This quantity is a part of the Ceramic Engineering and technological know-how continuing (CESP) series. This sequence includes a choice of papers facing matters in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complicated ceramics. issues coated within the region of complex ceramic comprise bioceramics, nanomaterials, composites, reliable oxide gas cells, mechanical homes and structural layout, complex ceramic coatings, ceramic armor, porous ceramics, and more.
Chapter 1 a brand new method of Joint study and improvement: picking out the opportunity of a Partnership among the Glass and the government (pages 1–8): Susanne R. Leonard
Chapter 2 identify V allows within the Glass undefined: Making Them uncomplicated, accomplished, and versatile (pages 9–18): Michael L. Newsom
Chapter three Glass Furnace HO, keep watch over with fuel 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 type Meltins method (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 construction of High?Quality classification (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 evaluate 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 purposes (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 choked with Water? (pages 170–179): John T. Brown and Hisashi Kobayashi
Chapter 20 Corrosion of Silica and Mullite Refractories utilized in Glass Furnaces lower 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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Extra resources for A Collection of Papers Presented at the 56th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 17, Issue 2
The upper component is the J burner, which supplies the natural gas and a portion of the oxygen. The lower component is the L lance, which supplies the remaining oxygen. The flexible hose entering the side of the L lance is the low-pressure cooling air from the side wall cooling system. Cooling air is needed if oxygen flow stops. The upper J burner is mounted into the furnace breast wall at a 2" angle; the lance is about 12 in. below the J burner and is mounted at a 6" angle. The burner separation helps achieve slower oxygen-fuel mixing for better luminosity and lower peak flame temperatures.
Traditional Control Techniques The first step to control particulate emissions form air-fuel furnaces is to implement process modifications as described in Ref. 2. These include reducing furnace temperature, increasing cullet ratio, decreasing excess air, preheating the batch, adding electric boost, and modifying the furnace design. When these modifications do not meet the limits, flue gas treatment such as baghouses and electrostatic precipitators are implemented. These flue gas treatment technologies are well-acceptedand have been successful.
At the high temperatures in the combustion chamber (>2300"F), it is likely that Na2S04 would not exist as a single species4 in the gas phase but would decompose in the gas phase to SO2 and a sodium species. The sodium species are primarily NaOH, sodium (a relatively small component), or NaCI. The most predominant of these species is NaOH. The appearance of NaCl obviously is a strong function of the amount of chlorine that is in the batch material. Figure 1 shows the vapor pressure curves for these three sodium-containing elements.