Biomedical Engineering Reference
In-Depth Information
APPENDIX
MASS AND ENERGY BALANCE OF TORREFIER
Assumptions
Torrefaction is mildly exothermic.
Torrefaction occurs at constant atmospheric pressure.
Negligible moisture in air.
A/F
5
Air
fuel ratio for stoichiometric combustion
5
14.6 for diesel oil.
T g0 is chosen higher than 100 C to avoid condensation in drier (assume
105 C).
T gi is chosen less than 300 C to avoid combustion of torrefied wood
(assume 300 C).
Heating values of volatile is estimated to be 1.286 MJ/kg on dry basis.
MASS BALANCE
Torrefier
From Figure 4A.1:
W 0 g 5
W t 1
W f 1
W g
On rearranging, one gets:
W 0 g 5
W f 1
W g
W t
(A.1)
W 0 g 5 W v 1 W vl 1 W g
where W vl is the volatile in fluid product leaving torrefier.
Moisture in fuel W v 5 MW f
(A.2)
where
is the excess air coefficient used in oil burner.
Substituting W 0 g
α
from Eq. (A.1) , we get:
W f 1
W g
W t 5
W v 1
W vl 1
W g
Substituting W v from Eq. (A.2) :
W vl 5
W f
W t
MW f
(A.3)
Oil Burner
From Figure 4A.2:
W g 5 W air 1 W oil 1 XW 0 g
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