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 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 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 choice 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 because of Oxy?Fuel Firing (pages 107–113): Gunter Frohlich
Chapter nine clearly 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 data 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 an eye on for Glass production procedures (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 study: 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 procedure 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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Extra resources for 59th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 20, Issue 1
For this reason, redox measurements must be included in the high-temperature measurements necessary to obtain the optical properties of the glass for radiative transfer modeling. In the following sections we will discuss the measurement principle, the design of the OTF, and the preliminary measurement results obtained on clear float glass. The OTF will be used to obtain a database of reliable data on the spectral absorption of various industrial glass compositions at temperatures up to 1450°C. I2 It was shown that most of the systematic errors can be significantly reduced by using the ratio of measurements obtained for different optical path lengths.
Coupled simulations provide complete, consistent representation of the transport phenomena processes occurring in the glass tank. The design and operation data from an existing oxy-fuel insulation fiberglass tank are used as a baseline case, and o comparison with measurements provides a validation of the simulation results. The results show an important effect of the crown height on heat flux to the glass surface and on crown temperature profile, suggesting the existence of an optimal height. The exhaust port location is also an important tank design parameter, and some ofthe advantages ofsidewall locations as opposed to the existing backwall location are presented.
Coupled combustion space-glass space codes have been proven to accurately simulate existing plant operation. Champinot4 shows very good agreement between operational data and the computer simulation for the well-documented TC2 1 float glass furnace. The numerical simulations have been proven also to accurately predict operational changes following the conversion of existing designs to alternative firing schemes. ' simulate the operation of the TC21 float glass furnace following its conversion from air combustion to oxy combustion.