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Modeling the alcoholic fermentation of cocoa by a selected yeast strain

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C o n ce p ti o n : C ira d , Mar tine Dupor tal,, O ct o b e r 2 0 1 8 - © p h o to s: C . Ko u a mé

The growth of a S. cerevisiae strain (LM, Lallemand) was modeled by mobilizing the Rosso primary model (Eq.1) and the gamma concept (Eq.2). The parameters of the models were determined by growing LM in synthetic liquid medium, by

varying the parameters independently. The model was implemented under Matlab-Simulink and two validations mimicking the natural fermentation

conditions (pH, temperature profile, initial glucose content) were performed.

Experimental approch

C

HOCOLATE

is a pleasure-food consumed mainly for its aromatic quality directly related to that of

the fermented and dried cocoa beans. The fermentation of the beans is a key step led by a wild

microflora, poorly controlled, that sometimes leads to beans of undesirable quality. Its

smooth running depends on multiple factors (Figure 1).


To control the quality of the beans, a mathematical model of alcoholic fermentation has been

developed; it can be used to predict and optimize the behavior of a yeast strain according to

the fermentation control parameters (inoculum level, T ° C, pH , PO2).

Modeling the alcoholic fermentation

of cocoa by a selected yeast strain

Christelle Kouamé

1

, Gérard Loiseau*

1, 2

, Joël Grabulos

1

, Renaud Boulanger

1

, Christian Mestres

1 1 CIRAD, UMR Qualisud, F-34398 Montpellier
 2 QualiSud, Univ Montpellier, CIRAD, Montpellier SupAgro, Univ Avignon,

Univ Réunion, Montpellier, France

*Contact: loiseau@cirad.fr

tél. : +33-04-67-61-57-13

Yeast

γ pH

γ T°C

γPO2 γ [etoh] γ [Acetate ]

γ gluc. γ N Ethanol Nitrogen O2 water … Glucose Bacteria Acétate pH Temperature

Equation 1 : dNt / dt = 0 si t ≤ λ dNt / dt = µmax Nt (1- Nt / Nmax ) si t ≥ λ

Equation 2 : µmax = µopt . γ T°C . γ pH . γ[Gluc] . γ[Etoh] . γ[Azote] .γ PO2 . γ[Acétate].

avec 0 < γ < 1

Rosso et al., 1995. Convenient model to describe the combined

effects of temperature and pH on microbial growth. Appl. Environ.

Microbiol. 61, 610–616.

Zwietering et al., 1993.

A decision support system for

prediction of microbial spoilage in f o o d s . J . I n d . M i c r o b i o l . Biotechnol. 12, 324–329 Figure 1. Schematic representation of bean fermentation. References

Model predicts LM growth and growth arrest quite well.

Inoculation at 104 CFU/mL: when the temperature reaches

41°C, the γ-temperature drops to 0, and the growth of LM stops. There is still glucose in the environment.

Inoculation at 106 CFU/mL: the growth stops when the

glucose level and γ-glucose reaches 0 (≈ 20h); there is no more glucose in the medium. The Tmax is reached later ≈ 35h.

Conclusion

A mechanistic model predicts yeast growth during cocoa fermentation.

The model predicts growth cessation depending on inoculation level.

For low inoculation level, yeast growth stops with increased temperature of cocoa.

For high inoculation level, depletion of glucose stops yeast growth.

The model explains that depending on the quality of the raw material (glucose content), the conditions of inoculation and temperature maintenance, the quality of the cocoa will vary.

The model is a tool to define the inoculation level of yeast for cocoa fermentation.

Results: modeling yeast

growth in "real" conditions

- - -

Model 104 Expe 104

- - -

Model 106 Expe 106 γ-glucose γ-T°C glucose T°C

- - -

Model 104 Expe 104

- - -

Model 106 Expe 106 γ-glucose γ-T°C glucose T°C

- - -

Model 104 Expe 104

- - -

Model 106 Expe 106 γ-glucose γ-T°C glucose T°C

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Model 104 Expe 104

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Model 106 Expe 106 γ-glucose γ-T°C glucose T°C

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