Dear all,
I am involved in designing vacuum catch pot to be installed in between batch distillation system(inclusing reactor, HEs, reflux pot , receivers etc.) & vacuum pump, to achieve reduction in solvent vapor going to vacuum pump.
I have read in the book "Rules of thumb" that such catch pots are jackettted having tangential entry & demister pad on top.
I have doubt that -
1)there will be vacuum drop due to tangential entry of vapor into catch pot .
2)demister will have some pressure drop which will result in poor vacuum at source.
Can anyone suggest me how to do process design of such catch pot?
system volume : 10 M3
Vacuum requirement: 40 torr during initial stage of distillation & full vacuum during Final degassing.
Vacuum pump: Once through oil lubrication rotary vane type(250 M3/Hr, 1 torr(g))
Vacuum: 1 torr(g) at vacuum pump
5 torr(g) at reactor
Solvent being distilled : Multiple solvents ( MeOH, EtOH,IPA, Methayl acetate,Ethyl acetate etc.)
Attachement: Vacuum catch pot schematic drawing for understanding & betterment if any.
Regards,
Hiren Dave
Vacuum catch pot schematic.pdf 37.91KB
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