This quantity is a part of the Ceramic Engineering and technological know-how continuing (CESP) series. This sequence incorporates a number of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complicated ceramics. subject matters coated within the region of complex ceramic comprise bioceramics, nanomaterials, composites, reliable oxide gasoline cells, mechanical homes and structural layout, complicated ceramic coatings, ceramic armor, porous ceramics, and more.
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 continuing development (pages 9–18): Chris Hamlin and Gordon Stewart
Chapter three Minimizing Glass Batch expenditures via Linear Programming (pages 19–24): D. W. Anderson
Chapter four Sulfate usage in glide 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 influence 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 appliance 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 dep. of Energy's study and improvement application for the Glass production (pages 90–98): William A. Obenchain
Chapter eleven more advantageous box functionality via energy 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 an eye on on a box Melter (pages 118–130): Carlos Herrera F. and Gabriel Noboa
Chapter 14 prestige file 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 enhanced Oxy?Fuel Combustion: managed Pulsated Combustion (pages 147–158): Sophie Drogue, Shannon Breininger and Roberto Rurz
Chapter sixteen fresh Firing of Glass Furnaces by utilizing 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
Read Online or Download A Collection of Papers Presented at the 54th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 15, Issue 2 PDF
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Additional info for A Collection of Papers Presented at the 54th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 15, Issue 2
The current range used in modern float furnaces is less than 10 lb. The operating practice that was developed was to manipulate the furnaces in such a way as to make sulfate solubility work for us. That means that the firing was adjusted to be more oxidized in the early ports in order to maximize the dissolution of sulfate into the melt. This effort could be augmented by addition of an oxidant, such as NaN03, but such additions failed to provide consistent desired results. Niter could also increase NO, emissions.
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. The furnaces examined in this study had pull rates from 420 to 650 tpd with cullet fraction (on charge weight) of 2849%.
Our cash reserves and lines of credit were depleted to the point that we had t o live on our cash flow. There was no opportunity to use capital to buy productivity improvements. Many outsiders had written the company off as lost. 9 Fortunately, crisis brings out capabilities in people and organizations that go far beyond normal expectations. Confronted with the likelihood of finan- cial collapse, the company's leadership laid out an aggressive recovery plan. The plan's foundation was based upon our employees and the ideal of quality.