Technologists at our chemical plant have an idea to storage liquide white phosphorus in concrete basin (instead of stainless steel tank). Principle is to store liquide phosphorus at 70-80 C deg under demineralized water blanket to prevent contact it with air (oxygen). Now I’m trying to find any...
Typical natural gas treatment plants (removing H2S, CO2 and H2O) work with pressure 10 MPa or less. Have you met plants designed for higher pressure (15 - 20 MPa)? If exist, what disadvantages they have?
Hi
After the first mechanical separation I want to use turboexpanders for expansion natural gas in LTS (Low Temp. Separation). This is condensate gas (even C35+ are present). During expansion higher HC will condensate inside turboexpander. Can HC droplets cause damage? If it's no problem I want...
Hi,
I'm young process engineer and I work for design office in gas industry. I use ChemCAD simulator. My problem: I want to simulate compressor for natural gas in ChemCAD. Program gives me two model to choose - adiabatic and polytropic compression. I'm creating now simualtion of underground gas...
