Environmental Engineering Reference
In-Depth Information
The physical processes described by the model include:
Convective and radiative heat transfer from the surrounding fluid/environment to
the surface of the biomass particle
Radiative, convective, and conductive heat transfer inside the biomass particle
Momentum transfer to account for nonzero pressure gradients and nonuniform
velocity
Variable properties (thermal conductivity, porosity, and permeability)
Accumulation of volatile enthalpy and mass in the biomass pores
Volatile convection and diffusion in the pores of both the virgin biomass and the
charred region
The model assumes:
No secondary vapor decomposition and gasification of char
No particle shrinkage/swelling
)
constant volume
Symmetry
These assumptions result in the following equations:
∂
ρ
b
∂
=
−
r
1
ð
Eq
:
11
:
5
Þ
t
∂
ρ
ab
∂
=
r
1
−
r
2
−
r
3
ð
Eq
:
11
:
6
Þ
t
∂
ρ
c
∂
=
ν
c
r
2
ð
Eq
:
11
:
7
Þ
t
∂
ε
ρ
g
∂
+
∂
ρ
g
u
∂
+
∂
ρ
g
v
∂
=
ν
g
r
2
+
r
3
ð
Eq
:
11
:
8
Þ
t
x
y
∂
T
∂
ρ
g
c
p
,
g
u
∂
T
∂
ρ
g
c
p
,
g
v
∂
T
∂
ρ
c
c
p
,
c
+
ρ
b
c
p
,
b
+
ρ
ab
c
p
,
ab
+
ε
ρ
g
c
p
,
g
t
+
x
+
y
0
@
1
A
+
∂
∂
0
@
1
A
+
Q
r
ð
Eq
:
11
:
9
Þ
=
∂
∂
λ
x
∂
T
∂
λ
y
∂
T
∂
x
x
y
y
B
x
η
∂
p
∂
u
=
−
ð
Eq
:
11
:
10
Þ
x
B
y
η
∂
p
v=
−
y
+
ρ
g
g
ð
Eq
:
11
:
11
Þ
∂
p
=
ρ
g
R
u
T
MW
g
The ideal gas law
ð
Eq
:
11
:
12
Þ
:
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