First carry out hydraulic run for the internals.
Check for % flooding.
You may need to change the internals of the column in case of excessive flooding.
At bubble point the liquid starts to boil so there is no change of temperature, at the dew point the vapors starts to condense. But why is the bubble point temperature differs from the dew point temperature. When phase changes there is no change of temperature but why is there a difference...
MMA DMA and TMA all are reversable reactions, it is impossible to have only DMA. They are all parellel reactions, it is possible to supress the formation of MMA and TMA by keeping there concentration high in the reactor, so that DMA formation is favoured that is why after separation of DMA using...
Does the size of the reactor (catalyst weight) needs to be changed if we want to change the feed.
Initially only fresh reactants were charged but now since the products forms not only the desired product but also undesired products as well, so I want to recycle back the undesired products but...
I want to calculate noise level and wearing of PCV with a nominal pipe dia of 2 in, valve size is 1 in and valve body is 0.375 in.
The process conditions are:
Pressure: 50Psig
Drop through valve: 15 psi
Flow: 310 lb/hr
Mol. Wt.: 57
Temp: 250 F
Please provide me the details to check this valve...
I have a case in which I know specific gr. (std conditions) of gas is 1.87
I know the density of gas at 100 Psig = 0.67 lb/ft3
Density of air at STP is = 0.0749 lb/ft3
So, actual specific gr. is = 0.67/0.0749 = 8.94
The gas is so heavy!
I want to know how can we express specific gravity for gases at actual conditions.
Is it density of gas/density of air at STP
or
Is it density of gas/density of air at that pressure and temperature
Please clarify.