| Literature DB >> 35206012 |
Annamaria Ricciardi1, Livia Vanessa Storti1, Marilisa Giavalisco1, Eugenio Parente1, Teresa Zotta1.
Abstract
Leuconostoc mesenteroides includes strains used as starter and/or adjunct cultures for the production of several fermented foods. In this study, the effect of anaerobic and respiratory cultivations, as well as of citrate supplementation and different pH values, was evaluated on growth, biomass, metabolite, and enzymatic activities (pyruvate oxidase, POX; NADH-dependent oxidase, NOX; NADH-dependent peroxidase, NPR) of Leuconostoc mesenteroides subsp. cremoris E30. We compared the respiration-increased growth rate and biomass production of Leuc. mesenteroides E30 to anaerobic cultivation. A supplementation of citrate impaired the growth rate of the respiratory cells. As expected, anaerobic cultures did not consume oxygen, and a similar trend in oxygen uptake was observed in respiratory cultures. The aerobic incubation caused changes in the metabolic pattern, reducing the production of ethanol in favour of acetic acid. Citrate was already exhausted in the exponential phase and did not affect the yields in acetic acid and ethanol. NOX activity increased in the presence of oxygen, while catalase was also detected in the absence of hemin. The absence of H2O2 suggested its degradation by NPR and catalase. Respiratory cultivation provided benefits (increase in growth rate, biomass, and activity in antioxidant enzymes) for Leuc. mesenteroides E30. Therefore, the exploitation of respiratory phenotypes may be useful for the formulation of competitive starter or adjunct cultures.Entities:
Keywords: Leuconostoc mesenteroides; aerobiosis; energy metabolism; respiration
Year: 2022 PMID: 35206012 PMCID: PMC8871477 DOI: 10.3390/foods11040535
Source DB: PubMed Journal: Foods ISSN: 2304-8158
Experimental design used to evaluate the effect of the type of incubation, carbon source, and pH on growth, biomass, metabolites production, and enzymatic activities.
| Fermentation | Incubation a | Citrate b | pH |
|---|---|---|---|
| F1 | AN | 0 | 6.5 |
| F2 | AN | 1 | 6.5 |
| F3 | AN | 0 | 5.5 |
| F4 | AN | 1 | 5.5 |
| F5 | RS | 0 | 6.5 |
| F6 | RS | 1 | 6.5 |
| F7 | RS | 0 | 5.5 |
| F8 | RS | 1 | 5.5 |
AN, anaerobic growth with nitrogen flow at 0.02 L/min; RS, respiratory growth with 15% dissolved oxygen (dO2%), supplementation with 1.25 μg/mL of hemin and 1 μg/mL of menaquinone. 0, absence of sodium citrate in mWMB; 1, supplementation of mWMB with 5 g/L of sodium citrate.
Figure 1Growth kinetics of Leuconostoc mesenteroides E30. The conditions of each fermentation (F1 to F8) are detailed in Table 1. X-axis, time (hours) of incubation; Y-axis, growth (lnX/X0), dissolved oxygen (dO2%), and NaOH:NaHCO3 (meq/L) consumption; black symbols, biomass production; blue line, kinetics of growth (ln X/X0) estimated with the model of Baranyi and Roberts [27] where X and X0 are, respectively, the biomass measured at each withdrawal time and at start of fermentation; green line, dO2% measured through polarographic electrode; red line, milliequivalents/L (meq/L) of NaOH:NaHCO3 consumed during fermentation. Code of fermentation name: AN, anaerobiosis; RS, respiration; 0, absence of sodium citrate in mWMB; 1, supplementation of mWMB with 5 g/L of sodium citrate; 5.5, pH controlled at 5.5; 6.5, pH controlled at 6.5.
Parameters of growth kinetics of Leuconostoc mesenteroides E30.
| Growth Condition | µmax (h−1) | lag (h) | R2 of Fit |
|---|---|---|---|
| F1_AN_0_6.5_a | 0.46 ± 0.02 | 0.00 ± 0.00 | 0.972 |
| F1_AN_0_6.5_b | 0.46 ± 0.01 | 1.38 ± 0.21 | 0.996 |
| F2_AN_1_6.5_a | 0.64 ± 0.01 | 1.05 ± 0.11 | 0.998 |
| F2_AN_1_6.5_b | 0.57 ± 0.01 | 1.13 ± 0.14 | 0.997 |
| F3_AN_0_5.5_a | 0.40 ± 0.02 | 1.92 ± 0.25 | 0.995 |
| F3_AN_0_5.5_b | 0.42 ± 0.02 | 3.09 ± 0.22 | 0.997 |
| F4_AN_1_5.5_a | 0.50 ± 0.01 | 0.00 ± 0.00 | 0.997 |
| F4_AN_1_5.5_b | 0.47 ± 0.01 | 1.54 ± 0.19 | 0.997 |
| F5_RS_0_6.5_a | 0.77 ± 0.03 | 2.17 ± 0.19 | 0.997 |
| F5_RS_0_6.5_b | 0.82 ± 0.06 | 0.36 ± 3.57 | 0.992 |
| F6_RS_1_6.5_a | 0.72 ± 0.07 | 4.58 ± 0.32 | 0.988 |
| F6_RS_1_6.5_b | 0.71 ± 0.03 | 2.58 ± 0.21 | 0.995 |
| F7_RS_0_5.5_a | 0.63 ± 0.03 | 2.11 ± 0.18 | 0.996 |
| F7_RS_0_5.5_b | 0.67 ± 0.03 | 2.41 ± 0.20 | 0.996 |
| F8_RS_1_5.5_a | 0.55 ± 0.06 | 3.24 ± 0.50 | 0.974 |
| F8_RS_1_5.5_b | 0.49 ± 0.03 | 3.00 ± 0.35 | 0.988 |
Growth condition: RS, respiratory growth (with 15% dissolved oxygen (dO2%), supplementation with 1.25 μg/mL of hemin and 1 μg/mL of menaquinone); AN, anaerobic growth (with nitrogen flow at 0.02 L/min). Conditions of each fermentation (F1 to F8) are detailed in Table 1. Code of fermentation name: AN, anaerobiosis; RS, respiration; 0, absence of sodium citrate in mWMB; 1, supplementation of mWMB with 5 g/L of sodium citrate; 5.5, controlled pH at 5.5; 6.5, pH controlled at 6.5; µmax, maximum specific growth rate; lag (h), duration of lag phase; R2 of fit quantified the goodness of modeling.
Figure 2RS, respiratory growth (with 15% dissolved oxygen (dO2%), supplementation with 1.25 μg/mL of hemin and 1 μg/mL of menaquinone); AN, anaerobic growth (with nitrogen flow at 0.02 L/min). Conditions of each fermentation (F1 to F8) are detailed in Table 1. Code of fermentation name: AN, anaerobiosis; RS, respiration; 0, absence of sodium citrate in mWMB; 1, supplementation of sodium citrate (5 g/L) in mWMB; 5.5, controlled pH at 5.5; 6.5, pH controlled at 6.5. Growth phase: E, exponential phase; S, stationary phase. Mean values and standard errors are reported.
The consumption of glucose and citrate and the production of metabolites of Leuconostoc mesenteroides E30.
| Growth Condition a | Growth Phase b | Biomass Yield c | Glucose | Lactic Acid Yield e | Acetic ACID Yield f | Ethanol Yield g |
|---|---|---|---|---|---|---|
| F1_AN_0_6.5 | E | 0.074 ± 0.032 | 34.8 ± 3.356 | 0.595 ± 0.248 | 0.038 ± 0.010 | 0.450 ± 0.0186 |
| S | 0.072 ± 0.009 | 131.93 ± 4.512 | 0.979 ± 0.043 | 0.019 ± 0.021 | 0.682 ± 0.046 | |
| F2_AN_1_6.5 | E | 0.102 ± 0.070 | 27.16 ± 21.253 | 1.707 ± 1.339 | 1.205 ± 0.978 | 0.158 ± 0.065 |
| S | 0.076 ± 0.006 | 116.81 ± 5.761 | 1.209 ± 0.070 | 0.196 ± 0.012 | 0.666 ± 0.108 | |
| F3_AN_0_5.5 | E | 0.074 ± 0.005 | 32.43 ± 0.746 | 0.763 ± 0.003 | 0.036 ± 0.024 | 0.606 ± 0.074 |
| S | 0.082 ± 0.009 | 130.78 ± 1.361 | 0.843 ± 0.001 | 0.010 ± 0.003 | 0.653 ± 0.087 | |
| F4_AN_1_5.5 | E | 0.140 ± 0.006 | 17.01 ± 2.424 | 1.706 ± 0.278 | 1.530 ± 0.176 | 0.247 ± 0.185 |
| S | 0.082 ± 0.006 | 122.02 ± 2.834 | 1.186 ± 0.287 | 0.177 ± 0.038 | 0.590 ± 0.148 | |
| F5_RS_0_6.5 | E | 0.232 ± 0.036 | 13.71 ± 4.847 | 0.802 ± 0.186 | 0.726 ± 0.181 | 0.090 ± 0.098 |
| S | 0.135 ± 0.051 | 126.43 ± 1.510 | 0.613 ± 0.011 | 0.634 ± 0.008 | 0.130 ± 0.146 | |
| F6_RS_1_6.5 | E | 0.145 ± 0.022 | 24.78 ± 1.491 | 0.924 ± 0.164 | 0.000 ± 0.000 | 0.000 ± 0.000 |
| S | 0.128 ± 0.004 | 124.88 ± 1.920 | 0.783 ± 0.069 | 0.611 ± 0.028 | 0.105 ± 0.059 | |
| F7_RS_0_5.5 | E | 0.077 ± 0.027 | 43.77 ± 14.169 | 0.244 ± 0.088 | 0.147 ± 0.073 | 0.000 ± 0.000 |
| S | 0.113 ± 0.005 | 126.91 ± 4.754 | 0.468 ± 0.070 | 0.499 ± 0.022 | 0.089 ± 0.097 | |
| F8_RS_1_5.5 | E | 0.455 ± 0.174 | 11.21 ± 0.559 | 1.877 ± 0.053 | 1.649 ± 0.094 | 0.000 ± 0.000 |
| S | 0.102 ± 0.033 | 122.41 ± 4.661 | 0.940 ± 0.009 | 0.469 ± 0.025 | 0.100 ± 0.008 |
Growth conditions: RS, respiratory growth (with 15% dissolved oxygen (dO2%), supplementation with 1.25 μg/mL of hemin and 1 μg/mL of menaquinone); AN, anaerobic growth (with nitrogen flow at 0.02 L/min). The conditions of each fermentation (F1 to F8) are detailed in Table 1. Code of fermentation name: AN, anaerobiosis; RS, respiration; 0, absence of sodium citrate in mWMB; 1, supplementation of mWMB with 5 g/L of sodium citrate; 5.5, controlled pH at 5.5; 6.5, pH controlled at 6.5. Growth phase: E, exponential phase; S, stationary phase. Mean values of two biological replicates ± standards errors are reported. Biomass yield: calculated as (X-X0)/(S0-S), i.e., biomass production (X-X0), g/L, relative to consumed glucose (S0-S), g/L. Glucose consumed: consumed glucose (S0-S), mM. Lactate yield: production of DL-lactic acid (P-P0), g/L, relative to consumed glucose (S0-S), g/L. Acetate yield: production of acetic acid (A-A0), g/L, relative to consumed glucose (S0-S), g/L. Ethanol yield: production of acetic acid (E-E0), g/L, relative to consumed glucose (S0-S), g/L.
Figure 3Enzymatic activity of NADH oxidase (NOX, (A)), NADH peroxidase (NPR, (B)), and catalase (CAT, (C)), respectively, expressed in µkatal/mg protein. Growth conditions: RS, respiratory growth (with 15% dissolved oxygen (dO2%), supplementation with 1.25 μg/mL of hemin and 1 μg/mL of menaquinone); AN, anaerobic growth (with nitrogen flow at 0.02 L/min). Conditions of each fermentation (F1 to F8) are detailed in Table 1. Code of fermentation name: AN, anaerobiosis; RS, respiration; 0, absence of sodium citrate in mWMB; 1, supplementation of sodium citrate (5 g/L) in mWMB; 5.5, controlled pH at 5.5; 6.5, pH controlled at 6.5. Growth phase: E, exponential phase; S, stationary phase. Mean values and standard errors are reported.