Modeling of Combustion Systems A Practical Approach 13 potx
Modeling of Combustion Systems A Practical Approach 13 potx
... tem-
perature, T
BWT
, and the adiabatic flame temperature, T
AFT
. The actual
flame temperature as a function of concentration and time is the
ultimate goal, but it is immeasurable and incalculable, practically
speaking.
• ... Taylor & Francis Group, LLC
422 Modeling of Combustion Systems: A Practical Approach
Next, we consider how one may measure flame length. We
discuss...
Modeling of Combustion Systems A Practical Approach 14 potx
... orthogonalization factor
instantaneous heat release at z
q
0
fractional heat release at the floor
instantaneous heat release at z = 0
q
1
fractional heat release at the roof
q
g
fractional thermal power ... the flue gas at a given elevation
R universal gas constant
internal mass ratio of flue gas recirculation
external mass ratio of flue gas recirculation
internal molar ratio of flue gas r...
Modeling of Combustion Systems A Practical Approach 1 pot
... (Dry) Waste Gases
Natural Gas LPG
Cracked
Gas
Coking
Gas
Reforming
Gas
FCC
Gas
Refinery Gas
Sample 1
Refinery Gas
Sample 2
PSA
Gas
Flexicoking
Gas
Tulsa Alaska Netherlands Algeria Propane Butane
CH
4
93.4% ... 2006 by Taylor & Francis Group, LLC
540 Modeling of Combustion Systems: A Practical Approach
TABLE A. 3 (CONTINUED)
Chemical, Physical, and Thermal Properties of Gases...
Modeling of Combustion Systems A Practical Approach 2 pptx
... Modeling of Combustion Systems: A Practical Approach
TABLE B.1 Areas and Circumferences of Circles and Drill Sizes
Drill Size Diameter (in.) Circumference (in.) Area (in.) Area (ft)
80 0. 0135 0.042 ... 2006 by Taylor & Francis Group, LLC
555
Appendix B
Mechanical Properties
© 2006 by Taylor & Francis Group, LLC
570 Modeling of Combustion Systems: A Practical...
Modeling of Combustion Systems A Practical Approach 3 docx
... by Taylor & Francis Group, LLC
576 Modeling of Combustion Systems: A Practical Approach
TABLE C.2 (continued)
Unit Dimensions for Some Combustion- Related Quantities
Generic Name Examples
Exponents
Moles ... 574 Modeling of Combustion Systems: A Practical Approach
TABLE C.1
Common Conversions
TEMPERATURE CONVERSIONS
°C = 5/9 (°F – 32) °F = 9/5°C + 32
K = °C + 27...
Modeling of Combustion Systems A Practical Approach 4 doc
... LLC
584 Modeling of Combustion Systems: A Practical Approach
TABLE D.3
Properties of Saturated Steam and Saturated Water
Absolute
Pressure
Vacuum
Inches
of Hg
Temper-
ature
t
Degrees F
Heat of ... Taylor & Francis Group, LLC
580 Modeling of Combustion Systems: A Practical Approach
TABLE D. 2A (continued)
Standard Atomic Weights 1981 (alphabetical by elem...
Modeling of Combustion Systems A Practical Approach 5 docx
... −n
χ
αα
2
1
2
2
21=+−[],xn
1
2
0
1
−=
−
=
′
−
∑
F
e
x
x
x
x
()
!
χ
λ
λ
χ
αα
2
3
1
2
9
2
9
=−=
⎛
⎝
⎜
⎞
⎠
⎟
n
n
z
n
F
n
xe
n
x
nx
dx
()χ
2
2
0
2
22
1
2
2
2
=
⎛
⎝
⎜
⎞
⎠
⎟
∫
−
−
Γ
© 2006 by Taylor & Francis Group, LLC
601
Appendix E
Statistical Tables
© 2006 by Taylor & Francis Group, LLC
606 Modeling of Combustion Systems: A Practical Approach
TABLE E.4
F-Distribution, ......
Modeling of Combustion Systems A Practical Approach 6 pdf
... same routine
as before. However, we can take a shortcut whenever two bases are related
by the formula base B = base (A)
n
where A, B, and n are integers. In such a
case, we may group the base ... to their base 4 equivalent yields 32,22.2 . Table F.4 may make
609
Appendix F
Numbers in Binary, Octal, and
Hexadecimal Representations
For readers unfamiliar with binary and related bases, w...
Modeling of Combustion Systems A Practical Approach 7 pot
... 614 Modeling of Combustion Systems: A Practical Approach
Usually, one defines a reaction coordinate known as the conversion (x
k
),
having the property that for species k the reaction starts at ... is a constant
and N
k
is a variable. We may also write
(G.6)
For constant density, we have
,
where [k] is the concentration of species k, and [k
0
] is the starting concentra-...
Modeling of Combustion Systems A Practical Approach 8 doc
... reactant, the double-headed arrow (↔) means
that both the forward and reverse reactions occur (typically at different rates),
k is an index from 1 to n products, p
k
is the number of moles of ... 617
Appendix H
Equilibrium Primer
Consider a general reaction:
or equivalently
(H.1)
Here, j is an index from 1 to m reactants, r
j
refers to the number of moles
of the j
th
reactant, R...