State the definition of the Knudsen Number and explain it’s relevance.
mit
λ: mittlere freie Weglänge der Moleküle
L: charakteristische Länge (z. B. Rohrdurchmesser)
Relevanz:
Sie beschreibt das Verhältnis zwischen molekularer Bewegung und makroskopischer Länge.
Für Kn < 0.01: Kontinuumsmechanik ist gültig → Navier-Stokes-Gleichungen anwendbar.
Für Kn > 0.1: Molekulare Effekte werden wichtig → Gasdynamik erfordert kinetische Modelle (z. B. Boltzmann-Gleichung).
Wichtig bei sehr kleinen Längen (z. B. Mikrokanälen) oder sehr dünner Atmosphäre (z. B. Höhenflug).
How is the speed of sound defined in the framework of thermodynamics?
Die Schallgeschwindigkeit aaa ist in der Thermodynamik definiert als:
p: Druck
ρ: Dichte
Ableitung bei konstanter Entropie (isentropisch)
Für ideale Gase:
γ: isentroper Exponent (cp/cv)
R: spezifische Gaskonstante
T: Temperatur
Which effects have to be neglected when Euler-Equations are applied?
Viscosity → No shear stresses (no internal friction)
Heat conduction → No heat transfer due to temperature gradients
Diffusion → No mass transfer due to concentration gradients
How is total enthalpy related to total energy?
H = U + p*V or H = E + p/rho
Which effects cannot take place in isentropic flows?
shocks (changes that are not smooth)
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Viscous dissipation → No friction or shear → no entropy production
Heat transfer → No heat exchange with surroundings
Shock waves → Shocks are irreversible and produce entropy
Mixing or diffusion → These cause entropy increase
Explain the concept of a “material derivative”.
The material derivative describes the rate of change of a quantity (e.g. temperature, velocity) as experienced by a moving fluid particle.
It combines local and convective changes:
Where:
ϕ: any scalar or vector field (e.g. temperature, velocity)
∂ϕ/∂t: local (Eulerian) time change at a fixed point
v*∇ϕ: change due to movement through a spatial gradient
Meaning: It tracks how a property ϕ\phiϕ changes along the path of a fluid element — essential for describing unsteady and spatially varying flows.
Why are the balance laws for momentum and total energy balance laws but not conservation laws (in a strict sense)?
The momentum and total energy equations are called balance laws, not strict conservation laws, because:
They include source terms:
Momentum balance includes body forces (e.g. gravity)
Energy balance includes work (e.g. pressure forces) and heat transfer
A conservation law requires that a quantity is conserved without external input or loss. → Only mass is conserved in a strict sense (no source or sink).
Conclusion: Momentum and energy can be added to or removed from the system by external actions → they obey balance, not strict conservation.
State the thermal and the caloric EoS for a perfect gas.
Under which conditions is total enthalpy constant?
Total enthalpy h0h_0h0 is constant when the flow is:
Adiabatic (no heat transfer)
No work is done on or by the fluid (no shaft work, no electrical work)
No viscous dissipation (frictionless flow)
Steady flow (no time dependence)
Summary: In an isentropic, steady, inviscid, adiabatic flow without body forces or external work, total enthalpy remains constant along a streamline.
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Does the total conditions relation for temperature require s=const?
At which position in a nozzle can M=1 be reached?
Only at the smallest cross-section
Can flows featuring shocks be isentropic?
no, shocks are always a jump in entropy (not const. entropy and no smooth change)
Give the definition of the critical Mach number.
What does “critical temperature” mean in a fluid mechanics sense?
Static Temperature when M = 1 is reached
How is the relative mass flow density defined?
The relative mass flow density
is the mass flow rate per unit area. For a perfect gas in isentropic flow, it is often expressed in terms of Mach number:
In dimensionless (normalized) form, relative to stagnation conditions:
This shows how the mass flow per area changes with Mach number under isentropic conditions.
Note: This expression reaches a maximum at M=1M = 1M=1 → used in choked flow and nozzle design.
Sketch relative mass flow density against Mach number.
Are solutions of the Mach-Area-Relation unique?
not necessarily; if the flow is supersonic in the div. part of the nozzle, the ma differs
Why is there a kink in the state distribution for a certain back pressure?
Bc. of the split up of two possible solutions, either we stay subsonic or reach supers.
1. last subsonic solution (critical subsonic solution)
2. isentropic solution/ ideal adapted flow solution
the kink is at A_min and is the point where it is decided
Why is total temperature constant across a steady normal shock?
How do static and total quantities vary across a normal shock?
Sketch the pressure distribution for subsonic and ideally adapted supersonic flow.
Explain the idea of normal shock solutions.
Normal shock solutions stem from the non-linear nature of the 1D Euler equations, which can mathematically admit multiple solutions.
The key idea:
When analyzing compressible flows, we must check if multiple solutions exist and whether they are physically admissible.
In the case of a normal shock:
A jump from supersonic (M > 1) to subsonic (M < 1) is physically possible, but
A jump from subsonic to supersonic would require a decrease in entropy, which violates the second law of thermodynamics → not physically allowed
Conclusion: Only solutions that satisfy the conservation laws and result in increasing entropy (or at least no decrease) are physically valid. This ensures the shock wave proceeds from M > 1 to M < 1.
Why do all transonic nozzle flows feature the same mass flow (for given p0 , T0 )?
Because at Mach 1 (choked flow), the mass flow rate reaches its maximum for a given total pressure and total temperature:
When M=1M = 1M=1 at the throat of the nozzle, → the flow is choked → the mass flow becomes independent of the exit pressure
Any further decrease in back pressure does not increase the mass flow → only leads to changes in the diverging section (e.g. shocks or expansion)
The converging section of the nozzle stays the same for all choked conditions
Therefore: All transonic flows with M=1M = 1M=1 at the throat have the same mass flow, and higher mass flow is only possible by increasing either:
the throat area A∗A^*A∗
the total pressure p0p_0p0
or the total temperature T0T_0T0
This is the essence of maximum mass flow condition in compressible nozzles.
Why is our theory not sufficient for explanation of all possible back pressures?
The quasi-1D theory (steady, isentropic, area-varying flow) cannot explain all possible back pressure scenarios because:
It neglects non-isentropic effects like shocks and viscous losses
It assumes 1D flow, but some phenomena (e.g. oblique shocks) are inherently 2D or 3D
It cannot model shock-induced flow separation, boundary layers, or shock reflections
For strongly over-expanded nozzles, the flow may become unstable or asymmetric, which 1D theory cannot capture
Example:
Oblique shocks and shock-boundary layer interactions require multi-dimensional models
Conclusion: The basic theory is a good approximation for many cases, but realistic nozzle flows under all back pressures require more advanced models, including shock theory, 2D/3D flow and viscous effects
Give three options for visualization of compressible flow features.
1) Schlieren technique
2) Shadowgraphy
3) Mach-Zehnder interferometry
Schlieren photography – Visualizes density gradients using light refraction – Commonly used to observe shock waves and expansion fans
Shadowgraphy – Also shows density changes, but based on second derivative of refractive index – Simpler setup than Schlieren, but less sensitive
Interferometry – Measures precise density fields by observing interference patterns in light – Allows quantitative flow field analysis
What does a schlieren knife do?
The Schlieren knife (or knife edge) cuts out a portion of the light in the focal plane of the Schlieren setup.
It blocks light rays that are deflected due to changes in fluid density, which affect the refractive index.
The angle and position of the knife determine how strongly these density variations appear (e.g., as brighter or darker regions).
By adjusting the knife’s angle, different aspects of the flow (e.g., shocks, shear layers) can be emphasized.
This selective blocking enhances the visibility of compressible flow phenomena like shock waves or expansion fans.
Which quantity is visualized in Schlieren and Shadow imaging?
Schlieren: 1st Derivative of Density
Schadow: 2nd Derivative of Density
Both Schlieren and Shadowgraph techniques visualize effects caused by variations in fluid density — but they differ in what quantity they highlight:
Schlieren imaging visualizes the first spatial derivative of density (∂ρ/∂x or ∂ρ/∂y), i.e. density gradients. → It is sensitive to the direction of the gradient and is adjustable via the knife edge orientation.
Shadowgraph imaging visualizes the second spatial derivative of density (∂²ρ/∂x² or ∂²ρ/∂y²), i.e. changes in the density gradient (density curvature). → It is more sensitive to sharp changes, like shock waves.
How can a boundary layer in a nozzle be visualized?
Schlieren Technique with the knife in normal direction so not in flow direction ?????
What properties do hyperbolic processes usually have?
Some kind of direction and some kind of speed
Hyperbolic processes typically have the following properties:
Directional wave propagation: Information travels along specific paths called characteristics, which define directions in space-time.
Finite propagation speed: Disturbances or signals propagate at finite speeds, so effects do not appear instantaneously at a distance.
Possibility of discontinuities: Solutions can develop shocks or sharp fronts even from smooth initial data due to nonlinear effects.
Well-posedness of initial value problems: Given initial conditions, solutions evolve uniquely and continuously over time.
These properties are fundamental in systems describing waves and compressible flows (e.g., Euler equations).
How is the characteristic velocity defined?
How is a characteristic curve defined?
A characteristic curve is a path in space-time along which information or disturbances travel. For 1D flow, its slope is given by:
where uuu is flow velocity and ccc is speed of sound.
Why are characteristic quantities constant along characteristic curves?
d_phy/d_t = 0 for the characteristic curve
Characteristic quantities are constant along characteristic curves because:
Along these curves, the governing PDEs reduce to ordinary differential equations (ODEs).
The ODEs describe invariants that do not change as information propagates.
Physically, these represent wave properties or Riemann invariants conserved along the path of wave propagation.
Thus, characteristic quantities remain unchanged along their respective characteristic curves.
VL 5….
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