This quantity is a part of the Ceramic Engineering and technology continuing (CESP) series. This sequence includes a selection of papers facing concerns in either conventional ceramics (i.e., glass, whitewares, refractories, and porcelain the teeth) and complex ceramics. themes lined within the quarter of complex ceramic comprise bioceramics, nanomaterials, composites, strong oxide gas cells, mechanical homes and structural layout, complex ceramic coatings, ceramic armor, porous ceramics, and more.
Chapter 1 Is Your Glass filled with Water? – half II (pages 1–13): John T. Brown and Hisashi Kobayashi
Chapter 2 struggling with warmth Loss and Volatility: An Oxy?Gas Forehearth Conversion for Borosilicate Glass (pages 15–28): Ian D. Travis and Alan Stephens
Chapter three Optimization of Oxy?Fuel Combustion with Optical Sensors (pages 29–45): W. Von Drasek, E. Duchateau, L. Philippe and R. Grosman
Chapter four An Oxy?Gas Furnace for Lead Crystal Glass Melting (pages 47–51): Jerry Kynik
Chapter five research of Liquid touch Refractory Corrosion below Oxy?Fuel Glass Melting Atmospheres (pages 53–73): S. M. Winder, A. Gupta and ok. R. Selkregg
Chapter 6 decision of Corrosion components in Glass Furnaces (pages 75–88): C. A. Paskocimas, E. R. Leite, E. Longo, W. Kobayashi, M. Zorrozua and J. A. Varela
Chapter 7 taking a look past the “Oxy?Fuel concerns for Glassmaking within the '90s” Workshop (pages 89–98): C. Philip Ross
Chapter eight know-how Priorities: result of the Glass know-how Roadmap Workshop (pages 99–110): Theodore Johnson
Chapter nine technique development via Statistical keep an eye on (pages 111–126): James C. Eckhart
Chapter 10 complex keep an eye on of Glass Tanks utilizing Simulation types and Fuzzy keep an eye on (pages 127–135): H. P. H. Muysenberg, R. A. Bauer and E. G. J. Peters
Chapter eleven Superstructure Corrosion in Glass Tanks: comparability of Mathematical version with box Measurements (pages 137–143): Mahendra okay. Misra, Stephen S. C. Tong and John T. Brown
Chapter 12 Rapidox: a brand new instrument for Redox Measurements in Glass Samples (pages 145–158): J. Plessers, P. Laimbock, A. J. Faber and T. Tonthat
Chapter thirteen Low?Cost Stirrer actual Modeling in Quarter?Scale (pages 159–165): Robert R. Thomas
Chapter 14 business adventure with a brand new Cruci?Form resolution for Regenerator Plugging (pages 167–180): J. J. Fillot, A. Zanoli, Y. Boussant?Roux and O. Citti
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This quantity is a part of the Ceramic Engineering and technological know-how continuing (CESP) series. This sequence includes a choice of papers facing concerns in either conventional ceramics (i. e. , glass, whitewares, refractories, and porcelain teeth) and complex ceramics. themes coated within the region of complicated ceramic contain bioceramics, nanomaterials, composites, good oxide gasoline cells, mechanical homes and structural layout, complicated ceramic coatings, ceramic armor, porous ceramics, and extra.
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Additional resources for A Collection of Papers Presented at the 58th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 19, Issue 1
2, where the amount of excess 0, in the flue (dry basis) for a small change in excess oxidant in the oxy-fuel process is nine times greater than for air combustion. Typically, two approaches have been used for optimal tuning of the process. First, the global stoichiometry can be controlled by performing an oxygen concentration measurement in the stack. This approach introduces long response times to the control strategy because of the process volume and the measurement location (stack) relative to the source (burner).
19 [l I (1998) 0 5 10 15 20 Excess Oxidant (%1 Figure 2. Comparison of oxygen and air for oxidant flow control. optical sensors integrated into an oxy-fuel burner. The information obtained from the sensors can then be used for stoichiometry and firing rate monitoring and control of the burners' performance. The concept offers a number of advantages such as fast response time, point-of-use monitoring, and safety monitoring. Here we present the sensor concept and results obtained in a 2 MMBtuh pilot furnace and an industrial glass melting furnace.
12, which shows a series of stoichiometry calibrations that were conducted over a range of burner firing rates. If the firing rate is known, one simply needs to select the appropriate curve from Fig. 12 to determine the stoichiometry. For monitoring andor control the firing rate must by determined by an alternative means that is not influenced by the stoichiometry. The procedure outlined above will not 40 Germ. Eng. Sci. , 19 [l I (1998) 1 i? 95 $! 2 OxygenlFuel Ratio Figure I I. Normalized calibration curves comparing the sensitivity for detecting stoichiometric changes.
A Collection of Papers Presented at the 58th Conference on Glass Problems: Ceramic Engineering and Science Proceedings, Volume 19, Issue 1