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Heat Exchanger Steam Flow
#1
Posted 25 November 2024 - 05:49 AM
The tube bundle was removed and found clean and the shell it self was clean
Any guess where the problem could be found
The reboiler using LP steam and heating sour water
#2
Posted 25 November 2024 - 06:15 AM
Can you be more descriptive? "Having a problem" does not tell us much. Give the inlet and outlet data (T, P, flow rates), the heat exchanger specifications (tube size and length and number, heat exchange area, MAWPs, etc.), the heat duties, and exactly the physical parameter that is limited. How do you know the HX is not at it's physical limit?
#3
Posted 25 November 2024 - 06:28 AM
Hi,
a PID is appreciated, on top of Latexman's requests.
Is it a new problem?
Could be accumulation of inert, could be quality of the steam? should be saturated, could be an issue with level ....
Nothing wrong with your process???
Many things, in fact.
Breizh
#4
Posted 25 November 2024 - 04:03 PM
Actually I don't know how to add a PID here, for your question is it a new problem, yes it is
We used to feed to the column 39 m3/HR with approx 5000 kg/h steam
Now with control valve opening 100 % the steam flow is approx 4200 kg /HR , the steam is saturated, pressures 3.5 bar, temp 175 degree C
Edited by aliebrahem17, 25 November 2024 - 04:04 PM.
#9
Posted 26 November 2024 - 07:56 AM
I can't find More in Reply button
When editing a post, you’ll see “Use Full Editor”. On a new post, you’ll see “More Reply Options”. Both give you the same functionality. The attachment functions are below the text box.
Open your eyes. Don't give up so easy.
#11
Posted 27 November 2024 - 07:33 PM
#12
Posted 15 March 2025 - 06:06 AM
What is the process outlet temp and steam pressure on the shell?
What is the FT span?
Did you verify field vs DCS position?
Did the process inlet temp change?
Condensate control loop functioning properly? Could you confirm shell isn’t backed up ?
Did the composition of process inlet stream change?
Process inlet stream phase composition change?
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