functionalized composite electrodes for electrocatalytic hydrogenation c. m. cirtiu, n.-a. bouchard,...
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Functionalized Composite Electrodes for Electrocatalytic Functionalized Composite Electrodes for Electrocatalytic Hydrogenation Hydrogenation
C. M. Cirtiu, N.-A. Bouchard, H. Oudghiri-Hassani, P. A. Rowntree and H. MénardDépartement de Chimie, Université de Sherbrooke, Sherbrooke, (QC), Canada, J1K 2R1
Electrocatalytic hydrogenationElectrocatalytic hydrogenation Hydrogen generation:
H3O+ + e- + M ↔ MHads + H2O (Volmer reaction)
H3O+ + MHads + e- ↔ M + H2 + H2O (Heyrovsky reaction)
2 MHads ↔ 2 M + H2 (Tafel reaction) ECH of unsaturated organic compound:
Y=Z + A ↔ (Y=Z)adsA
(Y=Z)adsA + 2MHads ↔ (YH-ZH)adsA
(YH-ZH)adsA ↔YH-ZH + A
M – Pd, Pt, Ni, Rh, etc.
Hads – adsorbed hydrogen
A – catalyst matrix
Y=Z – unsaturated molecule
YH-ZH – saturated molecule
Design and characterization of the catalystDesign and characterization of the catalyst
Alumina is able to adsorb the aliphatic
acids and to generate an organic
monolayer on the surface of the matrix
(functionalization).
This functionalization can be carried
out in situ in the electrolysis cell.
The presence of the aliphatic acids adsorbed as carboxylate on alumina is confirmed by DRIFT spectra.
This new organic phase is stable for all temperature below to 200 ºC.
ECH resultsECH results
Concentration of co-solvent (MeOH)
Aliphatic carboxylic acid is more strongly adsorbed than phenol on catalyst (10% Pd/Al2O3).
Functionalized alumina supported Pd catalysts adsorb significantly more phenol than a Pd unsupported catalyst.
As predicted, the aliphatic chains adsorbed on alumina also influence the adsorption of phenol; as the chain lengthens, the adsorption is favoured.
The ECH efficiency increases with the length of the aliphatic chain (butyric acid > propionic acid > acetic acid).
The presence of a co-solvent (MeOH) modifies the polarity of the medium and also influences the adsorption of the target molecule to the functionalized catalyst surface; this too is predicted by the comparison with the reverse –phase chromatography.
A new concept is presented here: in situ functionalized materials for electrocatalytic hydrogenation processes.
These new materials are based on the strong controllable adsorption of aliphatic carboxylic acids onto the catalyst support.
This surface modification plays a key role in the adsorption/desorption phenomena of the target molecule onto catalyst surface.
A direct correlation has been established between current efficiency and adsorption phenomena for the phenol ECH, under our experimental conditions.
This sequence is predicted if the This sequence is predicted if the functionalized surface behave as a functionalized surface behave as a
reverse-phase chromatographic supportreverse-phase chromatographic support
ECH of phenol in water: methanol solution (80:20v/v) using different support electrolyte: (■) - acetic acid;
(●) - propionic acid; (▲) - butyric acid;
0 50 100 150 200 250 3000
10
20
30
40
50
60
70
80
90
100
Phen
ol C
once
ntra
tion
(%)
Charge (C)
Adsorption isotherms of phenol on 10% Pd/Al2O3 in
water: methanol solution (80:20v/v) in the presence of different electrolytes: (●) - acetic acid; (■) - propionic
acid; (▲) - butyric acid;
0,0 0,5 1,0 1,5 2,0 2,50,0
0,1
0,2
0,3
0,4
0,5
0,6
0,7
0,8
0,9
1,0
1,1
1,2
Q ad
s (m
ol g
-1)
Ce ( mol mL
-1)
IntroductionIntroductionThe aim of our research is to develop «intelligent electrodes» that are able to make use of molecular recognition at interface to facilitate electrocatalytic hydrogenation (ECH).
The present study demonstrates that the efficiency of the ECH process is related to the controllable adsorption phenomena. A functionalized surface can be obtained by in situ adsorption of aliphatic carboxylic acids on the catalyst matrix, adsorption which is supported by energy considerations.
These organically functionalized materials promote the adsorption of the target molecules under our experimental conditions, and may permit the development of selective ECH electrodes.
Ce= 0.1 µmole mL-1
Q= 100 C
ECH of phenol using different concentrations of MeOH as co-solvent: (♦) - 0 % MeOH; (●) - 20 %
MeOH; (■) - 50 % MeOH; (▲) - 60 % MeOH; T = 298 K;
0 50 100 150 200 250 300 3500
10
20
30
40
50
60
70
80
90
100
Ph
eno
l Co
nce
ntr
atio
n (
%)
Charge (C)
Adsorption isotherms of phenol on 10% Pd/Al2O3 in 0.5 M acetic buffer solution (pH = 5) for different
concentrations of co-solvent: (♦) – 0 % MeOH; (●) – 5 % MeOH; (■) – 20 % MeOH; (▲) – 50 % MeOH; T = 323 K;
0,0 0,1 0,2 0,3 0,4 0,5 0,6 0,7 0,8 0,9 1,0 1,1
0,00
0,01
0,02
0,03
0,04
0,05
0,06
Q ad
s (m
ol g
-1)
Ce (mol mL
-1)
0,000 0,005 0,010 0,015 0,020 0,025 0,0300
10
20
30
40
50
60
70
80
90
100
Eff
icie
ncy
(%)
Q ads
(mol g-1)
The ECH efficiency depends on the adsorption of phenol onto functionalized alumina catalyst surface
Micrographics of the secondary electrons (1) and cartography of the elements (2,3,4) for a ultra thin cut of 10% Pd/Al2O3
catalysts
Pd
Alumina
PdY=Z
Y=Z
Y=Z
YH-ZHYH-ZH
HHHH
H
H
H
Y=Z
organicchains
Al
2
O
3
Pd
4
10% Pd/Al2O3
1
Thermal analysis - mass spectroscopic data for Pd/Al2O3 butyric acid modified catalyst (under Ar)
0 100 200 300 400 500 600 700
H2
Temperature (°C)
CO2
Mass S
pectr
om
ete
r S
ign
al (a
.u.)
DRIFT spectra of the Pd/Al2O3 catalyst aliphatic
acids modified: (a) - acetic acid; (b) - propionic acid; (c) - butyric acid
TEM image of a ultra thin cut of 10% Pd-alumina catalyst (TEM Mag = 200000 x; HV= 80 kV)
ConclusionsConclusions
Catalyst support
Electrolyte: 0.5 M organic acid buffer (pH=5);
Solvent: H2O / H2O – MeOH;
Current intensity: 20 mA
Working electrode: CVR 100 ppi;
Catalyst: 200 mg 10%Pd/Al2O3;
Phenol concentration: 8.8510-3 M;
T = 298 K;
Experimental conditions for ECHExperimental conditions for ECH
Electrochemical dynamic cell
0 50 100 150 200 250 300
0
10
20
30
40
50
60
70
80
90
100
Ph
eno
l Co
nce
ntr
atio
n (
%)
Charge (C)
ECH of phenol in aqueous medium 0.5 M acetic buffer (pH = 5); catalyst: (■) – Pd submicron; (●) – 10% Pd/Al2O3;
0,0 0,5 1,0 1,5 2,0 2,5 3,0 3,5 4,0
0,00
0,01
0,02
0,03
0,04
0,05
0,06
Q ad
s (
mo
l g-1)
Charge (C)
Adsorption isotherms of phenol on: (■) – Pd 63 μm and (●) – 10% Pd/Al2O3 in 0.5 M acetic buffer
solution (pH = 5);
0,0 0,2 0,4 0,6 0,8 1,0 1,20,0
0,1
0,2
0,3
0,4
0,5
0,6
0,7
0,8
0,9
1,0
1,1
1,2
Q ad
s (
mo
le g
-1)
Ce (mole mL-1)
Adsorption isotherms of (▲) phenol and (■) acetic acid (pH=5) in water using 10% Pd-alumina supports.
ReferencesReferences
« Modification of the surface adsorption properties
of alumina supported Pd catalysts for the
electrocatalytic hydrogenation of phenol »
Ciprian M. Cirtiu, Hicham Oudghiri Hassani, Nicolas-
A. Bouchard, Paul A. Rowntree and Hugues Ménard,
accepted for publication in Langmuir
Organic phase nature
AcknowledgementsAcknowledgementsWe would like to thank:
Irène Kelsey Lévesque (SEM
analyses)
Charles Bertrand (TEM analyses)
NSERC ($$$) & FQRNT ($$$)