogen-concentrated air supply device, the nitrogen concentration in the container can be increased in a short time.
発明の効果
以上の様に本発明によれば、気体分離膜を用いた酸素除
去手段、釦よび窒素濃縮手段によシ、室内から酸素を除
去すると同時に室内に窒素濃縮空気を供給することによ
り、短時間に高濃度の窒素濃縮雰囲気が得られその実用
的効果は大なるものがある。Effects of the Invention As described above, according to the present invention, oxygen is removed from the room and nitrogen-concentrated air is supplied into the room at the same time by means of an oxygen removal means using a gas separation membrane, a button, and a nitrogen concentration means. A highly concentrated nitrogen atmosphere can be obtained in a short period of time, which has great practical effects.
第1図は本発明の一実施例における窒素濃縮装置の溝底
を示す模式図、第2図は同実施例の容器内窒素濃度の経
時変化を示す特性図、第3図は従来の窒素濃縮装置の溝
底を示す模式図である。
101・・・・・・窒素富化容器、104・・・・・・
酸素除去装置、107・・・・・・気体分離膜、111
・・・・・・窒素濃縮空気供給装置、114・・・・・
・気体分離膜。Fig. 1 is a schematic diagram showing the groove bottom of a nitrogen concentrator according to an embodiment of the present invention, Fig. 2 is a characteristic diagram showing changes over time in the nitrogen concentration in the container of the same embodiment, and Fig. 3 is a conventional nitrogen concentrator. FIG. 3 is a schematic diagram showing the groove bottom of the device. 101... Nitrogen enrichment container, 104...
Oxygen removal device, 107... Gas separation membrane, 111
...Nitrogen enriched air supply device, 114...
・Gas separation membrane.
Claims (1)
濃縮気体を得て前記室内に供給する手段とを備え、前記
酸素除去手段および窒素濃縮手段は、窒素よりも酸素の
透過速度が大きい気体分離膜を備えていることを特徴と
する窒素濃縮装置。The device includes means for removing oxygen from indoor air, and means for obtaining a nitrogen-enriched gas from outdoor air and supplying it into the room, and the oxygen removing means and the nitrogen concentrating means are gas separators having a higher permeation rate for oxygen than for nitrogen. A nitrogen concentrator characterized by comprising a membrane.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1200552A JPH0365213A (en) | 1989-08-01 | 1989-08-01 | Nitrogen concentrating apparatus |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP1200552A JPH0365213A (en) | 1989-08-01 | 1989-08-01 | Nitrogen concentrating apparatus |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0365213A true JPH0365213A (en) | 1991-03-20 |
Family
ID=16426210
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP1200552A Pending JPH0365213A (en) | 1989-08-01 | 1989-08-01 | Nitrogen concentrating apparatus |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0365213A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0381657U (en) * | 1989-12-08 | 1991-08-21 | ||
| JP2013112547A (en) * | 2011-11-26 | 2013-06-10 | National Institute For Agro-Environmental Science | Purification method of ultrahigh-purity gaseous nitrogen |
-
1989
- 1989-08-01 JP JP1200552A patent/JPH0365213A/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH0381657U (en) * | 1989-12-08 | 1991-08-21 | ||
| JP2013112547A (en) * | 2011-11-26 | 2013-06-10 | National Institute For Agro-Environmental Science | Purification method of ultrahigh-purity gaseous nitrogen |
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