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Glycol Dehydration System Problem
#1
Posted 01 March 2013 - 09:58 AM
#2
Posted 01 March 2013 - 01:12 PM
Wizgal:
You don’t furnish all the information to get to the source of what you identify as a problem.
- First, confirm that your dewpoint measurements are correct. Have you calibrated your DP meter? Have you compared your readings with that of your client’s (or of the pipeline operator)?
- What dewpoint is your meter measuring?
- How much moisture does your product gas contain?
- Next, confirm that your TEG pumps are working correctly and that the correct amount of TEG is being continuously circulated.
- Make sure that your stripping gas is flowing in at the correct flow rate and temperature.
- Confirm that your reboiler is maintained at 400 oF.
If the above all checks out well, then you are either not absorbing moisture in the contactor or you are not stripping out the moisture in the Stripper. Which ever, it is can be due to a packing failure in the contactor (channeling, distributors bad, trays damaged, etc.). This means that you have to bring the process down for cleanout, vessel entry, and inspection – all very costly and time consuming.
#3
Posted 01 March 2013 - 11:13 PM
#4
Posted 01 March 2013 - 11:15 PM
#5
Posted 02 March 2013 - 02:15 PM
What about the rest of the questions:
- What dewpoint is your meter measuring?
- How much moisture does your product gas contain?
- Next, confirm that your TEG pumps are working correctly and that the correct amount of TEG is being continuously circulated.
- Make sure that your stripping gas is flowing in at the correct flow rate and temperature.
Is 65 lb/MMScf the value of moisture content in the PRODUCT gas - or in the raw feed gas? Please be specific. We waste a lot of time and effort in "guessing" or "speculating" what you mean to write. Also confirm that your client or pipeline transporter verifies your product gas dew point readings. You should be operating your reboiler at 400 oF unless your operating manual states otherwise. If so, then how do you propose to produce product gas with only 7 lb of water/MMScf of product gas? That is why the stripping gas conditions and flow rates are very important.
Await your detailed and specific responses.
#6
Posted 02 March 2013 - 04:32 PM
could you ensure please that the problem arise after increasing gas rate and/or replacing trays with structure packing?!
#7
Posted 03 March 2013 - 11:49 PM
@Art Montemayor : We only measure the moisture of the gas,thus the dew point is not available in our platform. 65 lb/MMScf is the value of water content in gas that feed to glycol contactor , we have to make it to 7 lb/MMSCf for our customer. Right now the moisture content in gas exceed 7 lb/MMSCf so now we got penalty from our customer. Sorry for making you wasting your time, I am still new engineer i am still lack of experience .
@ahmed abd elmonem: The problem occur after rising gas rate and in the past it's sometime happen after the structure packing has been installed. Currently it's always happen.The mosisture content always exceed 7lb/MMSCF
#8
Posted 04 March 2013 - 09:34 AM
Wizgal:
You still have not answered my questions.........
Therefore, I won't answer yours.
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