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 complicated ceramics. issues coated within the sector of complex ceramic contain bioceramics, nanomaterials, composites, strong oxide gasoline cells, mechanical homes and structural layout, complicated ceramic coatings, ceramic armor, porous ceramics, and more.
Content:
Chapter 1 a brand new method of Joint examine and improvement: choosing 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 basic, entire, and versatile (pages 9–18): Michael L. Newsom
Chapter three Glass Furnace HO, keep an eye on 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 category Meltins procedure (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 waft and box Furnaces (pages 93–102): Warren Turner
Chapter 12 Lift?Out Rolls and Lehr Rolls for creation of High?Quality category (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 effect on Corrosion of Nonglass touch Refractories, half 2 (pages 112–120): A. Gupta and S. M. Winder
Chapter 14 Model?Based overview 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): okay. 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 response to Case Histories (pages 162–169): Ronald W. Schroeder and Allan E. Zak
Chapter 19 Is Your category choked 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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Extra resources for A Collection of Papers Presented at the 56th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 17, Issue 2
Example text
General furnace design and operating standards and evaluation of pollutant emissions, energy and oxygen consumption, and glass quality also are presented. Discussion A full-scale field demonstration experimental R&D program was conducted at OwensBrockway's Los Angeles plant to evaluate the performance of a commercial container glass furnace fired with low-NO, oxy-fuel burners. The main goal of this project was to measure the NO, per ton of glass manufactured while operating the melter under realistic glass furnace production conditions using oxygen supplied from a vacuum pressure swing adsorbtion plant.
The furnace's design specifications followed many of Owens-Brockway standards for furnace design to meet our current standards for furnace life, furnace energy, and glass quality. 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).
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. Some redesign of the existing fuel nozzles will be required for good mixing, such as concentric high-velocity nozzles, flue gas blending, or additional nozzles on the port side or top walls.