| dc.contributor.author |
Mountzouris, K |
en |
| dc.contributor.author |
Gilmour, S |
en |
| dc.contributor.author |
Grandison, A |
en |
| dc.contributor.author |
Rastall, R |
en |
| dc.date.accessioned |
2014-06-06T06:43:53Z |
|
| dc.date.available |
2014-06-06T06:43:53Z |
|
| dc.date.issued |
1999 |
en |
| dc.identifier.uri |
http://dx.doi.org/10.1016/S0141-0229(98)00093-3 |
en |
| dc.identifier.uri |
http://62.217.125.90/xmlui/handle/123456789/1531 |
|
| dc.subject |
Cell Membrane |
en |
| dc.subject |
Empirical Model |
en |
| dc.subject |
Enzyme |
en |
| dc.subject |
Membrane Reactor |
en |
| dc.subject |
Response Surface Methodology |
en |
| dc.subject |
Dextrose Equivalent |
en |
| dc.title |
Modeling of oligodextran production in an ultrafiltration stirred-cell membrane reactor |
en |
| heal.type |
journalArticle |
en |
| heal.identifier.primary |
10.1016/S0141-0229(98)00093-3 |
en |
| heal.publicationDate |
1999 |
en |
| heal.abstract |
The aim of this study was to investigate the types of oligodextrans that could be generated via controlled enzymatic depolymerization of dextran using an endodextranase. An ultrafiltration stirred-cell membrane reactor was employed to provide the means of controlling product molecular size and characteristics. The process was operated in batch mode and the products were recovered as permeates. The effect of |
en |
| heal.journalName |
Enzyme and Microbial Technology |
en |
| dc.identifier.doi |
10.1016/S0141-0229(98)00093-3 |
en |