Dilution of a Polymer Additive in a Turbulent Boundary Layer on a Body of Revolution.

Abstract

This paper treats the problem of calcuating wall concentration of a polymer additive injected into a turbulent boundary layer on a body of revolution. The theory requires specification of a similarity law for local concentration as well as a form for the time averaged velocity profile. The chosen concentration law is a generalized form of an empirical profile found valid for the flat plate case. solutions are presented for a 1/n power law profile (not deemed suitable for polymer seeded flows), and for a generalized logarithmic law of wall corrected by Coles' law of wake. the 1/n power law leads to a final solution for the boundary layer thickness (obtained from the momentum integral equation), which involves a straight-forward numerical quadrature dependent upon the geometry of the body. Assuming the generalized profile leads to a nonlinear differential equation for the shear velocity (related to the boundary layer thickness) requires a numerical solution. In nearly cylindrical regions, the solution of this equation simplifies to a quadrature dependent only on a boundary condition and on a polymer constant in the velocity profile. In each case, the dilution law, while appearing complicated, depends on a one-time evaluation of several special functions using values of the constants appearing in the assumed profiles. (Author)

Document Details

Document Type
Technical Report
Publication Date
Jul 15, 1970
Accession Number
AD0874793

Entities

People

  • R. C. Lessman

Organizations

  • Naval Underwater Systems Center

Tags

DTIC Thesaurus Topics

  • Additives (Chemicals)
  • Boundaries
  • Boundary Layer
  • Differential Equations
  • Dilution
  • Equations
  • Geometry
  • Integral Equations
  • Layers
  • Nonlinear Differential Equations
  • Numerical Quadrature
  • Revolutions
  • Thickness
  • Turbulent Boundary Layer

Fields of Study

  • Physics

Readers

  • Calculus or Mathematical Analysis
  • Fluid Dynamics.