This quantity is a part of the Ceramic Engineering and technology continuing (CESP) series. This sequence features a number of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complex ceramics. themes coated within the zone of complex ceramic contain bioceramics, nanomaterials, composites, reliable oxide gasoline cells, mechanical houses and structural layout, complicated ceramic coatings, ceramic armor, porous ceramics, and more.
Chapter 1 a brand new method of Joint examine and improvement: selecting the potential of a Partnership among the Glass and the government (pages 1–8): Susanne R. Leonard
Chapter 2 name V allows within the Glass undefined: Making Them easy, complete, and versatile (pages 9–18): Michael L. Newsom
Chapter three Glass Furnace HO, keep watch over with gasoline Reburn (pages 19–35): Richard Koppang, David Moyeda and Lesley Donaldson
Chapter four Particulate Emissions in Oxy?Fuel Fired Glass Furnaces (pages 36–46): Benjamin Jurcik, Louis Philippe, Steve Wayman and Roberto Ruiz
Chapter five Demonstration on an Ultra?Low?NO, Oxygen?Fuel classification Meltins approach (pages 47–54): Thomas ok. Dankert and Geoffrey B. Tuson
Chapter 6 Volatilization in the course of Thermal Plasma Processing of Glass Melts Containing Heavy Metals (pages 55–61): Jeffrey W. wooden, David G. Cahill, Rebecca Cortez, Larry D. Stephenson and Hany H. Zaghloul
Chapter 7 Glass box Reuse: Refillables carry chance for Glass (pages 62–70): Michael Lewis
Chapter eight Use of Zinc Selenite in Glass Manufacture (pages 71–77): Charles Merivale
Chapter nine Segregation impacts Glass caliber (pages 78–83): David Stuart?Dick
Chapter 10 Submersed Combustion Furnace for Glass Melts (pages 84–92): Vladimir M. Olabin, Leonard S. Pioro, Alexander B. Maximuk, Mark J. Khinkis and Hamid A. Abbasi
Chapter eleven Thermal Efficiencies of flow and box Furnaces (pages 93–102): Warren Turner
Chapter 12 Lift?Out Rolls and Lehr Rolls for creation of High?Quality type (pages 103–111): D. Bucko, J. M. Vignot, P. Guillo, D. Gautier, Y. Takahashi and S. Inoue
Chapter thirteen Ongoing research of Oxy?Fuel Firing influence on Corrosion of Nonglass touch Refractories, half 2 (pages 112–120): A. Gupta and S. M. Winder
Chapter 14 Model?Based review of Oxy?Fuel Glass?Melting Furnace functionality (pages 121–131): M. G. Carvalho and M. Nogueira
Chapter 15 layout Modeling of Glass Furnace OXY?Fuel Conversion utilizing Three?Dimensional Combustion versions (pages 132–140): ok. T. Wu and M. okay. Misra
Chapter sixteen warmth move Optimization in television Glass Furnaces (pages 141–151): William J. Horan, Aleksandar G. Slavejkov and Leon L. Chang
Chapter 17 High?Performance Oxy?Fuel Melting: 3 Flat Jet Burner functions (pages 152–161): Carl Schatz
Chapter 18 Oxy?Fuel Economics replace in keeping with Case Histories (pages 162–169): Ronald W. Schroeder and Allan E. Zak
Chapter 19 Is Your category jam-packed with Water? (pages 170–179): John T. Brown and Hisashi Kobayashi
Chapter 20 Corrosion of Silica and Mullite Refractories utilized in Glass Furnaces less than a hundred% Oxy?Firing method (pages 180–188): J. Boillet, W. Kobillet, W. J. Snyder, C. A. Paskocimas, E. R. Leite, E. Longo and J. A. Varela
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Additional resources for A Collection of Papers Presented at the 56th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 17, Issue 2
10 - 9- a1- i :I B 4- 3- '1 2- 0 0 , 1 1 2 1 3 1 4 Fmaw Width [m] 1 S 1 6 1 1 Figure 5. Contours of V. for the furnace Wlth oxy combustion (cm/s). 5 1 25,000 I . 30,000 . . I , 35,000 , . ' I " ' I . 40,000 45,000 Volatilization Antoine's Constant . . 50 100 Figure 6. Ratio of volatilization metric for various values of the parameter A In Eq. (5). E - 25 20 0 5 15 3a 5 x 5 % r h 10 5 0 10 Particle Radius (microns) Figure 7. Area over which physical resuspenslon can occur as functlon of particle radius from Eq.
The decision to build an oxy-fuel furnace at the Owens-Brockway Los Angeles plant was influenced by the need to meet increasingly stringent air quality requirements in the Southern California area. The Los Angeles B furnace was built as a 93 m2 (lo00 ft2) melter. It was designed to include 12 burners (six on each side). The first pair of burners, which are closest to the charge end wall, are directly opposed. The remaining burners are staggered from side to side. All burners have the same maximum-rated capacities of 184 m3h (6500 ft3h) natural gas and 408 m3h (14 400 ft%) for 90% purity oxygen.
Experimental results for reburning wlth agent injectlon in reburning zone. 5. (a) influence of agent injection temperature, burnout air Injected a t 785°C; ( b ) influence of burnout alr injection temperature, agent Injection temperature = 900°C. 5' r nlric Nozzle Figure 6. Reburn and overflre air nozzle arrangements. 90 Design Point Melter Side Regenerator Side Figure 7. Isothermal subscale model reburn fuel flow visualization and delstrlbution map (plotted as local stolchlometry). has reduced mixing effectiveness if injected through the primary burners.
A Collection of Papers Presented at the 56th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 17, Issue 2