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Use of LCA tools in the early stages of a research
project - A case study about an innovative process for
cellulose nanocrystals extraction
Lille, November 2013
Olivier Talon, Séverine Coppée, Jevgenij Lazko,
Tangi Sénéchal, Jean-Marie Raquez
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microfibril
fiber
H2SO4 Heating
Centrifugation Dialysis
Cellulose Fiber Cellulose Nanocrystals
Cellulose nanocrystals extraction
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Cellulose nanocrystals extraction
Process not so green
High consumption of acid and water
Cellulose nanocrystals :
 High Young’s Modulus (= steel)
 Interesting shape/aspect ratio (needle like)
 Extracted from biomass (potentially from local biomass)
Green nanoparticles
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Cellulose nanocrystals extraction
Ionic Liquids are presented as green solvents of cellulose :
Reuse of reagent
+ Recyclability
+ Low VOC emissions
+ Good solvation of lignocellulose
Low amount of sulfuric acid
Decrease of water consumption during purification
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- Environmental cost of IL production?
Currently not industrial scale product
- How much recycling to improve our process?
How many cycles needed for environmental benefit?
How many possible to keep a good extraction?
The success of nanocrystals extraction at bench will not directly
provide information about the greenness of the process
First bench results coupled with Simple LCA can help to pinpoint
critical points
Background of the study
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Background of the study
Evaluation of the “greenness” potential of the study
Simultaneous kick-off as first lab experiments
 Identification of hotspots
hydrolysis
water
H2SO4 hydrolysis
[BMIM]Cl
water
H2SO4
purificationwater purification
water
H2SO4
H2SO4
[BMIM]Cl
CNC
fibers
CNC
fibers
[BMIM]Cl
©MateriaNova–Allrightsreservedforallcountries
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Comparison of lab scale processes
s-o-a and experimental data
Virtual upscaling of the new process
(industrial scale)
Need to recover values of
s-o-a process
No data on detailed or described
industrial process
NEWSTRATEGY
Comparison needs data for same scale of production
Background of the study
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Highly simplified hypotheses
Identical yields and raw materials
 fibers out of system boundaries
No intrinsic impact of BMIM Recycling  modeled by input division
Same energetic input  not taken into account
No effluent treatment  treated as emission to water
Same nanocrystal quality
 FU = treatment for 1 kg of CNC
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Data collection / choice of the method
Emissions : Choice of a proxy based on toxicology literature (phenol)
LCA literature negligible about IL or CNC, non existent for the combination
Material inputs: firsts lab tests estimation
No IL in the DB, neither as process nor as substance
DB : no waste water treatment for a comparable process
1 publication about LCA of [BMIM]Cl production
Calculation method:
- including phenol and H2SO4 emissions
- including a “water depletion” category
 restricted choice: ILCD 2011 Midpoint
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BMIM-Cl modelisation
From literature, Righi 2011
Single score, Eco-indicator
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Impacts of the different processes
ILCD calculation
0
20
40
60
80
100
[BMIM]Cl process / 10 cycles
sulphuric acid process
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Major impact contributors for « BMIM »
process
ILCD calculation
0
20
40
60
80
100
BMIM-Cl
water / purification
water / hydrolysis
sulphuric acid
process emissions
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Le Fonds Européen de Développement Régional et
la Région Wallonne investissent dans votre avenir
Optimisation way of BMIM process
IL recycling optimization
ILCD calculation
0
20
40
60
80
100
process BMIM V2 - 10 cycles
process BMIM V2 - 20 cycles
process BMIM V2 - 40 cycles
process sulfu V4
©MateriaNova–Allrightsreservedforallcountries
Cannotbedisclosed,usedorreproducedwithoutpriorwrittenspecificauthorizationofMateriaNova
Le Fonds Européen de Développement Régional et
la Région Wallonne investissent dans votre avenir
BMIM-Cl synthesis optimization (yield)
ILCD calculation
0
10
20
30
40
50
60
70
80
90
100
BMIM[Cl] process / 10 cycles
BMIM[Cl] process / 10 cycles / optimized IL synthesis
sulphuric acid process
Optimisation way of BMIM process
48%  90%
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Le Fonds Européen de Développement Régional et
la Région Wallonne investissent dans votre avenir
Conclusions
Necessity to refine the model:
- treatment/ recycling of the acid
- intrinsic impact of recycling of ionic liquid (if cycles nb increased)
First results
 environmental benefit is not automatic
Numerous ways of improvement:
- IL recycling (> 20 cycles in some publications)
- “greener” production of [BMIM]Cl (or other ILs) ?
(not matured production, scale effect, biosourcing…)
- Yield and quality of CNC ?  FU modification ?
(theoretical better thermal resistance)
Scientific contribution of the project is not in balance with LCA
©MateriaNova–Allrightsreservedforallcountries
Cannotbedisclosed,usedorreproducedwithoutpriorwrittenspecificauthorizationofMateriaNova
Le Fonds Européen de Développement Régional et
la Région Wallonne investissent dans votre avenir
MATERIA NOVA
Olivier Talon, Séverine Coppée, Jevgenij Lazko,
Tangi Sénéchal, Jean-Marie Raquez
email: ylca@materianova.be
Thanks for your attention

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Use of LCA tools in the early stages of a research project