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

1
- - - - -

Kettle-Type Heat Exchanger

process design design heat exchanger heat transfer process heat transfer

No replies to this topic
Share this topic:
| More

#1 Kentucky08

Kentucky08

    Junior Member

  • Members
  • 14 posts

Posted Today, 01:32 AM

Good day, everyone,

I am currently revising our existing evaporator design, as the current configuration has been observed to cause oil entrainment. We initially considered two possible causes:

  1. Excess heating

  2. Insufficient vapor disengagement space

After evaluation, insufficient vapor disengagement has been identified as the primary cause.

In this regard, I am reviewing the existing evaporator design prepared by my former colleague (please see the attached file: Existing Design). I am currently evaluating two revised options:

  1. My proposed revision (File name: Own Design)

  2. An alternative design suggestion from an external colleague (File Name: Additional Design)

While both options appear technically feasible, I would greatly appreciate your expertise and insights to determine the most suitable approach.

 

For reference, the process fluid consists of palm olein with excess methanol and water of reaction from the esterification process. Oil entrainment into the vapor stream has been observed, which affects downstream separation.

 

Thank you in advance for your guidance and recommendations.

Attached Files


Edited by Kentucky08, Today, 01:38 AM.





Reply to this topic



  

Similar Topics