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Desalination 200 (2006) 477-479

Authors

Conclusion

It is technically feasible to use a two-stage ultrafiltration process with different membranes to extract lysozyme and ovalbumin from chicken egg white and to separate them into individual proteins with sufficient purity and product recovery. Selection of membranes and operational conditions is the key to success. Recovery Transmission x100 Parameters/100 Parameters/100 1.0 0.8 0.6 0.4 0.2 0.0 13.23 26.46 39.69 52.92 Flux (L/h m ) (a) Lysozyme purification 66.15 Purity Recovery 1.0 0.9 0.8 0.7 0.6 0.5 0.4 0.3 0.2 0.1 0.0 13.23 26.46 39.69 Flux (L/h 52.92 66.15 m2 ) (b) Ovalbumin purification Fig. 1. The transmission (t ), purity and the recovery of lysozyme and ovalbumin (conditions: 16 mL Permeate from stage 1, at pH 11.0, buffer: [NaCl] 200 mM, stirring speed 2100 rpm, 30 kDa PES membrane).

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