JPS6178416A - Method for removing adsorbed gas of activated carbon - Google Patents
Method for removing adsorbed gas of activated carbonInfo
- Publication number
- JPS6178416A JPS6178416A JP59200906A JP20090684A JPS6178416A JP S6178416 A JPS6178416 A JP S6178416A JP 59200906 A JP59200906 A JP 59200906A JP 20090684 A JP20090684 A JP 20090684A JP S6178416 A JPS6178416 A JP S6178416A
- Authority
- JP
- Japan
- Prior art keywords
- activated carbon
- voltage
- degassing
- electrolyte
- side walls
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Pending
Links
Landscapes
- Separation Of Gases By Adsorption (AREA)
Abstract
Description
【発明の詳細な説明】
〔技術分野〕
本発明は、電気化学的電極現象の原理を利用した活性炭
の吸着ガス除去方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION [Technical Field] The present invention relates to a method for removing gas adsorbed on activated carbon using the principle of electrochemical electrode phenomena.
吸着ガス除去の目的は、活性炭表面を液体で覆って使う
用途での活性炭表面の液体での被覆率の向上であり、活
性炭を電極とする電気二重層コンデンサの性能向上に用
いることも応用分野の一つの例である。The purpose of adsorbed gas removal is to improve the coating rate of the activated carbon surface with liquid in applications where the activated carbon surface is covered with liquid.It is also an application field that it can be used to improve the performance of electric double layer capacitors using activated carbon as electrodes. This is one example.
一般に活性炭は、比表配積が犬きく、表面が活性でらる
ことから、活性炭の製造工程および保管−中に、表面に
、 (1!X、 ffl素、炭酸ガス、水蒸気等を多量
に吸着している。このため、活性炭の表面積を有効に液
体で覆う手段として従来は1例えば600℃の高温で、
10”−”〜10−’ Torr 、の真空処理を
行った後、他の気体や液体に接触させることなく直接に
所望の液体に浸す等の極めて困難な脱ガス工程を必要と
した。In general, activated carbon has a large specific area and an active surface, so during the manufacturing process and storage of activated carbon, large amounts of (1!X, ffl, carbon dioxide, water vapor, etc.) are For this reason, as a means to effectively cover the surface area of activated carbon with liquid, the conventional method is to use 1, for example, 600°C high temperature,
After performing vacuum treatment at 10''-'' to 10-' Torr, an extremely difficult degassing process was required, such as immersing it directly in the desired liquid without contacting it with any other gas or liquid.
本発明は、かかる従来欠点を除去した祈らしい活性炭の
吸着ガス除去方法を提供することを目的とする。An object of the present invention is to provide a method for removing adsorbed gases from activated carbon, which eliminates such conventional drawbacks.
以下、本発明の実施例を第1図を用いて説明する。 Embodiments of the present invention will be described below with reference to FIG.
第1図は1本発明による活性炭の吸着ガス除去装置の断
面図を示す。FIG. 1 shows a sectional view of an activated carbon adsorbed gas removal device according to the present invention.
第1図において、1aおよび1bは、活性炭と電解質(
績度30重量%の稀硫酸)とを約1:2<X量比)で混
せしたペースト状の混合物を示し、この混合物1a、1
bii、アルミナ系の素焼(厚さ3」)の多孔性セパレ
ータ2を介して対向しており、混合物1aと1bとはほ
ぼ等鉦である。In Figure 1, 1a and 1b are activated carbon and electrolyte (
A paste-like mixture of dilute sulfuric acid with a concentration of 30% by weight) is mixed at a ratio of approximately 1:2<X amount), and this mixture 1a, 1
The mixtures 1a and 1b face each other with a porous separator 2 made of unglazed alumina (thickness: 3") interposed therebetween, and the mixtures 1a and 1b are approximately equal in proportion.
また、混合物1a+1bは一対の41!注ゴムからなる
側壁3a+3bにそれぞれ対接し紙板4a、上値4bと
からなる絶縁性の枠体4で上下をかこまれている。Moreover, the mixture 1a+1b is a pair of 41! It is surrounded from above and below by an insulating frame 4 made of a paper board 4a and a top plate 4b, which are in contact with side walls 3a and 3b made of rubber.
上蓋4bには、ガス放出用の貫通孔4Cを設けである。The upper lid 4b is provided with a through hole 4C for releasing gas.
また、側壁3a、3bの外側にそれぞれ加圧ヘッド5a
、5bt−設けた脱ガス処理装置を用意して加圧ヘッド
5a+5bの外部から圧力を加えて混合物1a、lb’
に約80%の体積に圧縮させた状態で保持する。Further, pressure heads 5a are provided on the outside of the side walls 3a and 3b, respectively.
, 5bt- is prepared, and pressure is applied from the outside of the pressure head 5a+5b to prepare the mixture 1a, lb'.
It is kept compressed to about 80% volume.
次に、この処理装置全体を70°Cの恒温槽中に置き、
側壁3b、3b間に1.1■の直流電圧1t1時間印加
して混合物1a、1bを左右から保持し上意の!2+!
孔4Cから炭酸ガスおよび!素ガスを放出する。Next, place the entire processing device in a constant temperature bath at 70°C.
A direct current voltage of 1.1 square meters is applied between the side walls 3b and 3b for 1 hour to hold the mixtures 1a and 1b from the left and right sides. 2+!
Carbon dioxide gas and! from hole 4C! Releases elementary gas.
次に本発明の処理を行った活性炭と、無処理の活性炭と
を用いて電気二重層コンデンサを製造して性能を比較測
定した。Next, electric double layer capacitors were manufactured using activated carbon treated according to the present invention and untreated activated carbon, and their performances were compared and measured.
電気二重層コンデンサの製造方法については。Regarding the manufacturing method of electric double layer capacitors.
米国特許第3536963号明m臀等に1る。US Patent No. 3,536,963 to Akira et al.
本発明実施例と従来例とを比較測定した結果は次表の如
くである。The results of comparative measurements between the embodiment of the present invention and the conventional example are shown in the following table.
すなわち、脱ガス処理により活性炭の電解質と接する有
効表[Ml槓が増えるため、約30%静電容量が増加し
ている。That is, due to the degassing treatment, the effective surface of the activated carbon in contact with the electrolyte increases, so the capacitance increases by about 30%.
なお、脱ガス時の印加電圧は、直流電圧O,SV以下で
は電気化学的電極現象かはとんと起らず脱ガス効果がな
く、また、直流電圧1.7Vを越える電圧では水の11
.気分解によるガス発生が起り、脱ガス効果がないこと
が砲認された。Note that when the voltage applied during degassing is less than the DC voltage O, SV, the electrochemical electrode phenomenon does not occur and there is no degassing effect, and when the voltage exceeds 1.7V, the water
.. It was confirmed that gas was generated due to gas decomposition and that there was no degassing effect.
本発明により下記の効果がある。 The present invention has the following effects.
(1)量産化可能な簡単な方法で活性炭の脱ガスができ
る。(1) Activated carbon can be degassed using a simple method that can be mass-produced.
(II) を気二重1層コンデンサの活性炭に適用す
れは、静電容it″増大させることが出来る。また、同
−静電容fi値のものを設計する場合は、小形化できる
ので原価低減となる。If (II) is applied to the activated carbon of a double-layer single-layer capacitor, the capacitance it'' can be increased.Also, when designing a capacitor with the same capacitance fi value, it can be made smaller and the cost can be reduced. Become.
第1図は本発明に↓る活性炭の吸着ガス除去装置の断面
図を示す。
1 ar 1 b・・・・・・活性炭と′I!L解質と
の混合物、2・・・・・・多孔性セパレータ、3a、3
b・・・・・・擾゛屯性ゴムの側壁、4・・・・・・(
絶縁体の)枠体、4a・・・・・・底板、4b・・・・
・・上蓋、4c・・・・・・上蓋の貫通孔、5”+5b
・・・・・・加圧ヘッド。FIG. 1 shows a sectional view of an activated carbon adsorbed gas removal device according to the present invention. 1 ar 1 b...Activated carbon and 'I! Mixture with L solute, 2...Porous separator, 3a, 3
b... Side wall of flexible rubber, 4... (
insulator) frame body, 4a...bottom plate, 4b...
...Top lid, 4c...Top lid through hole, 5"+5b
・・・・・・Pressure head.
Claims (1)
して二群に分け、両活性炭間に0.5〜1.7Vの直流
電圧を印加して、活性炭表面に吸着している気体を除去
し、活性炭表面を電解質で覆う面積を増すことを特徴と
する活性炭の吸着ガス除去方法。Activated carbon soaked in water-soluble electrolyte is divided into two groups via an ion-permeable partition, and a DC voltage of 0.5 to 1.7 V is applied between both activated carbons to remove the gas adsorbed on the activated carbon surface. A method for removing adsorbed gases from activated carbon, which is characterized by increasing the area covered by an electrolyte on the activated carbon surface.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59200906A JPS6178416A (en) | 1984-09-26 | 1984-09-26 | Method for removing adsorbed gas of activated carbon |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP59200906A JPS6178416A (en) | 1984-09-26 | 1984-09-26 | Method for removing adsorbed gas of activated carbon |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS6178416A true JPS6178416A (en) | 1986-04-22 |
Family
ID=16432230
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP59200906A Pending JPS6178416A (en) | 1984-09-26 | 1984-09-26 | Method for removing adsorbed gas of activated carbon |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6178416A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110953600A (en) * | 2019-12-16 | 2020-04-03 | 合肥杰通环境技术有限公司 | Temperature and pressure flow integrated machine for plasma photocatalysis treatment device for organic compounds |
-
1984
- 1984-09-26 JP JP59200906A patent/JPS6178416A/en active Pending
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN110953600A (en) * | 2019-12-16 | 2020-04-03 | 合肥杰通环境技术有限公司 | Temperature and pressure flow integrated machine for plasma photocatalysis treatment device for organic compounds |
CN110953600B (en) * | 2019-12-16 | 2020-10-09 | 合肥杰通环境技术有限公司 | Temperature and pressure flow integrated machine for plasma photocatalysis treatment device for organic compounds |
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