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This quantity is a part of the Ceramic Engineering and technological know-how continuing  (CESP) series.  This sequence includes a number of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complicated ceramics. issues coated within the zone of complicated ceramic comprise bioceramics, nanomaterials, composites, stable oxide gas cells, mechanical homes and structural layout, complex ceramic coatings, ceramic armor, porous ceramics, and more.

Content:
Chapter 1 Philosophy, layout, and function of Oxy?Fuel Furnaces (pages 1–14): Marvin Gridley
Chapter 2 In?Situ checking 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 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 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 below Oxy?Fuel Firing stipulations (pages 109–119): A. J. Faberand and O. S. Verheijen
Chapter eleven Glass Furnace NOx keep watch over with gasoline 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 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, okay. R. Selkregg and S. Gould
Chapter sixteen choice 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 solid 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 superior 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

Example text

Full furnace OEAS demonstration testing began with a reduction in PSR with no staging applied. Results for NO, and CO stack emissions are presented in Fig. 9. The NO, reduction with lower combustion air follows the relationship illustrated in Fig. 1. 02 decreased NO, by up to 40% while causing a sharp increase in CO emissions. Note that furnace operation changes between the single port pair testing and the full furnace testing significantly reduced NO, values for this furnace. Therefore, the baseline NO, values were very low before application of OEAS during the full furnace testing.

The OEAS technology is an excellent choice if 50-75% NO, reduction is needed. The OEAS cost in dollars per ton of glass is optimum at 60% NO, reduction. There may be cost increases in dollars per ton of glass at lower NO, abatement levels since optimum eficiency may not be maintained. An additional NO, abatement cost consideration in selecting OEAS is the impact o f secondary oxidant and air staging options. Several air staging options are available for secondary oxidant injection, and oxidant can be supplied by ambient air, compressed air, hot air, or oxygen-enriched hot or ambient air.

2% SO,). Figure 36 shows the sample Ceram. €DQ. Sci. , 18 111 (1997) 25 Figure 33. Figure 34. Figure 35. Figure 36. installed in the peephole between burner 5 and 6 of the 9211 air-fuel furnace, and Fig. 37 shows the sample installed in the port of the 9212 oxyfuel furnace. This test is not a valid comparison, but the sample held up in the air-fuel application; however, it showed significant corrosion, erosion, and condensate attack in the port of the oxy-fuel furnace. This material is believed to be too porous for oxy-fuel applications since the flux has easy access to the matrix of the refractory, thus enhancing refractory breakdown.

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