Heat transfer augmentation in 3D inner finned helical pipe
- Li, Longjian, Cui, Wenzhi, Liao, Quan, Mingdao, Xin, Jen, Tien-Chien, Chen, Qinghua
- Authors: Li, Longjian , Cui, Wenzhi , Liao, Quan , Mingdao, Xin , Jen, Tien-Chien , Chen, Qinghua
- Date: 2004
- Subjects: Heat transfer , Helical tubes
- Language: English
- Type: Conference proceedings
- Identifier: http://hdl.handle.net/10210/16052 , uj:15733 , Citation: • Li, L. et al. 2004, “Heat transfer augmentation in 3D inner finned helical pipe,” ASME Heat Transfer/Fluids Engineering Conference, July 11-15, 2004, Charlotte, North Carolina, Vol. 3, pp. 139-143. HT-FED2004-56430. ISSN: 0-7918-4692-X.
- Description: Abstract: Experiments were performed to investigate the performance enhancement of single-phase flow and boiling heat transfer in the 3D inner finned helical tubes. The tests for single-phase flow and heat transfer were carried out in the helical tubes with a curvature of 0.0663 and a length of 1.15m, the range of the Reynolds number examined varies from 1000 to 8500. In comparison to the smooth helical tube, the experimental results of two finned helical tubes with different inner fin geometry showed that the heat transfer and flow resistance in the 3D inner finned helical tube gains greater augmentation. Within the measured range of Reynolds number, the average augmentation ratio of heat transfer of the two finned tubes are 71% and 103%, compared with the smooth helical tube, and 90% and 140% for flow resistance, respectively. The tests for flow boiling heat transfer was carried out in the 3D inner finned helical tube with a curvature of 0.0605 and a length of 0.668m.Compared with that in the smooth helical tube, the boiling heat transfer coefficient in the 3D inner finned helical tube is increased by 40%~120% under varied mass flow rate and wall heat flux conditions, meanwhile, the flow resistance coefficient increased by 18%~119%.
- Full Text:
- Authors: Li, Longjian , Cui, Wenzhi , Liao, Quan , Mingdao, Xin , Jen, Tien-Chien , Chen, Qinghua
- Date: 2004
- Subjects: Heat transfer , Helical tubes
- Language: English
- Type: Conference proceedings
- Identifier: http://hdl.handle.net/10210/16052 , uj:15733 , Citation: • Li, L. et al. 2004, “Heat transfer augmentation in 3D inner finned helical pipe,” ASME Heat Transfer/Fluids Engineering Conference, July 11-15, 2004, Charlotte, North Carolina, Vol. 3, pp. 139-143. HT-FED2004-56430. ISSN: 0-7918-4692-X.
- Description: Abstract: Experiments were performed to investigate the performance enhancement of single-phase flow and boiling heat transfer in the 3D inner finned helical tubes. The tests for single-phase flow and heat transfer were carried out in the helical tubes with a curvature of 0.0663 and a length of 1.15m, the range of the Reynolds number examined varies from 1000 to 8500. In comparison to the smooth helical tube, the experimental results of two finned helical tubes with different inner fin geometry showed that the heat transfer and flow resistance in the 3D inner finned helical tube gains greater augmentation. Within the measured range of Reynolds number, the average augmentation ratio of heat transfer of the two finned tubes are 71% and 103%, compared with the smooth helical tube, and 90% and 140% for flow resistance, respectively. The tests for flow boiling heat transfer was carried out in the 3D inner finned helical tube with a curvature of 0.0605 and a length of 0.668m.Compared with that in the smooth helical tube, the boiling heat transfer coefficient in the 3D inner finned helical tube is increased by 40%~120% under varied mass flow rate and wall heat flux conditions, meanwhile, the flow resistance coefficient increased by 18%~119%.
- Full Text:
Heat transfer augmentation in 3D internally finned and micro-finned helical tube
- Li, Longjian, Cui, Wenzhi, Liao, Quan, Mingdao, Xin, Jen, Tien-Chien, Chen, Qinghua
- Authors: Li, Longjian , Cui, Wenzhi , Liao, Quan , Mingdao, Xin , Jen, Tien-Chien , Chen, Qinghua
- Date: 2005
- Subjects: Helical tubes , Finned tubes , Heat transfer
- Type: Journal
- Identifier: uj:5263 , http://hdl.handle.net/10210/14932
- Description: Experiments are performed to investigate the single-phase flow and flow-boiling heat transfer augmentation in 3D internally finned and micro-finned helical tubes. The tests for single-phase flow heat transfer augmentation are carried out in helical tubes with a curvature of 0.0663 and a length of 1.15 m, and the examined range of the Reynolds number varies from 1000 to 8500. Within the applied range of Reynolds number, compared with the smooth helical tube, the average heat transfer augmentation ratio for the two finned tubes is 71% and 103%, but associated with a flow resistance increase of 90% and 140%, respectively. A higher fin height gives a higher heat transfer rate and a larger friction flow resistance. The tests for flow-boiling heat transfer are carried out in 3D internally micro-finned helical tube with a curvature of 0.0605 and a length of 0.668 m. Compared with that in the smooth helical tube, the boiling heat transfer coefficient in the 3D internally micro-finned helical tube is increased by 40–120% under varied mass flow rate and wall heat flux conditions, meanwhile, the flow resistance is increased by 18–119%, respectively.
- Full Text:
- Authors: Li, Longjian , Cui, Wenzhi , Liao, Quan , Mingdao, Xin , Jen, Tien-Chien , Chen, Qinghua
- Date: 2005
- Subjects: Helical tubes , Finned tubes , Heat transfer
- Type: Journal
- Identifier: uj:5263 , http://hdl.handle.net/10210/14932
- Description: Experiments are performed to investigate the single-phase flow and flow-boiling heat transfer augmentation in 3D internally finned and micro-finned helical tubes. The tests for single-phase flow heat transfer augmentation are carried out in helical tubes with a curvature of 0.0663 and a length of 1.15 m, and the examined range of the Reynolds number varies from 1000 to 8500. Within the applied range of Reynolds number, compared with the smooth helical tube, the average heat transfer augmentation ratio for the two finned tubes is 71% and 103%, but associated with a flow resistance increase of 90% and 140%, respectively. A higher fin height gives a higher heat transfer rate and a larger friction flow resistance. The tests for flow-boiling heat transfer are carried out in 3D internally micro-finned helical tube with a curvature of 0.0605 and a length of 0.668 m. Compared with that in the smooth helical tube, the boiling heat transfer coefficient in the 3D internally micro-finned helical tube is increased by 40–120% under varied mass flow rate and wall heat flux conditions, meanwhile, the flow resistance is increased by 18–119%, respectively.
- Full Text:
- «
- ‹
- 1
- ›
- »