Abstract:
:Downstream processing operations are often carried out blind in the process timescale since product monitoring on-line is not common. Knowledge of the location and concentration of the product and key contaminants is complementary to other process information for process development and, if available on-line in conjunction with a suitable model, control. This article sets out to demonstrate a model describing a two-cut fractional protein precipitation process and how this may be used for control of the process to maximize yield in the face of variable process stream conditions. Estimation of the model parameters is achieved by means of data-fitting by least squares and in comparison prediction by a Kalman filter algorithm. A description and error analysis of equipment for at-line monitoring of the soluble product in a pilot plant environment is presented which includes a micro-centrifuge necessary to clarify small volumes of sample prior to analysis. Finally, an account of the successful implementation of this equipment and the Kalman filter algorithm for control at bench scale is given where conditions in the process stream are deliberately disturbed to test the control operation. (c) 1997 John Wiley & Sons, Inc.
journal_name
Biotechnol Bioengjournal_title
Biotechnology and bioengineeringauthors
Holwill IJ,Chard SJ,Flanagan MT,Hoare Mdoi
10.1002/(SICI)1097-0290(19970105)53:1<58::AID-BIT9subject
Has Abstractpub_date
1997-01-05 00:00:00pages
58-70issue
1eissn
0006-3592issn
1097-0290journal_volume
53pub_type
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