Abstract:
:The aim of this work deals with the development of new approaches to the production of furfural from xylose. It combines relatively cheap heterogeneous catalysts (Amberlyst 70) with simultaneous furfural stripping using nitrogen under semi-batch conditions. Nitrogen, compared to steam, does not dilute the vapor phase stream when condensed. This system allowed stripping 65% of the furfural converted from xylose and almost 100% of selectivity in the condensate. Moreover, high initial xylose loadings led to the formation of two water-furfural phases, which could reduce further purification costs. Constant liquid-vapor equilibrium along stripping could be maintained for different xylose loadings. The modeling of the experimental data was carried out in order to obtain a liquid-vapor mass-transfer coefficient. This value could be used for future studies under steady-state continuous conditions in similar reaction-systems.
journal_name
Bioresour Technoljournal_title
Bioresource technologyauthors
Agirrezabal-Telleria I,Larreategui A,Requies J,Güemez MB,Arias PLdoi
10.1016/j.biortech.2011.05.015subject
Has Abstractpub_date
2011-08-01 00:00:00pages
7478-85issue
16eissn
0960-8524issn
1873-2976pii
S0960-8524(11)00654-7journal_volume
102pub_type
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