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Shell And Tube Heat Exchanger Design


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#1 Guest_Tshepang_*

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Posted 23 September 2009 - 01:12 PM


A shell and tube heat exchanger is required to cool 75kg/s of oil from 500K to 450K by means of 100kg/s water entering at 350K.

How would one calculate the required surface area for the above-mentioned requirements for a partly counter-current and partly co-current heat exchanger?

DATA:

  • Specific heat capacity of water is 4.2kJ/kg.K
  • Specific heat capacity of oil is 3.0kJ/kg.K
  • Overall heat transfer co-efficient is 4kW/m2.K
  • Temperature correction factor is 0.75 with reference to counter-current flow


#2 breizh

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Posted 26 September 2009 - 10:12 PM

HI ,
What is the meaning of partly co current and partly counter current ?

Basic equation on heat transfer : heat transfer on both side ( cold & hot are equal)
1) M*cpcold *( Tcold out - Tcold in) =m*cphot * ( Thot in -Thot out) =Q
overall :
2) Q=U*A*Y*Dt ml(log mean)

from equation 1 you will get Tcold out
from equation 2 you will get A after calculating Dt ml with Y corection factor refering to counter current

Hope it helps
Breizh

#3 Guest_Tshepang_*

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Posted 01 October 2009 - 06:12 PM

Thank you for your response. I assumed that the Heat Exchanger Design in question has Reversed, Mixed or Cross-Flow.

Attached, is my solution (Heat Exchanger Design - Surface Area.pdf).

Anybody is welcome to correct any error(s) that I might have committed.

Attached Files



#4 Art Montemayor

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Posted 02 October 2009 - 06:18 AM


Tshepang:

I haven't read all your calculated answer, but you have made an oversight in not specifically addressing Breizh´s question: what specific pass arrangement(s) do you have on the shell and tube side? Without this specific information, you cannot generate the required "F" factor in order to modify the Log Mean Temperature Difference (LMTD).

You should address the question and supply at least a sketch of the exchanger, clearly showing the passes. The temperature vs. distance curve you supply in your solution is that of a pure counterflow exchanger. I frankly don't have even a vague idea of what you mean by "Reversed, Mixed or Cross-Flow" just like I don't know what "partly co current and partly counter current" flow means. What country are you in or where have you obtained your technology descriptions? This could help us understand what you are trying to describe.


#5 Guest_Tshepang_*

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Posted 06 October 2009 - 07:11 PM


Tshepang:

I haven't read all your calculated answer, but you have made an oversight in not specifically addressing Breizh´s question: what specific pass arrangement(s) do you have on the shell and tube side? Without this specific information, you cannot generate the required "F" factor in order to modify the Log Mean Temperature Difference (LMTD).

You should address the question and supply at least a sketch of the exchanger, clearly showing the passes. The temperature vs. distance curve you supply in your solution is that of a pure counterflow exchanger. I frankly don't have even a vague idea of what you mean by "Reversed, Mixed or Cross-Flow" just like I don't know what "partly co current and partly counter current" flow means. What country are you in or where have you obtained your technology descriptions? This could help us understand what you are trying to describe.




QUESTION/REQUEST: what specific pass arrangement(s) do you have on the shell and tube side? Without this specific information, you cannot generate the required "F" factor in order to modify the Log Mean Temperature Difference (LMTD)"

RESPONSE: The Temperature Correction Factor is given as 0.75. Please note that this is a standard assignment/class test/examination problem. Attached, please find the original problem statement (Heat Exchanger Design - Problem Statement.pdf). “Pass arrangement(s)” and other topics are covered in other problems. Similar problems can be found in Coulson & Richardson’s Chemical Engineering (Volume 1) under Heat Transfer.

----------------------------------------------------

REQUEST/SUGGESTION: You should address the question and supply at least a sketch of the exchanger, clearly showing the passes.

RESPONSE: Same as above

----------------------------------------------------

COMMENT: I frankly don't have even a vague idea of what you mean by "Reversed, Mixed or Cross-Flow" just like I don't know what "partly co current and partly counter current" flow means.

RESPONSE: "Reversed, Mixed or Cross-Flow" is described in Perry’s Chemical Engineers’ Handbook, 7th edition, 11-5. It is a premise upon which my solution is based.

----------------------------------------------------

QUESTION/REQUEST/SUGGESTION: What country are you in or where have you obtained your technology descriptions? This could help us understand what you are trying to describe.

RESPONSE:

On my bookshelf:

  • Perry’s Chemical Engineers’ Handbook, 7th edition
  • Basic Principles and Calculations in Chemical Engineering, D.M Himmelblau & J.B Riggs, 7th edition
  • Coulson & Richardson’s Chemical Engineering, Volume 1, 6th edition
  • Coulson & Richardson’s Chemical Engineering, Volume 2, 5th edition
  • Coulson & Richardson’s Chemical Engineering, Volume 6, 4th edition
  • Shreve’s Chemical Process Industries, 5th edition
  • Organic Chemistry, John McMurry, 6th edition
  • Organic Chemistry , Janice Smith, 2nd edition
  • Calculus – Early Transcendentals, James Stewart, 5th edition
  • Engineering Mathematics, K.A Stroud, 6th edition
  • Physics, J.D Cutnell & K.W Johnson, 7th edition
  • Fundamentals of Physics, D. Halliday, R. Resnick & J. Walker, 7th edition

Other resources:

I also consult governmental depatments, corporations and a myriad of other resources.

Attached Files






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