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Is there a formula to determine the distance of pipeline that CP can protect from a single rectifier influence? Please reference the source of your response as I would like to document this process. Also is there any rule of thump as to the interval between test leads on pipelines?

Thanks David I believe you've pointed me in the right direction. Also, regarding going from aCF to MaCF I should have known that was the case but after looking at my model for so long my mind goes to mush :=). Thanks again.

Thanks for the feed back. I will look further into the BOE conversions. Question I have other HVL products I'm attempting to model how do I acquire the HHV for them? By the way what is HHV? zdas04 in your last post does MaCF stand for Thousand Actual Cubic Feet, is so how did you get from...

Okay so we're back here again. It seems the formula in my orig post produces the same results as the ones which I've received, which is a good thing. I guess the problem I have now is that the gaseous state of my Highly Volatile Liquid is producing high bbls amount. I'm attempting to model a...

It seems I posted this topic in the wrong forum please reply to my question in "Piping & fluid mechanics engineering" by the way thanks zdas04

I think you'll find what your looking for at the following link: http://www.air-dispersion.com/feature2.html

Below I have two scenarios, both expressing a volume in cubic feet to pounds then expressing the pounds in barrels of oil equivalent, or something like that. Volume of Crude spilled = 400 ft^3 in five mins Crude density 58 lbs/ft^3 Is the Pounds to barrels conversion then...

I've been away for a couple of days. Thanks for all the help Latexman.

Latexman @ 16:18 you’re asking all the right questions but as stated in the attached document the equation is meant to give us a conservative flow rate. If I were looking for a more precise leak volume I would have to consider the things you’re mentioning but the current equation does the...

Latexman @ 16:18 your asking all the right questions but as stated in the attached document the equation is mean to give us a conservitive flowrate.

Latexman, Your right the method which I am trying to utilize is very conservative. Based on this method if I can determine the volume of Gas release (Conservatively) over a 10 min period I would just need to multiply that value times my product value of $7 Mcf to get the total conservative...

Problem solved.

Ladies and Gentlemen I'm attempting to model the scenario described in the attached document. Ultimately what I'm attempting to do is estimate product loss in dollars in the event of a line rupture, in order for me to do so I have to first calculate the leak volume (product released) for a full...