What do you mean you did it in reverse?
As for temp and pressure - I was just supplying what info I had from the material balance. Unfortunately, the pressure of the equivalent liquid barrels wasn't documented. I'm guessing it was set to some standard condition.
1. I thought this was Chemical Engineering forum and I'm a chemical engineer, seemed logical at the time... is there a better forum i should have used? And I guess I haven't looked at the different forum options, as I think I've always ended up in this forum when I've searched topics over the...
it should be 100% vapor at this point. I am looking at the equivalent liquid volume after it's completely condensed. But yes, there is some propane, n- butane, iso-pentane in the mixture. I'm just trying to see if i conceptually have the math right, so I can apply it to actual process...
So I'm new to the oil and gas field, having been in more of a non-technical and unrelated industry for the past 20+ years. So, I'm pretty rusty!
I have a M&E balance for hydrocarbon stream where I'm trying to confirm the calculations to convert a vapor stream to nominal liquid barrels/day...