A membrane-assisted solvent extraction (MASX) system coupled to a memb
rane-assisted distillation stripping (MADS) system for use in decontam
inating ground-water is evaluated. Volatile organic compounds (VOCs) i
n the groundwater are extracted in the MASX unit using a sunflower oil
solvent. In the MADS unit, VOCs are stripped from the sunflower oil,
which is recycled to the MASX unit. Thermodynamic data for the sunflow
er oil-water-VOCs system were measured. The results were used along wi
th published membrane mass-transfer data to design MASX and MADS modul
es.