Table 1.
Extrusion conditions | Chemical composition | |||||||
---|---|---|---|---|---|---|---|---|
Cyanogenic compounds (mg/kg) | Tannin (mg/100 g) | Mucilage (g/100 g) | Oil yield (g/100 g) | Fatty acids | ||||
Oleic (% of TFA) | Linoleic (% of TFA) | α-Linolenic (% of TFA) | ||||||
Barrel exit temperature (°C) | 100 | 52.3 ± 0.4e | 59.3 ± 0.6e | 7.6 ± 0.2c | 31.6 ± 0.1b | 18.6 ± 0.1a | 11.4 ± 0.2a | 47.7 ± 0.4a |
120 | 45.1 ± 0.5f | 51.4 ± 0.6h | 7.1 ± 0.2f | 30.2 ± 0.2c | 18.8 ± 0.2a | 11.3 ± 0.1a | 47.1 ± 0.5a | |
140 | 31.5 ± 0.6h | 39.2 ± 0.5j | 6.5 ± 0.2h | 29.8 ± 0.2c | 19.1 ± 0.1a | 11.1 ± 0.2a | 46.6 ± 0.6a | |
Screw speed (rpm) | 50 | 70.5 ± 0.5a | 74.8 ± 0.4a | 7.3 ± 0.3e | 31.3 ± 0.2b | 19.0 ± 0.2a | 11.4 ± 0.2a | 49.0 ± 0.6a |
100 | 52.9 ± 0.4e | 53.1 ± 0.6g | 7.5 ± 0.3c | 29.0 ± 0.1d | 18.7 ± 0.2 a | 11.5 ± 0.2a | 48.3 ± 0.5a | |
150 | 61.8 ± 0.5c | 64.9 ± 0.7c | 7.9 ± 0.2a | 31.5 ± 0.1b | 18.4 ± 0.1a | 11.7 ± 0.1a | 49.1 ± 0.5a | |
Feed rate (kg/h) | 30 | 59.0 ± 0.5d | 61.9 ± 0.7d | 7.4 ± 0.1d | 31.4 ± 0.2b | 18.9 ± 0.1a | 11.4 ± 0.2a | 49.5 ± 0.6a |
60 | 46.3 ± 0.6f | 57.1 ± 0.4f | 6.9 ± 0.3g | 31.3 ± 0.2b | 18.7 ± 0.2a | 11.5 ± 0.3a | 48.4 ± 0.5a | |
90 | 66.7 ± 0.3b | 72.7 ± 0.8b | 7.7 ± 0.2b | 29.9 ± 0.1c | 18.6 ± 0.2a | 11.6 ± 0.2a | 49.2 ± 0.6a | |
Feed moisture (%) | 10 | 26.4 ± 0.3i | 35.9 ± 0.4k | 7.0 ± 0.2g | 31.3 ± 0.2b | 18.7 ± 0.2a | 11.4 ± 0.1a | 48.0 ± 0.6a |
20 | 43.7 ± 0.4g | 45.9 ± 0.5i | 7.4 ± 0.1d | 32.0 ± 0.1a | 18.5 ± 0.1a | 11.7 ± 0.1a | 48.3 ± 0.5a | |
30 | 62.4 ± 0.5c | 58.1 ± 0.6f | 7.9 ± 0.2a | 32.1 ± 0.1a | 18.5 ± 0.1a | 11.8 ± 0.2a | 48.6 ± 0.5a |
Values represent the mean ± standard deviation; n = 3
a–kMeans in a column with different superscripts were significantly different (p < 0.05)
TFA = Total fatty acids
The effect of single condition of extrusion was determined by setting the all other three conditions at mean values, respectively