Candler 2018
Candler 2018
                                                                                                                                                                                                                                   379
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                                                                                        FL51CH15_Candler    ARI     12 September 2018    12:50
                                                                                                                        Another recent article reviews key fluid dynamics issues associated with the operation of scramjets
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                                        (Urzay 2018). An older review of planetary entry gas dynamics is also relevant (Gnoffo 1999).
                                                                                                                            Figure 1 illustrates several hypersonic flows: the 1960s-era X-15 Mach 6.7 rocket plane, a
                                                                                                                        generic lifting hypersonic vehicle, and the Mars Science Laboratory capsule flying at 6 km/s
                                                                                                                        in the Mars atmosphere. The latter two images are from computational fluid dynamics (CFD)
                                                                                                                        simulations of the flow field, and both visualize the temperature on the flow symmetry plane. The
                                                                                                                        hypersonic speeds result in high temperatures in the shock layer that envelops the vehicle and in
                                                                                                                        the boundary layer where there are extreme levels of shear.
                                                                                                                            The elevated temperatures in hypersonic flows give rise to many processes, such as vibra-
                                                                                                                        tional and electronic energy excitation, chemical reactions, ionization, and gas-surface interac-
                                                                                                                        tions. When these processes occur, the perfect gas shock relations are no longer valid and the
                                                                                                                        equations of state become nontrivial. For example, a Mach-6 normal shock wave produces con-
                                                                                                                        ditions such that the vibrational energy is excited to about 10% of the total internal energy. At
                                                                                                                        higher Mach numbers, additional processes become important, and therefore hypersonic flows are
a c
V∞
                                                                                              Figure 1
                                                                                              Visualizations of three hypersonic flows: (a) the NASA X-15, (b) a generic lifting hypersonic body, and (c) the Mars Science Laboratory
                                                                                              capsule at Mars entry conditions. Panel a courtesy of NASA.
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                                                                                                  usually characterized by imperfect gas effects. The rates of vibrational excitation and chemical re-
                                                                                                  actions depend on the local thermodynamic state, and these rates increase with increasing density
                                                                                                  and temperature. At typical hypersonic conditions, these rates are often similar to the advection
                                                                                                  rates.
                                                                                                      In this review, we discuss the effects of the internal energy relaxation and chemical reaction
                                                                                                  rate processes on hypersonic flows. We see that it is seldom possible to assume that the gas is in
                                                                                                  a state of local thermodynamic equilibrium; rather, the thermodynamic state changes as the gas
                                                                                                  responds to rapid compressions and expansions. Several examples are provided to illustrate what
                                                                                                  happens in a typical hypersonic flow and to motivate the development of the governing equations
                                                                                                  and the scaling properties of these flows. Specific examples of interactions between finite-rate gas-
                                                                                                  phase and gas-surface reactions are discussed. These include interaction of acoustic disturbances
                                                                                                  and vibrational energy relaxation, chemical freezing in high-enthalpy wind tunnel nozzles, and
                                                                                                  control flap effectiveness at hypersonic flight conditions.
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                                                                                                                                                                            Pressure, p (bar)
                                                                                                                                                                   9,500
T, Tve × 10 3 (K)
                                                                                                                                                                                                                                                            Mass fraction
                                                                                                                                                                   8,500                                                           8                                        10–2                    YN
                                                                                                     1.5
                                                                                                                                                                                                         0.6                                                                                        YO
                                                                                                                                                                   7,500
                                                                                               y/R                                                                                                                                 6                                        10–3                    YNO
                                                                                                                                                                   6,500                                                                                                                            YNO+
                                                                                                     1.0                                                           4,500                                 0.4
                                                                                                                                                                   5,500                                                           4                                        10–4
                                                                                                                                                                   3,500
                                                                                                     0.5                                                                                                 0.2
                                                                                                                                                                   2,500                                                           2                                        10–5
                                                                                                                                                                   1,500
                                                                                                      0                                                            500                                     0                       0                                        10–6   0
                                                                                                                                                                                                        0.08                       12                                        100
                                                                                                            60 km altitude
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                                                                                                     2.0                                                                                                                           10                                       10–1
                                                                                                                                                                                                        0.06
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Pressure, p (bar)
T, Tve × 10 3 (K)
                                                                                                                                                                                                                                                            Mass fraction
                                                                                                                                                                                                                                   8                                        10–2
                                                                                                     1.5
                                                                                                      0                                                                                                   0                        0                                        10–6
                                                                                                                                                                                                          4                        12                                        100
                                                                                                                                                                                                          3
                                                                                                                                                                                                                                        T, Tve × 10 3 (K)
                                                                                                                                                                                                                                                            Mass fraction
                                                                                                                                                                                                                                   8                                        10–2
                                                                                                     1.5
                                                                                               y/R                                                                                                        2                        6                                        10–3
                                                                                                     1.0
                                                                                                                                                                                                                                   4                                        10–4
                                                                                                                                                                                                          1
                                                                                                     0.5
                                                                                                                                                                                                                                   2                                        10–5
                                                                                                      0                                                                                                   0                        0                                        10–6
                                                                                                            0     0.5        1.0         1.5   2.0       2.5                                                   0       1    2                                                      0     1          2
                                                                                                                                   x/R                                                                  Distance on streamline, s/R                                         Distance on streamline, s/R
                                                                                              Figure 2
                                                                                              Temperature contours in the flow field of a sphere-cone at three altitudes and a speed of 5 km/s (left), along with flow properties
                                                                                              extracted on the streamline (center and right). The symbols at s/R = 2 in the mass fraction plots (right) denote the equilibrium state of
                                                                                              air at the local p, T. Variables: p, pressure; R, nose radius (10 cm); s, distance along the streamline; T, translational–rotational
                                                                                              temperature; Tve , vibrational–electronic temperature; Y , mass fraction.
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                                                                                                  1% level, and its ion, NO+ , at a much lower level. This is the most prevalent ionized species at
                                                                                                  the present conditions.
                                                                                                      In the high-pressure region immediately behind the shock, the gas is in local thermodynamic
                                                                                                  equilibrium. However, at s/R = 2, the gas state is far from equilibrium, with four orders of
                                                                                                  magnitude more N atoms present than predicted by equilibrium. This out-of-equilibrium, or
                                                                                                  nonequilibrium, state is a result of the rapid expansion of the gas around the body. The drop in
                                                                                                  pressure and temperature results in a sudden reduction in the chemical recombination rate, and the
                                                                                                  gas is approximately frozen near its postshock thermochemical state. Thus, there is a competition
                                                                                                  between the reaction and advection rates; this is one of the main features of hypersonic flows.
                                                                                                      Now let us compare the 40-km altitude flow field with the higher-altitude cases. At 60 km, the
                                                                                                  flow field is generally similar, but the elevated temperature region behind the shock wave is more
                                                                                                  pronounced, and the postshock temperature is higher, reaching about 11,400 K. The vibrational–
                                                                                                  electronic modes are close to equilibrium until the gas expands, then Tve lags the change in T.
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                                                                                                  Also note that at s/R = 2, there are three orders of magnitude more N atoms than predicted by
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                  local thermodynamic equilibrium. These differences are due to the lower pressure and density at
                                                                                                  this altitude, which results in reduced rates of internal energy relaxation and chemical reaction.
                                                                                                      At 80 km, the flow field is significantly different, with a more diffuse bow shock wave and
                                                                                                  a large region of elevated temperature. The shock standoff distance is also notably larger. The
                                                                                                  vibrational–electronic temperature lags the translational–rotational temperature at all locations
                                                                                                  on the extracted streamline. The level of dissociation is greatly reduced, and at s/R = 2, there
                                                                                                  are fewer N and O atoms than predicted by equilibrium. This is caused by the low-density free-
                                                                                                  stream conditions, which suppress the reaction rates, resulting in subequilibrium levels of reaction
                                                                                                  throughout the flow field. Thus, this case is significantly different than the previous two.
                                                                                                                                                            300                                                        12                                                            0.25
                                                                                                                                                                                Catalytic                                         T catalytic
                                                                                                                                                                                Noncatalytic                                      T noncatalytic
                                                                                                                                                            250                                                        10         Tve catalytic
                                                                                                                             Heat transfer rate (W/cm 2 )
                                                                                                                                                                                                                                                                                     0.20
                                                                                                                                                                                                                                  Tve noncatalytic
                                                                                                       40 k m a l titu d e
200 8
T, Tve × 10 3 (K)
                                                                                                                                                                                                                                                                     Mass fraction
                                                                                                                                                                                                                                                                                     0.15
                                                                                                                                                            150                                                        6
                                                                                                                                                                                                                                                                                     0.10
                                                                                                                                                            100                                                        4
                                                                                                                                                                                                                                                                                     0.05
                                                                                                                                                             50                                                        2
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                                                                                                                                                                                                                        0
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150 12 0.25
                                                                                                                                                            125                                                        10
                                                                                                                             Heat transfer rate (W/cm 2 )
                                                                                                                                                                                                                                                                                     0.20
                                                                                                       60 k m altitud e
                                                                                                                                                            100                                                        8
                                                                                                                                                                                                   T, Tve × 10 3 (K)
                                                                                                                                                                                                                                                                     Mass fraction
                                                                                                                                                                                                                                                                                     0.15
                                                                                                                                                             75                                                        6
                                                                                                                                                                                                                                                                                     0.10
                                                                                                                                                             50                                                        4
                                                                                                                                                                                                                                                                                     0.05
                                                                                                                                                             25                                                        2
                                                                                                                                                              0                                                         0                                                               0
                                                                                                                                                                  0       1          2         3                            0   0.02    0.04   0.06    0.08   0.10                           0   0.02    0.04   0.06    0.08   0.10
                                                                                                                                                             40                                                        12                                                            10 0
                                                                                                                                                                                                                       10                                                            10 –1
                                                                                                                             Heat transfer rate (W/cm 2 )
                                                                                                                                                                                                                                                                                                    O2 catalytic
                                                                                                                                                             30                                                                                                                                     O2 noncatalytic
                                                                                                       80 km altitud e
                                                                                                                                                                                                                       8                                                             10 –2          N catalytic
                                                                                                                                                                                                   T, Tve × 10 3 (K)
Mass fraction
                                                                                                                                                                                                                                                                                                    N noncatalytic
                                                                                                                                                                                                                                                                                                    O catalytic
                                                                                                                                                             20                                                        6                                                             10 –3          O noncatalytic
                                                                                                                                                                                                                       4                                                             10 –4
                                                                                                                                                             10
                                                                                                                                                                                                                       2                                                             10 –5
                                                                                                                                                              0                                                         0                                                            10 –6
                                                                                                                                                                  0       1          2         3                            0          0.1       0.2          0.3                            0          0.1       0.2          0.3
                                                                                                                                                             Distance along surface, ξ/R                                    Distance from surface, n/R                                       Distance from surface, n/R
                                                                                              Figure 3
                                                                                              Heat transfer rate to the sphere-cone surface (left), the temperature distribution along the stagnation streamline (center), and the species
                                                                                              mass fraction distribution along the stagnation streamline (right) for three altitudes: 40 km, 60 km, and 80 km. Two surface models are
                                                                                              used: catalytic, such that all atomic species impacting the surface recombine, and noncatalytic, in which the surface does not promote
                                                                                              recombination. Variables: ξ , distance along the surface from the stagnation point; n, the surface-normal distance at the stagnation point.
                                                                                                                                                            384       Candler
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104 1.0
a b
                                                                                                                                                                                                                                                                    8 km/s
                                                                                                                                                                                                                                                                              7
                                                                                                                                                                                                                                                                                  6
                                                                                                                                   103                                                                                                                                                5
                                                                                                                                                                                                                                                     0.6                                  4
                                                                                                                                                                                                                                                                             4 km/s
                                                                                                                                                                                                                                                     0.4                          5
                                                                                                                                   102
                                                                                                                                                                                                                                                                                  6
                                                                                                                                                                                                                                                                                  7
                                                                                                                                                                                                                                                     0.2                          8
                                                                                                                                                                                 Catalytic                                                                                                                  Catalytic
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                                                                                                                                                                                 Noncatalytic                                                                                                               Noncatalytic
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                                                                                                                                   101                                                                                                                0
                                                                                                                                         10 – 5     10 – 4    10 – 3    10 – 2      10 – 1       10 0                                                      10 – 5       10 – 4            10 – 3   10 – 2     10 – 1       10 0
                                                                                                                                                     Free-stream density (kg/m 3)                                                                                        Free-stream density (kg/m 3)
                                                                                                  Figure 4
                                                                                                  (a) Heat transfer rate to the stagnation point of a 10-cm sphere in air at 5 km/s as a function of free-stream density. (b) Stagnation-point
                                                                                                                                                                                                               √
                                                                                                  heat transfer rate normalized by the square root of the free-stream density and free-stream speed cubed, ρ∞ u3∞ , for five free-stream
                                                                                                  speeds (in meter–kilogram–second units).
                                                                                                      Figure 4a shows the variation of the stagnation-point heat transfer rate as a function of the
                                                                                                  free-stream density for the 0.1-m radius sphere at 5 km/s and a surface temperature of 1,000 K.
                                                                                                  The noncatalytic boundary condition has a large effect on the heat transfer rate at moderate
                                                                                                  densities, but it has a minimal effect at high and low densities. At low densities, there is little to
                                                                                                  no dissociation, as shown in the 80 km case discussed above. At high densities, the atomic species
                                                                                                  recombine in the low-temperature boundary layer, reducing the effect of surface catalysis.
                                                                                                      Figure 4b summarizes a series of CFD simulations comparing catalytic and noncatalytic bound-
                                                                                                  ary conditions at different free-stream conditions. The same sphere-cone is run at speeds ranging
                                                                                                  from 4 km/s to 8 km/s across a wide range of free-stream densities. The ratio of the assumed wall
                                                                                                  temperature to the free-stream total temperature is fixed at Tw /To = 0.079 for all cases. The figure
                                                                                                                                                            √
                                                                                                  plots the stagnation-point heat transfer rate scaled by ρ∞ u3∞ , which approximately collapses the
                                                                                                  data (see Tauber et al. 1987). Note that with this scaling, the catalytic surface stagnation-point
                                                                                                  heat flux is approximately independent of density, while the noncatalytic surface condition shows
                                                                                                  strong variations over a range of free-stream densities. The largest effect is for the highest speed
                                                                                                  condition, but even at 4 km/s there is a substantial reduction in the stagnation-point heat flux for
                                                                                                  densities of about ρ∞  3 × 10−4 kg/m3 . As in Figure 4a, the reduction in heat flux diminishes
                                                                                                  when the flow is close to chemically frozen (low ρ∞ ) and when the near-surface boundary layer is
                                                                                                  close to chemical equilibrium (high ρ∞ ).
                                                                                                      These computational results are consistent with the reacting boundary layer theory results of
                                                                                                  Fay & Riddell (1958), as reproduced in Figure 5. The heat transfer coefficient on a flat plate is
                                                                                                  plotted as a function of the gas-phase recombination rate and the catalytic activity of the surface.
                                                                                                  The heat flux is shown to be independent of the recombination rate for a catalytic surface and
                                                                                                  falls off significantly if the surface is noncatalytic and the recombination is slow. This effect was
                                                                                                  known at the time of the design of the Space Shuttle orbiter, but it was not possible to test the
                                                                                                  reaction-cured glass tiles at flight conditions, and therefore the conservative fully catalytic heat
                                                                                                  flux was used to design the thermal protection system. During the early reentries of the orbiter,
0.5
                                                                                                                                                          0
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                                                                                                                                                          10 – 6     10 – 5       10 – 4     10 – 3     10 – 2    10 – 1                10 0            10 1              10 2        10 3    10 4
                                                                                                                                                                                                 Recombination rate parameter
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                                                                                                                       Figure 5
                                                                                                                       Nondimensional stagnation-point heat transfer rate for a reacting boundary layer with finite recombination
                                                                                                                       rates and limiting values of surface catalytic activity. Adapted with permission from Fay & Riddell (1958).
                                                                                                                       experiments were performed to assess the catalytic surface effects. Several tiles were coated with
                                                                                                                       a highly catalytic material, and in-flight measurements showed a large heat flux increase on those
                                                                                                                       tiles due to catalytic effects (Stewart et al. 1983, Curry 1993), reflecting the effects shown in
                                                                                                                       Figures 4 and 5.
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                                                                                                  shock, which causes the shock standoff distance to decrease. This in turn changes the location of
                                                                                                  the sonic line and the resulting pressure distribution on the capsule forebody.
                                                                                                      Experiments, theory, and numerical simulations show that finite-rate processes (vibrational
                                                                                                  relaxation in particular) can affect laminar–turbulent transition in hypersonic boundary layers.
                                                                                                  For example, Adam & Hornung (1997) and Germain & Hornung (1997) correlated experimental
                                                                                                  data on a sharp cone as a function of free-stream total enthalpy for air, nitrogen, and carbon
                                                                                                  dioxide. They showed that reactive CO2 has a larger transition Reynolds number relative to air,
                                                                                                  and particularly in contrast to low-reactivity nitrogen. Subsequent theoretical analyses showed
                                                                                                  that the relaxation of the CO2 vibrational modes damps instability growth in these flows, resulting
                                                                                                  in transition delay. This interaction is discussed in more detail in Section 4.2.
                                                                                                      Many hypersonic flight vehicles require the use of ablative thermal protection systems, in
                                                                                                  which the surface material interacts with the external high-temperature flow and undergoes finite-
                                                                                                  rate gas-surface reactions. These processes include oxidation and nitridation reactions, catalytic
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                                                                                                  recombination, sublimation, and erosion. Ablation results in surface mass loss and the injection of
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                                                                                                  surface reaction products into the flow. The mass injection pushes the boundary layer away from
                                                                                                  the surface and shields the body from the high-temperature shock-layer gas. The ablation species
                                                                                                  undergo gas-phase reactions in the boundary layer and wake. Such a thermal protection system is
                                                                                                  not reusable because the ablation process consumes a portion of the surface material. An example
                                                                                                  of graphite ablation is given in Section 6.
                                                                                                      The operation of many high-enthalpy test facilities is affected by finite-rate processes. For
                                                                                                  example, shock tunnels are used to generate a short-duration flow to simulate hypersonic flight in
                                                                                                  the atmosphere. To do so, a shock wave is driven into a quiescent test gas; the shock wave reflects
                                                                                                  off of the shock tube end wall, producing a slug of high-temperature and -pressure gas. This gas
                                                                                                  then expands through a converging-diverging nozzle to hypersonic conditions. However, when
                                                                                                  the test gas is compressed, it undergoes chemical reactions, and it is this reacted gas that expands
                                                                                                  through the nozzle. Just as the stagnation region gas chemical state is frozen in the sphere-cone
                                                                                                  flow, the test gas state may freeze during the expansion through the nozzle, resulting in a partially
                                                                                                  reacted test gas. This gas is at low temperature, but with potentially large mass fractions of atoms
                                                                                                  and other reaction products. In some cases, particularly N2 flows, the vibrational energy can also
                                                                                                  be frozen near the nozzle throat temperature.
                                                                                                  2. GOVERNING EQUATIONS
                                                                                                  The governing equations and associated boundary conditions for hypersonic flows are discussed in
                                                                                                  this section. The examples described above show that these flows are not in local thermodynamic
                                                                                                  equilibrium and that there can be significant effects of rate processes on important flow features.
                                                                                                  Thus, it is necessary to track the evolution of the thermochemical state of the gas with appropriate
                                                                                                  conservation equations. The overall form of the governing equations is described; more details
                                                                                                  may be found in Gnoffo et al. (1989) and Lee (1985), for example.
                                                                                                                                      ∂ρs    ∂
                                                                                                                                          +     (ρs u j + ρs vs j ) = ωs ,                                         1.
                                                                                                                                      ∂t    ∂xj
                                                                                                  where ρs is the species-s density, u j is the mass-averaged velocity in the x j direction, vs j is the
                                                                                                  species-s mass diffusion velocity, and ωs is the species-s chemical source term.
                                                                                                                       where e int is the mass-averaged internal energy (in the previous examples, e int is the sum of the
                                                                                                                       vibrational and electronic energies), and q int, j is the j -direction energy flux due to gradients of
                                                                                                                       internal energy. The source term, Q int , represents the rate of internal energy relaxation due to
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                                                                                                                       collisional processes in the gas mixture. The internal energy, e int can be written as
                                                                                                                                                                          
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                                                                                                                                                               ρe int =       ρs e int,s ,                                 4.
                                                                                                                                                                               s
                                                                                                                       where e int,s is the species-s internal energy. The specific form of e int,s used to represent a particular
                                                                                                                       flow depends on the flow conditions, gas properties, and quantities of interest being simulated. In
                                                                                                                       some cases, multiple internal energy equations must be solved. For example, it may be necessary
                                                                                                                       to track several vibrational energies or to solve a separate electronic energy equation.
                                                                                                                           Finally, the total energy conservation equation is given by
                                                                                                                                                ∂E       ∂                                           
                                                                                                                                                     +       (E + p)u j − σij ui +    ρs h s vs j + q j = 0,                    5.
                                                                                                                                                 ∂t     ∂xj                        s
                                                                                                                       Here, e s is the species-s total specific energy, including all energy modes (translational, rotational,
                                                                                                                       vibrational, electronic, and chemical):
                                                                                                                                                                e s = e tr,s + e int,s + h ◦s ,                                7.
                                                                                                                       where e tr,s is the translational–rotational energy and h ◦s is the heat of formation. In the above
                                                                                                                       conservation equation, h s is the species-s specific enthalpy, h s = e s + p s /ρs . The pressure is the
                                                                                                                       sum of the partial pressures of the gas mixture.
                                                                                                                          Unless all scales are resolved, which is currently prohibitive at vehicle scales, these equa-
                                                                                                                       tions must be augmented for turbulent flows, either by adding transport equations for Reynolds-
                                                                                                                       averaged Navier–Stokes turbulence model variables or by including large-eddy simulation subgrid-
                                                                                                                       scale models. The present state of turbulence modeling for hypersonic flows is deficient, and
                                                                                                                       turbulence models developed for low-speed flows are typically used.
                                                                                                                       2.2. Thermodynamics
                                                                                                                       It is critical to correctly represent the thermodynamics of high-temperature hypersonic flows.
                                                                                                                       For moderate–Mach number flows, there is little to no electronic excitation, and the vibrational
                                                                                                                       energy modes can be adequately represented with a simple harmonic oscillator. Above about
                                                                                                                       Mach 15 in air, it is important to include electronic energy excitation. This can be done with
                                                                                                                       algebraic expressions for the electronic energy states of each species, utilizing data for energy
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                                                                                                  levels and degeneracies. However, this can be cumbersome and it is usually preferable to use
                                                                                                  curve fits for thermodynamic quantities such as those of McBride et al. (2002) and Scoggins &
                                                                                                  Magin (2014). With a two-temperature model for the translational–rotational and vibrational–
                                                                                                  electronic energies, care must be taken to correctly evaluate the different energies at the appropriate
                                                                                                  temperatures.
s s
                                                                                                  Ms is the species-s molecular weight, and kf,s and kb,s are the forward (dissociation) and backward
                                                                                                  (recombination) reaction rates, respectively. Usually, the dissociation rate is computed from a
                                                                                                  temperature-dependent Arrhenius reaction rate, and the recombination rate is set so that the
                                                                                                  source term is zero in thermodynamic equilibrium.
                                                                                                      The internal energy relaxation term, Q int , is complicated for ionizing gases and is not discussed
                                                                                                  in full here; readers are referred to Gnoffo et al. (1989) and Lee (1985) for more details. Rather, we
                                                                                                  focus on the term that is responsible for vibrational energy relaxation through collisional processes.
                                                                                                  The standard approach is to use a Landau–Teller model,
                                                                                                                                         ρs e v,s
                                                                                                                                               ∗
                                                                                                                                                   (T) − ρs e v,s       
                                                                                                                                 Qv =                               +       ωs ẽ v,s ,                            10.
                                                                                                                                         s
                                                                                                                                                     τv,s               s
                                                                                                  where τv,s is the species-s translational–vibrational relaxation time that is appropriately averaged
                                                                                                  to account for different relaxation times for each collision pair. Here, ẽ v,s is the average vibrational
                                                                                                  energy removed or added to the vibrational energy pool due to dissociation and recombination
                                                                                                  reactions, respectively. As discussed below, vibrationally excited molecules dissociate more readily,
                                                                                                  and therefore this value should be larger than the average vibrational energy.
                                                                                                                       the 1960s and 1970s. Standard approaches use Millikan & White’s (1963) correlation for the
                                                                                                                       vibrational relaxation times, with some corrections for particular relaxation pairs (Park 1993). A
                                                                                                                       standard set of air reaction rates was tabulated by Park (1993) and, for gas-phase reactions of
                                                                                                                       ablation products, by Martin et al. (2015).
                                                                                                                          As is discussed in more detail in Section 5, computational chemistry is now providing accurate
                                                                                                                       potential energy surfaces (PESs) that can be used to simulate the reaction dynamics of air species.
                                                                                                                       These are being used to compute more accurate vibrational relaxation times and reaction rates,
                                                                                                                       which are starting to become available in the literature.
                                                                                                                       provide two examples and refer to appropriate references for more complex boundary conditions.
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                                       2.6.1. Catalytic surface boundary condition. The basic statement of mass balance for species
                                                                                                                       s at a reactive surface is given by (MacLean et al. 2011, Marschall & MacLean 2011, Marschall
                                                                                                                       et al. 2015):
                                                                                                                                                                    ∂ ys
                                                                                                                                                         − (ρ Ds )w      + (ρu)w ys w = ωs .                              11.
                                                                                                                                                                    ∂n w
                                                                                                                       We have assumed Fickian diffusion; Ds is the mass diffusivity, ys is the species-s mass fraction, and
                                                                                                                       u is the rate of motion of the surface due to reactive mass loss by the gas-surface reactions with
                                                                                                                       rate ωs . The w subscript indicates the wall condition. These reactions produce a flux of reacted
                                                                                                                       species to or from the surface, rather than a volumetric rate of mass production, as in the gas-phase
                                                                                                                       reactions.
                                                                                                                           Let us consider the example of a catalytic surface discussed above. The catalytic efficiency, α,
                                                                                                                       is the fraction of atoms impinging on a surface that undergo reaction (recombine to molecules)
                                                                                                                       on the surface. The surface mediates the recombination process by one of several possible surface
                                                                                                                       reaction processes. From kinetic theory, the one-way flux of species-s particles across a surface is
                                                                                                                                                                         1
                                                                                                                                                                   Js = ρs C̄s ,                                         12.
                                                                                                                                                                         4
                                                                                                                       where C̄s is the thermal speed of the species-s particles. Of those particles that impact the surface,
                                                                                                                       a fraction α of them recombine and 1−α bounce off and do not react. Thus, the rate of production
                                                                                                                       of species-s mass is ωs = 14 αρs C̄s evaluated at the wall state. Within the continuum description,
                                                                                                                       the flux of reacted particles must be equal to the diffusive flux of reactive gas to the surface. This
                                                                                                                       is represented by the above mass balance expression, and therefore we have a boundary condition
                                                                                                                       of the form
                                                                                                                                                                       ∂ ys   1
                                                                                                                                                            − (ρ Ds )w      = αρs ,w C̄s ,w ,                             13.
                                                                                                                                                                       ∂n w   4
                                                                                                                       since uw = 0 (no mass change of the surface) for this catalytic surface reaction. With the assumption
                                                                                                                       that the normal pressure gradient is zero in the boundary layer, we can then solve for the surface
                                                                                                                       or wall state.
                                                                                                                           Implicit in this formulation is a rate of reaction on the surface. A noncatalytic surface with
                                                                                                                       α = 0 has surface reactions that are negligibly slow relative to the diffusion timescales. Likewise,
                                                                                                                       a large catalytic efficiency (α → 1) represents a rapid surface reaction, and the rate of catalytic
                                                                                                                       recombination is limited by the rate of diffusion to the surface. In more complex gas-surface
                                                                                                                       interaction models, there can be competing surface reactions and reactions that depend on surface
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                                                                                                  coverage (the fraction of surface material bond sites occupied by gas-phase species). Then the
                                                                                                  gas-surface reaction rates are explicitly temperature- and pressure-dependent, and the law of mass
                                                                                                  action is used to develop the rate of chemical species formation on the surface (Marschall et al.
                                                                                                  2015).
                                                                                                  2.6.2. Velocity and temperature slip boundary conditions. The extended form of the Navier–
                                                                                                  Stokes equations provided above can be derived using a Chapman–Enskog solution of the Boltz-
                                                                                                  mann equation. Conceptually, a first-order perturbation to a Maxwellian velocity distribution is
                                                                                                  substituted into the Boltzmann equation and appropriate moments are taken. This results in the
                                                                                                  Navier–Stokes equations with assumptions for linear relationships between stress and strain and
                                                                                                  between temperature gradients and heat flux. The surface boundary conditions that are consistent
                                                                                                  with this kinetic theory–based derivation are the so-called slip boundary conditions. It is only in
                                                                                                  the limit of small mean free path that the conventional no-slip boundary conditions are recovered.
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                                                                                                      The dependence of the surface state on the mean free path is easy to visualize. For example,
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                  consider a rarefied gas with a mean free path, λ. The particles than impinge on the surface originate
                                                                                                  about a distance λ from the surface, interact with and accommodate to the surface state, and then
                                                                                                  collide again about λ from the surface. The influence of the surface is then transmitted to the rest
                                                                                                  of the flow field through subsequent collisions. This region of adjustment to the surface state thus
                                                                                                  scales with λ.
                                                                                                      Maxwell (1879) derived an expression for the velocity slip in the surface-tangent direction as
                                                                                                  (see also Gupta et al. 1985),
                                                                                                                                                   2 − σ ∂u
                                                                                                                                         uslip =        λ          ,                                         14.
                                                                                                                                                     σ    ∂n   w
                                                                                                  where σ is the accommodation coefficient (the fraction of particles that are diffusely reflected),
                                                                                                  and n is a surface-normal coordinate. Note that the usual no-slip boundary condition is obtained
                                                                                                  as λ → 0.
                                                                                                     A similar temperature jump or slip boundary condition for a perfect gas was derived by Kennard
                                                                                                  (1938) as
                                                                                                                                               2 − αT 2γ    1 ∂T
                                                                                                                                Tslip − Tw =                  λ              ,                                15.
                                                                                                                                                 αT (γ + 1) Pr ∂n        w
                                                                                                                       where the bar variables are nondimensional quantities. Note that the relevant scaling parameters
                                                                                                                       are:
                                                                                                                                                                                     ρ∞ L
                                                                                                                                                       forward (dissociation) rate :       ,                        17.
                                                                                                                                                                                      u∞
                                                                                                                                                                                     ρ∞2
                                                                                                                                                                                         L
                                                                                                                                                   backward (recombination) rate :         .                        18.
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                                                                                                                                                                                      u∞
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                                                                                                                       The dissociation source term scales with the density, while recombination scales with the density
                                                                                                                       squared. Therefore, the relative importance of dissociation and recombination can change as
                                                                                                                       the free-stream density changes. It should also be noted that the flow-field temperature scales
                                                                                                                       with u2∞ , so that the temperature-dependent rates, kf and kb , scale with the free-stream velocity
                                                                                                                       magnitude squared.
                                                                                                                           Dissociation is a two-body binary collision process, so the ρ∞ L scaling is termed binary scal-
                                                                                                                       ing (Hornung 1972b). Other two-body processes such as exchange reactions (e.g., N2 + O 
                                                                                                                       NO + N) also have binary scaling. Similarly, the vibrational relaxation process is a two-body pro-
                                                                                                                       cess and is characterized by binary scaling (τv in Equation 10 scales inversely with density). Recom-
                                                                                                                       bination is a three-body or ternary process, accounting for its dependence on the density squared.
                                                                                                                           The flows discussed above clearly exhibit these scaling properties. The rate of dissociation
                                                                                                                       and vibrational relaxation behind the bow shock decreases with decreasing free-stream density, as
                                                                                                                       expected. However, the recombination process exhibits a stronger dependence on density. When
                                                                                                                       the gas suddenly expands around the nose and onto the cone, the density decreases and the rate of
                                                                                                                       recombination decreases quadratically with the density. This is why there is little recombination
                                                                                                                       during the flow expansion and why the chemical freezing is stronger at 60 km than at 40 km. In
                                                                                                                       contrast, because vibrational relaxation is a binary collisional process, it more closely follows the
                                                                                                                       changes in the translational temperature.
                                                                                                                           A more subtle scaling effect occurs in the near-surface boundary layer. At 40 km, the density
                                                                                                                       is high enough that significant recombination occurs in the thermal boundary layer. However, at
                                                                                                                       60 km, the density is lower and recombination is reduced due its quadratic dependence on density.
                                                                                                                       This causes the dependence of the noncatalytic heat transfer rate on density shown in Figure 4.
                                                                                                                           The scaling of the gas-surface reactions is not as clear as the gas-phase reactions. For example,
                                                                                                                       consider the catalytic recombination of oxygen according to O + O(s) → O2 ; here, O(s) is an
                                                                                                                       oxygen atom that is bonded to an open surface site. The rate of this process is not simple since it is
                                                                                                                       proportional to both the gas-phase O atom concentration and the number of O atoms bonded to
                                                                                                                       the surface. Typically, the surface coverage depends on the surface temperature and gas pressure.
                                                                                                                           These rates can be nondimensionalized by a characteristic advection rate, resulting in
                                                                                                                       Damköhler numbers for each process. In the limit of large Damköhler number, a process will
                                                                                                                       be close to equilibrium, while small values indicate that it is frozen.
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                                                                                                  modes are relatively slow to adjust. When this occurs, the fundamental assumptions of the kinetic
                                                                                                  theory derivation of the Navier–Stokes equations are violated.
                                                                                                      An obvious example of translational nonequilibrium occurs within a strong shock wave. The
                                                                                                  preshock velocity distribution function has a small thermal component and a large component
                                                                                                  in the free-stream direction. Postshock, the opposite is true, with much of the upstream directed
                                                                                                  motion converted to thermal motion. Within the shock wave itself, the velocity distribution
                                                                                                  function is much more complicated, with features of the pre- and postshock distribution functions.
                                                                                                  Such a bimodal velocity distribution function cannot be represented as a perturbed Maxwellian
                                                                                                  distribution, as assumed by the Chapman–Enskog derivation of the Navier–Stokes equations.
                                                                                                  Thus, the Navier–Stokes equations cannot correctly represent the flow within a shock wave.
                                                                                                  Likewise, higher-order Chapman–Enskog solutions of the Boltzmann equation (e.g., the Burnett
                                                                                                  equations) cannot represent this effect.
                                                                                                      When translational energy relaxation is important, a kinetic theory–based approach such as the
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                                                                                                  direct simulation Monte Carlo method must be used (Bird 1994, Boyd & Schwartzentruber 2017).
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                  Typically, this occurs under rarefied conditions, which can be identified using a gradient-length
                                                                                                  local Knudsen number (Boyd et al. 1995):
                                                                                                                                                        λ
                                                                                                                                              KnGLL =     ∇ρ.                                                19.
                                                                                                                                                        ρ
                                                                                                  If this quantity exceeds a value of about 0.05, the Navier–Stokes equations are likely to be invalid.
                                                                                                      Typically, rotational energy relaxation does not need to be considered separately since it is
                                                                                                  only important for flows where the Navier–Stokes equations are already suspect or invalid. This
                                                                                                  is because the rotational modes relax very rapidly (in about five to ten collisions), and that rate is
                                                                                                  similar to the rate at which the translational modes relax to equilibrium. This is not the case for
                                                                                                  the vibrational modes.
                                                                                                  4. VIBRATIONAL PROCESSES
                                                                                                  The relatively slow relaxation of the vibrational modes of a gas can interact with the gas dynamics
                                                                                                  in several ways. Most obviously, the vibrational modes absorb energy and change the postshock
                                                                                                  conditions when they are active. The vibrational state of the gas also has a strong effect on its
                                                                                                  dissociation rate, as discussed in the next section. Vibrational freezing and thermal nonequilibrium
                                                                                                  can be important in rapidly expanding flows such as in the wake of a planetary entry capsule or
                                                                                                  in a hypersonic wind tunnel nozzle, as shown above. In some flows, the vibrational relaxation rate
                                                                                                  may be tuned to match acoustic disturbances, which can lead to the dissipation and dispersion
                                                                                                  of sound in high-temperature gases. Acoustic damping by this mechanism can counter boundary
                                                                                                  layer instabilities and delay transition to turbulence if tuned to the dominant instabilities. In this
                                                                                                  section, we summarize the interaction of vibrational relaxation with acoustic processes.
                                                                                                                         0.14                                                                                                           10 – 2
                                                                                                                                    a                                                                                                             b
                                                                                                                                                                                          T/θ v
                                                                                                                         0.12                                                                                                           10 – 3
                                                                                                                                                                                             0.1
                                                                                                                                                                                             0.2
                                                                                                                                                                                             0.5                                                 16,000 K   4,600 K                         750K
                                                                                                                         0.10                                                                                                           10 – 4
                                                                                                                                                                                             1                                                                          2,000 K    1,000K
                                                                                                                                                                                             2
                                                                                                                         0.08                                                                5                                          10 – 5
                                                                                                                                                                                                                                                                      N2 –N2 vibrational
                                                                                                                                                                                                                                                                      N2 –N2 rotational
                                                                                                                         0.06                                                                                                           10 – 6
                                                                                                                                                                                                                                                                      CO2 –N2 vibrational
0.04 10 – 7
                                                                                                                         0.02                                                                                                           10 – 8
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                                                                                                                           0                                                                                                            10 – 9
                                                                                                                           10 – 3         10 – 2      10 – 1      10 0           10 1   10 2       10 3                                            0.04      0.06         0.08       0.10          0.12
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                              Figure 6
                                                                                              (a) Vibrational damping rate as a function of the product of the angular frequency and relaxation time, ωτv , from the results of Meador
                                                                                              et al. (1996), and (b) typical vibrational and rotational relaxation times. θv is the molecular characteristic temperature of vibration.
                                                                                                                                                   the speed of sound and its attenuation. However, Meador et al. (1996) showed that μB is zero and
                                                                                                                                                   that its interpretation as an internal energy relaxation parameter is incorrect. Rather, absorption
                                                                                                                                                   and dispersion of sound are the result of internal energy relaxation, but these effects are not
                                                                                                                                                   embodied in μB . Instead, the internal energy should be represented with a conservation equation,
                                                                                                                                                   as discussed in Section 2.1. Meador also derived closed-form expressions for the speed of sound
                                                                                                                                                   and its dissipation rate and dispersion as functions of the internal energy relaxation time.
                                                                                                                                                       Figure 6a shows the damping rate of acoustic waves as a function of the acoustic angular
                                                                                                                                                   frequency times the relaxation time, ωτv , and the damping of the acoustic wave per wavelength
                                                                                                                                                   (Meador et al. 1996). Clearly, ωτv  1 produces significant damping, provided that the temperature
                                                                                                                                                   is large enough so that the vibrational modes are excited. Here, θv is the characteristic temperature
                                                                                                                                                   of vibration, which is 3,395 K for N2 and 2,239 K for O2 . Figure 6b shows that the relaxation
                                                                                                                                                   times for vibrational and rotational processes vary widely. Therefore, to obtain effective damping,
                                                                                                                                                   the relaxation process must be resonant with the acoustic frequency of interest. The next section
                                                                                                                                                   discusses how this effect may be used to damp instabilities in a hypersonic boundary layer.
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                                                                                                                     101                                                                                           100
                                                                                                                                 a                                                                                 90        b         Exothermic disturbances
                                                                                                                                                                                                                                       Endothermic disturbances
                                                                                                                                                                                                                   80                  Nonreacting disturbances
                                                                                                                                                                                                                                                                         x=
                                                                                                                                                                                                                    70                   Increasing
                                                                                                                                                                                                                                         Incre
                                                                                                                                                                                                                                             e      x                 0.106 m
                                                                                                                                                                                                                   60
                                                                                                   Re*tr (10 – 6 )
x=
                                                                                                                                                                                                      –α i (1/m)
                                                                                                                                                                                                                   50                     x=     0.316 m
                                                                                                                     10 0                                                                                                              0.943 m
                                                                                                                                                                                                                   40
                                                                                                                                                                                                                   30
                                                                                                                                                                    N2        Cold tunnels                         20
                                                                                                                                                                    CO2       Air cold                              10
                                                                                                                                                                    Air       CO2 cold                                                                                          Unstable
                                                                                                                                                                              N2 cold                               0
                                                                                                                     10 –1                                                                                         -10
                                                                                                                             0         2        4       6       8        10   12       14      16                        0       500       1,000        1,500   2,000       2,500     3,000
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                                                                                                  Figure 7
                                                                                                  (a) The transition Reynolds number based on reference conditions, Re∗tr , on a 5◦ cone as a function of free-stream total enthalpy, h o , for
                                                                                                  three gases. (b) The acoustic disturbance growth rate, −αi , at various axial locations on a sharp cone in CO2 for disturbances with exother-
                                                                                                  mic reactions, endothermic reactions, and no reactions. Panels adapted with permission from (a) Adam (1997) and (b) Johnson (2000).
                                                                                                  growth rate, while endothermic processes decrease it. This demonstrates that there is an interac-
                                                                                                  tion between rate processes and the growth of second-mode disturbances in a hypersonic boundary
                                                                                                  layer. Figure 7b summarizes the linear stability theory results. The exothermic reactions are sig-
                                                                                                  nificantly more unstable, while the endothermic reactions are damped relative to the nonreacting
                                                                                                  flow.
                                                                                                       Fujii & Hornung (2001) showed that at the experimental conditions, there is an overlap between
                                                                                                  the most unstable acoustic frequencies and the vibrational relaxation rate of CO2 . Their work
                                                                                                  shows that if boundary layer instabilities are tuned to CO2 relaxation, their amplitude may be
                                                                                                  damped. Based on this work, Leyva et al. (2009) and Jewell et al. (2013) studied the injection of
                                                                                                  CO2 into the boundary layer of a hypersonic cone in an attempt to delay transition to turbulence.
                                                                                                  With careful injection, it was shown that it is possible to stabilize the boundary layer.
                                                                                                       Wagnild & Candler (2014) used direct numerical simulations to study the tuning of acoustic
                                                                                                  disturbances to hypersonic boundary layers. The results of this work are consistent with the
                                                                                                  theoretical results and illustrate the effects of vibrational relaxation tuning on acoustic disturbances.
                                                                                                  There have been many other studies of hypersonic boundary layers including rate effects; however,
                                                                                                  there are very few that focus on vibrational rate processes and their interaction with the acoustic
                                                                                                  modes (e.g., Hudson et al. 1997, Knisely & Zhong 2018). Many other authors have studied the
                                                                                                  effects of equilibrium gas models and chemical nonequilibrium processes. However, chemical rate
                                                                                                  processes are much slower than the relevant disturbances in hypersonic boundary layers and are
                                                                                                  not tuned to relevant disturbance frequencies.
                                                                                                       This work shows that there are three regimes for vibrational damping of acoustic waves:
                                                                                                  (a) equilibrium, in which the vibrational state rapidly adjusts to the acoustic disturbance (this
                                                                                                  occurs at low frequencies); (b) nonequilibrium, when the vibrational mode responds to the passage
                                                                                                  of the acoustic disturbance with a phase lag, which absorbs energy from the acoustic mode; and
                                                                                                  (c) frozen, in which the acoustic timescale is much smaller than the vibrational relaxation timescale
                                                                                                  and does not respond to the passage of the wave, so that there is negligible acoustic damping.
                                                                                                       Figure 8 illustrates these regimes for a 100-kHz acoustic wave passing through CO2 at a range
                                                                                                  of initial temperatures. At low temperature (300 K), the acoustic modes are only weakly excited,
                                                                                                  and the relaxation time is much slower than the characteristic time of the acoustic wave. Thus,
                                                                                                                                                                                                             1.5
                                                                                                                          0.5                                                                                1.0
                                                                                                   Disturbance
                                                                                                                                                                                                             0.5
                                                                                                                            0                                                                                  0
                                                                                                                                                                                                            – 0.5
                                                                                                                         – 0.5                                                                    T‘        – 1.0
                                                                                                                                                                                                  T ‘ve     – 1.5
                                                                                                                         – 1.0
                                                                                                                                                                                                            – 2.0
                                                                                                                                 2           3           4    5         2        3           4     5                 2       3           4     5
                                                                                                                                             x × 10 –2 (m)                       x × 10 –2 (m)                               x × 10 –2 (m)
                                                                                              Figure 8
                                                                                              Damping of a 100-kHz acoustic disturbance in CO2 as a function of temperature: (a) 300 K, (b) 1,000 K, and (c) 2,500 K. Adapted from
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                                                                                                                                              the vibrational modes do not respond and are frozen. This is the case in room-temperature air,
                                                                                                                                              for example. At 1,000 K, the bending modes of CO2 are excited (θv = 960 K) and their relaxation
                                                                                                                                              times are close to the optimal frequency for acoustic damping. In this case, the vibrational energy is
                                                                                                                                              excited and its response is out of phase with the translational–rotational temperature; this results in
                                                                                                                                              strong acoustic damping. At higher temperatures, the vibrational energy approaches equilibrium
                                                                                                                                              and rapidly responds to the temperature perturbations caused by the acoustic wave.
                                                                                                                                              5. CHEMICAL REACTIONS
                                                                                                                                              As illustrated in the introduction, dissociation is an important process in hypersonic flows. Disso-
                                                                                                                                              ciation is complicated because its rate depends on the level of vibrational excitation; vibrationally
                                                                                                                                              excited molecules have a lower energy barrier to dissociation and more readily dissociate. Fur-
                                                                                                                                              thermore, when vibrationally excited molecules dissociate, they are removed from the vibrational
                                                                                                                                              energy pool, suppressing the overall vibrational energy of the gas mixture. The coupling between
                                                                                                                                              vibration and dissociation has been known since the 1960s, and models were postulated to repre-
                                                                                                                                              sent the process (e.g., Marrone & Treanor 1963). These models make the effective dissociation
                                                                                                                                              rate a function of T and Tv .
                                                                                                                                                  In the late 1980s, Park (1986, 1987) recognized that a new approach was needed. The dissoci-
                                                                                                                                              ation rates used in flow field modeling were obtained from shock tube experiments, and models
                                                                                                                                              were required to infer the reaction rates from the raw data. Park reinterpreted the shock tube
                                                                                                                                              data to calibrate a model in a form that would be consistent with the data. This was an important
                                                                                                                                              advance over previous models that took the reaction rates as given and then developed models for
                                                                                                                                              dissociation. Such an approach is inconsistent because the      inferred reaction rates depend on the
                                                                                                                                              model used to infer them. Park’s analysis resulted in the TT v model,     in which reaction rates in
                                                                                                                                              Arrhenius form are evaluated at an effective temperature equal to TT v . The model suppresses
                                                                                                                                              the dissociation rate when Tv is low, consistent with the understanding of the dissociation process
                                                                                                                                              (e.g., Hornung 1972a). A component of this model is the average energy removed from the total
                                                                                                                                              vibrational energy due to dissociation (ẽ v,s in Equation 10). Park assumed ẽ v,s = 0.3De , where De
                                                                                                                                              is the dissociation energy of the molecule. This value is incorrect and causes numerical problems,
                                                                                                                                              and in practice, ẽ v,s is typically approximated as the average vibrational energy. The Park model is
                                                                                                                                              now widely used, not because it has proven to be accurate, but because it is more straightforward to
                                                                                                                                              implement than many other models. Subsequently, other models have been proposed (e.g., Knab
                                                                                                                                              et al. 1995, Luo et al. 2018, Singh & Schwartzentruber 2018).
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                                                                                                      Recently, it has become possible to better understand the dissociation process through the use
                                                                                                  of ab initio computational chemistry methods. Electronic-structure calculations are carried out
                                                                                                  for many possible atomic configurations to build a PES for molecular interactions (e.g., Paukku
                                                                                                  et al. 2013). Collisions between air species are simulated using the relevant PES to obtain statistical
                                                                                                  data for relaxation and reaction rates at specified conditions (e.g., Bender et al. 2015, Valentini
                                                                                                  et al. 2016). Such an analysis reveals the complete physics of dissociation    and its dependence on
                                                                                                                                                                      
                                                                                                  the vibrational energy state. Soon this work will supplant Park’s TT v model with physics-based
                                                                                                  models of known fidelity. There are many recent papers related to this subject, including those
                                                                                                  of Kim & Boyd (2013), Panesi et al. (2014), Andrienko & Boyd (2016), Schwartzentruber et al.
                                                                                                  (2017), and Macdonald et al. (2018).
                                                                                                  6. SURFACE PROCESSES
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                                                                                                  As discussed in the introduction, gas-surface rate processes can have a profound effect on
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                  heat transfer rates to hypersonic vehicles. Ablation is significantly more complicated than
                                                                                                  surface-catalyzed recombination. The simplest ablative surface is carbon in one form or another,
                                                                                                  such as graphite or a carbon–carbon matrix. The basic reactions that can take place are oxidation
                                                                                                  and nitridation, surface-catalyzed recombination, and at high temperatures, sublimation. A
                                                                                                  representative gas-surface kinetics model is (Zhluktov & Abe 1999):
                                                                                                                        O + (s) ↔ O(s),               O(s) + C(b) ↔ CO + (s),
                                                                                                                        N + (s) ↔ N(s),          O + O(s) + C(b) ↔ CO2 + (s),
                                                                                                                          2O(s) ↔ O2 + 2(s),           O(s) + C(b) ↔ CO2 + 2(s),
                                                                                                                       O2 + (s) ↔ O + O(s),                 C + (s) ↔ (s) + C(b),
                                                                                                                       N2 + (s) ↔ N + N(s),              C2 + 2(s) ↔ 2(s) + 2C(b),
                                                                                                                     CO2 + (s) ↔ CO + O(s),              C3 + 3(s) ↔ 3(s) + 3C(b).
                                                                                                  Here, (s) indicates an open bond site, O(s) denotes an O atom occupying a bond site, and C(b) indi-
                                                                                                  cates a bulk or solid carbon atom. Rates for each of these processes are required to close the model.
                                                                                                      Until recently, such a finite-rate model was not used for analysis, and a gas-surface equilibrium
                                                                                                  approximation was made. In this case, the equilibrium composition of a mixture of air and the
                                                                                                  surface material is computed at the surface pressure and temperature; this provides the surface
                                                                                                  state for the gas-phase boundary condition. This approach is commonly termed a B method (the
                                                                                                  nondimensional mass blowing rate) and is valid at high pressures where equilibrium is approached,
                                                                                                  but is unlikely to be valid at low to moderate pressures.
                                                                                                      Figure 9 shows CFD simulations of ablation using three models: the equilibrium B ap-
                                                                                                  proach, Zhluktov & Abe’s (1999) finite-rate model, and a recently developed finite-rate model
                                                                                                  (Poovathingal et al. 2017). The main difference between the finite-rate models is that the more
                                                                                                  recent model favors the formation of CO relative to CO2 ; this is consistent with oxygen molec-
                                                                                                  ular beam experiments (Murray et al. 2015). Here, the properties of graphite are used, and the
                                                                                                  gas-surface mass and energy balances are solved at the interface between the gas and the solid.
                                                                                                  The thermal response of the material is included, and the body changes shape due to ablative
                                                                                                  mass loss. Clearly, there are large differences between the models, with the equilibrium B model
                                                                                                  producing much larger recession relative to the finite-rate models. The Zhluktov & Abe (1999)
                                                                                                  model produces the lowest level of recession. Experiments (Alba et al. 2016) indicate that this
                                                                                                  model is deficient, and the third model is more consistent with data. In any case, it is clear that
                                                                                                  the finite-rate models produce significantly reduced levels of surface recession at these conditions.
                                                                                                  Furthermore, the boundary layer composition predicted by the models is completely different,
                                                                                                                             B' model                            Zhluktov & Abe model               Poovathingal et al. model           T (K)
                                                                                                                                                                                                                                           2,500
                                                                                                       6       a                                             b                                      c
                                                                                                                                                                                                                                          2,300
                                                                                              y (cm)
4 2,100
                                                                                                                                                                                                                                          1,900
                                                                                                       2
                                                                                                                                                                                                                                          1,700
                                                                                                       0                                                                                                                                  1,500
                                                                                                           0       2         4         6        8     10 0        2     4        6    8      10 0       2     4        6     8     10
                                                                                                                                 x (cm)                                     x (cm)                                x (cm)
                                                                                              Figure 9
                                                                                              Predicted recession and solid temperature for a graphite sphere-cone (6.35 cm in radius) at conditions corresponding to an altitude of
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                                                                                              30 km and a flight speed of 3.5 km/s after 830 s of exposure: (a) B model, (b) Zhluktov & Abe (1999) model, and (c) Poovathingal et al.
                                                                                              (2017) model. The gray region indicates the initial preablated geometry.
    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                                                      and as shown in Section 4.2, the boundary layer internal energy dynamics can lead to important
                                                                                                                                      effects. Additional experimental data are required to fully validate the models.
                                                                                                                                           SUMMARY POINTS
                                                                                                                                           1. Hypersonic flows involve interactions of gases and thermal protection system materials
                                                                                                                                              at extreme conditions.
                                                                                                                                           2. In hypersonic flows, internal energy relaxation, gas-phase reactions, and gas-surface in-
                                                                                                                                              teractions typically occur at rates that are similar to the gas motion rates, resulting in an
                                                                                                                                              out-of-equilibrium thermochemical state.
                                                                                                                                           3. These rate processes affect aerodynamic performance, heat transfer rates, instability
                                                                                                                                              growth leading to boundary layer transition, catalytic gas-surface interactions, and
                                                                                                                                              ablation.
                                                                                                                                           4. Hypersonic flows are sensitive to the scaling of the chemical rate processes, with disso-
                                                                                                                                              ciation governed by binary scaling and recombination by ternary scaling.
                                                                                                                                           5. Advanced multiphysics simulations and computational chemistry methods are being used
                                                                                                                                              to understand and accurately model key rate processes.
                                                                                                                                           FUTURE ISSUES
                                                                                                                                           1. Validation of hypersonic flow simulations and the underlying models remains a critical
                                                                                                                                              issue. It is difficult to reproduce all relevant rate processes in ground-based wind tunnels,
                                                                                                                                              and making nonintrusive measurements in these flows is a challenge.
                                                                                                                                           2. Advanced simulations should be used to design experiments that target modeling uncer-
                                                                                                                                              tainties and that can be performed in existing wind tunnels.
                                                                                                                                           3. Progress has been made in the development of finite-rate models for graphite ablation,
                                                                                                                                              but much work is needed to represent the interaction of more complex thermal protection
                                                                                                                                              materials with air reaction products.
                                                                                                                             398      Candler
                                                                                                   Review in Advance first posted on
                                                                                                   September 19, 2018. (Changes may
                                                                                                   still occur before final publication.)
                                                                                        FL51CH15_Candler    ARI     12 September 2018     12:50
                                                                                                     4. Little effort has been directed toward understanding turbulent motion at the extreme
                                                                                                        conditions of hypersonic flight.
                                                                                                     5. The prediction of hypersonic rate-dependent flows relies on computational fluid dynam-
                                                                                                        ics methods, which have been adapted from methods designed for lower-speed flows.
                                                                                                        Improved numerical methods need to be developed that are less sensitive to grid imper-
                                                                                                        fections, have low levels of dissipation and yet can capture strong discontinuities, and are
                                                                                                        efficient for problems with many chemical species and stiff source terms.
                                                                                                     6. The high-fidelity simulation of the hypersonic flow environment is far from complete; a
                                                                                                        hypersonic flight system changes during flight over a large range of time scales. Relevant
                                                                                                        processes include thermal expansion, material degradation and shape change, surface
                                                                                                        roughness changes, and fluid–structure interactions and vibrations.
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    Annu. Rev. Fluid Mech. 2019.51. Downloaded from www.annualreviews.org
                                                                                                  DISCLOSURE STATEMENT
                                                                                                  The author is not aware of any biases that might be perceived as affecting the objectivity of this
                                                                                                  review.
                                                                                                  ACKNOWLEDGMENTS
                                                                                                  This work was sponsored by the Air Force Office of Scientific Research (AFOSR) under grants
                                                                                                  FA9550-16-1-0161, FA9550-17-1-0057, and FA9550-17-1-0250. The views and conclusions con-
                                                                                                  tained herein are those of the author and should not be interpreted as necessarily representing the
                                                                                                  official policies or endorsements, either expressed or implied, of the AFOSR or the US Govern-
                                                                                                  ment. The author would like thank Joseph Brock, Ross Chaudhry, Ioannis Nompelis, and Thomas
                                                                                                  Schwartzentruber for helpful comments.
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