TY - JOUR
T1 - Adsorption of vanillin and syringaldehyde onto a macroporous polymeric resin
AU - Mota, Maria Inês F.
AU - Pinto, Paula C.Rodrigues
AU - Loureiro, José Miguel
AU - Rodrigues, Alírio E.
N1 - Funding Information:
Inês Mota gratefully acknowledges her Ph.D. scholarship (SFRH/BD/91582/2012) from Fundação para a Ciência e Tecnologia (FCT).
Funding Information:
This work was co-financed by FCT and FEDER under Programme PT2020 (Project UID/EQU/50020/2013) and Programme COMPETE (FCOMP-01-0124-FEDER-123456).
Funding Information:
The authors also thank to Project No. 33969 Conception of bio-based products from renewable lignocellulosic sources as precursors for bioindustry of chemical synthesis and biomaterials – funded by FEDER through the National Strategic Reference Framework.
Publisher Copyright:
© 2015 Elsevier B.V.
PY - 2016/3/15
Y1 - 2016/3/15
N2 - Pulp and paper mill and biorefinery side-streams are rich in lignin which can be partially converted to vanillin and syringaldehyde through an oxidation process. These value-added compounds can be recovered with an integrated separation process encompassing an adsorption step. In this work the potential of a macroporous polymeric resin, Sepabeads SP700, was assessed. The resin was characterized regarding particle size, solid density, apparent density and particle porosity by means of laser dispersion, helium pycnometry and mercury intrusion porosimetry, respectively. Values within the ranges given by supplier were achieved: solid density, apparent density, particle size and particle porosity were 1294gL-1, 1012gL-1, 483μm and 0.73mLporesmL-1particle, respectively. Batch equilibrium isotherms for three different temperatures 283/288, 298 and 333K were found for vanillin and syringaldehyde in aqueous solutions. Experimental results were fitted to Langmuir and Freundlich isotherm models. Equilibrium isotherms were validated by fixed bed studies at different temperatures and feed concentrations. A mathematical model comprising the equilibrium isotherms, linear driving force approximation, and intraparticle mass transfer resistances was used to describe the adsorption/desorption histories of concentration at the outlet of the fixed bed experiments. Although Langmuir model reasonably fit to the experimental results, the empirical Freundlich model was best to describe the experimental results for equilibrium concentrations bellow 1gL-1.
AB - Pulp and paper mill and biorefinery side-streams are rich in lignin which can be partially converted to vanillin and syringaldehyde through an oxidation process. These value-added compounds can be recovered with an integrated separation process encompassing an adsorption step. In this work the potential of a macroporous polymeric resin, Sepabeads SP700, was assessed. The resin was characterized regarding particle size, solid density, apparent density and particle porosity by means of laser dispersion, helium pycnometry and mercury intrusion porosimetry, respectively. Values within the ranges given by supplier were achieved: solid density, apparent density, particle size and particle porosity were 1294gL-1, 1012gL-1, 483μm and 0.73mLporesmL-1particle, respectively. Batch equilibrium isotherms for three different temperatures 283/288, 298 and 333K were found for vanillin and syringaldehyde in aqueous solutions. Experimental results were fitted to Langmuir and Freundlich isotherm models. Equilibrium isotherms were validated by fixed bed studies at different temperatures and feed concentrations. A mathematical model comprising the equilibrium isotherms, linear driving force approximation, and intraparticle mass transfer resistances was used to describe the adsorption/desorption histories of concentration at the outlet of the fixed bed experiments. Although Langmuir model reasonably fit to the experimental results, the empirical Freundlich model was best to describe the experimental results for equilibrium concentrations bellow 1gL-1.
KW - Adsorption
KW - Breakthrough
KW - Nonpolar resin
KW - Syringaldehyde
KW - Vanillin
UR - http://www.scopus.com/inward/record.url?scp=84952887541&partnerID=8YFLogxK
U2 - 10.1016/j.cej.2015.12.041
DO - 10.1016/j.cej.2015.12.041
M3 - Article
SN - 1385-8947
VL - 288
SP - 869
EP - 879
JO - Chemical Engineering Journal
JF - Chemical Engineering Journal
ER -