New analytical solutions to water wave radiation by vertical truncated circular cylinders are developed based on linear potential flow theory. Two typical cylinder configurations of a surface-piercing cylinder and a submerged floating cylinder are considered. The multi-term Galerkin method is employed in the solution procedure, in which the fluid velocity on the interface between different regions is expanded into a set of basis function involving the Gegenbauer polynomials, and the cube-root singularity of fluid velocity at the side edges of the truncated cylinders is correctly modeled. The present solutions have the merits of very rapid convergence. The results with six-figure accuracy for added mass and radiation damping can be obtained using a few truncated numbers in the basis function for three motions (surge, heave and roll). The calculated results of the present solutions agree well with that by a higher-order boundary element method solution. Calculation examples are presented to investigate the influence of the motion frequency on the added mass and the radiation damping of the truncated cylinders with different geometric parameters. The present solutions can be used as a reliable benchmark for numerical solutions to water wave radiation by complicated structures.
相似文献Wärmeübergang an eine senkrecht anf eine Zylinderreihe auftreffende Gas-Flüssigkeits-Sprüh-Strömung
Zusammenfassung Es wurden Messungen und theoretische Analysen des Wärmeübergangs zwischen einer Gas-FlüssigkeitsSprüh-Strömung und den glatten Oberflächen einer Zylinderreihe durchgeführt, die senkrecht zum Sprühstrahl angeordnet waren. Dabei wurde in der Analyse unter anderem das Phänomen betrachtet, daß die Tropfen die Zylinderwand treffen und verfehlen können und daß sich ein Verdampfungsprozeß aus dem flüssigen Film an der Zylinderoberfläche einstellt.Gemessen wurde an einem zwischen zwei Randzylindern befindlichen Zylinder.Die Experimente und die Analyse gestatten die Schlußfolgerung, daß der Wärmeübergangskoeffizient für eine Zylinderreihe höher ist als für einen einzelnen Zylinder in der Sprühströmung.
Nomenclature a distance between axes of cylinders, m - c l specific heat capacity of liquid, J/kg K - c g specific heat capacity of gas, J/kg K - D cylinder diameter, m - g l mass velocity of liquid, kg/m2s - ¯k average volume ratio of liquid entering film to amount of liquid directed at the cylinder in gas-liquid spray flow, dimensionless - k() local volume ratio of liquid entering film to amount of liquid directed at the cylinder in gas-liquid spray flow, dimensionless - L specific latent heat of vaporisation, J/kg - m mass fraction of water in gas-liquid spray flow, dimensionless - M constant in Eq. (9) - p pressure, Pa - p g statical pressure of gas, Pa - p w pressure of gas on the cylinder surface, Pa - p external pressure on the liquid film surface, Pa - r cylindrical coordinate, m - R radius of cylinder, m - T temperature, K, °C - T l, tl liquid temperature in the gas-liquid spray, K, °C - T w,tw temperature of cylinder surface, K, °C - T temperature of gas-liquid film interface, K - U liquid film velocity, m/s - w gas velocity on cylinder surface, m/s - w g gas velocity in free stream, m/s - W l liquid vapour mass ratio in free stream, dimensionless - W liquid vapour mass ratio at the edge of a liquid film, dimensionless - x coordinate, m - y coordinate, m - z complex variable, dimensionless - average heat transfer coefficient, W/m2K - local heat transfer coefficient, W/m2 K - average heat transfer coefficient between cylinder surface and gas, W/m2 K - g, local heat transfer coefficient between cylinder surface and gas, W/m2 K - mass transfer coefficient, kg/m2s - liquid film thickness, m - lg dynamic diffusion coefficient of liquid vapour in gas, kg/m s - pressure distribution function on a cylinder surface - function defined by Eq. (3) - l liquid dynamic viscosity, kg/m s - g gas dynamic viscosity, kg/m s - cylindrical coordinate, rad, deg - l thermal conductivity of liquid, W/m K - g thermal conductivity of gas, W/m K - mass transfer driving force, dimensionless - l density of liquid, kg/m3 - g density of gas, kg/m3 - w shear stress on the cylinder surface, N/m2 - w shear stress exerted by gas at the liquid film surface, N/m2 - air relative humidity, dimensionless - T -T w - w =T wTl Dimensionless parameters I= enhancement factor of heat transfer - m *=M l/Mg molar mass of liquid to the molar mass of gas ratio - Nu g= D/ g gas Nusselt number - Pr g=c g g/g gas Prandtl number - Pr l=clll liquid Prandtl number - ¯r=(r–R)/ dimensionless coordinate - Re g=wgD g/g gas Reynolds number - Re g,max=wg,max D g/g gas Reynolds number calculated for the maximal gas velocity between the cylinders - Sc=m * g/l–g Schmidt number =/R dimensionless film thickness 相似文献