NZ709994B2 - Process of producing a lactate ferment - Google Patents

Abstract

The present invention relates to fermentation processes. The objective of the invention was to provide methods for producing ferments and formulating such ferments into preservatives. It was in particular an object of the present invention to provide improved processes for producing lactic acid containing ferments by simple and efficient (batch) culturing and allowing for simple down-stream processing either into a liquid, semi-liquid or a dry powder product, having sufficient stability, good handling properties and satisfactory organoleptic properties. Such processes are provided, as well as the products that can be obtained with it and their use as food preservative. aining ferments by simple and efficient (batch) culturing and allowing for simple down-stream processing either into a liquid, semi-liquid or a dry powder product, having sufficient stability, good handling properties and satisfactory organoleptic properties. Such processes are provided, as well as the products that can be obtained with it and their use as food preservative.

Description

PROCESS OF PRODUCING A LACTATE FERMENT Field of the ion The present invention relates to fermentation processes. More in particular, an improved method is provided for the production of lactic acid ferments.

Background of the Invention To prevent decay and quality deterioration of food products, preservatives are commonly added. For decades, chemically sized food preservatives have been the primary choice to e this goal. More recently, safety issues have been raised with respect to these chemically synthesized food preservatives. Ever since, there has been a growing interest in antimicrobial substances derived from traditional foods.

Lactic acid bacteria are useful microorganisms, which have been traditionally used in the production of various fermented food products. Lactic acid fermentation results in inhibition of the growth of other contaminating bacteria. Due to the pH reduction of the systems with lactic acid produced via lactic acid fermentation, decay and quality deterioration of such food products can be prevented and/or reduced. onally, it has been determined that certain additional antimicrobial substances, such as bacteriocins, are produced by some lactic acid ia. These bacteriocins belong to the lantibiotics group (class I bacteriocins) and have a long history as food preservative.

It is becoming increasingly common to use lactic acid containing ferments produced by such strains as preservative agents in all kinds of food products.

Lactic acid ferments are often not produced at the same plant where they are also applied to produce the final food products. In most instances ferments will be ctured at one plant to be used, typically some time later, at another plant in the production of the food t. The fermentation products therefore often need to be processed into formulations that can be stored for some time without loss of quality and/or activity, can be transported efficiently and are convenient to handle and to dose in the production of food products. For economic reasons it is often desirable to provide the products in concentrated forms. Such formulations may ly be , semi-liquid or solid type formulations, each type of ation having its specific advantages and disadvantages. The most preferred choice will typically vary from one use to another.

The possibilities of producing stable and easy-to-use liquid, semi-liquids and/or solid formulations of ferments are to a large extent determined by the thermodynamic behavior of the lactic acid salt(s), constituting the bulk of the ferment. This thermodynamic or sets to a great extent the conditions ed for downstream processing into the formulation type of choice.

Last but not least, organoleptic, y and food tory requirements additionally put restraints on the fermentation and down-stream processing steps and the types and amounts of the materials to be used n.

In summary, manufacturers lactic acid containing ts encounter a number of interrelated technological challenges to optimize the process and satisfy the needs and requirements imposed by specific (end-)uses of the product, in ular with regard to production rate and yield, stabilization of the activity, and the processing into stable and easy- to-use formulations. As will be understood, keeping the manufacturing costs at an acceptable level is always a factor in the design of the process.

It is an object of the invention to provide methods for producing lactic acid containing ferments and formulating such ts into preservatives. It is in particular an object of the t ion to provide improved processes for producing such ferments by simple and efficient (batch) culturing and allowing for simple down-stream processing either into a liquid, semi-liquid or a dry powder product, having suff1cient stability, good handling properties and actory organoleptic properties.

Summary of the Invention The present invention provides a process of producing a lactic acid containing ferment comprising the consecutive steps of: a) providing a nutrient medium comprising a solution of a fermentable substrate and a nitrogen source in an aqueous medium, b) inoculating said nutrient medium with a lactic acid producing micro-organism, preferably lactic acid bacteria, and c) incubating the inoculated nutrient medium nutrient medium under conditions favorable to the growth and/or metabolic activity of said lactic acid producing micro-organism for a period sufficient to produce a tation broth containing at least 20 g/l of e equivalents, during which period the pH of the fermentation broth is controlled by addition of one or more alkalization agents comprising ne sodium and alkaline calcium salts, wherein the NazCa (w/w) ratio of the added salts is within the range of 1/6 — l/l, preferably within the range of U6 — l/2.

In an advantageous embodiment of the invention, the nutrient medium comprises a dairy base, preferably whey.

In an ageous embodiment of the invention the nutrient medium is inoculated with an inoculation medium comprising activated lactic acid producing micro-organisms.

In an ageous embodiment of the invention the s comprises the additional step dl) of acidification of the fermentation broth by the addition of an acid, preferably lactic acid, in an amount sufficient to reduce the pH of the fermentation broth to below 4.8.

In an advantageous embodiment of the invention, the process comprises the additional step d2) of inactivating the lactic acid producing micro-organisms by subjecting the fermentation broth to a temperature of at least 40 0C for a period of at least 10 minutes.

In an advantageous ment of the invention the process comprises the onal step e) of concentrating the ferment obtained in step c) or d) to a dry solids content of at least 30 wt.%, ably within the range of 30-50 wt.%, by evaporation.

In an advantageous embodiment of the invention the process comprises the additional step f) of cooling the concentrate obtained in step e) to a temperature of below 40 0C.

In an ageous embodiment of the invention the process comprises the additional step e’) of spray drying the ferment obtained in step c) or d) to produce a free flowing .

The present invention also provides the ts and ferment products obtainable by the above-described method and their various applications as preservatives.

These and other aspects and ments of the invention will become apparent to those skilled in the art on the basis of the following detailed description and the mental work described in the subsequent section.

Detailed description of the Invention As stated herein, the first step a) of the process comprises the ation of a nutrient medium. In this document, the term "nutrient medium" is used to refer to media in the form originally provided for fermentation. The nutrient medium supplies the ates and the nutrients the lactic acid producing micro-organism need to grow and to produce the various fermentation products. The nutrient medium typically is an aqueous medium comprising a fermentable substrate, a nitrogen source and utrients, wherein the lactic acid producing micro-organism can grow and reproduce. In principle any combination of a carbon source, a nitrogen source and micronutrients may be used as long as it promotes the growth of the lactic acid producing micro-organism.

The term ‘fermentation broth’ is used herein to refer to the nutrient medium after inoculation with the lactic acid producing micro-organism. Thus, strictly speaking, several types of “fermentation broths” can be distinguished based on the stage to which the tation has progressed: (i) nutrient media in the form ally provided including micro-organisms directly after inoculation; (ii) nutrient media undergoing fermentation wherein some or most of the originally provided nutrients has already been consumed and fermentation products ing e have been excreted into the media by the micro- organisms; and, (iii) media that have been removed from the fermentor after part or all of the nutrients have been consumed.

As used herein, the term “fermentable substrate” refers to the carbon source that is converted into another compound by the metabolic action of lactic acid producing micro- organisms. As a carbon source, mono-, di-, tri-, oligo and polysaccharides can be used, in particular sugars such as glucose, sucrose, fructose, galactose and lactose and/or starch (hydrolysates).

Preferably, in this invention, the substrate is a carbohydrate selected from the group consisting of lactose, sucrose and glucose, most preferably lactose.

These carbohydrates can be derived from a variety of sources, such as dairy products and plant, fruit or vegetable derived products, e.g. molasses, fruit or vegetable juices, fruit or vegetable pulp, etc. The invention can be practiced using one or more ydrates in partly or substantially purif1ed form. Alternatively, the invention can practiced using a raw material ning one or more ydrates.

The nutrient medium typically contains at least 1 g/l, more preferably 5-300 g/l, most preferably 10-80 g/l, of the carbohydrate.

Suitable es of nitrogen sources e plant derived protein, such as soy protein and pea protein, dairy protein, yeast or yeast extract, meat extract, various kinds of fermentation filngi, as well as hydrolysates of any of the afore mentioned proteins. It is preferred that the en source comprises free amino acids and/or short peptides. le nitrogen sources may be prepared by hydrolysing a protein . In one embodiment of the invention the nitrogen source is ed from the group consisting of pea protein, yeast extracts and dairy n hydrolysates, more preferably yeast extracts and dairy protein hydrolysates, especially casein hydrolysate.

The nutrient medium typically contains at least 0.1 g/l, more preferably 0.2-50 g/l, most preferably 0.5-20 g/l of the nitrogen source. These amounts refer to the total dry solids weight of the material added as the nitrogen source per liter of nt medium, as will be understood by those skilled in the art. Hence, the nutrient medium typically ns at least 0.1 g/l, more ably 0.2-50 g/l, most preferably 0.5-20 g/l of proteins, peptides and/or free amino acids.

In some embodiment of the invention, the nutrient medium further comprises micronutrients that support the growth metabolic action of the lactic acid producing micro- organism, such as vitamins, minerals, co-factors and/or other trace-elements. The micronutrients are generally used at a rate of at least 0.01 % (w/v), preferably at a rate of between 0.1 and 2 % (w/v) in the nutrient medium. Typically, the carbohydrate sources and/or nitrogen sources that may be used in accordance with the ion ntly contain micronutrients.

A particularly preferred embodiment of the invention concerns the tation of a dairy t. As used herein, the term "dairy product" refers to whole (animal) milk, ents of the milk as well as products derived from milk, such as whey, whey permeate, milk te, yoghurt and quark and by-products from the preparation of yoghurt and quark.

In some preferred embodiments, by volume, the major component of the nutrient medium is the dairy product. In some embodiments, the nutrient medium ses at least 80%, at least 90%, at least 95%, at least 99%, or at least 99.9% of the volume of milk, e.g. a product selected from whole milk, raw milk, skim milk, reconstituted milk, condensed milk, re- hydrated milk and the like. In some embodiment, the nutrient medium comprises at least 80%, at least 90%, at least 95%, at least 99%, or at least 99.9% of the dry solids weight of milk solids, e.g. whole milk , raw milk solids, skim milk solids, whey and the like. In a particularly preferred embodiment said milk solid is whey.

Another preferred embodiment of the invention ns the fermentation of a fruit or vegetable derived product, such as fruit or vegetable derived juices, pastes or pulp. In some preferred embodiments, by volume, the major component of the nutrient medium is the fruit or vegetable derived product. le examples include tomato, carrot, spinach, molasses, etc. In a particularly preferred embodiment of the invention the fruit or vegetable derived product is a juice obtained by mechanically ing or macerating the raw fruit or vegetable. In some embodiments, the fruit or vegetable derived product comprises at least 80%, at least 90%, at least 95%, at least 99%, or at least 99.9% of the volume of the nutrient WO 12870 2014/050015 medium. In some embodiments, the nutrient medium ses at least 80%, at least 90%, at least 95%, at least 99% of the dry solids weight of fruit or vegetable solids.

As stated herein, the uent step b) comprises inoculating the nutrient medium with alactic acid producing micro-organism.

In a preferred embodiment of this invention, the lactic acid producing micro-organism is selected from the group consisting of lactic acid bacteria, more preferably from lactic acid bacteria belonging to the order acillales, preferably the occus genus. The lactic acid bacteria preferably belong to Lactococcus lactis ssp. lactis. Embodiments are also envisaged wherein the lactic acid producing micro-organism is a yeast, such as Saccharomyces cerevisiae, Kluyveromyces nus var. lactis, Candida inconspicua, Candida maris, Acetobacter aceti or Acetobacter rasens, or a filngus, such as Geotrichum candidum. In preferred embodiments, the lactic acid producing micro-organismhave GRAS status.

In some embodiments, the fermentation broth comprises a single species of lactic acid producing micro-organisms, while in other embodiments, the fermentation broth comprises a mixture of different lactic acid producing micro-organisms.

In one embodiment the nutrient medium is ated with a fermentation broth comprising activated lactic acid producing micro-organisms. The term ‘activated’ is used herein to indicate that the composition used to inoculate the nt medium ses lactic acid producing micro-organisms in a metabolically active state. When the micro-organisms are introduced into the nutrient medium during direct seeding i.e. in the form of a dry, liquid or frozen concentrate, they do not take effect straight away and require time to become active.

This ‘time lag’, also referred to as ‘lag phase’, may e re-establishment of the stored micro-organisms into the natural form (rehydration phase), restoration of the metabolic activity and/or adaptation to the new environment. In accordance with a preferred embodiment of this invention, the inoculation of the ction) nutrient medium is done with a fermentation broth comprising activated lactic acid producing micro-organisms, which typically shortens the lag phase, which can significantly decrease the overall fermentation time. The use of activated lactic acid producing micro-organisms may also increase the rate of reproduction during the exponential phase and/or the rate of lactic acid tion during the exponential and/or stationary phases of the fermentation process.

In one embodiment of the invention, a fermentation broth comprising activated lactic acid producing micro-organisms is used for inoculating the nutrient medium, wherein the broth comprises more than 12 g/l of e equivalents, more preferably more than 14 g/l, most preferably more than 16 g/l. As used herein, the term “lactate equivalent” refers to the total of the free lactic acid and the conjugated base (dissociated acid), as will be understood by those of ordinary skill. The terms "lactic acid" and "free lactic acid" are employed interchangeably herein to refer to the acid form. The term lactate refers to the dissociated form of lactic acid. The (dissolved) salt of lactate is also specifically referred to herein as "lactate salt".

In one embodiment of the invention, the fermentation broth comprising activated lactic acid producing micro-organisms used for inoculating the nutrient medium is prepared by incubating the lactic acid producing micro-organisms in an activation medium, which is similar in composition to the production nutrient medium. In one embodiment of the ion, the tion medium has the same composition as the production nutrient medium. In one particularly red ment of the ion, the activation medium is ed as compared to the production nutrient , preferably one or more nutrients applied in the production nutrient medium are used in excess amounts in the activation medium, typically meaning that the tration is at least 120 % of the concentration employed in the nutrient medium. More preferably the activation medium ses one or more of said nutrients in concentrations of at least 130 % of the concentrations employed in the production nutrient medium, even more preferably at least 140 %. In a ularly preferred embodiment of the invention the nitrogen source is used in excess amounts in the activation medium.

As will be understood by those d in the art the fermentation broth comprising activated lactic acid producing micro-organisms can be prepared using rd equipment and methodology.

As stated herein, the process comprises a step c), wherein the inoculated nutrient medium is incubated to produce a fermentation broth. Production-scale lactic acid fermentation requires strict control of fermentation conditions, in ular of the pH.

Without control of the pH, the formation of lactic acid as a product of the metabolic action of the lactic acid producing producing micro-organisms, the pH will decrease as the fermentation proceeds. A drop in pH below a al value, depending on the microorganism used in the s, could negatively affect the microorganism's metabolic process and eventually bring the fermentation process to a stop. The exact critical value will depend on the specific set of incubation conditions. In general, it is preferred that, during the incubation step, the pH of the fermentation broth is maintained within the range of 4.5to 8.0, preferably within the range of 4.8 to 6.5, more preferably within the range of 5.0-6, e. g. 5.5, in order to prevent 2014/050015 tion of lactate production. Inhibition of lactate production is considered to have occurred when the amount of e produced in (batch) fermentation does not increase by more than about 3% upon further incubation for a period of up to about twelve hours under the same conditions. This definition presumes that sufficient nts for lactate production are still available in the fermentation broth and s to both batch and continuous operations.

As mentioned before, prevention of the pH drop to below the critical value is accomplished by adding one or more alkalization agents comprising alkaline sodium and calcium salts. Alkalization, as used herein, refers to the effect of lowering the amount of acid in a solution to any extent and, hence, increasing the pH value. It does not imply an increase of the pH to above neutral. As such the term ‘alkalization’ is deemed to be mous to and interchangeable with ‘neutralization’. The term "alkaline salt" means an organic or inorganic salt of the respective alkaline metal or alkaline earth metal, which reacts with an acid to accept hydrogen atoms and/or donate a pair of valence electrons, and, as such, can be added to the fermentation broth to increase the pH to the desired value. Examples of the alkaline salts in accordance with the invention include the hydroxides of sodium and calcium, carbonates of sodium and calcium. In a preferred embodiment of the invention the one or more alkalization agents comprise sodium ide and calcium hydroxide.

The invention in part resides in the finding that it is advantageous to use both sodium and calcium salts as zation agent and especially to combine sodium and calcium salts in amounts resulting in a NazCa ratio (w/w) within the range of 1/6 — l/l. In a more preferred embodiment of the invention, the NazCa (w/w) ratio is within the range of 1/6 — 1/2, more preferably within the range of l/5.5-1/2.5, most preferably the NazCa (w/w) ratio is within the range of l/5-l/3, e.g. l/4.

As will be understood by those skilled in the art, in the context of this invention it is not critical whether or not the sodium and calcium salts are mixed before addition to the ferment. It is envisaged that the sodium and calcium salts are added separately to the ferment, which can be done simultaneously or uently. For practical reasons it is however preferred to pre-mix the sodium and calcium salts, as will be understood by those skilled in the art. Hence, the present s typically comprises the addition of an alkalization comprising a mixture of alkaline sodium and calcium salts in relative amounts yielding the above recited ratios of sodium and m ions. In an even more preferred ment of the invention, an zation agent is added in the form of an aqueous solution of the alkaline sodium and calcium salts in relative amounts yielding the above recited ratios of sodium and calcium ions, e.g. an aqueous solution of 25-20 % (w/v) sodium hydroxide, preferably 3-10 % (w/v), e. g. about 5 % w/v, and 5-40 % (w/v) calcium hydroxide, preferably 10-30 % (w/v), e.g. about 20 % (w/v).

It is also envisaged that other alkalizing agents may be used in conjunction with the alkaline sodium and calcium salts. For example, other alkali or earth alkali metal hydroxides, such as potassium hydroxide, may be added in addition. Typically such other alkalizing agents are used only in minor amounts. It is preferred that the alkaline sodium and calcium salts are used in such amounts that at least 75 % of the total mol amount of alkali and earth alkali metal ions added is calcium and sodium, more preferably at least 80 %, at least 85 %, at least 90 %, at least 95 %, or at least 97%.

As will be understood by those of ry skill in the art, pH control will typically involve continuous or repeated administration of alkalizing agent. The s is preferably automated for precise control of the pH at a ermined value.

Fermentation generally will be conducted at temperatures conventionally employed in lactic acid tation processes. Temperatures in the range of 20°C to 40°C typically will be employed, with atures in the range of 20°C to 35°C, such as about 30°C, being preferred.

Under the conditions described , production-scale fermentations can be performed with a duration typically varying between 10-24 hours, although the invention is not particularly limited in this respect. Shorter fermentation times are generally preferred as it ntly reduces the risks of the fermentation broth becoming contaminated with other microbiological species.

The incubation can be performed using standard ent for batch and/or continuous processing. Typically the process is performed in a (standard) tion fermentor comprising a vessel having a volume of at least 250 L, at least 500 L or at least 1000 L.

In a preferred embodiment of the invention, the process is carried out in a wise fashion. In a batch process ing to this invention, the lactate content of in the fermentation broth will gradually increase provided the pH drop is prevented by the addition of the one or more alkalization agents. Still, at some point the "limiting lactate concentration" may be reached, which is the lactate concentration ntration of undissociated and dissociated lactic acid) at which, under a given set of incubation ions (pH, nutrient medium, temperature, degree of aeration), further lactate production is inhibited. In other words, growth and/or lactate material production may stop due to the accumulation of one or more fermentation products as well as in response to the pH drop resulting from the production of fermentation products, i.e. the fermentation reaction has a self limiting point for the given set of incubation conditions. In the present process, according to an embodiment of the invention, the incubation step is typically stopped before the point where the concentration of lactate equivalents reaches 25 g/L, preferably 24 g/L, more preferably 23 g/L, more preferably 22 g/L. Preferably, the incubation step is d to proceed to the point where the concentration of lactate equivalents exceeds 15 g/L, more preferably 17 g/l, more preferably 18 g/L, more preferably 19 g/L, most preferably 20 g/l. In a preferred ment of this invention, the fermentation process is stopped by the addition to the fermentation broth of an amount of acid, in particular lactic acid, sufficient to stop lactate production. A s is accordingly provided as defined in the ing, wherein step c) is followed by a step dl) comprising adding an amount of acid to reduce the pH of the fermented broth to below 6 preferably to below 5.5, preferably to below 5, more preferably below 4.8, e.g. to 4.7. In a ularly preferred embodiment said acid is lactic acid. The lactic acid will typically be added in concentrated or dilute liquid form, such in the form of an s solution having a lactic acid content of at least 100 g/l, although the invention is not particularly limited in this respect.

After incubation of the inoculated nutrient medium for a period sufficient to reach the desired lactate levels and, optionally, after stopping the tation by the on of an acid, the fermentation broth is typically subjected to a r ent aimed at the inactivation of the lactic acid producing micro-organisms, by heat-treatment. A process is ingly provided as defined herein before, comprising the additional step d2) of heating the fermentation broth obtained after step c) or dl) by subjecting it to a temperature of at least 40°C, at least 45°C, or at least 50°C, for a period of at least 10, at least 20, at least 30, at least 40 or at least 50 s, so as to vate the lactic acid producing micro-organisms.

The fermentation broth obtained using the present invention can be processed into a suitable product formulation simply by removing water, typically to obtain a paste. The lactate will be present mainly as mixture of sodium and m salts and the present inventors have established that these ferments can suitably be concentrated to dry solids contents of 30 wt% and more without the problem of salts crystallizing out of the product.

The present inventors, furthermore, found that processing of the ferment into a concentrated form in accordance with this embodiment, gave particularly advantageous results in terms of the quality of the resulting t, especially in terms of stability and/or organoleptic properties. Hence, in an ment of the invention, a process is provided as described WO 12870 herein before, comprising the additional step e) of concentrating the ferment obtained in step c), d1) or d2) to a paste having a dry solids content of at least 30 wt.%, preferably within the range of 30-50 wt.%. Any conventional process can be used to perform step e). In a preferred embodiment step e) is performed by subjecting the ferment obtained in step c), d1) or d2) to an environment of above-ambient temperatures, typically to an environment of C, and, ably, reduced pressure, e.g. at a pressure of 190-250 mbar. For performing this step conventional equipment can be used that one of average skill is well-acquainted with.

In one embodiment, following step e), the concentrated liquid or paste is quickly cooled to a temperature of below 40 C, preferably below 30°C, more preferably below 20 °C, more preferably to a temperature of below 10°C. The present inventors established that this step significantly aids to the quality of the resulting product. An embodiment of the invention is accordingly provided comprising a step f) wherein the concentrated liquid or paste obtained in step e) is cooled to a temperature of below 40°C, preferably below 30°C, more preferably below 20°C, more preferably to a temperature of below 10°C, typically by placing it in an environment of below ambient atures for a period ient to accomplish the above recited ng of the temperature. In a particularly preferred embodiment this step comprises placing the composition in a cooling or refrigerating apparatus operated at a temperature of less than 15°C, less than 10°C or less than 5°C. Preferably, during this step, the concentrated liquid or paste is agitated in order to avoid accumulation of al on parts of the equipment.

Alternatively, the fermentation broth obtained using the t invention can be processed into a free flowing powder product by evaporation of substantially all of the water.

Such powders, containing (anhydrous) m lactate in combination with sodium lactate as the bulk of the powder, e high stability with excellent rehydration/dissolution behavior. In particular, ts obtained in accordance with the invention, in this regard, have superior properties compared to ferments containing only calcium e as the major lactate salt.

Hence, in an embodiment of the ion, a process is provided as described herein before, comprising the additional step e’) of subjecting the ferment obtained in step c), d1) or d2) to a drying step to produce a dry powder composition having a water content of less than wt.%, preferably less than 5 wt.%, more preferably less than 3.5 wt.%. In one embodiment the step e’) comprises spray-drying of the t, to produce a owing powder product.

Preferably drying of the aqueous liquid comprises spray drying of the aqueous liquid. In the present method, prior to the spray drying, aqueous liquid may be concentrated by evaporation.

Preferably, the aqueous liquid has a dry matter content of 1-80 wt.%, most preferably of 10- 60 wt.% when it is fed into a spray dryer. Alternatively, a powder may be produced by first drying the aqueous liquid to produce a dry residue, e.g. by means of drum drying) and subsequently reducing the size of the dry residue by, for instance, grinding, g or cutting.

In an embodiment of the invention, a ferment may be concentrated and optionally cooled in accordance with steps e) and f) as described above, before being subjected to a further drying step e’) to produce a dry powder composition.

Owing to the use of the one or more alkalizing agents comprising alkaline sodium and calcium salts in the above recited relative s, the t invention allows for the production of ferments, including dairy based ferments, that do not need any clarification processing or other type of processing aimed at the removal of certain (solid) components from the fermentation broth in order to obtain an acceptable food-grade preservative product.

Hence, in a preferred embodiment of the present invention, a process as defined herein before is ed, wherein the fermentation broth is not subjected to a processing step wherein dissolved or non-dissolved solid matter is removed from the fermented broth following step c), i.e. regardless of the ation of the optional steps d), e) and/or f).

Another aspect of the invention, concerns a lactate ferment product obtainable by the ses as defined herein above. The use of the one or more alkalization agents described herein results in a product containing lactate mainly in the form of sodium and calcium lactate, which confers certain advantageous properties to the fermentation products, especially with regard to the ability to s such fermentation ts into various liquid, semi- liquid and solid formulations and/or with regard to the organoleptic ties of these fermentation products.

In a particularly preferred embodiment of the invention, the lactate ferment product contains at least 25 wt.% of e, on the basis of dry solids , more preferably at least 40 wt.%, most preferably at least 50 wt.%. As will be understood, this includes all forms of lactate, including free lactic acid as well as lactate containing salts.

Typically, in the lactate ferment product of the invention the major part of the lactate is in the form of sodium and calcium salts. Hence, in a preferred embodiment, a e ferment product as defined herein is provided comprising lactate anions and sodium and calcium cations, wherein the amount of sodium and calcium cations exceeds 0.5 of the stoichiometric equivalent, preferably it exceeds 0.75 of the stoichiometric lent, more preferably it exceeds 0.9 of the stoichiometric lent. Furthermore, in a preferred embodiment, a lactate ferment product as defined herein is provided sing lactate anions and sodium and calcium cations, n the amount of sodium and calcium cations is equal to or less than 1.0 of the iometric equivalent. As will be understood by those skilled in the art, the stoichiometric equivalent refers to the combined amount of sodium and calcium cations that would theoretically be ary to provide counterions for all lactate anions.

As indicated herein before, in an ment, the product will typically n sodium and calcium ions in a NazCa ratio (w/w) within the range of 1/6 — 1/2. In a more preferred embodiment of the invention, the NazCa (w/w) ratio is within the range of l/5.5- l/2.5, most preferably, the NazCa (w/w) ratio is within the range of 1/5-1/3, e.g. l/4.

Further aspects of the present invention concerns the use of a e ferment product as defined in any of the foregoing for the preservation of an alimentary product, especially a food product or a ge, more in particular a product selected from the group consisting of sed and natural s, cooked meats, canned foods, seafoods, alcoholic beverages, dairy deserts, dairy drinks/liquids, prepared meals, dressings, sauces, flour based products, liquid egg products, etc., and to s of preserving such alimentary products comprising the step of incorporating therein or applying thereon a lactate ferment product as defined in any of the foregoing. The lactate ts of the ion are particularly useful in the preservation against spoilage by a microorganism, especially a microorganism selected from the group consisting of Listeria spp, clostridium spp, lactic acid bacteria and bacillus spp. It is within the purview of those of ordinary skill in the art to determine the most riate dosages for optimal protection against spoilage while avoiding negative impact on other quality aspects of the tary product, especially organoleptic ties. As ned before, the present lactate ferment products can be applied in relatively high dosages without negative impact on organoleptic properties and salt content.

Thus, the invention has been described by reference to certain embodiments discussed above. It will be recognized that these embodiments are susceptible to various modifications and alternative forms well known to those of skill in the art.

Many modifications in addition to those bed above may be made to the structures and techniques described herein without departing from the spirit and scope of the invention. Accordingly, although specific embodiments have been described, these are examples only and are not limiting upon the scope of the invention.

Furthermore, for a proper understanding of this document and in its claims, it is to be understood that the verb "to comprise" and its conjugations is used in its non-limiting sense to mean that items following the word are included, but items not specifically mentioned are not excluded. In addition, reference to an element by the indefinite article "a" or "an" does not exclude the possibility that more than one of the element is present, unless the context clearly requires that there be one and only one of the elements. The indefinite article "a" or "an" thus usually means "at least one".

All patent and literature references cited in the present specification are hereby incorporated by reference in their entirety.

The ing examples are offered for illustrative purposes only, and are not ed to limit the scope of the present invention in any way Example 1 Batch flasks (2 L) are used as reactors for fermentation. This reactor is sterilized empty for 20 min at 121 0C. All cultivations are performed aseptically. Whey powder 5% w/w and Yeast extract 0.2% w/w (based on dry weight) is used as the nutrient medium (pasteurized for 30 min at 80 oC inside the r) for all fermentations. A mixture of Ca(OH)2/NaOH (composition in table below) is used to control the pH, which is kept at approximately pH, 5.5.

A first batch flask containing the nutrient medium is inoculated from a glycerol stock of Lactococcus lactis ATCC 11454 and incubated overnight at 30 oC. The inoculum is 2.5% w/w. During exponential growth phase ferment from the first batch flask is transferred as inoculum for the next 2 L reactor containing nt medium, which is ran under the same conditions. The fermentation in the second reactor is d after the lactate concentration had reached more than 25 g/l. Around 10 ml of lactic acid (80% dry solids) is sufficient to lower the pH to 4.7. The reactor is kept at 50 0C for 1 hour for inactivation.

Alkalization agent NaOH Ca(OH)2 Concentration in pure stock (%) 50.0 25.0 Proportion in base (%) 10.5 89.5 Final concentration in base (%) 5.3 22.4 Ca2+/Na+ ratio H 4.0 The ferment can be further d and/or concentrated according to s known to a person skilled in the art. By means of evaporation e.g. a paste or concentrate can be prepared. By means of spray drying e. g. a powder can be prepared.

The ferments and concentrates have sufficient stability to allow for ortation and storage of the product in accordance with usual ry practice. The incorporation of the ferment and/or concentrates thereof in various alimentary products at effective dosages results in organoleptic properties that are generally favoured over those obtained with prior art ferments.

Example 2: Lactic acid ferment is produced according to the procedure of example 1. The raw ferment is not purified and processed into a powder by spray-drying.

Products with anhydrous calcium lactate were obtained by drying at a product temperature during the spray-drying process of 90 0C, whereas the air temperature varies n 165 and 180 0C.

Products with calcium lactate pentahydrate were obtained using the spray ation que using a continuously operating fluidized bed. The product ature was 60 0C, the temperature of the fluidization air was 110 0C.

For ution tests 2 g of a powder was accurately weighed in a plastic cup and two glass beads with a diameter of 6 mm were added. The blend was manually mixed for 1 min.

To prevent water uptake, the air was purged with dry nitrogen. Dissolution tests were performed by adding the powder sample to 198 g demineralized water which was stirred with a stirring flea. The test conditions are such that sink conditions are always fulfilled (i.e. after complete dissolution of the material the concentration in the liquid is less than around 30% of the tion solubility). Times to reach 10%, 50%, 90% and 95% of complete dissolution were calculated.

For stability tests samples are stored in hermetically sealed glass jars to prevent any re exchange. The samples have been stored at temperatures of 4°C, room temperature (around C) and 40°C. The properties of the powders are visually assessed at different time-points. The ferment powder is stable when it remains a free-flowing powder.

It is possible to lize the fermentation broth using calcium hydroxide (Ca(OH2), sodium hydroxide (NaOH) or a combination thereof. This leads to a certain calcium to sodium (Ca/Na) ratio in the final product. A solid product containing only Na is not le because of high Na content and unacceptable hygroscopicity of the dry product. A solid product with ous calcium lactate and with a high Ca/Na ratio of 20 has been produced.

This product suffered from the antage of unacceptable taste and long dissolution time (95%) of 88 s.

A product with calcium lactate pentahydrate and a Ca/Na ratio of 3-4 was acceptable from a taste and Na content perspective. Dissolution time (95%) of this product is around 30 s, which is acceptable. However, the t lacked suff1cient stability. This is because the calcium e is present in the form of calcium lactate pentahydrate. Sodium lactate, which is also present, presumably, was able to extract the l water from calcium lactate pentahydrate crystals. This leads to dissolution of sodium lactate in the water extracted from calcium lactate and, as a result of that, paste ion, even when packed in aluminum sachets.

It has been found that a product with calcium lactate anhydrate and sodium lactate (in a Ca/Na ratio of 3) still has an acceptable dissolution time (95%) of 31 s. ity proved acceptable as well, as paste formation did not occur. The composition of this product was as follows: Lactic Acid (% w/w) 51 Succinic Acid (% w/w) 1.12 Total Nitrogen (% w/w) 1.6 Na (% w/w) 2.9 Ca (% w/w) 8.1 e (% w/w) 11 pH (10%) 4.7 Example 3 In order to test for the taste impact of calcium and sodium in the neutralization agents, model products have been prepared. Milk was used as the reference product. Different samples have been prepared, consisting of milk to which ferments (produced following the general procedure of e 1), have been added with different concentrations of calcium and sodium, as presented in the table below.

Na- Ca- Model Model Model —----mm —-----m RATIO Ca:Na . . . . .

These samples were tested by a panel. The results are ed by means of pal Component is and summarized in a Bi-Plot (cf. B.S. Everitt, An R and S-Plus Companion to Multivariate Analysis). This Bi-Plot is depicted in Figure 1.

From the results, it is clear that the use of sodium as the sole counterion in the neutralization agent (Na-based) leads to a salty taste, whereas the use of calcium as the sole counterion (Ca-based) leads to an astringent and bitter taste. By using both calcium and sodium in a ratio of between approximately 1:1 and 6:1 w/w a much more neutral taste, closer to milk, can be achieved.

Claims (1)

Claims 1.

1. Process of producing a lactate ferment comprising the utive steps of: a) providing a nutrient medium comprising a solution of a fermentable substrate and a nitrogen source in an aqueous medium; b) inoculating said nutrient medium with lactic acid producing micro-organism; and c) incubating the inoculated nutrient medium to produce a fermentation broth ning at least 20 g/l of lactate equivalents, during which period the pH of the fermentation broth is controlled by addition of one or more alkalization agents comprising alkaline sodium and alkaline calcium salts, wherein the Na:Ca (w/w) ratio of the added salts is within the range of