Light-Driven Reduction of CO2 to CO in Water with a Cobalt Molecular Catalyst and an Organic Sensitizer/Visible-Light Driven CO2 Reduction with 1/TATA+/BIH + TEOA under Various Conditions: Difference between revisions
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< Light-Driven Reduction of CO2 to CO in Water with a Cobalt Molecular Catalyst and an Organic Sensitizer
Molecular process, Photocatalytic CO2 conversion experiments
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|TON H2=0 | |TON H2=0 | ||
|TON HCOOH=0 | |TON HCOOH=0 | ||
|include=No | |||
}}{{Photocatalytic CO2 conversion | |||
|catalyst=Molecule:100788 | |||
|cat conc=0.002 | |||
|e-D=Molecule:100508 | |||
|e-D conc=0.1 | |||
|solvent A=Molecule:100530 | |||
|solvent B=Molecule:100507 | |||
|solvent-ratio=85/15 | |||
|λexc=450 | |||
|TON CO=0 | |||
|TON H2=0 | |||
|TON HCOOH=0 | |||
|include=No | |||
}}{{Photocatalytic CO2 conversion | |||
|catalyst=Molecule:100788 | |||
|cat conc=0.002 | |||
|PS=Molecule:100797 | |||
|PS conc=0.2 | |||
|solvent A=Molecule:100530 | |||
|solvent B=Molecule:100507 | |||
|solvent-ratio=85/15 | |||
|λexc=450 | |||
|TON CO=950 | |||
|TON H2=86 | |||
|TON HCOOH=316 | |||
|include=No | |include=No | ||
}} | }} | ||
}} | }} |
Revision as of 13:33, 17 November 2023
cat | cat conc [µM] | PS | PS conc [mM] | e-D | e-D conc [M] | H-D | H-D conc [M] | solvent A | solvent B | solvent C | solv A/B/C | additives | additives conc [M] | feedstock gas | feedstock volume | intensity | pH | T [°C] | λexc [nm] | t [h] | TON CO | TOF CO | Φ CO [%] | TON CH4 | TOF CH4 | Φ CH4 [%] | TON H2 | TOF H2 | Φ H2 [%] | TON HCOOH | TOF HCOOH | Φ HCOOH [%] | TON MeOH | TOF MeOH | Φ MeOH [%] | selectivity [%] [CO;CH4;H2;HCOOH;MeOH] | Φ all [%] | Details | include |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
0.002 | 0.2 | 0.1 |
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|
85/15 | 450 | 2332 | 106 | 1370 | 61.2%; 0%; 2.8%; 36.0%; 0% |
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No | |||||||||||||||||||||||||||
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0.2 | 0.1 |
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85/15 | 450 | 0 | 0 | 0 | n/a |
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No | |||||||||||||||||||||||||||
0.002 |
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0.1 |
|
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85/15 | 450 | 0 | 0 | 0 | n/a |
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No | |||||||||||||||||||||||||||
0.002 | 0.2 |
|
|
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85/15 | 450 | 950 | 86 | 316 | 70.3%; 0%; 6.4%; 23.4%; 0% |
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No |