Water-Assisted Highly Efficient Photocatalytic Reduction of CO2 to CO with Noble Metal-Free Bis(terpyridine)iron(II) Complexes and an Organic Photosensitizer/photocatalytic CO2 conversion: Difference between revisions
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< Water-Assisted Highly Efficient Photocatalytic Reduction of CO2 to CO with Noble Metal-Free Bis(terpyridine)iron(II) Complexes and an Organic Photosensitizer
investigation
Molecular process, Photocatalytic CO2 conversion experimentsNo edit summary |
No edit summary |
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|TON CO=6320 | |TON CO=6320 | ||
|TOF CO=127 | |TOF CO=127 | ||
|include=Yes | |||
}}{{Photocatalytic CO2 conversion | |||
|catalyst=Molecule:100948 | |||
|cat conc=0.01 | |||
|PS=Molecule:100938 | |||
|PS conc=0.05 | |||
|e-D=Molecule:100505 | |||
|e-D conc=0.28 | |||
|solvent A=Molecule:100529 | |||
|solvent B=Molecule:100616 | |||
|solvent-ratio=3:2 | |||
|feedstock gas=CO2 | |||
|λexc=420-650 | |||
|irr time=2 | |||
|TON CO=2780 | |||
|include=No | |||
}}{{Photocatalytic CO2 conversion | |||
|catalyst=Molecule:100947 | |||
|cat conc=0.01 | |||
|PS=Molecule:100938 | |||
|PS conc=0.05 | |||
|e-D=Molecule:100505 | |||
|e-D conc=0.28 | |||
|solvent A=Molecule:100529 | |||
|solvent B=Molecule:100616 | |||
|solvent-ratio=3:2 | |||
|feedstock gas=CO2 | |||
|λexc=420-650 | |||
|irr time=2 | |||
|TON CO=4500 | |||
|include=No | |||
}}{{Photocatalytic CO2 conversion | |||
|catalyst=Molecule:100949 | |||
|cat conc=0.01 | |||
|PS=Molecule:100680 | |||
|PS conc=0.05 | |||
|e-D=Molecule:100505 | |||
|e-D conc=0.28 | |||
|solvent A=Molecule:100529 | |||
|solvent B=Molecule:100616 | |||
|solvent-ratio=3:2 | |||
|feedstock gas=CO2 | |||
|λexc=420-650 | |||
|irr time=2 | |||
|TON CO=19 | |||
|include=No | |||
}}{{Photocatalytic CO2 conversion | |||
|catalyst=Molecule:100949 | |||
|cat conc=0.01 | |||
|PS=Molecule:100680 | |||
|PS conc=0.05 | |||
|e-D=Molecule:100505 | |||
|e-D conc=0.28 | |||
|solvent A=Molecule:100530 | |||
|solvent B=Molecule:100616 | |||
|solvent-ratio=3:2 | |||
|feedstock gas=CO2 | |||
|λexc=420-650 | |||
|irr time=2 | |||
|TON CO=992 | |||
|include=No | |include=No | ||
}} | }} | ||
}} | }} |
Revision as of 11:36, 16 May 2024
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 |
---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|---|
0.01 | 0.05 | 0.28 |
|
|
3:2 | CO2 | 420-650 | 2 | 6320 | 127 | n/a |
|
Yes | ||||||||||||||||||||||||||
0.01 | 0.05 | 0.28 |
|
|
3:2 | CO2 | 420-650 | 2 | 2780 | n/a |
|
No | |||||||||||||||||||||||||||
0.01 | 0.05 | 0.28 |
|
|
3:2 | CO2 | 420-650 | 2 | 4500 | n/a |
|
No | |||||||||||||||||||||||||||
0.01 | 0.05 | 0.28 |
|
|
3:2 | CO2 | 420-650 | 2 | 19 | n/a |
|
No | |||||||||||||||||||||||||||
0.01 | 0.05 | 0.28 |
|
|
3:2 | CO2 | 420-650 | 2 | 992 | n/a |
|
No |