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Reduction of OH− ions in tellurite glasses using chlorine and oxygen gases

Published online by Cambridge University Press:  25 November 2013

Purushottam Joshi*
Affiliation:
Department of Mechanical and Manufacturing Engineering (MME), M. S. Ramaiah School of Advanced Studies, Bengaluru 560 058, India
Billy Richards
Affiliation:
Institute for Materials Research, School of Process, Environmental and Materials Engineering, The University of Leeds, Leeds LS2 9JT, United Kingdom
Animesh Jha
Affiliation:
Institute for Materials Research, School of Process, Environmental and Materials Engineering, The University of Leeds, Leeds LS2 9JT, United Kingdom
*
a) Address all correspondence to this author. e-mail: joshi.purushottam@gmail.com

Abstract

Absorption losses in tellurite glasses due to OH− ions were reduced by melting the glasses under a reactive atmosphere of Cl2 + O2 gas. Incorporation of dry Cl2 + O2 gas has a major influence on the reduction of OH− species, which is found to be consistent with thermochemical data. Absorption loss due to OH− ions in bulk glasses prepared from the as-received raw materials and processed under a reactive atmosphere was 1000 and 60 dB/m, respectively. Gaussian fits have been used to identify the different species of OH− attached to the structural units present in the glass. All of the OH− species (free and bonded to Te), units can be reduced by melting the starting raw materials in a reactive atmosphere of Cl2 + O2. The net reduction in OH− absorbance at 3.2 µm was 1.1 cm−1, which is equivalent to 500 ppm. OH− reduction in tellurite glasses using O2 gas bubbling shows a reduction in the fundamental absorption band from 1.8 to 0.57 cm−1 after 75 min.

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Articles
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Copyright © Materials Research Society 2013 
Figure 0

FIG. 1. Gibbs free energy as a function of temperature.

Figure 1

FIG. 2. Comparison of the equilibrium partial pressures (log (pi, atm)) against temperature for gaseous species in the system.

Figure 2

FIG. 3. Setup for purification of raw materials.

Figure 3

FIG. 4. Classification of OH− peaks using infrared absorption spectroscopy of 80TeO2–10Na2O–10ZnO glass.18

Figure 4

TABLE I. Molar extinction coefficient of OH− in various glass hosts.20

Figure 5

TABLE II. Position (P) cm−1, FWHM (W) cm−1, and areas (A) (cm−1)2 of OH− groups for 80TeO2–10Na2O–10ZnO glass before purification.

Figure 6

TABLE III. OH− groups for 80TeO2–10Na2O–10ZnO glass before purification.

Figure 7

FIG. 5. The Gaussian deconvolution of the OH− absorption bands in 80TeO2–10Na2O–10ZnO (mol%) glass.

Figure 8

TABLE IV. Position (P) cm−1, FWHM (W) cm−1, and areas (A) (cm−1)2 of OH− groups in glass samples purified at different temperatures.

Figure 9

TABLE V. Position (P) cm−1, FWHM (W) cm−1, and areas (A) (cm−1)2 of OH− groups in a glass sample purified at 623 K with different melting conditions.

Figure 10

FIG. 6. Infrared absorption spectra of 80TeO2–10Na2O–10ZnO glasses for different drying temperatures.

Figure 11

FIG. 7. Infrared absorption spectra of 80TeO2–10Na2O–10ZnO glasses for different melting conditions.

Figure 12

TABLE VI. Assignment of absorption bands.

Figure 13

FIG. 8. Infrared absorption spectra of 80TeO2–10ZnO–Na2O glass with different O2 bubbling durations. The inset graph shows the trend of absorption coefficient reduction of the OH− bands at 3000 and 2300 cm−1 with total O2 bubbling duration.