Table 3 Nusselt number versus geometry configuration at \(Re=100\).

From: Investigation of mixing viscoplastic fluid with a modified anchor impeller inside a cylindrical stirred vessel using Casson–Papanastasiou model

 

ACI

AI1

AI2

AI3

\(Nu\)

0.707

0.709

0.7173

0.781

\(\Delta (Nu)\%\)

–

0.28

1.4

10.46

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