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ME 475/675 Introduction to
Combustion
Lecture 3
Thermodynamic Systems (reactors)
1π‘Š2
1𝑄2
Inlet i
π‘šπ‘– 𝑒 + 𝑃𝑣
Outlet o
𝑖
Dm=DE=0
π‘š0 𝑒 + 𝑃𝑣
π‘œ
m, E
𝑄𝐢𝑉
π‘ŠπΆπ‘‰
• Closed systems
•
1𝑄2
− 1π‘Š2 = π‘š 𝑒2 − 𝑒1 +
𝑣22
2
−
𝑣12
2
+ 𝑔 𝑧2 − 𝑧1
• Open Steady State, Steady Flow (SSSF) Systems
• 𝑄𝐢𝑉 − π‘ŠπΆπ‘‰ = π‘š β„Žπ‘œ − β„Žπ‘– +
π‘£π‘œ2
2
−
𝑣𝑖2
2
+ 𝑔 π‘§π‘œ − 𝑧𝑖
• How to find changes, 𝑒2 − 𝑒1 and β„Žπ‘œ − β„Žπ‘– , for mixtures when temperatures and
composition change due to reactions (not covered in Thermodynamics I)
Calorific Equations of State for a pure substance
• 𝑒 = 𝑒 𝑇, 𝑣 = 𝑒(𝑇) ≠ 𝑓𝑛(𝑣)
• β„Ž = β„Ž 𝑇, 𝑃 = β„Ž(𝑇) ≠ 𝑓𝑛(𝑃)
For ideal gases
• Differentials (small changes)
• 𝑑𝑒 =
• π‘‘β„Ž =
πœ•π‘’
𝑑𝑇
πœ•π‘‡ 𝑣
πœ•β„Ž
𝑑𝑇
πœ•π‘‡ 𝑃
• For ideal gas
•
πœ•π‘’
=
πœ•π‘£ 𝑇
0;
+
+
πœ•π‘’
πœ•π‘£ 𝑇
πœ•β„Ž
πœ•π‘ƒ 𝑇
πœ•π‘’
πœ•π‘‡ 𝑣
= 𝑐𝑣 𝑇
πœ•β„Ž
πœ•π‘‡ 𝑃
= 𝑐𝑃 𝑇
• 𝒅𝒖 = 𝒄𝒗 𝑻 𝒅𝑻
•
πœ•β„Ž
=
πœ•π‘ƒ 𝑇
0;
• 𝒅𝒉 = 𝒄𝑷 𝑻 𝒅𝑻
• Specific Heats, 𝑐𝑣 and 𝑐𝑃 [kJ/kg K]
• Energy input to increase temperature of one
kg of a substance by 1°C at constant volume
or pressure
• How are 𝑐𝑣 𝑇 and 𝑐𝑃 𝑇 measured?
𝑑𝑣
𝑑𝑃
𝑐𝑝
𝑐𝑣
w
Q
m, T
V = constant
Q
m, T
P = wg/A = constant
• Calculate 𝑐𝑝 π‘œπ‘Ÿ 𝑣 =
𝑄
π‘šΔ𝑇 𝑝 π‘œπ‘Ÿ 𝑣
• Molar based
• 𝑐𝑝 = 𝑐𝑝 ∗ π‘€π‘Š; 𝑐𝑣 = 𝑐𝑣 ∗ π‘€π‘Š
T [K]
Q [joules]
Molar Specific Heat Dependence on Temperature
𝑐𝑝 𝑇
π‘˜π½
π‘˜π‘šπ‘œπ‘™ 𝐾
𝑇 [K]
• Monatomic molecules: Nearly independent of temperature
• Only possess translational kinetic energy
• Multi-Atomic molecules: Increase with temperature and number of molecules
• Also possess rotational and vibrational kinetic energy
Specific Internal Energy and Enthalpy
• Once 𝑐𝑣 𝑇 and 𝑐𝑝 𝑇 are known, specific enthalpy h(T) and internal energy u(T)
can be calculated by integration
• 𝑒 𝑇 = π‘’π‘Ÿπ‘’π‘“ +
• β„Ž 𝑇 = β„Žπ‘Ÿπ‘’π‘“ +
𝑇
𝑐
π‘‡π‘Ÿπ‘’π‘“ 𝑣
𝑇
𝑐
π‘‡π‘Ÿπ‘’π‘“ 𝑝
𝑇 𝑑𝑇
𝑇 𝑑𝑇
• Primarily interested in changes, i.e. β„Ž 𝑇2 − β„Ž 𝑇1 =
𝑇2
𝑐
𝑇1 𝑝
𝑇 𝑑𝑇,
• When composition does not change π‘‡π‘Ÿπ‘’π‘“ and β„Žπ‘Ÿπ‘’π‘“ are not important
• Tabulated: Appendix A, pp. 687-699, for combustion gases
• bookmark (show tables)
• Curve fits, Page 702, for Fuels
• Use in spreadsheets
• 𝑐𝑣 = 𝑐𝑝 − 𝑅𝑒 ;
• 𝑐𝑝 =𝑐𝑝 /π‘€π‘Š; 𝑐𝑣 =𝑐𝑣 /π‘€π‘Š
Mixture Properties
• Extensive Enthalpy
• π»π‘šπ‘–π‘₯ = π‘šπ‘– β„Žπ‘– = π‘š π‘‡π‘œπ‘‘π‘Žπ‘™ β„Žπ‘šπ‘–π‘₯
• π’‰π’Žπ’Šπ’™ (𝑻) =
• π»π‘šπ‘–π‘₯ =
π‘š 𝑖 β„Žπ‘–
π‘šπ‘‡π‘œπ‘‘π‘Žπ‘™
=
π’€π’Š π’‰π’Š (𝑻)
𝑁𝑖 β„Žπ‘– = π‘π‘‡π‘œπ‘‘π‘Žπ‘™ β„Žπ‘šπ‘–π‘₯
• π’‰π’Žπ’Šπ’™ (𝑻) =
𝑁𝑖 β„Žπ‘–
π‘π‘‡π‘œπ‘‘π‘Žπ‘™
=
πŒπ’Š π’‰π’Š (𝑻)
• Specific Internal Energy
• π’–π’Žπ’Šπ’™ (𝑻) = π’€π’Š π’–π’Š (𝑻)
• π’–π’Žπ’Šπ’™ 𝑻 = πŒπ’Š π’–π’Š 𝑻
• Use these relations to calculate
mixture specific enthalpy and internal
energy (per mass or mole) as functions
of the properties of the individual
components and their mass or molar
fractions.
• u and h depend on temperature, but
not pressure
Standardized Enthalpy and Enthalpy of Formation
• Needed to find 𝑒2 − 𝑒1 and β„Žπ‘œ − β„Žπ‘– for chemically-reacting systems because
energy is required to form and break chemical bonds
• Not considered in Thermodynamics I
π‘œ
• β„Žπ‘– 𝑇 = β„Žπ‘“,𝑖
π‘‡π‘Ÿπ‘’π‘“ + Δβ„Žπ‘ ,𝑖 (𝑇)
• Standard Enthalpy at Temperature T =
• Enthalpy of formation from “normally occurring elemental compounds,” at standard
reference state: Tref = 298 K and P° = 1 atm
• Sensible enthalpy change in going from Tref to T =
𝑇
𝑐
π‘‡π‘Ÿπ‘’π‘“ 𝑝
𝑇 𝑑𝑇
• Normally-Occurring Elemental Compounds
• Examples: O2, N2, C, He, H2
π‘œ
• Their enthalpy of formation at π‘‡π‘Ÿπ‘’π‘“ = 298 K are defined to be β„Žπ‘“,𝑖
π‘‡π‘Ÿπ‘’π‘“ = 0
• Use these compounds as bases to tabulate the energy to form other compounds
Standard Enthalpy of O atoms
• To form 2O atoms from one O2 molecule requires 498,390 kJ/kmol of energy
input to break O-O bond (initial and final T and P are same)
• At 298K (1 mole) O2 + 498,390 kJ οƒ  (2 mole) O
498,390 kJ
π‘˜π½
π‘œ
• β„Žπ‘“,𝑂 π‘‡π‘Ÿπ‘’π‘“ =
= + 249,195
2 π‘˜π‘šπ‘œπ‘™π‘‚
π‘˜π‘šπ‘œπ‘™π‘‚
π‘œ
• β„Žπ‘“,𝑖
π‘‡π‘Ÿπ‘’π‘“ for other compounds are in Appendices A and B, pp 687-702
• To find enthalpy of O at other temperatures use
π‘œ
• β„Ž 𝑂2 𝑇 = β„Žπ‘“,
𝑂2 π‘‡π‘Ÿπ‘’π‘“ + Δβ„Žπ‘ , 𝑂2 (𝑇)
Example:
• Problem 2.14, p 71: Consider a stoichiometric mixture of isooctane and
air. Calculate the enthalpy of the mixture at the standard-state
temperature (298.15 K) on a per-kmol-of-fuel basis (kJ/kmolfuel), on a
per-kmol-of-mixture basis (kJ/kmolmix), and on a per-mass-of-mixture
basis (kJ/kgmix).
• Find enthalpy at 298.15 K of different bases
• Problem 2.15: Repeat for T = 500 K
Standard Enthalpy of Isooctane
T [K]
298.15
theta
0.29815
h [kJ/Kmol]
-224108.82
a1
a2
-0.55313 181.62
-0.16492 8.072412
a3
a4
a5
-97.787 20.402 -0.03095
-0.8639 0.040304 0.103807
a6
-60.751
-60.751
• Coefficients π‘Ž1 to π‘Ž8 from Page 702
𝑇 [𝐾]
;
1000 𝐾
π‘˜π½
π‘œ
β„Ž
=
π‘˜π‘šπ‘œπ‘™π‘’
• πœƒ=
•
4184(π‘Ž1 πœƒ
πœƒ2
+ π‘Ž2
2
πœƒ3
+ π‘Ž3
3
• Spreadsheet really helps this calculation
+
πœƒ4
π‘Ž4
4
−
π‘Ž5
πœƒ
+ π‘Ž6 )
a8
20.232
Enthalpy of Combustion (or reaction)
Reactants
298.15 K, P = 1 atm
Stoichiometric
𝑄𝐼𝑁 < 0
π‘Šπ‘‚π‘ˆπ‘‡
Products
Complete Combustion
CCO2 HH2O
= 0 298.15 K, 1 atm
• How much energy can be released if product temperature and pressure are the
same as those of the reactant?
• Steady Flow Reactor
• 𝑄𝐼𝑁 − π‘Šπ‘‚π‘ˆπ‘‡ = 𝐻𝑃 − 𝐻𝑅 = π‘š β„Žπ‘ƒ − β„Žπ‘…
• π‘„π‘‚π‘ˆπ‘‡ = 𝐻𝑅 − 𝐻𝑃 = π‘š β„Žπ‘… − β„Žπ‘ƒ
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