How to Place Deresonating Baffles in a Shell and Tube Heat Exchanger?

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SUMMARY

The placement of deresonating baffles in a Shell and Tube heat exchanger is critical for minimizing resonation and optimizing flow. Baffles should be positioned parallel to the tube bundle, particularly in areas identified as prone to resonation, which can be detected using a stethoscope. Anti-swirl baffles are typically installed near the tube inlets and outlets. Additionally, understanding the thermal properties of white liquor, a mixture of NaOH, Na2S, and Na2CO3, is essential for effective design and operation.

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  • Understanding of Shell and Tube heat exchanger design
  • Knowledge of baffle types and their functions
  • Familiarity with fluid dynamics and flow characteristics
  • Basic principles of thermal properties in chemical engineering
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  • Research the design and placement of baffles in Shell and Tube heat exchangers
  • Learn about the thermal properties of white liquor used in the pulp industry
  • Investigate methods for measuring resonation in heat exchangers
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Engineers, heat exchanger designers, and chemical process professionals seeking to optimize the performance and reliability of Shell and Tube heat exchangers.

jeewana
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Hi,

Anyone knows how to place the DERESONATING BAFFLES in a Shell and Tube heat Exchanger? How does it look likes?
 
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jeewana said:
Hi,

Anyone knows how to place the DERESONATING BAFFLES in a Shell and Tube heat Exchanger? How does it look likes?

I am sure some engineer can locate the areas that are most prone to resonating, or even just someone with a stethescope - that is the place for the interiour baffles ... the ones I am familiar with lie within and to parallel the tube bundle.

I have also seen anti-swurrl (is that a word?) baffles placed near the tube inlet and outlets. If they are within the bundle they have to be removed for maintenence on the tube sheets etc - if inside the piping leading to the exchanger, not.

Other than that - differences in flow and pressure on the shellside can make a big difference.
 
Can anyone help me to find the the thermal properties (Density,Heat capacity,viscosity,thermal conductivity) of WHITE LIQUOR used in pulp industry?

[WHITE LIQUOR is a mixture of NaOH,Na2S,Na2CO3.]
 
Does this help? I think this is something that you'll need to calculate yourself.
http://www.sciencedirect.com/science?_ob=ArticleURL&_udi=B6WHM-4MBJK4C-1&_user=10&_rdoc=1&_fmt=&_orig=search&_sort=d&_docanchor=&view=c&_searchStrId=1174338322&_rerunOrigin=google&_acct=C000050221&_version=1&_urlVersion=0&_userid=10&md5=02b5229bb0f9b771161a241ec0872a5d
 
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Thanks for the reply.

Yes, As you said this should be calculated since the percentages of its content varies. However I was expecting some typical values for a design.

Thanks again.
 
croghan27 said:
I am sure some engineer can locate the areas that are most prone to resonating, or even just someone with a stethescope - that is the place for the interiour baffles ... the ones I am familiar with lie within and to parallel the tube bundle.

I have also seen anti-swurrl (is that a word?) baffles placed near the tube inlet and outlets. If they are within the bundle they have to be removed for maintenence on the tube sheets etc - if inside the piping leading to the exchanger, not.

Other than that - differences in flow and pressure on the shellside can make a big difference.


Thanks for the reply. It helped me to get some idea.
Jeewana
 

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