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14/7/2016 1
Development of an artificial photosynthesis device: from nano to macro-scale.
The BiVO4 example.
Simelys Hernández,*,1
Guido Saracco,1,2 Nunzio Russo.1
* E-mail: [email protected]
1 DISAT, Politecnico di Torino, Corso Duca degli Abruzzi 24, 10129 Torino (Italy)
2 Center for Sustainable Futures, CSF@POLITO, Istituto Italiano di Tecnologia, C.so Trento 21, 10129 Torino (Italy)
2H2O O2 + “2H2”
Solar EnergyLight reaction
“2H2” + CO2 (CH2O)Organic
molecules
Dark reacion
Two basic reactions of photosynthesis
UV
H++
Solar Fuels via Artificial Photosynthesis The “mimicking nature” approach:separation of the functions of light
collection and conversion from catalysis (e.g. Transition metal oxides: IrO2, Co3O4, RuO2, Mn2O3,… or Ru/ Co-
based molecular catalyst)
Many semiconductor materials (e.g.oxides, oxynitrides, oxysulfides,
oxyfluorides, and oxyfluoronitride) have been studyed to meet specific
requirements.
The direct water photo-electrolysis:
Why BiVO4 is interesting for water splitting ?
+ Good solar light absorption (band gap = 2.4 eV)
+ Conduction and Valence band edges straddling the red-ox potentials of water.
+ High chemical stability around neutral pHs
+ Earth abundant components
- Poor e- transport and limited superficial transfer properties that can lead to recombination of photo-exited charges.
Strategies to increase photo-activity of BiVO4
Study of Reaction kinetics of Water Splitting Catalysts
Evaluation of photoelectrodes
performance
9 cm2200 cm2
2500 cm2
Implementation of PEM Photo-electrolyzerfrom lab- to pilot-scale
1.6 m2
MJ-PV cell
H2 evolving PEC lab-reactor
Our work towards the Artificial Leaf…
Outline
1 cm2
Development of a system and a mathematical model to measure the actual activity of Water Oxidation Catalysts and Photo-catalysts (semiconductors) in powder form, for the water splitting reaction
Solar simulated light sourceBubbling Reactor
Clark-sensor & PH-meter
Mass Flow Controllers
Our research
Hernández S. et .al., Chem. Eng. J. 2014, 238, 17-267
Study of the kinetics for water oxidation half reactionof powder photo-catalysts
Vg
VLRO2
a)
b)
pO2
QAr+ ΦO2
pO2,analyzer
c)
d)
QAr
O2 CO2
Ag+1 Ag0
2H2O
BiVO4 Ar Bubble
hvh+
e-
4h+ + 2H2O → O2 +4H+ + 4e-
4Ag+1+ 4e- → 4Ag0
Water Oxidation
Silver Nitrate Reduction
8
RORO,O
LOR V)ε1(VH
akV)ε1(22
2
2−+⋅
−⋅=− RC
pC b
RTQV
Hak
RT εV ,O
RO,O
L,O
R2
2
22 bbb pC
pp⋅−⋅
−⋅−=
−⋅=
RTRTQ
RT V 222 O,OO
g
ppp b
)()(22 O,O ttptp analyzer ∆−=
Mathematical Model: O2 balance into the Bubbling reactor
- In the liquid phase:
- In the gaseous bubble phase:
- In the gas phase in the headspace above liquid
- In the gas phase at the analyzer:
Oxygen is formed on the catalyst surface
Actual rate of O2 evolution over time: RO2Hernández S. et .al., Chem. Eng. J. 2014, 238, 17-26
Strategies to increase photo-activity of BiVO4
BiVO4 in Powder form
14/7/2016 11
1μm
BiVO4 morphology control by Hydrothermal Synthesis
Thalluri S-M, et. al. Chem. Eng. J. 2014, 245, 124-132.
pH of the synthesis
media
Precursors: Bi(NO3)3.5H2O; NH4VO3 and (NH4)2CO3
0
2
4 - 6
8 - 10
14/7/2016 12
1μm
Thalluri M. et . al., Chem. Eng. J. 2014, 245, 124-132
BiVO4 morphology control by hydrothermal synthesis
14/7/2016 13Thalluri M. et. al., Ind. & Eng. Chem. Res. 2013, 52, 19, 17414-17418.
Optimization of calcination temperature of BiVO4 powders made at pH 0
Metal-doped BiVO4 powders by hydrothermal synthesis
Thalluri, S. M.; Hernández, S.; et. al. Appl. Catal. B: Environm. 2016, 180, 630-636.
We’ve improved the state-of-the-art photo-activity
(RO2o ~ 200 to 400 μmol/gcat.h) of
Mo & W-doped BiVO4
Development of a Photo-electrochemical Device for water splitting
BiVO4 electrodes from powders: By doctor-blade
PEC tests in Na2SO4 (0,1M) pH=6.5
Max. photo-current density at 1 sun & 1.23VRHE = 0.04
mA/cm2
Preparation of electrodes from BiVO4 powders
Max. photo-current density at 1 sun & 1.23VRHE = 0.6 mA/cm2
Dip-coating:
PEC tests in Na2SO4 (0,1M) pH=6.5
Preparation of BiVO4 electrodes by in-situ synthesis
S. Hernández, et.al., Applied Catalysis A: General, 2015, 504, 266-271.
Modeling of transport properties
S. Hernández, et. al., Applied Catalysis A: General, 2015, 504, 266-271.
Limitation of use dip-coating technique with intermediate calcination steps: Decrease of activity after a certain thickness (~160nm)
trapping of charges in the surface states
charge transfer between the electrolyte and the surface states
Rct: direct charge transfer
at the semiconductor/
electrolyteinterface
BV-3: larger impedance than the other two films -> reduced quantity of the deposited material.
BV-10 and BV-15: an additional process with time constant at very large frequencies (around 5 kHz) occurs, suggesting that a charge transfer mechanism occur via surface states -> due to an imperfect interconnection between adjacent layers in the thicker films.
Rct: 540 Ω
Rct + Rtrap = 580 Ω
Procedure 1 Precursors: Bi(NO3)3 ∙5H2O - NH4VO3
C1=50 mmol L-1 (in HNO3 1 M)Calcination: T1=773 K per 2 h.2 steps spin-coating on FTO:
500 rpm-10 s/ 2000 rpm- 15 s
Procedure 3Precursors: Bi(NO3)3 ∙5H2O -
VO(AcAc)2C3 =33 mmol L-1
(in Acetic Acid & Acetilacetone)Calcination: T3=673 K per 2 h.
1 step spin-coating on FTO:500 rpm-10 s
Procedure 2Precursors: Bi(NO3)3 ∙5H2O -
NH4VO3C2=200 mmol L-1 (in HNO3 2 M)Calcination: T2=673 K per 2 h.2 steps spin-coating on FTO:
500 rpm-10 s/ 2000 rpm- 15 s
Higher stability of the solution
Spin-coating
1.23V vs. RHE under solar light illumination (100
mW/cm2) in Na-phosphate Buffer (pH=7), active area:
4cm2
(Used for dip-coating)
Preparation of BiVO4 electrodes by in-situ synthesis
S. Hernández, et. al., Applied Catalysis B: Environm., 2016, 190, 66-74.
Strategies to increase the activity of BiVO4
BiVO4 photo-electrodes in FTO-glass
0
5
10
15
20
25
30
300 400 500
IPCE
(%
)
Wavelenght (nm)
IPCE at 1.23 V vs. RHEBiVO4 (6L)_WO3Mo-BiVO4BiVO4 (6L)WO3 (2)
WO3
Mo-BiVO4
BiVO4 / WO3Modification of high porous BiVO4 electrodes to better
exploits the high surface area
Preparation of BiVO4 electrodes by in-situ synthesis
S. Hernández et. al., Applied Catalysis B: Environm., 2016, 190, 66-74.D. Valerini et. al. Materials Science in Semiconductor Process. 2016, 42, Part 1, 150-154.
+ CoPi
0.4 0.6 0.8 1.0 1.2 1.40.0
0.5
1.0
1.5
2.0
Cur
rent
den
sity
(mA/
cm2 )
Potential vs. RHE (V)
WO3 (2)_BiVO4 (6L) 3%Mo-BiVO4 (6L) BiVO4 (6L) WO3 (2)
0.4 0.6 0.8 1.0 1.2 1.40.0
0.5
1.0
1.5
2.0
Cur
rent
den
sity
(mA/
cm2 )
Potential vs. RHE (V)
WO3 (2)_BiVO4 (6L)+CoPi 3%MoBiVO4_6L+CoPi
0 1 2 3 4 5 6 7 8 9 100.00.20.40.60.81.01.21.41.61.82.02.2
Cur
rent
den
sity
(mA/
cm2 )
time (min)
WO3 (2)_BiVO4 (6L) WO3 (2)_BiVO4+CoPi 3%Mo-BiVO4 (6L) 3%MoBiVO4+CoPi BiVO4 (6L) WO3 (2)
Mo doping enhances BiVO4activity by 6.5 fold.
Heterojunction BiVO4/WO3improves by 13 times BiVO4
performance
CoPi deposition increases de photocurrent of about 2 to 3
times.
Modification of high porous BiVO4 electrodes
Preparation of BiVO4 electrodes by in-situ synthesis
0.4 0.6 0.8 1.0 1.2 1.4 1.60.0
0.5
1.0
1.5
2.0
2.5
3.0
3.5
4.0CoPi-BiVO4 photo-anode with Illuminated area of
0.785 cm2
6 cm2
Cur
rent
den
sity
( m
A/cm
2 )
Potential vs. RHE (V)
At higher O2 evolution rates the higher covering of electrodes by bubbles creates mass transfer
limitations
Increase of electrode size can induce formation of defects
acting as recombination centres
MJ-PV cellLab H2 evolving PEC
Issues on scaling-up of photo-electrodes
S. Hernández et. al., Applied Catalysis B: Environm., 2016, 190, 66-74.S. Hernandez et. al., Journal of Physical Chemistry C 2015, 119, 9916-9925.
e-
H2O
2H+ + ½O2
2H+ + 2e-
H2
BiVO4 active area:8x8 cm2
Photo-electrodes scaling-up
24
Upper Plate housing BiVO4 over FTO
Grooved plates containing electrolyte
Lower Plate holding setupGrooved plates containing electrolyte
Nafion membrane separating two chambersCo NPs/C-GDL adjacent to Nafion membrane
Cathode: Co NPs / GDL
Cathodic electrolyte: 0.5mM Co-nitrate + 0.5M Na-Phosphate (pH=7)
Anode: 3%Mo-BiVO4 (AR5)
Anodic electrolyte: 0.5mM Co-nitrate + 0.1M Na-Phosphate (pH=7)
Liquid flow rate: 30 rpm (300 ml/min)
Artiphyction device configuration
e-
2H++2e-
H2
H2O
2H++ ½O2
H+
0 50 100 150 200 250 30050
100
150
200
250
300
350
Curre
nt (m
A)
time (s)
Photocurrent over time for each PV-PEC couples
00.5
11.5
22.5
33.5
44.5
55.5
0 1 2 3 4 5
J (m
A/cm
2 )
V bias (V)
Efficiency (%)5
4
3
2
1
Trade-off of performance
0.0 0.5 1.0 1.5 2.0 2.5 3.0 3.5 4.0 4.5 5.0 5.5 6.00
4080
120160200240280320360400
current decrease
of 19%
2 PVs for each PEC305 mA => 2.2 mA/cm2
Although activity reduces by 25%
-> current will decrease only 5%
Curre
nt d
ensit
y (m
A)
Voltage (V)
PEC curve (Active area 64 cm2) Hyphotesis of 25% of loss in activity on PEC Performance of 1.2 PV for each PEC (Area=75 cm2) 2 PVs for each PEC
Working Point = 192 mA => 1.4 mA/cm2
Artiphyction device operation
Lab-scale results
1.6 m2
Prototype…27
1.6 m2
Prototype…
Conclusions
In order to develop an efficient device for sun driven water splitting more advances on different fields are necessary:
- Development of efficient and stable water splitting(photo)electrocatalysts prepared by using scalable techniques
- Design of optimum device configurations able to diminishmass transfer limitations
- Improve of compactness of the system, for instance byincorporating solar capture systems (ex. PV cells) in thephotoelectrochemical reactor design.
Diana Hidalgo, Carminna Ottone, Adriano Sacco, Angelica Chiodoni, Marco Fontana, Marzia Quaglio, Katarzyna Bejtka, Guido Saracco, Nunzio Russo, Samir Bensaid, Mouli Thalluri, Marco Armandi, Barbara Bonelli, Edoardo Garrone, Giovanni Barbero, Anca Ionescu, Domenico Mombello, Fabrizio Pirri, Elena tresso.
Dr. Antonella Rizzo and Dr. Gabriele Valerini.
Dr. Vincent Artero and Dr. Bruno Jousselme
The European commission is gratefully acknowledged for the financial support and the partners of the 7th Framework Programme projects:
Acknowledgments
FP7- NMP2012 Collaborative project nr.309701 (2013-2016)
FCH-JU Call 2011-1 ArtipHyctionProject nr.303435(2013-2015)