[go: up one dir, main page]

JPH02256595A - Aspiration gas feeding system - Google Patents

Aspiration gas feeding system

Info

Publication number
JPH02256595A
JPH02256595A JP7780489A JP7780489A JPH02256595A JP H02256595 A JPH02256595 A JP H02256595A JP 7780489 A JP7780489 A JP 7780489A JP 7780489 A JP7780489 A JP 7780489A JP H02256595 A JPH02256595 A JP H02256595A
Authority
JP
Japan
Prior art keywords
carbon dioxide
gas
adsorbent
oxygen
gas supply
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.)
Granted
Application number
JP7780489A
Other languages
Japanese (ja)
Other versions
JP2684755B2 (en
Inventor
Hisashi Mitani
三谷 寿
Hidefumi Saito
英文 斎藤
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Shimadzu Corp
Original Assignee
Shimadzu Corp
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Shimadzu Corp filed Critical Shimadzu Corp
Priority to JP7780489A priority Critical patent/JP2684755B2/en
Publication of JPH02256595A publication Critical patent/JPH02256595A/en
Application granted granted Critical
Publication of JP2684755B2 publication Critical patent/JP2684755B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Landscapes

  • Respiratory Apparatuses And Protective Means (AREA)

Abstract

PURPOSE:To regenerate and adsorbent for carbon dioxide for removing carbon dioxide from aspiration gas and realize the continuous use of the adsorbent in the title system mounted onto an aeroplane in which aspiration gas from which carbon dioxide is removed is allowed to circulate into a gas feeding passage. CONSTITUTION:The gas for aspiration which is bleeded from the compressor of an engine is supplied into the mask M of a driver through a gas feeding passage L1 by the supplement of the oxygen supplied from an oxygen cylinder 3 in a mixing chamber 2, and the aspiration gas discharged into the mask M is returned into the mixing chamber 2 through a gas circulation passage L2. In this case, the gas circulation passage L2 is branched into two branched passages L2a and L2b through a pair of rotary selector valve 8 and 9 which are interlocked with each other, and carbon dioxide gas removing devices 10a and 10b are installed and the both devices 10a and 10b can be regenerated alternately. The regeneration is carried out by introducing the high temperature air into heating tanks 13a or 13b through a selector valve 25 and by discharging the carbon dioxide adsorbed onto an adsorbent 12.

Description

【発明の詳細な説明】 A0発明の目的 (1)  産業上の利用分野 本発明は、空気のfilな高高度を飛行する航空機の搭
乗員等が装着するマスクに呼吸用の気体を供給する呼吸
用気体供給システムに関し、特に、二酸化炭素を分離し
た呼気を気体供給路に循環させることにより、この呼気
中に残留する酸素を再利用することを可能とした呼吸用
気体供給システムに関する。
Detailed Description of the Invention A0 Object of the Invention (1) Industrial Field of Application The present invention relates to a respirator for supplying breathing gas to a mask worn by the crew of an aircraft flying at high altitudes with air filtration. The present invention relates to a respiratory gas supply system, and more particularly to a respiratory gas supply system that makes it possible to reuse oxygen remaining in exhaled air by circulating exhaled air from which carbon dioxide has been separated through a gas supply path.

(2)従来の技術 従来の航空機においては、その機内圧力が普通外気圧力
よりも少し高い値に保持されている。したがって、航空
機が空気の稀薄な高高度を飛行する際には機内圧力が低
くなり、酸素分圧も低くなる。そうすると、搭乗者にと
って酸素不足となり、搭乗者の判断が鈍る等の問題点が
生じる。
(2) Prior Art In conventional aircraft, the cabin pressure is normally maintained at a value slightly higher than the outside air pressure. Therefore, when an aircraft flies at a high altitude where the air is thin, the cabin pressure is low and the oxygen partial pressure is also low. This causes problems such as a lack of oxygen for the passengers and impaired judgment by the passengers.

このため、高高度を飛行する航空機には、搭乗者が装着
する酸素補給用のマスクに呼吸用の気体を供給する呼吸
用気体供給システムが装着されている。この呼吸用気体
供給システムは、酸素ボンベまたは酸素凝縮装置等の酸
素供給源からの酸素およびエンジンから抽気した空気等
の呼吸用気体を前記マスクに供給しており、その供給す
る呼吸用気体の圧力も機内圧力の低下とともに低下する
ようになっている。そして、呼吸用気体の圧力の低下と
ともに酸素濃度を高めることにより、マスクに供給され
る呼吸用気体の酸素分圧を略一定に保持するようにして
いる。そして従来の呼吸用気体供給システムにおいては
、マスクに供給された呼吸用気体は、マスク装着者が一
度吸入して吐出する際、機内に放出されるように構成さ
れていた。
For this reason, aircraft flying at high altitudes are equipped with a breathing gas supply system that supplies breathing gas to oxygen supplementation masks worn by passengers. This breathing gas supply system supplies breathing gas such as oxygen from an oxygen supply source such as an oxygen cylinder or an oxygen condensing device and air bled from an engine to the mask, and the pressure of the supplied breathing gas. The pressure also decreases as the cabin pressure decreases. By increasing the oxygen concentration as the pressure of the breathing gas decreases, the oxygen partial pressure of the breathing gas supplied to the mask is maintained substantially constant. In conventional respiratory gas supply systems, the respiratory gas supplied to the mask is discharged into the cabin when the mask wearer inhales and exhales the gas.

ところが、前記マスクに供給される呼吸用気体は酸素濃
度が高いので、その呼吸用気体をマスク装着者が一度吸
入してから吐出する気体すなわち呼気の中にはまだ多く
の酸素が残っている。したがって、このような多くの酸
素を含む呼気をそのまま機内に放出することはせっかく
製造した酸素を無駄に消費することになる。
However, since the breathing gas supplied to the mask has a high oxygen concentration, a large amount of oxygen still remains in the gas that is breathed out after the mask wearer inhales the breathing gas, that is, the breath. Therefore, if exhaled air containing a large amount of oxygen is released into the aircraft as it is, the produced oxygen will be wasted.

その無駄をな(すために、前記酸素の多い呼気を、二酸
化炭素除去装置等を通過させて酸素割合の多い気体とし
て再生し、この再生気体を前記酸素供給源からの酸素と
混合して前記マスクに循環させる呼吸用気体供給システ
ムが提案されている。
In order to eliminate waste, the oxygen-rich exhaled air is passed through a carbon dioxide removal device or the like to be regenerated as a gas with a high oxygen content, and this regenerated gas is mixed with the oxygen from the oxygen supply source. Breathing gas supply systems have been proposed that circulate through the mask.

(3)  発明が解決しようとする課題しかしながら、
上記従来の呼吸用気体供給システムは、二酸化炭素除去
装置の吸着剤によって呼気中の二酸化炭素を連続して吸
着除去していると、その二酸化炭素の吸着剤が次第に劣
化して性能が低下する問題があった。
(3) Problems to be solved by the invention However,
The above-mentioned conventional breathing gas supply system has a problem in that when carbon dioxide in exhaled breath is continuously adsorbed and removed by the adsorbent of the carbon dioxide removal device, the carbon dioxide adsorbent gradually deteriorates and performance decreases. was there.

本発明は、前述の事情に鑑みてなされたもので、搭乗者
の呼気から二酸化炭素を除去する二酸化炭素の吸着剤を
再生することにより、その継続的な使用を可能にした呼
吸用気体供給システムを提供することを課題とする。
The present invention has been made in view of the above-mentioned circumstances, and is a breathing gas supply system that enables continuous use of a carbon dioxide adsorbent that removes carbon dioxide from exhaled breath of passengers by regenerating it. The challenge is to provide the following.

B0発明の構成 (1)課題を解決するための手段 前記課題を解決するために、本発明は、エンジンから抽
気した呼吸用気体をマスクに供給する気体供給路と、こ
の気体供給路に接続されて該気体供給路に酸素を補給す
る酸素供給源と、マスク内に吐出された呼気を前記気体
供給路に循環させる気体循環路と、この気体循環路に排
出された呼気中の二酸化炭素を吸着除去する吸着剤を有
する二酸化炭素除去装置とを備え、この二酸化炭素除去
装置で得られた二酸化炭素減少気体を呼吸用気体として
再利用する呼吸用気体供給システムにおいて、二酸化炭
素の吸着量が飽和状態に近づいた前記吸着剤から二酸化
炭素を分離させる再生手段と、分離した二酸化炭素を二
酸化炭素除去装置から排出する排出路とを備えてなるこ
とを特徴とする。
B0 Structure of the Invention (1) Means for Solving the Problems In order to solve the above problems, the present invention provides a gas supply path that supplies breathing gas extracted from an engine to a mask, and a gas supply path that is connected to the gas supply path. an oxygen supply source that replenishes oxygen to the gas supply path, a gas circulation path that circulates exhaled air exhaled into the mask to the gas supply path, and adsorbs carbon dioxide in the exhaled air discharged into the gas circulation path. In a breathing gas supply system that includes a carbon dioxide removal device having an adsorbent to remove carbon dioxide and reuses the carbon dioxide reduced gas obtained by the carbon dioxide removal device as breathing gas, the amount of carbon dioxide adsorbed is saturated. The present invention is characterized by comprising a regenerating means for separating carbon dioxide from the adsorbent that has approached the temperature, and an exhaust path for discharging the separated carbon dioxide from the carbon dioxide removal device.

前記二酸化炭素除去装置を2個設け、一方の二酸化炭素
除去装置で二酸化炭素の吸着除去を行ないながら、他方
の二酸化炭素除去装置の吸着剤の再生を行うと効果的で
ある。
It is effective to provide two carbon dioxide removal devices, and while one carbon dioxide removal device adsorbs and removes carbon dioxide, the adsorbent in the other carbon dioxide removal device is regenerated.

また、前記吸着剤としてはたとえば活性炭またはモレキ
ュラーシープ等を採用することができる。
Further, as the adsorbent, for example, activated carbon or molecular sheep can be used.

そして、これらの吸着剤を採用した場合、前記再生手段
は、二酸化炭素除去装置の吸着剤を加熱する加熱槽と、
この加熱槽にエンジンから抽気した高温空気を導入する
高温抽気路とにより構成することができる。
When these adsorbents are employed, the regeneration means includes a heating tank that heats the adsorbent of the carbon dioxide removal device;
The heating tank may be configured with a high-temperature bleed passage that introduces high-temperature air extracted from the engine into the heating tank.

(2)作 用 前述の構成を備えた本発明によれば、エンジンから気体
供給路に抽気された呼吸用気体は酸素供給源から酸素の
補給を受けてマスクに供給され、ここで一部の酸素を消
費された呼気となって気体循環路に排出される。気体循
環路に排出された呼気は二酸化炭素除去装置の吸着剤を
通過して二酸化炭素減少気体となり、再び気体供給路に
戻されて呼吸用気体として再利用される。二酸化炭素除
去装置の吸着剤の二酸化炭素吸着量が飽和状態に近づく
と、前記再生手段により、吸着剤から二酸化炭素が分離
され、この吸着剤は再び二酸化炭素を吸着可能な状態に
再生される。
(2) Effect According to the present invention having the above-described configuration, the breathing gas bled from the engine into the gas supply path is supplied with oxygen from the oxygen supply source and then supplied to the mask, where a portion of the breathing gas is supplied to the mask. The exhaled air is depleted of oxygen and is discharged into the gas circulation path. The exhaled air discharged into the gas circulation path passes through the adsorbent of the carbon dioxide removal device, becomes a carbon dioxide-depleted gas, and is returned to the gas supply path to be reused as breathing gas. When the amount of carbon dioxide adsorbed by the adsorbent of the carbon dioxide removal device approaches a saturated state, the regeneration means separates carbon dioxide from the adsorbent, and the adsorbent is regenerated into a state capable of adsorbing carbon dioxide again.

そして、二酸化炭素除去装置を2個設けて吸着剤の再生
を交互に行えば、いずれかの二酸化炭素除去装置が常に
機能して二酸化炭素の除去を連続して行うことができる
If two carbon dioxide removal devices are provided and the adsorbent is regenerated alternately, one of the carbon dioxide removal devices can always function and remove carbon dioxide continuously.

さらに、前記吸着剤として活性炭またはモレキュラーシ
ーブを採用し、前記再生手段を、二酸化炭素除去装置の
吸着剤を加熱する加熱槽とエンジンから抽気した高温空
気を導入する高温油気路とから構成すれば、特別な熱源
を用いずに吸着剤の加熱再生を行うことができる。
Furthermore, if activated carbon or molecular sieve is adopted as the adsorbent, and the regeneration means is composed of a heating tank that heats the adsorbent of the carbon dioxide removal device and a high-temperature oil passage that introduces high-temperature air extracted from the engine. , the adsorbent can be thermally regenerated without using a special heat source.

(3)実施例 以下、図面に基づいて本発明の詳細な説明する。(3) Examples Hereinafter, the present invention will be described in detail based on the drawings.

第1図に示す本発明の一実施例による呼吸用気体供給シ
ステムSは、エンジンの圧縮機から抽気した呼吸用気体
を図示しない汚染物質除去フィルタおよび流Ill整弁
1等を介して搭乗者のマスクMに供給する気体供給路L
1を備えている。気体供給路L1の中間に設けたミキシ
ング室2には酸素ボンベ等の酸素供給源3が流量調整弁
4を介して接続されており、このミキシング室2におい
てエンジンからの抽気に酸素を補給された呼吸用気体は
、気体供給弁5を通ってマスクMの内部に供給され、搭
乗者の呼吸に使用される。マスクMの内部に吐出された
搭乗者の呼気は気体排出弁6を介して気体循環路L2に
排出され、この気体循環路L2を通って前記ミキシング
室2に循環する。
A breathing gas supply system S according to an embodiment of the present invention shown in FIG. Gas supply path L that supplies the mask M
1. An oxygen supply source 3 such as an oxygen cylinder is connected to a mixing chamber 2 provided in the middle of the gas supply path L1 via a flow rate regulating valve 4, and oxygen is supplied to the bleed air from the engine in this mixing chamber 2. Breathing gas is supplied to the inside of the mask M through the gas supply valve 5 and is used for the occupant's breathing. The exhaled breath of the passenger discharged into the inside of the mask M is discharged into the gas circulation path L2 through the gas discharge valve 6, and circulated to the mixing chamber 2 through this gas circulation path L2.

そして、呼気の一部は気体循環路L2に設けた排気弁7
を介して機内または機外に排出される。
A part of the exhaled air is removed from an exhaust valve 7 provided in the gas circulation path L2.
are discharged into or out of the aircraft via the

気体循環路L2に介装された互いに連動する一対のロー
タリ切換弁8,90間には2本の分岐路L2a、L2b
が並設されており、各分岐路L2a、L2bにはそれぞ
れ二酸化炭素除去装置10a、10bが配設されている
。そして、これらの二酸化炭素除去装置10a、10b
は前記ロータリ切換弁8.9の開閉によって気体循環路
L2に選択的に接続される。また、ロータリ切換弁9と
ミキシング室2を結ぶ気体循環路L2からは、中間にオ
リフィス11を有する補助路L3が前記切換弁9に帰還
接続されるとともに、他の切換弁8には低圧の機外に連
通ずる排気路L4が接続されている。なお、この排気路
L4は機内に連通させることも可能である。
Two branch paths L2a and L2b are provided between a pair of mutually interlocking rotary switching valves 8 and 90 interposed in the gas circulation path L2.
are arranged in parallel, and carbon dioxide removal devices 10a and 10b are arranged in each branch path L2a and L2b, respectively. And these carbon dioxide removal devices 10a, 10b
is selectively connected to the gas circulation path L2 by opening and closing the rotary switching valve 8.9. Further, from the gas circulation path L2 connecting the rotary switching valve 9 and the mixing chamber 2, an auxiliary path L3 having an orifice 11 in the middle is connected back to the switching valve 9, and the other switching valve 8 is connected to a low-pressure machine. An exhaust path L4 communicating with the outside is connected. Note that this exhaust path L4 can also be communicated with the inside of the machine.

前記二酸化炭素除去装置10a、10bの内部には例え
ば活性炭、モレキュラーシープ4A、モレキユラーシー
ブ5A、あるいはモレキュラーシーブ13X等の二酸化
炭素の吸着剤12が充填されている。上記吸着剤12は
、第2図に示すように、二酸化炭素のいずれの分圧にお
いても温度の上昇に伴って吸着可能な二酸化炭素の最大
量が減少する特性を備えている。したがって、二酸化炭
素を吸着して飽和状態に達した吸着剤12を加熱すると
、吸着した二酸化炭素を分離放出して再び二酸化炭素を
吸着可能な状態に再生される。
The interior of the carbon dioxide removal devices 10a and 10b is filled with a carbon dioxide adsorbent 12 such as activated carbon, molecular sieve 4A, molecular sieve 5A, or molecular sieve 13X. As shown in FIG. 2, the adsorbent 12 has a characteristic that the maximum amount of carbon dioxide that can be adsorbed decreases as the temperature increases at any partial pressure of carbon dioxide. Therefore, when the adsorbent 12 that has adsorbed carbon dioxide and reached a saturated state is heated, the adsorbed carbon dioxide is separated and released, and the adsorbent is regenerated into a state capable of adsorbing carbon dioxide again.

二酸化炭素除去装置10a、10bの外周には吸着剤1
2を囲むように加熱槽13a、13bが設けられている
。この加熱槽13a、13bには、連動機構14で前記
一対のロータリ切換弁8,9と連動して開閉するローク
リ切換弁15を介してエンジンから抽気した高温空気を
導く高温抽気路L5a、L5bと、この高温空気を機外
に排出する高温排気路L6a、L6bとが接続されてい
る。
An adsorbent 1 is placed on the outer periphery of the carbon dioxide removal devices 10a and 10b.
Heating tanks 13a and 13b are provided so as to surround 2. The heating tanks 13a and 13b are provided with high-temperature bleed air passages L5a and L5b that guide high-temperature air extracted from the engine via a rotary switching valve 15 that opens and closes in conjunction with the pair of rotary switching valves 8 and 9 by an interlocking mechanism 14. , and high-temperature exhaust paths L6a and L6b that discharge this high-temperature air to the outside of the machine are connected.

そして、前記加熱槽13a、13bと高温抽気路L5a
、L5bとによって吸着剤の再生手段が構成されている
The heating tanks 13a, 13b and the high temperature bleed passage L5a
, L5b constitute an adsorbent regeneration means.

次に、前述の構成を備えた本発明の実施例の作用につい
て説明する。
Next, the operation of the embodiment of the present invention having the above-described configuration will be explained.

エンジンの圧縮機から気体供給路L1に抽気された呼吸
用気体は流量調整弁1を介してミキシング室2に達し、
ここで酸素供給源3から酸素の補給を受けた後、気体供
給弁5を通って搭乗者のマスクM内に供給される。一方
、搭乗者の呼気は気体排出弁6を通って気体循環路L2
に排出され、その一部は排気弁7を介して機外に放出さ
れる。
The breathing gas extracted from the engine compressor into the gas supply path L1 reaches the mixing chamber 2 via the flow rate adjustment valve 1,
Here, after oxygen is supplied from the oxygen supply source 3, it is supplied into the passenger's mask M through the gas supply valve 5. On the other hand, the exhaled breath of the passenger passes through the gas exhaust valve 6 and passes through the gas circulation path L2.
A part of it is discharged to the outside of the machine via the exhaust valve 7.

気体循環路L2に排出された呼気の大部分は、図示の位
置にあるロータリ切換弁8および分岐路L2aを介して
一方の二酸化炭素除去装置10aに導入され、その内部
に充填された吸着剤12を通過する。その際、呼気中に
含まれる二酸化炭素は吸着剤12によって吸着除去され
、酸素割合の増加した空気は分岐路L2a、ロータリ切
換弁9、および気体循環路L2を介して前記ミキシング
室2に循環し、再び搭乗者の呼吸用に利用される。
Most of the exhaled air discharged into the gas circulation path L2 is introduced into one carbon dioxide removal device 10a via the rotary switching valve 8 located at the position shown in the figure and the branch path L2a, and the adsorbent 12 filled therein is introduced into one of the carbon dioxide removal devices 10a. pass through. At this time, carbon dioxide contained in the exhaled breath is adsorbed and removed by the adsorbent 12, and the air with increased oxygen content is circulated to the mixing chamber 2 via the branch path L2a, the rotary switching valve 9, and the gas circulation path L2. , which will be used again for passenger breathing.

このとき、他方の二酸化炭素除去装置10bの加熱槽1
3bには、図示の位置にあるロータリ切換弁15および
高温抽気路L5bを介してエンジンから抽気した高温空
気が導入され、この高温空気により加熱された吸着剤1
2はそれまでに吸着した二酸化炭素を放出する。そして
、ロータリ切換弁9からミキシング室2に循環する空気
の一部は、オリフィス11を有する補助路L3、ロータ
リ切換弁9、および分岐路L2bを介して二酸化炭素除
去装置10bに導入され、加熱によって分離された前記
二酸化炭素と共に分岐路L2b、ロータリ切換弁8、お
よび排気路L4を介して機外に放出される。
At this time, the heating tank 1 of the other carbon dioxide removal device 10b
3b, high-temperature air bled from the engine is introduced through the rotary switching valve 15 located at the illustrated position and the high-temperature bleed passage L5b, and the adsorbent 1 is heated by this high-temperature air.
2 releases the carbon dioxide that has been adsorbed up to that point. A part of the air circulating from the rotary switching valve 9 to the mixing chamber 2 is introduced into the carbon dioxide removal device 10b via the auxiliary path L3 having the orifice 11, the rotary switching valve 9, and the branch path L2b, and is heated. Together with the separated carbon dioxide, it is discharged to the outside of the machine via the branch path L2b, the rotary switching valve 8, and the exhaust path L4.

上述のようにして、一方の二酸化炭素除去装置10aの
吸着剤12によって二酸化炭素の吸着除去を行いながら
、他方の二酸化炭素除去装置10bの吸着剤12の加熱
再生が行われる。そして、二酸化炭素除去装置10aの
吸着剤12が二酸化炭素を吸着して飽和状態に近づ(と
、前記3個のロータリ切換弁8,9.15が連動機構1
4によって同時に切り換えられ、今度は二酸化炭素除去
装置tabにおいて二酸化炭素の吸着除去が行われると
ともに、二酸化炭素除去装置10aの吸着剤12の加熱
再生が行われる。このようにして、ロータリ切換弁8.
9.15を交互に切り換えることにより、いずれかの二
酸化炭素除去装置10a、10bにおいて二酸化炭素の
吸着除去を行うことができる。
As described above, while carbon dioxide is being adsorbed and removed by the adsorbent 12 of one carbon dioxide removing device 10a, the adsorbent 12 of the other carbon dioxide removing device 10b is heated and regenerated. Then, the adsorbent 12 of the carbon dioxide removal device 10a adsorbs carbon dioxide and approaches a saturated state (and the three rotary switching valves 8, 9, 15
4, and this time carbon dioxide is adsorbed and removed in the carbon dioxide removal device tab, and the adsorbent 12 of the carbon dioxide removal device 10a is heated and regenerated. In this way, the rotary switching valve 8.
By alternately switching 9.15, carbon dioxide can be adsorbed and removed in either of the carbon dioxide removal devices 10a, 10b.

前述の実施例によれば、二酸化炭素除去装置を2個設け
て吸着剤の加熱再生を交互に行うようにしたので、いず
れかの二酸化炭素除去装置が常に機能して二酸化炭素の
除去を連続して行うことができる。
According to the above-mentioned embodiment, two carbon dioxide removal devices are provided and the adsorbent is heated and regenerated alternately, so that one of the carbon dioxide removal devices always functions to continuously remove carbon dioxide. It can be done by

さらに、二酸化炭素除去装置の吸着剤に接触する加熱槽
にエンジンから抽気した高温空気を導入するようにした
ので、特別な熱源を用いずに吸着剤の加熱再生を行うこ
とができる。
Furthermore, since high-temperature air extracted from the engine is introduced into the heating tank that contacts the adsorbent of the carbon dioxide removal device, the adsorbent can be heated and regenerated without using a special heat source.

以上、本発明の実施例を詳述したが、本発明は、前記実
施例に限定されるものでなく、特許請求の範囲に記載さ
れた本発明を逸脱することなく、種々の小設計変更を行
うことが可能である。
Although the embodiments of the present invention have been described in detail above, the present invention is not limited to the embodiments described above, and various small design changes may be made without departing from the scope of the present invention as set forth in the claims. It is possible to do so.

例えば、二酸化炭素除去装置10a、10bは必ずしも
2個とする必要はなく、1個または3個以上とすること
も可能である。また、吸着剤12を加熱する高温空気を
加熱槽13a、13bの内部に導入する代わりに、この
高温空気を汚染物質除去フィルタを通過させてから、吸
着剤12を充填した二酸化炭素除去装置10a、10b
の内部に直接導入することも可能であり、このようにす
れば、分離した二酸化炭素を高温空気と共に機外に放出
することができる。さらに、エンジンから抽気した高温
空気で吸着剤12を加熱する代わりに、電気ヒータ等の
他の熱源を用いて吸着剤12の加熱を行うことも可能で
ある。さらにまた、吸着剤を再生する手段としては、二
酸化炭素除去装置10a、10b内部の気体を吸引排出
して、その内部の二酸化炭素の分圧を低下させる手段を
採用することも可能である。
For example, the number of carbon dioxide removal devices 10a, 10b does not necessarily have to be two, and it is also possible to have one or three or more. Moreover, instead of introducing high-temperature air that heats the adsorbent 12 into the heating tanks 13a and 13b, this high-temperature air is passed through a pollutant removal filter, and then the carbon dioxide removal device 10a filled with the adsorbent 12, 10b
It is also possible to introduce the carbon dioxide directly into the inside of the machine, and in this way, the separated carbon dioxide can be released outside the machine together with the high temperature air. Furthermore, instead of heating the adsorbent 12 with high-temperature air extracted from the engine, it is also possible to heat the adsorbent 12 using another heat source such as an electric heater. Furthermore, as a means for regenerating the adsorbent, it is also possible to employ means for sucking and discharging the gas inside the carbon dioxide removal apparatuses 10a and 10b to lower the partial pressure of carbon dioxide therein.

C0発明の効果 前述の本発明の呼吸用気体供給システムによれば、飽和
状態に近づいた二酸化炭素の吸着剤が再生手段により再
び二酸化炭素を吸着可能な状態に再生されるので、この
吸着剤を繰返し使用することができる。したがって、二
酸化炭素除去装置の吸着剤を度々交換する必要がなくな
るだけでなく、吸着剤の量を減らして二酸化炭素除去装
置を小形化することが可能となる。
Effects of the C0 Invention According to the above-described breathing gas supply system of the present invention, the carbon dioxide adsorbent that has reached a saturated state is regenerated by the regeneration means to a state capable of adsorbing carbon dioxide again. Can be used repeatedly. Therefore, not only is it not necessary to frequently replace the adsorbent in the carbon dioxide removal device, but also it is possible to reduce the amount of adsorbent and downsize the carbon dioxide removal device.

【図面の簡単な説明】[Brief explanation of drawings]

第1図は本発明の一実施例による呼吸用気体供給システ
ムの全体構成図、第2図は吸着剤の温度特性を示すグラ
フである。 M・・・マスク、Ll・・・気体供給路、L2・・・気
体循環路、L5a、L5b・・・高温抽気路、L6a、
L6b・・・高温排出路、3・・・酸素供給源、lla
、11b・・・二酸化炭素除去装置、12・・・吸着剤
、13a、13b・・・加熱槽 平衡吸着量(g/100gMS)
FIG. 1 is an overall configuration diagram of a breathing gas supply system according to an embodiment of the present invention, and FIG. 2 is a graph showing the temperature characteristics of an adsorbent. M...Mask, Ll...Gas supply path, L2...Gas circulation path, L5a, L5b...High temperature bleed path, L6a,
L6b...High temperature exhaust path, 3...Oxygen supply source, lla
, 11b... Carbon dioxide removal device, 12... Adsorbent, 13a, 13b... Heating tank equilibrium adsorption amount (g/100gMS)

Claims (1)

【特許請求の範囲】 エンジンから抽気した呼吸用気体をマスクに供給する気
体供給路と、この気体供給路に接続されて該気体供給路
に酸素を補給する酸素供給源と、マスク内に吐出された
呼気を前記気体供給路に循環させる気体循環路と、この
気体循環路に排出された呼気中の二酸化炭素を吸着除去
する吸着剤を有する二酸化炭素除去装置とを備え、この
二酸化炭素除去装置で得られた二酸化炭素減少気体を呼
吸用気体として再利用する呼吸用気体供給システムにお
いて、 二酸化炭素の吸着量が飽和状態に近づいた前記吸着剤か
ら二酸化炭素を分離させる再生手段と、分離した二酸化
炭素を二酸化炭素除去装置から排出する排出路とを備え
てなる呼吸用気体供給システム。
[Claims] A gas supply path that supplies breathing gas extracted from the engine to the mask, an oxygen supply source that is connected to this gas supply path and supplies oxygen to the gas supply path, and an oxygen supply source that supplies oxygen to the gas supply path; The carbon dioxide removal device includes a gas circulation path that circulates exhaled air to the gas supply path, and a carbon dioxide removal device that has an adsorbent that adsorbs and removes carbon dioxide in the breath discharged to the gas circulation path. A breathing gas supply system that reuses the obtained carbon dioxide reduced gas as a breathing gas, comprising: a regeneration means for separating carbon dioxide from the adsorbent whose adsorption amount of carbon dioxide has approached a saturated state; and an exhaust path for discharging carbon dioxide from the carbon dioxide removal device.
JP7780489A 1989-03-29 1989-03-29 Breathing gas supply system Expired - Lifetime JP2684755B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7780489A JP2684755B2 (en) 1989-03-29 1989-03-29 Breathing gas supply system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7780489A JP2684755B2 (en) 1989-03-29 1989-03-29 Breathing gas supply system

Publications (2)

Publication Number Publication Date
JPH02256595A true JPH02256595A (en) 1990-10-17
JP2684755B2 JP2684755B2 (en) 1997-12-03

Family

ID=13644199

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7780489A Expired - Lifetime JP2684755B2 (en) 1989-03-29 1989-03-29 Breathing gas supply system

Country Status (1)

Country Link
JP (1) JP2684755B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100917089B1 (en) * 2008-12-31 2009-09-15 김창용 Air respirator and clothing equipped with it

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100917089B1 (en) * 2008-12-31 2009-09-15 김창용 Air respirator and clothing equipped with it

Also Published As

Publication number Publication date
JP2684755B2 (en) 1997-12-03

Similar Documents

Publication Publication Date Title
US5642729A (en) Gas supply systems
AU2021201685B2 (en) Oxygen concentrating self-rescuer device
US6666039B2 (en) Aircraft air conditioner
JP2005516743A (en) Life support system for aircraft
US20040094201A1 (en) Fuel tank safety system
EP2679281B1 (en) Emergency oxygen supply mask and emergency oxygen supply arrangement adapted for rescuing a passenger of an aircraft in an emergency situation, method of rescuing a passenger of an aircraft in an emergency situation
US8210175B2 (en) Method and apparatus for emergency supply of oxygen in an aircraft
US4461155A (en) Aircraft cabin ventilation system
EP1273515A2 (en) Aircraft air conditioner
US7089933B2 (en) CO2 sorbent for inhalation drug therapy system
KR102256728B1 (en) Moisture Resistance Molecular Filter Bed
JPH02256595A (en) Aspiration gas feeding system
JP4345917B2 (en) Gas generation system and gas generation method
JP4174606B2 (en) Air conditioner for aircraft
JP2585698Y2 (en) Breathing gas supply system
JP4182350B2 (en) Air conditioner for aircraft
US7442238B2 (en) Means for air fractionization
JP2764956B2 (en) Aircraft passenger breathing system
JP2789638B2 (en) Breathing gas supply system
JPH05137941A (en) Adsorption type gas separation equipment
JPH077972Y2 (en) Breathing air generator
JPH02241896A (en) Gas feeding system for breathing
JP2560356Y2 (en) Breathing air generator
JPH0727945Y2 (en) Aircraft expiratory regeneration device
JP2003312594A (en) Air conditioner for aircraft