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No contamination of distillate with saline water was experimentally detected in the single distillation cell, and the experimental observation of the wick and the measurements of the temperature drop through the cell with the 5-mm gap showed that dry patches hardly appear on the wick.
A single distillation cell with a 5-mm diffusion gap between vertical partitions has been experimentally explored.
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Analyte transfer from the matrix in a thin layer distillation (TLD) cell and its subsequent measurement were investigated in a flow injection configuration.
The concentrated syrup is combined with the solid cake from the distillation bottoms, biogas and cell mass (sludge) obtained from wastewater treatment and this is fed to the combustor (Area G) for combined heat and power (CHP) generation.
In this paper we develop a generic, dynamic, nonequilibrium (NEQ) cell model for reactive distillation (RD) tray columns.
Solid oxide fuel cell systems integrated with a distillation column (SOFC-DIS) have been investigated in this study.
The concentrated syrup and solid cake from the distillation is combined with the biogas and cell mass (sludge) from wastewater treatment to be fed to the combustor (Area G) for Combined Heat and Power (CHP) generation.
Morpholinos were dissolved in double distillation water and injections performed at the 1 4 cell stage, using standard techniques previously described (32, 34).
A solvent recovery system using short path distillation was also developed for installation in hot cells.
Heat and mass transfer in direct contact membrane distillation (MD) has been analyzed by using a specifically designed cell.
In this paper we develop a nonequilibrium (NEQ) cell model to describe the dynamic operation of reactive distillation (RD) tray columns.
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