Figures & data
Figure 1. (a) Rheometer Haake model VT550 with a concentric cylinder system, (b) mango pulp, and (c) rheometer operation scheme Haake Viscotester.
![Figure 1. (a) Rheometer Haake model VT550 with a concentric cylinder system, (b) mango pulp, and (c) rheometer operation scheme Haake Viscotester.](/cms/asset/445a53ee-810f-4647-9a2d-1e3dce472954/ljfp_a_1297948_f0001_oc.jpg)
Figure 4. Ratio between the normalized sensitivity coefficients at: (a) 20°C, (b) 30°C, and (b) 40ºC.
![Figure 4. Ratio between the normalized sensitivity coefficients at: (a) 20°C, (b) 30°C, and (b) 40ºC.](/cms/asset/1bbc072b-edcb-4732-8c58-cfce2043f237/ljfp_a_1297948_f0004_oc.jpg)
Table 1 Rheological parameters estimated by the Levenberg–Marquardt method.
Figure 5. Reogrames (experimental and calculated from the Mizrahi–Berk equation) and residues at: (a) 20°C, (b) 30°C, and (c) 40°C.
![Figure 5. Reogrames (experimental and calculated from the Mizrahi–Berk equation) and residues at: (a) 20°C, (b) 30°C, and (c) 40°C.](/cms/asset/04f87d9b-0ac1-439e-b368-4e357b06ab31/ljfp_a_1297948_f0005_oc.jpg)