JPS62210040A - System for dissolving carbon dioxide - Google Patents

System for dissolving carbon dioxide

Info

Publication number
JPS62210040A
JPS62210040A JP5065586A JP5065586A JPS62210040A JP S62210040 A JPS62210040 A JP S62210040A JP 5065586 A JP5065586 A JP 5065586A JP 5065586 A JP5065586 A JP 5065586A JP S62210040 A JPS62210040 A JP S62210040A
Authority
JP
Japan
Prior art keywords
carbon dioxide
seawater
pressure
gas
bubbles
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
Application number
JP5065586A
Other languages
Japanese (ja)
Inventor
Yutaka Suzuki
裕 鈴木
Nobuaki Nakajima
中島 信顕
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.)
Sumitomo Heavy Industries Ltd
Original Assignee
Sumitomo Heavy Industries Ltd
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 Sumitomo Heavy Industries Ltd filed Critical Sumitomo Heavy Industries Ltd
Priority to JP5065586A priority Critical patent/JPS62210040A/en
Publication of JPS62210040A publication Critical patent/JPS62210040A/en
Pending legal-status Critical Current

Links

Landscapes

  • Physical Or Chemical Processes And Apparatus (AREA)

Abstract

PURPOSE:To completely dissolve carbon dioxide and to prevent the generation of noise accompanying with the generation of bubbles by injecting carbon dioxide wherein its pressure is regulated so as to oppose the pressure of seawater as fine bubbles into underwater through a nozzle having a porous film in a submarine boat or the like. CONSTITUTION:After carbon dioxide generated in a closed space is separated and concentrated, it is subjected to pressure regulation in coincidence with the depth of seawater through a regulator 16 for discharged pressure of carbon dioxide and injected into seawater through a nozzle 1 having a porous film. The porous film preferably has many fine holes of about <=0.2mmphi hole diameter and is constituted of a ceramic material, sintered metal and a high polymer compound substance, etc. In case of using this system for dissolving carbon dioxide, the generation of noise due to the generation of bubbles is prevented and therefore this system is extremely available as a device discharging carbon dioxide from a manned submarine boat used with an acoustic apparatus.

Description

【発明の詳細な説明】 [産業上の利用分野コ 本発明は、多孔質膜を利用した炭酸ガス溶解システムに
関する。特に、炭酸ガスを効率的に騒音発生なしに水中
に排出する炭酸ガス溶解システムに関する。
DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a carbon dioxide dissolving system using a porous membrane. In particular, the present invention relates to a carbon dioxide dissolving system that efficiently discharges carbon dioxide into water without generating noise.

[従来の技術] 炭酸ガス(CO+)は、ガス温度、圧力に応じて。[Conventional technology] Carbon dioxide (CO+) depends on gas temperature and pressure.

その水溶性能を変化させる。そして、加圧下で炭酸ガス
を海水中に放出させる場合、噴出時の騒音を伴い、その
溶解速度にもよるが、微細な気泡を発生し、この気泡が
水面に向かって上昇する際に、減圧効果により拡大し1
分裂し、気泡の発生時及び上昇時に騒音を発生ずること
となり、静粛な環境を必要とする音響管制下には、不適
当である。特に、辞響測定機器を使用する有人潜水船か
ら炭酸ガスを排出するとき、或いは、潜水船の空気清浄
装置の付属装置において、炭酸ガスを海水中に排出する
ときに、この炭酸ガス排出の際に生しる騒音は、永年問
題にされているが、解決きれていない。
Changes its water solubility. When carbon dioxide gas is released into seawater under pressure, it produces noise when ejected, and depending on its dissolution rate, it generates fine bubbles, and as these bubbles rise toward the water surface, the pressure is reduced. Expands due to effect 1
It splits and generates noise when bubbles are generated and rise, making them unsuitable for sound control systems that require a quiet environment. In particular, when carbon dioxide gas is discharged from a manned submersible that uses diaphragm measurement equipment, or when carbon dioxide gas is discharged into seawater by an attached device to the submersible's air purification system, The noise generated by the road has been a long-standing problem, but it has not been completely solved.

一方、原子力推進潜水船等においては、液体アミン式炭
酸ガス除去装置を装備しているが、原子力動力装置で発
生した大きな電力供給能力により、潜行中に吸収した炭
酸ガスを海水中に放出する処理を潜行中実流できる。こ
のため海水中に炭酸ガスを放出する際に炭酸ガス溶解処
理が必要であるが、従来、”水中噴射分散器”と呼ばれ
る鉄格子と金属網を用いた気泡細分化のための装置があ
るとする情報があった。然し乍ら、どのような装置を利
用して完全に気泡を無くすることができるかについての
具体的な情報はなかった。亦、その他の技術として、気
泡を発生すると考えられる圧縮空気を利用する装置、器
具1例えば、信号発射筒、水圧射出器などでも、気泡を
防止する手段、装置は考えられていない。
On the other hand, nuclear powered submersibles are equipped with liquid amine carbon dioxide removal equipment, which uses the large power supply capacity generated by the nuclear power equipment to release the carbon dioxide absorbed during the dive into the seawater. You can actually stream it while diving. For this reason, carbon dioxide dissolution treatment is necessary when releasing carbon dioxide into seawater, but there is a conventional device called an "underwater injection disperser" that uses iron grates and metal nets to fragment bubbles. There was information. However, there was no specific information regarding what kind of equipment could be used to completely eliminate air bubbles. In addition, as for other techniques, no means or device for preventing air bubbles has been considered even in devices and instruments 1 that utilize compressed air that are thought to generate air bubbles, such as signal launchers and hydraulic injectors.

一方、潜水船からの炭酸ガスの排出については、194
0年代に排出ガス径と気泡の状態について研究されてお
り、それによると、〔水中30フイートの場合、初期ガ
ス気泡径が0.32mm以下なら水面に気泡が現れない
こと、最も効果的な水中噴射分散器は、排出孔径1/8
イン・チであること]が明らかにされている。
On the other hand, regarding carbon dioxide emissions from submersibles, 194
In the 1990s, research was conducted on the diameter of exhaust gas and the state of bubbles, and it was found that [in the case of 30 feet underwater, if the initial gas bubble diameter is 0.32 mm or less, no bubbles will appear on the water surface; The injection disperser has a discharge hole diameter of 1/8
It has been made clear that the

[発明が解決しようとする問題点コ 本発明は、高い水溶性を有する気体である炭酸ガスを、
加圧条件下における海水中に気泡を発生させることなく
、完全に溶解させる炭酸ガス溶解システムを提供するこ
とを目的とする。更に2本発明は、ガス側と海水との境
界に”多孔質膜”物質を応用することにより、炭酸ガス
の完全溶解状態を作ることのできる炭酸ガス溶解システ
ムを提供することを目的とする。亦1本発明は、加圧状
態の海水中に完全溶解できる微細化したガス粒子を作り
出すことができる多孔質膜ノズルと、排出ガス圧力II
I整機構との組合せにより、最適な排出ガス圧力条件を
保持しながら、気泡発生と気泡浮上による音響障害の影
響を受けることなく炭酸ガスを海水中に放出し、溶解さ
せることができる炭酸ガス溶解システムを提供すること
を目的とする。
[Problems to be solved by the invention] The present invention solves the problem by using carbon dioxide, which is a gas with high water solubility,
The purpose of the present invention is to provide a carbon dioxide dissolving system that completely dissolves carbon dioxide in seawater under pressurized conditions without generating bubbles. A further object of the present invention is to provide a carbon dioxide gas dissolution system that can create a state in which carbon dioxide gas is completely dissolved by applying a "porous membrane" material to the boundary between the gas side and seawater. (1) The present invention provides a porous membrane nozzle capable of producing fine gas particles that can be completely dissolved in pressurized seawater, and an exhaust gas pressure II.
In combination with the I adjustment mechanism, carbon dioxide dissolution allows carbon dioxide to be released and dissolved into seawater while maintaining optimal exhaust gas pressure conditions and without being affected by acoustic disturbances due to bubble generation and bubble surfacing. The purpose is to provide a system.

C問題点を解決するための手段] 本発明は、炭酸ガスを水中或いは海水中に溶解させる炭
酸ガス溶解システムにおいて、炭酸ガス噴出用の多孔質
膜ノズルを備えることを特徴とする炭酸ガス溶解システ
ムである。その炭酸ガス噴出用多孔質膜は、セラミ7り
材、焼結合金、或いは高分子化合物より製造することが
できる。亦。
Means for Solving Problem C] The present invention provides a carbon dioxide dissolving system for dissolving carbon dioxide in water or seawater, which is characterized by being equipped with a porous membrane nozzle for ejecting carbon dioxide. It is. The porous membrane for ejecting carbon dioxide gas can be manufactured from a ceramic material, a sintered alloy, or a polymer compound. also.

その炭酸ガス噴出用多孔質膜より噴出したガス粒径は、
0.2mmφ以下であることが適する。
The diameter of the gas particles ejected from the porous membrane for ejecting carbon dioxide gas is
It is suitable that the diameter is 0.2 mmφ or less.

[作用コ 炭酸ガス(Co、)は、高い水溶性を有する気体の一種
であるが、加圧条件下で海水中に放出すると通常は気泡
を生じ、その気泡は水面に向かって上昇し、その際に減
圧に伴い拡大し1分裂し、気泡の発生時及び上昇時にw
A音を発生し亦、水面に泡を生しる。この騒音は、潜水
船或いは海底探査のための測量船など静粛な環境を必要
とする音響管制下の環境を乱すので、このような加圧下
の水中へ炭酸ガスを溶解吸収せしめる技術が望まれる。
[Effects] Carbon dioxide (Co) is a type of gas with high water solubility, but when released into seawater under pressurized conditions, it usually produces bubbles that rise toward the water surface and When the pressure is reduced, it expands and splits into one, and when bubbles are generated and rise,
It makes a sound and also creates bubbles on the water surface. This noise disturbs environments under acoustic control, such as submarines or survey ships for seabed exploration, which require a quiet environment, so a technology for dissolving and absorbing carbon dioxide gas into such pressurized water is desired.

本発明は、加圧下における海水中などに炭酸ガス気泡を
発生させることなく、炭酸ガスを完全に溶解させるため
に、ガス側と海水の境界に”多孔質膜”物質を置くこと
により、加圧下での炭酸ガス溶解に必要な排出ガス径の
微細化を図ったものである。この結果、加圧状態の海水
中に完全溶解できるガス粒子を作り出し、排出ガスの圧
力調整機構と組合せ、最適な排出ガス圧力条件で気泡発
生が事実上無く、騒音発生の生じない炭酸ガス排出装置
を提供できたものである。
In order to completely dissolve carbon dioxide gas without generating carbon dioxide gas bubbles in seawater under pressure, the present invention has been developed by placing a "porous membrane" material at the boundary between the gas side and seawater. This is aimed at reducing the diameter of the exhaust gas necessary for dissolving carbon dioxide gas. As a result, gas particles that can be completely dissolved in pressurized seawater are created, and in combination with an exhaust gas pressure adjustment mechanism, there is virtually no bubble generation under optimal exhaust gas pressure conditions, and a carbon dioxide gas discharge device that does not generate noise. We were able to provide the following.

本発明の炭酸ガス溶解システムは、排出ガス粒子径を微
細化するための”多孔質膜”の応用と溶解を促進させる
に適した排出ガス圧力調整装置を組合上ることによる新
規な技術である。
The carbon dioxide dissolving system of the present invention is a new technology that combines the application of a "porous membrane" to reduce the particle size of exhaust gas and an exhaust gas pressure adjustment device suitable for promoting dissolution.

潜水船、海中測量船などの海水中における閉鎖空間内で
発生する炭酸ガスは、船内に設けられた炭酸ガスを除去
し空間内の炭酸ガス濃度を低下させるための装置により
濃縮される。濃縮された炭酸ガスの圧力は、約IKgf
/cm”である。次に、a路次酸ガスは、炭酸ガス圧縮
機によって、一定圧力(即ち、炭酸ガスの排出予想の最
高圧力)に加圧される。1実施例では、加圧力を最大5
0Kgf/cn+’Gとする。炭酸ガス圧縮機は、電動
機により駆動され、振動防止と船体構造に伝播される騒
音を遮断する目的で防振台盤上に装備される。加圧され
た炭酸ガスは、炭酸ガス気蓄器に一次的に貯蔵される。
Carbon dioxide gas generated in a closed space underwater, such as a submarine or an underwater survey ship, is concentrated by a device installed inside the ship to remove carbon dioxide gas and reduce the concentration of carbon dioxide gas in the space. The pressure of concentrated carbon dioxide is approximately IKgf
/cm''.Next, the a-path suboxygen gas is pressurized to a constant pressure (i.e., the highest expected pressure for carbon dioxide gas discharge) by a carbon dioxide gas compressor.In one embodiment, the pressurizing force is Maximum 5
It is assumed to be 0Kgf/cn+'G. The carbon dioxide compressor is driven by an electric motor and is mounted on a vibration-proof platform for the purpose of preventing vibration and blocking noise propagated to the hull structure. The pressurized carbon dioxide gas is temporarily stored in a carbon dioxide gas storage device.

気蓄圧力は最大50Kgf/cm”Gにきれる。炭酸ガ
ス排出圧力′IA′vi装置は、I@水深深度より変化
する圧力を検知し、#P出する炭酸ガスが海水の圧力に
抗して、海水中に噴出する圧力に炭酸ガスを加圧或いは
減圧し調整する。排出圧力が調整された炭酸ガスは、炭
酸ガス排出室に導入される。炭酸ガス排出室の海水と直
接接触する部分は、多孔質膜であり、好適には、孔径的
0.2開φ以下の多数の倣細な孔を有するものである。
The air storage pressure can reach a maximum of 50Kgf/cm"G. The carbon dioxide discharge pressure 'IA'vi device detects the pressure that changes from the depth of the water, and the carbon dioxide gas emitted resists the pressure of seawater. The carbon dioxide gas is pressurized or depressurized to adjust the pressure to be ejected into the seawater.The carbon dioxide gas whose discharge pressure has been adjusted is introduced into the carbon dioxide gas discharge chamber.The part of the carbon dioxide gas discharge chamber that comes into direct contact with the seawater is It is a porous membrane, preferably having a large number of narrow pores with a diameter of 0.2 or less.

多孔質膜を構成する材料は1例えば、セラミ7り材、焼
結金属或いは合金、高分子化合物等である。
Examples of materials constituting the porous membrane include ceramic materials, sintered metals or alloys, and polymer compounds.

閉鎖空間例えば、潜水船、海底油田、海底鉱床等の探査
のための水中作業船などにおける炭酸ガスを船外にJJ
I出するための炭酸ガス溶解システムについて論しると
次のようである。
JJ
The following is a discussion of the carbon dioxide dissolving system for releasing I.

現在の電気推進の潜水船などの場合、炭酸ガス除去装置
は、液体アミン式炭酸ガス除去装置が一般的であり、潜
行中発生する炭酸ガスを一括して吸収処理する方式で運
用され、吸収した炭酸ガスは海水中又は潜水船が浮上航
行中に、大気中に放出される。然し乍ら、他の場合1例
えば、原子力推進潜水船においては、液体アミン式炭酸
ガス除去装置を装備しているが、原子力動力装置を持つ
ことから船内で消費する電力供給能力に大さな余裕があ
るために潜行中に吸収した炭酸ガスを放出する処理を潜
行中実流できる。このため海水中に炭酸ガスを放出する
際に炭酸ガス溶解処理が必要であり、換言すれば、気泡
対策が必要である。
In the case of current electric propulsion submersibles, the carbon dioxide removal device is generally a liquid amine type carbon dioxide removal device, which is operated in a system that absorbs and processes all the carbon dioxide gas generated during the dive. Carbon dioxide gas is released into the atmosphere in the sea or while a submersible is floating on the surface. However, in other cases 1, for example, a nuclear-powered submersible is equipped with a liquid amine carbon dioxide removal device, but since it has a nuclear power unit, there is a large margin in the power supply capacity for consumption on board. Therefore, the process of releasing carbon dioxide absorbed during the dive can be carried out during the dive. For this reason, carbon dioxide dissolution treatment is required when releasing carbon dioxide into seawater, or in other words, bubble countermeasures are required.

海水或いは水に周囲を取り囲まれた閉鎖空間の中で発生
する炭酸ガスは、炭酸ガス除去手段により環境大気より
分離され、a縮され、そのa路次酸ガスは、閉鎖空間の
外へ排出しなければならない。然し乍ら2例えば、潜水
船の場合、自船の使用する音響機器等への悪影響を避け
るために静粛な環境を作る音響管制をすることがある。
Carbon dioxide gas generated in a closed space surrounded by seawater or water is separated from the ambient air by a carbon dioxide removal means and a-condensed, and the a-path acid gas is discharged outside the closed space. There must be. However, in the case of a submersible, for example, sound control may be used to create a quiet environment in order to avoid adverse effects on the audio equipment used by the ship.

この音響管制下における炭酸ガスの排出を容易にする必
要がある。このような時に2本発明の炭酸ガス溶解シス
テムによると、炭酸ガスを多孔質膜を通して海水或いは
水中に排出することにより、炭酸ガス気泡は微細化され
、微細な気泡は、炭酸ガスの高い溶解度により容易に水
中に溶解してしまい。
It is necessary to facilitate the discharge of carbon dioxide gas under this acoustic control. In such cases, 2 According to the carbon dioxide dissolving system of the present invention, carbon dioxide gas bubbles are made fine by discharging carbon dioxide gas into seawater or water through a porous membrane, and the fine bubbles are dissolved due to the high solubility of carbon dioxide gas. It easily dissolves in water.

気泡は、早急に消えて、v&音発生はない。The bubbles disappeared quickly and no v&sound was generated.

排出する炭酸ガスは、圧力#A!装置によって海水深度
による圧力に抗するため、それより約6Kgf/cm’
Gはど高い圧力に調整される。排出圧力に調整された炭
酸ガスは、多孔質膜を通過することによって、最も、海
水に溶解し易い排出気泡径を作り、その微細泡は溶解さ
れ、気泡になることはない。
The carbon dioxide gas discharged has pressure #A! Approximately 6Kgf/cm' more than that because the device resists pressure due to seawater depth.
G is adjusted to a high pressure. By passing through the porous membrane, the carbon dioxide gas adjusted to the discharge pressure creates a discharge bubble diameter that is most easily dissolved in seawater, and the microbubbles are dissolved and do not become bubbles.

前記のようにこの微細泡の径は、最大で0.2mmφで
ある。これは、深度200m以上約500mまでの深度
範囲について、排出炭酸ガスの微細泡が気泡になること
なく、排出より浮上運動的1.0m以内に微細炭酸ガス
泡は溶解されてしまうように設定したものである。他の
気体と同じ様に炭酸ガスは圧力が高いほど溶解度が高い
、換言すれば、深度が深いほど溶ける炭酸ガス体積は大
きいのである。従って、深度200m以上の場合は、多
孔質膜の孔径は、約0.2mmφ以下として問題がない
As mentioned above, the diameter of these microbubbles is at most 0.2 mmφ. This is set so that the fine carbon dioxide gas bubbles are dissolved within 1.0 m of the evacuation movement without becoming bubbles in the depth range from 200 m to approximately 500 m. It is something. Like other gases, the higher the pressure, the higher the solubility of carbon dioxide; in other words, the deeper the depth, the larger the volume of carbon dioxide that can dissolve. Therefore, if the depth is 200 m or more, the pore diameter of the porous membrane should be about 0.2 mmφ or less without any problem.

本発明の炭酸ガス溶解システムは、余計な騒音を周囲に
まき散らさない装置であるという意味から、海中油田等
の探査のための海中作業船或いは潜水船などに用いられ
る。具体的に述べると、第1に、音9機器を使用する有
人潜水船からの炭酸ガスを排出する装置として、第2に
、潜水船の空気清浄装置用の付属装置として非常に有用
である0次に、有用気体を液体中に均一に溶けこます効
果を期待できる意味で、化学プラントでの、液体中にガ
ス体を溶解するプロヒスにおいて、気泡発生がそのプロ
セス或いは製品に悪影響を及ぼす場合に非常に有用であ
り、必要なものとなる。
The carbon dioxide dissolving system of the present invention is a device that does not spread unnecessary noise to the surrounding area, and is therefore used in underwater work vessels or submersibles for exploration of underwater oil fields and the like. Specifically, firstly, it is extremely useful as a device for exhausting carbon dioxide gas from manned submersibles that use Sound9 equipment, and secondly, it is extremely useful as an auxiliary device for air purifying devices on submersibles. Next, in the sense that the effect of uniformly dissolving useful gases into liquids can be expected, if bubble generation has a negative impact on the process or product in chemical plants where gaseous substances are dissolved in liquids, Very useful and necessary.

[実施例] 次に1本発明の1実施の態様について図の炭酸ガス溶解
システムに関して、更に具体的に説明するが1本発明は
、その要旨を変えない限り次の実施例に限定されるもの
ではない。
[Examples] Next, an embodiment of the present invention will be described in more detail with respect to the carbon dioxide dissolving system shown in the figure, but the present invention is limited to the following examples unless the gist thereof is changed. isn't it.

第1図は1本発明の炭酸ガス溶解システムの1実施例の
多孔質膜ノズル部を示す概略断面図である。これにより
説明すると、海水深度に合わせて加圧きれた炭酸ガスは
、供給管から、逆止弁5を通り、仕切り弁4から2円錐
状に開いた炭酸ガス排出室3に供給される。炭酸ガス排
出室3は、その先端部に多孔質膜よりなるガス噴出ノズ
ル部1を備える。この多孔質膜ノズル1は2例えば1図
のごとく円筒形であり、主にその円筒形の底部の多孔質
膜の微細な孔から炭酸ガスが噴出跡れる。
FIG. 1 is a schematic sectional view showing a porous membrane nozzle portion of an embodiment of the carbon dioxide dissolving system of the present invention. To explain this, carbon dioxide gas that has been pressurized according to the depth of the seawater is supplied from a supply pipe, through a check valve 5, and from a gate valve 4 to a carbon dioxide discharge chamber 3 that is open in the shape of two cones. The carbon dioxide gas discharge chamber 3 is equipped with a gas ejection nozzle section 1 made of a porous membrane at its tip. This porous membrane nozzle 1 has a cylindrical shape, for example, as shown in FIG. 1, and carbon dioxide gas is ejected mainly from fine holes in the porous membrane at the bottom of the cylindrical shape.

この多孔質膜ガス溶解室は、多孔質膜よりなるノズル部
1.その多孔質膜ノズルを周囲から補強する円筒部2.
多孔質膜ノズルに炭酸ガスを供給する円錐形に開いた炭
酸ガス排出室3.海水などの圧力に耐える封水装置25
.海水などの逆流を止める仕切り弁4及び逆止弁5並び
に海水たまり9などよりなる。船体の一部の凹部の海水
たまり9の中に多孔質膜ノズル1の円筒形多孔質膜部が
設置されており、そして、船体と外部との間に格子21
が設けられ、その格子21は、蝶番22とボルト23で
取り付けられ、開閉できる。船体は。
This porous membrane gas dissolving chamber includes a nozzle portion 1 made of a porous membrane. A cylindrical part that reinforces the porous membrane nozzle from the periphery 2.
3. Conically opened carbon dioxide gas discharge chamber that supplies carbon dioxide gas to the porous membrane nozzle. Sealing device 25 that can withstand pressure from seawater, etc.
.. It consists of a gate valve 4, a check valve 5, a seawater pool 9, etc. that stop the backflow of seawater. The cylindrical porous membrane part of the porous membrane nozzle 1 is installed in a seawater pool 9 in a recessed part of the hull, and a grid 21 is installed between the hull and the outside.
The lattice 21 is attached with hinges 22 and bolts 23 and can be opened and closed. The hull.

海水の高い圧力を船体外板構造7と船体内部構造8によ
り受は止めている。多孔質膜ノズル1は。
The high pressure of seawater is blocked by the hull outer structure 7 and the hull internal structure 8. Porous membrane nozzle 1.

船体外板構造7と船体内部構造8の間に設けられた円筒
部2の中に図の如く配置きれる0円筒部2は、炭酸ガス
排出室3及びノズルの外径と合う内径を有し、メカニカ
ルバッキング式の封水袋e25を図の如く内側端部に有
する。炭酸ガスは海水等の圧力に抗する圧力をかけられ
、多孔質膜を通して、海水中に噴出きれる。炭酸ガスは
多数の泡となり、海水中に格子21を通して、噴出し上
昇する間に海水中に溶ける。
The cylindrical part 2, which can be disposed as shown in the figure in the cylindrical part 2 provided between the hull outer plate structure 7 and the hull internal structure 8, has an inner diameter that matches the outer diameter of the carbon dioxide gas discharge chamber 3 and the nozzle, A mechanical backing type water-sealing bag e25 is provided at the inner end as shown in the figure. Carbon dioxide gas is subjected to pressure that resists the pressure of seawater, etc., and is ejected into the seawater through a porous membrane. The carbon dioxide gas forms a large number of bubbles, passes through the grid 21 into the seawater, and dissolves in the seawater while erupting and rising.

次に、第2図は1本発明の炭酸ガス溶解システムの全体
を説明する透視斜視概略図である。
Next, FIG. 2 is a schematic perspective view illustrating the entire carbon dioxide dissolving system of the present invention.

船内で発生した炭酸ガスは、炭酸ガス除去手段により環
境大気中より分離され、a縮される。この濃縮された炭
酸ガス11は、圧力的I Kgf/am”で配管より、
炭酸ガス圧縮機12に入り、圧力最大50Kgf/cm
’Gに加圧される。炭酸ガス圧縮@12は、si音を発
生しないように防振台盤14に載置きれて電動機13に
より駆動きれている。濃縮加圧された炭酸ガスは、−次
的に炭酸ガス気蓄器15にためられる(気蓄圧力;最大
50Kgf/cm″G)。
The carbon dioxide gas generated on board the ship is separated from the ambient air by a carbon dioxide removal means and a-condensed. This concentrated carbon dioxide gas 11 is transported from the pipe at a pressure of I Kgf/am.
Enters carbon dioxide compressor 12, maximum pressure 50Kgf/cm
'G is pressurized. The carbon dioxide gas compressor 12 is placed on a vibration-proof base plate 14 and fully driven by an electric motor 13 so as not to generate any noise. The concentrated and pressurized carbon dioxide gas is then stored in the carbon dioxide gas accumulator 15 (accumulation pressure: maximum 50 Kgf/cm''G).

27は安全弁であり、28は1通常の炭酸ガス船外排出
口へ通じる配管である。26はドレン弁であり、炭酸ガ
ス気蓄器15内にたまった水分などを船内に排出するも
のである。炭酸ガス気蓄、器15から71行中などに外
部に炭酸ガスを排出しなけれならないときは、炭酸ガス
は、炭酸ガス排出圧力調整装置1日を通して1図の如く
、又、第1図に示すように1本発明の炭酸ガス溶解シス
テムにより炭酸ガスを外部に排出できる。即ち、海水深
度を深度圧力検知センサ17により検知し、その圧力に
依存して、jj2酸ガスを16で減圧PA整して、逆止
弁5.仕切り弁4を設けた配管を通して、炭酸ガス排出
室3で均一圧力となり、多孔質膜ノズル1を通して、海
水中の矢印で示すように、海水中に多数の泡となり噴出
され、その多数の微細な泡は急速に水中に吸収され、溶
解せしめられる。なお1図のおいて、Aは船内を示し、
Bは海水を示す。
27 is a safety valve, and 28 is a pipe leading to a normal carbon dioxide gas overboard discharge port. Reference numeral 26 denotes a drain valve, which discharges moisture accumulated in the carbon dioxide gas accumulator 15 into the ship. When it is necessary to discharge carbon dioxide to the outside, such as during carbon dioxide gas accumulation or during lines 15 to 71, the carbon dioxide is discharged through a carbon dioxide discharge pressure regulator throughout the day, as shown in Figure 1, or as shown in Figure 1. 1. Carbon dioxide gas can be discharged to the outside by the carbon dioxide dissolving system of the present invention. That is, the seawater depth is detected by the depth pressure detection sensor 17, and depending on the detected pressure, the jj2 acid gas is reduced in pressure PA at 16, and the check valve 5. Through the piping equipped with the gate valve 4, the pressure becomes uniform in the carbon dioxide discharge chamber 3, and through the porous membrane nozzle 1, a large number of bubbles are ejected into the seawater as shown by the arrows in the seawater. The foam is quickly absorbed into the water and dissolved. In Figure 1, A indicates inside the ship,
B indicates seawater.

[発明の効果] 本発明の炭酸ガス溶解システムは、炭酸ガス噴出用の多
孔質膜ノズルを備えることにより、加圧下の海水中或い
は水中に気泡を発生することなく炭酸ガスを完全に溶解
させることができるものである。従って、第1に、加圧
ガスと加圧海水中或いは水中との境界に多孔質膜物質を
設け、更に。
[Effects of the Invention] The carbon dioxide dissolving system of the present invention is equipped with a porous membrane nozzle for ejecting carbon dioxide gas, thereby completely dissolving carbon dioxide gas in pressurized seawater or underwater without generating bubbles. It is something that can be done. Therefore, firstly, a porous membrane material is provided at the interface between the pressurized gas and the pressurized seawater or water;

排出ガスの圧力を調整する装置と組合せることにより、
最適な排出ガス圧力条件で気泡発生がなく炭酸ガスを海
水中或いは水中に放出し溶解させることができること、
第2に、多孔質膜を通じる炭酸ガス放出により、雑音を
発生することなく、炭酸ガスを海水或いは水中に放出で
き、音!測定装置等への悪影響を与えず、海水中或いは
水中での有人潜水測定船の使用が可能にできること、第
3に、液体中に炭酸ガス体を溶解するプロセスにおいて
、気泡発生によるプロセスへの悪影響及び製品への悪影
響を低減できる処理法が可能になることなどの技術的効
果が本発明の炭酸ガス溶解システムにより得られる。
By combining it with a device that adjusts the exhaust gas pressure,
Capable of discharging and dissolving carbon dioxide gas into seawater or water without generating bubbles under optimal exhaust gas pressure conditions;
Second, by releasing carbon dioxide through a porous membrane, carbon dioxide can be released into seawater or water without making any noise. It is possible to use a manned submersible measurement vessel in seawater or underwater without adversely affecting measurement equipment, etc. Thirdly, in the process of dissolving carbon dioxide gas in a liquid, there is no adverse effect on the process due to the generation of bubbles. The carbon dioxide gas dissolving system of the present invention provides technical effects such as enabling a treatment method that can reduce adverse effects on products.

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

第1図は1本発明の炭酸ガス溶解システムの1実施例の
炭酸ガス噴出ノズルの構成を示す断面説明図である。 第2図は2本発明の炭酸ガス溶解システムの全体の構成
を示す概略透視斜視図である。 口主要部分の符号の説明] 1   、多孔質膜ノズル部 28. 炭酸ガス排出室補強円筒部 3、  炭酸ガス排出室 4   仕切り弁 5 、、、、、、逆止弁 6 、 、炭酸ガス 7、1.船体外板構造; 8、  、船体内部構造; 9、、、、、海水たまり部; 11 、、、、fi縮炭酸ガス; 12)、、、、炭酸ガス圧縮機; 16、、、炭酸ガス排出圧力調整装置 A、、、、、船内; B、、、、、海水;
FIG. 1 is an explanatory cross-sectional view showing the configuration of a carbon dioxide gas jetting nozzle in an embodiment of the carbon dioxide dissolving system of the present invention. FIG. 2 is a schematic perspective view showing the overall configuration of the carbon dioxide dissolving system of the present invention. Explanation of symbols of main parts of mouth] 1. Porous membrane nozzle part 28. Carbon dioxide discharge chamber reinforcing cylindrical part 3, carbon dioxide discharge chamber 4, gate valve 5, check valve 6, carbon dioxide 7, 1. Hull outer plate structure; 8. Hull internal structure; 9. Seawater pool; 11. Ficondensed carbon dioxide; 12) Carbon dioxide compressor; 16. Carbon dioxide discharge Pressure regulator A, ..., inside the ship; B, ..., seawater;

Claims (4)

【特許請求の範囲】[Claims] (1)炭酸ガスを水中或いは海水中に溶解させる炭酸ガ
ス溶解システムにおいて、水中或いは海水中の深度の圧
力に抗するように圧力調整された炭酸ガスを水中或いは
海水中に微細な泡状で噴出する多孔質膜ノズルを備える
ことを特徴とする炭酸ガス溶解システム。
(1) In a carbon dioxide dissolving system that dissolves carbon dioxide in water or seawater, carbon dioxide whose pressure is adjusted to resist the pressure at the depth of the water or seawater is ejected into the water or seawater in the form of fine bubbles. A carbon dioxide dissolving system characterized by being equipped with a porous membrane nozzle.
(2)特許請求の範囲第1項の炭酸ガス溶解システムに
おいて、更に、炭酸ガス噴出の圧力を噴出水中或いは海
水中の圧力に合わせて調整する装置を備えることを特徴
とする炭酸ガス溶解システム。
(2) The carbon dioxide dissolving system according to claim 1, further comprising a device for adjusting the pressure of the carbon dioxide gas jet in accordance with the pressure in the jet water or seawater.
(3)特許請求の範囲第1項或いは第2項の炭酸ガス溶
解システムにおいて、前記の炭酸ガス噴出ノズル用多孔
質膜は、セラミック材、焼結合金、或いは高分子化合物
よりなることを特徴とする炭酸ガス溶解システム。
(3) In the carbon dioxide dissolving system according to claim 1 or 2, the porous membrane for the carbon dioxide gas jetting nozzle is made of a ceramic material, a sintered alloy, or a polymer compound. Carbon dioxide dissolution system.
(4)特許請求の範囲第1項或いは第2項の炭酸ガス溶
解システムにおいて、前記の炭酸ガス噴出ノズル用多孔
質膜より噴出する微細泡のガス粒径は0.2mmφ以下
であることを特徴とする炭酸ガス溶解システム。
(4) The carbon dioxide dissolving system according to claim 1 or 2, characterized in that the gas particle size of the microbubbles ejected from the carbon dioxide gas ejection nozzle porous membrane is 0.2 mmφ or less. Carbon dioxide dissolution system.
JP5065586A 1986-03-10 1986-03-10 System for dissolving carbon dioxide Pending JPS62210040A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP5065586A JPS62210040A (en) 1986-03-10 1986-03-10 System for dissolving carbon dioxide

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP5065586A JPS62210040A (en) 1986-03-10 1986-03-10 System for dissolving carbon dioxide

Publications (1)

Publication Number Publication Date
JPS62210040A true JPS62210040A (en) 1987-09-16

Family

ID=12864962

Family Applications (1)

Application Number Title Priority Date Filing Date
JP5065586A Pending JPS62210040A (en) 1986-03-10 1986-03-10 System for dissolving carbon dioxide

Country Status (1)

Country Link
JP (1) JPS62210040A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5693113A (en) * 1993-01-25 1997-12-02 International Partners In Glass Research Container gripper apparatus

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4861681A (en) * 1971-12-01 1973-08-29

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS4861681A (en) * 1971-12-01 1973-08-29

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5693113A (en) * 1993-01-25 1997-12-02 International Partners In Glass Research Container gripper apparatus

Similar Documents

Publication Publication Date Title
JP4953296B2 (en) Hull frictional resistance reduction device
KR100558907B1 (en) Submarine with exhaust discharge structure in sailing under water
JP2006263563A (en) Apparatus for sterilizing microbe or the like in ballast water
FR2817230B1 (en) DEVICE AND METHOD FOR CLEANING PARTS OF A BOAT UNDERWATER
CN217598812U (en) Exhaust type auxiliary desilting seabed base
JPS62210040A (en) System for dissolving carbon dioxide
JP4688085B2 (en) Ballast water treatment equipment
JP4085093B2 (en) Ballast water treatment equipment
JPWO2007125996A1 (en) Water quality improvement device and water quality improvement device
JP2008188502A (en) Water treatment apparatus and water treatment method
JP4365331B2 (en) Method for removing residual ozone in water and method for removing residual ozone in ballast water
JP2712068B2 (en) Abrasive jet type underwater cutting method and apparatus
JP4523450B2 (en) A method of shielding water discharge noise from ships.
CN204750532U (en) Marine pressure balance survival capsule
JP2003166224A (en) Aeration system
KR20130095672A (en) Method for blowing a ballast tank of a submarine and blowing device therefor
JP6223656B2 (en) Small stream approach prevention method and small stream approach prevention apparatus
JP4133045B2 (en) Gas dissolver and water treatment apparatus equipped with them
JPH0880897A (en) Emergency vessel stop device
JPH04313384A (en) Production of active water
KR102217477B1 (en) Exhaust gas treatment system and method for a submarine using a fuel cell
JPH0370534B2 (en)
JP2001106179A (en) Device for preventing attachment of marine fouling
JP2004097982A (en) Mobile water purification apparatus
JP2011046268A (en) Submarine boat having gas tank made of flexible material