We present exptl. results on the liq.-side mass transfer characteristics of a structured packing (Mellapak). We have measured the product of the liq.-side mass transfer coeff. kL and the effective specific area ae by the NTU-HTU method in a column of 0.295 m internal diam. The column was operated in counter-current, O from a satd. water stream being stripped into air. In order to elucidate the effect of the specific area, we report results on 3 different packing types of specific geometric areas of 125, 250 and 500 m3/m2 (Mellapak 125.Y, 250.Y and 500.Y, resp.). The dependence of kLae on liq. load and gas velocity is qual. similar to that of random packings. Quant., however, the values of kLae for the structured packings studied in this wor...
Optimization of industrial gas-liquid columns dedicated to CO2 capture requires prediction of liquid...
This paper presents the results of a study carried out to examine the effective mass transfer area o...
AbstractPacked towers are common as gas/liquid contacting units for separation processes. Several st...
textThe mass transfer area of nine structured packings was measured as a function of liquid load, su...
The effective mass-transfer efficiency in a column equipped with structured packings was investigate...
AbstractThe effective mass transfer area (ae) of three structured packings (Mellapak 250Y, Mellapak ...
The impact of the Sulzer SMV 16 packing elements on mass transfer characteristics in a packed column...
The effect of liquid viscosity (μ<sub>L</sub>) on the effective mass transfer area (<i>a</i><sub>e</...
The mass transfer characteristics of 3·5, 7·3, 10·16 and 15·6 cm i.d. packed liquid—liquid extractio...
The effective mass transfer efficiency in a column equipped with structured packings was investigate...
The effective mass transfer area (a [subscript e]), liquid film mass transfer coefficient (k [subscr...
AbstractThree mass transfer properties: the effective area (ae), liquid film and gas film mass trans...
An increasing number of heterogeneous reactive separation processes is being investigated also favou...
This paper presents an experimental procedure and an extended modelling analysis aimed to characteri...
The theory of gas absorption accompanied by fast pseudo-mth order reaction was used to obtain values...
Optimization of industrial gas-liquid columns dedicated to CO2 capture requires prediction of liquid...
This paper presents the results of a study carried out to examine the effective mass transfer area o...
AbstractPacked towers are common as gas/liquid contacting units for separation processes. Several st...
textThe mass transfer area of nine structured packings was measured as a function of liquid load, su...
The effective mass-transfer efficiency in a column equipped with structured packings was investigate...
AbstractThe effective mass transfer area (ae) of three structured packings (Mellapak 250Y, Mellapak ...
The impact of the Sulzer SMV 16 packing elements on mass transfer characteristics in a packed column...
The effect of liquid viscosity (μ<sub>L</sub>) on the effective mass transfer area (<i>a</i><sub>e</...
The mass transfer characteristics of 3·5, 7·3, 10·16 and 15·6 cm i.d. packed liquid—liquid extractio...
The effective mass transfer efficiency in a column equipped with structured packings was investigate...
The effective mass transfer area (a [subscript e]), liquid film mass transfer coefficient (k [subscr...
AbstractThree mass transfer properties: the effective area (ae), liquid film and gas film mass trans...
An increasing number of heterogeneous reactive separation processes is being investigated also favou...
This paper presents an experimental procedure and an extended modelling analysis aimed to characteri...
The theory of gas absorption accompanied by fast pseudo-mth order reaction was used to obtain values...
Optimization of industrial gas-liquid columns dedicated to CO2 capture requires prediction of liquid...
This paper presents the results of a study carried out to examine the effective mass transfer area o...
AbstractPacked towers are common as gas/liquid contacting units for separation processes. Several st...