Hostname: page-component-cd9895bd7-7cvxr Total loading time: 0 Render date: 2024-12-20T08:43:18.832Z Has data issue: false hasContentIssue false

Confined axisymmetric laminar jets with large expansion ratios

Published online by Cambridge University Press:  09 April 2002

A. REVUELTA
Affiliation:
Area de Mecánica de Fluidos, Departamento de Ingeniería Mecánica, Universidad Carlos III de Madrid, 28911 Leganés, Spain
A. L. SÁNCHEZ
Affiliation:
Area de Mecánica de Fluidos, Departamento de Ingeniería Mecánica, Universidad Carlos III de Madrid, 28911 Leganés, Spain
A. LIÑÁN
Affiliation:
Departamento de Motopropulsión y Termofluidodinámica, E. T. S. I. Aeronáuticos, Universidad Politécnica de Madrid, 28040 Madrid, Spain

Abstract

This paper investigates the steady round laminar jet discharging into a coaxial duct when the jet Reynolds number, Rej, is large and the ratio of the jet radius to the duct radius, ε, is small. The analysis considers the distinguished double limit in which the Reynolds number Rea = Rejε for the final downstream flow is of order unity, when four different regions can be identified in the flow field. Near the entrance, the outer confinement exerts a negligible influence on the incoming jet, which develops as a slender unconfined jet with constant momentum flux. The jet entrains outer fluid, inducing a slow back flow motion of the surrounding fluid near the backstep. Further downstream, the jet grows to fill the duct, exchanging momentum with the surrounding recirculating flow in a slender region where the Reynolds number is still of the order of Rej. The streamsurface bounding the toroidal vortex eventually intersects the outer wall, in a non-slender transition zone to the final downstream region of parallel streamlines. In the region of jet development, and also in the main region of recirculating flow, the boundary-layer approximation can be used to describe the flow, while the full Navier–Stokes equations are needed to describe the outer region surrounding the jet and the final transition region, with Rea = Rejε entering as the relevant parameter to characterize the resulting non-slender flows.

Type
Research Article
Copyright
© 2002 Cambridge University Press

Access options

Get access to the full version of this content by using one of the access options below. (Log in options will check for institutional or personal access. Content may require purchase if you do not have access.)