 | Cutting hydrogenation times in half |
| Decreasing the batch time of a polymerization from 12 hours to under 1
hour with a resulting purer product |
| Doubling the throughput of a fermentation |
| Increasing kLa by 100% without a new motor and gearbox |
| Switching to a solvent based reaction, increased production rate from a
mere 5 kg/day to an excess of 1000 kg/batch |
| Reverse order of addition of components eliminated the need of a very
costly mixing system |
| Improving the mixing reduced the leaching time of a precious metals plant
from 1 week to less than 1 day |
| Decreased the entrainment of solvents in solvent extractions of mining
operations from several percents to about 10 ppm |
| Increased the throughput in PTA plants by decreasing the solids build up
in the reactors |
| Dramatically decreasing the mixing time by merely readjusting the position
of the impeller for a portable mixer installation |
| Doubling the heat transfer capacity of a tank by changing the location of
heat transfer surfaces |
| Decreasing dead zones in a high viscosity solution increased yields,
reduced unwanted impurities, and kept the temperature of the solution within
± 1 degree |
| Predicted conditions for reaction extinction for a high pressure, high
temperature oxidation in a horizontal tank |
| Achieved a uniform droplet size distribution by making minor design
changes to an inline mixing device |
| Optimized dissolution times of floating solids by implementing up-pumping
technology |
