Modeling of Advanced Melting Zone for Manufacturing of Optical Fibers

Optical fibers are drawn from preforms (fused silica glass rods) typically made up of two concentric cylinders (the core rod and the clad tube), which are usually joined in a separate fusion process. The setup time and hence manufacturing cost can be significantly reduced if the two cylinders can be joined in the same furnace in which the fiber is drawn. A good understanding of the transient temperature distribution is needed for controlling the feed rate to avoid thermally induced cracks. Since direct measurement of the temperature fields is often impossible, the geometrical design of the preform and the control of the feed rate have largely been accomplished by trials-and-errors. The ability to predict the transient temperature distribution and the thermally induced stresses will provide a rational basis to design optimization and feed rate control of the process In this paper, we present an analytical model to predict the transient conductive-radiative transfer as two partially, joined, concentric glass cylinders with specular surfaces are fed into the furnace. Finite volume method (FVM) is used to solve the radiative transfer equation (RTE). The specular surface reflectivity is obtained by the Fresnel's law and the Snell's law. The boundary intensities are obtained through the coupling of the interior glass radiative transfer and the exterior furnace enclosure analysis. The model has been used to numerically study the transient conductive-radiative transfer in the advanced melting zone (AMZ) of an optic fiber drawing process. This problem is of both theoretical and practical interest in the manufacture of optical fibers. The computational method for the radiation transfer developed in this paper can also be applied to the simulation of the fiber drawing process and other glass-related manufacturing processes.

[1]  A. Kesten RADIANT HEAT FLUX DISTRIBUTION IN A CYLINDRICALLY-SYMMETRIC NONISOTHERMAL GAS WITH TEMPERATURE-DEPENDENT ABSORPTION COEFFICIENT , 1968 .

[2]  Kyong Sei Lee,et al.  Effects of Radiative Transfer Modeling on Transient Temperature Distribution in Semitransparent Glass Rod , 2003 .

[3]  Philip J. Smith,et al.  Predicting Radiative Transfer in Axisymmetric Cylindrical Enclosures Using the Discrete Ordinates Method , 1988 .

[4]  A computational method for generating the free-surface neck-down profile for glass flow in optical fiber drawing , 1999 .

[5]  B. N. Raghunandan,et al.  Prediction of radiative transfer from potential core of a hot jet , 1994 .

[6]  S. Baek,et al.  MODIFICATION OF THE DISCRETE-ORDINATES METHOD IN AN AXISYMMETRIC CYLINDRICAL GEOMETRY , 1997 .

[7]  E. E. Anderson,et al.  Heat Transfer in Semitransparent Solids , 1975 .

[8]  M. Modest Radiative heat transfer , 1993 .

[9]  Y. S. Touloukian,et al.  Thermal radiative properties: Nonmetallic solids. , 1972 .

[10]  R. Pletcher,et al.  Computational Fluid Mechanics and Heat Transfer. By D. A ANDERSON, J. C. TANNEHILL and R. H. PLETCHER. Hemisphere, 1984. 599 pp. $39.95. , 1986, Journal of Fluid Mechanics.

[11]  Matthew R. Myers,et al.  A model for unsteady analysis of preform drawing , 1989 .

[12]  U. C. Paek,et al.  Physical behavior of the neck-down region during furnace drawing of silica fibers (A) , 1977 .

[13]  Prediction of radiative transfer in general body-fitted coordinates , 1997 .

[14]  S. Patankar,et al.  Finite volume method for radiation heat transfer , 1994 .

[15]  R. Siegel,et al.  Effect of Index of Refraction on Radiation Characteristics in a Heated Absorbing, Emitting, and Scattering Layer , 1992 .

[16]  Y. Jaluria,et al.  Zonal Method to Model Radiative Transport in an Optical Fiber Drawing Furnace , 1997 .