dc.contributor.author |
Marton, Gy |
en |
dc.contributor.author |
Kovacs, M |
en |
dc.contributor.author |
Oreopoulou, V |
en |
dc.contributor.author |
Koukios, EG |
en |
dc.date.accessioned |
2014-03-01T01:07:12Z |
|
dc.date.available |
2014-03-01T01:07:12Z |
|
dc.date.issued |
1988 |
en |
dc.identifier.issn |
0009-2509 |
en |
dc.identifier.uri |
https://dspace.lib.ntua.gr/xmlui/handle/123456789/9849 |
|
dc.subject |
biomass fractionation |
en |
dc.subject |
delignification by chlorination |
en |
dc.subject |
diffusion |
en |
dc.subject |
hemicellulose hydrolysis |
en |
dc.subject |
modeling |
en |
dc.subject.classification |
Engineering, Chemical |
en |
dc.title |
Modelling of biomass fractionation by prehydrolysis-delignification |
en |
heal.type |
journalArticle |
en |
heal.identifier.primary |
10.1016/0009-2509(88)87045-3 |
en |
heal.identifier.secondary |
http://dx.doi.org/10.1016/0009-2509(88)87045-3 |
en |
heal.language |
English |
en |
heal.publicationDate |
1988 |
en |
heal.abstract |
A two-stage process is investigated as a potential fractionation method for barley straw biomass. Modeling of dilute-acid prehydrolysis shows that hemicellulose saccharification rate is controlled by chemical reaction; in the case of delignification of the prehydrolyzed residue by high-consistency clorination, the rate-controlling step is diffusion of chlorine through the layer of the reacted material. © 1985. |
en |
heal.publisher |
PERGAMON-ELSEVIER SCIENCE LTD |
en |
heal.journalName |
Chemical Engineering Science |
en |
dc.identifier.doi |
10.1016/0009-2509(88)87045-3 |
en |
dc.identifier.isi |
ISI:A1988P663100009 |
en |
dc.identifier.volume |
43 |
en |
dc.identifier.issue |
8 |
en |
dc.identifier.spage |
1807 |
en |
dc.identifier.epage |
1812 |
en |