WO1991017081A1 - Respiratory apparatus used in water - Google Patents
Respiratory apparatus used in water Download PDFInfo
- Publication number
- WO1991017081A1 WO1991017081A1 PCT/JP1990/000550 JP9000550W WO9117081A1 WO 1991017081 A1 WO1991017081 A1 WO 1991017081A1 JP 9000550 W JP9000550 W JP 9000550W WO 9117081 A1 WO9117081 A1 WO 9117081A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- gas
- hollow fiber
- fiber membrane
- inlet
- exchange module
- 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.)
- Ceased
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Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63C—LAUNCHING, HAULING-OUT, OR DRY-DOCKING OF VESSELS; LIFE-SAVING IN WATER; EQUIPMENT FOR DWELLING OR WORKING UNDER WATER; MEANS FOR SALVAGING OR SEARCHING FOR UNDERWATER OBJECTS
- B63C11/00—Equipment for dwelling or working underwater; Means for searching for underwater objects
- B63C11/46—Divers' sleds or like craft, i.e. craft on which man in diving-suit rides
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63C—LAUNCHING, HAULING-OUT, OR DRY-DOCKING OF VESSELS; LIFE-SAVING IN WATER; EQUIPMENT FOR DWELLING OR WORKING UNDER WATER; MEANS FOR SALVAGING OR SEARCHING FOR UNDERWATER OBJECTS
- B63C11/00—Equipment for dwelling or working underwater; Means for searching for underwater objects
- B63C11/02—Divers' equipment
- B63C11/18—Air supply
- B63C11/184—Artificial gills
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B63—SHIPS OR OTHER WATERBORNE VESSELS; RELATED EQUIPMENT
- B63C—LAUNCHING, HAULING-OUT, OR DRY-DOCKING OF VESSELS; LIFE-SAVING IN WATER; EQUIPMENT FOR DWELLING OR WORKING UNDER WATER; MEANS FOR SALVAGING OR SEARCHING FOR UNDERWATER OBJECTS
- B63C11/00—Equipment for dwelling or working underwater; Means for searching for underwater objects
- B63C11/02—Divers' equipment
- B63C11/18—Air supply
- B63C11/22—Air supply carried by diver
- B63C11/24—Air supply carried by diver in closed circulation
Definitions
- the present invention relates to a breathing apparatus with a moving device that can be used for a long time when diving underwater.
- the present invention also relates to a portable respiratory apparatus that can be worn on a human body during underwater diving and used.
- a person usually inhales air containing about 20.8 vol% of oxygen and about 0.03 vol% of carbon dioxide as inhaled air, and a mixed gas of about 16.4 vol% of oxygen and about 4.1 vol% of carbon dioxide. Is exhaled.
- an underwater structure that provides a living space for humans in the water is disclosed in Japanese Patent Publication No. 56-35488.
- those that are used by attaching to the human body instead of oxygen cylinders are described in JP-B-42-14589, JP-B-50-37956, USP 3,228,394, It is disclosed in USP 3,318,306.
- a gas exchange membrane made of silicone rubber is used. ⁇ ⁇ ⁇ ⁇ m.
- An object of the present invention is to provide a respiratory apparatus with a moving device that can extend the dive time of a diver.
- Another object of the present invention is to provide a portable underwater breathing apparatus that is compact and has excellent gas exchange efficiency.
- the breathing apparatus with the underwater moving device of the present invention has a built-in hollow fiber membrane, and has a gas inlet and a gas outlet.
- a gas exchange module A, an air reservoir B with an inlet and an outlet, and a gas outlet with a valve that opens only during exhalation and a gas inlet with a valve that opens only during inhalation The mouthpiece C is connected to the inlet and outlet in series, and an assembly is attached to the underwater moving device D.
- the portable breathing apparatus of the present invention has a hollow fiber membrane, a gas exchange module A having a gas inlet and a gas outlet, an air reservoir B having an inlet and an outlet, and a valve that opens only when exhalation is discharged.
- Mouthpiece C equipped with a gas inlet with a gas outlet and a valve that opens only at the time of intake, a baggage E for carrying an air reservoir B, and a gas exchange module A and an air reservoir B It has a fixing belt F for fixing, and the inlet and outlet of each of the gas exchange module A, the air reservoir B and the mouthpiece C are connected in series.
- FIG. 1 to 8 are drawings related to the respirator with the underwater moving device
- FIG. 1 is a schematic diagram showing the entire image of the respirator with the underwater moving device
- FIG. 2 is X— in FIG.
- FIG. 4 is a schematic cross-sectional view of the X ′ cross section viewed in the direction of the arrow.
- FIG. 3 is an enlarged schematic cross-sectional view of the gas exchange module in FIG. 2, and most of the hollow fiber membranes are not shown.
- the 4th The figure is an external view of the gas exchange module A in which the perforated container has a double frusto-conical structure.
- FIG. 5 is a schematic side view of a gas exchange module A having a double cylindrical structure with a baffle plate, and FIG.
- FIG. 6 is a schematic view of the gas exchange module A as viewed from behind.
- FIGS. 7 and 8 are schematic side views of a gas exchange module A in which two fixing members are fixed by plate-like supporting members, in which the illustration of the hollow fiber membrane is omitted.
- FIG. 9 is a schematic diagram showing an example of a portable respirator.
- the breathing apparatus with a moving device is basically configured such that an assembly including a gas exchange module A, an air reservoir B and a mouthpiece C is attached to the underwater moving device D.
- the gas exchange module A has a large number of hollow fiber membranes arranged in a bundle, two fixing members that fix both ends of the hollow fiber membrane with both ends opened, and two fixing members joined to both ends.
- a porous container containing a hollow fiber membrane inside, or two fixing members are joined to both ends, and a supporting member that fixes the positional relationship between the fixing members.
- a gas introduction unit having a gas communication inlet and an inlet for gas inflow, and a gas discharge unit joined to the other fixing member and communicating with the hollow portion of the hollow fiber membrane and having an outlet for gas outflow.
- 1 is a hollow fiber membrane
- 2 is a gas inlet of a gas exchange module
- 3 is a gas outlet
- 4 is a fixing member
- 5 is a porous container
- 6 is a gas inlet of an air reservoir
- 7 is a gas inlet.
- Outlet, 8 is a bellows (air reservoir)
- 9 is the mouthpiece inlet
- 10 is the gas inlet of the mousepiece
- 11 is the gas outlet
- 12 is the underwater moving device main body
- 13 is for operation Handle
- 14 for screw
- 15 for power switch 16 for air reservoir fixed belt
- 17 for mouthpiece fixed belt
- 18 for water inlet to screen Express.
- FIG. 3 is an enlarged view of the gas exchange module in FIG. 2, in which a bundle of hollow fiber membranes 1 is housed in a cylindrical porous container 5.
- the gas exchange module has a structure in which a plurality of gas exchange modules are housed between two net-like objects 19 and 20 arranged substantially concentrically.
- the net-like objects 19 and 20 in FIG. 3 may be used as a porous container, and a bundle of hollow fiber membranes may be housed in this double cylindrical porous container to form a gas exchange module.
- the porous container has a porous structure in order to facilitate the flow, movement and exchange of water around the hollow fiber membrane. It protects the hollow fiber membrane and also provides a gas exchange module A for the whole. Physical It has the role of maintaining the structure.
- the gas exchange module is placed at a location where the water around the hollow fiber membrane is easily exchanged, and that the water flow due to the rotation of the screw 14 of the submersible moving device is positively controlled. Available locations are preferred. However, it is preferable to consider this point if it is placed at the position (just behind) where the water flow by the screw directly hits, because the propulsion will be obstructed. For example, as shown in Fig. 2, if the gas exchange module is arranged behind the screen so that the water flow from the screen is wound in a cylindrical shape, the screw can be propelled. It is possible to easily exchange water around the hollow fiber membrane without lowering the force. Further, the gas exchange module may be arranged at the position of the water inlet 18 in front of the screen.
- Fig. 4 shows a schematic external view of the gas exchange module A in which the perforated container has a double frusto-conical structure.
- the diameter of the cone gradually decreases along the direction of the water flow, and the exchange of water around the hollow fiber membrane by the screw water flow is easier than in the double cylindrical structure. You can go to The method of narrowing the diameter of the cone can be appropriately changed depending on the strength of the water flow of the screw.
- a baffle plate 21 for disturbing the water flow is provided at the outlet of the propulsion water flow. Have been.
- a baffle plate 21 for disturbing the water flow is provided at the outlet of the propulsion water flow.
- the hollow fiber membrane is housed in the porous container, but a structure using a support member 22 instead of the porous container may be adopted.
- the supporting member 22 has a role of holding the fixing members 4 and 4 ′ at a predetermined interval, and is usually fixed to the outer peripheral portion of the two fixing members as a plurality of rods or plate-like objects. . It is preferable that the surface and side surfaces of the support member are smoothly processed to prevent damage to the hollow fiber membrane.
- the shape of the support member may be another shape.
- Ri Contact shown hollow fiber membrane 1 between two fixing members length 4, 4 1 of the distance to about 1 to 5% of a long gas exchange module A, six Are arranged at equal intervals on the circumference. 7 and 8 show the state of the hollow fiber membrane when the underwater moving device D is stopped and when it is activated, respectively. During operation, the water flow causes the bundle of hollow fiber membranes to swell outward, and water around the hollow fiber membrane can be easily exchanged. As shown in these figures, if the length of the hollow fiber membrane is 1 to 50% longer than the distance between the two fixing members 4 and 4 ', the hollow fiber membrane is shaken by the water flow, so that the gas Exchange Efficiency can be increased.
- Figures 7 and 8 show the gas exchange module A with different sizes of the left and right fixing members, but almost the same effect even if the left and right fixing members have the same size. Is obtained.
- the hollow fiber membrane used in the gas exchange module of the breathing apparatus of the present invention may be either a homogeneous membrane (non-porous membrane) or a microporous membrane.
- the membrane material a known material may be used, but as the homogeneous membrane material, a silicone rubber-based polymer such as polymethyl siloxane, a copolymer of silicone and polycarbonate is used.
- Polymers Polymers such as polymethyl pentene-1, low-density polyethylene, etc .: Non-fluoroalkyl-based fluorine-containing polymers; ethyl cellulose, etc. Cellulose-based polymers; Polyphenylene oxide; Poly (vinylvinylpyridine); Monomer copolymers constituting these polymers; and Mixtures thereof.
- microporous membrane material examples include polyolefins such as polyethylene, polypropylene, poly3-methylbutene-11, and poly4-methylpentene-11.
- Polymers Fluoropolymers such as fusibivinylidene and tetrafluoroethylene; hydrophobic polymers such as polystyrene and polyetheretherketone; it can .
- the oxygen permeation rate of the homogeneous membrane is preferably the above-mentioned value.
- the film thickness must be about 30 ⁇ m or less even in the case of silicone rubber, which is considered to have the highest oxygen permeation rate. Further, in the case of a copolymer of silicone and polycarbonate, it is necessary that the film thickness be 6 ⁇ or less.
- the hollow fiber membrane is configured with a homogeneous membrane layer in the middle layer and porous membrane layers in the inner and outer layers on both sides.
- a three-layer structure is preferred.
- Such a three-layered film can be obtained, for example, by a melt spinning method disclosed in US Pat. No. 4,713,292 followed by a drawing treatment.
- the air reservoir ⁇ is disposed on the outlet side or the inlet side of the mouse piece C, and has a role of temporarily storing expiration or inspiration. Therefore, it expands and contracts when breathing
- the structure has a bellows structure or a bellows structure.
- the air reservoir with a coiled tube structure is placed between each device such as between the mouse piece and the gas exchange module, the air reservoir can also serve as a connecting pipe through which gas passes, so it is compact. It is preferable to be able to design an appropriate device.
- the air reservoir has an air storage capacity of about 0.5 to 20 pounds under normal conditions.
- the material of the air reservoir B should be an elastic body that can easily expand and contract.
- the air reservoir B may be a rubber-like material such as silicone rubber, acryl rubber, or natural rubber.
- the mouthpiece C has an outlet for sending the exhaled air from the human mouth to the air reservoir B (or the gas exchange module A), and the gas exchange module A (or the air reservoir). It has an inlet for introducing respiratory (oxygen-enriched) inhalation from the bar B), and a mouth connected to the human mouth.
- a gas outlet valve that opens only at the time of exhalation discharge is provided at the outlet, and a gas inlet valve that opens only at the time of inhalation is provided at the inlet.
- the underwater moving device D connects a driving source such as a battery to water.
- the main body for isolation has a drive source, a steering wheel 13, a screw 14 for generating propulsion, and the like, and a known one is used. be able to.
- the mobile device with the respiratory device of the present invention with steam, but it may also be provided dewatering device for removing water vapor in order to prevent the breath that is saturated becomes condensed water droplets in the gas flow path c
- the portable breathing apparatus basically comprises a gas exchange module A, an air reservoir B, a mouthpiece C, a backpack E and a fixed belt F, and the expansion and contraction of the air reservoir B.
- the gas exchange module A is characterized in that it is configured to be able to swing.
- the gas exchange module A and the mouse piece C those having the same configuration as described in the respiratory apparatus with a moving device can be used, but the gas exchange module A has a hollow fiber membrane protected. Therefore, the evening eve stored in a perforated container is preferred.
- the air reservoir B may be the same as that described for the breathing apparatus with a moving device, but is shown in Fig. 9 to facilitate the swinging of the gas exchange module. It is preferable to use one having a bellows-like side wall.
- the backpack E is for mounting the air reservoir B and the gas exchange module A and mounting them on the human back. At least a plate or ladder for the backrest is used. And a pair of straps 24 for shoulder straps.
- the material of the backpack is not particularly limited, and for example, a resinous material such as polyethylene or polypropylene can be used.
- the air reservoir B is fixed directly to the backpack E, and the gas exchange module A is fixed to the backpack E via the air reservoir B. If such a fixing method is adopted, the operation of the air reservoir B, which expands and contracts repeatedly during breathing, is transmitted to the gas exchange module A, and the gas exchange module A is moved underwater, and is moved underwater. Gas exchange capacity can be improved.
- the fixing method is not particularly limited, but the gas exchange module A and the air reservoir B are usually fixed by a fixing belt F.
- the gas exchange module A and the air reservoir B and the air reservoir B and the backpack D may be fixed with the same fixed belt F. In this case, the movement of the gas exchange module A is performed in accordance with the movement of the air reservoir B.
- the fixed belt is preferably made of a material with good elasticity, such as silicone rubber or natural rubber, so that it can be tuned.
- reference numeral 24 denotes a belt for fixing the air reservoir B to the backpack
- reference numeral 25 denotes a hose.
- the gas exchange module A can be connected to a fin or the like with a string to promote the swing.
- Melt spinning and subsequent drawing process have an inner diameter of 200 ⁇ m, a porous inner layer with a thickness of 20 ⁇ , a non-porous intermediate layer with a thickness of 0.7 ⁇ , and a porous outer layer with a thickness of 20 ⁇
- a hollow fiber membrane with a three-layer structure the polymer material of the inner and outer layers is high-density polyethylene, and the polymer material of the middle layer is segmented polyurethane.
- oxygen transmission rate of 1. 1 X 10 "5 cm 3 (STP) / / cm was 2 -sec-cmHg ⁇ ⁇ ⁇ ⁇ 3 ⁇ 4 ⁇ .
- Melt spinning and subsequent drawing treatment have an inner diameter of 200 ⁇ in and a porous inner layer of 25 ⁇ , a non-porous intermediate layer of ⁇ . ⁇ , and a porous outer layer of 25 ⁇ .
- a hollow fiber membrane having an oxygen transmission rate of 4.1 ⁇ 10-cm 3 (STP) / cm 2 -sec.cmHg was obtained.
- Example 1 Using the hollow fiber membrane thus obtained, a respirator with an underwater moving device as in Example 1 was manufactured.
- a portable respirator as shown in Fig. 9 was manufactured to evaluate gas exchange capacity in water.
- a microporous hollow fiber membrane 1 made of polypropylene having an inner diameter of 200 ⁇ , a film thickness of 25 ⁇ m, an average pore diameter of 0.2 ⁇ m, and a porosity of 40% is placed in a porous container 5 made of polycarbonate.
- a gas exchange module A having a membrane area of 15 m 2 and a container of 20 pounds was manufactured.
- Air reservoir B is normal
- a bellows structure made of natural rubber with a capacity of 4 £, a backpack D made of high-density polyethylene, and a fixed belt F made of silicone rubber were used.
- This portable respirator is placed in a water tank of 100 cm in length, 100 cm in width and 60 cm in depth with the backpack facing down, and fresh tap water is poured into the water tank at a rate of 100 £ / min. While feeding, a man weighing 70 kg breathed on this respirator for 30 minutes without wearing mouthpiece C and walking underwater.
- a gas exchange module was manufactured in exactly the same manner as in Example 3 except that the three-layer hollow fiber membrane obtained in Example 2 was used in place of the porous hollow fiber membrane made of polypropylene. A respiratory device for medical use was manufactured.
- the respiratory apparatus with the underwater moving device of the present invention has excellent gas exchange performance because the water around the hollow fiber membrane is easily exchanged when moving in the water together with the underwater moving device.
- the gas exchange module is fixed to the underwater moving device, people who dive can move easily and move underwater by the underwater moving device, which reduces human oxygen consumption due to movement. Reduced dive time can be extended and the range of action can be extended.
- portable respirators equipped with backpacks have much higher gas exchange efficiency than conventional ones because the expansion and contraction of the air reservoir facilitates water exchange around the gas exchange module. . And since this device does not require any special power source, it is possible to dive for a long time.
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Abstract
Description
明 細 書 水 中 で の 呼 吸 装 置 Description Respirator in water
技 術 分 野 Technical field
本発明は水中潜水時に長時間使用可能な移動装置付 き呼吸装置に関する。 The present invention relates to a breathing apparatus with a moving device that can be used for a long time when diving underwater.
また、 本発明は水中潜水時に人体に装着して使用可 能な携帯用呼吸装置に関する。 The present invention also relates to a portable respiratory apparatus that can be worn on a human body during underwater diving and used.
背 景 技 術 Background technology
人は通常空気中において酸素濃度約 20.8 vol%、 炭 酸ガス濃度約 0.03 vol%を含有する空気を吸気と して 吸入し、 酸素濃度約 16.4 vol%、 炭酸ガス濃度約 4.1 vol %の混合気体を呼気と して排出する。 A person usually inhales air containing about 20.8 vol% of oxygen and about 0.03 vol% of carbon dioxide as inhaled air, and a mixed gas of about 16.4 vol% of oxygen and about 4.1 vol% of carbon dioxide. Is exhaled.
水中において膜を介して呼吸気と水とを接触させ、 人体から排出された呼気中の炭酸ガスを水中へ排出し 水中に溶存している酸素を呼気中へ取込みそれを吸気 と して用いる装置は古く から知られている。 例えば水 中において人の居住空間を提供する水中構造物が、 特 公昭 56— 35488 号公報に開示されている 。 ま た、 酸 素ボンベの代 り と して人体に装着して使用する もの (人工鰓) は、 特公昭 42 - 14589 号公報、 特公昭 50 - 37956 号公報、 USP 3, 228, 394 号、 USP3, 318, 306号に 開示されている。 これらの人工鰓においてはシ リ コ一 ンゴム製のガス交換膜が使用されてお り 、 その厚みは Ι Ο Ο μ m 程度である。 A device that contacts respiratory air and water in water through a membrane, discharges carbon dioxide in the exhaled breath discharged from the human body into the water, takes in oxygen dissolved in the water into the exhaled breath, and uses it as inhaled air. Has been known for a long time. For example, an underwater structure that provides a living space for humans in the water is disclosed in Japanese Patent Publication No. 56-35488. In addition, those that are used by attaching to the human body instead of oxygen cylinders (artificial gills) are described in JP-B-42-14589, JP-B-50-37956, USP 3,228,394, It is disclosed in USP 3,318,306. In these artificial gills, a gas exchange membrane made of silicone rubber is used. Ι Ο Ο μm.
このよ う なガス交換膜を用いた水中呼吸装置におい ては、 膜中の酸素透過速度がある一定値以上であれば 膜と水の界面に形成される境膜抵抗が酸素透過速度を 支配する。 従って酸素透過速度を高めるためには境膜 の厚みを減少させる こ とが必要となる。 In such an underwater breathing apparatus using a gas exchange membrane, if the oxygen permeation rate in the membrane exceeds a certain value, the membrane resistance formed at the interface between the membrane and water controls the oxygen permeation rate. . Therefore, in order to increase the oxygen transmission rate, it is necessary to reduce the thickness of the film.
しか し ながら、 ガス交換用膜モジュールを人が背 負って水中を人力のみで移動する人工鰓では膜表面の 水流の流速を高める こ とができず、 したがって境膜抵 抗を低下できないため膜モジュールの酸素透過速度が 充分でなかった。 このため適量のガス交換を行なう た めには非常に多く の膜面積が必要であ り 、 膜モジュ一 ルの大型化が避けられなかっ た。 However, artificial gills, in which a person carries a gas exchange membrane module and moves in water only by human power, cannot increase the flow velocity of the water flow on the membrane surface, and therefore cannot reduce the membrane resistance. Oxygen permeation rate was not sufficient. For this reason, an extremely large amount of membrane area is required to perform an appropriate amount of gas exchange, and an increase in the size of the membrane module was inevitable.
ま た、 人力で水中を移動する ための多 く のェネル ギー消費量、 したがって多く の酸素消費量を要するた め、 潜水時間を長く する こ とはできず水中での行動範 囲も狭かっ た。 In addition, a large amount of energy was consumed to move underwater by human power, and thus a large amount of oxygen was consumed, so that the dive time could not be extended and the range of action in water was narrow.
発 明 の 開 示 Disclosure of the invention
本発明の目的は、 ダイバーの潜水時間の長時間化が 可能な移動装置付き呼吸装置を提供する こ と にある。 An object of the present invention is to provide a respiratory apparatus with a moving device that can extend the dive time of a diver.
本発明の他の目的は、 コ ンパク トでガス交換効率の 優れた携帯用の水中呼吸装置を提供する こ と にある。 Another object of the present invention is to provide a portable underwater breathing apparatus that is compact and has excellent gas exchange efficiency.
すなわち、 本発明の水中移動装置付き呼吸装置は、 中空糸膜を内蔵し、 気体入口および気体出口を有する ガス交換モ ジ ュール A、 入口 と 出口を有する空気 リ ザ一バー B、 および呼気排出時にのみ開く 弁を有する 気体導出用の出口と吸気吸入時にのみ開く弁を有する 気体導入用の入口とを備えたマウスピース Cを各々の 入口と出口とを直列に接続してなる組立体が水中移動 装置 D に付設されて構成される。 That is, the breathing apparatus with the underwater moving device of the present invention has a built-in hollow fiber membrane, and has a gas inlet and a gas outlet. A gas exchange module A, an air reservoir B with an inlet and an outlet, and a gas outlet with a valve that opens only during exhalation and a gas inlet with a valve that opens only during inhalation The mouthpiece C is connected to the inlet and outlet in series, and an assembly is attached to the underwater moving device D.
ま た、 本発明の携帯用呼吸装置は、 中空糸膜を内 蔵 し、 気体入口および気体出口を有するガス交換モ ジュール A、 入口と出口を有する空気リザーバー B、 呼気排出時にのみ開く弁を有する気体導出用の出口お よび吸気吸入時にのみ開く弁を有する気体導入用の入 口を備えたマウス ピース C、 空気リザーバー Bを乗せ るための背負子 E、 およびガス交換モジュール A と空 気リザーバー Bを固定するための固定ベル 卜 Fを有し てな り 、 ガス交換モジュール A、 空気リ ザーバー Bお よびマウスピース Cの各々の入口と出口が直列に接続 されて構成される。 Further, the portable breathing apparatus of the present invention has a hollow fiber membrane, a gas exchange module A having a gas inlet and a gas outlet, an air reservoir B having an inlet and an outlet, and a valve that opens only when exhalation is discharged. Mouthpiece C equipped with a gas inlet with a gas outlet and a valve that opens only at the time of intake, a baggage E for carrying an air reservoir B, and a gas exchange module A and an air reservoir B It has a fixing belt F for fixing, and the inlet and outlet of each of the gas exchange module A, the air reservoir B and the mouthpiece C are connected in series.
図面の簡単な説明 BRIEF DESCRIPTION OF THE FIGURES
第 1 〜 8図は水中移動装置付き呼吸装置に関する図 面であ り 、 第 1 図は水中移動装置付き呼吸装置の全体 像を示す模式図であ り 、 第 2 図は第 1 図の X — X ' 断 面を矢印方向に見た模式断面図である。 第 3 図は第 2 図におけるガス交換モジュールの拡大模式断面図であ り 、 大部分の中空糸膜の図示は省略されている。 第 4 図は多孔容器が二重截頭円錐構造のガス交換モ ジュ一 ル Aの外観図である。 第 5図は邪魔板を付設した二重 円筒構造のガス交換モジュール Aの模式側面図を示 し、 第 6図はそれを後ろから見た模式図であ り 、 第 5 図においても大部分の中空糸膜の図示は省略されてい る、 第 7図と第 8図は 2つの固定部材が板状の支持部 材で固定されたガス交換モジュール Aの模式側面図で ある。 第 9図は携帯用呼吸装置の一例を示す模式図で ある。 1 to 8 are drawings related to the respirator with the underwater moving device, FIG. 1 is a schematic diagram showing the entire image of the respirator with the underwater moving device, and FIG. 2 is X— in FIG. FIG. 4 is a schematic cross-sectional view of the X ′ cross section viewed in the direction of the arrow. FIG. 3 is an enlarged schematic cross-sectional view of the gas exchange module in FIG. 2, and most of the hollow fiber membranes are not shown. the 4th The figure is an external view of the gas exchange module A in which the perforated container has a double frusto-conical structure. FIG. 5 is a schematic side view of a gas exchange module A having a double cylindrical structure with a baffle plate, and FIG. 6 is a schematic view of the gas exchange module A as viewed from behind. FIGS. 7 and 8 are schematic side views of a gas exchange module A in which two fixing members are fixed by plate-like supporting members, in which the illustration of the hollow fiber membrane is omitted. FIG. 9 is a schematic diagram showing an example of a portable respirator.
発明を実施するための最良の形態 BEST MODE FOR CARRYING OUT THE INVENTION
本発明の移動装置付き呼吸装置は、 基本的にはガス 交換モジュール A、 空気 リ ザーバー Bおよびマウス ピース Cからなる組立体が、 水中移動装置 D に付設さ れて構成される。 The breathing apparatus with a moving device according to the present invention is basically configured such that an assembly including a gas exchange module A, an air reservoir B and a mouthpiece C is attached to the underwater moving device D.
ガス交換モジ ュール Aは、 集束して配置された多本 数の中空糸膜、 該中空糸膜の両端を開口させたまま両 端を固定する 2つの固定部材、 2つの固定部材を両端 に接合し中空糸膜を内部に収納する多孔容器または 2 つの固定部材を両端に接合し、 固定部材間の位置関係 を固定する支持部材、 一方の固定部材に接合され、 中 空糸膜の中空部と連通しかつ気体流入用の入口を有す る気体導入部、 および他方の固定部材に接合され中空 糸膜の中空部と連通しかつ気体流出用の出口を有する 気体導出部を有して構成される。 第 1 図に示した移動装置付き呼吸装置では、 ガス交 換モジュール Aは水中移動装置 Dの後方に配置され、 空気リザーバーとマウス ピース Cはそれぞれ水中移動 装置 D の側方に配置されている。 図中、 1 は中空糸 膜、 2 はガス交換モジュールの気体導入口、 3 は気体 導出口、 4は固定部材、 5 は多孔容器、 6 は空気リザ 一バーの気体導入口、 7 は気体導出口、 8は蛇管 (空 気リザーバー) 、 9 はマウスピース嚙み口、 1 0 はマ ウス ピースの気体導入口、 1 1 は気体導出口、 1 2 は 水中移動装置本体、 1 3は操作用ハン ドル、 1 4 はス ク リ ュー、 1 5 は電源スィ ッチ、 1 6 は空気リザーバ 一固定ベル ト 、 1 7 はマウス ピース固定ベル 卜、 1 8 はスク リ ユーへの水導入部を表わす。 The gas exchange module A has a large number of hollow fiber membranes arranged in a bundle, two fixing members that fix both ends of the hollow fiber membrane with both ends opened, and two fixing members joined to both ends. A porous container containing a hollow fiber membrane inside, or two fixing members are joined to both ends, and a supporting member that fixes the positional relationship between the fixing members. A gas introduction unit having a gas communication inlet and an inlet for gas inflow, and a gas discharge unit joined to the other fixing member and communicating with the hollow portion of the hollow fiber membrane and having an outlet for gas outflow. You. In the breathing apparatus with a mobile device shown in Fig. 1, the gas exchange module A is located behind the underwater mobile device D, and the air reservoir and the mouthpiece C are each located beside the underwater mobile device D. In the figure, 1 is a hollow fiber membrane, 2 is a gas inlet of a gas exchange module, 3 is a gas outlet, 4 is a fixing member, 5 is a porous container, 6 is a gas inlet of an air reservoir, 7 is a gas inlet. Outlet, 8 is a bellows (air reservoir), 9 is the mouthpiece inlet, 10 is the gas inlet of the mousepiece, 11 is the gas outlet, 12 is the underwater moving device main body, and 13 is for operation Handle, 14 for screw, 15 for power switch, 16 for air reservoir fixed belt, 17 for mouthpiece fixed belt, 18 for water inlet to screen Express.
第 3図は、 第 2 図中のガス交換モジュールの拡大図 であ り 、 中空糸膜 1 の束が円筒状の多孔容器 5内に収 納されている。 ま た、 こ こでは複数個のガス交換モ ジュールが、 ほぼ同心円状に配置された 2 つのネ ヅ 卜 状物 1 9 と 2 0 の間に収納された構造となっている。 なお、 第 3 図のネ ッ ト状物 1 9、 2 0 を多孔容器と し、 こ の二重円筒多孔容器内に中空糸膜の束を収納し てガス交換モジュールと してもよい。 多孔容器は中空 糸膜の周囲にある水の流れ、 移動、 交換を容易にする ために多孔構造とされている ものであ り 、 中空糸膜を 保護する と と もにガス交換モジュール A全体の物理的 構造を保持する役割を有している。 FIG. 3 is an enlarged view of the gas exchange module in FIG. 2, in which a bundle of hollow fiber membranes 1 is housed in a cylindrical porous container 5. Here, the gas exchange module has a structure in which a plurality of gas exchange modules are housed between two net-like objects 19 and 20 arranged substantially concentrically. In addition, the net-like objects 19 and 20 in FIG. 3 may be used as a porous container, and a bundle of hollow fiber membranes may be housed in this double cylindrical porous container to form a gas exchange module. The porous container has a porous structure in order to facilitate the flow, movement and exchange of water around the hollow fiber membrane. It protects the hollow fiber membrane and also provides a gas exchange module A for the whole. Physical It has the role of maintaining the structure.
ガス交換モジュールの配置場所は、 中空糸膜の周囲 の水が容易に交換されやすい位置に配置する こ とが好 ま し く 、 水中移動装置のスク リ ュー 1 4 の回転による 水流を積極的に利用でき る位置が好ま しい。 但し、 ス ク リ ューによる水流が直接当たる位置 (真後) に配置 する と推進力が妨害されるので、 この点を考慮する こ と が好ま し い。 例えば、 第 2 図の よ う にガス交換モ ジュールをスク リ ユーの後方であってスク リ ユーによ る 水流を円筒状に と り 巻 く よ う に配置すれば、 ス ク リ ューの推進力を低下させる こ と な く 、 中空糸膜周囲 の水の交換を容易に行なう こ とができ る。 ま た、 ガス 交換モジュールは、 スク リ ユーの前方の水流入部 1 8 の位置に配置しても よい。 It is preferable that the gas exchange module is placed at a location where the water around the hollow fiber membrane is easily exchanged, and that the water flow due to the rotation of the screw 14 of the submersible moving device is positively controlled. Available locations are preferred. However, it is preferable to consider this point if it is placed at the position (just behind) where the water flow by the screw directly hits, because the propulsion will be obstructed. For example, as shown in Fig. 2, if the gas exchange module is arranged behind the screen so that the water flow from the screen is wound in a cylindrical shape, the screw can be propelled. It is possible to easily exchange water around the hollow fiber membrane without lowering the force. Further, the gas exchange module may be arranged at the position of the water inlet 18 in front of the screen.
第 4 図は、 多孔容器が二重截頭円錐構造であるガス 交換モジ ュール Aの模式外観図を示している。 このガ ス交換モジュール Aは水流の方向に沿っ て円錐の直径 が序々 に小さ く なつてお り 、 スク リ ューの水流による 中空糸膜周辺の水の交換が二重円筒構造に比べて更に 容易に行な う こ とができ る。 円錐の直径の絞 り方につ いてはスク リ ユーの水流の強さ等によっ て適宜変える こ と がで き る。 Fig. 4 shows a schematic external view of the gas exchange module A in which the perforated container has a double frusto-conical structure. In this gas exchange module A, the diameter of the cone gradually decreases along the direction of the water flow, and the exchange of water around the hollow fiber membrane by the screw water flow is easier than in the double cylindrical structure. You can go to The method of narrowing the diameter of the cone can be appropriately changed depending on the strength of the water flow of the screw.
第 5 図のガス交換モジュール A においては、 推進水 流の出口部に、 水流を乱すための邪魔板 2 1 が付設さ れている。 二重円筒構造または截頭円錐構造のガス交 換モジュール Aにこのよ う な邪魔板を設ける こ と によ り 、 中空糸膜の周辺の水の交換を更に容易に行なう こ とができる。 In the gas exchange module A in Fig. 5, a baffle plate 21 for disturbing the water flow is provided at the outlet of the propulsion water flow. Have been. By providing such a baffle plate in the gas exchange module A having a double cylindrical structure or a frusto-conical structure, water exchange around the hollow fiber membrane can be performed more easily.
上述したガス交換モジュール A において中空糸膜は 多孔容器内に収納されていたが、 多孔容器の代り に支 持部材 2 2 を用いた構造とする こ と もできる。 支持部 材 2 2 は固定部材 4、 4 ' 相互を所定間隔に保持する 役割を有する ものであって、 通常複数本の棒または板 状物と して 2つの固定部材の外周部に固定される。 中 空糸膜の損傷防止のため支持部材の表面や側面は滑ら かに加工してある こ とが好ま しい。 支持部材の形状は 他の形状であってもよい。 In the above-described gas exchange module A, the hollow fiber membrane is housed in the porous container, but a structure using a support member 22 instead of the porous container may be adopted. The supporting member 22 has a role of holding the fixing members 4 and 4 ′ at a predetermined interval, and is usually fixed to the outer peripheral portion of the two fixing members as a plurality of rods or plate-like objects. . It is preferable that the surface and side surfaces of the support member are smoothly processed to prevent damage to the hollow fiber membrane. The shape of the support member may be another shape.
第 7図と第 8図においては、 中空糸膜 1 の長さが 2 つの固定部材間 4、 4 1 の距離に対し約 1 5 %程度長い ガス交換モジュール Aが示されてお り 、 6本の支持部 材が円周上に等間隔で配置されている。 また、 第 7図 と第 8図はそれぞれ水中移動装置 Dの停止時と作動時 における中空糸膜の状態を示している。 作動時には水 流によって中空糸膜の束が外側にふく らんだ状態にな り 中空糸膜周辺の水の交換を容易に行なう こ とができ る。 また、 これらの図に示すよ う に 2つの固定部材 4 と 4 ' の間の距離よ り も中空糸膜の長さを 1〜5 0 %長 く する と水流によって中空糸膜が揺れるためガス交換 効率を高める こ と ができ る。 In FIG. 7 and FIG. 8, Ri Contact shown hollow fiber membrane 1 between two fixing members length 4, 4 1 of the distance to about 1 to 5% of a long gas exchange module A, six Are arranged at equal intervals on the circumference. 7 and 8 show the state of the hollow fiber membrane when the underwater moving device D is stopped and when it is activated, respectively. During operation, the water flow causes the bundle of hollow fiber membranes to swell outward, and water around the hollow fiber membrane can be easily exchanged. As shown in these figures, if the length of the hollow fiber membrane is 1 to 50% longer than the distance between the two fixing members 4 and 4 ', the hollow fiber membrane is shaken by the water flow, so that the gas Exchange Efficiency can be increased.
第 7 図 と第 8 図 に は左右の固定部材のサイ ズが異 なっ たガス交換モジュール Aが示されているが、 左右 の固定部材のサイ ズが同 じ構造であってもほぼ同様の 効果が得られる。 Figures 7 and 8 show the gas exchange module A with different sizes of the left and right fixing members, but almost the same effect even if the left and right fixing members have the same size. Is obtained.
本発明の呼吸装置のガス交換モジュールで用い られ る中空糸膜は、 均質膜 (非多孔質膜) ま たは微多孔質 膜のいずれであって も よい。 The hollow fiber membrane used in the gas exchange module of the breathing apparatus of the present invention may be either a homogeneous membrane (non-porous membrane) or a microporous membrane.
膜素材と しては公知のものを用いう るが、 均質膜の 膜素材と してはポ リ ジメ チルシロ キサン、 シ リ コーン と ポ リ カーボネー ト の共重合体等のシ リ コーン ゴム系 ポ リ マー ; ポ リ 4 ーメ チルペンテン一 1 、 低密度ポ リ エチ レン等のォ レフ ィ ン系ポ リ マー : ノ 一フ ロ ロ アル キル系フ ヅ素含有ポ リ マー ; ェチルセルロース等のセ ルロース系ポ リ マー ; ポ リ フ エ二レンォキサイ ド ; ポ リ 4 一ビニルピ リ ジン ; これらの重合体を構成する単 量体の共重合体 ; あるいはこれらの混合物を挙げる こ と ができ る。 ま た、 微多孔質膜の膜素材と しては、 ポ リ エチ レン、 ポ リ プロ ピレン、 ポ リ 3 —メ チルブテン 一 1 、 ポ リ 4 ーメ チルペンテン一 1 等のポ リ オ レフ ィ ン系ポ リ マー : フ ツイヒビニ リ デン、 テ ト ラ フ ロ ロェチ レン等フ ッ素系ポ リ マー ; ポ リ スチ レン、 ポ リ エーテ ルエーテルケ 卜 ン等の疎水性ポ リ マ一を挙げる こ とが でき る 。 均質膜を用いる場合は、 空気中における空気透過時 の酸素透過速度がおよそ 10_ 5cm3 (STPi Zcn^ 'sec'cmHg 以上であれば、 水中における酸素透過時の酸素透過速 度が境膜抵抗のみに支配される こ と になる ので、 均質 膜の酸素透過速度は前述の値である こ と が好ま しい。 As the membrane material, a known material may be used, but as the homogeneous membrane material, a silicone rubber-based polymer such as polymethyl siloxane, a copolymer of silicone and polycarbonate is used. Polymers: Polymers such as polymethyl pentene-1, low-density polyethylene, etc .: Non-fluoroalkyl-based fluorine-containing polymers; ethyl cellulose, etc. Cellulose-based polymers; Polyphenylene oxide; Poly (vinylvinylpyridine); Monomer copolymers constituting these polymers; and Mixtures thereof. Examples of the microporous membrane material include polyolefins such as polyethylene, polypropylene, poly3-methylbutene-11, and poly4-methylpentene-11. Polymers: Fluoropolymers such as fusibivinylidene and tetrafluoroethylene; hydrophobic polymers such as polystyrene and polyetheretherketone; it can . When using a homogeneous film, as long as the oxygen transmission rate at the time of air permeation is about 10 _ 5 cm 3 (STPi Zcn ^ 'sec'cmHg more in air, the oxygen permeability speed during oxygen permeation in water is boundary film Since the resistance is governed only by the resistance, the oxygen permeation rate of the homogeneous membrane is preferably the above-mentioned value.
このよ う な条件を満たすためには酸素透過速度が最 も大き い と されている シ リ コーン ゴムの場合で も膜厚 を約 30 μ m 以下 と し なければな ら ない。 ま た、 シ リ コーン と ポ リ カーボネー 卜 の共重合体の場合には、 膜 厚を 6 μ ιη 以下と する こ と が必要と なる。 In order to satisfy these conditions, the film thickness must be about 30 μm or less even in the case of silicone rubber, which is considered to have the highest oxygen permeation rate. Further, in the case of a copolymer of silicone and polycarbonate, it is necessary that the film thickness be 6 μιη or less.
いずれに して も均質膜の薄層化が必要と なるが、 そ の場合の中空糸膜の形態と しては中間層が均質膜層で その両側の内層 と外層に多孔質膜層が配置された三層 構造の も のが好適であ る 。 こ の よ う な三層構造の膜 は、 例えば USP 4, 713, 292 号に開示された溶融紡糸と それに続く 延伸処理によ る方法によ っ て得る こ と がで き る。 In any case, it is necessary to reduce the thickness of the homogeneous membrane, but in such a case, the hollow fiber membrane is configured with a homogeneous membrane layer in the middle layer and porous membrane layers in the inner and outer layers on both sides. A three-layer structure is preferred. Such a three-layered film can be obtained, for example, by a melt spinning method disclosed in US Pat. No. 4,713,292 followed by a drawing treatment.
一方、 微多孔質膜を用いる場合は、 呼吸装置を使用 する水中の水圧 (水深) とガス透過速度の両者を考慮 し て適当な細孔径を有す る も のを適宜選択すればよ い 0 On the other hand, in the case of using a microporous membrane, have yo be selected from even that consider water pressure to use breathing apparatus and (depth) of both of the gas permeation rate having a suitable pore size appropriately 0
空気 リ ザーバー Β は、 マウ ス ピース C の出口側ま た は入口側に配設され、 呼気ま たは吸気を一時的に貯蔵 する役割を有する 。 し たがっ て、 呼吸時に膨張、 収縮 する構造である こ と が好ま し く 、 例えば蛇腹構造や、 蛇管構造のものが挙げられる。 特に蛇管構造の空気リ ザ一バーはマ ウ ス ピース と ガス交換モジ ュールの間等 の各装置間に配置すれば空気 リ ザーバーが気体を通す 連結管を兼ねる こ とができ る ためコ ンパク ト な装置を 設計する こ と がで き好ま しい。 空気 リザーバーの空気 貯蔵容量と しては、 常態での容積が 0 . 5〜2 0 £程度で ある こ とが好ま しい。 The air reservoir Β is disposed on the outlet side or the inlet side of the mouse piece C, and has a role of temporarily storing expiration or inspiration. Therefore, it expands and contracts when breathing Preferably, the structure has a bellows structure or a bellows structure. In particular, if the air reservoir with a coiled tube structure is placed between each device such as between the mouse piece and the gas exchange module, the air reservoir can also serve as a connecting pipe through which gas passes, so it is compact. It is preferable to be able to design an appropriate device. Preferably, the air reservoir has an air storage capacity of about 0.5 to 20 pounds under normal conditions.
ま た、 呼吸時の抵抗を極力抑制する ためには水圧と 同 じ圧力下で呼吸でき る こ とが好ま しいので、 空気リ ザ一バー B の材質は膨張、 収縮が容易な弾性体とする こ と が好ま し く 、 空気リ ザーバー B と しては例えばシ リ コ ーン ゴム、 アク リ ルゴム、 天然ゴム等のゴム状素 材のものを用いる こ とができ る。 In order to minimize the resistance during breathing, it is preferable to be able to breathe under the same pressure as the water pressure.Therefore, the material of the air reservoir B should be an elastic body that can easily expand and contract. Preferably, the air reservoir B may be a rubber-like material such as silicone rubber, acryl rubber, or natural rubber.
マ ウ ス ピース C は、 人の口から排出された呼気を空 気 リ ザ一バー B (ま たはガス交換モジュール A ) へ送 り 出す 出口、 ガス交換モ ジ ュール A ( ま たは空気 リ ザ一バー B ) から呼吸用の (酸素富化された) 吸気を 導入する ための入口、 更に人間の口に接続される嚙み 口を有する ものである。 呼吸気を一方向へのみ流すた めに、 出口では呼気排出時にのみ開く 気体導出弁が、 ま た入口には吸気導入時にのみ開く 気体導入弁が設け られている。 The mouthpiece C has an outlet for sending the exhaled air from the human mouth to the air reservoir B (or the gas exchange module A), and the gas exchange module A (or the air reservoir). It has an inlet for introducing respiratory (oxygen-enriched) inhalation from the bar B), and a mouth connected to the human mouth. In order to allow the respiratory gas to flow in only one direction, a gas outlet valve that opens only at the time of exhalation discharge is provided at the outlet, and a gas inlet valve that opens only at the time of inhalation is provided at the inlet.
水中移動装置 D は、 バッ テ リ ー等の駆動源と水と を 隔離する ための本体に、 駆動源、 操縦用ノ\ ン ドル 1 3 および推進力を生じさせるスク リ ユ ー 1 4等を有して な る も のであ り 、 公知の も のを使用す る こ と がで き る。 The underwater moving device D connects a driving source such as a battery to water. The main body for isolation has a drive source, a steering wheel 13, a screw 14 for generating propulsion, and the like, and a known one is used. be able to.
ま た、 本発明の移動装置付き呼吸装置には、 水蒸気 で、 飽和された呼気が気体流路内で凝縮し水滴と なる のを防ぐために水蒸気を除去する除水器を設けて もよ い c Also, the mobile device with the respiratory device of the present invention, with steam, but it may also be provided dewatering device for removing water vapor in order to prevent the breath that is saturated becomes condensed water droplets in the gas flow path c
次に、 水中潜水時に人体に装着して使用される本発 明の携帯用呼吸装置を第 9 図によ っ て説明する。 Next, the portable respirator of the present invention, which is used while worn on the human body during diving underwater, will be described with reference to FIG.
本発明の携帯用呼吸装置は、 基本的にはガス交換モ ジュール A、 空気 リ ザーバー B 、 マウス ピース C、 背 負子 Eおよび固定ベル 卜 F からな り 、 空気 リ ザ一バ一 B の伸縮によ っ てガス交換モジュール Aを揺動させる こ と ができ る よ う 構成されている点に特徴を有してい る 。 The portable breathing apparatus according to the present invention basically comprises a gas exchange module A, an air reservoir B, a mouthpiece C, a backpack E and a fixed belt F, and the expansion and contraction of the air reservoir B. Thus, the gas exchange module A is characterized in that it is configured to be able to swing.
ガス交換モジ ュール A お よびマ ウ ス ピース C と して は、 移動装置付き呼吸装置において説明 し た と 同様な 構成の ものが使用でき るが、 ガス交換モジュール Aは 中空糸膜が保護されるので多孔容器中に収納された夕 イ ブのものが好ま しい。 As the gas exchange module A and the mouse piece C, those having the same configuration as described in the respiratory apparatus with a moving device can be used, but the gas exchange module A has a hollow fiber membrane protected. Therefore, the evening eve stored in a perforated container is preferred.
空気 リ ザーバ一 B も、 移動装置付き呼吸装置におい て説明 し た と 同様なものが使用でき るが、 ガス交換モ ジュールの揺動を容易にする ために、 第 9 図に示され る よ う な蛇腹構造の側壁を有する ものが好ま しい。 背負子 E は空気 リ ザ一バー B とガス交換モジュール A と を載せこれらを人間の背中に装着する ためのもの であ り 、 少な く と も背あて用の板状体若し く はは しご と肩かけ用の一対のひも 2 4 と を有する。 背負子の材 質は特に限定されず、 例えばポ リ エチ レン、 ポ リ プロ ピレン等の樹脂製のものを用いる こ と ができ る。 The air reservoir B may be the same as that described for the breathing apparatus with a moving device, but is shown in Fig. 9 to facilitate the swinging of the gas exchange module. It is preferable to use one having a bellows-like side wall. The backpack E is for mounting the air reservoir B and the gas exchange module A and mounting them on the human back. At least a plate or ladder for the backrest is used. And a pair of straps 24 for shoulder straps. The material of the backpack is not particularly limited, and for example, a resinous material such as polyethylene or polypropylene can be used.
空気 リ ザ一バー B は直接背負子 E に固定され、 ガス 交換モジュール Aは空気 リ ザーバー B を介して背負子 E に固定される。 このよ う な固定方法を採用すれば、 呼吸時に膨張と収縮を繰 り返す空気 リ ザーバー B の運 動をガス交換モジュール A に伝えてガス交換モジュ一 ル Aを水中で運動させ、 水中でのガス交換能を向上さ せる こ と ができ る。 これらの固定方法は特に限定され ないが、 通常ガス交換モジュール A と空気 リ ザーバ一 B は固定ベル ト F に よ っ て固定さ れる 。 ガス交換モ ジュール A と空気 リ ザーバー B および空気 リ ザーバー B と背負子 D は同一の固定ベル 卜 Fで固定して も よい が、 その場合は空気 リ ザーバー B の動き にガス交換モ ジュール Aの動きが同調でき る よ う に、 固定ベル ト は シ リ コ ン ゴム、 天然ゴム等の伸縮性の良好な素材から なる もの とする こ とが好ま しい。 なお、 図中 2 4 は空 気リ ザ一バー B を背負子に固定するベル ト 、 2 5 はホ —スを表わす。 ま た、 ガス交換モジュール A を足ヒ レ等と ひもで接 続してその揺動を促進する こ と もで き る。 The air reservoir B is fixed directly to the backpack E, and the gas exchange module A is fixed to the backpack E via the air reservoir B. If such a fixing method is adopted, the operation of the air reservoir B, which expands and contracts repeatedly during breathing, is transmitted to the gas exchange module A, and the gas exchange module A is moved underwater, and is moved underwater. Gas exchange capacity can be improved. The fixing method is not particularly limited, but the gas exchange module A and the air reservoir B are usually fixed by a fixing belt F. The gas exchange module A and the air reservoir B and the air reservoir B and the backpack D may be fixed with the same fixed belt F. In this case, the movement of the gas exchange module A is performed in accordance with the movement of the air reservoir B. The fixed belt is preferably made of a material with good elasticity, such as silicone rubber or natural rubber, so that it can be tuned. In the figure, reference numeral 24 denotes a belt for fixing the air reservoir B to the backpack, and reference numeral 25 denotes a hose. In addition, the gas exchange module A can be connected to a fin or the like with a string to promote the swing.
以下、 本発明の呼吸装置につき、 実施例に し たがい よ り 具体的に説明する。 Hereinafter, the respiratory apparatus of the present invention will be described more specifically with reference to examples.
実施例 1 Example 1
溶融紡糸と それに続く 延伸処理によ っ て内径が 200 μ m で、 20μ ηι の厚みの多孔質内層、 0.7 μ πι の厚み の非多孔質中間層、 20μ πι の厚みの多孔質外層を有す る 三層構造の中空糸膜であ っ て、 内層 と 外層のポ リ マー素材が高密度ポ リ エチ レン、 中間層のポ リ マー素 材がセグメ ン ト 化ポ リ ウ レタ ンであ り 、 酸素透過速度 が 1. 1 X 10"5cm3 (STP) //cm2 -sec-cmHg© Φ^^ΙΙ ¾ί た。 Melt spinning and subsequent drawing process have an inner diameter of 200 μm, a porous inner layer with a thickness of 20 μηι, a non-porous intermediate layer with a thickness of 0.7 μπι, and a porous outer layer with a thickness of 20 μπι A hollow fiber membrane with a three-layer structure, the polymer material of the inner and outer layers is high-density polyethylene, and the polymer material of the middle layer is segmented polyurethane. oxygen transmission rate of 1. 1 X 10 "5 cm 3 (STP) / / cm was 2 -sec-cmHg © Φ ^^ ΙΙ ¾ί.
このよ う に して得られた中空糸膜を内径 65mm、 全長 450mm のポ リ カーボネー ト製多孔容器 5 内に収納した ガス交換モジュールを 24本製作し、 これらを更に二重 管構造のネ ツ 卜状物 1 9 および 2 0 にほぼ均等に配'置 収納して膜面積 15m2のガス交換モジュール (群) と し た。 ま た、 空気 リ ザーバー と し て常態での容積が 4 の天然ゴム製蛇管構造の も のを用 い、 ガス交換モ ジュール、 空気 リ ザーバーおよびマウ ス ピースを市販 の水中移動装置 (株式会社アポロスポーツ製、 アポロ スクーター A V — 1 ) に据え付け第 1 図に示すよ う な 水中移動装置付き呼吸装置を製作し た。 この呼吸装置を用いて体重 70kgの男性が水中 (水深 約 5m ) を 2. 0 Km/Hr の速度で 60分間走行し た と こ ろ、 何ら問題を起こすこ となく 呼吸可能であっ た。 実施例 2 Twenty-four gas exchange modules containing the hollow fiber membrane obtained in this way in a polycarbonate porous container 5 having an inner diameter of 65 mm and a total length of 450 mm were manufactured, and these were further formed into a double-pipe net. A gas exchange module (group) with a membrane area of 15 m 2 was arranged and stored almost evenly in the burrs 19 and 20. In addition, a natural rubber serpentine tube structure with a normal volume of 4 was used as the air reservoir, and the gas exchange module, air reservoir, and mousepiece were purchased from a commercial underwater vehicle (Apollo Co., Ltd.). Installed on an Apollo scooter AV-1) made of sports, a respirator with a water moving device as shown in Fig. 1 was manufactured. Using this respirator, a man weighing 70 kg ran in water (at a depth of about 5 m) at a speed of 2.0 Km / Hr for 60 minutes and was able to breathe without any problems. Example 2
溶融紡糸とそれに続く延伸処理によって内径が 200 μ in で、 25μ ηι の厚みの多孔質内層、 Ο. ΐ μ πι の厚み の非多孔質中間層、 25μ ηι の厚みの多孔質外層を有す る三層構造の中空糸膜であっ て、 内層と外層のポ リ マ一素材がポ リ 4 ーメチルペンテン— 1 、 中間層のポ リ マー素材がシ リ コーン とポ リ カーボネー 卜 の共重合 体であ り 、 酸素透過速度が 4. 1 X 10- cm3 (STP) /cm2 - sec.cmHgの中空糸膜を得た。 Melt spinning and subsequent drawing treatment have an inner diameter of 200 μin and a porous inner layer of 25 μηι, a non-porous intermediate layer of Ο.Ομπι, and a porous outer layer of 25 μηι. A hollow fiber membrane with a three-layer structure, in which the polymer material of the inner and outer layers is poly 4-methylpentene-1, and the polymer material of the middle layer is a copolymer of silicone and polycarbonate. Thus, a hollow fiber membrane having an oxygen transmission rate of 4.1 × 10-cm 3 (STP) / cm 2 -sec.cmHg was obtained.
このよ う にして得た中空糸膜を用いて実施例 1 と同 様の水中移動装置付き呼吸装置を製作した。 Using the hollow fiber membrane thus obtained, a respirator with an underwater moving device as in Example 1 was manufactured.
この呼吸装置を用いて体重 70kgの男性が水中 (水深 約 5m ) を 2. 0 Km/Hr の速度で 60分間走行した と こ ろ、 何ら問題を起こすこ となく 呼吸可能であっ た。 実施例 3 Using this respirator, a man weighing 70 kg ran in water (at a depth of about 5 m) at a speed of 2.0 Km / Hr for 60 minutes and was able to breathe without any problems. Example 3
第 9図に示すよ う な携帯用呼吸装置を製作して水中 におけるガス交換能を評価した。 内径 200 μ ιη 、 膜厚 25 μ m、平均孔径 0.2 μ m 、 空孔率 40 %のポ リ プロ ピレ ン製微多孔質中空糸膜 1 をポ リ カーボネー ト製の多孔 容器 5 に収容し、 膜面積 15m2、 容器 20£のガス交換モ ジュール Aを製作した。 空気リザーバー Bは常態での 容積が 4 £ の天然ゴム製の蛇腹構造のもの、 背負子 D は高密度ポ リ エチ レン製のもの、 ま た、 固定ベル 卜 F はシ リ コーン ゴム製のものを用いた。 A portable respirator as shown in Fig. 9 was manufactured to evaluate gas exchange capacity in water. A microporous hollow fiber membrane 1 made of polypropylene having an inner diameter of 200 μιη, a film thickness of 25 μm, an average pore diameter of 0.2 μm, and a porosity of 40% is placed in a porous container 5 made of polycarbonate. A gas exchange module A having a membrane area of 15 m 2 and a container of 20 pounds was manufactured. Air reservoir B is normal A bellows structure made of natural rubber with a capacity of 4 £, a backpack D made of high-density polyethylene, and a fixed belt F made of silicone rubber were used.
この携帯用呼吸装置を縦 100cm 、 横 100cm 、 深さ 60 cmの水槽の中に背負子が下方 と な る よ う に し て設置 し、 水槽中へ 100 £ /分の割合で新鮮な水道水を供給 しつつ、 体重 70kgの男性がマウス ピース C を装着して 水中に も ぐる こ と なく この呼吸装置で 30分間呼吸を行 なっ た。 This portable respirator is placed in a water tank of 100 cm in length, 100 cm in width and 60 cm in depth with the backpack facing down, and fresh tap water is poured into the water tank at a rate of 100 £ / min. While feeding, a man weighing 70 kg breathed on this respirator for 30 minutes without wearing mouthpiece C and walking underwater.
その間、 10分間毎にガス交換モジュール Aの気体導 出部の炭酸ガス濃度を測定し た と こ ろ、 その値は常に During that time, the carbon dioxide concentration at the gas outlet of gas exchange module A was measured every 10 minutes.
0. lvol %以下であっ た。 0. It was less than lvol%.
実施例 4 Example 4
ポ リ プロ ピレン製多孔質中空糸膜の代わ り に実施例 2 で得た三層構造の中空糸膜を用いたこ と を除き実施 例 3 と全く 同様に してガス交換モジュールを製作し、 携帯用呼吸装置を製作し た。 A gas exchange module was manufactured in exactly the same manner as in Example 3 except that the three-layer hollow fiber membrane obtained in Example 2 was used in place of the porous hollow fiber membrane made of polypropylene. A respiratory device for medical use was manufactured.
そ して実施例 3 と 同様に して この呼吸装置の性能を 評価し た と こ ろ ほぼ同様の結果が得られた。 本発明の水中移動装置付き呼吸装置は水中移動装置 と共に水中を移動する際に中空糸膜の周囲の水が容易 に交換される ためガス交換性能が優れている。 特にガ ス交換モジュールをスク リ ユーによ る水流発生部の周 囲に配置すれば更に優れたガス交換性能が達成され る。 また、 水中移動装置にガス交換モジ ュールが固定 されているため、 潜水する人間が身軽に行動できる と 共に、 水中移動装置によ り水中を移動するため移動に 伴なう人間の酸素消費量が低減された潜水時間の長時 間化や行動範囲の拡大が可能である。 When the performance of the respiratory apparatus was evaluated in the same manner as in Example 3, almost the same results were obtained. The respiratory apparatus with the underwater moving device of the present invention has excellent gas exchange performance because the water around the hollow fiber membrane is easily exchanged when moving in the water together with the underwater moving device. In particular, install the gas exchange module around the water flow generation part by the screw. If it is arranged in a surrounding area, more excellent gas exchange performance can be achieved. In addition, since the gas exchange module is fixed to the underwater moving device, people who dive can move easily and move underwater by the underwater moving device, which reduces human oxygen consumption due to movement. Reduced dive time can be extended and the range of action can be extended.
ま た、 背負子を備えた携帯用呼吸装置は、 空気リ ザ一バーの伸縮によってガス交換モジュール周辺の水 の交換が容易に行なわれるため従来のものよ り ガス交 換効率がはるかに優れている。 そしてこの装置は特別 の動力源を必要と しないため、 長時間の潜水が可能で ある。 In addition, portable respirators equipped with backpacks have much higher gas exchange efficiency than conventional ones because the expansion and contraction of the air reservoir facilitates water exchange around the gas exchange module. . And since this device does not require any special power source, it is possible to dive for a long time.
Claims
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002030804A CA2030804A1 (en) | 1990-04-27 | 1990-04-27 | Underwater breathing apparatus |
| PCT/JP1990/000550 WO1991017081A1 (en) | 1990-04-27 | 1990-04-27 | Respiratory apparatus used in water |
| AU55447/90A AU5544790A (en) | 1990-04-27 | 1990-04-27 | Respiratory apparatus used in water |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CA002030804A CA2030804A1 (en) | 1990-04-27 | 1990-04-27 | Underwater breathing apparatus |
| PCT/JP1990/000550 WO1991017081A1 (en) | 1990-04-27 | 1990-04-27 | Respiratory apparatus used in water |
| AU55447/90A AU5544790A (en) | 1990-04-27 | 1990-04-27 | Respiratory apparatus used in water |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO1991017081A1 true WO1991017081A1 (en) | 1991-11-14 |
Family
ID=27154996
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/JP1990/000550 Ceased WO1991017081A1 (en) | 1990-04-27 | 1990-04-27 | Respiratory apparatus used in water |
Country Status (3)
| Country | Link |
|---|---|
| AU (1) | AU5544790A (en) |
| CA (1) | CA2030804A1 (en) |
| WO (1) | WO1991017081A1 (en) |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101044390B1 (en) * | 2010-12-06 | 2011-06-27 | 한국기계연구원 | Breathing apparatus using hollow fiber |
| KR101051020B1 (en) * | 2010-12-24 | 2011-07-21 | 한국기계연구원 | Underwater breathing apparatus using hollow fiber membrane with radial arrangement |
| KR101076701B1 (en) * | 2011-02-17 | 2011-10-26 | 한국기계연구원 | Snorkel Using Hollow Fiber |
| KR101078280B1 (en) * | 2011-04-13 | 2011-10-31 | 한국기계연구원 | Hollow fiber membrane underwater respirator with buffer |
| KR101094939B1 (en) * | 2011-05-12 | 2011-12-15 | 한국기계연구원 | Dissolved gas distribtuing type breathing apparatus using hollow fiber |
| KR101131195B1 (en) * | 2011-06-27 | 2012-03-28 | 한국기계연구원 | Pressurizing rebreather using hollow fiber membrane |
| KR101328615B1 (en) * | 2013-06-18 | 2013-11-12 | 한국기계연구원 | Sub-marine propulsion apparatus using hollow fiber |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| ATE320961T1 (en) | 2000-11-15 | 2006-04-15 | Alan-Izhar Bodner | OPEN CIRCUIT, INDEPENDENT UNDERWATER BREATHING APPARATUS |
| GB202212475D0 (en) * | 2022-08-26 | 2022-10-12 | Amphibio Ltd | Artificial gill |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US3692026A (en) * | 1969-10-20 | 1972-09-19 | Mine Safety Appliances Co | Underwater breathing apparatus |
| JPS4930070B1 (en) * | 1969-07-16 | 1974-08-09 | ||
| JPS5219181A (en) * | 1975-08-01 | 1977-02-14 | Haidoroomemuburonikusu Inc | Separating wall for selective transportation of carbon dioxide and apparatus using it |
| JPS5957090A (en) * | 1982-08-05 | 1984-04-02 | インタ−スピロ ゲ−エムベ−ハ− | Breathing protective device suitable for use under pressure |
-
1990
- 1990-04-27 CA CA002030804A patent/CA2030804A1/en not_active Abandoned
- 1990-04-27 WO PCT/JP1990/000550 patent/WO1991017081A1/en not_active Ceased
- 1990-04-27 AU AU55447/90A patent/AU5544790A/en not_active Abandoned
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS4930070B1 (en) * | 1969-07-16 | 1974-08-09 | ||
| US3692026A (en) * | 1969-10-20 | 1972-09-19 | Mine Safety Appliances Co | Underwater breathing apparatus |
| JPS5219181A (en) * | 1975-08-01 | 1977-02-14 | Haidoroomemuburonikusu Inc | Separating wall for selective transportation of carbon dioxide and apparatus using it |
| JPS5957090A (en) * | 1982-08-05 | 1984-04-02 | インタ−スピロ ゲ−エムベ−ハ− | Breathing protective device suitable for use under pressure |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| KR101044390B1 (en) * | 2010-12-06 | 2011-06-27 | 한국기계연구원 | Breathing apparatus using hollow fiber |
| KR101051020B1 (en) * | 2010-12-24 | 2011-07-21 | 한국기계연구원 | Underwater breathing apparatus using hollow fiber membrane with radial arrangement |
| KR101076701B1 (en) * | 2011-02-17 | 2011-10-26 | 한국기계연구원 | Snorkel Using Hollow Fiber |
| KR101078280B1 (en) * | 2011-04-13 | 2011-10-31 | 한국기계연구원 | Hollow fiber membrane underwater respirator with buffer |
| KR101094939B1 (en) * | 2011-05-12 | 2011-12-15 | 한국기계연구원 | Dissolved gas distribtuing type breathing apparatus using hollow fiber |
| KR101131195B1 (en) * | 2011-06-27 | 2012-03-28 | 한국기계연구원 | Pressurizing rebreather using hollow fiber membrane |
| KR101328615B1 (en) * | 2013-06-18 | 2013-11-12 | 한국기계연구원 | Sub-marine propulsion apparatus using hollow fiber |
Also Published As
| Publication number | Publication date |
|---|---|
| CA2030804A1 (en) | 1991-10-28 |
| AU5544790A (en) | 1991-11-27 |
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