By III Charles H. Drummond
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Extra resources for 61st Conference on Glass Problems
Gas velocity: Scale-up economics depend strongly on the operating gas velocities in the interior channels of the module. Gas flow rates 9 47 Figure 7. Flow diagram of E-Batch pilot test facility. through a single channel of up to 350 scfm (595 m3/h) were achieved before incipience of batch entrainment. Heat transfer rate: Conventional convective heat transfer rates from gases to solid surfaces are in the range of 2 4 Btu/h/ft2/"F (12-24 J/s/m2/"C). Measured heat transfer rates of the test device were typically 15-20 Btu/h/ft2/"F (90-120 J/s/m2/"C).
J. Klouzek, Determination of the equilibrium partial pressures of sulphur dioxide and oxygen in float glass melt, 111. International seminar on mathematical simulation in glass melting, 1995, Horni Becva, Czech Republic. 19 Application of the Fining Shelf to Furnace Melting Technology Ruediger Nebel Nikolaus Sorg GmbH & Co. KG, Lohr am Main, Germany Introduction The glass melting process can be divided into a number of partial processes, such as initial reaction, melting, refining, homogenization, and conditioning.
Each tube was of design identical to that anticipated for full-scale units. As such the pilot program results should be a valid predictor of performance of full-scale installations. Furthermore, it was desired to use a full-scale tube design to test issues of tube surface fouling, material flow, thermal expansion, high-voltage parameters, and so on. Operational Results The testing program consisted of an 11-day continuous run of the E-Batch system. Many key operational features were demonstrated.
61st Conference on Glass Problems by III Charles H. Drummond