Download e-book for kindle: A Collection of Papers Presented at the 54th Conference on by

ISBN-10: 0470314400

ISBN-13: 9780470314401

ISBN-10: 0470375302

ISBN-13: 9780470375303

This quantity is a part of the Ceramic Engineering and technology continuing  (CESP) series.  This sequence includes a selection of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain tooth) and complex ceramics. subject matters coated within the region of complex ceramic contain bioceramics, nanomaterials, composites, sturdy oxide gas cells, mechanical homes and structural layout, complex ceramic coatings, ceramic armor, porous ceramics, and more.

Content:
Chapter 1 Pelletizing and Recycling of airborne dirt and dust from and to a Lead Glass Furnace (pages 1–8): Robert Hinkle, Jeffrey T. Lowry and Larry Tock
Chapter 2 Philosophy, ideas, and Implementation of constant development (pages 9–18): Chris Hamlin and Gordon Stewart
Chapter three Minimizing Glass Batch bills via Linear Programming (pages 19–24): D. W. Anderson
Chapter four Sulfate usage in go with the flow Glass construction (pages 25–42): W. B. Gibbs and Warren Turner
Chapter five Nonmetallic Liners in Batch dealing with gear (pages 43–49): J. H. Chaney, M. J. Newman and M. J. Pratko
Chapter 6 impression of power Codes at the Glass (pages 50–61): Merle F. Mcbride and Mark L. Bulger
Chapter 7 Recycling of Electrostatic Precipitator airborne dirt and dust from Glass Furnaces (pages 62–72): David T. Boothe, Harold Severin and Clint Braine
Chapter eight Refractory Recycling advancements (pages 73–77): John Noga
Chapter nine the applying of a Mass warmth Extractor to extend the Pull of a Forehearth (pages 78–89): Charles Henry Viel and G. M. Stanley
Chapter 10 the dept of Energy's learn and improvement software for the Glass production (pages 90–98): William A. Obenchain
Chapter eleven more advantageous box functionality via power Enhancement Coatings (pages 99–111): P. O. Austel and S. W. Carson
Chapter 12 fresh Air Act Amendments NOx Compliance Requirements—Glass (pages 112–117): Anthony J. Gallo
Chapter thirteen Oxy?Fuel Firing for Emissions keep watch over on a box Melter (pages 118–130): Carlos Herrera F. and Gabriel Noboa
Chapter 14 prestige record at the improvement of an Oxygen?Fuel?Fired Forehearth (pages 131–146): John T. Brown, William P. Coppin, Alan Stephens and Richard W. Marshall
Chapter 15 Minimization of NOx Emissions with better Oxy?Fuel Combustion: managed Pulsated Combustion (pages 147–158): Sophie Drogue, Shannon Breininger and Roberto Rurz
Chapter sixteen fresh Firing of Glass Furnaces by using Oxygen (pages 159–174): Prince B. Eleazer and Aleksandar G. Slavejkov
Chapter 17 issues and ends up in making use of Oxygen Firing to business Glass Melters (pages 175–185): William J. Snyder, Frederic N. Steigman and Abilio Tasca
Chapter 18 Conversion of a Fiberglass Furnace from a hundred% electrical Firing to Oxy?Fuel Combustion (pages 186–190): Daniel Ertl and Arlene Mcmahon
Chapter 19 A Partial Conversion of a Gas?Air?Fired tv Furnace to Oxy?Fuel Combustion (pages 191–195): Arlene McMahon and Maynard Ding

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Additional resources for A Collection of Papers Presented at the 54th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 15, Issue 2

Sample text

Summary The seed contents of float and container glasses are orders of magnitude apart. Float glass furnaces create a solubility gradient whereas container furnaces do not-this explains most of the difference in seed quality. Laboratory melts do not adequately model the process and therefore do not represent a method that can lead to experimental data to verify theory, or 41 to guide the furnace operator. The best prospect for predicting furnace behavior and seed quality is the careful sampling of the furnace itself.

4 Fig. 9. Seed distribution in float glass-quivalent (examination by point source light). 9 Fig. 10. Seed distribution in float glass-equivalent spherical diameter (examination by edge light). 0 G 1 . 9 SIZE INTERVAL (MM) POINT SOURCE EDGE LIGHT Fig. 11. Seed distribution in float glassequivalent spherical diameter. 15 I I 39 I I I I argue that over a large range of sulfate additions to batch, the seed quality of float glass is more a function of sulfate solubility than of sulfate availability.

Day, “A Computer Program for Optimizing Batch Calculations,” GZw Technol, 32 [4] (1991). 24 Ceramic Engineering and Science Proceedings David L. Wilcox & John Kieffer Copyright© 1994, by the American Ceramic Society Ceram. Eng. Sci. Proc. B. GIBBS PPG Industries Wichita Falls, TX 76307 WARREN TURNER Turner Process Research, Inc. Spring Church, PA 15686 The use of batch sulfate as a melting and fining agent is common to both the float glass and container industries. But, to satis- quality requirements, the float glass process must produce glass that is orders-of-magnitude better than needed for a container operation.

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A Collection of Papers Presented at the 54th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 15, Issue 2


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