| 000 | 01590nam a2200253Ia 4500 | ||
|---|---|---|---|
| 003 | MX-MdCICY | ||
| 005 | 20250625153923.0 | ||
| 040 | _cCICY | ||
| 090 | _aB-13453 | ||
| 245 | 1 | 0 | _aScale-up of a pharmaceutical granulation in fixed bowl mixer-granulators |
| 490 | 0 | _vInternational Journal of Pharmaceutics, 133(1-2), p.127-131, 1996 | |
| 520 | 3 | _aScale-up in fixed bowl mixer-granulators has been studied by applying the classical dimensionless numbers of Power, Reynolds and Froude to end-point prediction in a range of geometrically similar machines. The simple relationship of Power number/Reynolds number, as suggested by previous workers, has been found to be nappropriate for large-scale production machines where corrections have to be made for gross vortexing and powder bed height variation by the incorporation of the Froude number and a scaling factor. When corrections are made, data from 25-, 100- and 600-1 machines all fall on the same curve allowing predictions of optimum granulation end-point conditions to be made for production-scale equipment from measurements on laboratory-scale equipment and vice-versa. | |
| 650 | 1 | 4 | _aGRANULATION |
| 650 | 1 | 4 | _aMIXER GRANULATORS |
| 650 | 1 | 4 | _aSCALE-UP |
| 700 | 1 | 2 | _aLandin, M. |
| 700 | 1 | 2 | _aYork, P. |
| 700 | 1 | 2 | _aCliff, M.J. |
| 700 | 1 | 2 | _aRowe, R.C. |
| 700 | 1 | 2 | _aWigmore, A.J. |
| 856 | 4 | 0 |
_uhttps://drive.google.com/file/d/1vvguDzaJTI19g8n1JPJrhEwPVrF3zQIf/view?usp=drivesdk _zPara ver el documento ingresa a Google con tu cuenta: @cicy.edu.mx |
| 942 |
_2Loc _cREF1 |
||
| 008 | 250602s9999 xx |||||s2 |||| ||und|d | ||
| 999 |
_c47653 _d47653 |
||