Conclusions
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1.
In the given setup the drying process is very intensive and ensures a moisture removal rate of 70 kg/m2 · h in the case of norsulfazole and 50kg/m2 · h in the case of pyramidon.
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2.
Compared with tray-type driers the duration of the process is reduced by a factor of 100 or more (2–3 min instead of 5–10 h).
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3.
The optimum process variables for the preparations studied have been found. Thus, in the case of pyramidon the air temperature should be 90° and its mass flow rate 0.7–0.5 kg/m2· h, and in the case of norsulfazone the air temperature should be 140° and the mass flow rate 0.8 kg/m2 · h. The corresponding height of the stationary layer of material should be 40–50 mm.
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4.
In the case of pyramidon drying should be continued to an equilibrium moisture content of 0.4%, and in the case of norsulfazone to a moisture content of 1.5–1.0%. If these levels are adhered to the tablets produced scarcely ever undergo compaction during storage.
In this drying setup product carry-over is insignificant.
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Translated from Khimiko-Farmatsevticheskii Zhurnal, No. 8, pp. 51–54, August, 1968.
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Reprintseva, S.M., Chizhik, K.G. Setup for granulating and drying tabletted preparations. Pharm Chem J 2, 461–464 (1968). https://doi.org/10.1007/BF00759403
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DOI: https://doi.org/10.1007/BF00759403