| Literature DB >> 27271598 |
Huu-Thanh Nguyen1,2, Dieu-Hien Truong3, Sonagnon Kouhoundé4, Sokny Ly5, Hary Razafindralambo6, Frank Delvigne7.
Abstract
The literature presents a growing body of evidence demonstrating the positive effect of probiotics on health. Probiotic consumption levels are rising quickly in the world despite the fluctuation of their viability and functionality. Technological methods aiming at improving probiotic characteristics are thus highly wanted. However, microbial metabolic engineering toolbox is not available for this kind of application. On the other hand, basic microbiology teaches us that bacteria are able to exhibit adaptation to external stresses. It is known that adequately applied sub-lethal stress, i.e., controlled in amplitude and frequency at a given stage of the culture, is able to enhance microbial robustness. This property could be potentially used to improve the viability of probiotic bacteria, but some technical challenges still need to be overcome before any industrial implementation. This review paper investigates the different technical tools that can be used in order to define the proper condition for improving viability of probiotic bacteria and their implementation at the industrial scale. Based on the example of Bifidobacterium bifidum, potentialities for simultaneously improving viability, but also functionality of probiotics will be described.Entities:
Keywords: biochemical engineering; cellular robustness; exopolysaccharide; prebiotics; probiotics; sub-lethal stress; survival
Mesh:
Year: 2016 PMID: 27271598 PMCID: PMC4926401 DOI: 10.3390/ijms17060867
Source DB: PubMed Journal: Int J Mol Sci ISSN: 1422-0067 Impact factor: 5.923
Figure 1Fermentation devices that can be used for improving the viability of probiotics: (A) Batch cultivation devices based on the recirculation of microbial cells between a stirred bioreactor and a plug-flow recycle loop. By his way, gradient of environmental conditions can be generated at the level of the recycle loop allowing to expose the cells to progressive and recurrent stresses [8]; (B) Continuous cultivation devices based on two stirred bioreactors in series. In this case, only two distinct cultivation conditions can be generated. However, this device had the advantage of maintaining the microbial population at a given stage by chemostat control [7]. Typical single cell traces (i.e., the history of environmental conditions met by cells) are represented for each bioreactor. As shown, the plug-flow recycle loop allows for the generation of much more variable environmental states from 1 to n (depending on the operating conditions).
Effect of sub-lethal temperature conditions on survival and heat tolerance to lethal temperature in Lactobacillus (Lb.) strains during the exponential growth phase review by De Angelis [42].
| Strain | Lethal Condition | Surviving Cells (%) | Sub-Lethal Condition | Improved Viability Rate |
|---|---|---|---|---|
| 63 °C, 20 min | 0.1–1 | 52 °C, 20 min | 11 | |
| 63 °C, 20 min | 0.1–1 | 50 °C, 20 min | 27 | |
| 60 °C, 30 min | 0.003 | 53 °C, 30 min | 166 | |
| 54 °C, 20 min | 0.1–1 | 42 °C, 20 min | 5 | |
| 60 °C, 10 min | ND | 52 °C, 15 min | 300–700 | |
| 52 °C, 30 min | 0.48 | 42 °C, 90 min | 24 |
The viability rate is calculated as the ratio: survival of adapted cells (%)/survival of control cells (%). The controls correspond to non-adapted cells to sub-lethal condition before exposure to lethal condition. ND: Not determined.
Figure 2Effect of sub-lethal heat shock (37–42 °C when cells are crossing the recycle loop, two-compartment reactor, see Figure 1) on cell size and zeta potential. Annulation of zeta potential is observed in the case of the bioreactor performed with heat shock. In this case, stress leads to the excretion of an EPS capsule that can be exploited in order to further increase the robustness of the strain during downstream processing operations (adapted from Nguyen [8]). (square: reference, well-mixed bioreactor, diamond: cold-shock two-compartment bioreactor, triangle: heat-shock two-compartment bioreactor).
Figure 3Diagram showing the biosynthetic pathways involved for the production of exopolysaccharides from lactose, fructose, galactose and glucose by lactic acid bacteria.