From: Heat-transfer performance of twisted tubes for highly viscous food waste slurry from biogas plants
Tubes | Equations | |
---|---|---|
Cooling | Heating | |
THT, ĪTā=ā25Ā Ā°C | 1. Nuā=ā1.69Re0.335Pr1/3, R2ā=ā0.973 | 2. Nuā=ā1.76Re0.346Pr1/3, R2ā=ā0.999 |
THT, ĪTā=ā50Ā Ā°C | 3. Nuā=ā0.798Re0.387Pr1/3, R2ā=ā0.993 | 4. Nuā=ā1.54Re0.265Pr1/3, R2ā=ā0.943 |
TET | 5. Nuā=ā0.422Re0.523Pr1/3, R2ā=ā0.984 | 6. Nuā=ā1.36Re0.325Pr1/3, R2ā=ā0.996 |
CT | 7. Nuā=ā0.617Re0.337Pr1/3, R2ā=ā0.995 | 8. Nuā=ā0.902Re0.295Pr1/3, R2ā=ā0.993 |