Hello, and thanks for your time and feedback.
I am recent graduate working on design of a compressor station that will compress and dehy well gas for entry to a pipeline.
I have simulated the process in HYSYS and after saturating with water, separation, compression, cooling, and the dehydration...
I am a recent graduate.
I am sizing some PSVs for a natural gas compressor station.
On the spec sheets the vendor gave me it asks for Oper. Sp. Gr.
Since HYSYS is not giving me a SG in the properties tab (other than the petroleum SG(60/60) which I am not sure what this is.
The MW of the gas is...
Thanks for the input.
SandCounter-
Would the concern for shear come from the viscosity?
What would be a concern regarding high shear?
The viscosity = .09019cP = 6.06*10^-5 lb/s*ft.
I am currently looking into the pressure surge that Little Inch stated. I assume the first step is to see if I...
Sorry about that,
I also posted this yesterday in the wrong area, and I believe it was deleted after a couple of responses were posted.
So I never got to see the responses.
Thanks for the help.
Fluid Velocity In Pipe
I am trying to determine if we need an additional pipe installed. Is our six inch pipe adequate to handle increased flow? At a cryo gas plant the NGL products are run to metering through a six inch pipe with inside diameter of 5.76 inches. This pipe only runs about 1000ft...
I am a first year chemical engineer
I am to estimate the amount (mass) of liquid and vapor in a number of vessels. Here are two examples:
1. I don't have the numbers yet, but was wondering about how best to estimate the mass of ethane and ethylene in our C2 splitter.
I was told that...
