Optimization of the alkaline lysis (P2) and neutralization (N3) steps in the recovery of DNA plasmids was pursued. Experiments were conducted at the test-tube and 5-litre scales with 3 kb (pUC18) and 20 kb (pQR 150) plasmids. The scale and degree of mixing/shear did not affect the optimum yield of super-coiled plasmid during the P2 step, but did effect the time required for the optimum to be achieved. This optimum time for P2 at the large scale was longer (8-9 min), especially when a low-shear impeller was used. Also, when the yield of supercoiled plasmid reached a maximum during the P2 step, the purity (percentage of plasmids in the supercoiled form) simultaneously reached a minimum. As the duration of the N3 step increased from I to 6 min, the yield of the supercoiled plasmids remained fairly constant, provided that a low-shear impeller was used. The neutralized (post-N3) plasmid solution was shear-sensitive; however, mixing with a Rushton turbine in a tank (maximum energy dissipation rate in the mixing tank, epsilon(max), 12 m(2)/s(3); mixing-tank power consumption/volume of mixing tank, 2.0 W/m(3) for 5-10 min resulted in a slight decrease in supercoiled plasmid and a notable increase in genomic DNA concentrations. The loss of the larger 20 kb plasmid (20%) was more than for the 3 kb plasmid. Finally, preparing the cells for alkaline lysis with lysozyme or low-pressure homogenization did not increase the plasmid yield. Furthermore, the homo-genizer broke up the genomic DNA into fragments that followed through the entire Qiagen prep with the plasmids as impurities.