Reverse osmotic concentration of aqueous ε-caprolactam solutions was carried out using composite membrane PEC-1000 supplied from Toray Co. Ltd. Separation of ε-caprolactam and flux through the membrane were measured under the following conditions : concentration of ε-caprolactam, 2.5, 5.0, 10.0 and 14.5wt%, operating pressures, 3.9, 5.5 and 6.9 MPa. Measured separations were always above 99.9%. Mass transfer coefficients on the surface of the cell used were measured using electrochemical method.
An analysis of the data with Spiegler-Kedem's transport model shows that the values of reflection coefficient σ, solute and hydraulic permeabilities ω and
LP were 1.0, 3.86×10
-13 and 5.29×
-8 mol/ (m
2. Pa.s), respectively.
Energy and membrane area required were calculated to concentrate dilute ε-caprolactam solutions by reverse osmosis. The energy per one kilsgram of the concentrated ε-caprolactam is inversely proportional to the initial concentration ofε-caprolactam and independent on the final concentration, and found 0.0565, 0.079 and 0.113 kWh/kg ε-caprolactam at 5, 7 and 10 MPa respectively to concentrate upto 20wt% from 2.5wt%.The area is inversely proportional to the operating pressures, and found 0.16, 0.10 and 0.06 m
2/ (kg ε-caprolactam/day) for 5, 7 and 10 MPa, respectively.
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