There will be a problem if dehydration equipment is taken out for services or totally removed from the offshore platform.
What is the typical estimates for glycol losses from dehydration unit?
Produced gas contains significant amount of methanol during startup used for Hydrate remidiation. Could someone please share some info on effect of methanol on gas dehydration (TEG) unit?
I am building a TEG dehydration contactor model using HYSYS. Is there a rule of thumb for contactor Pressure drop as well as gas temperature change (should increase!!)?
My simulation model contains dry Gas / Lean Glycol exchanger but I was told that it is not recomended. Can someone share knowledge on this issue?
Is there any disadvangtage of using internal coils in TEG regenerators?
Maximum recommended temperatures for Glycol reboilers
What the parameters for dehydration contactor (absorber) pressure?
What are the issues to the downstream system a Glycol (TEG) entrainment can cause?
Can you list out the various gas dehydration technologies currently used in oil and gas industry?