Table 2.

Defined parameters of test 2 with fluid density of ${\mathrm{\rho }}_1\simeq 1000\left(\mathrm{k}\mathrm{g}/{\mathrm{m}}^3\right)$, tenth seconds of test (T1) and 5 s after the test (T2).

P (bar)	V (m/s)	Parameters	Nozzle Diameter 0.2 mm – Pure Water
			T1		T2
			$K/Dc$	$S/Dc$	$K/Dc$	$S/Dc$
1	11.6	Mean	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	$-$	$-$	$-$	$-$
2	16.9	Mean	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	$-$	$-$	$-$	$-$
3	22.5	Mean	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	$-$	$-$	$-$	$-$
4	26.3	Mean	0.050	0.233	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0056	0.021	$-$	$-$
5	28.1	Mean	0.055	0.261	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0385	0.029	$-$	$-$
6	31.8	Mean	0.061	0.288	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0043	0.023	$-$	$-$
7	35	Mean	0.066	0.312	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0053	0.031	$-$	$-$
8	37	Mean	0.070	0.323	0.05	0.3
		Stand. deviation	0.0084	0.025	$-$	$-$
P (bar)	V (m/s)	Parameters	Nozzle Diameter 0.3 mm – Pure Water
			T1		T2
			$K/Dc$	$S/Dc$	$K/Dc$	$S/Dc$
1	6.3	Mean	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	$-$	$-$	$-$	$-$
2	9.6	Mean	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	$-$	$-$	$-$	$-$
3	12	Mean	0.051	0.251	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0031	0.025	$-$	$-$
4	13.5	Mean	0.060	0.278	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0054	0.026	$-$	$-$
5	15.4	Mean	0.067	0.302	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0053	0.024	$-$	$-$
6	17.7	Mean	0.075	0.321	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0056	0.029	$-$	$-$
7	19.1	Mean	0.081	0.349	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0089	0.038	$-$	$-$
8	20.6	Mean	0.088	0.355	0.05	0.3
		Stand. deviation	0.0088	0.032	$-$	$-$
P (bar)	V (m/s)	Parameters	Nozzle Diameter 0.4 mm – Pure Water
			T1		T2
			$K/Dc$	$S/Dc$	$K/Dc$	$S/Dc$
1	9.3	Mean	0.074	0.341	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0067	0.037	$-$	$-$
2	14.6	Mean	0.109	0.453	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0087	0.041	$-$	$-$
3	18.1	Mean	0.136	0.556	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0068	0.044	$-$	$-$
4	20.6	Mean	0.160	0.644	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0161	0.071	$-$	$-$
5	23.4	Mean	0.181	0.727	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0127	0.073	$-$	$-$
6	26.5	Mean	0.200	0.805	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0120	0.072	$-$	$-$
7	28.8	Mean	0.218	0.871	0.05	0.4
		Stand. deviation	0.0174	0.061	$-$	$-$
8	31	Mean	0.235	0.923	0.08	0.4
		Stand. deviation	0.0117	0.074	$-$	$-$
P (bar)	V (m/s)	Parameters	Nozzle Diameter 0.5 mm – Pure Water
			T1		T2
			$K/Dc$	$S/Dc$	$K/Dc$	$S/Dc$
1	7.7	Mean	0.093	0.411	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0084	0.045	$-$	$-$
2	12	Mean	0.138	0.562	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0110	0.051	$-$	$-$
3	15.2	Mean	0.174	0.714	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0139	0.057	$-$	$-$
4	17	Mean	0.205	0.816	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0143	0.082	$-$	$-$
5	18.5	Mean	0.232	0.924	$\simeq$ 0	$\simeq$ 0
		Stand. deviation	0.0234	0.065	$-$	$-$
6	21.6	Mean	0.258	1.017	0.05	0.3
		Stand. deviation	0.0155	0.081	$-$	$-$
7	24	Mean	0.282	1.096	0.08	0.4
		Stand. deviation	0.0141	0.098	$-$	$-$
8	26	Mean	0.304	1.159	0.10	0.4
		Stand. deviation	0.0212	0.116	$-$	$-$