S. Majumdar et al., A pilot-scale demonstration of a membrane-based absorption-stripping process for removal and recovery of volatile organic compounds, ENVIRON PR, 20(1), 2001, pp. 27-35
A new membrane-based continuous absorption-stripping process has been devel
oped to separate gas/vapor mixtures, such as volatile organic compounds (VO
Cs), from a nitrogen/air stream. Two different hollow fiber membrane module
s are needed in this process to remove the VOCs. In the first module, VOC-l
aden nitrogen/air stream flows through the bore of the hollow fibers. A sui
table absorbent liquid with a high solubility for the VOC and essentially n
o solubility for nitrogen/air is pumped countercurrently over the outside o
f the fibers. This liquid is an inert, nontoxic, and essentially non-volati
le, organic solvent. The VOCs are effectively removed from nitrogen/air to
a very low level and are concentrated in the absorbent for recovery, while
the absorbent is regenerated by heating and subjecting it to vacuum in a se
parate hollow fiber membrane module called the stripping module.
A pilot-scale membrane-based absorption-stripping unit was located next to
a paint spray booth at Robins Air Force Base, Warner Robins, GA. Tests were
performed on slip-streams of real-time air emissions from scheduled interm
ittent painting operations, so the concentration of VOC in the exhaust air
fluctuated with time. The VOC removal efficiency was determined as a functi
on of the feed air flow rate and the absorbent (silicone oil) flow rate. De
pending on the gas/liquid flow rates and the inlet VOC concentration, the p
rocess successfully removed as much as 95+% of the VOC present. The experim
ental results have been compared with theoretical predictions.