Modeling of Combustion Systems A Practical Approach 14 potx
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 ... LLC
Modeling of Combustion Systems
A Practical Approach
Joseph Colannino
A CRC title, part of the Taylor & Francis imprint, a member of the
Taylor & Francis Gr...
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 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% ... LLC
542 Modeling of Combustion Systems: A Practical Approach
TABLE A. 3 (CONTINUED)
Chemical, Physical, and Thermal Properties of Gases: Gases and Vapors,
Including Fuels...
Modeling of Combustion Systems A Practical Approach 2 pptx
... 2006 by Taylor & Francis Group, LLC
555
Appendix B
Mechanical Properties
© 2006 by Taylor & Francis Group, LLC
570 Modeling of Combustion Systems: A Practical Approach
TABLE B.3
K Factors
Contractions
1. ... LLC
556 Modeling of Combustion Systems: A Practical Approach
TABLE B.1 Areas and Circumferences of Circles and Drill Sizes
Drill Size Diameter (in.) Ci...
Modeling of Combustion Systems A Practical Approach 3 docx
... Btu/ft-hr-°F
641.4 kcal/hr
745.7 W
© 2006 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 ... 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...
Modeling of Combustion Systems A Practical Approach 4 doc
... 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 the
Liquid
Btu/lb.
Latent
Heat of ... 174.967
Magnesium Mg 12 24.305 g
Manganese mn 25 54.9380
© 2006 by Taylor & Francis Group, LLC
580 Modeling of Combustion Systems: A Practical Approach
TABLE D. 2A (cont...
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
... A Practical Approach
Base 2 is ideal for constructing factorial designs because the system com-
prises only two states for any factor: high and low. In base 2, the only
numbers we may use are ... = base (A)
n
where A, B, and n are integers. In such a
case, we may group the base A symbols in groups of n and convert each
group directly to its base B equivalent. In the present cas...
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 ... the total moles of the reaction. This gives
(G.13)
We may also write as a function of conversion:
(G .14)
Typically, we use Equation G.8 or Equation G.10 to recast Equation G...
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...