7000 tonne/hr of water at 300 deg celcius flows through Steam generator tubeside to leave at 260deg celcius. How head loss due to friction & pressure drop due to shrinkage are taken in to account.
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How To Calculate Pressure Drop Through Heat Exchanger Taking In To Acc
Started by rsk, Feb 16 2009 08:05 AM
4 replies to this topic
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#1
Posted 16 February 2009 - 08:05 AM
#2
Posted 16 February 2009 - 08:49 AM
To begin you will need to first size the exchanger which of course will require you to choose a suitable type of exchanger for your application.
Only when these are available can you begin to calculate the pressure drop.
If a general 'guide' is required try Coulson and Richardson.
Only when these are available can you begin to calculate the pressure drop.
If a general 'guide' is required try Coulson and Richardson.
#3
Posted 16 February 2009 - 11:51 AM
Dear rsk,
Your query appears somewhat 'vague' probably due to my incapability
What and how much is the other heated stream if your's reffered is (as appears) cooled stream?
thanks/regards
Qalander
Your query appears somewhat 'vague' probably due to my incapability
What and how much is the other heated stream if your's reffered is (as appears) cooled stream?
thanks/regards
Qalander
#4
Posted 17 February 2009 - 09:52 AM
You need to design the heat exchanger, and in the design stage, you will need to calculate the pressure drop due to friction and so on. There is normally a range of acceptable pressure drop for the tube and shell side, if you are referring to shell and tube HE of course. For more information, you can refer to process heat transfer by Kern.
QUOTE (rsk @ Feb 16 2009, 09:05 PM) <{POST_SNAPBACK}>
7000 tonne/hr of water at 300 deg celcius flows through Steam generator to leave at 260deg celcius. How head loss due to friction & pressure drop due to shrinkage are taken in to account.
#5
Posted 17 February 2009 - 11:35 AM
please refer to my edited post. flow of water is from tube side.
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