Abstract
Isomaltose–oligosaccharides (IMOs), as food ingredients with prebiotic functionality, can be prepared via enzymatic synthesis using α-glucosidase. In the present study, the α-glucosidase (GSJ) from Geobacillus sp. strain HTA-462 was cloned and expressed in Escherichia coli BL21 (DE3). Recombinant GSJ was purified and biochemically characterized. The optimum temperature condition of the recombinant enzyme was 65 °C, and the half-life was 84 h at 60 °C, whereas the enzyme was active over the range of pH 6.0–10.0 with maximal activity at pH 7.0. The α-glucosidase activity in shake flasks reached 107.9 U/mL and using 4-Nitrophenyl β-D-glucopyranoside (pNPG) as substrate, the Km and Vmax values were 2.321 mM and 306.3 U/mg, respectively. The divalent ions Mn2+ and Ca2+ could improve GSJ activity by 32.1% and 13.8%. Moreover, the hydrolysis ability of recombinant α-glucosidase was almost the same as that of the commercial α-glucosidase (Bacillus stearothermophilus). In terms of the transglycosylation reaction, with 30% maltose syrup under the condition of 60 °C and pH 7.0, IMOs were synthesized with a conversion rate of 37%. These studies lay the basis for the industrial application of recombinant α-glucosidase.
Keywords: α-glucosidase, isomaltose-oligosaccharides, heterologous expression, transglycosylation, thermostability
1. Introduction
Isomalto–oligosaccharides (IMOs) are a group of functional oligosaccharides with a degree of polymerization (DP) ranging 2–10, which consist of glucosyl saccharide units linked by α-1, 6-glycosidic linkages [1]. Isomaltose, panose, isomaltotriose and tetrasaccharides are defined as the main functional components of IMOs [2]. As functional oligosaccharides, which are non-digestible in nature, IMOs have the function of regulating intestinal flora by promoting the proliferation of Bifidobacterium and Lactobacillus in the human intestinal tract [3], and also have the additional properties of: low caloric value [4], the promotion of gastrointestinal peristalsis, and the improvement of constipation and lipid metabolism [5,6]. Based on these functions, IMOs are widely utilized as prebiotics, food additives and feed ingredients [7,8,9,10].
IMOs are commonly produced from starch via enzymatic conversion using α-amylase, β-amylase, pullulanase and transglucosidase [11]. The typical process for IMO production usually comprises three steps: (1) liquefaction, where starch is liquefied by a thermostable α-amylase to produce dextrin; (2) saccharification, where the dextrin is then saccharified by β-amylase and pullulanase; (3) transglycosylation, where α-glucosidase is used for converting maltose (saccharified products) into IMOs [12]. Since commercial α-amylase, β-amylase and pullulanase are well-studied and their industrial uses are relatively mature, studying the transglycosylation reaction catalyzed by α-glucosidase is the key step in IMO production. α-glucosidase (EC 3.2.1.20, GH13) catalyzes the liberation of glucose from non-reducing terminals of substrates [13]. In addition to the hydrolysis activity, some α-glucosidases, for instance, those from Aspergillus niger [14], Bacillus stearothermophilus [15] and Xantophyllomyces dendrorhous [16], possess transglycosylation activity, which can transfer a glucosyl residue to the 6-OH group of the non-reducing glucose unit and yield IMOs [17].
To date, a large number of α-glucosidases with transglycosylation activity have been identified and characterized. Aspergillus niger α-glucosidase was reported to have high transglycosylation activity, and was hence successfully applied to produce IMOs [18,19]. With the increasing commercial interest and industrial application prospects, α-glucosidase production has drawn extensive attention. Generally, α-glucosidase from A. niger is stable below 50 °C, restricting the current commercial transglycosylation reaction optimally operated at around 50 °C. However, if the temperature of the transglycosylation reaction can be increased, the faster reaction rate, higher conversion rate and decreased viscosity of the substrate would be advantageously achieved. Previously, α-glucosidase from Geobacillus sp. strain HTA-462 (an isolate from Mariana Trench sediment) was characterized, and the results showed that the wild-type enzyme exhibited good thermostability and good transglycosylation activity [20], indicating that GSJ has potential application in the IMO industry.
In the present study, for the first time, E. coli BL21 (DE3) was selected as the host strain for the expression of the gene encoding α-glucosidase (GSJ) from Geobacillus sp. strain HTA-462. The ability of the purified recombinant α-glucosidase to synthesize IMOs was investigated and our studies aimed to provide a platform for the development of GSJ into an industrial enzyme.
2. Results
2.1. Expression and Purification of α-Glucosidase
The prokaryotic expression system (E. coli BL21 (DE3)/pET28a-gsj) was established for the inducible expression of GSJ. The synthesized gene was sub-cloned into the EcoR I and Xho I sites of pET-28a (+). The transformation of the designated pET28a/gsj into E. coli BL21 (DE3) yielded the recombinant strain. Since we used the T7 promoter-based expression system in this study, isopropyl β-D-1-thiogalactopyranoside (IPTG) was used for the induction of protein overexpression. The expression efficiency of the engineered E. coli was explored in a shake flask. Under the optimized culture conditions, the intracellular α-glucosidase activity kept rising rapidly and reached a maximum value of 107.9 U/mL at 30 h (Figure 1).
The enzyme purification process is summarized in Table 1. The N-terminal his-tagged recombinant α-glucosidase from the cell-free extract was purified through a combination of heat treatment and chromatographic separation. GSJ was purified 6.6-fold, with a specific activity of 283.3 U/mg and an overall recovery of 73.7%. Sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) analysis showed that the purified recombinant enzyme was detected as a single protein band with an apparent molecular mass of about 70 kDa, and the exact molecular weight, determined using MALDI-TOF mass spectrometry, was 68.9 KDa, matching the theoretically calculated value (Figure 2B).
Table 1.
Purification | Total Protein (mg) | Total Activity (U) | Specific Activity (U/mg) | Purification Fold | Yield (%) |
---|---|---|---|---|---|
Crude enzyme | 90.90 | 3876.1 | 42.64 | 1.0 | 100.0 |
Heat treatment | 25.05 | 3206.9 | 128.0 | 3.0 | 82.7 |
Ni-Sepharose | 10.08 | 2856.0 | 283.3 | 6.6 | 73.7 |
2.2. Characterization of the Recombinant Enzymes
2.2.1. Temperature Optimum and Thermostability
The optimum temperature curve of the purified enzyme indicated that the activity increased with temperature until it peaked at 65 °C, and the enzyme retained above 50% activity between 55 °C and 75 °C (Figure 3A). The thermostability of the recombinant enzyme was determined at pH 7.0 and temperatures of 60 °C and 65 °C. As shown in Figure 3C, the enzyme still retained 90% of activity after 30 h at 60 °C, and with a half-time of 84 h. Upon incubation at 65 °C, the enzyme showed 57% residual activity after 18 h. A GSJ with good thermostability and high optimum temperature is beneficial for applications operating at a high temperature for a long time in industry.
2.2.2. pH Optimum and Stability
The enzyme exhibited high enzymatic activity (>75%) between pH 6.0 and 9.0, and the optimum pH was 7.0 (Figure 3B). Furthermore, GSJ was stable at a wide range of pH values, of 6.0–10.0. Additionally, the GSJ retained 93.9% and 84.1% after incubation for 48 h and 72 h at pH 7.0, respectively. It also retained almost initial activity after incubation for 72 h at pH 10.0 (Figure 3D).
2.2.3. Kinetic Studies
The kinetic parameter of the enzyme was analyzed using 4-Nitrophenyl β-D-glucopyranoside (pNPG) as the substrate at 65 °C and pH 7.0 (Figure 4). As shown in Table 2, the kinetic constant Km was found to be 2.32 mM and the catalytic efficiency kcat/km was 151.6 mM−1s−1.
Table 2.
Substrate | Km (mM) | Vmax (U mg−1) | kcat (s−1) | kcat/Km (mM−1s−1) |
---|---|---|---|---|
pNP-α-D-glucopyranoside | 2.321 | 306.3 | 352 | 151.6 |
2.2.4. Metal Requirements
Previously, Mn2+ was reported to stimulate the activity of α-glucosidase from Thermotoga maritima [21], Ca2+ was required for the catalytic efficiency of the enzyme from E. coli [22], and Mucor racemosus α-glucosidase was able to be stimulated by Al3+, Ca2+, Mg2+ and Na+ [23]. In this study, the effect of metal ions on the activity of GSJ was analyzed by preincubating the enzyme with 1 mM metal ions at 65 °C for 1 h. As shown in Figure 5, Mg2+ and K+ did not affect the enzyme activity of GSJ, Cu2+, Zn2+ and Ni2+ strongly inhibited the enzyme activity by 12.3%–38.6%, while Fe2+ almost completely inhibited the enzyme activity. However, its activity was significantly improved by 113.8% and 132.1% in the presence of Ca2+ and Mn2+.
2.2.5. Substrate Specificity
Nine pNP derivatives were chosen as substrates to determine the substrate specificity of GSJ. As the results show in Table 3, GSJ exhibited high activity and specificity toward pNPαGlu, whereas the enzyme showed no activity against the other eight pNP derivatives (pNPβGlu, pNPαArap, pNPαGal, pNPβGal, pNPαAra, pNPαRha, pNPβMan, pNPβXyl). The enzyme exclusively hydrolyzed α-1, 4-linked terminal glucose residue.
Table 3.
Substrate | Relative Activity (%) |
---|---|
pNP-α-D-glucopyranoside | 100.0 |
pNP-β-D-glucopyranoside | 4.1 |
pNP-α-L-arabinofuranoside | 6.6 |
pNP-α-L-arabinopyranoside | 0.6 |
pNP-α-D-galactopyranoside | 2.7 |
pNP-β-D-galactopyranoside | 0.0 |
pNP-α-L-rhamnopyranoside | 6.8 |
pNP-β-D-mannopyranoside | 0.0 |
pNP-β-D-xylopyranoside | 3.9 |
2.3. Hydrolysis Activity
α-glucosidase is a typical exo-type glycosidase, which could cleave the terminal α-1, 4-glucosidic linkage from the non-reducing ends of oligosaccharides to form glucose. To determine the hydrolysis activity of the recombinant GSJ, commercial α-amylase was utilized to degrade soluble starch to oligosaccharides, which was subsequently hydrolyzed to glucose by the recombinant GSJ/commercial α-glucosidase (Bacillus. Stearothermophilus, E-TSAGS, Megazyme, Ireland), and the degradation products were analyzed by high-performance anion-exchange chromatography (HPAEC). When using α-amylase alone, the degradation products were mainly oligosaccharides and a small amount of glucose. However, when α-amylase and GSJ/commercial α-glucosidase were combined, the degradation products were almost entirely glucose (Figure 6), suggesting that the recombinant enzyme has high hydrolysis activity, the same as the commercial enzyme.
2.4. Transglycosylation Activity of Recombinant α-Glucosidase
To determine the transglycosylation activity of GSJ, the recombinant α-glucosidase was incubated with 30% (w/v) maltose solution at 60 °C. The progress of the reaction was monitored by HPAEC, and IMO standards were used to identify the retention time of the components. As shown in Figure 7, after 2 h of the reaction, more than 80% of the maltose was consumed, and glucose and a series of transglycosylation products (isomaltose, panose and isomaltotriose) were formed and clearly assigned by HPAEC. Isomaltose, panose and isomaltotriose were measured for total IMOs, and IMOs were synthesized with approximately 37% conversion in 2 h by the recombinant enzyme.
3. Discussion
Due to the transglycosylation activity, α-glucosidase is utilized in IMO production [24]. α-amylase, β-amylase and pullulanase hydrolyses starch to maltose, which subsequently transglycosylates to IMOs by α-glucosidase. Currently, A. niger α-glucosidase has been applied to produce IMOs in industry, and the relatively mature technology is used by Amano Enzymes Inc., Japan [19]. IMOs, one of the emerging prebiotics, have proved their beneficial effects on bifidogenic flora, bowel function and metabolism, as well as on the immune system [17]. In response to consumers paying more attention to personal health and well-being and increasing demand, the production of IMOs has been promoted in recent years. In order to enhance the IMO yield, many technologies have been developed, such as heterologous expression and the immobilization of α-glucosidase, the combination of different enzymes, and enzymes being bound to living cells. Recombinant enzyme technology was reported to significantly improve IMO production [12].
Thermostable enzymes, which have the advantage of high reactivity, better yield, high stability, low viscosity and little contamination, are important and highly attractive candidates for industrial applications [25]. Previously, α-glucosidase from the Geobacillus sp. strain HTA-462 was identified and characterized, and the encoding gene was sequenced and expressed in Bacillus subtilis ISW1214 [20]. E. coli is the preferred host for recombinant protein expression due to its high-level production of heterologous proteins, fast growth and simple culture conditions. Therefore, in order to improve the enzyme activity and study of the production of IMOs by GSJ, in the present study the gene encoding α-glucosidase from Geobacillus sp. strain HTA-462 was cloned and expressed in E. coli BL21 (DE3). The enzyme activity of the recombinant GSJ in shake flasks reached 107.9 U/mL. However, the biochemical properties of the GSJ expressed in E. coli revealed dissimilarity from the wild-type enzyme. The optimum temperature of the wild-type GSJ was 60 °C, while, in contrast, the recombinant GSJ showed a shift in optimum temperature to 65 °C. The optimal pH of the wild-type GSJ was 9.0 in the glycine-NaOH buffer, while the optimum pH of the recombinant GSJ was 7.0 in phosphate buffer, and it maintained more than 70% activity ranging from pH 6.0 to 10.0. Significantly, recombinant GSJ exhibited higher thermostability. At 60 °C, the half-life of the recombinant GSJ was 84 h, which was 6.3-fold greater than that of the wild-type. The big difference in thermostability was probably caused by the detection at different pHs and in different buffer systems. Notably, in comparison to the recombinant α-glucosidase from A. niger, the recombinant GSJ exhibited greater thermostability with a longer half-life, which was 28-fold greater than that of the A. niger α-glucosidase (half-life of 3.0 h at 60 °C) [18]. The good thermal stability suggests that GSJ has potential for application in IMO industries.
Both the hydrolysis and transglycosylation activities of the recombinant GSJ were determined. α-amylase and the recombinant α-glucosidase/commercial α-glucosidase were simultaneously used to convert soluble starch. The results showed that both the α-glucosidase and the commercial α-glucosidase could almost completely hydrolyze the soluble starch to glucose in only 1 h, indicating that the recombinant GSJ had good hydrolysis activity towards the terminal α-1, 4-glycosidic bond. With regard to the transglycosylation activity, the IMOs were synthesized by GSJ with a conversion rate of 37% when using maltose as a substrate. In industry, the yield of IMOs produced by α-glucosidase is generally reported to be about 60%. Although the IMO yield in our study was not ideal, optimizing the conditions of the transglycosylation reaction may raise the yields further. Additionally, because of its good thermal stability, the recombinant GSJ could be immobilized to recycle and reuse it, which could reduce the production costs.
4. Materials and Methods
4.1. Cloning and Expression of GSJ in E. coli BL21 (DE3)
The nucleotide sequence of a 1668-bp fragment encoding GSJ gene (AB154818) was synthesized by Synbio Technologies Inc. (Jiangsu, China). The synthesized GSJ was digested using EcoR I and Xho I, and then cloned into a pET-28a (+) vector with a strong T7 promoter, and the recombinant plasmid was transformed into the E. coli BL21 (DE3) for overexpression. A single colony of E. coli BL21 (DE3) harboring the recombinant plasmid was inoculated into a 10 mL Luria–Bertani (LB) culture-grown medium containing 0.1 mg/mL kanamycin and grown at 37 °C. The overnight culture was diluted into 50 mL terrific broth (TB), when the cell density was OD600 0.5–0.6, the expression of the recombinant α-glucosidase was induced by 0.4 mM IPTG for continuous 36 h cultivation at 25 °C.
4.2. Assay of α-Glucosidase Activity
The hydrolysis activity of α-glucosidase was determined spectrophotometrically by measuring the amount of p-nitrophenol (pNP) released from p-nitrophenyl-α-glucopyranoside (pNPG, Sigma). The reaction mixture (200 μL) containing 10 mM pNPG, 15 mM phosphate buffer (pH 7.0) and appropriately diluted enzyme, was incubated at 65 °C for 10 min. The reaction was terminated by adding 50 μL of 1 M Na2CO3 and the liberated pNP was measured at 405 nm. One unit of α-glucosidase activity was defined as the amount of enzyme required to release 1 μmol pNP per minute under the conditions described above.
4.3. Enzyme Preparation and Purification
Cells were harvested and disrupted by sonication, and the intracellular soluble fraction was centrifuged at 12,000× g for 10 min to remove insoluble cell debris and proteins. The crude extracts of the enzymes were purified according to the following procedures. The intracellular soluble fraction was heated at 60 °C for 20 min and centrifuged at 12,000 for 10 min. The sample was then filtered with 0.22 μm filters (Jiangsu Green Union Science Instrument Co., Ltd.) followed by loading onto a Ni-NTA column. The fractions containing the target enzyme were pooled and dialyzed against phosphate buffer at 4 °C for 24 h. Proteins were monitored using sodium dodecyl sulfate-polyacrylamide gel electrophoresis (SDS-PAGE) and the Bradford method was used to determine the protein concentrations [26].
4.4. Effects of Temperature and pH on the Enzyme Activity and Stability
Temperature optimum and thermostability. The optimal temperature of α-glucosidase was determined by measuring the enzyme activity between 30 °C and 80 °C at pH 7.0, using pNPG as the substrate. The thermostability of α-glucosidase was determined by incubating the enzyme in 15 mM sodium phosphate buffer (pH 7.0) at 60 °C and 65 °C, and samples were assayed for residual activity at different intervals.
pH optimum and stability. pH optimum of α-glucosidase was measured at 65 °C over the range between 4.0–11.0 with increments of 1.0 pH unit, using 15 mM acetate buffer (pH 4.0–6.0), sodium phosphate buffer (pH 6.0–9.0) and glycine-NaOH buffer (pH 9.0–11.0). To determine the pH stability, the enzyme was incubated in the above various buffers at 4 °C for 24–48 h, followed by residual activity determination at pH 7.0 and 65 °C.
4.5. Metal Requirement
To determine the effect of metal ions on the recombinant α-glucosidase activity, the enzyme (30 ng) was preincubated with 1 mM of each metal ion (Ca2+, Mg2+, Fe2+, Zn2+, Mn2+, Ni2+, Cu2+ and K+) in 15 mM sodium phosphate buffer (pH 7.0) for 1 h at 65 °C. The residual enzyme activity was assayed at 65 °C.
4.6. Kinetic Parameters
Enzymatic assays for determining kinetic parameters were performed in the 15 mM sodium phosphate buffer (pH 7.0) at 65 °C with 0.1–4.0 mM pNPG as substrate. The apparent kinetic constants were calculated using the GraphPad software.
4.7. Substrate Specificity
The substrate specificity of purified GSJ was determined with various pNP derivatives (pNPαGlu, pNPβGlu, pNPαArap, pNPαGal, pNPβGal, pNPαAra, pNPαRha, pNPβMan, pNPβXyl) as substrates. The reaction contained 1 mM pNP-glycoside, 15 mM sodium phosphate buffer (pH 7.0) and 2 μg recombinant enzymes were carried out at 65 °C for 10 min. All of the pNP derivatives were purchased from Sigma (St. Louis, MO, USA).
4.8. Hydrolysis Reaction
Commercial α-amylase (Bacillus licheniformis, A3403, Sigma) was added into the 1% (w/v) soluble starch and this mixture was incubated at 90 °C for 30 min. Then the mixture was incubated at 100 °C for 20 min to inactivate the enzyme, and centrifuged at 12,000× g for 15 min. After adding 5 ug recombinant GSJ or commercial α-glucosidase (Bacillus. Stearothermophilus, E-TSAGS, Megazyme, Ireland), the supernatant was incubated at 60°C. Following incubation for 1 h, the mixtures were incubated at 100 °C for 5 min to inactivate the enzyme, and centrifuged at 12,000× g for 15 min. The hydrolysis products were determined by HPAEC.
4.9. Transglycosylation Reaction
The reaction mixture, which consisted of 30% maltose and 5 μg enzyme in sodium phosphate buffer, was incubated at 60 °C for 2 h. Reaction mixtures were incubated at 100 °C for 5 min to inactivate the enzyme, and the samples were then centrifuged at 12,000× g for 10 min and analyzed by HPAEC.
4.10. HPAEC Analysis
Both the hydrolysis products and transglycosylation products were analyzed using HPAEC. The HPAEC-PAD analysis was performed on a Dionex ICS 5000 system with a CarboPac PA-200 column and pulsed electrochemical detector. The samples were eluted at 0.5 mL/min with a linear gradient from 0 to 50 mM NaAc in 50 mM NaOH for 20 min, and then eluted by 200 mM NaOH and 400 mM NaAc for 10 min. The standards of glucose, maltose, isomaltose, panose and isomaltotriose were obtained from Shanghai Hui Cheng Biological Technology Co. Ltd. (Shanghai, China).
4.11. MALDI-TOF Mass Spectrometry
The purified GSJ were dissolved into 0.1% trifluoroacetic acid (TFA). The reagent 2.5-dihydroxy benzoic acid was dissolved in 30/70 (w/w) acetonitrile/0.1% TFA as the matrix. Equal volumes of sample and matrix were mixed. The mixture (1 μL) was placed on an AnchorChip Standard (800 μm) plate and examined using a BRUKER Autoflex Speed mass spectrometer. Data were recorded using the FlexControl software and analyzed using FlexAnalysis software. Protein adduct ions [M + 2H]2+ or [M + H]+ were assigned.
5. Conclusions
In conclusion, α-glucosidase of the Geobacillus sp. strain HTA-462 was cloned and expressed in E. coli, and the recombinant enzyme was characterized in detail. The α-glucosidase activity in shake flasks was 107.9 U/mL. A detailed biochemical characterization showed that the recombinant α-glucosidase had high activity and stability at high temperatures and in a broad pH range. Additionally, the GSJ showed high α-1, 4-glucosidic hydrolysis and high transglycosylation activity, and converted maltose to IMOs with a yield of 37%. These studies indicated that the recombinant α-glucosidase has a great potential for industrial-scale applications. To the best of our knowledge, this is the first report to express the GSJ gene in E. coli and study IMO synthesis by the recombinant enzyme.
Author Contributions
F.Z., W.W. and C.S. performed the experiments; F.Z. analyzed the data and wrote the manuscript; F.B.M.B. and Y.Z. revised the manuscript; F.Z., L.J. and Y.Y. designed the experiments.
Funding
This research was funded by the National Natural Science Foundation of China (No: 31770852), Natural Science Foundation of Changchun City of China (17DY026) and“Fundamental Research Funds for the Central Universities (2412018QD010)”.
Conflicts of Interest
The authors declare no conflict of interest.
References
- 1.Huang Z.H., Li Z.H., Su Y.J., Zhu Y.F., Zeng W., Chen G.G., Liang Z.Q. Continuous production of isomalto-oligosaccharides by thermo-inactivated cells of Aspergillus niger J2 with coarse perlite as an immobilizing material. Appl. Biochem. Biotechnol. 2018;185:1088–1099. doi: 10.1007/s12010-018-2706-6. [DOI] [PubMed] [Google Scholar]
- 2.Shi Q., Hou Y.X., Juvonen M., Tuomainen P., Kajala I., Shukla S., Goyal A., Maaheimo H., Katina K., Tenkanen M. Optimization of isomaltooligosaccharide size distribution by acceptor reaction of Weissella confusa dextransucrase and characterization of novel α-(1→2)-branched isomaltooligosaccharides. J. Agric. Food Chem. 2016;64:3276–3286. doi: 10.1021/acs.jafc.6b01356. [DOI] [PubMed] [Google Scholar]
- 3.Ojha S., Mishra S., Chand S. Production of isomalto-oligosaccharides by cell bound α-glucosidase of Microbacterium sp. LWT-Food Sci. Technol. 2015;60:486–494. doi: 10.1016/j.lwt.2014.08.009. [DOI] [Google Scholar]
- 4.Soto-Maldonado C., Concha-Olmos J., Cáceres-Escobar G., Meneses-Gómez P. Sensory evaluation and glycaemic index of a food developed with flour from whole (pulp and peel) overripe banana (Musa cavendishii) discards. LWT-Food Sci. Technol. 2018;92:569–575. doi: 10.1016/j.lwt.2018.03.011. [DOI] [Google Scholar]
- 5.Meyer T.S.M., Miguel Â.S.M., Fernández D.E.R., Ortiz G.M.D. Food Production and Industry. IntechOpen; Rijeka, Croatia: 2015. Biotechnological production of oligosaccharides-applications in the food industry. [DOI] [Google Scholar]
- 6.Yen C.H., Tseng Y.H., Kuo Y.W., Lee M.C., Chen H.L. Long-term supplementation of isomalto-oligosaccharides improved colonic microflora profile, bowel function, and blood cholesterol levels in constipated elderly people—A placebo-controlled, diet-controlled trial. Nutrition. 2011;27:445–450. doi: 10.1016/j.nut.2010.05.012. [DOI] [PubMed] [Google Scholar]
- 7.Madsen L.R., Stanley S., Swann P., Oswald J. A Survey of Commercially Available Isomaltooligosaccharide-Based Food Ingredients. J. Food Sci. 2017;82:401–408. doi: 10.1111/1750-3841.13623. [DOI] [PubMed] [Google Scholar]
- 8.Rudeekulthamrong P., Sawasdee K., Kaulpiboon J. Production of long-chain isomaltooligosaccharides from maltotriose using the thermostable amylomaltase and transglucosidase enzymes. Biotechnol. Bioproc. Eng. 2013;18:778–786. doi: 10.1007/s12257-012-0777-8. [DOI] [Google Scholar]
- 9.Zhang L., Su Y.L., Zheng Y., Jiang Z.Y., Shi J.F., Zhu Y.Y., Jiang Y.J. Sandwich-structured enzyme membrane reactor for efficient conversion of maltose into isomaltooligosaccharides. Bioresour. Technol. 2010;101:9144–9149. doi: 10.1016/j.biortech.2010.07.001. [DOI] [PubMed] [Google Scholar]
- 10.Li Y.J., Zhao G.Y., Du W., Zhang T.J. Effect of dietary isomaltooligosaccharides on nutrient digestibility and concentration of glucose, insulin, cholesterol and triglycerides in serum of growing pigs. Anim. Feed Sci. Technol. 2009;151:312–315. doi: 10.1016/j.anifeedsci.2009.01.012. [DOI] [Google Scholar]
- 11.Kaulpiboon J., Rudeekulthamrong P., Watanasatitarpa S., Ito K., Pongsawasdi P. Synthesis of long-chain isomaltooligosaccharides from tapioca starch and an in vitro investigation of their prebiotic properties. J. Mol. Catal. B Enzym. 2015;120:127–135. doi: 10.1016/j.molcatb.2015.07.004. [DOI] [Google Scholar]
- 12.Sorndech W., Nakorn K.N., Tongta S., Blennow A. Isomalto-oligosaccharides: Recent insights in production technology and their use for food and medical applications. LWT-Food Sci. Technol. 2018;95:135–142. doi: 10.1016/j.lwt.2018.04.098. [DOI] [Google Scholar]
- 13.Kato N., Suyama S., Shirokane M., Kato M., Kobayashi T., Tsukagoshi N. Novel α-glucosidase from Aspergillus nidulans with strong transglycosylation activity. Appl. Environ. Microb. 2002;68:1250–1256. doi: 10.1128/AEM.68.3.1250-1256.2002. [DOI] [PMC free article] [PubMed] [Google Scholar]
- 14.Casa-Villegas M., Marín-Navarro J., Polaina J. Synthesis of isomaltooligosaccharides by Saccharomyces cerevisiae cells expressing Aspergillus niger α-glucosidase. ACS Omega. 2017;2:8062–8068. doi: 10.1021/acsomega.7b01189. [DOI] [PMC free article] [PubMed] [Google Scholar]
- 15.Chen P., Xu R.X., Wang J.H., Wu Z.R., Yan L., Zhao W.B., Liu Y.H., Ma W.T., Shi X.F., Li H.Y. Starch biotransformation into isomaltooligosaccharides using thermostable alpha-glucosidase from Geobacillus stearothermophilus. PeerJ. 2018;6:e5086. doi: 10.7717/peerj.5086. [DOI] [PMC free article] [PubMed] [Google Scholar]
- 16.Fernández-Arrojo L., Marin D., De Segura A.G., Linde D., Alcalde M., Gutiérrez-Alonso P., Ghazi I., Plou F.J., Fernández-Lobato M., Ballesteros A. Transformation of maltose into prebiotic isomaltooligosaccharides by a novel α-glucosidase from Xantophyllomyces dendrorhous. Process Biochem. 2007;42:1530–1536. doi: 10.1016/j.procbio.2007.08.007. [DOI] [Google Scholar]
- 17.Goffin D., Delzenne N., Blecker C., Hanon E., Deroanne C., Paquot M. Will isomalto-oligosaccharides, a well-established functional food in Asia, break through the European and American market? The status of knowledge on these prebiotics. Crit. Rev. Food Sci. Nutr. 2011;51:394–409. doi: 10.1080/10408391003628955. [DOI] [PubMed] [Google Scholar]
- 18.Chen D.L., Tong X., Chen S.W., Chen S., Wu D., Fang S.G., Wu J., Chen J. Heterologous expression and biochemical characterization of α-glucosidase from Aspergillus niger by Pichia pastroris. J. Agric. Food Chem. 2010;58:4819–4824. doi: 10.1021/jf1000502. [DOI] [PubMed] [Google Scholar]
- 19.Zhao N.N., Xu Y.S., Wang K., Zheng S. Synthesis of isomalto-oligosaccharides by Pichia pastoris displaying the Aspergillus niger α-glucosidase. J. Agric. Food Chem. 2017;65:9468–9474. doi: 10.1021/acs.jafc.7b04140. [DOI] [PubMed] [Google Scholar]
- 20.Hung V.S., Hatada Y.J., Goda S., Lu J., Hidaka Y.K., Li Z.J., Akita M., Ohta Y., Watanabe K., Matsui H., et al. α-Glucosidase from a strain of deep-sea Geobacillus: A potential enzyme for the biosynthesis of complex carbohydrates. Appl. Microbial. Biot. 2005;68:757–765. doi: 10.1007/s00253-005-1977-3. [DOI] [PubMed] [Google Scholar]
- 21.Raasch C., Streit W., Schanzer J., Bibel M., Gosslar U., Liebl W. Thermotoga maritima AglA, an extremely thermostable NAD+-, Mn2+-, and thiol-dependent α-glucosidase. Extremophiles. 2000;4:189–200. doi: 10.1007/PL00010711. [DOI] [PubMed] [Google Scholar]
- 22.Olusanya O., Olutiola P.O. Characterisation of maltase from enteropathogenic Escherichia coli. FEMS Microbial. Lett. 1986;36:239–244. doi: 10.1111/j.1574-6968.1986.tb01702.x. [DOI] [Google Scholar]
- 23.Yamasaki Y., Suzuki Y., Ozawa J. Certain properties of α-glucosidase from Mucor racemosus. Agric. Biol. Chem. 1977;41:1559–1565. doi: 10.1271/bbb1961.41.1559. [DOI] [Google Scholar]
- 24.Gutiérrez-Alonso P., Gimeno-Pérez M., Ramírez-Escudero M., Plou F.J., Sanz-Aparicio J., Fernández-Lobato M. Molecular characterization and heterologous expression of a Xanthophyllomyces dendrorhous α-glucosidase with potential for prebiotics production. Appl. Microbial. Biot. 2016;100:3125–3135. doi: 10.1007/s00253-015-7171-3. [DOI] [PubMed] [Google Scholar]
- 25.Prakash O., Jaiswal N. α-Amylase: An ideal representative of thermostable enzymes. Appl. Biochem. Biotech. 2010;160:2401–2414. doi: 10.1007/s12010-009-8735-4. [DOI] [PubMed] [Google Scholar]
- 26.Bradford M.M. A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of protein-dye binding. Anal. Biochem. 1976;72:248–254. doi: 10.1016/0003-2697(76)90527-3. [DOI] [PubMed] [Google Scholar]