This quantity is a part of the Ceramic Engineering and technology continuing (CESP) series. This sequence includes a number of papers facing concerns in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complex ceramics. themes lined within the sector of complex ceramic contain bioceramics, nanomaterials, composites, reliable 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 fundamental Glass Manufacture (pages 66–75): Paul F. Guttmann
Chapter 7 forte 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 lower than Oxy?Fuel Firing stipulations (pages 109–119): A. J. Faberand and O. S. Verheijen
Chapter eleven Glass Furnace NOx regulate with fuel Reburn: the sphere try (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 collection 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 lower 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 selection 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 components 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
This method solves the radiative transfer equation in a number of discrete, angular directions spanning all solid angles. l The solution of the radiative transfer equation is coupled with the energy equation through the (source term), which represents divergence of the radiation flux vector the net rate of inflow (outflow) of radiant energy per unit volume of each elementary control volume. -V-s Capabilities The computer model is capable of predicting general three-dimensional, turbulent gas combustion in glass melting furnaces.
It was also determined that complete CO destruction could be achieved at high jet velocities (approximately 300 ft/s). 7 lb/t, NO, formation was predicted to decrease by at least 34%. However, secondary combustion was shown to occur completely within the exhaust port, as shown in Fig. 6. This prediction was consistent with the experimental data of Platten and Keffer,* who studied the extent of penetration of jets into a uniform stream at various angles in a low-speed wind tunnel under isothermal conditions.
And oxidation along with pollutant concentrations like NO,. Improvements to the radiative heat transfer model will be made to account for the presence of soot. Additional validation studies will be performed to evaluate the capabilities of the code and further refine various submodels. 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.
A Collection of Papers Presented at the 57th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 18, Issue 1