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[Engineer87]

Hi Guys,

 

I need to  determine if I can just use a  tank ( say 400 bbl) and vent to atmosphere or use a NGL bullet with flare stack, 

 

Process data is as follows:

 

· Condensate Rate = 50 m3/day

· Separator Pressure = 500 psig

· Separator Temperature = 38°C

 

I used VMG to  Pre-flash the condensate in the separator to model the gas that would flash off in the separator naturally before you flash it across

the dump valve…

 

I need to calculate the estimated Vent  volume based on flash calculation.Sorry i dont have API 2000 any information on above?