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A packing type is determined from the porosity (see Table 2).
Recently, a new structured packing type coated with a thin alumina layer (KATAPAKTM) has been developed.
It is affected by packing type, CO2 concentration in flue gas, capture level and solvent type (Kothandaraman et al. 2009).
In this work, there is described a design supporting tool for pre-selection of packing type for RD column.
Among the absorbent studies, the overall mass transfer coefficient was used as a key data for design packing type and absorber height to achieve cost effective process.
In that pilot plant the closed cycle of the absorption/desorption process is continuously operated (column diameters: 0.125 m, absorber/desorber packing height: 4.2/2.5 m, packing type: Sulzer Mellapak 250.Y™, flue gas flow rate: 30 110 kg/h, CO2 partial pressure: 35 135 mbar, solvent flow rate: 50 350 kg/h).
Similar(52)
Packed column design is presented with comparison of available packing types.
Currently however, different vendor supplied design tools predict different results for some very similar packing types.
Good agreement is found between measured and simulated results for both packing types.
The relationship between the packing types and the concentration of TiO2 nanorods and oleic acid has been established.
A new development in the field of internals in packed columns is the use of structured packing types.
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