This quantity is a part of the Ceramic Engineering and technological know-how continuing (CESP) series. This sequence incorporates a number of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain tooth) and complicated ceramics. themes lined within the zone of complex ceramic comprise bioceramics, nanomaterials, composites, good oxide gas cells, mechanical houses and structural layout, complex ceramic coatings, ceramic armor, porous ceramics, and more.
Chapter 1 Philosophy, layout, and function of Oxy?Fuel Furnaces (pages 1–14): Marvin Gridley
Chapter 2 In?Situ trying out of Superstructure Refractories (pages 15–28): Don Shamp
Chapter three improvement and Implementation of a Three?Dimensional Combustion Code to be used in Glass Melting Furnaces (pages 29–42): ok. L. Jorgensen, S. Ramadhyani, R. Viskanta and L. W. Donaldson
Chapter four Demonstration of Cost?Effective NOx aid on a Regenerative Sideport Glass Furnace utilizing Oxygen?Enriched Air Staging (pages 43–59): P. Mohr, D. Neff, D. Rue, H. Abbasi, J. Li and S. Hope
Chapter five Pilkington 3R expertise: An replace (pages 60–65): I. N. W. Shulver and R. Quirk
Chapter 6 uncooked fabrics for basic Glass Manufacture (pages 66–75): Paul F. Guttmann
Chapter 7 strong point Glass uncooked fabrics: prestige and advancements (pages 76–86): Richard J. Bauer and Sandra L. Gray
Chapter eight replace at the Glass of the longer term (pages 87–94): Theodore R. Johnson
Chapter nine strength Benchmarking: a device for carrying on with procedure development for the Glass (pages 95–108): C. Philip Ross
Chapter 10 Refractory Corrosion less than Oxy?Fuel Firing stipulations (pages 109–119): A. J. Faberand and O. S. Verheijen
Chapter eleven Glass Furnace NOx keep watch over with fuel Reburn: the sphere try (pages 120–135): Richard Koppang, Antonio Marquez, David Moyeda, Michael Joshi, Patrick Mohr and Roger Madrazo
Chapter 12 trying out of Superstructure Refractories in a Gas?Oxy surroundings opposed to High?Alkali Glasses (pages 136–145): L. H. Kotacska and T. J. Cooper
Chapter thirteen choice of optimal Refractories for the Superstructure of Oxy?Fuel Glass Melting Furnaces (pages 146–163): Gerard Duvierre, Alain Zanoli, Yves Boussant?Roux and Mike Nelson
Chapter 14 Stabilizing Distressed Glass Furnace Melter Crowns (pages 164–179): Laura A. Lowe, John Wosinski and Gene Davis
Chapter 15 Refractory Corrosion habit less than Air?Fuel and Oxy?Fuel Environments (pages 180–207): H. T. Godard, L. H. Kotacska, J. F. Wosinski, S. M. Winder, A. Gupta, ok. R. Selkregg and S. Gould
Chapter sixteen decision of hint Impurities in a Furnace surroundings at working Temperature (pages 208–215): Stephen S. C. Tong, John T. Brown and Lawrence H. Koiacska
Chapter 17 Molybdenum/Fused forged AZS fabric for severe parts in Glass Melting Tanks (pages 216–224): M. Dunkl, A. Fantinel, G. Dinelli and R. Tognon
Chapter 18 Chromic Oxide Blocks to be used within the Glass box (pages 225–238): F. Gebhardt, G. Boymanns, E. Goerenz, H. Ebigt and G. Frohlich
Chapter 19 Low Emissions from Endport Furnaces (pages 239–250): T. J. Harper
Chapter 20 Regenerative Oxygen warmth restoration for more advantageous Oxy?Fuel Glass Melter potency (pages 251–265): Richard Browning and James Nabors
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Additional info for A Collection of Papers Presented at the 57th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 18, Issue 1
5 ft into the regenerator were used. Stack samples were obtained through a stainless steel tube. Table I shows baseline port and stack measurements made during single port pair testing. 3 and 3 lb/t of glass during the week of OEAS testing. Ports are numbered from the charging end. The baseline emissions monitoring confirmed a wide variation in port stoichiometries with the highest excess air used in ports 1, 2, and 6. Because the ports are not isolated, port emission levels are affected by mixing in the furnace and by regenerator top crossflow.
10 & -----& 35 40 45 0 2 , X in secondary oxidant c - , 4-__ 55 50 200 0 60 Figure 11. Effect of OEAS oxygen concentration on NO, and CO emissions. Analysis of the data in Fig. 02 for OEAS demonstration. Staging was then applied to all ports using enriched air containing 35% O2 to raise the overall stoichiometric ratio to various levels. The results of this testing are presented in Fig. 10. Firing the furnace from the left and right side produces different NO, values at the same stoichiometric ratio, but the trend is the same for both.
Data sets with gas temperature measurements and wall radiative and total heat flux measurements will be most useful in this effort. Of primary concern is a validation against data from an industrial-scale glass melting furnace. Also, extending the validation to other types of furnaces can prove helpful in exercising the code and submodels. Parametric calculations will be performed to gain insights to the transport phenomena, gain expertise in using the computer code, and identify critical model parameters.
A Collection of Papers Presented at the 57th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 18, Issue 1