An electrochemically modulated complexation (EMC) process was designed
to selectively extract and concentrate ethylene from a feed-phase mix
ture with ethane. Unlike previous EMC processes, where the separation
was based on equilibrium solubility differences, this separation was b
ased on differences in the rate of complexing with copper(I) solution
between the two gases. The EMC process employed flow through electroly
sis cells that electrochemically modulate aqueous-phase copper chlorid
es between high, copper(I), and low, copper(II), affinity states. The
liquid phase in the high affinity form contracts a feed gas phase in a
hollow-fiber membrane module for selective extraction and contacts th
e receiving gas phase in the low affinity form for concentration. Expe
rimental results and modeling of the process are reported.