2005Applied science and technologyRequires access

Application of discontinuous helical baffles in shell-and-tube heat exchanger

Licheng Sun

Open publisher page 0 citations

Abstract

Experimental investigations of heat transfer and flow resistance performance on shell-and-tube heat exchanger with smooth tubes supported by different kinds of baffles are carried out. Discontinuous helical baffles and segment baffles are used in the experiments and their performances are compared. The experimental results show that applying discontinuous helical baffles in shell-and-tube heat exchanger can enhance the heat transfer apparently. Under the same liquid velocity condition, the average convection heat transfer coefficient in the shell side of discontinuous helical baffles shell-and-tube heat exchanger is 1.39~1.67 times compared with that in the shell side of segment baffles shell-and-tube heat exchanger ,and the total average convection heat transfer coefficient is 1.15~1.37 times. But it makes flow resistance increase,and the flow resistance in the shell side is 3.25~3.67 times compared with that in the shell side of segment baffles shell-and-tube heat exchanger.

About this research paper

What this paper is about

Experimental investigations of heat transfer and flow resistance performance on shell-and-tube heat exchanger with smooth tubes supported by different kinds of baffles are carried out. Discontinuous helical baffles and segment baffles are used in the experiments and their performances are compared. The experimental results show that applying discontinuous helical baffles in shell-and-tube heat exchanger can enhance the heat transfer apparently. Under the same liquid velocity condition, the average convection heat transfer coefficient in the shell side of discontinuous helical baffles shell-and-tube heat exchanger is 1.39~1.67 times compared with that in the shell side of segment baffles shell-and-tube heat exchanger ,and the total average convection heat transfer coefficient is 1.15~1.37 times. But it makes flow resistance increase,and the flow resistance in the shell side is 3.25~3.67 times compared with that in the shell side of segment baffles shell-and-tube heat exchanger.

Why it matters

A significance statement is not available in the OpenAlex record.

Key contribution

A contribution statement is not available in the OpenAlex record.

Method / approach

Method details are not available in the OpenAlex metadata.

Main findings

Findings are not separately available in the OpenAlex metadata.

Limitations

Limitations are not available in the OpenAlex metadata.

Applications

Application details are not available in the OpenAlex metadata.

Available abstract

Experimental investigations of heat transfer and flow resistance performance on shell-and-tube heat exchanger with smooth tubes supported by different kinds of baffles are carried out. Discontinuous helical baffles and segment baffles are used in the experiments and their performances are compared. The experimental results show that applying discontinuous helical baffles in shell-and-tube heat exchanger can enhance the heat transfer apparently. Under the same liquid velocity condition, the average convection heat transfer coefficient in the shell side of discontinuous helical baffles shell-and-tube heat exchanger is 1.39~1.67 times compared with that in the shell side of segment baffles shell-and-tube heat exchanger ,and the total average convection heat transfer coefficient is 1.15~1.37 times. But it makes flow resistance increase,and the flow resistance in the shell side is 3.25~3.67 times compared with that in the shell side of segment baffles shell-and-tube heat exchanger.

Key concepts: Baffle, Shell and tube heat exchanger, Heat exchanger, Mechanics, Concentric tube heat exchanger, Shell (structure), Heat transfer, Tube (container)

Related papers

Back to paper searchBrowse research topicsOriginal source
Application of discontinuous helical baffles in shell-and-tube heat exchanger — Research Paper | ScholarLens