dehydratase was unchanged by the detergent treatment, but this step was necessary to remove lipid vesicles. The 12,000 x g centrifugation that followed the detergent treatment resulted in a decrease in the specific activity of diol dehydratase. Table 4-1. Diol dehydratase activity during organelle purification Protein Activity Specific Fold Sample (mg) (U)a activity Yield () purification (U/mg) Crude extract 500.0 1,346 2.7 100.0 1.0 Detergent/salts 370.6 1,000 2.7 74.3 1.0 treatment 12,000 x g 357.0 573 1.6 42.6 0.6 super 48,000 x g 9.4 194 20.8 14.4 7.7 pellet 12,000 x g 7.0 195 27.9 14.5 10.3 super Sucrose density 0.6 16 27.5 1.2 10.2 gradient aOne unit activity is defined as the amount of enzyme that catalyzes the formation of 1 [tmol of propionaldehyde per min per mg protein. However, this step was needed to remove aggregates, which included many organelles that were not released from vesicles by the detergent treatment. Following aggregate removal, the polyhedral organelles were pelleted by centrifugation at 48,000 x g, resuspended in buffer, and clarified by a second centrifugation at 12,000 x g. These two steps proved very effective and increased the specific activity of diol dehydratase from 1.6 to 27.9 [tmol/min/mg. The final sucrose density gradient step typically resulted in a slight drop in the specific activity of diol dehydratase (Table 4-1). The reason is uncertain. It may have been due to removal of an unknown factor that enhances diol dehydratase activity or due to partial enzyme inactivation. For the complete purification, the specific activity of diol dehydratase increased approximately 10-fold, from 2.7 to 27.5 [tmol/min/mg protein (Table 4-1). This indicates