Abstract

In this research, a numerical study was carried out on heat transfer by natural convection, in a closed tunnel greenhouse, in the range of the Rayleigh number (103≤Ra≤106). Were considered in the study, the number of heating tubes used (1≤Nt≤7), which were equidistant inside the greenhouse volume, when the bottom at an average temperature and cold Roof. The governing equations written in a bicylindrical coordinates were discretized using the finite volume method and vorticity-stream function formulation; the resulting algebraic equations were solved using successive over relaxation method (S.O.R). First, the effect of the Rayleigh number on heat transfer was examined for a fixed number of tubes as reference (Nt = 3) and the number of tubes was varied to investigate the influence on heat transfer in the greenhouse. Finally, the results obtained were summarized in the form of isotherms and streamlines, and for the average Nusselt number profile; in addition to the horizontal and vertical velocities and temperatures. However, in the reference case, for low Rayleigh numbers, the heat transfer is dominated by pure conduction.With the increase of the Rayleigh number and the number of tubes Nt, the natural convection becomes more dominant and the heat transfer increases, and in general the heat transfer increase with the increasing number of tubes.

Highlights

  • The tunnel greenhouse is a production tool, allowing to create artificially a microclimate intended to favor the growth and the development of cultures

  • A numerical investigation is made on the natural convection in the greenhouse, and the fluid is chosen as air with a Prandtl number Pr=0.702

  • The objective of this study is to examine the influence of the Rayleigh number and the number of tubes Nt on the flow and the heat transfer inside the greenhouse

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Summary

Introduction

The tunnel greenhouse is a production tool, allowing to create artificially a microclimate intended to favor the growth and the development of cultures. Has primarily focused on the influence of the various parameters of the system, in particular the inclination with respect to the horizontal plane, the shape factor, the number of Grashof, the average and local values of the Nusselt numbers, as well as temperature and streamlines distributions of. He has find that the minimum heat transfer is obtained for angles of inclination between 30 and 45°. Bondareva et al [4] inspected

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