This quantity is a part of the Ceramic Engineering and technology continuing (CESP) series. This sequence encompasses a selection of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complex ceramics. issues lined within the sector of complicated ceramic contain bioceramics, nanomaterials, composites, good oxide gasoline 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 know-how: 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 uniqueness Glass uncooked fabrics: prestige and advancements (pages 76–86): Richard J. Bauer and Sandra L. Gray
Chapter eight replace at the Glass of the long run (pages 87–94): Theodore R. Johnson
Chapter nine power Benchmarking: a device for carrying on with approach development for the Glass (pages 95–108): C. Philip Ross
Chapter 10 Refractory Corrosion below Oxy?Fuel Firing stipulations (pages 109–119): A. J. Faberand and O. S. Verheijen
Chapter eleven Glass Furnace NOx regulate with fuel Reburn: the sector try out (pages 120–135): Richard Koppang, Antonio Marquez, David Moyeda, Michael Joshi, Patrick Mohr and Roger Madrazo
Chapter 12 checking 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 number 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, okay. 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 resources for A Collection of Papers Presented at the 57th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 18, Issue 1
It is important that Ceram. Eng. Sci. , 18 111 (1997) 29 designers have as much information as possible about furnace behavior to evaluate alternatives. There are basically three methods to obtain this information: measurements on operating furnaces, physical modeling using small-scale laboratory models, and numerical simulation. Measurements on full-size furnaces are both difficult to perform and expensive. Few industrial-size furnaces are designed for the purpose of obtaining measurements. It is also difficult to obtain the desired range of operating conditions on a large furnace.
This arrangement maintained a glass temperature of about 2400-2600°F while simultaneously allowing the measurement of heat transfer rates to the molten glass. Inlet ports consisted of a 20 x 11 in. 94 cm) inclined roof and floor air port and two underfire Combustion Tec gas burners at one endwall. Combustion air was preheated with an indirectly fired air heater to 1000°F and then heated to 2300°F using a direct-fired air heater. Oxygen was then added to the combustion air before entering the furnace to replace the oxygen used during the direct heating process to simulate typical regenerative furnace inlet air composition.
Underport injection has fewer safety risks but is intuitively questionable since direct opposition to the exhaust flow might again cause jet penetration to be limited. To quantitatively evaluate these options, three models were examined: crown injection with one nozzle, underport injection with one nozzle, and underport injection with two nozzles. The results revealed that while crown injection recovers more than 90% of the energy due to secondary combustion, only about 21% NO, reduction (as compared to more than 34%) is achieved, possibly due to interaction between the staging oxidant and the primary combustion zone.
A Collection of Papers Presented at the 57th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 18, Issue 1