Abstract
Machining operation and presence of water droplets cause increase the surface roughness of wet steam ejector walls and change its performance in the refrigeration cycle. The purpose of this work is to investigate the influences of the primary nozzle surface roughness on wet steam ejectors in the refrigeration cycle with steam water as a working flow. The Eulerian-Eulerian model is validated by a comparison of numerical results with experimental data. Moreover, different surface roughness has been successfully applied to the primary nozzle, and its effect on the entire flow is shown. Six properties of wet steam are selected, including pressure, temperature, Mach number, average droplet radius, droplet growth rate, and liquid mass fraction. The result shows increasing roughness resulted in a shift of the shock chain to the primary nozzle, damping shock strength, and rising temperature in the diffuser. In addition, increment of the primary nozzle surface roughness decreases ER and COP of the refrigeration cycle by 3.67% and 3.8%, respectively. The designers and operators should be considered the roughness effects in the design and operation of wet steam ejectors due to the vital impact of the roughness on the liquid mass fraction, average droplet radius, droplet growth rate, ER, and COP.
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Abbreviations
- \({D}_{\omega }\) :
-
Cross-diffusion term (kgm−1 s−3)
- E:
-
Total energy (J)
- ER:
-
Entrainment ratio (-)
- \({f}_{r}\) :
-
Roughness function (-)
- G:
-
Gibbs free energy (J kg−1)
- \({\tilde{G }}_{k}\) :
-
Turbulence kinetic energy generation (kgm−1 s−3)
- \({G}_{\omega }\) :
-
Generation of ω(kgm−1 s−3)
- h:
-
Enthalpy (J kg−1)
- J:
-
Nucleation rate (m−3 s−1)
- k:
-
Turbulent dissipation rate (m2 s−3)
- \({K}_{s}^{+}\) :
-
Non-dimensional roughness height
- \({k}_{s}\) :
-
Physical roughness height (m)
- \({K}_{B}\) :
-
Boltzmann’s constant
- L:
-
Nozzle length(m)
- m:
-
Mass of one molecule (mg)
- \(\dot{m}\) :
-
Mass flow rate (kg s−1)
- Ma:
-
Mach number
- P:
-
Pressure (Pa)
- \(\dot{Q}\) :
-
Rate of heat exchange (W m−2 s−1)
- \({q}_{c}\) :
-
Condensation coefficient (-)
- r∗ :
-
Critical radius of droplets (μm)
- r:
-
Droplet radius (μm)
- \(\dot{r}\) :
-
Droplet growth rate (μm s−1)
- R:
-
Gas constant (JK−1 mol−1)
- S:
-
Saturation ratio (-)
- \({S}_{k}\) :
-
Source terms of ω (kgm−1 s−3)
- \({S}_{\omega }\) :
-
Source terms of ω (kgm−1 s−3)
- T:
-
Temperature (K)
- u:
-
Velocity (m s − 1)
- \({V}_{d}\) :
-
Mean volume of the droplets (m3)
- x:
-
Spatial component (m)
- Yk :
-
Dissipation of k (kgm−1 s−3)
- Yω:
-
Dissipation of ω (kgm−1 s−3
- α:
-
Thermal conductivity (W m−1 K−1)
- β:
-
Liquid mass fraction (-)
- Γ:
-
Mass generation rate (kg m−3 s−1)
- δij:
-
Rate of mixing layer growth (-)
- η:
-
Number of droplets (m−3)
- μ:
-
Dynamic viscosity (Pa s)
- ρ:
-
Density (kg m−3)
- σ:
-
Liquid surface tension (N m−1)
- σk :
-
Indicate turbulent Prandtl numbers for k
- σω :
-
Turbulent Prandtl numbers for ω
- τ:
-
Stress tensor (Pa)
- ω:
-
Specific turbulence dissipation (s−1)
- s:
-
Secondary
- p:
-
Primary
- e:
-
Exit
- g:
-
Gas (vapor)
- eff:
-
Effective
- l:
-
Liquid
- v:
-
Vapor
- CAE:
-
Constant Area Exit
- MCE:
-
Mixing Chamber Exit
- PNE:
-
Primary Nozzle Exit
- -:
-
Average
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Rad, M.P., Lakzian, E. & Grönman, A. Numerical investigation of roughness effect on wet steam ejector performance in the refrigeration cycle. Heat Mass Transfer 58, 1545–1560 (2022). https://doi.org/10.1007/s00231-022-03197-z
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DOI: https://doi.org/10.1007/s00231-022-03197-z