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Lignin Production by Organosolv Fractionation of Lignocellulosic Biomass W.J.J. Huijgen P.J. de Wild J.H. Reith Presented at the International Biomass Valorisation Congress, 13-15 September 2010, Amsterdam, The Netherlands. ECN-L--10-083 September 2010

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Page 1: Lignin Production by Organosolv Fractionation of ... · Lignin Production by Organosolv Fractionation of Lignocellulosic ... Lignin Production by Organosolv Fractionation of Lignocellulosic

Lignin Production by Organosolv Fractionation of Lignocellulosic

Biomass

W.J.J. Huijgen

P.J. de Wild

J.H. Reith

Presented at the International Biomass Valorisation Congress, 13-15 September 2010, Amsterdam, The Netherlands.

ECN-L--10-083 September 2010

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Lignin Production by Organosolv Fractionation of

Lignocellulosic Biomass

Wouter Huijgen, Paul de Wild & Hans Reith

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Contents

Introduction

Lignin & lignocellulosic biomass

Biomass pre-treatment & fractionation

Organosolv fractionation

Experimental set-up

Process conditions

Catalysts

Lignin

Production

Characterisation

Conclusions

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Lignin & Lignocellulosic Biomass

Lignin major structural constituent of lignocellulosic biomass.

Lignocellulosic biomass:

Hardwood: e.g., poplar, willow (LignoValue).

Softwood: e.g., spruce, pine.

Herbaceous: e.g., miscanthus, wheat straw (LignoValue).

Available in form of:

(Forestry / agricultural) residues.

Energy crops.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Lignocellulose Constituents

Cellulose

Factors influencing composition:

Type of plant

Part of plant (bark, stem, …)

Age of plant

Lignin (model)

Based on its chemical composition, lignocellulose potential feedstock for:

Biofuels (e.g., bioethanol).

Wide range of chemicals (including aromatics from lignin).

Lignin:

Polymer of aromatic compounds.

Sugar polymers:

Cellulose, linear polymer of glucose.

Hemicellulose, branched copolymer of C5 and C6 sugars.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Ultrastructure Lignocellulosic Biomass

Structural components strongly linked (physically & chemically).

Cellulose:

Present in fibers.

Crystalline structure with amorphous regions.

Cellulose fibrils backbone of wood.

Lignin:

Functions as ‘glue’, providing physical strength.

Protection against decay.

Cellulose chain:

up to 1000’s

glucose units

Micro-

& macrofibrils

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Enzymatic Cellulose Hydrolysis

Route for production sugar derivatives including 2G biofuels:

Enzymatic hydrolysis cellulose to sugars.

(Bio)chemical conversion of sugars.

Pre-treatment: overcoming nature’s protection (biomass ‘recalcitrance’).

Pre-treatment:

Improving accessibility cellulose for enzymes by:

Removing non-cellulose components (fractionation).

Reducing crystallinity of cellulose.

Creating specific surface area.

….

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Pre-treatment

Alternative:

Separation of lignin prior to enzymatic hydrolysis, while preserving the

chemical structure of lignin organosolv.

Several physical-chemical pre-treatment routes under development.

Main pretreatment routes:

(Dilute) acid pre-treatment

Steam explosion

Routes effective for cellulose.

However:

Lignin ends up in residue (with unconverted sugars, process chemicals, ash, etc).

Residue generally only suitable for CHP.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Organosolv Process

HemicelluloseOrganosolvLignin

separation

Solvent

separation

Cellulose (S)

(to enzymatic hydrolysis)

Lignin (S)

Solvent recycling

Water (+ catalyst)

Organic solvent

Lignocellulose

LignoValue organic solvent:

Ethanol

Typical process conditions:

160-200 °C, 15-120 min, 5-30 bar.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Lignocellulose Biorefinery

Pretreatment

&

fractionation

Lignin

Enzymatic

hydrolysis

Pretreatment

&

fractionation

Lignocellulosic

biomass &

residual streams

Fermentation

Conversion

&

synthesis

Ethanol

Butanol

Lactic acid

Propanediol

Thermochemical

depolymerisation

& conversion

H/P

Chemical derivatives,

e.g. surfactants

Platform chemicals,

e.g. phenolics, styrene,…

Performance products

Electricity

Heat

Cellulose

Hemi-

cellulose

Primary biorefinery Secondary biorefinery

Fuel additives

Pretreatment

&

fractionation

Lignin

Enzymatic

hydrolysis

Pretreatment

&

fractionation

Lignocellulosic

biomass &

residual streams

Fermentation

Conversion

&

synthesis

Ethanol

Butanol

Lactic acid

Propanediol

Thermochemical

depolymerisation

& conversion

H/P

Chemical derivatives,

e.g. surfactants

Platform chemicals,

e.g. phenolics, styrene,…

Performance products

Electricity

Heat

Cellulose

Hemi-

cellulose

Primary biorefinery Secondary biorefinery

Fuel additives

Aim ECN organosolv technology:

Fractionation of all major constituents in a sufficient quality for valorisation.

Including extraction of high-quality lignin for production of chemicals.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Experimental Set-up Organosolv Fractionation

Willow / straw

Filtration

Milling

Solid residue

Filtrate

Washing

Optional:

catalyst

Lignin separation &

analysis

Analysis

composition

Enzymatic hydrolysis

Analysis sugars

(monomeric +

oligomeric)

Analysis other

compounds

EtOH / H2O

Volume: 0.5 / 2 ltr

Stirring

Temperature ↑

T reactor

T jacket

p

0 tt

T p

T reactor

T jacket

0 t

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Process Parameters

Extensive parametric study performed:

Ethanol-based fractionation of willow wood and wheat straw.

Fractionation and enzymatic hydrolysis of cellulose-enriched

fraction.

Studied variables:

Particle size (0.25-10 mm)

Solvent mixture : solid ratio (L/S) (5-20 L/kg)

Solvent-water ratio (0-85 wt%)

Pretreatment severity:

– Temperature (160-220 °C)

– Reaction time (0-120 min)

– Acid catalysts such as H2SO4

Stirring rate (100-500 rpm)

Aft

er

org

an

oso

lvF

resh

wh

ea

t str

aw

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International Biomass Valorisation Congress, Amsterdam21-04-2010

Process Temperature

Organosolv fractionation & pre-treatment effective, positive effect temperature:

Lignin extraction and hemicellulose hydrolysis increase.

Above 200 ºC, cellulose hydrolysis and degradation of sugars during pre-treatment.

Large enhancement of enzymatic hydrolysis cellulose (LignoValue: yield up to ~90%).

0

20

40

60

80

100

160 190 200

T [°C]

Fra

cti

on

ati

on

[%

]

Pulp yield

Glucan hydrolysis

Xylan hydrolysis

Delignification

0

20

40

60

80

100

160 190 200

Ethanol : water [% w/w]

En

zy

ma

tic

glu

co

se

yie

ld [

%]

Willow

EtOH:H2O 60:40 wt%

60 min

No catalyst

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Pre-treatment Effect

Fresh willow Pre-treated willow

(190°C, 60 min, 60wt% EtOH)

Cellulose fibrous structure remains intact.

Extraction of hemicellulose and lignin.

More open structure better access for enzymes.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Solvent-Water Ratio: Fractionation

Ethanol major influence on delignification and hemicellulose hydrolysis.

Optimum EtOH-H2O ratio for delignification (~60 wt% EtOH).

Solubility of lignin (fragments) dependent on solvent mixture composition.

Willow

190 °C

60 min

No catalyst

0

20

40

60

80

100

0 28 57 85

EtOH:H2O [w/w %]

Fra

cti

on

ati

on

[%

]

Pulp yield Glucan hydrolysis

Xylan hydrolysis Delignification

0

5

10

15

20

25

30

0 20 40 60 80 100

EtOH : H2O [w/w %]

Lig

nin

[g

/L]

20 g/L (ECN)

40 g/L (ECN)

20 g/L (Ni et al.)

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Solvent-Water Ratio: Enzymatic Hydrolysis

Willow

190 °C

60 min

No catalyst

Enzymatic digestibility very low at high EtOH

percentage (poor fractionation).

Cellulose digestibility optimum around 30% w/w

EtOH (trade-off delignification and hemicellulose

hydrolysis).

Optimization process conditions dependent on

revenues various products.

LignoValue:

Focus on lignin.

Ethanol-water ratio ~60% w/w selected.

0

20

40

60

80

100

0 28 57 85

Ethanol : water [% w/w]

En

zy

ma

tic

glu

co

se

yie

ld [

%]

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Catalysts

Addition of H2SO4:

Improved fractionation (especially hemicellulose hydrolysis, but also delignification).

Increase enzymatic digestibility pretreated willow.

However, cellulose hydrolysis during fractionation and increase degradation reactions.

Willow

60:40% w/w EtOH-H2O

200 °C

30 min

0

20

40

60

80

100

0 0.01 0.025 0.033

H2SO4 [M]

Fra

cti

on

ati

on

[%

]

Pulp yield

Glucan hydrolysis

Xylan hydrolysis

Delignification

0

500

1000

1500

2000

2500

3000

0 0.01 0.025 0.033

T [°C]

Co

nc

en

tra

tio

n [

mg

/L]

5-(Hydroxymethyl)-2-furaldehyde

2-Furaldehyde

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Feedstocks

Effectiveness organosolv dependent on type of

lignocellulosic biomass.

In general:

Organosolv less effective for softwoods and

(more dense) hardwoods.

More severe pretreatment conditions or use of

catalyst required.

LignoValue:

Organosolv effective for both willow wood and

wheat straw.

Organosolv particularly suitable for straw.

Str

aw

Will

ow

Pre-treatedFresh

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Lignin dissolved in ethanol-water liquor together

sugars, soluble ash minerals, etc.

Separation by adjusting ethanol-water ratio.

Lignin Separation from Organosolv Liquor

0

5

10

15

20

25

30

0 20 40 60 80 100

Composition solvent [wt% EtOH]

Lig

nin

dis

so

lve

d [

g/L

]

20 g/L (ECN)

40 g/L (ECN)

20 g/L (Ni et al.)

Lab protocol:

Preconcentration and water addition.

Rapid & efficient separation of lignin from filtrate.

Maximum lignin yield obtained LignoValue

feedstocks: ~70%.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Lignin Characterisation

Lignin appearance:

Light brown to black (compacted) powder.

Colour and structure dependent on process conditions

organosolv, biomass type and contaminants.

Purity:

Lignin relatively pure (>90 wt%, up to 96% for wheat

straw derived lignin).

Main contaminant oligomeric xylose (hemicellulose).

Lignin sulphur- and ash-free (max 0.1 wt% S).

Solubility:

H2O (none), ethanol, acetone & dioxane (good).

160, 180, 200, 220 °C

0

20

40

60

80

100

- 20 40 60 80 100

Solvent composition [wt% organic solvent]

Part

lig

nin

dis

so

lved

[%

]

Ethanol

Acetone

Dioxane

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Lignin Characterisation - II

Molecular weight:

Low mean molecular weight (2000-3500) relative to other types of lignins.

Relatively narrow distribution.

Organosolv lignin promising properties for valorisation (relative to other types of lignin).

Organosolv lignin

31P-NMR:

Identification of functional groups.

SGH type lignins in different ratios depending on feedstock.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Conclusions

Fractionation & pre-treatment:

Ethanol-based organosolv able to fractionate willow wood and wheat straw.

Enzymatic hydrolysis cellulose improved substantially (up to ~90% for wheat straw).

Organosolv particularly effective for straw.

Recycling organic solvent crucial process element to be studied further.

Organosolv lignin:

Efficient separation of lignin.

High purity (up to 96% for wheat straw derived lignin).

Promising properties for production of chemicals and performance products.

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International Biomass Valorisation Congress, Amsterdam14-09-2010

Thank you for your attention!

More information:

[email protected]

http://www.lignovalue.nl/

Agentschap NL, EOS-LT (2007-2010)