Patent Application
20110104733
The present invention relates to a method for cultivating microorganisms in order to increase the biomass and/or the metabolic activity of microorganisms (i.e. to increase the production of certain metabolites, namely certain molecules produced by the microorganisms), this by the combined adjustment of the oxidation-reduction potential and the dissolved oxygen.
As an illustration, the invention may relate for example to lactic bacteria, but also to microorganisms having preferably an anaerobic metabolism such as yeasts.
The invention also relates to the field of certain finished products, such as wine or beer, for which the production method employs a fermentation step.
The actual cultivation step takes place in a vessel, with or without stirring, in a culture medium of which the composition is suited to the specific requirements of each microorganism. The composition of the culture medium may be extremely varied, but mention is usually made of the presence of one or more elements among polysaccharides, glycerol, milk, glucose, etc.
Similarly, parameters such as for example pH, temperature and dissolved oxygen pressure may be adjusted.
Various types of cultivation procedure exist:
The step of preserving the biomass may be carried out in liquid form, by freezing, by cryopreservation, by freeze drying or by drying. Protective agents are used to protect the microorganisms from the harmful effects of preservation treatments.
Freeze drying is known to be a low temperature dehydration operation, which consists of removing the major part of the water contained in the product, after freezing, by sublimation.
As has been said, microorganisms are widely used in the food field, notably lactic bacteria, such as probiotic cultures or ferments. The viability and metabolic activity of these lactic bacteria, produced on a large scale for their criteria of technological ability, may be affected by the various steps that they undergo during their production (inoculation, cultivation and concentration) and their preservation (freezing or freeze drying).
Microorganisms may also be made use of in the production of biofuels, notably by the conversion of sugar into ethanol. Microorganisms also enable molecules of interest to be produced, notably in the pharmaceutical field.
Optimization of the biomass and/or of the metabolic activity of these cultures is therefore very important and of necessity has both technological and economic importance.
Environmental parameters play a key role in the growth of microorganisms, in the metabolic reactions and in the physiological mechanisms responsible for the activity of microorganisms.
Like the pH, temperature or composition of the medium, the value of the oxidation-reduction potential seems to have an effect on the growth and viability of bacterial strains. In point of fact, several studies on lactic bacteria have demonstrated an effect of the oxidation-reduction potential on metabolic flow, the survival of probiotic ferments and the production and/or stability of molecules of interest. In this respect, reference may be made to the following documents: documents EP-1 856 241 and EP-1 619 705 as well as WO 2007/036693 A1 in the name of the Applicant, or patent U.S. Pat. No. 7,078,201.
It will be noted that document WO 2007/036653 relates to the adjustment of the redox potential at one or more steps of a method for producing a food or biotechnological product comprising a fermentation step, so as to perform at least one of the steps of the method under reducing conditions and at least one of the steps of the method under oxidizing conditions, and notably making it possible to alternate the phases of the fermentation considered under reducing conditions with the phases of the fermentation considered under oxidizing conditions.
Various compounds may be used as a reducing agent and for inducing a reduction in and/or maintenance of the oxidation-reduction potential. Among these, mention may be made of sulfites and ammonia but also of reducing gases such as hydrogen or mixtures containing hydrogen.
These studies of the prior art have made it possible to demonstrate that the use of reduced media, media where the oxidation-reduction potential is low, makes it possible to increase the biomass produced but also the viability of the product during its subsequent preservation, and also makes it possible to increase the production of metabolites.
Another means reported by the prior art for increasing the biomass produced is the use of a small quantity of oxygen. Although oxygen has an inhibiting effect on lactic bacteria, facultative anaerobic bacteria, it is described in the literature as being able to be of benefit to their growth. Thus, studies have shown that for an MG1363 strain of Lactococcus lactis, addition of oxygen enables the biomass produced to be increased. In this way, the concentration of biomass moves from 0.54 g/l (dry weight) in an anaerobic culture to 0.68 g/l for a culture to which a percentage of dissolved oxygen of 5% is added (reference will be made to the studies by Jensen et al. entitled “Metabolic behavior of Lactococcus lactis MG1363 in microaerobic continuous cultivation at a low dilution rate” that appeared in AEM—2001, Vol. 67, No. 6).
It would then appear that the two solutions recommended by the prior art, namely the establishment of a low redox potential in the first case and action on the quantity of dissolved oxygen in the second case, clearly seem to be incompatible. Indeed, since oxygen is a powerful oxidizing agent, adding it to the culture medium will significantly increase the redox potential.
As will be seen below in greater detail, it is therefore the merit of the present invention to have demonstrated that it is possible to provide and adjust a quantity of dissolved oxygen while adjusting the redox potential to a desired fixed low value, this bringing about, in an extremely advantageous manner, a significant increase in the productivity of cultivated strains, while action on the two aforementioned parameters could appear to a person skilled in the art at first sight, in view of the prior art referred to above and highly logically, to be destructive.
The present invention thus provides a method employing simultaneous adjustments, preferably using gases or gaseous mixtures to ensure these adjustments:
It will be noted that document U.S. Pat. No. 7,078,201 referred to above indicates that an optimum value of the redox potential may increase the production of ethanol, reduce the formation of glycerol and reduce the fermentation time as compared with a conventional fermentation. The method proposed by this document proposes for this the maintenance of a value of the redox potential in the fermenter of between −250 and +50 mV by means of continuous aeration of the medium by air injection. The objective sought by the authors of the document is to proceed counter to a lowering of the redox potential, and for this, according to one of the methods recommended by the document, the author recommends adding sodium hydroxide in order to limit the reduction of the value of the redox potential instead and in place of the traditional use of ammonia (considered as too reducing) in order to adjust the pH during growth.
It will therefore be understood that the authors do not at any time refer to stable and continuous adjustment of the redox to a fixed value being made (fine adjustment) and even less do they refer to the fact of adjusting the quantity of dissolved oxygen while adjusting the redox potential to a desired fixed low value (the dissolved oxygen content which would naturally have the tendency to raise the redox potential).
The present invention then relates to a method for cultivating microorganisms, a method of the type where, in particular, a step is performed of seeding a culture medium with one or more microorganism strains, and a step of cultivating the medium seeded in this way, which is characterized in that, during the entirety or part of the cultivation, two of the following adjustments are made simultaneously:
It should be understood on reading the preceding account that according to the invention, the value of the redox potential Eh of the medium is adjusted to a set point value that is less than the value that would be naturally reached by only adjusting the dissolved oxygen.
The invention could moreover adopt one or more of the following technical features:
The invention will be better understood on reading the following example with reference to
Tests were carried out on a mesophilic strain, Lactococcus lactis, in a fermenter with a capacity of 1.5 liters.
The fixed target values (set points) for the oxidation-reduction potential and the dissolved oxygen were respectively −200 mV and 10%.
Here is what should be understood by this 10% dissolved oxygen value: the apparatus used is capable of measuring the oxygen concentration of the culture medium by means of a probe. This probe is calibrated in the following way: an H2/N2 mixture (4/96) is injected into the culture medium in order to draw off all the oxygen present. At this stage, the probe should then indicate a concentration of 0% dissolved oxygen. Secondly, the aforementioned H2/N2 mixture is replaced by air, which is injected in a large quantity (typically at the maximum flow rate that the system can provide). After waiting until the measured value is stable, the system should then indicate a value of 100% dissolved oxygen. If this is not the case, the probe is calibrated with a value of 100% being given to the probe. This “100% dissolved oxygen” then corresponds to the maximum oxygen that the medium considered can dissolve. Once this calibration has been carried out, adjustment of dissolved oxygen can be activated with the set point that that it is desired to establish in the culture medium (here for example 10%). Tests were then carried out with 10% of the maximum that the medium considered could dissolve.
Similarly, one embodiment of the two simultaneous adjustments according to the present invention will be explained in detail hereinafter.
An automaton is used that periodically (according to a period that has been imposed on it, for example less than a second), examines each of the mass flow controllers, namely its set point value and the value of the measurement of the parameter considered and that consequently corrects its output, i.e. the instruction, which it gives as feedback. In this case, use is made of a control of the PID type which here makes it possible to adjust both the redox and the dissolved oxygen. As will be explained in greater detail hereinafter, it should in point of fact be pointed out that the redox potential and the dissolved oxygen do not have the same behavior, and they do not have the same time constants or the same reaction amplitude for an identical flow rate variation. Consequently, the parameters of each controller are not identical and fine adjustment employed on each PID enables the controllers not to oscillate, this implementation thus limiting interferences between them.
The implementation described above is only an illustration of one embodiment, which does not of course exclude other means of adjustment and this without at any time departing from the scope of the present invention.
The inputs and outputs of the controller typically installed are described below:
For the Redox:
More precisely, as an example of the implementation indicated above:
Taking account of this identification of transfer functions, it is thus possible to determine the parameters of each corrector, the objective being that the system reacts correctly to a disturbance of the system for a fixed point. In point of fact, according to the invention, a given set point is established during all or part of the growth, and on the other hand the effect of the growth of bacteria in the culture medium should be included in the determination of corrector parameters. It is known in point of fact that the growth of bacteria has an influence on the redox potential: the redox potential falls during growth and oxygen consumption increases. It consists of a phenomenon that disturbs adjustments: adjustment of the correctors is made to react to this disturbance as best as possible.
In this way, it is the combination of identifications made and the manner in which the corrector is adjusted (response to a disturbance and not to a change of set point) that makes it possible to obtain the results observed with the use of “simple” controllers of the PID (monovariable) type.
The objective of the adjustment during the tests referred to above is to maintain, during at least part of the growth of the strain, a constant value of the redox potential as well as a constant dissolved oxygen value (this will indeed be seen moreover in
The biomass, the acidifying activity and the productivity per operation were measured at the end of fermentation (end of cultivation) but also on frozen pellets and on the freeze-dried product. These results were compared with a control culture in which neither the redox potential nor the dissolved oxygen were adjusted (an aerobic culture prepared with a simple flushing with nitrogen at 0.5 l/min in the headspace of the fermenter).
The results shown in
The various gains obtained during various production steps are described in the table below.
The essential result of this invention is demonstrated, according to which it is possible, by a system of controlled adjustment, to uncouple the two parameters while adjusting them simultaneously: oxidation-reduction potential and dissolved oxygen.
It is then found that the gains obtained are greater than 50% at the step of the freeze-dried product, which is very satisfying. By simultaneously adjusting the two parameters, oxidation-reduction potential and dissolved oxygen, large gains are obtained in biomass and acidifying activity.
As it will appear clearly to a person skilled in the art, the optimum dissolved oxygen and redox potential values will have to be adapted according to the strains and targeted objective (production of biomass and/or production of metabolites).
The performance of different adjustment sequences may also be envisaged as a function of the growth phase concerned, that is to say the establishment of different couples (value of redox/pO2) as a function of the growth phase of the strain, and a numerical example is given below as an illustration:
| Number | Date | Country | Kind |
|---|---|---|---|
| 08 50976 | Feb 2008 | FR | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/FR09/50174 | 2/5/2009 | WO | 00 | 1/5/2011 |
