This quantity is a part of the Ceramic Engineering and technology continuing (CESP) series. This sequence features a selection 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 quarter of complicated ceramic comprise bioceramics, nanomaterials, composites, good oxide gas cells, mechanical houses and structural layout, complicated ceramic coatings, ceramic armor, porous ceramics, and more.
Chapter 1 a brand new method of Joint study 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, accomplished, and versatile (pages 9–18): Michael L. Newsom
Chapter three Glass Furnace HO, regulate 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 process (pages 47–54): Thomas okay. 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 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 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 types (pages 132–140): ok. T. Wu and M. ok. 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 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 procedure (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 info for A Collection of Papers Presented at the 56th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 17, Issue 2
For the furnace operation with air combustion (cm/s). 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.
3) over the glass surface. In Eq. 5 represents the friction velocity. Equation (3) can be interpreted as a mass transfer coefficient and an equilibrium driving force in the sense of the film theory of mass transfer. In this sense, the driving force is equal to the interfacial concentration, and the mass transfer coefficient is the premultiplier. (2). The mass transfer coefficient is determined by the local flow and transport properties as indicated in Eq. (3). ’o The equation for the partial pressure (in Torr) of the NaOH at the glass surface is shown below: A +B In(Ppp) = T By integrating the flux of NaOH into the combustion atmosphere for both the batch and melt volatilization mechanisms, we can estimate what effect the combustion atmosphere will have on the volatilization mechanism.
12J. Kim, and P. Moin, “Flow Structures Responsible for the Bursting Process,” Bull. Am. Phys. SOC. 31 (1986). S 46 Ceramic Engineering and Science Proceedings Gerald P. Wirtz Copyright © 1996 The American Ceramic Society Ceram. Eng. Sci. , 17  47-54 (1996) Demonstration on an Ultra-Low-NO, Oxygen-Fuel Class Meltins System THOMAS K. DANKERT Owens-Brockway Glass Container, Toledo, Ohio GEOFFREY B. , Tanytown, New York This paper discusses a joint development project of Owens-Bmckway and Praxair to produce low-NO,on the Owens-Bmckway LQS Angeles B furnace.
A Collection of Papers Presented at the 56th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 17, Issue 2