๐”– Bobbio Scriptorium
โœฆ   LIBER   โœฆ

Use of a batch-stirred reactor to rationally tailor biocatalytic polytransesterification

โœ Scribed by Billie J. Kline; Smita S. Lele; Philip J. Lenart; Eric J. Beckman; Alan J. Russell


Publisher
John Wiley and Sons
Year
2000
Tongue
English
Weight
189 KB
Volume
67
Category
Article
ISSN
0006-3592

No coin nor oath required. For personal study only.

โœฆ Synopsis


Despite favorable thermodynamics, highmolecular weight and low-dispersity polyesters are difficult to synthesize biocatalytically in organic solvents. We have reported previously that the elimination of solvent can improve the kinetics and apparent equilibrium significantly (Chaudhary et al., 1997a). We now present the design and use of a batch-stirred enzyme reactor to control the biocatalytic polymerization. Using the reactor, polyester having a molecular weight of 23,400 Da and a polydispersity of 1.69 was synthesized in only 1 h at 60ยฐC. Additional factors like enzyme-deactivation kinetics, enzyme specificity, and initial exothermicity were investigated to develop a better understanding of this complex reaction system.


๐Ÿ“œ SIMILAR VOLUMES


The Role of Mass Transfer in the Kinetic
โœ N.K. Amin; S.A. Nosier; M.S.M. Hassan; G.H. Sedahmed ๐Ÿ“‚ Article ๐Ÿ“… 2004 ๐Ÿ› John Wiley and Sons ๐ŸŒ English โš– 137 KB

## Abstract The kinetics of chemical oxidation of anthracine powder by acidified dichromate in a batch agitated vessel stirred by a 45ยฐ four pitched blade turbine impeller was studied under different conditions. Variables studied were impeller rotation speed, solution physical properties and temper