| Literature DB >> 35205038 |
Marion Nabot1,2, Marie Guérin1,2, Dharini Sivakumar3, Fabienne Remize4, Cyrielle Garcia1,2.
Abstract
Various homopolysaccharides (HoPSs) can be produced by bacteria: α- and β-glucans, β-fructans and α-galactans, which are polymers of glucose, fructose and galactose, respectively. The synthesis of these compounds is catalyzed by glycosyltransferases (glycansucrases), which are able to transfer the monosaccharides in a specific substrate to the medium, which results in the growth of polysaccharide chains. The range of HoPS sizes is very large, from 104 to 109 Da, and mostly depends on the carbon source in the medium and the catalyzing enzyme. However, factors such as nitrogen nutrients, pH, water activity, temperature and duration of bacterial culture also impact the size and yield of production. The sequence of the enzyme influences the structure of the HoPS, by modulating the type of linkage between monomers, both for the linear chain and for the ramifications. HoPSs' size and structure have an effect on rheological properties of some foods by their influence on viscosity index. As a consequence, the control of structural and environmental factors opens ways to guide the production of specific HoPS in foods by bacteria, either by in situ or ex situ production, but requires a better knowledge of HoPS production conditions.Entities:
Keywords: exopolysaccharide; natural polymers; rheology; texture
Year: 2022 PMID: 35205038 PMCID: PMC8869377 DOI: 10.3390/biology11020171
Source DB: PubMed Journal: Biology (Basel) ISSN: 2079-7737
Figure 1Classification of bacterial homopolysaccharides according to the enzymes involved and their linear chain linkages.
Size and linkages according to the producing strain. HoPS: homopolysaccharide; Glc: glucose units; Fru: fructose units.
| Strain | HoPS | Molecular Weight Range (Da) | Linkage | Reference |
|---|---|---|---|---|
| Dextran | 9 × 107 | α(1→6) Glc linear | [ | |
| Dextran | 4 × 108 | α(1→6) Glc and branched | [ | |
| Dextran | 2 × 108 | α(1→6) Glc and partially branched in the | [ | |
| Dextran | 6 × 105 | 95% α(1→6) Glc and 5% α(1→3) Glc | [ | |
|
| Dextran | 1 × 104 to 4 × 104 | α(1→6) Glc linear | [ |
| Reuteran | α(1→6) Glc and 4,6-disubstituted α-glucosyl units at the branching points | [ | ||
| β-Glucan | β(1 → 3) Glc ramified with β-Glc residues at position | [ | ||
| Levan | 2 × 105 to 2 × 106 | 98% β(2→6) Fru and 2% β(1→2) and β(2→6) Fru branched | [ | |
| Levan | β(2→6) fructofuranoside | [ | ||
|
| Inulin | 11 × 106 | β(2→1) Fru glycosidic and Fru branched at the β(2→6) position | [ |
| Inulin | 6 × 106 | β(2→1) Fru glycosidic | [ | |
| Galactan | α(1 → 6) galactose | [ |
Influence of culture conditions and strains on HoPS production yield.
| Strain | MW (Da) | Optimum Temperature (°C) | pH | Medium Composition | Yield (g L−1) | Application | Reference |
|---|---|---|---|---|---|---|---|
| 8.8 × 107 | 25 | 6.8 | MRS 1 medium | 71.23 | Used in food industries as an emulsifier or as part of starter culture | [ | |
| 4.4 × 108 | 30 | 4.8 | CDM 2 0.8% sucrose | 1.25 | Used as adjuvant and stabilizer in food industries | [ | |
| 1.7 × 108 | 30 | MRS 2% sucrose | 1.72 | Used for biofilm formation | [ | ||
| 7.2 × 108 | 30 | 4.0–4.1 | MRS 10% sucrose | Used in bakery for sorghum bread | [ | ||
| 35 | 4.7 | Sucrose (purified enzyme) | 5.12 | [ | |||
|
| 37 | 4.8 | MRS medium sucrose | 5.2 | [ | ||
| 1.0 × 107 | 37 | 3.6 | MRS 10% sucrose | Used in bakery for sorghum bread | [ | ||
| 37 | 5.6–5.8 | SM 3 sucrose 20% | 70.60 | Used in pharmaceutical industries as a commercial spore, on alginate matrix for repeated production of levan | [ | ||
| 20.3 × 104 | 20 | 5 | MRS sucrose 30% | 74.00 | [ | ||
|
| 2.0 × 106 | 37 | 4.5–5.5 | In vitro enzyme | [ | ||
|
| 11.1 × 106 | 37 | 5.0 | YNB 4 | 2.10 | [ | |
| 8.9 × 106 | 37 | 3.7–3.8 | MRS 2.5% sucrose or raffinose | [ | |||
| 5.8 × 106 | 35 | 5.5 | sucrose | 53.00 | [ |
1 MRS is composed of sucrose, yeast extract, beef extract, anhydrous sodium acetate, ammonium citrate; 2 CDM, chemically defined medium; 3 SM, Spizizen medium; 4 YNB, yeast nitrogen base.
Figure 2Relation between food matrix, processing parameters and product technological parameters.
Influence of some food pretreatment and processing condition on EPS production and properties.
| EPS | Strain | Processing Conditions | Effects | Reference |
|---|---|---|---|---|
| Dextran | Different fermented flours (buckwheat, quinoa, sorghum and teff) used as the basis for bread recipes using sourdough | Yield depended on the substrate and was highest in buckwheat and quinoa sourdough. The level of maltose in flour influences the MW of synthetized EPSs in sourdoughs (lower maltose in buckwheat resulting in the most high-MW dextran). | [ | |
| Dextran | [ | |||
| Dextran | Lentil flour sprouting | Increase slightly the dextran synthesis in comparison to nonsprouted lentil sourdoughs (9.7% and 9.2% w/w flour weight, respectively). | [ | |
| EPS | Kefir starter culture | Ultrasonic sound waves | The treatment allows kefir production in a shorter time by affecting the growth rate and lactic acid and EPS production rate. | [ |
| EPS | Ripening period and fermentation temperature | Increase of EPS production level, associated with hardness reduction of the fat-reduced products and lower loss and storage moduli, when the ripening period was prolonged and the fermentation temperature was higher. | [ | |
| Dextran | Only HPMC and the dextran of | [ | ||
| Dextran | Stabilization, prevention of protein aggregation. Improvement in rheological and textural parameters in sucrose-added pastes after fermentation. | [ | ||
| Dextran | Quinoa flour subjected to desaponification and gelatinization prior to fermentation | The content of 35%, w/w of quinoa flour in water was determined as optimal regarding the viscosity parameter. The viscosity and water holding capacity increased during fermentation with | [ |