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Air Compressor Intercooler - Water Drop Out


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#1 Guest_quantum_*

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Posted 08 March 2012 - 12:50 PM

Dear all,

I am currently designing the intercoolers of a 5 stage centrifugal compressor (i.e. designing 4 intercoolers) by trying to follow the example given in "Process Heat Transfer" by D.Q Kern (Example 9.2 page 196, section titled "Gases").

My understanding of the process of compression and intercooling of air: the humid air (at 1atm) is compressed - reducing the volume whilst increasing the temperature and pressure in accordance to the pressure ratio. This flow is then sent to the intercooler where it is cooled to the original inlet temperature (assuming 100% efficiency and no pressure drop in the intercooler for simplicity). However, because of the change in volume (as a result of the compression) reducing the temperature in the intercooler means that a portion of the original water vapour will become liquid and "drop out". Thus resulting in a new (lower) humidity entering the 2nd stage of the compressor. A very simple explanation but I think it is right - please correct me if I am wrong!!

Now referring back to the solution of example 9.2 in Kern. I follow all the steps up until the calculation of the "Specific volume of atmospheric air = (359/29)(555/492)14.7/(14.7-0.8153)=14.8 ft3/lb" i.e the specific volume of the air entering the 2nd stage.

My understanding of the numbers (since I cant find the equation using just symbols anywhere!!) is that 29 = MW air. 555/492 = inlet temp/ref temp in oR. 14.7 = atm pressure in psi and 0.8153 = sat partial pressure of water at inlet temp in psi.

I understand this is a rather trivial humidity question - but I have been looking at it for days and cant get my head around where the 359 comes (or infact what the equation is?!!) Perhaps it is the imperial units that are confusing me!!

Any help understanding this last equation would be much appreciated!!

I have attached the problem for you information.

Attached File  Kern problem.pdf   180.46KB   40 downloads

#2 pavanayi

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Posted 08 March 2012 - 04:10 PM

quantum,
Let us try and use a dimensional analysis approach.
The equation can be analysed as
(359/29) * (temperature/temperature)*(pressure/pressure) = 14.8 ft3/lb

so, (359/29) has units of ft3/lb.

Now 29, if indeed is MW, should have a unit of lb/lbmol, which will mean
unit of 359 is ft3/lbmol. (or in SI, should be m3/kgmol)

The unit points towards molar volume.
Ideal gas occupies 22.4 l/mol or 22.4 m3/kgmol
1 m3/kg = 16.01 ft3/lb
so, converting m3/kgmol into ft3/lbmol = 22.4*16.01 = 358.6 ( is near 359)

Hope the methodology helped.

Edited by pavanayi, 08 March 2012 - 04:14 PM.


#3 Guest_quantum_*

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Posted 08 March 2012 - 04:42 PM

pavanayi, your explanation is perfect! Thankyou!

I had attempted dimensional analysis but had completely forgotten to include the volume of an ideal gas! Doh! It is always the simpliest things one tends to forget!!

Thank you once again!




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