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

机译:通过膜技术生产低植酸含量的大豆分离蛋白:萃取和超滤/渗滤条件的影响

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摘要

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 2~3 factorial experimental design, pH (7.5 or 9), solvent (0.06 M KC1 or water), and temperature (25 ℃ or 50 ℃). The most promising extraction conditions were 0.06 M KCl/pH 9.0/25 ℃ for the lowest phosphorus to protein ratio (12.2 ± 0.1 mg P/g protein) and H_2O/PH 9.0/50 ℃ for the combination of low phosphorus to protein ratio and the lowest ash content (13.9 ± 1.2 mg 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 0.06 M KCl/pH 9.0/25 ℃ and the purification conditions UF pH 9.0/DF pH 6.5 showed the lowest phosphorus to protein ratio (4.4 ± 0.3 mg P/e Drotein) and reduced membrane fouline when comoared to extraction conditions with water.
机译:通过一系列的超滤和渗滤步骤,在大豆蛋白的抗营养素,植酸含量的提取和纯化过程中进行了分析。提取物中的磷含量被用作其植酸含量的指标,其灰分含量被用作其矿物质含量的指标。大豆蛋白的提取采用2〜3阶乘实验设计,pH(7.5或9),溶剂(0.06 M KCl或水)和温度(25℃或50℃)进行。最有希望的提取条件是:最低的磷蛋白比(12.2±0.1 mg P / g蛋白质)为0.06 M KCl / pH 9.0 / 25℃;对于低磷蛋白比的组合,H_2O / PH 9.0 / 50℃灰分最低(13.9±1.2 mg P / g蛋白质,9.6±0.8%w / w灰分)。提取后,大豆蛋白通过体积浓度比(VCR)为5的连续超滤(UF)和体积渗滤率(VD)为4的渗滤(DF)纯化。提取物无需进行pH调节或将pH调节至6.5在UF和DF步骤之间。萃取条件为0.06 M KCl / pH 9.0 / 25℃,纯化条件为UF pH 9.0 / DF pH 6.5时,磷蛋白比最低(4.4±0.3 mg P / e视黄质),膜烟碱降低。水。

著录项

  • 来源
    《Journal of food engineering》 |2013年第2期|221-227|共7页
  • 作者单位

    Department of Chemical Engineering, University of Waterloo, 200 University Avenue West, Waterloo, Ontario, Canada N2L 3G1;

    Food Research and Development Centre, Agriculture and Agri-Food Canada, 3600 Casavant Blvd. West, Saint-Hyadnthe, Quebec, Canada J2S 8E3;

    Department of Chemical Engineering, University of Waterloo, 200 University Avenue West, Waterloo, Ontario, Canada N2L 3G1;

    Food Research and Development Centre, Agriculture and Agri-Food Canada, 3600 Casavant Blvd. West, Saint-Hyadnthe, Quebec, Canada J2S 8E3;

    Food Research and Development Centre, Agriculture and Agri-Food Canada, 3600 Casavant Blvd. West, Saint-Hyadnthe, Quebec, Canada J2S 8E3;

    Food Research and Development Centre, Agriculture and Agri-Food Canada, 3600 Casavant Blvd. West, Saint-Hyadnthe, Quebec, Canada J2S 8E3;

    Food Research and Development Centre, Agriculture and Agri-Food Canada, 3600 Casavant Blvd. West, Saint-Hyadnthe, Quebec, Canada J2S 8E3;

    Food Research and Development Centre, Agriculture and Agri-Food Canada, 3600 Casavant Blvd. West, Saint-Hyadnthe, Quebec, Canada J2S 8E3;

  • 收录信息 美国《科学引文索引》(SCI);美国《工程索引》(EI);
  • 原文格式 PDF
  • 正文语种 eng
  • 中图分类
  • 关键词

    diafiltration; fouling; Phytic acid; soy protein; ultrafiltration;

    机译:渗滤结垢植酸大豆蛋白超滤;

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