EFFECT OF GLIDANT ADDITION ON FLOWABILITY OF SOLIDS 495 reduction in surface rugosity will minimise the mechanical interlocking of the particle and thereby reduce the rolling friction. This would be parti- cularly relevant when flow improvement is caused by the addition of material of similar chemical constitution to the original granulation. Secondly, the added material may possess a coefficient of friction which is lower than that of the bulk solid to which it is added and therefore decrease interparticle friction. It has been suggested that the glidants which possess laminar crystalline forms, e.g. talc, graphite, roll up under low shear stresses to produce a 'ball bearing type' action (20). In addition, it may be that some substances are acting as boundary lubricants between the particles but it is considered that the low shear stresses involved in most handling processes do not seem great enough to place too much emphasis on this mechanism. Separation effects Although glidants may possess a minute crystallite size (of the order of several nm) on addition to bulk which the individual particles may become aggregated (sizes up to several [tm) (2). The aggregates increase the interparticulate distances of the coarse material and may reduce the forces of attraction between the surface asperities. This is also the case for fine material added to coarse material of similar chemical constitution but under these conditions the separation is much greater. Thus, during the gravity discharge of a bulk solid from a hopper, the points of slippage in a free fall arch over the orifice are increased by the interposition of the fine particles and flow may be increased (21). Many of the glidants used are also flow conditioning or anticaking agents, e.g. calcium phosphate, silico aluminates. The physical separation of the coarse particles which is produced when these materials adhere to their surfaces is thought to reduce the action of capillary adhesion forces and also prevent the formation of solid bridges between particles (22, 23). This is of importance where bin residence time is prolonged or the formulation subjected to a variable environment. The particle size of the added material is important since it is the ability of the additive to coat the surface of the coarse material that determines its efficiency (2, 19). The combination of both frictional and separation effects should therefore produce a useful improvement in flowability and this can be demonstrated by the improvement in flow produced on the addition of fines and talc to a tablet granulation {8).
496 JOURNAL OF THE SOCIETY OF COSMETIC CHEMISTS Antistatic effects Many powders acquire a static charge during their handling and it has been shown that the addition of løfo or more of magnesium stearate, polyethylene glycol 4 000 or talc effectively lowers the accumulation of static charge in a number of pharmaceutical formulations (24). (Received.' 2nd January 19( 9) REFERENCES (1) Strickland, V• •. A. Jnr. Drug Cosmetic Ind. 8õ 318 (1959). (2) Augsberger, L. L. and Shangraw, R. F..[. Phar•n. $ci. õõ 418 (1966). (3) Harwood, C. F. and Pilpel, N. Lab. Pract. 17, 1236 (1068). (4) Tawashi, yon R. Pharmazeutische Technologie, 2 64 (1063). (5) Gold, G., Duvall, R. N., Palermo, B. T. and Slater, J. G. J. Pharm. Sci. õõ 1201 (1966). (6) Craik, D. J. and Miller, B. F. J. Pharm. Pharmacol. 10 136T (1958). (7) Gold, G., Duvall, R. N., Palermo, B. T. and Slater, J. G. J. Pharm. Sci., õ,1 667 (1968). (8) Hammerness, F. C. and Thompson, H. O. J. Am. Pharm. Assoc. Sci. Ed. 4'1 58 (1958). (0) Jones, T. M. Mfg. Chemist 30 38 (March 1068). (10) Hansen, G. Arch. Pharm. Chemi. 01 632 (1954). (11) Bulsara, P. U., Zenz, F. A. and Eckert, R. A. IEC Proc. Des. and Der. 3 348 (1964). (12) Jones, T. M. and Pilpel, N.J. Pharm. Phar•nacol. 18 429 (1966). (13) Sumner, E. D., Thompson, H. O., Poole, W. K. and Grizzle, J. E. J. Pharm. Sci. õ5 1441 (1966). (14) Tucker, S. J. and Hays, H. M. J. Am. Pharm. Assoc. Sci. Ed. 48 362 (1959). (15) Farley, R. and Valentin, F. H. H. Powder Technol. I 344 (1967/68). (16) HawksIcy, P. G .W. Inst. Fuel Conf. on Pulv. Fuel 656 (1947). (17) Shotton, E. and Simons, F. M. J. Pharm. Pharmacol. 2 231 (1950). (18) Davis, H. Pharm. J. 150 118 (1943). (19) Irani, R. R. and Callis, C. F. Particle Size Measurement, Interpretation and Application 3 (1963). (John Wiley, N.Y.). (20) Train, D. and Hersey, J. A. J. Pharm. Pharmacol. 12 97T (1960). (21) Jones, T. M. J. Pharm. Sci. 57 2015 (1968). (22) Hardesty, J. O. and Kumagai, R. Agr. Chem. 7 (2) 38 (1952). (23) Whynes, A. L. and Dee, T. P. J. Sci. Food Agr. 8 577 (1957). (24) Gold, G. and Palermo, B. T. J. Pharm. Sci. 54 1517 (1965). (25) Rose, H. E. and Tanaka, T. Engineer, 208 465 (1959). (26) Burak, N. Chem. Ind. London 844. (1966). (27) Jones, T. M. and Pilpel, N.J. Pharm. Pharmacol. 17 440 (1965). (28) Jones, T. M. Ph.D. thesis University of London (1967). (29) Smalley, I. J., Hearer, A. A. and McGrath, L. Trans. Inst. Mining Met. (Sect. C Mineral Process Extr. Met.) 76 183 (1967). (30) Harwood, C. F. and Pilpel, N. Chem. Process Eng. 49 92 (July 1968). (31) Segovia, E. Acta Pharm. Suecica, 4 171 (1967). (32) Kaneniwa, N., Ikekawa, A. and Aoki, H. Chem. Pharm. Bull. 15 1441 (1967). (33) Egrova, V. I. Med. Prom. SSSR. 20 (11) 47 (1966). (34) Brown, R. L. S.C.oe. Monograph No. 14 150 (1961). (35) Nelson, E. J. Am. Pharm. Assoc. Sci. Ed. 44 435 (1955). (36) Gstirner, F. and Pick, C. Arch. Pharm. 300 757 (1967). (37) Czetsch Lindenwald, H. v. E1 Khawas, F. and Tawashi, R. J. Soc. Cosmetic Chemists, 16 251 (1965).
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