59th Conference on Glass Problems: Ceramic Engineering and

Chapter 1 reviews 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 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 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, okay. R. Selkregg and A. Gupta
Chapter eight A Fused Silica Pumpable Refractory for Crown harm as a result of Oxy?Fuel Firing (pages 107–113): Gunter Frohlich
Chapter nine obviously taking place 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 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 approaches (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 heart 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 strategy for Controlling NOx Emissions: A Refractory standpoint (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 a right away 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

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In practice, the furnaces will be used only up to 1450°C to avoid unnecessary aging of the heater wires and other materials. Measurement Modes In the high-temperature range (>900°C) for which the glass has a sufficient low viscosity, measurements can be performed for two different immersion depths, thereby obtaining two different optical path lengths. This is also the range for simultaneous redox measurements. The ratio of the measured spectra for these two optical path lengths is used to calculate the absorption spectrum.

Numerical modeling of the existing tank includes separate geometries for the combustion space and the glass melt space. The combustion space, modeled with Athena, consists of 270 000 cells, while the glass tank, modeled with the licensed TNO-GTMI computer program, consists of 67 000 cells. The coupled Athena/TNO-GTM calculation of the existing tank operation (base case) has been checked for appropriate numerical convergence, as well as for an accurate description of the measured parameters. Besides the natural gas and oxygen flow rates into the furnace, the numerical calculations simulate an additional flow of infiltration air, in order to account for the approximate 11% oxygen concentration measured in the flue gases.

3. 4. 5. 6. 36 59th Conjerence on Glass Problems Charles H. Dmmmond I I I Copyright01999 by The American Ceramic Society TV Oxy-Fuel Conversion and Experience with Noncatalytic Denitrification Matthias R. Lindig Schott Glas, Mainz. Germany Int roduct ion Schott Glas in Mainz operates three TV tanks. Until 1996, all three were regenerative cross-fired tanks. The two TV panel tanks used to run with mixed gadoil underport firing, and the TV funnel tank ran with gas sideport firing. The TV panel tanks had already been rebuilt with a catalyzer system for NO, abatement when the discussion about oxy-fuel conversion just started.

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