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May 16, 2010, 05:19 |
Mesh refinement
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#1 |
New Member
Join Date: Apr 2010
Posts: 6
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To understand mesh refinement concepts I modelled a pipe (10 mm dia, 500 mm long) having three flow velocities (4, 6 and 8 m/s, water as fluid). Mesh refinement was carried out in the 2 mm thick layer by changing no of elements in the layer. Four runs were taken with no of elements 5, 7, 9 and 11. The mesh was generated in such a way that element thickness is smallest near the wall and gradually increases towards the centre. Figure shows the typical grid profile showing 11 elements in 2 mm thick layer.
Fig-1 The analysis was carried out using k-e model with scalable wall function. (As a rule, none of the defaults were changed). Inlet temperature for water was 300 K. Wall temperature was 373 K. Values for y+ and wall heat transfer coefficient (hf) were noted at a distance of 400 mm from entry. Line averaging was carried out. Inlet pressure was also noted (using ‘area averaged’ tool). Outlet pressure was set 0 Pa. Figure shows variation in y+ as a function of number of elements (at a plane 400 mm from inlet). Fig-2 Figures show variation in heat transfer coefficient (at a plane 400 mm from inlet) and inlet pressure as a function of number of elements. Fig-3 and Fig-4 Doubts:- - Can I consider that I have obtained mesh convergence with 5 elements? The two important parameters ‘heat transfer coefficient’ and ‘pressure drop’ remain practically unchanged. - Should I be greedier and try to use even less than 5 elements say 3 or 4 in the 2 mm thick layer near wall? |
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