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Torrefaction of biomass : influence of operating conditions on products

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(1)

Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 1

Torrefaction of biomass:

influence of operating conditions on products

Jean-Michel COMMANDRE

(2)

Context

-

High quality syngas

-Small amounts

of residual hydrocarbons and solid carbon

Biomass

must be ground finely

(≈ 100µm) before injection

Thermo-chemical conversion of biomass in

entrained flow reactor (EFR)

Grinding consumes large amounts of energy

High temperature (1400°C)

Short residence time (≈ s)

EFR

Syngas (CO, H

2

)

H

2

(3)

Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 3

Torrefaction

Torrefaction

: biomass pretreatment used to reduce mechanical properties

Objectives

:

Characterisation of

biomass torrefaction products

,

by the way of a complete quantification of the

products

released

from

biomass

analysis to precise

mass balances

,

(4)

Torrefaction at laboratory scale:

Crossed fixed bed reactor

- control of gas and wood temperature

-

control of gas nature and flow rate

-

gas flow rate sufficiently high to avoid

heterogeneous reactions

-

wood particles mixed with glass balls to ensure:

good contact between gas and wood particles

homogeneous gas flow inside the bed

Time

10°C/min 45 min

240 to

300°C

Operating conditions

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Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 5

Analytical devices

Karl-Fischer

GC-MS

(6)

Influence of torrefaction temperature

Pine wood

Good

reproducibility

Increase of mass loss

with temperature

(7)

Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 7

Global mass balance

(8)

Global mass balance

260°C

240°C

300°C

280°C

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Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 9

(10)

Detailed mass balance

(11)

Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 11

Detailed mass balance

240°C

260°C

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Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 13

Heating value

(14)

Ultimate analysis

Van Krevelen diagram

(15)

Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 15

Torrefaction at high heating rate

Simple first-order kinetic model

m

.

k

t

d

m

d

=

Mass loss ≈ 20%

Resid. time ≈ min

350°C

440°C

(16)

Torrefaction at high heating rate

Operating conditions:

Temperature = 350°C

Residence time:

5 min

Raw biomass

Torrefied biomass

(17)

Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 17

Torrefaction at high heating rate

Compared to 280 and 300°C:

• Less water and gas

Much more dry condensables

Global mass balance

Detailed mass balance

Compared to 280 and 300°C:

• Less formaldehyde

Much more propionic acid

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Forum PNRB Bioénergies – 21/01/10

WasteEng 2010 - Beijing 17/05/2010 19

Conclusions

A complete characterisation of products of biomass torrefaction has been realised

Cellulose, Hemicellulose and Lignin contents

Grindability: energy consumption during grinding

Work in progress:

Volatile matters released mainly contain water, dry condensable species,

CO

2

and CO

Dry Condensable species mainly contain acids, aldehydes and ketones

High heating rate influences significantly the torrefaction products

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