JPH04311586A - Device for electrolytically reducing carbon dioxide - Google Patents
Device for electrolytically reducing carbon dioxideInfo
- Publication number
- JPH04311586A JPH04311586A JP3075434A JP7543491A JPH04311586A JP H04311586 A JPH04311586 A JP H04311586A JP 3075434 A JP3075434 A JP 3075434A JP 7543491 A JP7543491 A JP 7543491A JP H04311586 A JPH04311586 A JP H04311586A
- Authority
- JP
- Japan
- Prior art keywords
- electrode
- electrolyte
- carbon dioxide
- electrolytic
- plated
- 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
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 title claims description 56
- 229910002092 carbon dioxide Inorganic materials 0.000 title claims description 28
- 239000001569 carbon dioxide Substances 0.000 title claims description 19
- 239000007784 solid electrolyte Substances 0.000 claims abstract description 10
- 230000001678 irradiating effect Effects 0.000 claims abstract description 4
- 238000006722 reduction reaction Methods 0.000 claims description 15
- 239000008151 electrolyte solution Substances 0.000 claims description 9
- 229910052751 metal Inorganic materials 0.000 claims description 9
- 239000002184 metal Substances 0.000 claims description 9
- BASFCYQUMIYNBI-UHFFFAOYSA-N platinum Chemical group [Pt] BASFCYQUMIYNBI-UHFFFAOYSA-N 0.000 claims description 3
- 239000003054 catalyst Substances 0.000 claims description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 abstract description 19
- 239000003792 electrolyte Substances 0.000 abstract description 10
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 abstract description 8
- 229910052799 carbon Inorganic materials 0.000 abstract description 8
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 abstract description 6
- 238000005868 electrolysis reaction Methods 0.000 abstract description 3
- 229910000028 potassium bicarbonate Inorganic materials 0.000 abstract description 3
- 235000015497 potassium bicarbonate Nutrition 0.000 abstract description 3
- 239000011736 potassium bicarbonate Substances 0.000 abstract description 3
- TYJJADVDDVDEDZ-UHFFFAOYSA-M potassium hydrogencarbonate Chemical compound [K+].OC([O-])=O TYJJADVDDVDEDZ-UHFFFAOYSA-M 0.000 abstract description 3
- 150000002500 ions Chemical class 0.000 abstract description 2
- 229920006395 saturated elastomer Polymers 0.000 abstract description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 2
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- 239000007789 gas Substances 0.000 description 7
- 230000003197 catalytic effect Effects 0.000 description 6
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 5
- 229910052802 copper Inorganic materials 0.000 description 5
- 239000010949 copper Substances 0.000 description 5
- 230000007423 decrease Effects 0.000 description 5
- 230000000694 effects Effects 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000007747 plating Methods 0.000 description 4
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- 239000007795 chemical reaction product Substances 0.000 description 3
- 230000014759 maintenance of location Effects 0.000 description 3
- 230000003247 decreasing effect Effects 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 1
- VGGSQFUCUMXWEO-UHFFFAOYSA-N Ethene Chemical compound C=C VGGSQFUCUMXWEO-UHFFFAOYSA-N 0.000 description 1
- 239000005977 Ethylene Substances 0.000 description 1
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 1
- 229920000557 Nafion® Polymers 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 239000007853 buffer solution Substances 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 230000005518 electrochemistry Effects 0.000 description 1
- 238000007772 electroless plating Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 239000000243 solution Substances 0.000 description 1
- 238000010792 warming Methods 0.000 description 1
Landscapes
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
Abstract
Description
【0001】0001
【産業上の利用分野】この発明は、炭酸ガスを電解還元
反応によって例えばメタンやメタノールなどに変化させ
る二酸化炭素の電解還元装置に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an electrolytic reduction device for carbon dioxide, which converts carbon dioxide gas into methane, methanol, etc. by an electrolytic reduction reaction.
【0002】0002
【従来の技術】近年、地球環境問題の1つである大気中
の炭酸ガスの増加による地球の温暖化を防止するため、
炭酸ガスを種々の方法によって固定する試みが為されて
いる。例えば、金属電極上で炭酸ガスの電解還元を行う
と、炭酸ガスが一酸化炭素,メタン又はエタンに変化す
ることが知られている。[Prior Art] In recent years, in order to prevent global warming caused by an increase in carbon dioxide gas in the atmosphere, which is one of the global environmental problems,
Attempts have been made to fix carbon dioxide gas by various methods. For example, it is known that when carbon dioxide gas is electrolytically reduced on a metal electrode, the carbon dioxide gas changes to carbon monoxide, methane, or ethane.
【0003】図3は1990年電気化学秋季大会で発表
された報告からの引用であり、Cu電極を用いたCO2
の還元に関するものである。この図では、0.1M
KHCO3溶液中においてCO2の電解還元を行い、2
0〜40%の電流効率でメタンやエタンが生成されたこ
とを示している。[0003] Figure 3 is a quote from a report presented at the 1990 Fall Conference on Electrochemistry.
It is related to the reduction of In this figure, 0.1M
Electrolytic reduction of CO2 is performed in KHCO3 solution, and 2
This shows that methane and ethane were produced at a current efficiency of 0 to 40%.
【0004】0004
【発明が解決しようとする課題】従来の電解反応による
炭酸ガスの還元方法では、長時間の電解を行うと触媒金
属電極の活性が低下し、また触媒金属電極表面における
CO2の電解還元反応の進行に伴って電極近傍のCO2
濃度が減少するため、エタンやエチレンの生成効率が低
下するなどの問題点があった。[Problems to be Solved by the Invention] In the conventional method for reducing carbon dioxide gas by electrolytic reaction, the activity of the catalytic metal electrode decreases when electrolysis is carried out for a long time, and the electrolytic reduction reaction of CO2 progresses on the surface of the catalytic metal electrode. As a result, CO2 near the electrode
Because the concentration decreased, there were problems such as a decrease in the production efficiency of ethane and ethylene.
【0005】この発明は、上記のような問題点を解決す
ることを課題としてなされたものであり、触媒金属電極
の活性低下を防止することができるとともに、触媒金属
電極の近傍でのCO2の濃度減少を防止することができ
、二酸化炭素を長時間に渡って効率良く電解還元するこ
とができる二酸化炭素の電解還元装置を得ることを目的
とする。[0005] This invention was made with the aim of solving the above-mentioned problems, and it is possible to prevent a decrease in the activity of the catalytic metal electrode, and also to reduce the concentration of CO2 in the vicinity of the catalytic metal electrode. An object of the present invention is to obtain an electrolytic reduction device for carbon dioxide that can prevent carbon dioxide from decreasing and efficiently electrolytically reduce carbon dioxide over a long period of time.
【0006】[0006]
【課題を解決するための手段】この発明に係る二酸化炭
素の電解還元装置は、電解液中に超音波を照射する超音
波照射手段を電解槽に設けたものである。[Means for Solving the Problems] A carbon dioxide electrolytic reduction device according to the present invention is one in which an ultrasonic irradiation means for irradiating ultrasonic waves into an electrolytic solution is provided in an electrolytic cell.
【0007】[0007]
【作用】この発明においては、電解液中に超音波を照射
することにより、電解液を振動させ、負極表面での反応
生成物の滞留やCO2の濃度勾配の発生を防止する。[Operation] In this invention, the electrolytic solution is vibrated by irradiating ultrasonic waves into the electrolytic solution, thereby preventing retention of reaction products on the surface of the negative electrode and generation of a concentration gradient of CO2.
【0008】[0008]
【実施例】以下、この発明の実施例を図について説明す
る。図1はこの発明の一実施例による二酸化炭素の電解
還元装置を示す構成図である。図において、1は電解液
2が収容された電解槽であり、電解液としては、例えば
0.1モルの炭酸水素カリウムを緩衝溶液として炭酸ガ
スを飽和させたものが使用される。3は電解槽1内に設
けられたプロトン導電性固体電解質であり、例えばデュ
ポン社製ナフィオン117が使用される。4はプロトン
導電性固体電解質3の一方の面に無電解めっきにより形
成された第1正極としての多孔性の白金めっき電極、5
はプロトン導電性固体電解質3の他方の面にめっきによ
り形成された負極としての多孔性の銅めっき電極である
。DESCRIPTION OF THE PREFERRED EMBODIMENTS Examples of the present invention will be described below with reference to the drawings. FIG. 1 is a block diagram showing a carbon dioxide electrolytic reduction apparatus according to an embodiment of the present invention. In the figure, reference numeral 1 denotes an electrolytic cell containing an electrolytic solution 2, which is saturated with carbon dioxide gas using, for example, 0.1 mol of potassium bicarbonate as a buffer solution. 3 is a proton conductive solid electrolyte provided in the electrolytic cell 1; for example, Nafion 117 manufactured by DuPont is used. 4 is a porous platinum-plated electrode as a first positive electrode formed by electroless plating on one side of the proton-conductive solid electrolyte 3;
is a porous copper-plated electrode as a negative electrode formed by plating on the other surface of the proton-conductive solid electrolyte 3.
【0009】6は電解槽1内に銅めっき電極5の対極と
して設けられた第2正極としてのカーボン電極、7は白
金めっき電極4と銅めっき電極5との間に直流を印加す
るための第1直流電源、8は銅めっき電極5とカーボン
電極6との間に直流を印加するための第2直流電源、9
は銅めっき電極5とカーボン電極6との間に設けられた
隔膜、10は電解槽1に取り付けられた超音波照射手段
としての超音波振動子である。Reference numeral 6 denotes a carbon electrode as a second positive electrode provided in the electrolytic cell 1 as a counter electrode to the copper-plated electrode 5. Reference numeral 7 denotes a second carbon electrode for applying direct current between the platinum-plated electrode 4 and the copper-plated electrode 5. 1 a DC power source; 8 a second DC power source for applying DC between the copper plating electrode 5 and the carbon electrode 6; 9;
1 is a diaphragm provided between the copper-plated electrode 5 and the carbon electrode 6, and 10 is an ultrasonic vibrator attached to the electrolytic cell 1 as an ultrasonic irradiation means.
【0010】上記のように構成された電解還元装置にお
いては、超音波振動子10により電解液2に振動を与え
ながら、第1直流電源7を用いてプロトン導電性固体電
解質3の両面の電極に電圧を印加する。即ち、白金めっ
き電極4を正極、銅めっき電極5を負極として、1.0
〜1.5ボルトの電圧を印加する。これにより、白金め
っき電極4の表面で水の電気分解が生じ、白金めっき電
極4の表面では酸素が発生し、また銅めっき電極5の表
面からは、プロトン導電性固体電解質3中を移動した水
素イオンが放出される。従って、銅めっき電極5は、プ
ロトンソース電極として作用することになる。このとき
、第2直流電源8を用いて銅めっき電極5とカーボン電
極6との間に0.1〜10mA/cm2の定電流を通電
すると、電解液2中に溶解したCO2が銅めっき電極5
上で還元され、この結果メタンやエタンが生成される。In the electrolytic reduction apparatus configured as described above, the first DC power source 7 is used to apply vibration to the electrolyte 2 by the ultrasonic vibrator 10, and the electrodes on both sides of the proton-conductive solid electrolyte 3 are heated. Apply voltage. That is, with the platinum-plated electrode 4 as the positive electrode and the copper-plated electrode 5 as the negative electrode, the
Apply a voltage of ~1.5 volts. As a result, electrolysis of water occurs on the surface of the platinum-plated electrode 4, oxygen is generated on the surface of the platinum-plated electrode 4, and hydrogen that has moved in the proton-conductive solid electrolyte 3 is generated from the surface of the copper-plated electrode 5. Ions are released. Therefore, the copper-plated electrode 5 acts as a proton source electrode. At this time, when a constant current of 0.1 to 10 mA/cm2 is applied between the copper plating electrode 5 and the carbon electrode 6 using the second DC power supply 8, the CO2 dissolved in the electrolyte 2 is transferred to the copper plating electrode 5.
is reduced above, resulting in the production of methane and ethane.
【0011】このような電解還元装置では、超音波振動
子10により電解液2中に超音波振動を与えているので
、銅めっき電極5の表面での反応生成物の滞留が防止さ
れるとともに、銅めっき電極5の近傍でのCO2の濃度
勾配の発生がなくなる。従って、例えば図2に示すよう
に、メタンやエタンが長時間に渡って効率良く生成され
る。In such an electrolytic reduction apparatus, since ultrasonic vibration is applied to the electrolytic solution 2 by the ultrasonic vibrator 10, retention of reaction products on the surface of the copper-plated electrode 5 is prevented, and The generation of a CO2 concentration gradient near the copper-plated electrode 5 is eliminated. Therefore, for example, as shown in FIG. 2, methane and ethane are efficiently produced over a long period of time.
【0012】なお、上記実施例では負極、即ち触媒金属
電極として銅めっき電極4を示したが、CO2電解還元
反応の触媒となるものであれば他のものであってもよく
、上記実施例に限定されない。また、第2正極もカーボ
ン電極6に限定されるものではない。[0012] In the above embodiment, the copper plated electrode 4 was shown as the negative electrode, that is, the catalytic metal electrode, but other materials may be used as long as they serve as a catalyst for the CO2 electrolytic reduction reaction. Not limited. Further, the second positive electrode is not limited to the carbon electrode 6 either.
【0013】[0013]
【発明の効果】以上説明したように、この発明の二酸化
炭素の電解還元装置は、電解槽に超音波照射手段を設け
、電解液中に超音波を照射するようにしたので、電解液
に振動が与えられ、反応生成物の滞留による触媒金属電
極、即ち負極の活性低下を防止することができるととも
に、負極の近傍でのCO2の濃度減少を防止することが
でき、これにより二酸化炭素を長時間に渡って効率良く
電解還元することができるという効果を奏する。Effects of the Invention As explained above, in the carbon dioxide electrolytic reduction device of the present invention, an ultrasonic irradiation means is provided in the electrolytic cell and ultrasonic waves are irradiated into the electrolyte, so that the electrolyte is vibrated. It is possible to prevent a decrease in the activity of the catalytic metal electrode, that is, the negative electrode, due to the retention of reaction products, and also to prevent a decrease in the concentration of CO2 near the negative electrode. The effect is that electrolytic reduction can be carried out efficiently over a period of time.
【図1】この発明の一実施例による二酸化炭素の電解還
元装置を示す構成図である。FIG. 1 is a configuration diagram showing a carbon dioxide electrolytic reduction apparatus according to an embodiment of the present invention.
【図2】図1の装置によりメタン生成した場合の電流効
率と時間との関係図である。FIG. 2 is a diagram showing the relationship between current efficiency and time when methane is produced by the apparatus in FIG. 1;
【図3】従来装置によりメタン生成した場合の電流効率
と時間との関係図である。FIG. 3 is a diagram showing the relationship between current efficiency and time when methane is produced by a conventional device.
1 電解槽
2 電解液
3 プロトン導電性固体電解質
4 白金めっき電極(第1正極)5 銅め
っき電極(負極)
6 カーボン電極(第2正極)1 Electrolytic cell 2 Electrolyte 3 Proton conductive solid electrolyte 4 Platinum plated electrode (first positive electrode) 5 Copper plated electrode (negative electrode) 6 Carbon electrode (second positive electrode)
Claims (1)
している電解槽と、多孔性の白金族からなる第1正極、
及び二酸化炭素の電解還元反応の触媒となる多孔性の金
属からなる負極を有し、前記電解液中に設けられたプロ
トン導電性固体電解質と、前記負極に対向して前記電解
液中に設けられた第2正極と、前記電解槽に設けられ、
前記電解液中に超音波を照射する超音波照射手段とを備
えたことを特徴とする二酸化炭素の電解還元装置。1. An electrolytic cell containing an electrolytic solution in which carbon dioxide is dissolved; a first positive electrode made of a porous platinum group metal;
and a negative electrode made of a porous metal that serves as a catalyst for the electrolytic reduction reaction of carbon dioxide, and a proton conductive solid electrolyte provided in the electrolytic solution, and a proton conductive solid electrolyte provided in the electrolytic solution opposite to the negative electrode. a second positive electrode provided in the electrolytic cell;
An apparatus for electrolytically reducing carbon dioxide, comprising: ultrasonic irradiation means for irradiating ultrasonic waves into the electrolytic solution.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3075434A JPH04311586A (en) | 1991-04-09 | 1991-04-09 | Device for electrolytically reducing carbon dioxide |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3075434A JPH04311586A (en) | 1991-04-09 | 1991-04-09 | Device for electrolytically reducing carbon dioxide |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH04311586A true JPH04311586A (en) | 1992-11-04 |
Family
ID=13576122
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3075434A Pending JPH04311586A (en) | 1991-04-09 | 1991-04-09 | Device for electrolytically reducing carbon dioxide |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH04311586A (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030033421A (en) * | 2001-10-22 | 2003-05-01 | 주식회사 미래소재 | Electrodeposition Apparatus and Method Using the Ultrasonic Wave |
JP2012112001A (en) * | 2010-11-25 | 2012-06-14 | Furukawa Electric Co Ltd:The | Electrolytic cell, electrolytic apparatus, and method for producing hydrocarbon |
US8277631B2 (en) * | 2007-05-04 | 2012-10-02 | Principle Energy Solutions, Inc. | Methods and devices for the production of hydrocarbons from carbon and hydrogen sources |
US8617375B2 (en) | 2010-04-26 | 2013-12-31 | Panasonic Corporation | Method for reducing carbon dioxide |
JP2014205878A (en) * | 2013-04-12 | 2014-10-30 | 株式会社日立製作所 | Cathode electrode and electrolyzer using the same |
CN108624906A (en) * | 2017-03-21 | 2018-10-09 | 株式会社东芝 | Electrochemical reaction appts and electrochemical reaction method |
-
1991
- 1991-04-09 JP JP3075434A patent/JPH04311586A/en active Pending
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030033421A (en) * | 2001-10-22 | 2003-05-01 | 주식회사 미래소재 | Electrodeposition Apparatus and Method Using the Ultrasonic Wave |
US8277631B2 (en) * | 2007-05-04 | 2012-10-02 | Principle Energy Solutions, Inc. | Methods and devices for the production of hydrocarbons from carbon and hydrogen sources |
US20120329657A1 (en) * | 2007-05-04 | 2012-12-27 | Principle Energy Solutions, Inc. | Methods and devices for the production of hydrocarbons from carbon and hydrogen sources |
US9315910B2 (en) * | 2007-05-04 | 2016-04-19 | Principle Energy Solutions Inc. | Methods and devices for the production of hydrocarbons from carbon and hydrogen sources |
US8617375B2 (en) | 2010-04-26 | 2013-12-31 | Panasonic Corporation | Method for reducing carbon dioxide |
JP2012112001A (en) * | 2010-11-25 | 2012-06-14 | Furukawa Electric Co Ltd:The | Electrolytic cell, electrolytic apparatus, and method for producing hydrocarbon |
JP2014205878A (en) * | 2013-04-12 | 2014-10-30 | 株式会社日立製作所 | Cathode electrode and electrolyzer using the same |
CN108624906A (en) * | 2017-03-21 | 2018-10-09 | 株式会社东芝 | Electrochemical reaction appts and electrochemical reaction method |
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