Chapter 1 experiences in Furnace research: comparability of estimated Thermal potency of Regenerative and High?Oxygen Glass Tanks (pages 1–21): Robert H. Essenhigh
Chapter 2 Oxy?Fuel Furnace layout Optimization utilizing Coupled Combustion/Glass bathtub Numerical Simulation (pages 23–36): D. Shamp, O. Marin, M. Joshi, C. Champinot, B. Jurcik and R. Grosman
Chapter three television Oxy?Fuel Conversion and event with Noncatalytic Denitrification (pages 37–45): Matthias R. Lindig
Chapter four High?Temperature IR Radiation Conductivity of commercial Glasses (pages 47–56): Peter A. Van Nijnatten, J. T. Broekhuijse and A. J. Faber
Chapter five Glass Furnace Air allows: remember the method (pages 57–64): Michael L. Newsom
Chapter 6 Fused Zirconia or Fused AZS: that is the most suitable choice? (pages 65–80): Gerard Duvierre and Yves Boussant?Roux
Chapter 7 replace on number of Refractories for Oxy?Fuel Glass?Melting carrier (pages 81–105): S. M. Winder, ok. R. Selkregg and A. Gupta
Chapter eight A Fused Silica Pumpable Refractory for Crown harm caused by Oxy?Fuel Firing (pages 107–113): Gunter Frohlich
Chapter nine obviously happening Radioactive fabrics: matters for Glassmakers (pages 115–132): Charles T. Simmons
Chapter 10 Mathematical Modeling of Forehearths (pages 133–141): O. M. G. C. Op Den Camp, E. G. J. Peters and V. O. Aume
Chapter eleven Oxy?Gas Forehearths: result of Mathematical Modeling of a Flint Glass and box Trials on a Borosilicate Glass (pages 143–154): Alan Stephens, Tom Clayton, Mahendra Misra, John Brown and James Cook
Chapter 12 statistics within the Batch Plant (pages 155–170): Richard ok. Pelle
Chapter thirteen blending version Simulation of an On?the?Fly Glass Conversion (pages 171–180): Richard Bergman
Chapter 14 Generalized Predictive keep watch over for Glass production tactics (pages 181–206): David M. Koenig
Chapter 15 The Glass in Germany: Environmentally Sound Melting and Recycling of Glass (pages 207–214): Helmut A. Schaeffer
Chapter sixteen The NSF Industry?University middle for Glass learn: an summary (pages 215–226): T. P. Seward
Chapter 17 A High?Efficiency, Low?NOx Burner for Oxy?Gas Glass Furnaces (pages 227–241): David Rue, Hamid Abbasi, David Neff and Patrick Mohr
Chapter 18 The Pilkington 3R approach for Controlling NOx Emissions: A Refractory point of view (pages 243–253): Ian Shulver
Chapter 19 enhancing Oxy?Fuel Furnace working potency: An Operator's viewpoint (pages 255–269): D. Shamp, J. Smith, M. Joshi, H. Borders, O. Charon and R. Grosman
Chapter 20 an instantaneous comparability of Oxy?Fuel Burner know-how (pages 271–281): John H. Tyler, James F. sales space, Robert D. Marchiando and Kevin A. Lievre
Chapter 21 The Glass production Council (pages 283–287): James A. Shell
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Additional resources for 59th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 20, Issue 1
8%, while the lowest crown case shows an increase of 4% as compared to the base case, suggesting a quasi-linear variation of the heat flux with the crown height, at least for this interval. The flue gas temperatures allow for better understanding of the differences in heat flux to the glass. Figure 6 presents the flue gas temperatures for the base case and for the cases involving different crown heights. Note that the low crown case does not significantly change the flue gas temperature. The lowest crown case shows a significantly lower flue gas temperature, attributed to an enhanced heat flux to the wall and to the glass, as well as in part to a lower exit location of the flue gases.
2. N. Neuroth, “Der TemperatureinfluR auf die optischen Konstanten von Glas im Gebiet starker Absorption, Glastech. 41 1-422 (1955). 3. J. E. Jellyman, “Infrared Transmission of Glass in the Range Room Temperature to 1400”,” J. , 39 ( I 955). 4. EJ. Grove, “Spectal Transmission of Glass at High Temperature and Its Application to Heat-Transfer Problems,” J. Am. Ceram. , 44. 3 17-320 (1961). 5. A. , “Strahlungswarmeleitfahigkeit van Glas - EinfluR det Glaszusammen-setzung auf seine Warmedurchlassigkeit-,” Glastech.
It became clear that it was almost impossible to retain the conventional firing system. The building, the TV panel tank, and the flue gas conditions forced us to face a conversion of that tank. Additionally, the bag house capacity did not allow an increase of the flue gas volume. The selective catalytic reduction processing for denitrification behind the bag house would have required reheating the clean gas. In light of these facts the conversion became reasonable, although during the project development phase it became clear that the conversion would cause problems in terms of permits.