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Dear Friend igot some tips from my collgs bumping is mainly due to High volume and low boiling liquid so during initial stage of vac distillation switch off the stirrer maintain relatively low tempt once substatial amount of solvent got distilled u can increase the tempt As u know water itself...

Dear Friends Wish u very happy new year i got one ? i am using H2 Cylinder 51 inch height 9 inch dia pressure 125 kg/cm2 g i am using hydrogen for my process at 50 kg/cm2 i stopped the hydrogen. is it possible to calc the remaining hydrogen amount with this data. i don't know the cylinder...

Dear jsummerfield mine is pharma not oil and gas but ur suggestion regarding equipment trouble shooting will be very helpful to me thanks for ur suggestion dear subhi i am monitoring now process tempt,pressure vs time & amps . mine involve reactor , scrubber(packed bed), centrifuge and FBD...

Dear friends I got Rupture disk of rating 4.8kg/cm2 g at 60 deg c can u able to tell me how to calc the bursting condition at other condition. like at atm at what tempt it will burst or at various pressure? regards K Madhavan K Madhavan

Dear Friends Thanks lot for your replies. In my plant i like to calc utility flow rate i got Pressure gauges in utility inlet and outlet of the reactor. i want to calc the flow rate of the utility. I just thought that if i got any correlation between pressur and velocity i can just calc...

Dear Friends Can u able to give me general guide lines for process monitoring. K Madhavan

Dear friend Is there any relation between pressure and velocity i like to know using line pressure is it possible to calculate velocity of the fluid. i got following data line pressure,line size, fluid property . velocity ? regards K Madhavan K Madhavan