Nozzles and diffusors
Stagnation properties
h0, T0, p0, v0, i0, s0 (Total)
State that the fluid reaches when the stream is slowing down up to rest by means of a reversible and adiabatic process.
We apply the first law of thermodynamics (considering adiabatic process)
Q̇E + ĊI = 0
Δh + ΔEK,g,Ψ
Technical equation conservation law
di = ν dp + dEK,g,Ψ + dΨw = 0
Ideal O = ν dp + dEK
We integrate this relation between initial condition and total condition:
O = ∫pp0 ν dp + ∫cc0 dEK
We follow an ideal process and an adiabatic process
Ψw = 0
QE = 0
Tds = dQe + dΨ = 0
dS = 0 (Isentropic Process)
Now:
∫pp0 ν dp = ∫pk=const dp = const1/kpk+1/k |pp0 = (pv)1/k = (p0)k - pk+1= 1/1/k ν = K/k-1 [ ( p0/P )k-1 - 1 ]
And also, about energy:
∫cc0 dEK = ∫cc0 c²/2 dc = c²/2 |cc0 = -c²/2
Nozzles and diffusors
h, T, p, v, i, sStagnation Properties
h⁰, T⁰, p⁰, v⁰, i⁰, s⁰ (total)
State that the fluid reaches when the stream is slowing down or to rest by means of reversible and adiabatic process.
We apply the first law of thermodynamics (considering adiabatic process)
∑Q̇e + ∑Ẇi = Δh + ΔEk, p, g, w
Technical Equation Conservation Law
dẋi = vdp + dEk, p, g, w + dẆw = 0
ideal 0 = vdp + dEk
We integrate this relation between initial condition and total condition:
0 = ∫pp⁰ vdp + ∫cc⁰ dEk
We follow an ideal process and an adiabatic process
Ẇw : 0
∑Tds = dqc + dẋw -> dS = 0 (isentropic process)
Now:
∫pp⁰ vdp = ∫pp⁰ const/ p1/k dp = const/kP1/k ∫pp⁰ pk+1 dp = (pv)1/k (k/k-1)k-k-1 [pk]= [pk]1/k - :=[p1/k vk/k-1 Pk-1/k Pk-1/k k/k-1 ]
And also, about energy:
∫cc⁰ dEk = ∫cc⁰ dc²/2 = -c²/2
PVkk-1 = c²/2
po = p[1 + k-1/2 M²]k/k-1
For Definition
cs2 = (∂p/∂ρ)s = k const ρk = const p/ρρk = const => P/ρk = const
SO k PV = cs2c/cs = M (MACH NUMBER)
- M < 1 → Subsonic
- M > 1 → Hypersonic
Substituting above we hold:
po = p[1 + k-1/2 M²]k/k-1
To compute the total density we consider p/pk = po/pok (Adiabatic transformation)
ρo = ρ(po/p)1/k => ρo = ρ[1 + k-1/2 M²]1/k-1
For Ideal Gas
PV = RT
dh = CpdT => h° - h = Cp(T° - T)
P°V° PV = T°T => T°T = P°V/PV(1 + k - 1/2Π2)k - 1/k - 1 = 1
Hence for Ideal Gas:
T° = T(1 + k - 1/2Π2)
We introduce the meaning of nozzles
In general, these are in machines. In a nozzle, the velocity increases => dc > 0, while if we have a diffuser, dc < 0.
We consider the inlet section and outlet section:
=> { } => 0 2
We don't know what there is in the middle. To study it in a simple way, we introduce some hypotheses:
- Ideal process (dL = 0)
- Adiabatic process (dQ = 0)
- One-dimensional fluid flow
- Steady state condition G = const
This is the meaning of steady state condition.
dG = 0 (remember that G = ρAC)
=> dG/G = dP/ρ + dA/A + dC/C = 0
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Appunti dell'esame Thermal and hydraulic machines
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Thermal and hydraulic machines - Temi d'esame svolti
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Thermal And Hydraulic Machine Part2
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Thermal Machines - Steam plants, Gas turbines, Hydraulic turbines