Hello experts,
What criteria (volume/pipeline dia/?) should be utilized to make the filters/strainers vessels as a Piping component. The intent here is to avoid safety valve for fire case or blocked in case by avoiding pressure vessel. Following are more details regarding proposed strainer...
Hello Experts,
how to calculate heating value at flare during equipment steam out operation. We have been observing flame-outs at flare during steam-out step in plant shutdown. Lowering the heating value below desired value (300 btu/scf or 12 MJ/m3) is probably cause for the same.
How to...
Hi gr2vessels,
Our feed to the furnace is diluent bitumen (mineral conten ranges from 0.4 to 0.8%). Furnace is having 6" tubes and we are heating the feed from 550 to 650 F (approx vaporization of 15%). Let me know if you need more details.
Thanks
Dear friends,
I would like to know about the generalization most oil industries use for accounting erosion problems in furnace tubes. In other words how do you quantify the erosion index in furnace tubes, currently we are using product of mineral content in the feed and squared tube velocity...
Hello Experts,
In our plant shut-down, we are facing problmes dealing with NORM (Naturally occuring radioactive materials). We are finding NORMS because of lead (Pb) salts in the rust(magnetite) scale on the shell of fractionator (distillation column). I'd really appreciate if someone can...
Hi, I need to model the gas flow across ID fan, i have datas of temp and pressure at the inlet and outlet of fan and also power datas for fan. typical values for pressure is -2kpa at suction and +3kpa at discharge of ID fan.
