JPH07207479A - Gaseous co2 generator - Google Patents
Gaseous co2 generatorInfo
- Publication number
- JPH07207479A JPH07207479A JP6025848A JP2584894A JPH07207479A JP H07207479 A JPH07207479 A JP H07207479A JP 6025848 A JP6025848 A JP 6025848A JP 2584894 A JP2584894 A JP 2584894A JP H07207479 A JPH07207479 A JP H07207479A
- Authority
- JP
- Japan
- Prior art keywords
- carbon
- anode
- gaseous
- generated
- electrolytic solution
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Water Treatment By Electricity Or Magnetism (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、気体状炭酸ガスを発生
する装置あり、炭酸ガスを利用する多くの産業分野、例
えば化学反応原料、植物の光合成、動物・植物の細胞の
培養、炭酸水の製造等に利用できる。また、酸素と炭酸
ガスの混合ガスの供給を受ける分野にも利用出来る。FIELD OF THE INVENTION The present invention relates to a device for generating gaseous carbon dioxide, which is used in many industrial fields utilizing carbon dioxide, such as raw materials for chemical reactions, photosynthesis of plants, cell culture of animals and plants, carbonated water. It can be used for manufacturing. It can also be used in the field where a mixed gas of oxygen and carbon dioxide is supplied.
【0002】[0002]
【従来の技術】炭酸ガスは通常ボンベから供給してい
る。高圧ボンベは中味に比してボンベの重量が重く、体
積も大きい。気体の炭酸ガスを電極反応によって発生さ
せる装置はない。2. Description of the Related Art Carbon dioxide is usually supplied from a cylinder. The high-pressure cylinder is heavier and has a larger volume than the contents. There is no device that generates gaseous carbon dioxide by an electrode reaction.
【0003】[0003]
【本発明が解決しようとする課題】気体状炭酸ガスまた
は炭酸ガスと酸素の混合ガスを電極反応によって発生さ
せる。SUMMARY OF THE INVENTION Gaseous carbon dioxide gas or a mixed gas of carbon dioxide gas and oxygen is generated by an electrode reaction.
【0004】[0004]
【課題を解決する為の手段】本発明は気体状炭酸ガス発
生装置に係り、酸性電解液中に配置した炭素を陽極とし
て水を電気分解することを特徴とする。陽極炭素上で発
生した酸素の全部または一部が陽極炭素と反応して炭酸
ガスとなるが、陽極近傍が酸性のため水中に殆ど溶解せ
ずガス化する。陽極の炭素としては黒鉛、活性炭、合成
樹脂を炭化した炭素等種々利用できる。純炭素だけでな
く、レジン、アルミサ、雲母、粘度等電極反応しない物
質を混練して焼成した炭素混練製品も陽極材料として利
用しうる。炭素は板状、棒状等に成型してもよいし、粉
末または粒子を用いてもよい。炭素の一部または全部を
親水性の素材で覆うとよい場合もある。親水性素材で形
成した袋の中に炭素粉や粒子を入れ、集電体を接触させ
て陽極を形成してもよい。また炭素は表面のみから陽極
反応するとは限らず、時には陽極の炭素内部に酸の電解
液が浸透して反応すると炭素が崩壊して脱落することも
あるので板状、棒状等の電極でも脱落防止用にケースに
入れてそのケースの一部を親水性素材で形成したり、電
極全体を親水性の袋につめて使ってもよい。電解液はP
H5以下の酸が望ましく、水1Kgに硫酸0.01モ
ル、またはフタル酸水素カリウム0.05モル、または
酒石酸水素カリウムを飽和に溶解した溶液等各種利用で
きる。SUMMARY OF THE INVENTION The present invention relates to a gaseous carbon dioxide gas generator, which is characterized in that water disposed in an acidic electrolyte is used as an anode to electrolyze water. All or part of the oxygen generated on the anodic carbon reacts with the anodic carbon to form carbon dioxide gas, but since the vicinity of the anode is acidic, it is hardly dissolved in water and gasified. As the carbon for the anode, various materials such as graphite, activated carbon and carbon obtained by carbonizing synthetic resin can be used. Not only pure carbon, but also a carbon kneaded product obtained by kneading and firing a substance such as resin, alumina, mica, or viscosity that does not react with the electrode can be used as the anode material. Carbon may be molded into a plate shape, a rod shape, or the like, or powder or particles may be used. In some cases it may be desirable to cover some or all of the carbon with a hydrophilic material. Carbon powder or particles may be placed in a bag formed of a hydrophilic material, and a current collector may be contacted to form the anode. In addition, carbon does not always undergo anodic reaction only from the surface, and sometimes the electrolytic solution of the acid penetrates into the carbon of the anode and reacts with it. For this purpose, a part of the case may be made of a hydrophilic material and the whole electrode may be packed in a hydrophilic bag for use. The electrolyte is P
An acid having an H5 or less is desirable, and 0.01 mol of sulfuric acid, 0.05 mol of potassium hydrogen phthalate, or a solution of saturated potassium hydrogen tartrate in a saturated solution in 1 Kg of water can be used.
【0005】陰極では水素が発生するが、陽極で発生す
る炭酸ガスのみまたは炭酸ガスと酸素の混合ガスを得た
い場合は、陽極室と陰極室を隔膜等で分離して陽極室の
みのガスを取り出せばよい。陽極室から発生するガスを
吐出する取出口を設けるとその取出口からガスが取出せ
るので便利である。Hydrogen is generated at the cathode, but when it is desired to obtain only carbon dioxide gas generated at the anode or a mixed gas of carbon dioxide gas and oxygen, the anode chamber and the cathode chamber are separated by a diaphragm or the like so that only the gas in the anode chamber is produced. Just take it out. It is convenient to provide an outlet for discharging the gas generated from the anode chamber because the gas can be taken out from the outlet.
【0006】活性炭に代表される非晶質の炭素を陽極に
すると、酸素ガスの発生は少なく炭酸ガスの発生比率が
高い。When amorphous carbon, typified by activated carbon, is used as the anode, oxygen gas is generated less and carbon dioxide is generated at a higher rate.
【0007】[0007]
【実施例1】本発明を実施例に従って詳細に説明する。
図1は本発明の実施例1の模式断面図を示す。陽極室1
及び陰極室2は隔膜3で分離されて、一般的なH型セル
を形成している。電解液4は硫酸0.1Nで陽極5は炭
素棒である。炭素棒は陽極室の蓋6にとりつけられてい
る。陽極で発生したガスは取出口7から取り出される。
炭素棒としてはレジンと炭素を混練して焼成したものを
用いると炭素棒中の穴がなくなるので電極表面から反応
し、炭素の利用効率がよく、炭素棒の脱落や崩壊が少な
い。炭素の脱落を防上するためには炭素棒を親水性の膜
で形成した袋8で覆うとよい。袋と炭素はOリング9で
固定すればよい。Example 1 The present invention will be described in detail with reference to examples.
1 shows a schematic cross-sectional view of Embodiment 1 of the present invention. Anode chamber 1
The cathode chamber 2 and the cathode chamber 2 are separated by a diaphragm 3 to form a general H-shaped cell. The electrolytic solution 4 is 0.1 N of sulfuric acid, and the anode 5 is a carbon rod. The carbon rod is attached to the lid 6 of the anode chamber. The gas generated at the anode is taken out from the outlet 7.
When a carbon rod obtained by kneading resin and carbon and firing is used as the carbon rod, the holes in the carbon rod are eliminated, and the reaction occurs from the electrode surface, the carbon utilization efficiency is good, and the carbon rod does not drop or collapse easily. In order to prevent carbon from falling off, the carbon rod may be covered with a bag 8 formed of a hydrophilic film. The bag and carbon may be fixed with an O-ring 9.
【0008】[0008]
【実施例2】図2は本発明の実施例2の模式断面図を示
す。陽極室1の底部は集電体10で形成され、陽極室に
は炭素粉または炭素粒11を充填してある。集電体から
はリード線12が引き出され、集電体及びこれに接する
炭素にプラス電圧をかけられる。陽極で炭酸ガスを発生
させれば陽極の炭素は消耗するがこの実施例の場合は炭
素粉または炭素粒がなくなれば追加すればよい。集電体
としては白金、白金メッキしたチタンや炭素等が利用で
きる。Second Embodiment FIG. 2 is a schematic sectional view of a second embodiment of the present invention. The bottom of the anode chamber 1 is formed of a current collector 10, and the anode chamber is filled with carbon powder or carbon particles 11. The lead wire 12 is drawn out from the current collector, and a positive voltage is applied to the current collector and carbon in contact with the current collector. When carbon dioxide gas is generated at the anode, carbon in the anode is consumed, but in this embodiment, carbon powder or carbon particles may be added if they are gone. As the current collector, platinum, platinum-plated titanium, carbon or the like can be used.
【0009】[0009]
【本発明のその他の実施形態】前記実施例に限らず陽極
は親水性の袋につめた炭素粉や炭素粒でもよい。陽極で
発生するガスは炭酸ガスと酸素が主であるが、その比率
は炭素の種類と電流密度によって決まる。一般的に結晶
化の進んでいない炭素の方が炭酸ガスの比率が高く、活
性炭では90%以上が炭酸ガスとなる。酸素を除く方が
よい系ではガス発生の下流に脱酸素工程を用いて酸素を
除くことができる。Other Embodiments of the Present Invention Not limited to the above embodiments, the anode may be carbon powder or carbon particles packed in a hydrophilic bag. The gas generated at the anode is mainly carbon dioxide and oxygen, but the ratio is determined by the type of carbon and the current density. Generally, carbon that is not crystallized has a higher ratio of carbon dioxide gas, and 90% or more of activated carbon is carbon dioxide gas. In systems where it is better to remove oxygen, a deoxygenation step can be used downstream of gas evolution to remove oxygen.
【0010】[0010]
【発明の効果】本発明によって炭酸ガスの発生量を電流
で制御できる。またボンベより体積効率がよいし、高圧
ガスを扱う必要もない。発生ガス圧も陽極室を耐圧構造
にすれば容易に上げられる。陽極炭素の種類を選定すれ
ば炭酸ガスと酸素の混合ガスも得られる。According to the present invention, the amount of carbon dioxide gas generated can be controlled by the electric current. It is also more volumetrically efficient than a cylinder and does not need to handle high pressure gas. The generated gas pressure can be easily increased by making the anode chamber a pressure resistant structure. A mixed gas of carbon dioxide and oxygen can be obtained by selecting the type of anode carbon.
【0011】[0011]
【図1】図1は本発明の実施例1の模式断面図を示すFIG. 1 is a schematic sectional view of a first embodiment of the present invention.
【図2】図2は本発明の実施例2の模式断面図を示すFIG. 2 is a schematic sectional view of a second embodiment of the present invention.
1:陽極室 2:陰極室 3:隔膜 4:電解液
5:炭素 6:蓋 7:取出口 8:袋 9:Oリング
10:集電体 11:炭素粉または炭素粒 12:リード線 1
3:陰極1: Anode chamber 2: Cathode chamber 3: Diaphragm 4: Electrolyte 5: Carbon 6: Lid 7: Outlet 8: Bag 9: O-ring
10: Current collector 11: Carbon powder or carbon particles 12: Lead wire 1
3: Cathode
Claims (3)
水を電気分解することを特徴とする気体状炭酸ガス発生
装置。1. A gaseous carbon dioxide generating device characterized in that water is electrolyzed using carbon arranged in an acidic electrolyte as an anode.
とする第1項に記載の炭酸ガス発生装置。2. The carbon dioxide generating device according to claim 1, wherein the carbon is carbon powder or particles.
材で覆うことを特徴とする第1項または第2項に記載の
炭酸ガス発生装置。3. A carbon dioxide gas generator according to claim 1 or 2, wherein a part or all of carbon of the anode is covered with a hydrophilic material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6025848A JPH07207479A (en) | 1994-01-12 | 1994-01-12 | Gaseous co2 generator |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP6025848A JPH07207479A (en) | 1994-01-12 | 1994-01-12 | Gaseous co2 generator |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH07207479A true JPH07207479A (en) | 1995-08-08 |
Family
ID=12177272
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP6025848A Pending JPH07207479A (en) | 1994-01-12 | 1994-01-12 | Gaseous co2 generator |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH07207479A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007077654A1 (en) * | 2005-12-28 | 2007-07-12 | Omsi Co., Ltd. | Process for producing carbon dioxide solution, production apparatus, and carbonated water |
CN114190206A (en) * | 2021-11-19 | 2022-03-18 | 清华大学 | Distributed CO2Gas fertilizer generating device and CO2Capture method |
KR102597615B1 (en) * | 2023-08-29 | 2023-11-02 | 주식회사 루비스코 | Electrolysis carbon dioxide generator |
-
1994
- 1994-01-12 JP JP6025848A patent/JPH07207479A/en active Pending
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2007077654A1 (en) * | 2005-12-28 | 2007-07-12 | Omsi Co., Ltd. | Process for producing carbon dioxide solution, production apparatus, and carbonated water |
JP5087408B2 (en) * | 2005-12-28 | 2012-12-05 | 株式会社 オムシー | Carbon dioxide solution manufacturing method, manufacturing apparatus, and carbonated water |
CN114190206A (en) * | 2021-11-19 | 2022-03-18 | 清华大学 | Distributed CO2Gas fertilizer generating device and CO2Capture method |
KR102597615B1 (en) * | 2023-08-29 | 2023-11-02 | 주식회사 루비스코 | Electrolysis carbon dioxide generator |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US6254762B1 (en) | Process and electrolytic cell for producing hydrogen peroxide | |
US6113773A (en) | Seawater electrolysis apparatus | |
US6387228B1 (en) | Electrochemical generation of carbon dioxide and hydrogen from organic acids | |
US4416747A (en) | Process for the synthetic production of ozone by electrolysis and use thereof | |
JP3007137B2 (en) | Electrolytic ozone generation method and apparatus | |
US5205994A (en) | Electrolytic ozone generator | |
CA2174545A1 (en) | Electrolytic cell for producing a mixed oxidant gas | |
CN101506406A (en) | Electrode, method of manufacture and use thereof | |
KR101218952B1 (en) | Method and Device for Producing One or Several Gases | |
JPH05295579A (en) | Production of ozone | |
US3446725A (en) | Electrolysis cell | |
JPH11269685A (en) | Production of infusible metal electrode and electrolytic cell using that electrode | |
Girenko et al. | Selection of the optimal cathode material to synthesize medical sodium hypochlorite solutions in a membraneless electrolyzer | |
JPH07109593A (en) | Electrolytic ozonizer | |
US3775272A (en) | Mercury diaphragm chlor-alkali cell and process for decomposing alkali metal halides | |
US4975171A (en) | Bipolar electrolytic cell | |
US6159349A (en) | Electrolytic cell for hydrogen peroxide production | |
JPH03154691A (en) | Method and apparatus for making high concentration ozone water | |
CN1085607A (en) | The method of bipolar oxygen-making electrochemical and device | |
JPH07207479A (en) | Gaseous co2 generator | |
JPS6041153B2 (en) | Diaphragmless electrolytic cell | |
EP0230737B1 (en) | Membrane pervaporation process for obtaining a chlorine dioxide solution | |
JPS6053115B2 (en) | electrolytic cell | |
US5840174A (en) | Process for the purification of gases | |
CN207130343U (en) | A kind of electrolytic ozone generator that can add electrolyte automatically |