Computational Modelling of Heat Transfer Coefficient
and Pressure Drop by Helical Baffles in Shell-Tube
Heat Exchanger
Journal:
GRENZE International Journal of Engineering and Technology
Authors:
Ramesha H, Sannamaregowda, Praveen D N
Volume:
10
Issue:
2
Grenze ID:
01.GIJET.10.2.775
Pages:
6334-6344
Abstract
Baffles are flow-directing or obstructing vanes or panels used in some industrial process
vessels (tanks), such as shell and tube heat exchangers, chemical reactors, and static mixers.
Baffles are an integral part of the shell and tube heat exchanger design. A baffle is designed to
support tube bundles and direct the flow of fluids for maximum efficiency. Baffle design and
tolerances for heat exchangers are discussed in the standards of the Tubular Exchanger
Manufacturers Association (TEMA). This use of continuous helical baffles reduces shell-side
pressure drop and helps improve heat transfer performance of shell and tube heat exchanger.
Properly designed continuous helical baffles can reduce fouling in the shell side and prevent the
flow- induced vibration as well. The use of continuous helical baffles results in nearly 10%
increase in heat transfer coefficient compared with that of conventional segmental baffles for
the same shell-side pressure drop. Helical baffles are employed increasingly in shell-and-tube
heat exchangers (helix exchangers) for their significant advantages in reducing pressure drop,
vibration, and fouling while maintaining a higher heat transfer performance.