Literature Presentation
Debabrata Bagchi
Ph. D. Student
11/09/2021
Electrochemical CO2 reduction in
Acid medium
1
1
Prof. Sargent
3
Prof. Sinton
2
Prof. Fengwang
1-3:University of Toronto, Canada; 2:University of Sydney.
CO2RR in basic, acid & neutral media
3
Acidic electrolyte
Neutral/alkaline
electrolyte
CO2RR in flow cell
Adv. Funct. Mater. 2021, 2102151
(CEM, nafion)
(AEM, fumasep)
CO2RR in Flow cell and MEA
4
Alkaline Flow Cell Neutral Flow Cell MEA Electrolyzer
Joule 2019, 3, 2777–2791
5
Alkaline vs. Acidic Electrolyte
Carbon efficiency in
alkaline media is lower
than in neutral media
owing to additional
consumption of CO2 by
bulk OH–
6
Which is good electrolyte
Acid
Neutral Alkaline
(H+)
(CO3
-) (OH-)
High Current
High CO2RR yield
Low carbonate formation
High CO2RR yield
Moderate CO2RR yield
Goal
7
Acidic Electrolyte
Acid with CEM @400 mA/cm2
8
CO2 crossover tests in different electrolytes
1 M KHCO3 with AEM 0.5 M H3PO4 + 0.5 M KH2PO4 with CEM
Acid with CEM Acid with CEM
9
Cation augmenting
strategy to improve CO2
activation kinetics in
strong acid
Central concept
10
Modelling of pH near the cathode
pH 1.94 pH 3.02 pH 3.96
pH 2 pH 3 pH 4
H3O+ mass transport limitation occurs and H2O becomes the main proton donor
at the cathode surface
11
Effect of KCl addition
Faradaic efficiency on sputtered Ag with
different KCl concentrations
200 mA/cm2
12
Effect of K+ addition
(A) 1 M H3PO4. (B) 1 M H3PO4 + 1 M KCl. (C)
1 M H3PO4 + 2 M KCl. (D) 1 M H3PO4 + 3 M KCl
At current densities <200 mA/cm2
K+ does not play a role in the
activation of CO2 nor does it suppress HER
in a locally acidic environment
13
Cation-enabled CO2 reduction in acid
1M H3PO4 at 400 mA/cm2
1 M H3PO4 and 3 M KCl
on Cu
1 M H3PO4 and 3 M KCl
Tafel slope analysis
1M H3PO4
+2 M KCl
14
Role of K+ on HER and CO2RR
Total 400 mA/cm2
+1 M KCl
+3 M KCl
Under a proton-depletion local environment, the
cation triggers CO2 activation,
15
Control study: Effect of anions on CO2RR
@ 400 mA/cm2
In-situ EXAFS
K+ is not changing electronic state of Cu
Overall activity
How to get more K+
near electrode surface
?
16
Use of Cation-augmenting layer (CAL)
v
FE at
different J
perfluorosulfonic acid
17
XPS of CAL
18
CuNPs/PFSA composite material
1 M KCl 2 M KCl 3 M KCl
CO2R selectivity reached
61%, including a total C2+FE of 40%
19
Extended CO2R performance
Current density of 1.2 A cm−2 1 M H3PO4 + 3 M KCl
20
Operational cost breakdown of neutral CO2RR MEA electrolyzer
and alkaline flow-cell electrolyzer in ideal scenario
21
Techno-economic assessment of neutral CO2R MEA electrolyzer
and alkaline flowcell electrolyzer, together with specific cost
distribution per ton of ethylene produced
Acid
High Current
High CO2RR yield
No carbonate formation
22

Electrochemical CO2 reduction in acidic electrolyte.pptx

  • 1.
    Literature Presentation Debabrata Bagchi Ph.D. Student 11/09/2021 Electrochemical CO2 reduction in Acid medium 1
  • 2.
    1 Prof. Sargent 3 Prof. Sinton 2 Prof.Fengwang 1-3:University of Toronto, Canada; 2:University of Sydney.
  • 3.
    CO2RR in basic,acid & neutral media 3 Acidic electrolyte Neutral/alkaline electrolyte CO2RR in flow cell Adv. Funct. Mater. 2021, 2102151 (CEM, nafion) (AEM, fumasep)
  • 4.
    CO2RR in Flowcell and MEA 4 Alkaline Flow Cell Neutral Flow Cell MEA Electrolyzer Joule 2019, 3, 2777–2791
  • 5.
    5 Alkaline vs. AcidicElectrolyte Carbon efficiency in alkaline media is lower than in neutral media owing to additional consumption of CO2 by bulk OH–
  • 6.
    6 Which is goodelectrolyte Acid Neutral Alkaline (H+) (CO3 -) (OH-) High Current High CO2RR yield Low carbonate formation High CO2RR yield Moderate CO2RR yield Goal
  • 7.
  • 8.
    8 CO2 crossover testsin different electrolytes 1 M KHCO3 with AEM 0.5 M H3PO4 + 0.5 M KH2PO4 with CEM Acid with CEM Acid with CEM
  • 9.
    9 Cation augmenting strategy toimprove CO2 activation kinetics in strong acid Central concept
  • 10.
    10 Modelling of pHnear the cathode pH 1.94 pH 3.02 pH 3.96 pH 2 pH 3 pH 4 H3O+ mass transport limitation occurs and H2O becomes the main proton donor at the cathode surface
  • 11.
    11 Effect of KCladdition Faradaic efficiency on sputtered Ag with different KCl concentrations 200 mA/cm2
  • 12.
    12 Effect of K+addition (A) 1 M H3PO4. (B) 1 M H3PO4 + 1 M KCl. (C) 1 M H3PO4 + 2 M KCl. (D) 1 M H3PO4 + 3 M KCl At current densities <200 mA/cm2 K+ does not play a role in the activation of CO2 nor does it suppress HER in a locally acidic environment
  • 13.
    13 Cation-enabled CO2 reductionin acid 1M H3PO4 at 400 mA/cm2 1 M H3PO4 and 3 M KCl on Cu 1 M H3PO4 and 3 M KCl Tafel slope analysis
  • 14.
    1M H3PO4 +2 MKCl 14 Role of K+ on HER and CO2RR Total 400 mA/cm2 +1 M KCl +3 M KCl Under a proton-depletion local environment, the cation triggers CO2 activation,
  • 15.
    15 Control study: Effectof anions on CO2RR @ 400 mA/cm2 In-situ EXAFS K+ is not changing electronic state of Cu Overall activity How to get more K+ near electrode surface ?
  • 16.
    16 Use of Cation-augmentinglayer (CAL) v FE at different J perfluorosulfonic acid
  • 17.
  • 18.
    18 CuNPs/PFSA composite material 1M KCl 2 M KCl 3 M KCl CO2R selectivity reached 61%, including a total C2+FE of 40%
  • 19.
    19 Extended CO2R performance Currentdensity of 1.2 A cm−2 1 M H3PO4 + 3 M KCl
  • 20.
    20 Operational cost breakdownof neutral CO2RR MEA electrolyzer and alkaline flow-cell electrolyzer in ideal scenario
  • 21.
    21 Techno-economic assessment ofneutral CO2R MEA electrolyzer and alkaline flowcell electrolyzer, together with specific cost distribution per ton of ethylene produced Acid High Current High CO2RR yield No carbonate formation
  • 22.