Natural Vanillin Composition

Abstract

The present invention relates to a natural vanillin composition comprising at least one compound selected from 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde. The present invention also relates to a process for obtaining the natural vanillin composition according to the invention.

Description

[Technical Field]

[0001] This application claims priority from French Patent No. 1908643, filed July 30, 2019, the contents of which are incorporated by reference in their entirety.

[0002] The present invention relates to a natural vanillin composition comprising at least one compound selected from 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde. The present invention also relates to a process for obtaining the natural vanillin composition according to the invention. [Background technology]

[0003] Vanillin, i.e. 4-hydroxy-3-methoxybenzaldehyde, can be obtained by various methods known to those skilled in the art, in particular by the following three routes: - "natural" routes based in particular on biotechnological processes, including the cultivation of microorganisms capable of enabling the biological conversion of a fermentation substrate to vanillin. Such a process, in which the fermentation substrate is ferulic acid, is known in particular from EP 0 885 968. The ferulic acid used may have several origins, in particular from rice bran or corn bran. - A "synthetic" route that does not involve microorganisms and involves conventional chemical reactions starting from guaiacol. This method produces vanillin, known as synthetic vanillin. Finally, vanillin can also be prepared by routes described as "biobased", in which vanillin is obtained from eugenol or lignin. Mention may be made, in particular, of US Pat. No. 2,745,796 and DE Pat. No. 1,132,113, as well as the article by Azadbakht et al. entitled "Preparation of lignin from wood dust as vanillin source and comparison of different extraction methods" in the International Journal of Biology and Biotechnology, 2004, Vol. 1, No. 4, pp. 535-537.

[0004] When the "natural route" is used for the industrial production of vanillin, multiple side reactions can occur, resulting in the formation of numerous by-products that can affect the sensory properties of the natural vanillin. The chemical synthesis of one of these by-products is described, inter alia, in EP 2 763 947 B1. As a result, the preparation of natural vanillin compositions with precise properties, especially in terms of color or sensory properties, is complicated. The present invention aims at the efficient and controlled preparation of natural vanillin compositions with a known and controlled content of by-products. Summary of the Invention

[0005] A first subject of the present invention therefore relates to a composition comprising natural vanillin and additionally comprising at least one compound chosen from 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde.

[0006] Another aspect relates to a method for preparing a natural vanillin composition according to the invention, comprising a step (a) of fermenting ferulic acid, and optionally also a step (b) of purifying the natural vanillin composition obtained at the end of step (a).

[0007] Finally, the present invention relates to the use of natural vanillin compositions in the field of human food and animal nutrition, in pharmaceuticals, as a flavoring agent or as a fragrance in the cosmetics, perfume and detergent industry. DETAILED DESCRIPTION OF THE INVENTION

[0008] In the context of the present invention, and unless otherwise indicated, the expression "between" is inclusive. Unless otherwise indicated, percentages and ppm are percentages and ppm by weight.

[0009] In the context of the present invention, and unless otherwise indicated, the term "ppm" means "parts per million". This unit represents a ratio by weight: 1 ppm = 1 mg / kg.

[0010] In the context of the present invention, and unless otherwise indicated, the expression "natural vanillin" may refer to a flavoring substance according to Article 9.2(c) of Regulation (EC) 1334 / 2008, i.e., a flavoring substance obtained by physical, enzymatic, or microbiological processes from substances of plant, animal, or microbial origin, either in their original form or after processing them by one or more conventional food preparation processes for human consumption. Natural flavoring substances correspond to substances that occur in nature and have been identified as such. Definitions provided by regulations in force in other countries or regions may also apply. Preferably, the term "natural vanillin" according to the present invention refers to vanillin obtained by a biotechnological process involving the cultivation of microorganisms capable of converting a fermentation substrate into vanillin. According to the present invention, the microorganism may be wild-type or genetically modified, in particular to improve the yield of vanillin or to prevent the formation of by-products. Highly preferably, this may be a process for the fermentation of ferulic acid, as described in EP 0 885 968 B1. The ferulic acid may be of any origin, in particular from rice bran, beet pulp, wheat bran, bagasse, sugarcane, or corn, in particular corn bran or corn fiber, especially from a starch factory or nixtamalization unit.

[0011] According to a first aspect, the present invention relates to a composition comprising natural vanillin and further comprising at least one compound selected from 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde. [ka]

[0012] According to a particular embodiment, the composition according to the invention contains 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde.

[0013] According to a preferred embodiment, the composition according to the present invention further comprises at least one compound selected from vanillyl alcohol, vanillic acid, acetovanillone, guaiacol, and vinylguaiacol. For example, the composition according to the present invention may comprise acetovanillone and / or vinylguaiacol. [ka]

[0014] Preferably, the composition according to the present invention may further comprise at least one compound selected from vanillyl alcohol, vanillic acid, and acetovanillone.

[0015] Advantageously, the composition according to the invention exhibits a natural vanillin titre of at least 90%, preferably more than 95% and very preferably at least 99%. According to a particular embodiment, the natural vanillin titre is at least 99.5%.

[0016] According to a preferred embodiment, the weight content of 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde relative to the total weight of the composition is less than or equal to 10,000 ppm, preferably less than or equal to 8,000 ppm, more preferably less than or equal to 7,000 ppm, and very preferably less than or equal to 5,000 ppm.

[0017] According to another preferred embodiment, the weight content of 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde relative to the total weight of the composition is greater than or equal to 10 ppm, preferably greater than or equal to 200 ppm, more preferably greater than or equal to 500 ppm, and very preferably greater than or equal to 100 ppm.

[0018] Advantageously, the content by weight of 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde relative to the total weight of the composition is between 600 ppm and 2500 ppm.

[0019] According to a preferred embodiment, the weight content of 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde relative to the total weight of the composition is less than or equal to 5000 ppm, preferably less than or equal to 2500 ppm, more preferably less than or equal to 1000 ppm, and very preferably less than or equal to 900 ppm.

[0020] According to another preferred embodiment, the weight content of 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde relative to the total weight of the composition is greater than or equal to 10 ppm, preferably greater than or equal to 100 ppm, more preferably greater than or equal to 200 ppm, and very preferably greater than or equal to 300 ppm.

[0021] Advantageously, the content by weight of 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde relative to the total weight of the composition is between 400 ppm and 800 ppm.

[0022] According to the present invention, the content by weight of vanillyl alcohol relative to the total weight of the composition is 4000 ppm or less, preferably 2000 ppm or less, very preferably 1000 ppm or less, preferably 800 ppm or less, more preferably 600 ppm or less, very preferably 500 ppm or less. According to the present invention, the content by weight of vanillyl alcohol relative to the total weight of the composition is 1 ppm or more, preferably 5 ppm or more, more preferably 10 ppm or more, very preferably 20 ppm or more.

[0023] Advantageously, the content by weight of vanillyl alcohol relative to the total weight of the composition is between 50 ppm and 250 ppm.

[0024] According to the present invention, the vanillic acid content by weight relative to the total weight of the composition is 1000 ppm or less, preferably 700 ppm or less, more preferably 500 ppm or less, and very preferably 200 ppm or less. According to the present invention, the vanillic acid content by weight relative to the total weight of the composition is 1 ppm or more, preferably 5 ppm or more, more preferably 10 ppm or more, and very preferably 20 ppm or more.

[0025] Advantageously, the content by weight of vanillic acid relative to the total weight of the composition is between 50 ppm and 100 ppm.

[0026] According to the present invention, the weight content of acetovanillone relative to the total weight of the composition is 1000 ppm or less, preferably 800 ppm or less, more preferably 600 ppm or less, and very preferably 500 ppm or less. According to the present invention, the weight content of acetovanillone relative to the total weight of the composition is 0.1 ppm or more, preferably 5 ppm or more, more preferably 10 ppm or more, and very preferably 20 ppm or more.

[0027] Advantageously, the content by weight of acetovanillone relative to the total weight of the composition is between 50 ppm and 400 ppm.

[0028] According to the invention, the guaiacol content by weight relative to the total weight of the composition is 100 ppm or less, preferably 50 ppm or less, more preferably 40 ppm or less, and very preferably 20 ppm or less. According to the invention, the guaiacol content by weight relative to the total weight of the composition is 0.01 ppm or more, preferably 0.1 ppm or more, more preferably 1 ppm or more, and very preferably 10 ppm or more. According to another alternative form of the invention, the vanillin composition does not contain guaiacol.

[0029] According to the invention, the content by weight of vinylguaiacol relative to the total weight of the composition is 100 ppm or less, preferably 50 ppm or less, more preferably 40 ppm or less, and very preferably 20 ppm or less. According to the invention, the content by weight of vinylguaiacol relative to the total weight of the composition is 0.01 ppm or more, preferably 0.1 ppm or more, more preferably 1 ppm or more, and very preferably 10 ppm or more. According to another alternative form of the invention, the vanillin composition is vinylguaiacol-free, in particular the vinylguaiacol content is below the detection limit of liquid chromatography methods.

[0030] Advantageously, the compositions according to the invention are lightly colored. Preferably, the natural vanillin composition has a color of 400 Hazen or less, preferably 200 Hazen or less, more preferably 100 Hazen or less, very preferably 50 Hazen or less, and even more preferably 20 Hazen or less. Color is measured in a 10% by weight ethanol solution. Color measurements are performed using a Konica Minolta CM-5 spectrophotometer using a 10 mm path length cuvette.

[0031] The natural vanillin composition according to the present invention may be in crystalline or amorphous form, preferably crystalline form. The natural vanillin composition may be formed as a powder, crystals, beads, prills, or flakes.

[0032] Advantageously, the natural vanillin compositions according to the invention have a compatible sensory profile, in particular with respect to visual appearance, texture, taste or aroma. Advantageously, the compositions according to the invention do not exhibit off-key aroma notes. In particular, the sensory profile of the compositions according to the invention is at least equivalent to that of natural vanillin extracted from vanilla pods.

[0033] The natural vanillin composition according to the invention may contain other compounds, the presence of which is related to the process for preparing natural vanillin. In particular, but not exclusively, mention may be made of 4-(3-hydroxy-4-methoxybenzyl)-2-methoxyphenol, 4,4'-methylenebis(2-methoxyphenol), ferulic acid, and vanillin dimer and / or trimer.

[0034] Another aspect relates to a method for preparing a natural vanillin composition according to the invention, characterized in that it comprises a step (a) of fermenting ferulic acid, optionally also comprising a step (b) of purifying the crude natural vanillin composition obtained at the end of step (a).

[0035] Step (a): According to the present invention, step (a) of the process is the fermentation of ferulic acid to produce a crude natural vanillin composition.

[0036] The crude natural vanillin composition refers to a composition obtained at the end of the ferulic acid fermentation process. In particular, the crude vanillin composition can be obtained after processing an aqueous fermentation medium. For example, the fermentation medium can be separated from the biomass, and then the aqueous phase can be extracted with a suitable solvent. As a result, the crude natural vanillin composition can be obtained indirectly at the end of the ferulic acid fermentation process. Specifically, during the production of natural vanillin, a liquid composition containing natural vanillin, impurities, and a large amount of solvent, typically a food-grade solvent such as ethyl acetate, is usually recovered.

[0037] The fermentation can be carried out as set out in EP 0 885 968. The fermentation is usually carried out in an aqueous medium.

[0038] Preferably, at the end of step (a), the weight concentration of natural vanillin is between 0.5% and 60%, preferably between 5% and 40%, more preferably between 10% and 35%, relative to the weight of the crude natural vanillin composition.

[0039] The crude natural vanillin composition used in step (a) may comprise at least one compound selected from 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde. The crude vanillin composition may further comprise at least one compound selected from vanillyl alcohol, vanillic acid, acetovanillone, guaiacol, and vinyl guaiacol.

[0040] Step (b): Step (b) is an optional step of purifying the composition obtained at the end of step (a). In one variation, step (b) is not optional.

[0041] Typically, step (b) may involve liquid-liquid extraction as described in EP 2791098. Preferably, the liquid-liquid extraction is carried out using a solvent that is compatible with food processing applications.

[0042] Step (b) may also comprise at least one crystallization step. According to another alternative, the purification step may comprise extraction with supercritical CO2.

[0043] Finally, according to another alternative, step (b) may comprise a step of evaporating the crude natural vanillin as described in EP 2948424 or a stripping step as described in WO 2018 / 146210.

[0044] According to a particular embodiment of the invention, step (b) is a step of evaporation in a wiped film evaporator or a falling film evaporator. Advantageously, this step allows the removal of compounds less volatile than vanillin present in the crude natural vanillin composition obtained at the end of step (a). The less volatile compounds are preferably chosen from vanillyl alcohol, vanillic acid, acetovanillone and heavier compounds.

[0045] The term "heavy compounds" refers to compounds that are less volatile than vanillin under the temperature and pressure conditions considered. Among the heavy impurities, mention may be made of dimers and trimers of vanillin (i.e., compounds exhibiting a skeleton with two or three phenyl groups, respectively), and ferulic acid.

[0046] This embodiment is particularly advantageous in that it makes it possible to purify the crude natural vanillin composition obtained at the end of step (a) and to prepare a natural vanillin composition according to the invention, the content of impurities being particularly well controlled and the natural vanillin composition being very lightly colored.

[0047] The process according to the invention makes it possible to limit the content of 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde.

[0048] Furthermore, this embodiment makes it possible to avoid stripping steps in the presence of entrained gases and / or vaporized liquids, which makes the process interesting from an industrial point of view as it is economically viable.

[0049] The temperature of the heat transfer fluid in step (b) is usually at least 130° C., preferably at least 145° C. The temperature of the heat transfer fluid is usually at most 230° C., preferably at most 180° C.

[0050] The pressure at which step (b) is carried out is usually at least 0.4 mbar, preferably at least 1 mbar. Usually, the pressure is at most 75 mbar, preferably at most 8 mbar, more preferably at most 4 mbar.

[0051] Advantageously, the concentration by weight of natural vanillin in the crude natural vanillin composition used in step (b) is at least 10%, preferably at least 20%, more preferably at least 30%, even more preferably at least 50%, and very preferably at least 70% by weight relative to the total weight of the crude natural vanillin composition. The method may comprise a step of concentrating the crude natural vanillin composition.

[0052] According to a preferred embodiment, step (b) is carried out in the presence of at least one technical auxiliary, such as a fluidizing agent. Thus, according to a particular embodiment of the present invention, a fluidizing agent approved by food regulations can be added to the natural vanillin. The fluidizing agent can be added before step (b), in particular between steps (a) and (b). According to another embodiment, the fluidizing agent can be added during step (b).

[0053] The fluidizing agent may be selected from white mineral oil, especially food-grade white mineral oil, polyethylene glycol, especially polyethylene glycol with an average molecular weight of 200 to 3000 g / mol, preferably 600 to 1500 g / mol, or castor oil.

[0054] Preferably, step (b) is carried out under an inert atmosphere, in particular argon, nitrogen, or a mixture thereof. Step (b) may also be carried out under low-oxygen air, typically with an oxygen content of 1% or less.

[0055] The evaporator makes it possible to recover a gas effluent comprising the evaporated natural vanillin composition, which is then condensed to recover a condensate of the natural vanillin composition according to the invention.

[0056] Advantageously, the natural vanillin titre is greater than or equal to 90%, very preferably greater than 95% and even more preferably greater than or equal to 99%. According to a particular embodiment, the vanillin titre is greater than or equal to 99.5%.

[0057] Advantageously, the natural vanillin concentrate obtained at the end of step (b) of purifying the natural vanillin is lightly colored. Advantageously, the natural vanillin concentrate obtained at the end of step (b) is a natural vanillin composition according to the invention.

[0058] Advantageously, this natural vanillin concentrate obtained at the end of step (b) is compatible and exhibits organoleptic properties that are at least equivalent to those of natural vanillin extracted from the pods or to synthetic vanillin.

[0059] According to a particular embodiment, the purification step (b) does not include a stripping step.

[0060] According to a particular embodiment, the method of the present invention does not comprise a step consisting of melting the natural vanillin composition before the step of evaporation in a falling film evaporator or a wiped film evaporator. According to a particular embodiment, the natural vanillin composition does not crystallize between steps (a) and (b).

[0061] The method further comprises, at the end of step (b), preferably by crystallization, more preferably by FEMA GRAS TM It may also include an optional step (c) of forming the resulting natural vanillin composition by crystallization in a solvent identified by the program. In a preferred embodiment, the natural vanillin composition is crystallized or recrystallized from water or from a water / alcohol (especially ethanol) mixture.

[0062] The process according to the invention can be carried out in continuous or batchwise operation.

[0063] The present invention also relates to a natural vanillin composition obtainable by the method described according to the invention.

[0064] Finally, the present invention relates to the use of natural vanillin compositions in the field of human food and animal diet, in pharmaceuticals, as flavorings or as fragrances in the cosmetics, perfume and detergent industries.

[0065] The following examples are intended to illustrate, but not limit, the present invention.

[0066] In the event that the disclosures of patents, patent applications, and publications cited herein by reference contradict the description of this application to the extent that there is a risk of rendering the term uncertain, the present description shall control. [Example]

[0067] Example 1: A crude natural vanillin composition is prepared from a fermentation carried out according to the procedure described in EP 0 885 968. In addition to the solvent, the crude vanillin composition contained the compounds listed in Table 1.

[0068] [Table 1]

[0069] Example 2: A crude natural vanillin composition obtained according to the method of EP 0 885 968 is purified by vacuum evaporation in a wiped film evaporator in the presence of castor oil.

[0070] Properties of natural vanillin compositions according to the invention.

[0071] [Table 2]

Claims

1. A composition comprising natural vanillin, 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde, and 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde, wherein the composition exhibits a natural vanillin titer of 90% or more.

2. 10. The composition of claim 1, further comprising at least one compound selected from vanillyl alcohol, vanillic acid, acetovanillone, guaiacol, and vinylguaiacol.

3. 3. The composition of claim 1, wherein the natural vanillin titer is greater than 95%.

4. The composition according to any one of claims 1 to 3, wherein the weight content of 4-((4-hydroxy-3-methoxybenzyl)oxy)-3-methoxybenzaldehyde relative to the total weight of the composition is 10,000 ppm or less and 10 ppm or more.

5. The composition according to any one of claims 1 to 4, wherein the weight content of 4-hydroxy-3-(4-hydroxy-3-methoxybenzyl)-5-methoxybenzaldehyde is 5000 ppm or less and 10 ppm or more relative to the total weight of the composition.

6. The composition according to any one of claims 1 to 5, characterized by a color of 400 Hazen or less.

7. Use of a composition according to any one of claims 1 to 6 in the field of human food and animal diet, in pharmaceuticals, as a flavouring agent or as a fragrance in the cosmetics, perfume and detergent industry.

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