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Design a shell and tube Heat exchanger

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Hello Everybody,
I am Kashfia Mahin from Bangladesh. I have been working on the project
about Heat Exchanger Design for Power Plant.
I am going to design a heat exchanger for coal based power plant.I have made a decision to design a shell and tube heat
exchanger. I have chosen this for high pressure and temperature. I
have decided to design a fixed tubesheet heat exchanger. In TEMA
nomenclature, i have chosen BEM geometric Terminology. Will it be a
good decision? in your account which Front head will be good and why?
I want to design tubesheet angle will be the 30 degree angle for
better heat transfer. Plate Segmental baffle are frequently used
for flow diversity but it causes vibration. How will I stop this
vibration? in segmental baffles Which are used to be good? Single
segmental or Double Segmental Baffle? Most Power Generation Company
they Used Single Segmental Baffle even Double segmental baffle is
better than single segmental baffle to reduce pressure drop.

1 Reply Last Post 27 janv. 2016, 08:39 UTC−5
Jeff Hiller COMSOL Employee

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Posted: 8 years ago 27 janv. 2016, 08:39 UTC−5
This Discussion Forum being dedicated to COMSOL modeling, I presume that you are interested in modeling this with COMSOL. If so, these links should be helpful:
www.comsol.com/video/shell-tube-heat-exchanger-model-tutorial
www.comsol.com/blogs/how-model-shell-and-tube-heat-exchanger/
Best regards,
Jeff
This Discussion Forum being dedicated to COMSOL modeling, I presume that you are interested in modeling this with COMSOL. If so, these links should be helpful: http://www.comsol.com/video/shell-tube-heat-exchanger-model-tutorial http://www.comsol.com/blogs/how-model-shell-and-tube-heat-exchanger/ Best regards, Jeff

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