Selective porphyrin-catalyzed electrochemical reduction of co2 into co, in particular in water

a porphyrincatalyzed electrochemical and electrochemical reduction technology, which is applied in the direction of organic compounds/hydrides/coordination complex catalysts, physical/chemical process catalysts, iron organic compounds, etc., can solve the problems of poor selective direct electrochemical reduction of co2 /sub>at inert electrodes, low chemical reactivity, etc., and achieve high and tunable selectivity

Inactive Publication Date: 2019-07-25
CENT NAT DE LA RECHERCHE SCI
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

The inventor's new type of catalyst has several technical benefits: it can be used with both polar or non-polar liquids like dimethylformamide (DMF) while still being effective even when there were no more than 25 ppm of oxygen remaining after treatment for 10 hours; this makes them ideal for use on different types of chemical reactions without losing their effectiveness due to lacking certain substances that could affect other things nearby during reaction time.

Problems solved by technology

The technical problem addressed in this patented text relates how to improve upon existing methods for analyzing data from large amounts of time-series data without sacrificing accuracy or efficiency by improving their ability to handle complex datasets with many variables simultaneously.

Method used

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  • Selective porphyrin-catalyzed electrochemical reduction of co2 into co, in particular in water
  • Selective porphyrin-catalyzed electrochemical reduction of co2 into co, in particular in water
  • Selective porphyrin-catalyzed electrochemical reduction of co2 into co, in particular in water

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Experimental program
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Effect test

first embodiment

of the Electrolyte Solutions

[0138]In a first embodiment, the solvent of the cathodic and anodic electrolyte solutions is water.

[0139]When syngas is produced in this embodiment, the pH of the cathodic electrolyte solution (notably through appropriate choice of buffer) and the potential applied to the cathode may be adjusted so as to tune (or choose) the CO / H2 molar ratio of the produced gas. In this case, the cathodic electrolyte solution preferably comprises a buffer such as a phosphate buffer. The pH of the cathodic electrolyte solution is also typically of between 6.5 and 7.5.

[0140]For producing pure CO, the pH of the cathodic electrolyte solution is preferably of between 6.5 and 7.5, and the cathodic electrolyte solution is advantageously devoid of buffer, in particular it is devoid of phosphate buffer. In this embodiment, the pH of the cathodic electrolyte solution is advantageously adjusted by adding alkali metal salts, preferably hydroxide, carbonate or bicarbonate alkali metal

second embodiment

Solvent of the Electrolyte Solutions

[0141]In a second embodiment, the solvent of the cathodic and anodic electrolyte solutions is an organic medium, such as DMF (dimethylformamide), ACN (acetonitrile), and aqueous mixtures thereof. Preferably, the electrolyte solutions further comprise a proton donor as described above.

[0142]Advantageously, the intensity applied to the cathode is between 2 and 5 A / m2, more preferably between 2.5 and 4 A / m2, even more preferably between 3 and 3.5 A / m2.

[0143]Advantageously, the potential applied to the cathode is between −2.5 V and −0.5 V versus NHE, more advantageously between −2.0 V and −0.5 V versus NHE, more advantageously between −1.5 V and −0.8 V versus NHE, more advantageously between −1.3 V and −0.9 V versus NHE, and the intensity applied to the cathode is advantageously between 2 and 5 A / m2, more preferably between 2.5 and 4 A / m2, even more preferably between 3 and 3.5 A / m2.

DESCRIPTION OF THE DRAWINGS

[0144]FIG. 1 represents the synth

example 1

and Characterization of Fe-o-TMA

[0162]Chemicals.

[0163]Dimethylformamide (Acros, >99.8%, extra dry over molecular sieves), the supporting electrolyte NBu4PF6 (Fluka, purriss.) were used as received. All starting materials were obtained from Sigma-Aldrich, Fluka, Acros and Alfa-Aesar, and were used without further purification. CHCl3 and CH2Cl2 were distilled from calcium hydride and stored under an argon atmosphere.

[0164]Materials.

[0165]1H NMR spectra were recorded on a Bruker Avance III 400 MHz spectrometer and were referenced to the resonances of the solvent used. The mass spectra were recorded on a MALDI 4800 TOF / TOF. The elemental analysis were performed by the Microanalysis Service of the Institut de Chimie des Substances Naturelles (ICSN-CNRS), Avenue de la Terrasse, 91198 Gif-sur-Yvette cedex, France.

[0166]Porphyrins.

[0167]Iron(III) 5,10,15,20-tetrakis(4′-N,N,N-trimethylanilinium)-porphyrin pentachloride (Fe-p-TMA) was prepared as described elsewhere in Costentin et al. (Proc.

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Abstract

The present invention relates to the use of complexes of water soluble porphyrins of formula (I). The present invention relates to water soluble porphyrins of formula (I), wherein R1 to R11 and R1′ to R8′ are as defined in claim 1, their iron complexes, use thereof as catalysts for the selective electrochemical reduction of CO2 into CO, electrochemical cells comprising them, and methods for reducing electrochemically CO2 into CO using said complexes or said electrochemical cells, thereby producing CO or syngas.

Description

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Claims

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Application Information

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Owner CENT NAT DE LA RECHERCHE SCI
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