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diameter column operated in the churn turbulent regime.
These controllers were implemented in a pilot-scale column operated in a water-air system.
bubble column operated in the pressure range of 0.1 0.5 MPa.
On the contrary, the 2-D spiral column operated on the same CCC device lacks this third-dimensional mixing force.
Experiments were carried out in a bubble cap distillation column operated at total reflux with the system: water ethanol methylacetate.
Experiments were carried out in an airlift loop reactor and a bubble column operated in two- and three-phase mode.
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Experiments were conducted in a 101.6 mm diameter column operating at pressures up to 9.0 MPa.
The new technique employs a continuously fed column, operating at steady state.
The column operates at 160 °C with 1-decanol as sample solvent and mobile phase.
Experiments were conducted in a 101.6 mm diameter column operating at pressures up to 6.5 MPa.
A control study of a four-product extended Petlyuk column operating close to minimum energy is reported here.
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