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Continuous rotary kiln calcination of YBaCuO precursor powders
A bench rotary kiln was used to produce pure YBa sub(2)Cu sub(3)O sub(6+x) by continuous calcination of spray-roasted precursor powder using a countercurrent air flow to avoid a reaction between evolved CO sub(2) and the product. Product agglomeration caused a spread in the velocity distribution, re...
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Published in: | Industrial & engineering chemistry research 1994-02, Vol.33 (2), p.421-427 |
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Main Authors: | , , , , |
Format: | Article |
Language: | English |
Subjects: | |
Online Access: | Get full text |
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Summary: | A bench rotary kiln was used to produce pure YBa sub(2)Cu sub(3)O sub(6+x) by continuous calcination of spray-roasted precursor powder using a countercurrent air flow to avoid a reaction between evolved CO sub(2) and the product. Product agglomeration caused a spread in the velocity distribution, requiring the use of extra calcination for a pure product. High-purity YBa sub(2)Cu sub(3)O sub(6.6) was obtained at 940 degree C for 0.9 vol% solid loading, an average residence time of 75 min, and N theta (N identical with rotation rate, theta identical with inclination) between 3 and 4.5 rpm deg. However, at a residence time of 77 min, increased product agglomeration at 2.5 rpm deg caused incomplete conversion to YBa sub(2)Cu sub(3)O sub(6.6). Increasing the average residence time above 75 min increased the oxygen content of the product, with pure orthorhombic YBa sub(2)Cu sub(3)O sub(6.9) forming at 160 min. Due to reaction and temperature induced changes in particle size and shape, existing correlations cannot predict the dependence of the average solid residence time on the operating conditions. |
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ISSN: | 0888-5885 1520-5045 |
DOI: | 10.1021/ie00026a038 |