This quantity is a part of the Ceramic Engineering and technology continuing (CESP) series. This sequence incorporates a number of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain teeth) and complex ceramics. issues coated within the zone of complicated ceramic contain bioceramics, nanomaterials, composites, sturdy oxide gasoline cells, mechanical houses and structural layout, complex ceramic coatings, ceramic armor, porous ceramics, and more.
Content:
Chapter 1 a hundred% Oxygen Firing of Regenerative Melters (pages 1–17): Geoffrey Tuson, Ray Higdon and R. D. Moore
Chapter 2 Conversion of a big box Furnace from Regenerative Firing to Direct Oxy?Fuel Combustion (pages 18–24): R. D. Moore and J. T. Brown
Chapter three dimension and keep an eye on of NOx in Oxygen?Fired Glass Furnaces (pages 25–41): Ronny Eriksson, Don Coe and Rudiger Eichler
Chapter four A Case research of NOx, PM, and Acid fuel keep an eye on structures for Glass Furnaces (pages 42–50): Joseph Hower, Patrick King, Paula Schoen, Anne Mcqueen and George L. Moilanen
Chapter five Glass Furnace functions of SNCR NOx keep an eye on know-how: comparability of estimated and real functionality (pages 51–64): George L. Moilanen, B. Van Kalsbeek and Anne McQueen
Chapter 6 machine Modeling of Glass Processing (pages 65–81): Simon Rekhson, Zhong?Hao Lu, Claud Day, Yang Wang and Misha Rekhson
Chapter 7 Cullet Preheating: The sensible resolution for All Glass Furnaces with Cullet Addition (pages 82–90): Josef Herzog and Randy J. Settimio
Chapter eight Batch and Cullet Preheating for power discounts and elimination of Air toxins (pages 91–103): Yongguo Wu and Alfred R. Cooper
Chapter nine Boundary floor Convection and steel Drilling in Glass Tank Bottoms (pages 104–113): William A. Underwood and W. John Tracey
Chapter 10 substitute Regenerator procedure for the Nineties (pages 114–125): James D. Hull
Chapter eleven Sulfate Burnout approaches for Checker Settings in Glass Melting Furnaces (pages 126–137): George Kopser
Chapter 12 The fresh Air Act Amendments: effect on Illinois (pages 138–145): Bharat Mathur and Sharon Davis
Chapter thirteen The fresh Air Act: previous, current, and destiny (pages 146–152): James T. Destefano
Chapter 14 Silica and Silicosis—What you have to comprehend (pages 153–159): Robert E. Glenn
Chapter 15 A Message from the Government…Get the Lead Out! (pages 160–171): Juanell N. Boyd
Chapter sixteen California Recycling replace (pages 172–177): Lee H. Wiegandt
Chapter 17 Technical and price Implications of Glass box Recycling from the point of view of a neighborhood group Processing Facility (pages 178–191): M. R. Lewis and T. A. Newell
Chapter 18 bought Cullet Used as a Fiberglass Batch uncooked fabric (pages 192–203): Ernest P. Guter
Chapter 19 Glass Recycling improvement and know-how replace (pages 204–214): J. Rosenthal
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Extra info for Proceedings of the 52nd Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 13, Issue 3/4
Example text
Moore, "100% Oxygen Firing of Regenerative Melters," Cerurn. Erg. ,15 [34]1-17 (1992). 24 Ceramic Engineering & Science Proceedings Editor John B. Wachtrnan Copyright 01992 The American Ceramic Society Ceram. Eng. Sci. Proc. 13[3-4] pp. 25-41 (1992) Measurement and Control of NO, in Oxygen-Fired Glass Furnaces RONNYERIKSSON A G A Gas Innovations Independence, OH 4413 1 DON COE A G A Gas, Inc. Independence, OH 441 3 1 RUDICEHEICALER A G A Gas Innovations, GmbH Hamburg, Germany In recent years, there has been increasing interest and activity in the glass industry concerning the application of total oxy-fwl firing for glass furnnces.
Table I. 01 7 NG,,,) 34 Residence Time Residence time is the time an individual particle spends in the reactor (furnace). For a small pipe without mixing (plug flow), it is the same for all particles and equal to the time it takes to go from the inlet to the outlet of the tube. For a glass furnace with perfect mixing in the gas phase, the gas residence time follows a distribution with a mean equal to gas volume in the furnace divided by the total gas flow rate at the actual pressure and temperature in the furnace.
3. The natural gas used for combustion may contain significant amounts of nitrogen (some natural gas sources contain up to 15 vol% nitrogen). 4. Significant amounts of cold air can be drawn into the furnace through openings in the furnace structure or the burner blocks. This can increase the fuel consumption by as much as 30%. 5. Finally, the time during which the reaction has progressed is important. The time taken to reach equilibrium concentration will depend not only on the initial concentrations of nitrogen, oxygen, and nitric oxide, but also on the reaction time, reaction rate, and hence the temperature of the flame with respect to the furnace headspace.
