“…on the assumption of negligible heat losses. The general solution to Equation (1) is of the form For gas-liquid batch columns k, is known to be large, roughly in the order of 20,000 W/m -K (Chen and McMillan, 1982). If this is assumed also true for continuous columns, Equation (2) can be well approximated by a series expansion to yield (3) suggests that for sufficiently small values of Gcp/k,, the effective thermal conductivity in continuous bubble columns can be determined in the same manner as suggested previously for batch columns; that is,…”