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Fig. 10 Variation in heating
value with increase in
torrefaction temperatures for
two different kinetics. (i)
Kinetics obtained from Wang
et al. ( 2012b ) and (ii) kinetics
from Table 4
Wang et al, 2012 [9]: 30 minutes
Present kinetics: 30 minutes
Wang et al, 2012 [9]: 60 minutes
Present kinetics: 60 minutes
1.3
1.25
1.2
1.15
1.1
1.05
1
200
220
240
260
280
300
Temperature ( o C)
variation in heating value ratios obtained for two different residence times. Kinetics
obtained from Wang et al. ( 2012b ) resulted in higher losses in Lignin which
decreased the heating value of the torre
ed samples.
3.3 RQ Factor for Fuels
3.3.1 CO 2 Emissions
Boie equation can be used to derive an expression to estimate the CO 2 emitted in
tons per GJ of energy input from the fuel chemical composition as given in the
Eq. ( 16 ).
1
44
1
;
000
n
422 ; 270
C
422 ; 270
C
o ð
CO 2 in tons/GJ
¼
16
Þ
117 ; 385
177 ; 440
422 ; 270
1 þ
The CO 2 in tons per GJ of energy input
is given according to Eq. ( 17a )
(Thanapal 2014 ).
kg O 2
HHV O 2 in GJ
kmol O 2
32 kg
01 kg
kmol CO 2
44
:
CO 2 in tons per GJ energy input
¼
RQ
0
:
001 tons
kg
ð
17a
Þ
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