Post on 19-Oct-2020
Technologies de prétraitement
Jean-Luc Wertz and Prof. Michel Paquot
VALEBIO 23 mars 2012
PLAN1 Transformation de la biomasse en énergie et produ its
1.1 La bioraffinerie
1.2 Voie biochimique
1.3 Voie thermochimique
2 Prétraitements
2.1 Prétraitements physiques
2.2 Prétraitements chimiques (p. ex. organosolv)
2.3 Prétraitements physico-chimiques (p. ex. steam explosion)
2.4 Prétraitements biologiques
2.5 Résumé
Définition Bioraffinage
Le bioraffinage est le processus durablede transformation de la biomasse en:1. bioénergie (biocarburants, électricité, chaleur) 2. produits biobasés (alimentation, produits chimiques, matériaux)
Raffineries de 1ère et 2ème génération
• Première génération: raffinage à partir de biomasse alimentaire (canne à sucre,, grains de maïs, huile végétale…)
• Deuxième génération: raffinage à partir de biomasse non alimentaire (résidus agricoles et forestiers, déchets municipaux…)
Crude oil refining
Crude oil
Fuels(Energy)
Building blocks(Petrochemistry)
Specialties(e. g. lubricants)
Biomass refining
Biomass
Biofuels(Bioenergy)
Building blocks(Agro-bio chemistry)
Specialties(e. g. biolubricants)
Procédés de transformation
• Plateforme biochimique- Hydrolyse acide (dilué ou concentré)- Hydrolyse enzymatique
• Plateforme thermochimique- Combustion- Gazéification- Pyrolyse & traitement hydrothermique
Dilute acid hydrolysis
Concentrated acid hydrolysis
Enzymatic hydrolysis
Plateforme biochimique Défis
- Prétraitement de la biomasse- Coût et efficacité des enzymes- Fermentation des sucres C5 and C6 - Valorisation de la lignine
Thermochemical conversion: primary routes
Gazéification + Fischer-Tropsch
Conversion de la biomasse en gaz de synthèse ou syngas (H2 + CO) suivie de la conversion du syngas par synthèse Fischer-Tropsch en carburants liquides (BtL)
Synthèse Fischer-Tropsch
Pyrolyse + conversion catalytique
Conversion de la biomasse en bio-huiles, eux-mêmes convertis en carburants liquides
Schematic of the role of pretreatment
Source: P. Kumar et al., 2009
Liquid hot water (LHW)Pretreatment with liquid water at high temperature and pressure
Source: N. Mosier et al., 2005
Liquid hot water
Performance: Strong removal of hemicelluloses but formation of inhibitor
Inbicon’s hydrothermal pretreatment pilot plant Source: Inbicon
Weak and strong acid hydrolysis
1 Weak acid:
-High-temperature (>160°C), continuous-flow process for low solids loadings
-Low-temperature (<160°C) batch process for high solids l oadings
Performance: Strong removal of hemicelluloses but formation of inhibitors
2. Strong acid:
Powerful agents for cellulose hydrolysis (no enzymes are needed after the strong acid process)
Performance: High monomeric sugar yield but toxic and corrosive
Alkaline hydrolysis
Well known in the pulp and paper industry as kraft pulping (or sulfate process) where wood chips are treated with a mixture of NaOH and Na2S
Performance: Weak removal of hemicelluloses, strong removal of lignin
Extraction of lignin from Kraft pulp mill black liquor by the LignoBoost process
Source: Metso, LignoBoost
� Precipitation of lignin from black liquor by lowering the pH with CO2
� Dewatering by filtration� Redispersion of lignin� Dewatering by filtration of the new slurry� Washing to produce lignin cakes
Organosolv processesSolvolytic cleavage of an alpha-aryl ether linkage by nucleophilic substitution; R=H or CH3; B=OH, OCH3
Performance: Weak removal of hemicelluloses, strong removal of lignin
Some important organosolv processes
ProcessName
Solvent / Additive
Asam Water + sodium carbonate + hydroxide + sulfide+ methanol / Anthraquinone
Organocell Water + sodium hydroxide + methanol
Alcell (APR) Water+ low aliphatic alcohol (e.g. ethanol)
Milox Water + formic acid + hydrogen peroxide (forming peroxyformic acid)
Acetosolv Water + acetic acid/Hydrochloric acid
Acetocell Water + acetic acid
Formacell Water + acetic acid + formic acid
Formosolv Water + formic acid + hydrochloric acid
Lignol’s process based on water/ethanol pre-treatment
Source: Lignol
Oxidative delignification
1. Hydrogen peroxide treatment
2. Ozone treatment
3. Wet oxidation: treatment with oxygen or air in combination with water at high temperature and pressure
Performance: Decrystalisation of cellulose, weak removal of hemicelluloses, strong removal of lignin
Room temperature ionic liquidsMain cations and anions in ionic liquids
Performance: Partial to complete dissolution of biomass with easy recovery of cellulose upon anti-solvent addition
Room temperature ionic liquidsDifferent types of interaction present in imidazolinium-based ionic liquids
Source: H. Olivier-Bourbigou, 2010
Room temperature ionic liquidsProposed mechanism for cellulose dissolution in EmimAc (1-ethyl-
3-methyl imidazolium acetate)
Source: J. ZHANG et al., 2010
Source: S. Bose et al., 2010
Room temperature ionic liquidsHydrolysis of cellulose in a mixture of cellulases and tris-(2-hydroxyethyl)
methyl ammonium methylsufate (HEMA)
+
Steam explosionSchematic of the steam explosion process. 1, sample charging valve; 2, steam supply valve; 3, discharge valve; 4, condensate drain valve
Performance: Strong removal of hemicelluloses but formation of inhibitors
Principle:Treatment of biomass with high-pressure saturated steam, followed by a rapid reduction of steam pressure to obtain an explosive decompression
Source: T. Jheo, 1998
Ammonia pre-treatments
1. Ammonia fiber explosion (AFEX™): biomass is exposed to liquid ammonia at high temperature and pressure and then pressure is reduced
2. Ammonia recycle percolation (ARP): aqueous ammonia passes through biomass at high temperature, after which ammonia is recovered
Performance: Strong decrystallisation of cellulose, weak removal of hemicelluloses
Ammonia Fiber Expansion Process
– Moist biomass is contacted with ammonia
– Temperature and pressure are increased
– Contents soak for specified time at temperature and ammonia load
– Pressure is released
– Ammonia is recovered and reused
Reactor Explosion
AmmoniaRecoveryRecovered
AmmoniaAmmonia
vapor
Reactor Expansion
Ammonia Recovery
BiomassTreated
Biomass
Heat
What is AFEX™?
AFEX™ is a trademark of MBI
Source: MBI
Glucan conversion for various AFEX treated Feed sto cks
SwitchgrassSugarcaneBagasse
DDGS
Rice straw
Corn stover
Miscanthus
UT=No PretreatmentAFEX=Ammonia Pretreatment
Biomass Conversion for Different Feedstocks Before and After AFEX
Glucan conversion afterenzymatic hydrolysis
Excellent Biomass Conversion After AFEX Pretreatment
Source: MBI
Carbon dioxide explosion
High pressure carbon dioxide, and particularly supercritical carbon dioxide is injected into the reactor and then liberated by an explosive decompression
Performance: Strong decrystalisation of cellulose, strong removal of hemicelluloses
Mechanical/alkaline pre-treatment
Continuous mechanical pre-treatment with the aid of an alkali
Performance: Weak removal of hemicelluloses, strong removal of lignin
Biological pre-treatmentsWhite-rot fungi are the most efficient in causing lignin degradation
Source: L. Goodeve, 2003
Source: R.A. Blanchette, 2006
Performance: strong removal of hemicelluloses and lignin
XX: Major effect; X: Minor effect;; *: increases crystallinity; 1) alters lignin structureInhibitors: furfural from hemicelluloses and hydroxymethylfurfural from cellulose and hemicelluloses
Pretreatment Decrystallization of cellulose Removal o f hemicelluloses Removal of lignin Inhibitor formati on
Liquid hot water 1) XX XX
Weak acid 1) XX XX
Alkaline X XX
Organosolv X XX
Wet oxidation XX X XX
Steam explosion* 1) XX XX
Ammonia fiber explosion (AFEX)
XX X
CO2 explosion XX XX
Mechanical/alkaline X XX
Biological XX XX
Performance summary
Performance summary
1. All pretreatments partially or totally remove hemicelluloses
2. Wet oxidation, AFEX and CO2 explosion reduce cellulose crystallinity
3. Alkaline, organosolv, wet oxidation, mechanical/alkaline and biological partially or totally remove lignin
4. High amounts of fermentation inhibitors are formed with liquid hot water, weak acid and steam explosion
Thank you for your attention