Recent studies have found that coal macerals have properties which may
allow their use as high-valued products. A conceptual approach for th
e production of individual maceral concentrates utilizing column flota
tion is presented in this publication. Before maceral separation, the
coal was ground to the particle size corresponding to near complete li
beration of the macerals, which was approximately 4 mu m for an Illino
is No. 6 seam coal. The production of maceral concentrates using flota
tion was based on the differences in the flotation rates among the var
ious macerals, which was manipulated by adjustment of the medium pH. A
n increase in pH from 8 to 11 resulted in an order of magnitude reduct
ion in the flotation rate of the liptinite maceral group while the cor
responding reduction for the inertinite group was about 50%. On the ot
her hand, the kinetic rate for the vitrinite group remained unchanged.
4, using pH control and column flotation, the inertinite content was
increased from 7.5% to 50%. Although the upgrading of the other two ma
ceral groups was not as significant, it was evident that the success o
f the maceral enrichment for a given coal is dependent on the maceral
liberation characteristics and the magnitude of the flotation kinetic
rate differences among the macerals.