Production of soy protein isolates with low phytic acid content by membrane technologies: Impact of the extraction and ultrafiltration/diafiltration conditions

► The lowest phosphorus to protein ratio was obtained for 0.06M KCl/pH 9.0/25°C extraction. ► Water soy extracts were more prone to membrane fouling than 0.06M KCl soy extracts. ► Isolate with total phosphorus to protein ratio as low as 4.4mg P/g protein d.b. was obtained. The content of the antinut...

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Veröffentlicht in:Journal of food engineering 2013-01, Vol.114 (2), p.221-227
Hauptverfasser: Lai, Yung Priscilla, Mondor, Martin, Moresoli, Christine, Drolet, Hélène, Gros-Louis, Michel, Ippersiel, Denis, Lamarche, François, Arcand, Yves
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container_end_page 227
container_issue 2
container_start_page 221
container_title Journal of food engineering
container_volume 114
creator Lai, Yung Priscilla
Mondor, Martin
Moresoli, Christine
Drolet, Hélène
Gros-Louis, Michel
Ippersiel, Denis
Lamarche, François
Arcand, Yves
description ► The lowest phosphorus to protein ratio was obtained for 0.06M KCl/pH 9.0/25°C extraction. ► Water soy extracts were more prone to membrane fouling than 0.06M KCl soy extracts. ► Isolate with total phosphorus to protein ratio as low as 4.4mg P/g protein d.b. was obtained. The content of the antinutrient, phytic acid, of soy protein was analyzed during their extraction and purification by a series of ultrafiltration and diafiltration steps. The phosphorus content of the extracts was used as an indication of their phytic acid content and their ash content as an indication of their mineral content. The extraction of soy proteins was conducted by using a 23 factorial experimental design, pH (7.5 or 9), solvent (0.06M KCl or water), and temperature (25°C or 50°C). The most promising extraction conditions were 0.06M KCl/pH 9.0/25°C for the lowest phosphorus to protein ratio (12.2±0.1mg P/g protein) and H2O/pH 9.0/50°C for the combination of low phosphorus to protein ratio and the lowest ash content (13.9±1.2mg P/g protein, 9.6±0.8% w/w ash content). After extraction, soy proteins were purified by sequential ultrafiltration (UF) with a volume concentration ratio (VCR) of 5 and diafiltration (DF) with volume diafiltration ratio (VD) of 4. Extracts were purified with no pH adjustment or with pH adjustment to 6.5 between the UF and the DF steps. The extraction conditions 0.06M KCl/pH 9.0/25°C and the purification conditions UF pH 9.0/DF pH 6.5 showed the lowest phosphorus to protein ratio (4.4±0.3mg P/g protein) and reduced membrane fouling when compared to extraction conditions with water.
doi_str_mv 10.1016/j.jfoodeng.2012.08.012
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The content of the antinutrient, phytic acid, of soy protein was analyzed during their extraction and purification by a series of ultrafiltration and diafiltration steps. The phosphorus content of the extracts was used as an indication of their phytic acid content and their ash content as an indication of their mineral content. The extraction of soy proteins was conducted by using a 23 factorial experimental design, pH (7.5 or 9), solvent (0.06M KCl or water), and temperature (25°C or 50°C). The most promising extraction conditions were 0.06M KCl/pH 9.0/25°C for the lowest phosphorus to protein ratio (12.2±0.1mg P/g protein) and H2O/pH 9.0/50°C for the combination of low phosphorus to protein ratio and the lowest ash content (13.9±1.2mg P/g protein, 9.6±0.8% w/w ash content). After extraction, soy proteins were purified by sequential ultrafiltration (UF) with a volume concentration ratio (VCR) of 5 and diafiltration (DF) with volume diafiltration ratio (VD) of 4. 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subjects Animal, plant, fungal and microbial proteins, edible seaweeds and food yeasts
Ashes
Biological and medical sciences
Diafiltration
Extraction
Food engineering
Food industries
Fouling
Fundamental and applied biological sciences. Psychology
General aspects
Phosphorus
Phytic acid
Proteins
Purification
Soy protein
Ultrafiltration
title Production of soy protein isolates with low phytic acid content by membrane technologies: Impact of the extraction and ultrafiltration/diafiltration conditions
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