A systematic, complexity-reduction approach to dissect the kombucha tea microbiome
- Department of Bioengineering, University of Illinois Urbana-Champaign, United States
- Carl R. Woese Institute for Genomic Biology, University of Illinois Urbana-Champaign, United States
- College of Food Science and Nutritional Engineering, China Agricultural University, China
- Department of Physics, University of Illinois Urbana-Champaign, United States
- Center for Biophysics and Quantitative Biology, University of Illinois Urbana-Champaign, United States
- National Center for Supercomputing Applications, United States
Figures
Figure 1
Characterization of the native KT microbiome.
(A) Image of a typical kombucha tea fermentation containing both broth and pellicle. (B, C) Microbial composition in the broths and pellicles of different kombucha teas at the bacterial (B) and …
Figure 2
Population and metabolic quantification of two-species core candidates.
(A) Colony forming units (CFU) counting of 25 two-species core candidates and 10 monoculture controls upon fermentation. Each core candidate is composed of one bacterial and one fungal species …
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Figure 2—source data 1
List of isolated bacterial and fungal species.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig2-data1-v1.xlsx
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Figure 2—source data 2
Counting data of different bacteria and yeasts co-cultures.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig2-data2-v1.xlsx
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Figure 2—source data 3
Chemical property analysis of the core candidates.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig2-data3-v1.xlsx
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Figure 2—source data 4
Statistics of HCA and PCA analysis.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig2-data4-v1.xlsx
Figure 3 with 1 supplement
Temporal compositional and metabolic dynamics of the minimal core (B2Y1).
(A, B) Populations of B2 (A) and Y1 (B) in broth throughout the course of a fermentation starting with 50 g/L sucrose. (C) Bacterium-to-yeast population ratio of the microbes in broth. (D) Ratio of …
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Figure 3—source data 1
Counting data of the minimal core.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig3-data1-v1.xlsx
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Figure 3—source data 2
Chemical property analysis of the minimal core.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig3-data2-v1.xlsx
Figure 3—figure supplement 1
Population dynamics and pellicle formation of the minimal core (B2Y1).
(A, B) Growth rates of B2 (A) and Y1 (B) in tea broth during the KT fermentation with 50 g/L sucrose. (C) Image of a typical pellicle formed during the fermentation. (D, E) Populations of B2 (D) and …
Figure 4 with 1 supplement
Comprehensive fermentation tests for the B2 and Y1 monocultures with different carbon sources.
Sucrose (abbreviated as S, 10 g/L), glucose (G, 10 g/L), fructose (F, 10 g/L), ethanol (E, 50 mL/L), and acetate (A, 2 g/L) were used alone or in combination for fermentation. The number on top left …
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Figure 4—source data 1
Counting and metabolic data of the B2 and Y1 monocultures.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig4-data1-v1.xlsx
Figure 4—figure supplement 1
Images of pellicles formed by B2 monoculture with different carbon sources.
GE: glucose and ethanol; GA: glucose and acetate; GFE: glucose, fructose and ethanol; GEA: glucose, ethanol and acetate.
Figure 5 with 4 supplements
Summary of metabolic processes underlying the core.
Black arrows refer to metabolic fluxes while brown arrows correspond to positive or negative regulatory interactions. The numbers associated with each arrow are the corresponding fermentation assays …
Figure 5—figure supplement 1
Sucrose invertase activity of Y1 monoculture and B2Y1 co-culture at different fermentation times.
The invertase activity is defined as the amount of sucrose reduction per minute for a given amount of yeast cells (inoculation amount: 1*106 CFU/mL). Bars and error bars correspond to means and …
Figure 5—figure supplement 2
Comparation of the population and metabolic dynamics of Y1 monoculture and B2Y1 co-culture.
(A, B) Population (A) and growth rate (B) of Y1 in monoculture and in the B2Y1 co-culture. (C–H) pH, carbon sources and metabolites during the fermentations of the monoculture and the co-culture. …
Figure 5—figure supplement 3
Population dynamics and metabolic profiles of the fermentations involving fixed Y1 and varied B2 initial abundances.
(A) Y1 population dynamics. (B) B2 population dynamics. (C–H) pH, carbon sources and metabolites during the fermentation. The initial Y1 inoculation was fixed as 1*106 CFU/mL but the B2 inoculation …
Figure 5—figure supplement 4
Population dynamics and metabolic profiles of the fermentations involving fixed B2 and varied Y1 initial abundances.
(A) Y1 population dynamics. (B) B2 population dynamics. (C–H) pH, carbon sources and metabolites during the fermentation. The initial B2 inoculation was fixed as 1*106 CFU/mL but the Y1 inoculation …
Figure 6 with 3 supplements
Fermentation by synthetic communities with increased complexity and altered conditions.
(A) Schematic illustration of a ten-species community involving B1-B5 and Y1-Y5 in a fermentation with 50 g/L of initial sucrose. (B–E) Population ratio (B), sucrose (C), ethanol (D), and acetate (E)…
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Figure 6—source data 1
Counting and metabolic data of the ten-species communities.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig6-data1-v1.xlsx
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Figure 6—source data 2
Counting and metabolic data of the two-species communities.
- https://cdn.elifesciences.org/articles/76401/elife-76401-fig6-data2-v1.xlsx
Figure 6—figure supplement 1
Fermentation by synthetic communities with increased complexity and altered conditions.
(A) Schematic illustration of a ten-species community involving B1-B5 and Y1-Y5 in a fermentation with 50 g/L of initial sucrose. (B–D) pH (B), glucose (C) and fructose (D) throughout the course of …
Figure 6—figure supplement 2
Temporal compositional and metabolic dynamics of the minimal core (B2Y1) during a fermentation with 5 g/L of initial sucrose.
(A, B) B2 (A) and Y1(B) population dynamics throughout the fermentation. (C) The B2-to-Y1 ratio in the fermentation. (D–I) pH, carbon sources and metabolites throughout the course of the …
Figure 6—figure supplement 3
Temporal compositional and metabolic dynamics of the minimal core (B2Y1) during a fermentation with 100 g/L of initial sucrose.
(A, B) B2 (A) and Y1(B) population dynamics during the fermentation. (C) The B2-to-Y1 ratio in the fermentation. (D–I) pH, carbon sources and metabolites during the fermentation driven by the core. …
Figure 7
Summary of the overall concept and steps of our complexity-reduction approach for microbiome dissection.
Tables
Key resources table
| Reagent type (species) or resource | Designation | Source or reference | Identifiers | Additional information |
|---|---|---|---|---|
| Commercial assay or kit | Fecal/soil Microbe Miniprep kit | ZYMO | Cat No./ID:D6010 | |
| Commercial assay or kit | Gluconic acid Kit | Megazyme, Ireland | Cat No./ID:K-GATE | |
| Sequence-based reagent | B-f | Huang et al., 2021 | PCR Primer | Forward primer used for amplifying bacterial DNA for Sanger sequencing |
| Sequence-based reagent | B-r | Huang et al., 2021 | PCR Primer | Reverse primer used for amplifying bacterial DNA for Sanger sequencing |
| Sequence-based reagent | NL-1 | Coton et al., 2017 | PCR Primer | Forward primer used for amplifying yeast DNA for Sanger sequencing |
| Sequence-based reagent | NL-4 | Coton et al., 2017 | PCR Primer | Reverse primer used for amplifying yeast DNA for Sanger sequencing |
| Software, algorithm | Canoco | Microcomputer Power, Ithaca, NY | Version 5.0 | |
| Software, algorithm | SIMCA | Umetricus, Sweden | Version 14.1 |
