Continuous clarification of grape juice using a packed bed bioreactor including pectinase enzyme immobilized on glass beads
Introduction
Grapes (Vitis vinifera) are one of the most popular fruits in the world, and are usually consumed as fresh fruit, juice, wine or marmalade (Ghafoor et al., 2009). Grape juice is rich in flavonols, anthocyanins, procyanidins and phenolic acids and therefore has positive effects on human health as anti-cancer and anti-inflammatory agents (Capanoglu et al., 2013; da Silva Haas et al., 2019). However, the major problems in the industrial production of juice is its turbidity and the formation of sediment during storage (Tapre & Jain, 2014). The cause of these problems is mainly a hydrocolloid called pectin and so removing it is needed to produce a customer-friendly product.
Pectin is a plant polysaccharide composed of galacturonic acid chains and used as an emulsifier, thickener and stabilizer agent in the food and drug industries (Mosayebi et al., 2018; Pasandide et al., 2018). Despite these unique properties, the presence of this polysaccharide in many fruit juice samples has been problematic as stated earlier, and the best way to remove pectin during the clarification step remains an issue. (Sharma et al., 2014). Enzymatic clarification of different fruit juice samples has a high potential and could be a cost-effective method (Lettera et al., 2016; Salim et al., 2018). Pectinase is the most important enzyme used for fruit juice clarification. This enzyme reduces cloudiness and improves the quality of fruit juice by hydrolysis of pectic substances (Sojitra et al., 2017). However, the native form of the enzyme has limitations such as high cost, low stability and problems related to its recovery and reusability. Enzyme immobilization on a suitable carrier can overcome some of the limitations and defects (Chauhan et al., 2015; dos Santos et al., 2019; Wang et al., 2016; Yu et al., 2018) and lead to a continuous process. The enzyme immobilization has been done using different methods of which covalent immobilization, adsorption and entrapment on/in the supports are the main ones (Ko et al., 2018; Rehman, Nawaz, et al., 2014; Sheldon, 2007). For instance, Amin et al. (2017) immobilized the fungal exo-polygalacturonase on sodium alginate support by covalent (using glutaraldehyde as a cross-linker) and/or adsorption methods. Rehman, Aman, et al. (2014) applied the entrapment method for pectinase immobilization in an agar-agar matrix. Lei and Jiang (2011) used glutaraldehyde for covalent immobilization of pectinase onto macroporous polyacrylamide microspheres. The covalent immobilization method seemed to have better results with less enzyme release. The choice of a suitable support such as glass beads with high performance, easy availability, high stability and low cost are important benefits (Eskandarloo & Abbaspourrad, 2018).
Although the enzyme immobilization is a necessary condition for a continuous enzymatic process, it is impossible to do without the use of a bioreactor. A packed bed reactor (PBR), is a simple and inexpensive reactor, which includes one or more tubes filled with a catalyst, in which the reaction mixture flows continuously with controlled conditions (de Oliveira et al., 2018). Continuous reactors have the advantage of ease of operation, better control of the reaction conditions and product quality, high production performance and low operating costs (Nakkharat & Haltrich, 2007).
The aim of this study was the immobilization of a pectinase enzyme on glass beads using a covalent method and the development of a continuous process for clarifying grape juice in a PBR. Pectinase was immobilized on functionalized glass beads using glutaraldehyde and then the optimum conditions of enzyme activity were determined. In the next step, a bioreactor after obtaining optimum conditions was used to clarify grape juice.
Section snippets
Materials
Apple pectin (United States Pharmacopeia (USP) grade and degree of esterification)DE () of 72–76%) was supplied by Herbstreith & Fox KG (Nuremberg, Bavaria, Germany). Pectinase enzyme (Pectinex® Ultra Color, with a protein content of 80 mg mL−1) with optimum temperature and pH of 50 °C and 5, which had been determined in a previous study (Hosseini et al., 2020), was obtained from Novozymes (Bagsvaerd, Denmark). Glass beads (6 mm diameter) were purchased from the Iran Beads Co. (Esfahan, Iran).
Influence of different flow rates with the immobilized pectinase activity
To evaluate the effect of flow rate (0.1–10 mL min−1) on the immobilized pectinase activity, the reducing sugar production in the buffered pectin solution (1 mg mL−1, pH 5.5, 50 °C) by the immobilized pectinase was studied in the continuous flow PBR. Fig. 1 shows that the production of reducing sugar was increased with a decrease in flow rate from 10 to 0.1 mL min−1. This behavior was probably related to an increase in residence time (Ansari & Husain, 2010). However, as can be seen, with
Conclusion
The pectinase enzymes were efficiently immobilized on the functionalized glass beads using glutaraldehyde and then the optimum temperature and pH of the immobilized pectinase were compared with the native one. A PBR charged with the glass beads immobilized pectinase was used to clarify grape juice. The results showed that the possible maximum clarification in PBR was obtained at a flow rate of 0.5 mL min−1 after 42 min. The investigation of the physicochemical properties of grape juice samples
CRediT authorship contribution statement
Seyedeh Zahra Azimi: Investigation, Methodology, Writing - original draft, Formal analysis. Seyed Saeid Hosseini: Investigation, Methodology, Formal analysis, Writing - review & editing. Faramarz Khodaiyan: Conceptualization, Supervision, Validation, Writing - review & editing.
Declaration of competing interest
The authors confirm that they have no conflicts of interest with respect to the work described in this manuscript.
Acknowledgements
This study was a part of a Master's degree research study, and was only supported by the Food Science and Technology Department, University of Tehran. Therefore the authors would like to thank all the members of the Food Science and Technology Department, University of Tehran, Iran.
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