| Literature DB >> 28980453 |
Lea Bircher1, Clarissa Schwab1, Annelies Geirnaert1, Christophe Lacroix1.
Abstract
Interest in faecal microbiota transplantation (FMT) has increased as therapy for intestinal diseases, but safety issues limit its widespread use. Intestinal fermentation technology (IFT) can produce controlled, diverse and metabolically active 'artificial' colonic microbiota as potential alternative to common FMT. However, suitable processing technology to store this artificial microbiota is lacking. In this study, we evaluated the impact of the two cryoprotectives, glycerol (15% v/v) and inulin (5% w/v) alone and in combination, in preserving short-chain fatty acid formation and recovery of major butyrate-producing bacteria in three artificial microbiota during cryopreservation for 3 months at -80°C. After 24 h anaerobic fermentation of the preserved microbiota, butyrate and propionate production were maintained when glycerol was used as cryoprotectant, while acetate and butyrate were formed more rapidly with glycerol in combination with inulin. Glycerol supported cryopreservation of the Roseburia spp./Eubacterium rectale group, while inulin improved the recovery of Faecalibacterium prausnitzii. Eubacterium hallii growth was affected minimally by cryopreservation. Our data indicate that butyrate producers, which are key organisms for gut health, can be well preserved with glycerol and inulin during frozen storage. This is of high importance if artificially produced colonic microbiota is considered for therapeutic purposes.Entities:
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Year: 2017 PMID: 28980453 PMCID: PMC5743790 DOI: 10.1111/1751-7915.12844
Source DB: PubMed Journal: Microb Biotechnol ISSN: 1751-7915 Impact factor: 5.813
Figure 1Microbial composition of donor faeces and fermentation effluents. Relative abundance of microbial phyla (A) and families (B) in the fermentation effluents and corresponding donors was analysed by V4 region 16S rRNA gene sequencing.
Relative abundance of Roseburia spp./E. rectale group, F. prausnitzii and E. hallii in fermentation effluents
| Targeted butyrate‐producing bacteria | Relative abundance | ||
|---|---|---|---|
| Effluent 1.1 | Effluent 1.2 | Effluent 2 | |
|
| 0.7 | 0.1 | 0.0 |
|
| 11.0 | 5.6 | 3.1 |
|
| 0.0 | 0.0 | 0.0 |
But genes of Roseburia spp./E.rectale and F. prausnitzii and 16S rRNA of E. hallii were targeted by qPCR. Relative abundance was calculated relative to total 16S rRNA gene copies. Results for but genes were multiplied by five to account for multiple 16S rRNA gene copies.
Percentage of total bacteria numbers from single measurements.
Figure 2Percentage of main metabolites in fermentation effluent samples. Ratios of major metabolites acetate, propionate and butyrate were calculated from the concentrations measured by HPLC‐RI giving an acetate:propionate:butyrate ratio of 1:0.2:0.8 for effluent 1.1, 1:0.4:1.3 for effluent 1.2 and 1:0.5:0.4 for effluent 2.
Figure 3Kinetics of main metabolites production after reactivation of effluent microbiota stored for 3 months. Main metabolites acetate, propionate and butyrate were analysed by HPLC‐RI after reactivation in batch fermentations. Each point represents the average of three replicates with standard deviation.
Production of major SCFA after 24 h batch fermentation of effluent samples prior and poststorage at −80°C
| Protective buffer | Effluent 1.1 | Effluent 1.2 | Effluent 2 | ||||||
|---|---|---|---|---|---|---|---|---|---|
| Prior to freezing (mM) | Postfreezing (mM) | Recovery (%) | Prior to freezing (mM) | Postfreezing (mM) | Recovery (%) | Prior to freezing (mM) | Postfreezing (mM) | Recovery (%) | |
| Glycerol and Inulin | |||||||||
| Acetate | 79.9 ± 0.2 | 70.6 ± 1.1 | 88.4 | 70.3 ± 1.9 | 61.7 ± 0.4 | 87.8 | 54.5 ± 0.5 | 52.7 ± 0.6 | 96.7 |
| Propionate | 12.2 ± 0.3 | 13.0 ± 0.3 | 106.6 | 17.2 ± 0.6 | 16.8 ± 0.5 | 98.0 | 14.2 ± 0.2 | 17.8 ± 0.2 | 125.3 |
| Butyrate | 17.1 ± 0.2 | 18.2 ± 0.7 | 106.4 | 19.9 ± 1.2 | 19.4 ± 1.0 | 97.5 | 12.9 ± 0.6 | 16.2 ± 0.1 | 125.6 |
| Total SCFA | 109.1 ± 0.7 | 101.9 ± 0.8 | 93.4 | 107.4 ± 1.3 | 98.0 ± 0.3 | 91.1 | 81.6 ± 0.6 | 86.8 ± 0.9 | 106.4 |
| Glycerol | |||||||||
| Acetate | 80.2 ± 4.0 | 68.6 ± 0.5 | 85.5 | 70.6 ± 2.0 | 60.3 ± 0.5 | 85.4 | 57.2 ± 1.1 | 53.8 ± 1.3 | 94.1 |
| Propionate | 9.8 ± 3.2 | 12.7 ± 1.1 | 129.6 | 16.4 ± 1.4 | 16.7 ± 0.9 | 102.1 | 17.7 ± 0.4 | 15.9 ± 0.8 | 90.0 |
| Butyrate | 17.1 ± 1.2 | 16.2 ± 0.6 | 94.7 | 20.9 ± 1.5 | 17.4 ± 0.1 | 83.5 | 16.4 ± 0.4 | 16.9 ± 0.1 | 103.3 |
| Total SCFA | 107.1 ± 6.0 | 97.5 ± 1.3 | 91.0 | 107.9 ± 1.9 | 94.5 ± 1.2 | 87.6 | 91.2 ± 1.0 | 86.6 ± 1.6 | 95.0 |
| Inulin | |||||||||
| Acetate | 77.9 ± 1.1 | 67.6 ± 1.4 | 86.8 | 71.0 ± 1.2 | 65.6 ± 3.1 | 92.4 | 59.4 ± 1.0 | 49.0 ± 0.9 | 82.5 |
| Propionate | 13.8 ± 0.3 | 9.3 ± 0.4 | 67.4 | 17.7 ± 0.1 | 17.4 ± 1.1 | 98.4 | 23.3 ± 0.3 | 16.2 ± 0.5 | 69.6 |
| Butyrate | 20.7 ± 0.7 | 9.4 ± 0.2 | 45.4 | 19.1 ± 0.5 | 16.0 ± 0.1 | 83.8 | 14.1 ± 0.0 | 14.4 ± 1.2 | 102.0 |
| Total SCFA | 112.7 ± 0.7 | 86.3 ± 1.6 | 76.6 | 107.7 ± 0.9 | 99.0 ± 3.9 | 91.9 | 96.8 ± 1.3 | 79.6 ± 2.0 | 82.2 |
| Control | |||||||||
| Acetate | 79.7 ± 1.5 | 63.5 ± 3.3 | 79.7 | 74.1 ± 1.5 | 60.5 ± 2.1 | 81.6 | 59.4 ± 0.2 | 47.9 ± 0.2 | 80.7 |
| Propionate | 12.6 ± 0.5 | 4.9 ± 0.5 | 38.9 | 18.1 ± 0.5 | 15.4 ± 0.3 | 85.2 | 21.6 ± 0.3 | 13.3 ± 0.4 | 61.4 |
| Butyrate | 16.3 ± 2.7 | 9.9 ± 0.5 | 60.7 | 18.9 ± 0.2 | 15.6 ± 0.8 | 82.3 | 12.9 ± 0.3 | 13.8 ± 0.7 | 107.2 |
| Total SCFA | 108.6 ± 1.7 | 78.3 ± 3.6 | 72.1 | 111.1 ± 2.2 | 91.5 ± 2.5 | 82.3 | 93.9 ± 0.3 | 75.0 ± 0.9 | 79.9 |
Main metabolites acetate, propionate and butyrate formed by effluents immediately after processing (t = 0) and after 3 months storage at −80°C were analysed by HPLC‐RI (means and standard deviations of independent fermentation triplicates).
Indicates that metabolite formed in treatment is significantly different from the control within the same effluent microbiota (P < 0.05).
Indicates that metabolite formed is significantly different prior and postfreezing within the same treatment and effluent microbiota (P < 0.05).
Growth and relative abundance of selected butyrate‐producing bacteria after 24 h batch fermentation of effluent samples prior and poststorage at −80°C
| Protective buffer | Effluent 1.1 | Effluent 1.2 | Effluent 2 | |||||||||
|---|---|---|---|---|---|---|---|---|---|---|---|---|
| Prior to freezing | Postfreezing | Prior to freezing | Postfreezing | Prior to freezing | Postfreezing | |||||||
| Δlog | Rel. ab. | Δlog | Rel. ab. | Δlog | Rel. ab. | Δlog | Rel. ab. | Δlog | Rel. ab. | Δlog | Rel. ab. | |
| Roseburia spp./ | ||||||||||||
| Glycerol & Inulin | 1.0 ± 0.0 | 6.3 ± 0.6 | 1.0 ± 0.1 | 6.9 ± 0.7 | 1.0 ± 0.1 | 4.7 ± 0.5 | 0.1 ± 0.1 | 1.4 ± 0.3 | 1.3 ± 0.0 | 0.2 ± 0.0 | 1.3 ± 0.0 | 0.1 ± 0.0 |
| Glycerol | 0.9 ± 0.2 | 3.3 ± 2.6 | 1.0 ± 0.0 | 6.4 ± 0.5 | 1.2 ± 0.1 | 6.5 ± 0.6 | −0.4 ± 0.0 | 0.5 ± 0.1 | 1.4 ± 0.2 | 0.2 ± 0.1 | 1.7 ± 0.1 | 0.2 ± 0.1 |
| Inulin | 1.1 ± 0.1 | 9.9 ± 1.1 | −0.2 ± 0.1 | 0.4 ± 0.0 | 1.2 ± 0.0 | 6.5 ± 0.6 | −0.5 ± 0.0 | 0.4 ± 0.0 | 0.7 ± 0.1 | 0.1 ± 0.0 | 0.8 ± 0.1 | 0.0 ± 0.0 |
| Control | 0.8 ± 0.2 | 4.8 ± 3.6 | −0.6 ± 0.3 | 0.2 ± 0.1 | 1.2 ± 0.0 | 7.4 ± 0.9 | −0.9 ± 0.2 | 0.2 ± 0.1 | 0.7 ± 0.2 | 0.1 ± 0.0 | 0.8 ± 0.1 | 0.0 ± 0.0 |
|
| ||||||||||||
| Glycerol & Inulin | 0.4 ± 0.0 | 3.6 ± 0.5 | 0.5 ± 0.1 | 1.1 ± 0.1 | 0.7 ± 0.1 | 0.4 ± 0.2 | 0.6 ± 0.1 | 1.7 ± 0.4 | 0.4 ± 0.1 | 0.3 ± 0.0 | 1.4 ± 0.1 | 1.2 ± 0.2 |
| Glycerol | 0.4 ± 0.1 | 3.8 ± 0.7 | −0.4 ± 0.0 | 0.1 ± 0.0 | 0.8 ± 0.0 | 0.4 ± 0.0 | 0.0 ± 0.1 | 0.5 ± 0.1 | 0.8 ± 0.0 | 0.8 ± 0.1 | 1.1 ± 0.0 | 0.7 ± 0.1 |
| Inulin | 0.6 ± 0.0 | 5.5 ± 0.2 | 0.8 ± 0.2 | 2.0 ± 0.3 | 0.5 ± 0.0 | 0.5 ± 0.0 | 0.7 ± 0.0 | 2.5 ± 0.1 | 1.0 ± 0.0 | 1.6 ± 0.1 | 1.3 ± 0.1 | 1.2 ± 0.3 |
| Control | 0.5 ± 0.0 | 4.1 ± 0.7 | 0.1 ± 0.0 | 0.4 ± 0.1 | 0.8 ± 0.1 | 0.5 ± 0.0 | 0.1 ± 0.1 | 0.6 ± 0.1 | 0.8 ± 0.1 | 1.0 ± 0.1 | 0.4 ± 0.1 | 0.1 ± 0.0 |
|
| ||||||||||||
| Glycerol & Inulin | 2.6 ± 0.1 | 1.0 ± 0.1 | 2.5 ± 0.2 | 1.8 ± 0.4 | 2.1 ± 0.0 | 0.5 ± 0.1 | 2.0 ± 0.1 | 2.5 ± 0.3b | 2.2 ± 0.0 | 0.6 ± 0.1 | 2.2 ± 0.1 | 0.7 ± 0.1 |
| Glycerol | 2.0 ± 0.4 | 0.3 ± 0.2 | 2.3 ± 0.0 | 1.2 ± 0.0 | 2.0 ± 0.0 | 0.5 ± 0.1 | 1.8 ± 0.1 | 1.8 ± 0.1 | 1.8 ± 0.2 | 0.3 ± 0.1 | 2.2 ± 0.1 | 0.7 ± 0.1 |
| Inulin | 2.0 ± 0.1 | 0.3 ± 0.0 | 2.3 ± 0.0 | 1.2 ± 0.2 | 2.1 ± 0.1 | 0.5 ± 0.0 | 1.8 ± 0.1 | 1.7 ± 0.1 | 2.1 ± 0.1 | 0.6 ± 0.1 | 2.0 ± 0.1 | 0.5 ± 0.1 |
| Control | 1.9 ± 0.0 | 0.2 ± 0.0 | 2.2 ± 0.0 | 1.1 ± 0.1 | 1.9 ± 0.2 | 0.4 ± 0.1 | 1.7 ± 0.1 | 1.5 ± 0.1 | 2.1 ± 0.1 | 0.6 ± 0.2 | 1.9 ± 0.1 | 0.3 ± 0.1 |
Growth (Δlog) was determined as log increase during 24 h batch fermentation of effluents immediately after processing (t = 0) and after 3 months storage at −80°C analysed by qPCR. Relative abundance (rel. ab.) was determined as ratio of target gene of respective bacterial group/total bacteria (means and standard deviations of independent fermentation triplicates).
Indicates that growth respectively relative abundance in treatment is significantly different from the control within the same effluent microbiota (P < 0.05).
Indicates that growth respectively relative abundance is significantly different prior and postfreezing within the same treatment and effluent microbiota (P < 0.05).