denniskb
Mechanical
- May 24, 2002
- 90
I am trying to set up an Excel spreadsheet to do a basic sizing of an ACHE for gas transmission pipeline aftercoolers. I need this so I can select an appropriate design then use the spreadsheet to simulate the selected unit under real operating conditions, not just the original design conditions.
I have used the methods set out in the Campbell's books and the GPSA data books and while they give different results they are in the same ball park. We have now had a unit designed by a reputable vendor and the air flow and surface area are significantly different to that calculated using my spreadsheet. I therefore no longer have a reliable way to do what I want with my spreadsheet.
The problem appears to be in two areas:
- the recommendations for ideal air temperature rise appear to be very inaccurate. Can anyone suggest an alternative method to determine this?
- the overall heat transfer coefficients from the books do not extend to the pressure I require (15,000 kPa or 2000 psi). I am now attempting to calculate this directly from heat transfer theory, but of course I need to know the air velocity to get Reynolds number for the film coefficient. Is there a typical air velocity that I can use for this type of unit?
- finally the typical overall heat transfer coefficients in the books do not state whether they include an allowance for fouling or are for new and clean service. Can anyone comment on this please?
Thanks in advance for any advice you can offer. Dennis Kirk Engineering
I have used the methods set out in the Campbell's books and the GPSA data books and while they give different results they are in the same ball park. We have now had a unit designed by a reputable vendor and the air flow and surface area are significantly different to that calculated using my spreadsheet. I therefore no longer have a reliable way to do what I want with my spreadsheet.
The problem appears to be in two areas:
- the recommendations for ideal air temperature rise appear to be very inaccurate. Can anyone suggest an alternative method to determine this?
- the overall heat transfer coefficients from the books do not extend to the pressure I require (15,000 kPa or 2000 psi). I am now attempting to calculate this directly from heat transfer theory, but of course I need to know the air velocity to get Reynolds number for the film coefficient. Is there a typical air velocity that I can use for this type of unit?
- finally the typical overall heat transfer coefficients in the books do not state whether they include an allowance for fouling or are for new and clean service. Can anyone comment on this please?
Thanks in advance for any advice you can offer. Dennis Kirk Engineering