processing swedish lignocellulosic residual material to ... · dennis jones, bror sundqvist sp wood...
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Processing Swedish lignocellulosic
residual material to furan pre-cursors
“Furu2Furan”
Dennis Jones, Bror Sundqvist
SP Wood Technology / EcoBuild
Sune Wännström
SP Energy Technology
William Mackintosh, Johan Malmberg, Anna Stenemyr
SP Process Development
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Furu2FuranConsortium comprising whole value chainsCompanies members of EcoBuild Competence Center(Competence centre for eco-efficient and innovative wood-based materials)
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VisionSP shall be a uniting force and a central resource contributingwith knowledge, research resources and management, test facilities and coordinationof bioeconomy initiatives in Sweden
SP – A uniting hub in
Bioeconomy
SP PROCESS
DEVELOPMENT
BIO-
ECONOMY
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� Today: too much focus on biofuel production (which may
not be the optimal use of the whole biomass)
� The furanic route to platform chemicals and high-value
commodities is almost neglected in current biorefinery
development
� There are some potential “winners” for the future biobased
economy but need to secure that enough chemicals for
these is produced in future biorefineries
Why are we doing this?
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The biorefinery concept
Jan van Dam, COST FP1205 presentation 2013
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The biorefinery concept – Furu2Furan
High value
chemicals
Jan van Dam, COST FP1205 presentation 2013
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Furu2Furan concept
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Softwoods yield hexoses
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Hardwoods and agri-fibres yield pentoses
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Some pathways
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5-hydroxymethylfurfural
(HMF)
Methylfuran
Bio-fuel
2-hydroxymethylfuran
Platform chemical
2,5-Dimethylfuran
Bio-fuel
2,5-bis(hydroxymethyl)furan
Monomer for polymer
production
Levulinic acid
Bulk chemical
Formic acid
Bulk chemical
2,5-Dimethyltetrahydrofuran
Solvent
2,5-Furandicarboxylic acid
Monomer for polymer
production
Conversion of HMF
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High-value end products of the F2F project
� Furfurylated wood (Kebony) with aesthetic appearance and performance similar to durable tropical timbers (and preservative treated timbers)
- European market for durable hardwood (tropical timber):
6 million m³/year => value: 6 billion Euro
- European market for preservative treated wood:
6 million m³/year => value: 1.5 billion Euro
� Coil Coatings (currently 99.9% fossil resource based). BioCoilCoat aims at 60% biobased.
SSAB alone use 4 kton/year (?): worth 20 million Euro
European market: 100 kton/year (?): worth 550 million Euro
� Thermoset composites today 99% fossil based
European market: 10 billion Euro worth?
bioderived resins can replace fossil based resins for many products
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Possible high-value bulk chemicals from the F2F project
� Maleic anhydride (currently 100% fossil based)
- Global production: worth 550 million Euro
� Adipic acid (currently 100% fossil based)
Global annual production: 2.3 million ton
Worth: 845 million Euro
� Caprolactone (currently 100% fossil based
Perstorp production (largest producer globally): 12 kton/year?
Perstorp caprolactone sales worth 60 million Euro/year
� Hexane diol (currently 100% fossil based)
BASF production (largest producer globally): 50 kton/year
Worth: 310 million Euro
� Aviation fuel (currently 100% fossil based). Possibly DMFu
Global annual prod of Jet fuel: 5 million barrels worth 500 million Euro
� Green aromatic solvents
Global prod. of BTX: 87 Mton worth 91 billion Euro
(BTX means Benzene, Toluene, Xylenes)( )
Thermoset polyesters
& polymerisat. catalyst
Polyamide (Nylon)
e.g. Shoe soles,
Medical plastics
Polymer building block
for e.g. PUR and PE
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� Saw dust
� Residuals from forest harvesting (stubs, tops and branches)
� Prehydrolysate from dissolving pulp production
� TMP and CTMP process water
Starting materialsA. Under-utilized forest products streams
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� Wheat straw
� Wheat bran
� Straw and bran from other Lantmännen crops
Starting materialsB. Under-utilized agricultural byproduct streams
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Lab scale work: SP-PD Chemical Processes: Xylose
to Furfural
From Hemicellulose
Furfural
Furfuryl alcohol
Furfural: Extracted from hydrolysate or transformed from isolated sugarIndustrial production in China, South Africa, Dominican republic
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Lit review from C5, xylose and furfural
Showed that furfural is currently being produced commercially from bagasse and/or corn stover
Inexpensive, high yields, tuned catalysts and conditions
However not from wheat straw.
Patents and publications containing furfural and wheat straw
Conclusions from literature
• More severe conditions, time, temp, acid: more furfural
• Milder conditions: more xylose to then produce furfural in a 2nd step.
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Experimental
Step 1:
Wheat straw and dilute sulfuric acid added to a microwave vial (10-20 mL) run under mild conditions.
The slurry was filtered, the filtrate analyzed, then used in step 2.
Step 2:
Filtrate & methyl isobutyl ketone (MIBK) combined in microwave vial (2-5 mL) High temps and short reaction time
Analysis of furfural yield by HPLC and/or LCMS
Microwavereactor
RP-HPLC
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Results- mild prehydrolysis of wheat
straw on the lab scale
Step 1: From mild conditions: A range of results is
observed in furfural and xylose content
The filtrate was then further reacted in step 2…
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•Liquid-liquid extraction
•Filter press
•Reactor system for synthesis
•Spinning unit
Filtration:Processum Pilot Park - Örnsköldsvik
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Results step 2-Conversion of xylose to
furfural
Higher temperatures: Highest yields of furfural were
achieved from the mildest hydrolysis runs from step 1.
72% yield obtained (78% in total, Aq phase included)
Yield in organic phase
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Literature Study of C6 sugars to HMF
Glucose is a sugar from cellulose and hemicellulose
Similar to mannose found in hemicellulose
Fructose to HMF
Vast amount of information in literature- 8 k items in scifinder.
Little in terms of
• Scaling up and production processes
Many catalysts for fructose to HMF
Not much reported regarding glucose to HMF
Fewer catalysts to convert glucose to HMF
Lower yields from glucose
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Experimental Work Flow for C6 sugars
Conditions and catalysts screened on
a small scale
• Via microwave in 2-5 ml vials
• Analysis of HMF performed by
HPLC and/or LCMS
Reaction of fructose to HMF first
investigated
• Higher yields and much
broader range of possibilities
• Catalysts screened
Then glucose to HMF investigated
• With use of knowledge
obtained from fructose trials
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Outline of the Experimental Parameters Considered
Catalyst
Soluble or insoluble
Reaction phase
biphasic (both water and solvent) vs. single phase
Ratio of water to solvent in biphasic system
Aqueous Phase Ionic Strength
Agitation
Solvent type
Concentration of sugar in the water phase
Temperature
Time
Replacing the solvent at intervals
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Screening of Catalysts
Less than desirable yields from:
Zeolites, Ag and Cs based polyacids,
phosphorylated niobium oxide, sulphuric acid
2 Best performers with fructose:
Phosphorylated Tantalum hydroxide vs. Calcium
phosphate (CaP2O6)
Next in trials with glucose:
Only 20% yield compared to 27% yield w same
conditions
• Glucose to HMF, 190oC, 20 min, 3 ml
MIBK to 2 ml H2O
*Daorattanachai, P. et al. Conversion of fructose, glucose, and cellulose to 5-hydroxymethylfurfural
by alkaline earth phosphate catalysts in hot compressed water, Carbohydrate Research, 363 (2012) 58-61.
* Yang, F. et al. Tantalum compounds as heterogeneous catalysts for saccharide dehydration to 5-hydroxymethylfurfural.
Chemical Communications, 47 (2011) 4469-4471.
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Reaction phases
Biphasic gave the best yields, with the solvent extracting HMF
Inhibits degrading/polymerizing of HMF in the water phase as it is extracted
Ratio of solvent to water likely requires optimization depending on the system
solvent:H2O optimum at 3:2 or 4:1
Higher concentrations of sugar in water does create more insoluble hummins and side reactions
Polymer (Humins)
formation
HMF +
glucose
HMF +
hydrated
HMF
* Rasmussen, H. et al. Formation of degradation compounds from lignocellulosic biomass in the
biorefinery:
Sugar reaction mechanisms, Carbohydrate Research, 385 (2014) 45-57.
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Agitation
Agitation is very important
• Creates maximum contact between the 2
phases.
• Important to transfer HMF from the
aqueous phase
• Decreases HMF degradation and
polymerization
*More humins with scale up in 20 ml
microwave vial
Alternative to agitation in larger scale
processing could be sonication
Catal
yst
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Solvent type
Extraction solvent is important
• Extracts HMF from water
M-THF: 8% HMF yield from glucose
MIBK: 27%
2-butanol: 30%, and 2% less HMF in water phase
2-butanol gave best results, but similar to MIBK
Is MIBK better for continuous processing?
-2-butanol dissolves a large amount of
water
Catal
yst
or Glucose
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Concentration of Sugar in the Aqueous Phase
The higher the concentration, the lower the yield
Due to HMF coming in contact with glucose and itself to form humins
This will also require optimization depending on the system
30 wt% glucose in water creates a large amount of side products
• Determined by HPLC
• Also much lower yields
6 wt% glucose in water used in most trials to provide high yields of HMF
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Scaling up: Pretreatment reactor
•Built for 230 °C and 30 bar
•Heated by steam (22bar)
•Used for batch reactions
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Both Mild and Harsh systems for wheat straw scaled
up in the Demo-Plant
Test Production
time
Temperature Acid
Load
Residence
time
Sampling
Unit h C % min Litres
1 6 187 0,2 5 1
2 6 190 0,5 5 1
4 6 205 1 5 1
5 6 215 1 5 1
5 12 187-190 0,2-0,5 5 100
6 12 205-215 1-1,5 5 100
Target: collecting 100 litres of xylose rich hydrolysate and 100 litres of furfural rich hydrolysate after dilute acid hydrolysis of wheat straw.
Demo Run Plan
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Biorefinery Demo Plant
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Demo plant
Domsjö Biorefinery site
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Fully integrated process from feedstock to distilled product
Operated 24h/ 7dTwo continuous flow-through hydrothermal reactors
One or two step acid hydrolysisDilute acid pretreatment + enzymatic hydrolysis
Five 10 m3 bio-reactorsEnzymatic hydrolysisFermentationCultivationGMM certified
FlexibleProcess configurationsForest and agro feedstocksBiorefinery applications (sugar platform)
Capacity, 2 tons of dry wood chips / 24 h
Demo Plant Facts
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1. Raw material intake
2. Feeding vessel
3. Steaming and impregnation
4. Pretreatment
5. Neutralisation and inhibitor control
6. Enzymatic hydrolysis and fermentation
7. Yeast propagation
8. Distillation
9. Product tank
10. Filter press
11. Solid material to incineration
12. Liquid to incineration/ biogas production
13. Evaporation Equipment
Layout
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horizontal reactor
vertical
reactor
impregnation
tank
slurry
tank
screw-s
screw-s
screw-s
H2SO
41
steam
steam
filtrate
sample position
wood
chips
Hydrothermal Pre-treatment of Lignocellulose
Feedstock
Feed
stock
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Earlier experiences (not targeting high yield of
furans)
Wheat straw
Mild pretreatment; ~2-6 g/l furfural, ~0-1 g/l HMF.
Harsh preteratment >10g/l
Spruce chips
Mild - medium pretreatment; ~2g/l furfural, ~3 g/l HMF
Pine chips
Medium – harsh pretreatment; ~4 g/l furfural, ~8-10 g/l HMF.
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Process – Sawdust and Wheat Straw
Ligno-cellulosic
Biomass (sawdust)
Pretreatment
&
fractionation
Lignin-rich solid residue
Sugars
and
furans
less
hydrolysed
Cellulose
Enzymatic
treatment
Pellet
processsing
Chemical
Processes
Chemical
Processes
Energy
Furfural
Furfuryl alcohol
FA/Furfural-mix
Fraction-
ation
HMF
Furfuryl alcohol
Dimethylfuran (fuel)
C5 & C6
(oligo-
& poly-
sacharides)
Fermentation
& distillationEthanol
Sugars
Or further hydrolysis
to furans
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Discussion
Understanding of the different streams. Contents, Assays, purity,
analytical methods and control.
Control of hydrolysis and extraction of Furans (Pilot/Demo plant)
How to process the different streams before chemical processing if
needed. Filtration, extraction, other methods
Defining Target furans of value based on the different streams and
demand.
No industrial process available for HMF from lignocellulose
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Separation Development
Feed stream: Sawdust hydrolysate containing furans, excluding lignin (from Örnsköldsvik).
Membrane filtration to separate furans from hydrolysate
Laboratory tests either at SPPD or at Alfa Laval
Pilot scale tests at Örnsköldsvik
“Purified streams” used for downstream chemistry
Extraction to separate furans from hydrolysate
Investigate downstream separation of product streams (when applicable)
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Reason for using filtration technology
Less chemicals in aqueous streams
Greater ease of disposal
Less need for additional chemical adidtional for clean up
Typically a TMP mill will release approx 3-5kg carbohydrates per
m3 of water
This means approx 300-400 kg of carbohydrates per hour
Potentially 3500 tonnes per annum ”lost”
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Potential of processing
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Concept of process
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Plant design
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Microwave applications
Lab scaleUp to 10 ml
Pilot scalePotential up to 0.6 m3
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Glucose/Fructose to HMF and downstream
Fructose is more reactive and selective to make HMF
than glucose i.e. higher yield
Starting from glucose likely involves isomerization to
fructose before dehydration to HMF
O
OHO
HMF
O OHH3C
OHHO
OH
Fructose
O
OHO
HMF
O OHH3C
OHHO
OH
Fructose
From Cellulose
FDCADimethyl furan
2,5-bishydroxymethyl furan
& Other Chemicals
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Conclusions of Furu2Furan
• Literature review, lab based experiments, pilot scale experiments
and demo plant runs carried
• All in a period of 9 months
• Additional work
• Environmental aspects
• Financial aspects
• Logistics
• Devising alternative pathways to new chemical derivatives
• Investigating pilot scale microwave processing
• Strong links built between industry partners
• New projects underway (OptiFuran, Furan2Market)