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. 2019 Apr 1;11(4):154. doi: 10.3390/pharmaceutics11040154

Table 1.

Design of Experiment of the extrusion process and the resulted responses (for all runs the spheronisation process was constant with 9 min time, 75% speed and 15 g load).

Run Pattern Screw Design Screw Speed [rpm] Hopper Speed 1 [rpm] mc [%] Roundness Roughness py SD uy [%]
1 100 L1 200 260 23.87 3 2 0.08 91.62
2 1+− L1 300 250 23.86 3 4 1.19 91.18
3 1−− L1 100 250 23.79 2 4 0.41 86.62
4 1++ L1 300 270 21.70 3 2 0.23 95.79
5 100 L1 200 260 23.55 3 3 0.12 98.12
6 1−+ L1 100 270 21.39 3 2 0.23 97.53
7 200 L2 200 260 23.15 2 2 0.36 98.04
8 2−− L2 100 250 24.09 5 4 1.3 0
9 2+− L2 300 250 22.78 4 4 0.56 42.42
10 2++ L2 300 270 21.85 3 3 0.26 95.96
11 200 L2 200 260 22.12 3 2 0.65 97.49
12 2−+ L2 100 270 22.78 3 2 0.22 96.43

1 Hopper speed set to 250, 260 and 270 resulted in a feed rate of 5.8 g/min, 6.2 g/min and 6.6 g/min. mc = moisture content; py = process yield; uy = useable yield.