Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins

Sinapine adsorption was studied on four weak cation exchanges at pHs ranging from 2 to 8. The best adsorption rate was observed with C106 resin at pH 4 (95.25%). The adsorption kinetics followed a pseudo-second-order model while the isotherm data better fitted the Langmuir model. The ΔG°, ΔH°, and Δ...

Full description

Saved in:
Bibliographic Details
Main Authors: Fatima Zahra Kdah, Arnaud Aymes, Luna Beau, Armelle Ropars, Jean-Pol Frippiat, Romain Kapel
Format: Article
Language:English
Published: MDPI AG 2025-01-01
Series:Separations
Subjects:
Online Access:https://www.mdpi.com/2297-8739/12/1/10
Tags: Add Tag
No Tags, Be the first to tag this record!
_version_ 1832587524291166208
author Fatima Zahra Kdah
Arnaud Aymes
Luna Beau
Armelle Ropars
Jean-Pol Frippiat
Romain Kapel
author_facet Fatima Zahra Kdah
Arnaud Aymes
Luna Beau
Armelle Ropars
Jean-Pol Frippiat
Romain Kapel
author_sort Fatima Zahra Kdah
collection DOAJ
description Sinapine adsorption was studied on four weak cation exchanges at pHs ranging from 2 to 8. The best adsorption rate was observed with C106 resin at pH 4 (95.25%). The adsorption kinetics followed a pseudo-second-order model while the isotherm data better fitted the Langmuir model. The ΔG°, ΔH°, and ΔS° values (−25.834 kJ·mol<sup>−1</sup>, −24.428 kJ·mol<sup>−1</sup>, and 0.004 kJ·mol<sup>−1</sup>·K<sup>−1</sup>) revealed that the adsorption process was spontaneous and exothermic. Acidified ethanol showed a better desorption rate (75.41%), while virtually no (3.32%) or low (31.14%) sinapine desorption was observed with 50% ethanol and 0.1 M HCl solution, respectively. This indicated that sinapine adsorption took place throughout both ionic and hydrophobic interactions. Very close sinapine adsorption performances were observed with an effluent of the patented rapeseed protein isolate process. Two-step desorption using 50% ethanol, then acidified ethanol, yielded a highly purified neutral sinapine-derivative phenol fraction (75.23%) in the first elution fraction and sinapine (98.85%) in the second one.
format Article
id doaj-art-c1b88f590faa42f4adce044583a08c5b
institution Kabale University
issn 2297-8739
language English
publishDate 2025-01-01
publisher MDPI AG
record_format Article
series Separations
spelling doaj-art-c1b88f590faa42f4adce044583a08c5b2025-01-24T13:49:31ZengMDPI AGSeparations2297-87392025-01-011211010.3390/separations12010010Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange ResinsFatima Zahra Kdah0Arnaud Aymes1Luna Beau2Armelle Ropars3Jean-Pol Frippiat4Romain Kapel5Université de Lorraine, CNRS, LRGP, F-54000 Nancy, FranceUniversité de Lorraine, CNRS, LRGP, F-54000 Nancy, FranceUniversité de Lorraine, CNRS, LRGP, F-54000 Nancy, FranceUniversité de Lorraine, SIMPA UR7300, F-54000 Nancy, FranceUniversité de Lorraine, SIMPA UR7300, F-54000 Nancy, FranceUniversité de Lorraine, CNRS, LRGP, F-54000 Nancy, FranceSinapine adsorption was studied on four weak cation exchanges at pHs ranging from 2 to 8. The best adsorption rate was observed with C106 resin at pH 4 (95.25%). The adsorption kinetics followed a pseudo-second-order model while the isotherm data better fitted the Langmuir model. The ΔG°, ΔH°, and ΔS° values (−25.834 kJ·mol<sup>−1</sup>, −24.428 kJ·mol<sup>−1</sup>, and 0.004 kJ·mol<sup>−1</sup>·K<sup>−1</sup>) revealed that the adsorption process was spontaneous and exothermic. Acidified ethanol showed a better desorption rate (75.41%), while virtually no (3.32%) or low (31.14%) sinapine desorption was observed with 50% ethanol and 0.1 M HCl solution, respectively. This indicated that sinapine adsorption took place throughout both ionic and hydrophobic interactions. Very close sinapine adsorption performances were observed with an effluent of the patented rapeseed protein isolate process. Two-step desorption using 50% ethanol, then acidified ethanol, yielded a highly purified neutral sinapine-derivative phenol fraction (75.23%) in the first elution fraction and sinapine (98.85%) in the second one.https://www.mdpi.com/2297-8739/12/1/10ion exchange resinadsorptionsinapinerapeseed phenolic compoundsadsorption mechanism
spellingShingle Fatima Zahra Kdah
Arnaud Aymes
Luna Beau
Armelle Ropars
Jean-Pol Frippiat
Romain Kapel
Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins
Separations
ion exchange resin
adsorption
sinapine
rapeseed phenolic compounds
adsorption mechanism
title Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins
title_full Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins
title_fullStr Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins
title_full_unstemmed Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins
title_short Adsorption of Sinapine from Rapeseed Protein Production Effluent to Cation Exchange Resins
title_sort adsorption of sinapine from rapeseed protein production effluent to cation exchange resins
topic ion exchange resin
adsorption
sinapine
rapeseed phenolic compounds
adsorption mechanism
url https://www.mdpi.com/2297-8739/12/1/10
work_keys_str_mv AT fatimazahrakdah adsorptionofsinapinefromrapeseedproteinproductioneffluenttocationexchangeresins
AT arnaudaymes adsorptionofsinapinefromrapeseedproteinproductioneffluenttocationexchangeresins
AT lunabeau adsorptionofsinapinefromrapeseedproteinproductioneffluenttocationexchangeresins
AT armelleropars adsorptionofsinapinefromrapeseedproteinproductioneffluenttocationexchangeresins
AT jeanpolfrippiat adsorptionofsinapinefromrapeseedproteinproductioneffluenttocationexchangeresins
AT romainkapel adsorptionofsinapinefromrapeseedproteinproductioneffluenttocationexchangeresins