From: Industrial dry spinning processes: algorithmic for a two-phase fiber model in airflows
Composite reference values | ||
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Description | Formula | Unit |
Length scale | \(s_{0}=r_{0}\) | m |
Fiber length | \(L_{0}=r_{0}\) | m |
Cross-sectional radius | \(R_{0}=d_{0}\) | m |
Mass density | \(\rho _{0}=\varrho _{M,0}/d_{0}^{2}\) | kg/m3 |
Scalar velocity | \(u_{0}=v_{0}\) | m/s |
Stress | \(\sigma _{0}=\varrho _{M,0}v_{0}^{2}\) | N |
Outer force | \(f_{0}=\varrho _{M,0}v_{0}^{2}/r_{0}\) | N/m |
Enthalpy | \(h_{0}=q_{0}T_{0}\) | J/kg |
Evaporation enthalpy | \(\delta _{0}=h_{0}\) | J/kg |
Mass transfer coefficient | \(\beta _{0}=\gamma _{0}/\rho _{\star ,0}\) | m/s |
Air temperature | \(T_{\star ,0}=T_{0}\) | K |
Air velocity | \(v_{\star ,0}=v_{0}\) | m/s |
Dimensionless numbers | |
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Description | Formula |
Slenderness | \(\varepsilon =d_{0}/r_{0}\) |
Reynolds | \(\mathrm{Re}=\varrho _{M,0}v_{0}r_{0}/(d_{0}^{2}\mu _{0})\) |
Froude | \(\mathrm{Fr}=v_{0}/\sqrt{gr_{0}}\) |
Drawing | \(\mathrm{Dr}=u_{\mathrm{out},0}/u_{0}\) |
Mass Peclet | \(\mathrm{Pe}_{c}=v_{0}d_{0}/D_{0}\) |
Temperature Peclet | \(\mathrm{Pe}_{T}=\varrho _{M,0}v_{0}q_{0}/(C_{0}d_{0})\) |
Mass Stanton | \(\mathrm{St}_{c}=\gamma _{0}d_{0}^{2}/(v_{0}\varrho _{M,0})\) |
Temperature Stanton | \(\mathrm{St}_{T}=\alpha _{0}d_{0}^{2}/(v_{0}\varrho _{M,0}q_{0})\) |
Air-fiber Reynolds | \(\mathrm{Re}_{\star }=d_{0}v_{0}/\nu _{\star ,0}\) |
Nusselt | \(\mathrm{Nu}_{\star }=\alpha _{0}d_{0}/\lambda _{\star ,0}\) |
Prandtl | \(\mathrm{Pr}_{\star }=q_{\star ,0}\rho _{\star ,0}\nu _{\star ,0}/\lambda _{\star ,0}\) |
Sherwood | \(\mathrm{Sh}_{\star }=\gamma _{0}d_{0}/(\rho _{\star ,0}D_{d,\star ,0})\) |
Schmidt | \(\mathrm{Sc}_{\star }=\nu _{\star ,0}/D_{d,\star ,0}\) |