Removal of methyl tert-butyl ether from water by pervaporation: bench- and pilot-scale evaluations.

The ability of pervaporation to remove methyl tert-butyl ether (MTBE) from water was evaluated at bench and pilot scales. Process parameters studied included flow rate, temperature, MTBE concentration, membrane module type, and permeate pressure. Pervaporation performance was assessed based on the calculated mass transport coefficient of MTBE, the single-pass removal of MTBE (only at the pilot scale), and the fluxes of water and MTBE. The observations for MTBE are compared to results for toluene and 1,1,1-trichloroethane, compounds for which removal by pervaporation has been demonstrated. MTBE removal and mass transfer coefficients were lower than for toluene and trichloroethane. However, MTBE removal efficiency improved significantly with increasing process temperatures from 40 to 80 degrees C. With one of the pilot-scale systems, MTBE removal efficiency approached that of the other VOCs. The observed response of pervaporation performance to temperature was attributed to the strong effect of temperature on the Henry's law constant of MTBE.

Field demonstration of pervaporation for the separation of volatile organic compounds from a surfactant-based soil remediation fluid.

As part of a Department of Defense project, the US Environmental Protection Agency was responsible for designing, building and field operating a pilot-scale pervaporation unit. The field site was an active dry cleaning facility on the grounds of Marine Corps Base Camp Lejeune in Jacksonville, NC. The overall goal of the project was to remove tetrachloroethylene (PCE) from the soil beneath the dry cleaning shop using a surfactant-based soil remediation fluid and to recycle/reuse the surfactant. In order to reinject the recovered surfactant, the pervaporation unit was required to achieve an average 95% removal of contaminants from the extracted fluid over the duration of the test period. PCE removal averaged 95.8% during peak surfactant levels and exceeded 99.9% in the absence of surfactant, thereby meeting the reinjection requirement. Removal of a group of secondary contaminants at the site, termed Varsol compounds, was monitored via concentrations of three Varsol marker compounds: decane, undecane and 1,3,5-trimethylbenzene. The pervaporation system processed 100,000 gal of groundwater and surfactant solution over a period of 70 days. In order to evaluate and validate process performance, a variety of process variables and properties were monitored over the course of the demonstration. Pervaporation costs are projected to be on the order of $20 per 1000 gal of surfactant solution treated for a moderate size system (10 gpm).