How would you condensate the overhead product of a distillation vacuum column?
If a shell&tubes heat exchanger is used to condensate this flow would it be a problem dealing with the reduced pressure?
|
|
Posted 15 August 2019 - 07:55 PM
Pressure drop is a key parameter in vacuum condensers. Use design features that tend toward low pressure drops for vacuum shell side condensing such as baffles with maximum spacing and maximum cut. Or use double segmental baffles. Use large vapor nozzles. Use a generous tube pitch. Use large shells. Consider a J shell. Exchangers for vacuum condenser service need to NOT try to use all the pressure available as when designing for other services.
Gas-Liquid Pipe Flow Friction Loss CorrectionStarted by Guest_Huba_* , 18 Dec 2025 |
|
|
||
Flow & Pressure Regulation For Compressible FluidsStarted by Guest_Abdessamed1961_* , 14 Dec 2025 |
|
|
||
Calculating Gas Flow Rate Without CvStarted by Guest_worrier_* , 25 Nov 2025 |
|
|
||
Seeking Feedback On My Process Flow Diagram. Biogas Steam Reforming ToStarted by Guest_Jacobaum_* , 27 Oct 2025 |
|
|
||
Two-Phase Fluid Flow Through An OrificeStarted by Guest_frwvelandria_* , 13 Oct 2025 |
|
|