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Content:
Chapter 1 reports in Furnace research: comparability of expected 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 tub 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 adventure with Noncatalytic Denitrification (pages 37–45): Matthias R. Lindig
Chapter four High?Temperature IR Radiation Conductivity of business Glasses (pages 47–56): Peter A. Van Nijnatten, J. T. Broekhuijse and A. J. Faber
Chapter five Glass Furnace Air allows: do not forget the method (pages 57–64): Michael L. Newsom
Chapter 6 Fused Zirconia or Fused AZS: that is the best option? (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 evidently happening Radioactive fabrics: concerns 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 information within the Batch Plant (pages 155–170): Richard okay. 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 techniques (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 outline (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 technique for Controlling NOx Emissions: A Refractory viewpoint (pages 243–253): Ian Shulver
Chapter 19 bettering Oxy?Fuel Furnace working potency: An Operator's point of view (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 expertise (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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Extra info for 59th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 20, Issue 1

Sample text

First Experience after Conversion In August 1996 the tank was heated up. The temperature profile in glass was adjusted by the energy distribution according to the temperature profile of the former regenerative funnel tank. From the first day on, the glass quality was not a point of concern at any time. The increase in water dissolved in glass because of the gas-oxy firing had no visible impact on any forming conditions. The conversion did not result in a more severe scum problem in the batch area.

Are investigated, allowing useful conclusions to be drawn and possible recommendations to be made. The parametric studies in this paper involve crown height and flue gas exhaust locations. Different tank designs have been studied and the results are presented and discussed in the following sections. Glass Furnace Validation The Johns Manville Cleburne, Texas, borosilicate (wool) glass furnace investigated here has a nominal pull rate of 136 t/day. The full oxy-fired furnace is equipped with 10 Alglass burners.

3 is less than 6°C. The glass outlet temperatures are also in excellent agreement. An additional indication of the glass tank simulation accuracy consists of the batch area, which is restricted to a surface upstream of the bub- 27 blers. The tank operation and the results obtained by the computer simulation are in good agreement, suggesting a good estimation of the batch properties. It is concluded that the results obtained by the computer simulation accurately describe the actual operation of the glass tank, both in the combustion space and in the glass space.

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