Dear experts,
We are LPG producer and we are planning to import LPG from other producers to increase our LPG market share.
However, LPG produced by other producers in the region contains H2S up to 10 ppm wt and Total Sulfur up to 40 ppm wt, that leads to the copper strip corrosion failure...
Dear Experts,
I am a junior process engineer. I would like to calculate the quantity of odorant needed to add to LPG (C3+C4)
Could you help me out please?
I did search on google, but I could find it nowhere
Thank in advance for your answers
Lee
In natural gas production, the wet gas coming to the processing plant is in the retrograde region ( in our plant, the natural gas is coming at 109 bar ). I would like to understand why 109 bar but not 130 bar or 100 bar.
Here is my thought: The presence of liquid phase may impair the velocity...
Hi all,
I would like to ask you what happen to a slug catcher ( finger type ) when it is operated at higher (or lower) pressure ? Is the separated liquid lower than normal operation ?
Thank you for your help
Hi everyone,
I am working on thermal couple column simulation.
While simulating a Petlyuk column, I face up to a problem.
The pre-fractionator has neither reboiler nor condenser, then the first time when the multicomponent feed is introduced to this column, the separation doesn't occur since...
