Search or ask a question
Pricing
Login
Sign up
Home
Notebook
BETA
Profile
Citation booster
Literature Review
Copilot
Citation generator
Paraphraser
AI Detector
Chrome Extension
Talk with us
Use on ChatGPT
All figures (22)
Fig. 15. Wall temperature profile in the middle of the period.
Fig. 4. Evolution of the dimensionless velocity profile as a function of the distance to the wall when Grz = 8.44 · 1010: comparison between our numerical results and Ref. [28].
Table 2 Results of the test for a transparent medium
Fig. 3. Evolution of the local heat transfer coefficient along the plate: comparison between our numerical results and Ref. [28].
Fig. 8. Dimensions of the enclosure used for testing the radiative model.
Table 3 Results of the test for a semi-transparent medium
Fig. 2. Definition of the variables used in the radiation calculations.
Fig. 7. Axial evolution of the dimensionless heat transfer coefficient: comparison between our numerical results and experimental values from [32].
Table 4 Absolute error of the suction pyrometers ( C)
Fig. 11. A–A view of the test regenerator showing the 36 sub-channels.
Fig. 12. Distribution of the thermocouples in the wing of a cruciform.
Fig. 6. Evolution of turbulence intensity as a function of the distance to the wall when Grz = 8.44 · 1010: comparison between our numerical results and Ref. [28].
Table 6 Working conditions
Fig. 13. Scheme of an elementary channel.
Table 5 Comparison of calculation methods for geometric data
Fig. 10. Tip of one of the suction pyrometers.
Fig. 9. Test section of our experimental regenerator.
Fig. 5. Evolution of the dimensionless temperature profile as a function of the distance to the wall when Grz = 8.44 · 1010: comparison between our numerical results and Ref. [28].
Table 7 Experimental results of Lagarenne [9] for an elementary channel
Fig. 14. Profile of the regenerated heat flux for the cold period: comparison between our numerical models and the experimental data from [9].
Table 8 Comparison of global energy exchanged for an elementary channel (models 1 and 2 have been presented in Section 2)
Fig. 1. Sketch of the flow in the channel of a glass furnace regenerator during each hot (a) and cold (b) period.
Journal Article
•
DOI
•
A numerical approach for the study of glass furnace regenerators
[...]
Y. Reboussin
1
,
Jean-François Fourmigué
,
Philippe Marty
,
Olivier Citti
1
•
Institutions (1)
Saint-Gobain
1
01 Oct 2005
-
Applied Thermal Engineering