Table 1.

The mean particle diameters and Herschel Bulkey model parameters of non-homogenized and high pressure homogenized mixed juices

	Mean particle diameters (µm)				Herschel Bulkey model parameters
	D[4,3]	D[3,2]	D50	D90	Consistency index (k) (Pa.sn)	Flow behavior index (n) (-)	Yield stress (η0) (Pa)	R2
NH	480.2 ± 1.9a	342.2 ± 2.0a	324.4 ± 9.0a	623.4 ± 8.7a	0.448 ± 0.011a	0.29 ± 0.04f	0.23 ± 0.04a	0.99
25/1(25)	242.7 ± 2.9b	149.2 ± 1.4b	126.5 ± 5.7a	297.8 ± 9.7b	0.223 ± 0.119b	0.58 ± 0.12e	0.10 ± 0.01c	0.99
100/1(25)	70.8 ± 1.8d	42.9 ± 0.4d	31.4 ± 4.1 cd	87.0 ± 5.7d	0.029 ± 0.003bc	0.81 ± 0.10c	0.05 ± 0.01d	0.99
140/1(25)	57.4 ± 0.6e	35.2 ± 0.7de	26.1 ± 1.0de	70.5 ± 0.8de	0.002 ± 0.001c	1.11 ± 0.12b	0.22 ± 0.09a	0.95
180/1(25)	50.2 ± 0.1e	30.6 ± 0.1e	22.4 ± 0.0e	61.4 ± 0.2e	0.003 ± 0.001c	1.05 ± 0.06b	0.18 ± 0.03b	0.96
100/2(25)	40.1 ± 0.2f	27.2 ± 0.5e	21.3 ± 0.6e	53.3 ± 0.5f	0.038 ± 0.003bc	0.69 ± 0.07d	0.05 ± 0.02d	0.99
100/1(40)	87.9 ± 0.1c	52.3 ± 0.5c	38.1 ± 1.3c	107.7 ± 0.6c	0.010 ± 0.002c	1.35 ± 0.10a	0.21 ± 0.06a	0.97

Values are the means of three replicates ± SD. Different letters in each column indicate significant differences among treatments at 0.05 level according to ANOVA analysis