I am working on a crude oil tank heating system which will be used to keeping the crude oil temperature not drop down because of the heat loss to Ambient. The heat loss through the tank wall at the coldest date had been calculated to be about 1 MMBtu/hr. The shell and tube type Glycol/Crude heat...
I had charatered the oil by using hysys. The result shows at 40C which is the temperature I was told the crude will be trucked in, the viscosity of the oil is about 2100cp. Does anyone has the experience on handling such high viscosity oil? Is this oil capable to flowing at this temperature...
Is anyone have a experience for designing an Glycol/Water heat Tracing Jacket system and know the typical length of the jacket could be?
I am in the processing of designing an glycol jacket heat tracing system to keep the sulfur line temperature above 138 degC. The sulfur line will be at least...
Are there any criteria for the dip angle of Valved Tray Distillation Tower Design? What is the tolerable limit which still allowing the tower working normally?
Our case is that a 90ft high 36 traies depropanizer tower is inclined a little bit. The head of the tower moved 3in after it is built...
Hi,
I am just working on an sour gas treating project.The problem is the inlet sour gas is under very low pressure situation (65psig @120F)and the composition of the gas is also light ( the heavist component is C3).I am not confident for this simulation, Although I can run it using Hysis. Did...
