Enzymatic Synthesis of Prebiotic Carbohydrates From Lactose: Evaluation of Transgalactosylation Activity and Kinetics of Osmotic Membrane Distillation Integrated Reactor

IF 2.7 3区 农林科学 Q3 ENGINEERING, CHEMICAL
Kadir Cinar, Haci Ali Gulec, Pelin Onsekiozlu Bagci, Ufuk Bagci, Gurbuz Gunes
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Abstract

This research focused on the augmentation of galactooligosaccharide (GOS) synthesis from lactose through an integrated methodology of osmotic membrane distillation (OMD) and enzymatic synthesis employing β-galactosidase from Aspergillus oryzae. The effect of temperature, initial lactose concentration, and enzyme concentration was explored through a factorial experimental design. Optimal conditions for the OMD integrated reactor (R-Batch+OMD) were established using response surface methodology, yielding a temperature of 36.7°C, an enzyme concentration of 6.0 U g LS−1, and a lactose concentration of 32°Brix (% wt/wt). At these optimal conditions, GOS-4 was predicted at 8.70%, GOS-3 at 19.86%, and the total GOS yield (GY) at 28.57% for lactose conversion of 52.40%. Kinetic analysis revealed that the membrane separation process notably impacts enzymatic reaction parameters. Compared to the non-integrated reactor (R-Batch), a notable result in the R-Batch+OMD was the achievement of higher GY values at the same lactose conversions, which were attributed to the OMD facilitating a shift in enzymatic activity toward transgalactosylation due to water extraction from the reaction medium. An increased ratio of apparent kinetic parameter of GOS formation/decomposition (k5/k−5) in the R-Batch+OMD indicated a more prominent role of transgalactosylation. Also, the R-Batch+OMD highlighted the positive impact of high levels of E:Lac and E:Gal complex formations. This suggests a crucial effect of OMD on GOS synthesis: the maintenance of high E:Gal complex concentrations in the reaction medium, thereby improving enzyme-lactose interactions. Moreover, these outcomes underscore the potential of membrane technology to enhance bioprocess efficiency, leading toward more sustainable and innovative approaches in food engineering.

Abstract Image

酶法从乳糖合成益生元碳水化合物:跨半乳糖基化活性评价及渗透膜蒸馏集成反应器动力学
本研究采用渗透膜蒸馏(OMD)和米曲霉β-半乳糖苷酶合成相结合的方法,提高乳糖半乳糖寡糖(GOS)的合成效率。通过析因实验设计探讨了温度、初始乳糖浓度和酶浓度的影响。利用响应面法确定了OMD集成反应器(R-Batch+OMD)的最佳条件,温度为36.7°C,酶浓度为6.0 U g LS−1,乳糖浓度为32°Brix (% wt/wt)。在此优化条件下,GOS-4产率为8.70%,GOS-3产率为19.86%,GOS总产率为28.57%,乳糖转化率为52.40%。动力学分析表明,膜分离过程对酶促反应参数有显著影响。与非集成反应器(R-Batch)相比,R-Batch+OMD的显著结果是在相同的乳糖转化中获得了更高的GY值,这归因于OMD促进了酶活性向半乳糖基化的转变,这是由于反应介质中的水被提取。R-Batch+OMD中GOS形成/分解表观动力学参数(k5/k−5)的比值增大,表明转半乳糖基化作用更加突出。此外,R-Batch+OMD强调了高水平E:Lac和E:Gal复合物形成的积极影响。这表明了OMD对GOS合成的关键影响:在反应培养基中维持高E:Gal复合物浓度,从而改善酶-乳糖相互作用。此外,这些结果强调了膜技术在提高生物过程效率方面的潜力,从而导致食品工程中更具可持续性和创新性的方法。
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来源期刊
Journal of Food Process Engineering
Journal of Food Process Engineering 工程技术-工程:化工
CiteScore
5.70
自引率
10.00%
发文量
259
审稿时长
2 months
期刊介绍: This international research journal focuses on the engineering aspects of post-production handling, storage, processing, packaging, and distribution of food. Read by researchers, food and chemical engineers, and industry experts, this is the only international journal specifically devoted to the engineering aspects of food processing. Co-Editors M. Elena Castell-Perez and Rosana Moreira, both of Texas A&M University, welcome papers covering the best original research on applications of engineering principles and concepts to food and food processes.
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