Has anyone came across this ? And how do we actually know it takes into account of condensation from result ? liquid holdup ? etc So what i am trying to find out is how do we define the condensate gas ratio input ?įrom my understanding is the Sm3(in liquid volume)/ Million Sm3 (in gas volume) at the current condition which is 55C and 55bar. When i tried to change the condensate gas ratio to let's say "8", it did give expected result To more specific for pipephase user, my fluid type is "gas condensate", as for condensate source inputĬondensate gas ratio = 0 ( as it is fully vapour at that condition)Īnd the result summary showing no condensation occur throughout the pipeline which i highly doubt it ( My question is will the simulation take into account of condensation when the content reached pipe ambient temperature (26C) ? The pipeline consists of gas condensate which is fully vapour at 55 bar, 55C (from booster pump and cooled down by an air cooler). I am currently using pipephase 9.1 to determine pressure & temperature profile and flow regime of a pipeline (120km).
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