|
Gas |
Gas |
Kappa |
Gas Constant |
Specific Heat |
|
Air |
|
1.4 |
286.7 |
1,004 |
|
Ammonia |
NH3 |
1.3 |
488.2 |
2,092 |
|
Argon |
Ar |
1.67 |
208.1 |
519 |
|
Carbon Dioxide |
CO2 |
1.28 |
188.9 |
845 |
|
Carbon Monoxide |
CO |
1.4 |
296.8 |
1,042 |
|
Helium |
He |
1.66 |
2,078.5 |
5,200 |
|
Hydrogen |
H2 |
1.4 |
4,124 |
14,350 |
|
Methane |
CH4 |
1.32 |
518.2 |
2,223 |
|
Nitrogen |
N2 |
1.4 |
296.9 |
1,038 |
|
Oxygen |
O2 |
1.4 |
259.8 |
916 |
|
Water Vapor |
H2O |
1.33 |
188.5 |
1,690 |
Here are some of the basic engineering formulas/equations related to energy conversion systems which are built into the Engineering Software product line:
Continuity Equation
m =
vA
Momentum Equation
F = (vm + pA)out - in
Energy Equation
Q - W = ((h + v2/2 + gh)m)out - in
State Equation for Ideal Gas
pv = RT/MW
Perfect Gas
cp = constant
k = cp / cv
Isentropic Compression
T2 / T1 = (p2 / p1)(k-1)/k
T2 / T1 = (V1 / V2)(k-1)
p2 / p1 = (V1 / V2)k
Combustion
hreactants = hproducts
Isentropic Expansion
T1 / T2 = (p1 / p2)(k-1)/k
T1 / T2 = (V2 / V1)(k-1)
p1 / p2 = (V2 / V1)k
Sonic Velocity
vs = (kRT/MW) 1/2
Mach Number
M = v/vs
Isentropic Flow
Tt / T = (1 + M2(k - 1)/2)
pt / p = (1 + M2(k - 1)/2)k/(k-1)
ht = (h + v2/2)
Tt = (T + v2/(2cp))
Thrust
Thrust = vm + (p - pa)A
Cycle Efficiency
Cycle Efficiency = Net Work/Heat
Carnot Cycle Efficiency
Carnot Cycle Efficiency = 1 - Theat rejection / Theat addition
Brayton Cycle Efficiency
Brayton Cycle Efficiency = 1 - 1/(p2 / p1)(k-1)/ k
Otto Cycle Efficiency
Compression Ratio = V1 / V2
Otto Cycle Efficiency = 1 - 1/Compression Ratio(k-1)
Diesel Cycle Efficiency
Compression Ratio (CR) = V1 / V2
Cut-Off Ratio (COR) = V3 / V2
Diesel Cycle Efficiency = 1 - (CORk - 1)/(k*CR(k-1) *(COR - 1))
Fuel Cell
Fuel Cell Efficiency = - (Gout - Gin)/HHV
Heat Rate
Heat Rate = (1/Cycle Efficiency)*3,412
Physical Properties
For each reaction species, the thermodynamic functions specific
heat, enthalpy and entropy
as functions of temperature are
given in the form of
least squares
coefficients as
follows:
Cp/R = A1 + A2T + A3T2 + A4T3 + A5T4
H/(R*T) = A1 + A2T/2 + A3T2/3 + A4T3/4 + A5T4/5 + A6/T
S/R = A1lnT + A2T + A3T2/2 + A4T3/3 + A5T4/4 + A7
or
S/R = A1lnT + A2T + A3T2/2 + A4T3/3 + A5T4/4 + A7 - lnp
For each species, two sets of coefficients are included for two
adjecent temperature intervals, 273 to 1,000 [K]
and 1,000
to 5,000 [K]. The
data have been
constrained to be equal
at 1,000 [K].
Also,
U = H - p*v*MW or U = H - R*T
G = H - S*T
and
u = h - p*v or u = h - R*T/MW
g = h - s*T
Legend:
Cp -- Specific Heat [kJ/kmol*K]
cp -- Specific Heat [kJ/kg*K]
MW -- Molecular Weight [kg/kmol]
R -- Universal Gas Constant [kJ/kmol*K]
Gas Constant = R/MW [kJ/kg*K]
H -- Enthalpy [kJ/kmol]
h -- Enthalpy [kJ/kg]
T -- Temperature [K]
S -- Entropy [kJ/kmol*K]
s -- Entropy [kJ/kg*K]
p -- Pressure [atm]
U -- Internal Energy [kJ/kmol]
u -- Internal Energy [kJ/kg]
V -- Volume [m^3]
v -- Specific Volume [m^3/kg]
G -- Gibbs Free Energy [kJ/kmol]
g -- Gibbs Free Energy [kJ/kg]