AbstractThe effective mass transfer area (ae) of three structured packings (Mellapak 250Y, Mellapak 500Y, and Flexipac 1Y) was measured via chemical absorption in a 0.427 m ID column as a function of liquid load (1–30 gpm/ft2 or 2.4–73.2 m3/m2.h), liquid viscosity (1−−15 mPa.s), and surface tension (30–72 mN/m). Viscosity had no effect and surface tension had only a weak effect on the effective area. The ratio of effective area to specific surface area (ae/ap) was correlated as a function of the liquid Weber and Froude numbers within limits of ±15% for the entire experimental database: aeap=1.362[(WeL)(FrL)−1/3]0.122
The mass transfer characteristics of 3·5, 7·3, 10·16 and 15·6 cm i.d. packed liquid—liquid extractio...
The gas–liquid mass transfer coefficient and other hydrodynamic parameters such as liquid holdup and...
An increasing number of heterogeneous reactive separation processes is being investigated also favou...
textThe mass transfer area of nine structured packings was measured as a function of liquid load, su...
The effect of liquid viscosity (μ<sub>L</sub>) on the effective mass transfer area (<i>a</i><sub>e</...
We present exptl. results on the liq.-side mass transfer characteristics of a structured packing (Me...
The effective mass-transfer efficiency in a column equipped with structured packings was investigate...
The effective interfacial area for chemical absorption in a laboratory column has been reported to b...
AbstractThere are many correlations of liquid phase mass transfer coefficient (kL) for packings in t...
In this investigation attention has been paid to the influence of surface tensions gradients on the ...
The correlations available in the literature cannot be used to est. the liq.-phase mass-transfer coe...
The effective mass transfer area (a [subscript e]), liquid film mass transfer coefficient (k [subscr...
The effect of liquid viscosity (μL) on liquid film mass transfer for packings was investigated in a ...
The effective mass transfer efficiency in a column equipped with structured packings was investigate...
AbstractPacked towers are common as gas/liquid contacting units for separation processes. Several st...
The mass transfer characteristics of 3·5, 7·3, 10·16 and 15·6 cm i.d. packed liquid—liquid extractio...
The gas–liquid mass transfer coefficient and other hydrodynamic parameters such as liquid holdup and...
An increasing number of heterogeneous reactive separation processes is being investigated also favou...
textThe mass transfer area of nine structured packings was measured as a function of liquid load, su...
The effect of liquid viscosity (μ<sub>L</sub>) on the effective mass transfer area (<i>a</i><sub>e</...
We present exptl. results on the liq.-side mass transfer characteristics of a structured packing (Me...
The effective mass-transfer efficiency in a column equipped with structured packings was investigate...
The effective interfacial area for chemical absorption in a laboratory column has been reported to b...
AbstractThere are many correlations of liquid phase mass transfer coefficient (kL) for packings in t...
In this investigation attention has been paid to the influence of surface tensions gradients on the ...
The correlations available in the literature cannot be used to est. the liq.-phase mass-transfer coe...
The effective mass transfer area (a [subscript e]), liquid film mass transfer coefficient (k [subscr...
The effect of liquid viscosity (μL) on liquid film mass transfer for packings was investigated in a ...
The effective mass transfer efficiency in a column equipped with structured packings was investigate...
AbstractPacked towers are common as gas/liquid contacting units for separation processes. Several st...
The mass transfer characteristics of 3·5, 7·3, 10·16 and 15·6 cm i.d. packed liquid—liquid extractio...
The gas–liquid mass transfer coefficient and other hydrodynamic parameters such as liquid holdup and...
An increasing number of heterogeneous reactive separation processes is being investigated also favou...