Recent content by gegio1960

Just for relax.... ;-) Assumptions: 1) line w/o fittings/curves 2) liquid @ SG=1 & visc = 1 cp Answer: yes, about 120 m3/h

in case of liquid there could be no flow....

I repeatedly observed that behavior, mainly in managers but also in young engineers with ambitions and "managerial skills"..... it is not a matter of Alzheimer or other mental disease.

Dear all, do you have practical experiences in the application of test methods for the analysis of Total Sulphur in diesel / kerosene / gasoline products when the concentration is under 10 ppm by weight? The following list includes ASTM methods theoretically applicable in this very low range...

25362, Thanks for your answer but my question is more general. I red that definition on a gasoil specification where it is normally used something like - cleveland open cup - abel pensky - pensky martens - tag Could someone give other help? Thanks

Hi.... did you ever heard of a "chevron flash point"? If yes, could you kindly give its definitions? Thanks

Generally speaking you will have problems to meet the purity spec on the btm product. Anyway you could avoid big troubles by using other possible operating margins. For example: - reduce the capacity - increase the stripping duty - take benefit of margins in the downstream plants, if any, where...

C4Reactor, it could be useful to know the column service and where the damaged trays are located. B-)