Additional input:
length of the pipeline: 120 km
dia of pipe: 26 inch
HSD: 5.8 MMTPA & ATF 5.4 MMTPA to be transported through above mentioned common line.
velocity limit 1.75 m/s
pump station at source to boost the fluid to the end point with min of 5 barg pressure.
HSD density: 846 kg/m3
ATF density: 826 kg/m3.
how to find out the optimum no. of batches to keep min interface quantity per anum and to keep optimum capacity of receipt tanks?
Appreciate your valuble suggistions....
Edited by Sunkara, 21 December 2011 - 12:39 AM.