I have never done line sizing of PIPELINES so far. Therefore this post has come.
Taking input from internet, API etc. I have prepared an excel sheet (attached herewith) with pressure drop calculation equations. The formula have been double checked by me and I believe it should be correct. The excel answers match approximately with that of hysys output for the same set of input.
Request you all to kindly see the excel file please. I have following questions;
1. Should there be any difference in pressure drop calculation equations for PIPING and PIPELINE? I believe there should not be any. I need to confirm this please.
2. In IPS-E-PR-440 (refer http://www.cheresour...id-line-sizing/), service pipeline company equation (for pressure drop) for single phase crude oil in PIPELINE is provided. What is the basis/origin of this equation?
3. Can we use Darcy-Weichbach equation for liquids in PIPELINE?
4. Can we use Hazen-Williams equation for water in PIPELINE?
5. Similarly other equations available for PIPING (Weymouth, Panhandle, Spitzglass, Babcock, modified Darcy equation for two phase flow) are also valid for PIPELINE?
I have seen several interesting threads in this site, but I could not be satified.

Thanking you in advance.
Ajay