TY - JOUR
T1 - Separation and recovery of polyphenols and carbohydrates from Eucalyptus bark extract by ultrafiltration/diafiltration and adsorption processes
AU - Pinto, Paula Rodrigues
AU - Mota, Inês Ferreira
AU - Pereira, Carla Marques
AU - Ribeiro, Ana Mafalda
AU - Loureiro, José Miguel
AU - Rodrigues, Alírio Egídio
N1 - Funding Information:
This work was financially supported by: Project POCI-01-0145-FEDER- 006984 – Associate Laboratory LSRE-LCM funded by Fundo Europeu de Desenvolvimento Regional (FEDER) – Portugal funds through COMPETE2020 - Programa Operacional Competitividade e Internacionalização (POCI) – and by national funds through FCT - Fundação para a Ciência e a Tecnologia – Portugal. This work was co-financed by FCT and FEDER under Programme COMPETE (Project PEst-C/EQB/LA0020/2013). This work was co-financed by FEDER through the Operational Program for Competitiveness Factors (POFC) - Project BIIPP No.11551 - Integrated Biorefinery in Pulp and Paper Industry.
Publisher Copyright:
© 2017 Elsevier B.V.
PY - 2017
Y1 - 2017
N2 - The processing of ethanol:water 52:48%v/v extract of Eucalyptus globulus bark containing bioactive polyphenols by ultrafiltration in diafiltration (DF) mode and adsorption/desorption was investigated. Three approaches for membrane processing were studied in DF mode using polymeric membranes (30 and 5 kDa). One of these approaches (pre-concentration followed by DF with 30 kDa membrane) provided an increment of 21% and 64% of total phenolic compounds (TPC) and proanthocyanidins (Pac), respectively, relative to the initial ethanolic extract composition. The resulting retentate was further purified by fixed-bed adsorption/desorption using a pre-selected polymeric adsorbent (SP700). By desorbing with ethanol:water 95:5%v/v about 45% of the carbohydrates (TC) were eliminated and an enriched fraction in polyphenols was obtained. The combination of these two environmentally-friendly technologies (DF and adsorption/desorption) as downstream processing produces a concentrate of the bark extract with 12.4 g L−1 (67%w/wdried weight) of TPC, 10.3 g L−1 (55%w/wdried weight) of Pac, and 1.6 g L−1 (9%w/wdried weight) of TC. Finally, a flowchart for an integrated process of extraction, membrane processing and adsorption/desorption was proposed to obtain enriched fractions of polyphenols, with the additional possibility of the ethanol and water recovery in both diafiltration and adsorption/desorption steps to be reused in the extraction step of the process. Moreover, the integrated process also led to the recovery of low molecular weight phenolic compounds at the permeate stream during membrane processing and the recovery of galacturonic acid rich carbohydrates coming from the washing step of the fixed-bed process.
AB - The processing of ethanol:water 52:48%v/v extract of Eucalyptus globulus bark containing bioactive polyphenols by ultrafiltration in diafiltration (DF) mode and adsorption/desorption was investigated. Three approaches for membrane processing were studied in DF mode using polymeric membranes (30 and 5 kDa). One of these approaches (pre-concentration followed by DF with 30 kDa membrane) provided an increment of 21% and 64% of total phenolic compounds (TPC) and proanthocyanidins (Pac), respectively, relative to the initial ethanolic extract composition. The resulting retentate was further purified by fixed-bed adsorption/desorption using a pre-selected polymeric adsorbent (SP700). By desorbing with ethanol:water 95:5%v/v about 45% of the carbohydrates (TC) were eliminated and an enriched fraction in polyphenols was obtained. The combination of these two environmentally-friendly technologies (DF and adsorption/desorption) as downstream processing produces a concentrate of the bark extract with 12.4 g L−1 (67%w/wdried weight) of TPC, 10.3 g L−1 (55%w/wdried weight) of Pac, and 1.6 g L−1 (9%w/wdried weight) of TC. Finally, a flowchart for an integrated process of extraction, membrane processing and adsorption/desorption was proposed to obtain enriched fractions of polyphenols, with the additional possibility of the ethanol and water recovery in both diafiltration and adsorption/desorption steps to be reused in the extraction step of the process. Moreover, the integrated process also led to the recovery of low molecular weight phenolic compounds at the permeate stream during membrane processing and the recovery of galacturonic acid rich carbohydrates coming from the washing step of the fixed-bed process.
KW - Adsorption
KW - Biorefinery
KW - Eucalyptus bark
KW - Polyphenols recovery
KW - Ultrafiltration
UR - http://www.scopus.com/inward/record.url?scp=85017279339&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2017.04.003
DO - 10.1016/j.seppur.2017.04.003
M3 - Article
AN - SCOPUS:85017279339
SN - 1383-5866
VL - 183
SP - 96
EP - 105
JO - Separation and Purification Technology
JF - Separation and Purification Technology
ER -