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Hi Little Inch, Many thanks for your response. And you have definitely raised some serious concerns on the large amount of BOG at the jetty end. Maybe this needs to be discussed with the end-user. If they have made arrangements for handling large BOG at the ship end I don't foresee any problem...

Hi George, The BOG recompression capacity is yet to be fixed. The calculations for tank vapor, rundown line and rundown pump heat ingress, loading pump recirculation line heat ingress and BOG generation by pump is taken into consideration for the tank area BOG calculations. Hi Little Inch, 1...

Dear All, I have a liquid ammonia pipeline from the ammonia storage tank used for ship loading with a 15 day cycle for each ship load. There are two aspects I am looking for the design of cooldown system for the nearly 10 km of pipeline. 1. The cooldown is to be completed just before the ship...

Dear All, Thanks for all your responses. For the time being I will stick to Peng-Robinson since the simulation software does not give a multitude of options for selecting the EOS with some variations in the original PR and SRK EOS. Regards,

I want to perform flash calculations of anhydrous ammonia rundown at a slightly higher temperature (say -32 degrees C)and pressure (say 1.5 bara) to the ammonia storage tank operating at atmospheric pressure. I am using the open source process simulator COCO to perform these flash. I am aware of...