首页> 外文期刊>Journal of the American Oil Chemists' Society >Protein extraction and membrane recovery in enzyme-assisted aqueous extraction processing of soybeans.
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Protein extraction and membrane recovery in enzyme-assisted aqueous extraction processing of soybeans.

机译:大豆酶辅助水提取过程中的蛋白质提取和膜回收。

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Enzyme-assisted aqueous extraction processing (EAEP) is an environmentally friendly process in which oil and protein can be simultaneously recovered from soybeans by using water and enzymes. The significant amount of protein-rich effluent (skim) constitutes a challenge to protein recovery. Countercurrent two-stage EAEP at a 1:6 solids-to-liquid ratio, 50 degrees C, pH 9.0, and 120 rpm for 1 h was used to extract oil and protein from dehulled, flaked and extruded soybeans. Different enzyme use strategies were used to produce different skim fractions: 0.5% protease (wt/wt extruded flakes) in both extraction stages; 0.5% protease only in the 2nd extraction stage; and no enzyme in either stage. Dead-end, stirred-cell membrane filtration was evaluated with each skim. About 96, 89, and 66% of the protein were extracted with the three enzyme treatments, respectively. Protein retentate yields of 91, 96, and 99% were obtained for the three enzyme treatments, respectively, by using double membrane filtration (30 kDa/500 Da) of the skims, achieving permeate fluxes up to 1.24 kg/m2 h at 3.9-4.8 concentration factors (CF) and 0.56 kg/m2 h at 1.9-2.9 CF for 30 kDa ultrafiltration and 500 Da nanofiltration, respectively. For cross-flow ultrafiltration with the 3-kDa membrane, pH and presence of insoluble protein aggregates significantly affected permeate flux. Maximum permeate flux occurred at high pH and in the presence of protein aggregates, achieving a mean value of 4.1 kg/m2 h at 1.7 bar transmembrane pressure.
机译:酶辅助水提取工艺(EAEP)是一种环境友好的工艺,其中可以使用水和酶从大豆中同时回收油和蛋白质。大量富含蛋白质的流出物(脱脂)构成了蛋白质回收的挑战。固液比为1:6的逆流两阶段EAEP,在50摄氏度,pH 9.0和120 rpm下进行1小时,用于从脱壳的,片状和挤压的大豆中提取油和蛋白质。不同的酶使用策略可用于产生不同的脱脂馏分:两个萃取阶段均使用0.5%的蛋白酶(wt / wt压片);仅在第二萃取阶段的蛋白酶含量为0.5%;在任何一个阶段都没有酶。用每个脱脂液评估死角,搅拌池膜过滤。三种酶处理分别提取了约96%,89%和66%的蛋白质。通过使用脱脂膜的双膜过滤(30 kDa / 500 Da),三种酶处理的蛋白质截留率分别达到91%,96%和99%,实现的渗透通量高达1.24 kg / m 2 30 kDa超滤和500 Da纳滤分别在3.9-4.8浓缩因子(CF)和1.9-2.9 CF下的0.56 kg / m 2 h。对于使用3-kDa膜的错流超滤,pH和不溶性蛋白聚集体的存在会显着影响渗透通量。在高pH值和蛋白质聚集的情况下,最大渗透通量出现,在1.7 bar跨膜压力下达到4.1 kg / m 2 h的平均值。

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