OMEGA-3 Fatty Acids Retention, Oxidative Quality, and Sensoric Acceptability of Spray-Dried Flaxseed Oil
Table 3
Impact of spray-drying conditions on free fatty acids in flaxseed oil dried powder at different days and storage intervals.
Spray-dryer process run
Independent variables
Free fatty acids (%)
Inlet air temperature (°C)
Feed flow rate (mL/hr)
Atomization speed (rpm)
Outlet temperature (°C)
0 days
Storage at temperature 4°C
Storage at temperature 25°C
30 days
60 days
30 days
60 days
1
140 (0)
300 (+1)
16000 (0)
60 (‒1)
0.29 ± 0.05d
0.35 ± 0.06cd
0.45 ± 0.07bc
0.46 ± 0.07bc
0.71 ± 0.08ab
2
140 (0)
250 (0)
12000 (‒1)
60 (‒1)
0.28 ± 0.04d
0.34 ± 0.05cd
0.44 ± 0.06bc
0.45 ± 0.06bc
0.70 ± 0.07ab
3
140 (0)
200 (‒1)
16000 (0)
80 (+1)
0.29 ± 0.05d
0.35 ± 0.06cd
0.45 ± 0.06bc
0.46 ± 0.07bc
0.71 ± 0.08ab
4
120 (‒1)
200 (‒1)
16000 (0)
70 (0)
0.27 ± 0.02d
0.33 ± 0.03cd
0.43 ± 0.04bc
0.44 ± 0.05bc
0.69 ± 0.06ab
5
160 (+1)
300 (+1)
16000 (0)
70 (0)
0.31 ± 0.06cd
0.37 ± 0.07c
0.47 ± 0.07bc
0.48 ± 0.08b
0.73 ± 0.09a
6 (C1)
140 (0)
250 (0)
16000 (0)
70 (0)
0.28 ± 0.04d
0.35 ± 0.05cd
0.45 ± 0.06bc
0.46 ± 0.06bc
0.71 ± 0.07ab
7
120 (‒1)
250 (0)
16000 (0)
80 (+1)
0.29 ± 0.04d
0.36 ± 0.05c
0.46 ± 0.05bc
0.47 ± 0.06bc
0.72 ± 0.08a
8 (C2)
140 (0)
250 (0)
16000 (0)
70 (0)
0.28 ± 0.05d
0.35 ± 0.06cd
0.45 ± 0.07bc
0.46 ± 0.07bc
0.71 ± 0.08ab
9
140 (0)
200 (‒1)
16000 (0)
60 (‒1)
0.28 ± 0.04d
0.34 ± 0.05cd
0.44 ± 0.05bc
0.46 ± 0.06bc
0.72 ± 0.07a
10
160 (+1)
250 (0)
16000 (0)
60 (‒1)
0.30 ± 0.06d
0.37 ± 0.07c
0.47 ± 0.07bc
0.48 ± 0.08b
0.74 ± 0.09a
11
160 (+1)
250 (0)
12000 (‒1)
70 (0)
0.31 ± 0.06cd
0.38 ± 0.07c
0.48 ± 0.08b
0.50 ± 0.08b
0.75 ± 0.09a
12
120 (‒1)
250 (0)
12000 (‒1)
70 (0)
0.27 ± 0.02d
0.33 ± 0.03cd
0.43 ± 0.04bc
0.44 ± 0.04bc
0.69 ± 0.05ab
13
140 (0)
200 (‒1)
20000 (‒1)
70 (0)
0.28 ± 0.03d
0.34 ± 0.04cd
0.44 ± 0.05bc
0.45 ± 0.05bc
0.70 ± 0.06ab
14
120 (‒1)
250 (0)
16000 (0)
60 (‒1)
0.26 ± 0.01d
0.32 ± 0.03cd
0.42 ± 0.04bc
0.43 ± 0.05bc
0.68 ± 0.06ab
15 (C3)
140 (0)
250 (0)
16000 (0)
70 (0)
0.28 ± 0.04d
0.35 ± 0.06cd
0.45 ± 0.06bc
0.46 ± 0.07bc
0.72 ± 0.08a
16
120 (‒1)
300 (+1)
16000 (0)
70 (0)
0.27 ± 0.02d
0.33 ± 0.03cd
0.43 ± 0.04bc
0.44 ± 0.05bc
0.69 ± 0.06ab
17
140 (0)
250 (0)
12000 (‒1)
80 (+1)
0.29 ± 0.05d
0.36 ± 0.06c
0.46 ± 0.07bc
0.47 ± 0.08bc
0.72 ± 0.09a
18 (C4)
140 (0)
250 (0)
16000 (0)
70 (0)
0.28 ± 0.04d
0.35 ± 0.04cd
0.45 ± 0.05bc
0.46 ± 0.06bc
0.71 ± 0.07ab
19
140 (0)
300 (+1)
16000 (0)
80 (+1)
0.29 ± 0.05d
0.36 ± 0.06c
0.46 ± 0.06bc
0.47 ± 0.07bc
0.72 ± 0.07a
20
160 (+1)
250 (0)
16000 (0)
80 (+1)
0.31 ± 0.07cd
0.38 ± 0.07c
0.48 ± 0.08b
0.49 ± 0.08b
0.75 ± 0.09a
21
140 (0)
300 (+1)
12000 (‒1)
70 (0)
0.28 ± 0.05d
0.35 ± 0.05cd
0.45 ± 0.06bc
0.46 ± 0.06bc
0.72 ± 0.07a
22
120 (‒1)
250 (0)
20000 (+1)
70 (0)
0.27 ± 0.02d
0.34 ± 0.03cd
0.44 ± 0.03bc
0.45 ± 0.04bc
0.70 ± 0.05ab
23
140 (0)
250 (0)
20000 (+1)
80 (+1)
0.29 ± 0.05d
0.36 ± 0.06c
0.46 ± 0.06bc
0.47 ± 0.07bc
0.72 ± 0.07a
24
140 (0)
300 (+1)
20000 (+1)
70 (0)
0.27 ± 0.03d
0.34 ± 0.03cd
0.45 ± 0.04bc
0.46 ± 0.04bc
0.72 ± 0.05a
25
140 (0)
250 (0)
20000 (+1)
60 (‒1)
0.27 ± 0.02d
0.33 ± 0.03cd
0.44 ± 0.04bc
0.45 ± 0.04bc
0.71 ± 0.05ab
26
160 (+1)
250 (0)
20000 (+1)
70 (0)
0.31 ± 0.06cd
0.38 ± 0.07c
0.49 ± 0.07b
0.51 ± 0.08b
0.77 ± 0.09a
27
160 (+1)
200 (‒1)
16000 (0)
70 (0)
0.31 ± 0.06cd
0.38 ± 0.06c
0.48 ± 0.07b
0.49 ± 0.07b
0.75 ± 0.08a
28
140 (0)
200 (‒1)
12000 (‒1)
70 (0)
0.29 ± 0.05d
0.36 ± 0.06c
0.45 ± 0.06bc
0.45 ± 0.07bc
0.70 ± 0.07ab
29 (C5)
140 (0)
250 (0)
16000 (0)
70 (0)
0.28 ± 0.04d
0.35 ± 0.05cd
0.45 ± 0.06bc
0.46 ± 0.06bc
0.72 ± 0.07a
30 (C6)
140 (0)
250 (0)
16000 (0)
70 (0)
0.28 ± 0.05d
0.35 ± 0.06cd
0.45 ± 0.07bc
0.46 ± 0.07bc
0.72 ± 0.08a
C1,C2,C3,C4,C5,C6Spray-drying process at center points. Experimental model = Box–Behnken design. Total number of spray-drying treatments = 30. Number of replicates = 03. a-dValues with similar letters show homogenous groups within the row and column ().