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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