Jump to content



Featured Articles

Check out the latest featured articles.

File Library

Check out the latest downloads available in the File Library.

New Article

Product Viscosity vs. Shear

Featured File

Vertical Tank Selection

New Blog Entry

Low Flow in Pipes- posted in Ankur's blog

Calculating Absorbtion Column Diameter Via Pressure Drop


This topic has been archived. This means that you cannot reply to this topic.
2 replies to this topic
Share this topic:
| More

#1 amifall

amifall

    Brand New Member

  • Members
  • 1 posts

Posted 14 May 2009 - 06:54 AM

How do we use pressure drop to obtain column diameter in equipment design? =P

#2 djack77494

djack77494

    Gold Member

  • ChE Plus Subscriber
  • 1,282 posts

Posted 14 May 2009 - 03:27 PM

QUOTE (amifall @ May 14 2009, 03:54 AM) <{POST_SNAPBACK}>
How do we use pressure drop to obtain column diameter in equipment design? =P

I assume you are refering to a distillation column here and you are wanting to determine the column's diameter, or size the column. Normally you are pretty well constrained in what column diameter to use by various considerations. The availability of heating and cooling utilities will limit the top and bottom operating pressures, though you could "push the envelope" a bit at the cost of increased surface areas for your condenser and reboiler. Tray spacing may allow for small adjustments in the tray's diameter - for example, you may be able to select a smaller column diameter by increasing the tray spacing. Doing so would also increase the pressure drop through the column. Both of these changes though are relatively small and it would be very unusual for pressure drop to be a very important variable in the design of a trayed tower. For a packed column, the selection of packing type is often closely related to the allowable pressure loss, but the performance requirements really drive the column diameter selection more than anything.

#3 katmar

katmar

    Gold Member

  • ChE Plus Subscriber
  • 694 posts

Posted 15 May 2009 - 01:42 AM

You should always calculate the expected pressure drop for a potential design, but the pressure drop isn't always the most important factor.

For columns operating at atmospheric pressure or above the pressure drop is often not critical, and you would design on the basis of approach to the flooding point. Once you have selected an approach to flooding and have calculated the column diameter required to achieve that, you would calculate the pressure drop to ensure that it is acceptable, and to get the pressures inside the column if you want to refine your physical properties to the actual conditions.

On the other hand, the pressure drop can be the most critical factor in a vacuum tower. If the pressure drop is too high the base pressure will be high and consequently the base temperature will be high too. Usually you will be using vacuum for the express purpose of keeping the base temperature low, so the pressure drop is important.

In a trayed column the pressure drop is less affected by flow rate than it is in a packed column because there is a (more or less) fixed head on each tray due to the height of the liquid retained on the tray. This makes packed columns more popular in low pressure drop applications - but this is certainly not a universal rule and you will find trayed vacuum towers as well.




Similar Topics