Internal circulation in the gasoline-diesel fractionation double tower?
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I would like to ask fellow users: while dealing with the reduction in output caused by faults in the gasoline/diesel combustion reaction system! The distillation twin towers need to have their internal circulation modified in order to maintain the heat required for distillation while waiting for operation to begin. Specifically, how should the internal circulation of these twin towers be altered? Do the reflux pumps of the stripping tower and distillation tower still need to be running? Additionally, if a single-tower cycle is required, what kind of single-tower process would that be? Thank you for the advice! ! !
Didn’t the colleagues discuss it? My question
It depends on the process design, I guess? Different design schemes will not be the same.
It depends on the process design, I guess? Different design schemes will not be the same.