Js. Smith et al., BUBBLE-COLUMN REACTORS FOR WASTE-WATER TREATMENT .1. THEORY AND MODELING OF CONTINUOUS COUNTERCURRENT SOLVENT SUBLATION, Industrial & engineering chemistry research, 35(5), 1996, pp. 1688-1699
Solvent sublation is a nonfoaming wastewater treatment process that co
mbines the benefits of bubble fractionation and liquid-liquid extracti
on in a way that does not require mixers, settlers, or subsequent down
stream treatment. A review of past work on small lab-scale batch colum
ns revealed that removal efficiencies of nonvolatile and volatile orga
nic compounds are generally higher than those observed in bubble fract
ionation, air stripping, and conventional liquid-liquid extraction. In
this work, the first of a three-part series, the transport mechanisms
in a three-phase continuous, countercurrent sublation process are pre
sented. Two mathematical models, namely, the series CSTR model (SCM) a
nd the two-phase axial dispersion model (ADM2), are developed. It is s
hown that these two models are equivalent and can be used interchangea
bly with the aid of a simple expression. Nondimensional correlations,
based upon simulated data obtained from the SCM, are generated to pred
ict the steady-state fractional removal, FR, and the separation factor
, Sigma (ratio of effluent solvent concentration to effluent water con
centration), for strongly hydrophobic compounds, The effects of operat
ional, hydrodynamic, thermodynamic, and design variables on sublation
performance are discussed.