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Table 3 Correlations of Re, Pr, and Nu in different tubes

From: Heat-transfer performance of twisted tubes for highly viscous food waste slurry from biogas plants

Tubes

Equations

Cooling

Heating

THT, Ī”Tā€‰=ā€‰25Ā Ā°C

1. Nuā€‰=ā€‰1.69Re0.335Pr1/3, R2ā€‰=ā€‰0.973

2. Nuā€‰=ā€‰1.76Re0.346Pr1/3, R2ā€‰=ā€‰0.999

THT, Ī”Tā€‰=ā€‰50Ā Ā°C

3. Nuā€‰=ā€‰0.798Re0.387Pr1/3, R2ā€‰=ā€‰0.993

4. Nuā€‰=ā€‰1.54Re0.265Pr1/3, R2ā€‰=ā€‰0.943

TET

5. Nuā€‰=ā€‰0.422Re0.523Pr1/3, R2ā€‰=ā€‰0.984

6. Nuā€‰=ā€‰1.36Re0.325Pr1/3, R2ā€‰=ā€‰0.996

CT

7. Nuā€‰=ā€‰0.617Re0.337Pr1/3, R2ā€‰=ā€‰0.995

8. Nuā€‰=ā€‰0.902Re0.295Pr1/3, R2ā€‰=ā€‰0.993