TY - JOUR
T1 - Purification of ferulic acid from corn fibre alkaline extracts for bio-vanillin production using an adsorption process
AU - Valério, Rita
AU - Torres, Cristiana A. V.
AU - Brazinha, Carla
AU - da Silva, Marco Gomes
AU - Coelhoso, Isabel M.
AU - Crespo, João G.
N1 - Funding Information:
info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDP%2F04378%2F2020/PT#
info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F04378%2F2020/PT#
info:eu-repo/grantAgreement/FCT/FARH/PD%2FBDE%2F113543%2F2015/PT#
info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDB%2F50006%2F2020/PT#
info:eu-repo/grantAgreement/FCT/6817 - DCRRNI ID/UIDP%2F50006%2F2020/PT#
This work is financed by national funds from FCT - Fundação para a Ciência e a and the project LA/P/0140/2020 of the Associate Laboratory Institute for Health and Bioeconomy - i4HB. FCT/MCTES.
Publisher Copyright:
© 2022 Elsevier B.V.
PY - 2022/10/1
Y1 - 2022/10/1
N2 - Ferulic acid is the most widely studied precursor for bio-vanillin production. This work assesses the use of an alkaline extract from corn fibre for bio-vanillin production. The results show that after extraction an additional step is needed to purify ferulic acid removing toxic/inhibitor compounds. An adsorption process was selected to purify the ferulic acid. The performances of four different macroporous resins prepared from different matrix materials were evaluated. Macronet® MN102 (not yet reported for ferulic acid purification) offered the highest ferulic acid adsorption capacity. A column packed with Macronet® MN102 was used to perform dynamic adsorption and desorption experiments, which showed a maximum ferulic acid adsorption capacity of 176 mgferulic acid.g−1dry resin at pH 4.5 at a flow rate of 3.7 BV (bed volumes).h−1. The breakthrough point was at 115 min, corresponding to an adsorption capacity of 85 mgferulic acid.g−1dry resin. In the desorption step, 90.9% of ferulic acid was recovered using absolute ethanol ≥ 99.8%) as eluent, at the same flow rate of 3.7 BV (bed volumes).h−1. This procedure confirmed the removal of compounds with a microbial inhibitory effect, such as organic acids, metals and some aldehydes. The purified ferulic acid extract was then used to produce bio-vanillin. The bio-vanillin production by Amycolatopsis sp. ATCC 39116, using a single pulse of an extract with 10 g.L-1 of ferulic acid extract, led to a maximum vanillin concentration of 5 g.L-1 and a vanillin yield of 0.52 gvanillin.gferulic acid-1, values comparable to those obtained with a commercial solution containing 10 g.L-1 of ferulic acid.
AB - Ferulic acid is the most widely studied precursor for bio-vanillin production. This work assesses the use of an alkaline extract from corn fibre for bio-vanillin production. The results show that after extraction an additional step is needed to purify ferulic acid removing toxic/inhibitor compounds. An adsorption process was selected to purify the ferulic acid. The performances of four different macroporous resins prepared from different matrix materials were evaluated. Macronet® MN102 (not yet reported for ferulic acid purification) offered the highest ferulic acid adsorption capacity. A column packed with Macronet® MN102 was used to perform dynamic adsorption and desorption experiments, which showed a maximum ferulic acid adsorption capacity of 176 mgferulic acid.g−1dry resin at pH 4.5 at a flow rate of 3.7 BV (bed volumes).h−1. The breakthrough point was at 115 min, corresponding to an adsorption capacity of 85 mgferulic acid.g−1dry resin. In the desorption step, 90.9% of ferulic acid was recovered using absolute ethanol ≥ 99.8%) as eluent, at the same flow rate of 3.7 BV (bed volumes).h−1. This procedure confirmed the removal of compounds with a microbial inhibitory effect, such as organic acids, metals and some aldehydes. The purified ferulic acid extract was then used to produce bio-vanillin. The bio-vanillin production by Amycolatopsis sp. ATCC 39116, using a single pulse of an extract with 10 g.L-1 of ferulic acid extract, led to a maximum vanillin concentration of 5 g.L-1 and a vanillin yield of 0.52 gvanillin.gferulic acid-1, values comparable to those obtained with a commercial solution containing 10 g.L-1 of ferulic acid.
KW - Adsorption
KW - Bio-vanillin precursor
KW - Extract purification
KW - Ferulic acid extract
KW - Macroporous polymeric resins
UR - http://www.scopus.com/inward/record.url?scp=85133923596&partnerID=8YFLogxK
U2 - 10.1016/j.seppur.2022.121570
DO - 10.1016/j.seppur.2022.121570
M3 - Article
AN - SCOPUS:85133923596
SN - 1383-5866
VL - 298
JO - Separation and Purification Technology
JF - Separation and Purification Technology
M1 - 121570
ER -