阅读说明：本技术 产生细菌来源的吲哚-3-丙酸的方法以及包含其的组合物 (Method for producing indole-3-propionic acid of bacterial origin and compositions comprising same ) 是由 A·文卡塔拉曼 C·L·布鲁斯特 K·C·科扎克 L·李 J·A·斯坦珀 于 2020-04-02 设计创作，主要内容包括：本文描述了经由细菌发酵产生吲哚-3-丙酸和其他吲哚衍生物的方法及其组合物。该方法包括将具有与SEQ ID NO:1的核酸序列具有至少80％同源性的核酸序列的细菌产芽胞梭状芽胞杆菌(Clostridium sporogenes)ATCC15579添加到液体发酵培养基中；在厌氧条件下于约36℃发酵；添加脱水剂；以及脱水以获得包含吲哚-3-丙酸和其他吲哚衍生物的发酵物粉末。(Described herein are methods of producing indole-3-propionic acid and other indole derivatives via bacterial fermentation and compositions thereof. The method comprises adding a bacterial spore-forming Clostridium (Clostridium sporogenes) ATCC15579 having a nucleic acid sequence with at least 80% homology to the nucleic acid sequence of SEQ ID NO. 1 to a liquid fermentation medium; fermenting under anaerobic conditions at about 36 ℃; adding a dehydrating agent; and dehydrating to obtain a fermentation broth powder comprising indole-3-propionic acid and other indole derivatives.)

1. A method of producing indole-3-propionic acid and other indole derivatives, comprising: adding a bacterium having a nucleic acid sequence with at least 80% homology to the nucleic acid sequence of SEQ ID NO. 1 to a liquid fermentation medium to form a bacterial solution; fermenting the bacterial solution under anaerobic conditions at 36 ℃; adding a dehydrating agent; and dehydrating to obtain a fermentation broth powder comprising indole-3-propionic acid and other indole derivatives.

2. The method of claim 1, further comprising centrifuging the fermented bacterial solution to form a supernatant and a bacterial pellet; taking out the supernatant; and adding the dehydrating agent to the supernatant.

3. The method of claim 1 or 2, wherein the ferment powder comprises 0.1 to 20mg/g indole-3-propionic acid.

4. The process according to any of the preceding claims, wherein the ferment powder comprises from 0.1 to 20mg/g of other indole derivatives.

5. The method of any one of the preceding claims, wherein the fermentation medium comprises water, an amino acid composition, a salt, a mineral, and optionally a carbohydrate.

6. The method according to any one of the preceding claims, further comprising homogenizing prior to the dewatering step.

7. The method of any one of the preceding claims, wherein the dewatering step is spray drying.

8. The method of any one of the preceding claims, wherein the dehydrating step is freeze-drying.

9. A composition, comprising: a ferment comprising indole-3-propionic acid of bacterial origin; and excipients, carriers and/or diluents.

10. The composition of claim 9, wherein the composition comprises 0.01 to 10% indole-3-propionic acid, by weight of the composition.

11. The composition of claim 9 or 10, wherein the composition further comprises an indole derivative selected from the group consisting of indole-3-acetic acid, indole-3-acrylic acid, indole-3-lactic acid, and combinations thereof.

12. The composition according to claims 9 to 11, wherein the composition further comprises one or more bacteria selected from the group consisting of: bifidobacterium bifidum (Bifidobacterium bifidum), Bifidobacterium breve (Bifidobacterium breve), Bifidobacterium infantis (Bifidobacterium infantis), Bifidobacterium longum (Bifidobacterium longum), Streptococcus cremoris (Streptococcus cremoris), Streptococcus diacetylactis (Streptococcus diacetobacter), Streptococcus lactis (Streptococcus lactis), Streptococcus thermophilus (Streptococcus thermophilus), Lactobacillus acidophilus (Lactobacillus acidophilus), Lactobacillus bifidus (Lactobacillus bifidus), Lactobacillus bulgaricus (Lactobacillus bulgaricus), Lactobacillus casei (Lactobacillus casei), Lactobacillus delbrueckii (Lactobacillus delbrueckii), Lactobacillus crispatus (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus casei), Lactobacillus casei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei, Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei, Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei, Lactobacillus (Lactobacillus paracasei, Lactobacillus), Lactobacillus paracasei, Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei, Lactobacillus), Lactobacillus (, Lactobacillus salivarius, Lactobacillus thermophilus, Lactococcus lactis, Clostridium sporogenes, Streptococcus anaerobiosis, Clostridium cadaveris, Clostridium bold, and combinations thereof.

13. The composition of claim 12, comprising from 1 × E3 Colony Forming Units (CFU) to 1 × E11CFU of the one or more bacteria.

14. The composition of claims 9-12, wherein the fermentate further comprises tryptophan.

15. A method of promoting brain health, the method comprising administering the composition of claim 9 to an individual in need thereof.

Technical Field

Described herein are methods of producing indole-3-propionic acid and other indole derivatives of bacterial origin. Also described herein are compositions comprising indole-3-propionic acid and other indole derivatives that can help support brain health and/or nervous system function.

Background

Following good nutritional practices can be challenging. Some people seek supplements to provide additional nutrients to improve the health and well-being of his (her) s, including maintaining healthy brain function. The brain is particularly susceptible to oxidative stress due to high oxygen consumption rates, high levels of polyunsaturated fatty acids and local high iron levels, and proportionately low antioxidant capacity. Oxidative stress is known to lead to reduced neurogenesis and increased neuronal death. Cognitive impairment has been shown to be associated with oxidative stress, and an effective antioxidant system can maintain cognitive function in the elderly.

Indole-3-propionic acid ("IPA") is a neuroprotective antioxidant that can improve the mood, cognition and/or maintain healthy brain function and nervous system in humans. IPA is produced by the intestinal flora in the colon and passes through the intestinal epithelium and the blood-brain barrier into the brain. In the brain, IPA has been shown to act as a protective agent to protect the structure and function of neurons. It is believed that the antioxidant properties of IPA may play a key role in promoting brain health. It is well known that oral administration of IPA increases IPA levels in situ (see Kaufmann SHE, 2018, "oil propionic acid: a small molecular links between gun microbiota and tuberculosis", Antimicrob Agents Chemother, Vol.62, p.00389-18; Niebler G, NCT 01898884: "Safety and Pharmacology Study of VP 20629 in Adults With Friedreich's Ataxia", 2018).

Although an increasing number of people recognize the beneficial effects of IPA on brain health, IPA is only commercially produced in a chemically synthesized form. However, more and more consumers are interested in product ingredients (including their source) and prefer supplements from natural sources. These consumers seeking natural sources of nutrition may not like direct intake of chemically synthesized IPA. In addition, other indole derivatives such as indole-3-acetic acid, indole-3-acrylic acid and indole-3-lactic acid have emerged in addition to IPA as providing positive health benefits. However, chemically synthesized forms of IPA deliver only pure IPA.

Accordingly, there is a need for a method of providing a natural source of a combination of indole derivatives in which IPA is the major component in order to promote brain health and/or nervous system function.

Disclosure of Invention

Described herein are compositions comprising: (a) a ferment comprising indole-3-propionic acid and other indole derivatives of bacterial origin; and (b) an excipient, carrier and/or diluent.

Described herein are methods of producing indole-3-propionic acid and other indole derivatives, comprising: (a) adding a bacterium having a nucleic acid sequence with at least 80% homology to the nucleic acid sequence of SEQ ID NO. 1 to a liquid fermentation medium to form a bacterial solution; (b) fermenting the bacterial solution under anaerobic conditions at about 36 ℃; (c) adding a dehydrating agent; and (d) dehydrating to obtain a fermentation broth powder comprising indole-3-propionic acid and other indole derivatives.

Described herein are compositions comprising: a ferment comprising indole-3-propionic acid and other indole derivatives of bacterial origin; and excipients, carriers and/or diluents; wherein the fermentation is obtained by a process comprising the steps of: (a) adding a bacterium having a nucleic acid sequence with at least 80% homology to the nucleic acid sequence of SEQ ID NO. 1 to a liquid fermentation medium to form a bacterial solution; (b) fermenting the bacterial solution under anaerobic conditions at about 36 ℃; (c) adding a dehydrating agent; and (d) dehydrating to obtain the fermentation.

Described herein is a method of promoting brain health by administering a composition to deliver antioxidant nutrients to the brain, the composition comprising: (a) a ferment comprising indole-3-propionic acid and other indole derivatives of bacterial origin; and (b) an excipient, carrier and/or diluent.

Detailed Description

Consumers are looking for an effective and natural way to supplement his (her) diet with IPA to promote brain and mental health. Described herein are methods of producing IPA and other indole derivatives by bacterial fermentation and compositions thereof. It has been found that bacterial fermentation in the presence of tryptophan and other components such as amino acids, vitamins and trace metals can produce naturally derived IPA and other indole derivatives that can be dried into a fermentation powder without adversely affecting the stability of the IPA or other indole derivatives. As used herein, "other indole derivatives" refers to tryptophan-derived indole metabolites, including indole-3-propenoic acid, indole-3-lactic acid, and indole-3-acetic acid.

As used herein, the terms "administering," "administering," and "administering" refer to any method of delivering a composition to a subject in a manner that provides a therapeutic effect in sound medical practice.

As used herein, "anaerobic conditions" refers to any growth or nutrient condition that excludes the presence of oxygen (e.g., less than about 1ppm free oxygen, preferably less than about 0.1ppm free oxygen, more preferably from about 0 to about 1ppm free oxygen).

As used herein, the abbreviation "CFU" ("number of colony forming units") refers to the number of bacterial cells represented by microbial counts on agar plates, as is commonly understood in the art.

As used herein, "fermentation" refers to the process by which a microorganism metabolizes a feedstock.

As used herein, "fermentate" refers to an isolated solid after removal of water from a fermentation medium with or without prior removal of bacteria.

The terms "microorganism" and "microorganism" are used interchangeably herein and refer to a bacterium. The terms "population", "microbiota" and "microbiota" are used interchangeably herein and may refer to a microbial ecological community that lives on or within the body of a subject. The flora may be present on or in many, if not most, parts of the subject. Some non-limiting examples of habitats of flora may include: body surfaces, body cavities, body fluids, intestinal tract, colon, skin surfaces and pores, vaginal cavity, umbilical region, conjunctival region, intestinal region, stomach, nasal and nasal passages, gastrointestinal tract, urogenital tract, saliva, mucus, and feces.

As used herein, the term "prebiotic" refers to a chemical and/or ingredient that can affect the growth and/or activity of a microorganism in a subject or host (e.g., can allow for a particular change in the composition and/or activity of the flora) and can impart a health benefit to the subject.

As used herein, the term "probiotic" may mean one or more live microorganisms (e.g., bacteria or yeast) that, when properly administered, may impart health benefits to a subject. As used herein, "nucleic acid sequence" and "nucleotide sequence" refer to oligonucleotides or polynucleotides and fragments or portions thereof, and to DNA or RNA of genomic or synthetic origin, which may be single-stranded or double-stranded and represent the sense or antisense strand. The nucleic acid sequence may be composed of adenine, guanine, cytosine, thymine and uracil (A, T, C, G and U) as well as modified forms (e.g., N6-methyladenosine, 5-methylcytosine, etc.).

The term "subject" refers to any animal subject, including humans, laboratory animals, livestock, and domestic pets.

As used herein, the articles "a" and "an" are understood to mean one or more of the materials claimed or described, for example, "active ingredient" or "probiotic".

The composition may comprise, consist of, or consist essentially of: the essential elements and limitations of the invention described herein, as well as any additional or optional ingredients, components, or limitations described herein or that can be used in compositions intended for use or consumption by a subject.

Methods of producing IPA and other indole derivatives may include the steps of:

a. adding bacteria capable of producing IPA and other indole derivatives to a liquid fermentation medium to form a bacterial solution;

b. fermenting the bacterial solution under anaerobic conditions to form a fermented bacterial solution;

c. terminating the fermentation;

d. optionally concentrating the bacterial solution by reducing the water content (e.g., by reverse osmosis, tray drying, microfiltration, nanofiltration, and combinations thereof);

e. adding a dehydrating agent; and

f. dehydrating to obtain a ferment powder comprising indole-3-propionic acid and other indole derivatives.

Bacteria capable of producing IPA and other indole derivatives include, for example, Clostridium sporogenes (Clostridium spongiogenes), streptococcus anaerobically digested (streptococcus anaerobicus), Clostridium cadaveris (Clostridium cadeveris), Clostridium bold (Clostridium bolthae), and any other bacteria having a nucleic acid sequence substantially homologous to the nucleic acid sequence of SEQ ID No. 1 (table 1) encoding the gene cluster of the phenyllactic acid dehydratase (fldL, fldI, and fldABC).

TABLE 1 DNA sequences

Bacteria comprise nucleic acid sequences having a particular degree of homology or identity with other bacteria. As used herein, the terms "identity", "homology" and "homology" refer to the degree to which other nucleotide sequences are complementary or share similarity. There may be partial homology or complete homology (i.e., identical sequences). A nucleotide sequence that is partially complementary (i.e., "substantially homologous" or "substantially identical") to a nucleic acid sequence is a sequence that at least partially inhibits hybridization of a fully complementary sequence to a target nucleic acid sequence.

In some aspects, the bacterium can comprise a nucleic acid sequence that has at least about 60%, at least about 61%, at least about 62%, at least about 63%, at least about 64%, at least about 65%, at least about 66%, at least about 67%, at least about 68%, at least about 69%, at least about 70%, at least about 71%, at least about 72%, at least about 73%, at least about 74%, at least about 75%, at least about 76%, at least about 77%, at least about 78%, at least about 79%, at least about 80%, at least about 81%, at least about 82%, at least about 83%, at least about 84%, at least about 85%, at least about 86%, at least about 87%, at least about 88%, at least about 89%, at least about 90%, at least about 91%, at least about 92%, at least about 93%, at least about 94%, at least about 95%, at least about 96%, at least about 97%, or a combination thereof, of the nucleic acid sequences of SEQ ID NO. 1, At least about 98% or at least about 99% homology or identity.

In some aspects, the bacterium comprising the nucleic acid sequence of SEQ ID NO. 1 can be a probiotic or a probiotic bacterium.

Bacteria require a fermentation medium in which they ferment and produce IPA and its derivatives. The fermentation medium can be any suitable medium that is capable of allowing the growth and fermentation of the microorganism. In some aspects, the fermentation medium can be a standard amino acid complete medium. In some aspects, the fermentation medium may comprise water, an amino acid composition, vitamins, salts, and minerals. In some aspects, the fermentation medium may comprise water, an amino acid composition, vitamins, salts, carbohydrates, and minerals.

In some aspects, the amino acid composition can comprise one or more amino acids. Non-limiting examples of amino acids may include glutamine, lysine, cysteine, methionine, aspartic acid, leucine, valine, alanine, arginine, glycine, tyrosine, tryptophan, phenylalanine, histidine, leucine, isoleucine, and combinations thereof. Amino acids should include those suitable for IPA production. Examples of amino acid compounds that can be used include cysteine hydrochloride, L-glycine, L-valine, L-leucine, L-isoleucine, L-methionine, L-histidine, L-arginine, L-phenylalanine, L-tyrosine, and L-tryptophan. The amount of amino acid will vary depending on the amount of IPA desired to be produced. In some aspects, the fermentation medium can comprise about 8 to about 10,000 μ g/mL, alternatively about 10 to about 8,000 μ g/mL, alternatively about 25 to about 5,000 μ g/mL, alternatively about 50 to about 1,000 μ g/mL, alternatively about 100 to about 500 μ g/mL of the amino acid.

In some aspects, the ratio of other amino acids to tryptophan should be greater than 1: 1. It is believed that the other amino acids should be present at a concentration greater than the tryptophan concentration in order to increase the yield of IPA and other indole derivatives.

In some aspects, the fermentation medium may comprise one or more salts. Salts may be added to the fermentation medium to improve the viability of the bacteria and/or may increase the yield of IPA and other indole derivatives. Non-limiting examples of salts may include calcium carbonate, ammonium sulfate, magnesium sulfate, potassium dihydrogen phosphate, dipotassium hydrogen phosphate, magnesium chloride, sodium bicarbonate, and combinations thereof. The amount of salt added to the fermentation medium should be sufficient to achieve the desired results of improving viability and/or increasing yield of IPA and its derivatives. In some aspects, the fermentation medium may comprise from about 10 to about 5,000mg/L, alternatively from about 20 to about 1,000mg/L, alternatively from about 50 to about 800mg/L, alternatively from about 75 to about 500mg/L of salt.

In some aspects, the fermentation medium may comprise a carbohydrate. The carbohydrate may include polysaccharides, oligosaccharides, disaccharides, monosaccharides, and combinations thereof. Non-limiting examples of suitable carbohydrates may include maltose, gum arabic, and glucose. In some aspects, the fermentation medium may comprise about 2 to about 40mM, alternatively about 5 to about 30mM, alternatively about 10 to about 25mM carbohydrate.

In some aspects, the fermentation medium may comprise one or more vitamins. Non-limiting examples of vitamins can include vitamin B1, vitamin B2, vitamin B3, vitamin B5, vitamin B6, vitamin B7, vitamin B9, vitamin B12, and combinations thereof. In some aspects, the fermentation medium may comprise a vitamin solution, such as Wolfe's vitamin solution or vitamin supplementMD-VS^TM(commercially available from ATCC (Manassas, Va.).

In some aspects, the fermentation medium may also include one or more trace elements, such as zinc, manganese, and nickel. In some aspects, the fermentation medium may comprise a trace element solution, such as Wolfe's mineral solution or trace mineral supplementMD-TMS^TM(commercially available from ATCC (Manassas, Va.).

The fermentation medium may have a pH of about 5 to about 8, alternatively about 5.5 to about 7.5, alternatively about 6 to about 7. Without being limited by theory, it is believed that the pH may be selected to increase the yield of IPA and derivatives thereof.

The fermentation medium may be prepared by any method known in the art.

The bacteria can be added anaerobically to the fermentation medium to form a bacterial solution. The number of CFUs of bacteria added to the fermentation medium may vary depending on the type of bacteria used and the amount of IPA desired to be produced. In some aspects, the fermentation can be conducted at an initial cell concentration of between 1E3 to about 1E9CFU/mL, preferably 1E5 to about 1E8CFU/mL, more preferably about 1E8CFU/mL of fermentation medium.

The bacterial solution may be maintained under conditions that allow optimal growth of the bacteria. For example, the bacterial solution may be maintained under anaerobic conditions at a temperature of from about 25 ℃ to about 45 ℃, preferably from about 30 ℃ to about 40 ℃, more preferably about 36 ℃.

In some aspects, the bacteria should be allowed to ferment for a sufficient period of time to produce the desired amount of IPA and derivatives thereof. In some aspects, the bacterial solution is incubated at about 36 ℃ for about 24 to about 48 hours, alternatively about 2 hours to about 72 hours, alternatively about 4 hours to about 48 hours, alternatively about 8 hours to about 36 hours, alternatively about 12 hours to about 36 hours, under anaerobic conditions.

In some aspects, fermentation may be terminated by one or more process steps in which the bacteria are inactivated or physically removed. The bacteria may be inactivated by heating (typically at a temperature between about 65 ℃ to about 93 ℃ for 30 minutes to 3 hours) or by treatment with a proteolytic enzyme such as papain or bromelain. Alternatively, the fermented bacterial solution may be centrifuged to form a bacterial pellet and a supernatant, and the bacterial pellet may be discarded, leaving a supernatant containing IPA and other indole derivatives, which may be dewatered to form a fermentation. Alternatively, the fermented bacterial solution may be passed through a membrane filter to remove bacteria.

In some aspects, the solution may be homogenized after fermentation in order to form a more uniform product. Methods of homogenization are known in the art and may be performed, for example, by a homogenizing pump, a shear pump, or a blender. Preferably, the solution is dehydrated after fermentation. Methods for dehydrating solutions are well known in the art and may include freeze drying, spray drying, open air drying, spray granulation, and drum drying. Preferred dehydration methods are spray drying or freeze drying.

Optionally, the residual water content in the fermented bacterial solution may be significantly reduced by a combination of e.g. reverse osmosis, tray drying, microfiltration and/or nanofiltration prior to dewatering. Methods of reverse osmosis, tray drying, microfiltration and nanofiltration may be performed using methods and equipment well known in the art.

Lyophilization may be carried out using methods well known in the art. In particular, the freeze-drying process may consist of a heat treatment step followed by a drying step. In the heat treatment step, the vial may be held at about 20 ℃ for about 30 minutes, then at about 0 ℃ for about 80 minutes, and then at about-25 ℃ for about 60 minutes. Freezing can be performed at about-25 ℃ (about-50 ℃ condenser) and about 200mtorr vacuum. In the drying step, the vial may be held at about-25 ℃ and about 200mtorr for a total of about 1800 minutes, then the temperature may be raised to about 4 ℃ and the vial held at about 4 ℃ and about 200mtorr for about 60 minutes.

Spray drying may be carried out using methods and equipment well known in the art. Preferably, a Spray Dryer is used, such as the Buchi Mini Spray Dryer B-191 available from Buchi Labortechnik AG (Flawil, Switzerland) or equivalent. The spray dryer may be operated with an inlet temperature of about 185 ℃, and the flow rate of the pump feeding the dryer may be set to achieve an outlet temperature of about 100 ℃. The spray dryer unit may be operated with a two-fluid atomizer. The sprayer can deliver the liquid feed to the dryer. The gas flow rate may be set to a volumetric flow rate of about 35 cubic meters per hour.

Prior to dehydration, a dehydrating agent may be added to the solution to facilitate drying and/or improve stability. In some aspects, the dehydrating agent can be a cryoprotectant, such as inositol, sorbitol, mannitol, trehalose, glucose, sucrose, corn syrup, DMSO, all types of starch and/or modified starch, polyvinylpyrrolidone (PVP), maltose or other mono-and disaccharides, and combinations thereof. The dewatering agent can be used at any level suitable to facilitate drying, for example, from about 2 to about 10 weight percent, alternatively from about 3 to about 8 weight percent, alternatively from about 4 to about 6 weight percent. Preferably, the dehydrating agent is a modified starch, such as that derived from waxy maize100 modified food starch (commercially available from Ingredion (Westchester, IL)).

The solution may be dehydrated to a residual water content of less than about 15 wt%, alternatively less than about 10 wt%, alternatively less than about 5 wt%. Alternatively, and particularly when the residual water content is greater than about 5 wt.%, additional agents may be included that reduce the water activity to a value equal to or less than about 0.75, alternatively equal to or less than about 0.7, alternatively equal to or less than about 0.65, alternatively equal to or less than about 0.55, alternatively equal to or less than about 0.40.

After dehydration, a powder fermentation comprising IPA and its derivatives is formed, which can then be incorporated into a dosage form or other form suitable for administration.

Also described herein is a composition comprising a ferment comprising IPA of bacterial origin and other indole derivatives and physiologically, pharmaceutically or nutraceutically acceptable excipients, carriers and/or diluents. In some aspects, the composition may comprise one or more bacterial strains or species in combination with bacterially derived IPA and other indole derivatives. In some aspects, the fermentation may further comprise tryptophan.

The composition may comprise a fermentate. The fermented product can be obtained by the above method. In some aspects, the fermentate may include IPA, other indole derivatives, and tryptophan. In some aspects, the fermentate may optionally comprise a non-viable bacterium having a nucleic acid sequence with at least 80% homology to the nucleic acid sequence of SEQ ID No. 1;

in some aspects, the composition may comprise from about 1mg to about 2g, alternatively from about 10mg to about 1.5g, alternatively from about 25mg to about 1g of fermentate. In some aspects, the composition may comprise from about 1mg to about 500mg, alternatively from about 15mg to about 250mg, alternatively from about 50mg to about 150mg of fermentate.

In one aspect, the composition may comprise from about 0.01% to about 90%, alternatively from about 0.1% to about 85%, alternatively from about 1% to about 80%, alternatively from about 2.5% to about 75%, alternatively from about 5% to about 60%, alternatively from about 10% to about 50%, alternatively from about 15% to about 25%, of the fermentate, all percentages being by weight of the composition.

In some aspects, the composition can comprise from about 1 × E3CFU/g fermentate to about 1 × E13CFU/g fermentate of bacteria.

In some aspects, the composition may comprise from about 0.1mg to about 20mg, alternatively from about 1mg to about 8mg, alternatively from about 2mg to about 6mg of IPA. In some aspects, the composition may comprise from about 0.01% to about 10%, alternatively from about 1% to about 8%, alternatively from about 2% to about 6%, IPA, all percentages by weight of the composition.

In some aspects, the composition may comprise from about 0.1mg/g to about 20mg/g, alternatively from about 1mg/g to about 8mg/g, alternatively from about 2mg/g to about 6mg/g IPA.

In some aspects, the composition may comprise from about 0.01mg to about 10mg, alternatively from about 0.1mg to about 8mg, alternatively from about 1mg to about 6mg, of the other indole derivative. In some aspects, the composition can comprise from about 0.01% to about 10%, alternatively from about 1% to about 8%, alternatively from about 2% to about 6%, of other indole derivatives, all percentages by weight of the composition.

In some aspects, the composition may comprise from about 0.01mg to about 10mg, alternatively from about 0.1mg to about 8mg, alternatively from about 1mg to about 5mg, of tryptophan. In some aspects, the composition may comprise from about 0.1% to about 10%, alternatively from about 1% to about 8%, alternatively from about 2% to about 5%, tryptophan, all percentages by weight of the composition.

In some aspects, the fermentate may comprise from about 0.1mg/g to about 0.5mg/g, preferably 0.2mg/g, tryptophan.

In some aspects, the fermentation may comprise glucose. The amount of glucose present in the fermentate may depend on when the fermentation reaction is terminated (which in turn will be a function of the bacterial growth phase) and the IPA yield.

In some aspects, the composition may comprise one or more bacteria. In some aspects, the one or more bacteria may be probiotics. Suitable probiotics may include Bifidobacterium bifidum (Bifidobacterium bifidum), Bifidobacterium breve (Bifidobacterium breve), Bifidobacterium infantis (Bifidobacterium infantis), Bifidobacterium longum (Bifidobacterium longum), Streptococcus cremoris (Streptococcus cremoris), Streptococcus diacetylactis (Streptococcus diacetobacter), Streptococcus lactis (Streptococcus lactis), Streptococcus thermophilus (Streptococcus thermophilus), Lactobacillus acidophilus (Lactobacillus acidophilus), Lactobacillus bifidus (Lactobacillus bifidus), Lactobacillus bulgaricus (Lactobacillus bulgaricus), Lactobacillus casei (Lactobacillus casei), Lactobacillus delbrueckii (Lactobacillus crispatus), Lactobacillus crispatus (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (, Lactobacillus reuteri (Lactobacillus reuteri), Lactobacillus salivarius (Lactobacillus salivarius), Lactobacillus thermophilus (Lactobacillus thermophilus), Lactococcus lactis (Lactobacillus lactis), and combinations thereof.

In some aspects, the one or more bacteria may comprise clostridium sporulatum (c. In some aspects, the clostridium spore-forming bacteria can be inactive.

In some aspects, the one or more bacteria is bifidobacterium infantis, in particular bifidobacterium infantis 35624.

In some aspects, the composition may comprise an excipient, carrier, and/or diluent. Nutritionally acceptable excipients, carriers or diluents include, but are not limited to, those suitable for human or animal consumption, as well as those standard for the food industry. Typical nutritionally acceptable excipients, carriers or diluents are familiar to those skilled in the art.

In some aspects, examples of such suitable Excipients for use in the various compositions described herein can be found in "Handbook of Pharmaceutical Excipients" edited by a Wade and P J Weller (2 nd edition, 1994). In some aspects, acceptable carriers or diluents are described, for example, in "Remington's Pharmaceutical Sciences" (Mack Publishing co., a.r. gennaro editors, 1985). Such suitable carriers include, but are not limited to, lactose, methylcellulose, magnesium stearate, and the like. Such suitable diluents include, but are not limited to, water, ethanol, and glycerol.

The choice of pharmaceutical excipient, carrier or diluent is selected according to the intended route of administration and standard pharmaceutical or nutritional practice. In some aspects, such compositions may comprise additional ingredients in addition to the excipient, carrier, or diluent. Such additional ingredients include, but are not limited to, any suitable binders, lubricants, suspending agents, coating agents, solubilizing agents, preservatives, dyes, flavoring agents, and/or suspending agents.

Examples of suitable binders include, but are not limited to, starch, gelatin, and natural sugars. Such natural sugars include, but are not limited to, glucose, anhydrous lactose, free-flowing lactose, beta-lactose, corn sweeteners, and natural and/or synthetic gums such as gum arabic, tragacanth or sodium alginate, carboxymethylcellulose, and polyethylene glycol. Examples of suitable lubricants include, but are not limited to, sodium oleate, sodium stearate, magnesium stearate, sodium benzoate, sodium acetate, sodium chloride, and the like. In some aspects, preservatives, stabilizers, dyes, and flavoring agents are also provided in the compositions. Examples of preservatives include, but are not limited to, sodium benzoate, sorbic acid, and esters of p-hydroxybenzoic acid. In some aspects, suspending agents may also be present in the compositions.

In some aspects, the composition may optionally comprise one or more active ingredients. Non-limiting examples of active ingredients may include vitamins, minerals, prebiotics, polysaccharides (e.g., as a bait that will restrict specific bacteria/viruses from binding to the intestinal wall), melatonin, and combinations thereof. Non-limiting examples of vitamins may include vitamin C, vitamin D, vitamin E, vitamin K1, vitamin K3, vitamin B1, vitamin B3, folic acid, vitamin B12, vitamin B2, vitamin B3, vitamin B6, vitamin B7, and pantothenic acid (vitamin B5). Non-limiting examples of minerals may include calcium, selenium, magnesium, iron, iodide, zinc, copper, manganese, chromium, molybdenum, beta-carotene, and combinations thereof.

As used herein, the term "prebiotic" may be a general term referring to a chemical and/or ingredient that may affect the growth and/or activity of a microorganism in a subject or host (e.g., may allow for a particular change in the composition and/or activity of the flora) and may impart a health benefit to the subject. Prebiotics include, but are not limited to, complex carbohydrates, complex sugars, resistant dextrins, resistant starches, amino acids, peptides, nutritional compounds, biotin, polydextrose, Fructooligosaccharides (FOS), Galactooligosaccharides (GOS), inulin, lignin, psyllium, chitin, chitosan, gums (e.g., guar gum), high amylose corn starch (HAS), cellulose, beta-glucan, hemicellulose, lactulose, Mannooligosaccharides (MOS), fructooligosaccharide-rich inulin, fructooligosaccharides, dextrose oligosaccharides, tagatose, transgalactooligosaccharides, pectin, and Xylooligosaccharides (XOS). Prebiotic substrates such as these improve colonization and survival of bacteria in the body. In some aspects, the prebiotic is selectively fermented, for example, in the colon.

In various aspects, prebiotics are present in food products (e.g., gum arabic, guar seeds, brown rice, rice bran, barley hulls, chicory roots, jerusalem artichoke, dandelion leaves, garlic, leek, onion, asparagus, wheat bran, oat bran, baked beans, whole wheat flour, bananas) and breast milk. In some aspects, the prebiotic is administered in other forms (e.g., capsules or dietary supplements).

Depending on the particular active ingredient, the active ingredient may be present in an amount above, below, and/or equal to the recommended daily nutrient amount ("RDA"). Exemplary RDA values for many nutritional compounds are listed in 21CFR101, and additional RDA values are also published by the Institute of Medicine of the National Academy of sciences.

In some aspects, the active ingredient is present in an amount of about 0.01 wt% to about 50 wt%, relative to the total weight of the composition. In some aspects, the active ingredient may be present in an amount of about 0.1% to about 40%, alternatively about 1% to about 30%, alternatively about 3% to about 25%, alternatively about 5% to about 20%, by weight. In some aspects, the active ingredient is present in an amount of about 1%, 2%, 3%, 4%, 5%, 6%, 7%, 8%, 9%, 10%, 11%, 12%, 13%, 14%, 15%, 16%, 17%, 18%, 19%, 20%, 21%, 22%, 23%, 24%, 25%, 26%, 27%, 28%, 29%, 30%, 35%, 40%, 45%, or 50%.

The composition may optionally comprise one or more herbal ingredients. Non-limiting examples of herbal ingredients may include rosemary (leaf), ginger, lemon balm, green tea, holy basil, oregano, thyme, kava, bacopa and combinations thereof. In some aspects, the composition comprises ashwagandha. In some aspects, the herbal ingredient may be a whole herb or plant part, an extract, a powder, a concentrate, or a combination thereof. In some aspects, the herbal component may be a supercritical extract and/or a hydroalcoholic extract. As used herein, the term "supercritical extraction" refers to a technique in which a hydrophobic compound can be extracted from a sample using a supercritical fluid. The solvating power of a supercritical fluid increases as the pressure and temperature increase above its critical point, thereby creating an effective solvent for separating hydrophobic molecules. In some aspects, the herbal ingredients may be fermented using methods known to those skilled in the art. Particularly suitable fermentation processes are described in U.S. patent 6,806,069, which is incorporated herein by reference in its entirety. The fermented herbal ingredients can be prepared by: the supernatant of the herbal broth is collected and the mixture is dried by any method known in the art, such as spray drying. The culture medium may contain a component selected from the group consisting of: ground organic soy, saccharomyces cerevisiae (organic yeast: active and inactive), organic maltodextrin, organic gum arabic, organic orange peel, organic lemon peel, organic carrot powder, organic alfalfa powder, lactobacillus (lactobacillus) (lactobacillus acidophilus (l.acidophilus), lactobacillus bifidus (l.bifidus), lactobacillus rhamnosus (l.rhamnosus)) and enzymes (inactivated) and combinations thereof. The fermented herbal ingredients may contain all or some of the ingredients from the culture medium.

In some aspects, the composition may comprise from about 0.1% to about 10%, alternatively from about 1% to about 8%, alternatively from about 2% to about 6%, of the one or more herbal ingredients, all percentages being by weight of the composition.

In some aspects, the composition may be substantially free of vitamins, minerals, and/or herbs that inhibit IPA production. In some aspects, the composition may be substantially free of vitamin B2, selenium, and/or vitamin B6. As used herein, "substantially free" is meant to include less than about 0.1%, alternatively less than about 0.05%, alternatively less than about 0.01%, alternatively less than about 0.001%, by weight of the composition.

The composition may be in any dosage form known in the art. Some non-limiting examples of dosage forms may include topical dosage forms, capsules, pills or tablets, soft candies, soft chews, polishing chews, sachets, gels, liquids, bulk powders for reconstitution or beverages prepared from bulk powders, and the like. In some aspects, the compositions can be incorporated into the form of a food and/or beverage. Non-limiting examples of food and beverages into which the composition can be incorporated can include bars, shakes, juices, beverages, frozen food products, fermented food products, and cultured dairy products (such as yogurt, yogurt drinks, cheese, lactic acid bacteria drinks, and kefir).

In some aspects, the composition may be in the form of a dietary supplement or a pharmaceutical composition. As used herein, the term "dietary supplement" refers to a composition of a diet intended to supplement food and water, wherein the diet is sufficient to sustain life.

In some aspects, the composition may comprise the one or more probiotics and the fermentate in an amount effective to provide a health benefit to the subject. In some aspects, the effective amount is a therapeutically effective amount.

In some aspects, the composition can be formulated such that the one or more bacteria present in the composition are replicable once delivered to the target habitat (e.g., intestinal tract). In one non-limiting example, the composition is formulated as a pill, powder, capsule, tablet, enteric-coated dosage form, or package such that the composition has a shelf life of at least about 1, 2, 3, 4, 5, 6,7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35, 36, 37, 38, 39, 40, 41, 42, 43, 44, 45, 46, 47, or 48 months. In some aspects, other components are added to the composition to aid the shelf life of the composition. In some aspects, the one or more bacteria may be formulated in a manner that allows survival in a non-natural environment. For example, bacteria native to the gut may not survive in an oxygen-rich environment. To overcome this limitation, the bacteria may be formulated in a pill or package that reduces or eliminates exposure to oxygen. Other strategies to extend the shelf life of bacteria may include the use of other microorganisms (e.g., if the bacterial consortium comprises a composition whereby one or more strains contribute to the survival of one or more strains).

In some aspects, the compositions may be formulated as a powder, tablet, capsule, enteric-coated dosage form (e.g., for delivery to the ileum/colon), or pill that may be administered to a subject by any suitable route. The lyophilized formulation may be mixed with saline or other solution prior to administration.

In some aspects, the composition is formulated for oral administration. In some aspects, the composition is formulated as a powder, tablet, capsule, enteric-coated dosage form, or pill for oral administration. In some aspects, the composition is formulated for delivery of bacteria to the ileal region of a subject. In some aspects, the composition is formulated for delivery of bacteria to a colonic region (e.g., upper colon) of a subject. In some aspects, the compositions are formulated for delivery of bacteria to the ileum and colon regions of a subject.

Enteric coatings protect the contents of an oral formulation (e.g., tablet or capsule) from gastric acid and provide delivery to the ileum and/or upper colon regions. Non-limiting examples of enteric coatings include pH sensitive polymers (e.g.FS30D), methyl acrylate-methacrylic acid copolymer, cellulose acetate succinate, hydroxypropyl methylcellulose phthalate, hydroxypropyl methylcelluloseAcetate succinate (e.g. hypromellose acetate succinate), polyvinyl acetate phthalate (PVAP), methyl methacrylate-methacrylic acid copolymer, shellac, cellulose acetate trimellitate, sodium alginate, zein, other polymers, fatty acids, waxes, shellac, plastics, and plant fibers. In some aspects, the enteric coating is formed from a pH-sensitive polymer. In some aspects, the enteric coating is comprised ofFS 30D.

In some aspects, the enteric coating can be designed to dissolve at any suitable pH. In some aspects, the enteric coating is designed to dissolve at a pH greater than about pH5.0, or at a pH greater than about pH 6.0, or at a pH greater than about pH 7.0. In some aspects, the enteric coating is designed to dissolve at a pH of greater than about pH5.0 to about pH 7.0. In some aspects, the enteric coating is designed to dissolve at a pH greater than about pH5.0, 5.1, 5.2, 5.3, 5.4, 5.5, 5.6, 5.7, 5.8, 5.9, 6, 6.1, 6.2, 6.3, 6.4, 6.5, 6.6, 6.7, 6.8, 6.9, 7, 7.1, 7.2, 7.3, 7.4, or 7.5.

The formulations provided herein can include the addition of one or more agents to the composition to enhance the stability and/or survival of the microbial preparation. Non-limiting examples of stabilizers may include genetic factors, glycerol, ascorbic acid, skim milk, lactose, tween, alginate, xanthan gum, carrageenan, mannitol, palm oil, poly-L-lysine (POPL), and combinations thereof.

In some aspects, the compositions may be formulated in unit dosage form, i.e., in discrete portions containing a unit dose, or multiple doses, or unit dose subunits. For example, a typical or common suitable or effective dose of the one or more bacteria in humans is from about 1 × E3(1 × E3 ═ 1 × 10^3 ═ 1 × (power of 3 of 10)) to about 1 × E13 Colony Forming Units (CFU). In some cases, a suitable or effective dose is about 1 × E6CFU to about 1 × E11 CFU. In particular instances, a suitable or effective dose is about 1 × E7CFU to about 1 × E10 CFU. In some further aspects, a suitable or effective dose of bacteria can be about 1 × E2CFU, 1 × E3CFU, 1 × E4CFU, 1 × E5CFU, 1 × E6CFU, 1 × E7CFU, 1 × E8CFU, 1 × E9CFU, 1 × E10CFU, 1 × E11CFU, 1 × E12CFU, 1 × E13CFU, 1 × E14CFU, or 1 × E15 CFU.

The composition may be administered once daily. Alternatively, the composition may be taken twice daily, alternatively three times daily, alternatively four times daily. The composition can be taken with meal or on an empty stomach. The composition can be administered in the morning, noon, afternoon, evening or night. The composition may be taken at the same time each day, or the time at which the composition is taken may vary. The user may administer one dosage form/dosage composition, in another example two dosage forms/dosage compositions, in another example three dosage forms/dosage compositions, in another example four dosage forms/dosage compositions, and in another example more than four dosage forms/dosage compositions. In some aspects, the dose is about 0.1 milligrams (mg), about 0.2mg, about 0.3mg, about 0.4mg, about 0.5mg, about 0.6mg, about 0.7mg, about 0.8mg, about 0.9mg, about 1.0mg, about 2.0mg, about 3.0mg, about 4.0mg, about 5.0mg, about 6.0mg, about 7.0mg, about 8.0mg, about 9.0mg, about 10mg, about 15mg, about 20mg, about 25mg, about 30mg, about 35mg, about 40mg, about 45mg, about 50mg, about 55mg, about 60mg, about 65mg, about 70mg, about 75mg, about 80mg, about 85mg, about 90mg, about 95mg, about 100mg, about 200mg, about 300mg, about 400mg, about 500mg, about 600mg, about 700mg, about 800mg, about 900mg, about 1 gram. In some aspects, the dose range is from about 1mg to about 500 mg.

In some aspects, the composition may comprise about 5 to about 10mg of IPA per dose of the composition. It has been found through pharmacokinetic studies that doses of about 5mg to about 10mg IPA can be sufficient to increase IPA levels in serum beyond endogenous baseline values.

In some aspects, the composition may comprise prebiotics, and the dosage of the composition may be from about 50mg to about 5g, alternatively from about 100mg to about 4g, alternatively from about 250mg to about 2 g.

In some aspects, the composition can comprise one or more bacteria in an amount of about 1 × E3 Colony Forming Units (CFU)/gram (g) to about 1 × E13CFU/g, relative to the weight of the composition. In some aspects, the one or more bacteria are present in an amount of about 1 × E5CFU/g to about 1 × E11 CFU/g. In some aspects, the one or more bacteria are present in an amount of about 1 × E6CFU/g to about 1 × E10 CFU/g. In some aspects, the one or more bacteria are present in the composition in an amount of about 1 × E8CFU/g to about 1 × E10 CFU/g. In some aspects, the composition comprises one or more bacteria present in an amount of about 1 × E1CFU/g, about 1 × E2CFU/g, about 1 × E3CFU/g, about 1 × E4CFU/g, about 1 × E5CFU/g, about 1 × E6CFU/g, about 1 × E7CFU/g, about 1 × E8CFU/g, about 1 × E9CFU/g, about 1 × E10CFU/g, about 1 × E11CFU/g, about 1 × E12CFU/g, about 1 × E13CFU/g, about 1 × E14CFU/g, or about 1 × E15 CFU/g.

Containers suitable for use with the compositions described herein include, for example, cans, jars, bottles with shaker lids, grinders, vials, syringes, tubes, pouches, sachets, bags, blister cards, or folds. The container may be formed from a variety of materials including, but not limited to, glass, plastic, polymer, metal, alloy, metal or alloy foil, rubber, cardboard, or paper. The container may also include a sealant, which may be formed of any material suitable for use in the art, such as a resin or polymer. The container may include a moisture barrier and/or an oxygen barrier to further enhance the viability of the probiotic during storage. Moisture barriers and oxygen barriers are known in the pharmaceutical and food industries. Barrier layers suitable for use in the present invention are described in U.S. Pat. No. 6,716,499 to Vadhar, U.S. Pat. No. 6,524,720 to Shah, U.S. Pat. No. 5,792,530 to Bonner et al, and U.S. Pat. No. 4,977,004 to Bettie et al. In addition to or instead of such a barrier layer, the container may include an oxygen scavenger and/or a desiccant/moisture absorbing compound. Suitable oxygen scavengers and desiccants are known in the art, for example, U.S. Pat. No. 6,746,622 to Yan et al, U.S. Pat. No. 6,387,461 to Ebner et al, U.S. Pat. No. 6,228,284 to Ebner et al, and U.S. Pat. No. 6,130,263 to Hekal.

Also described herein are methods of providing one or more health benefits comprising orally administering to a user a composition of the present invention. In some aspects, the one or more health benefits may be selected from promoting brain health; promoting healthy aging of brain; promoting emotional health through brain health; delivering antioxidant nutrients to the brain; managing oxidative stress in the brain; attenuating and/or maintaining oxidative stress or total antioxidant capacity in the brain; protecting neurons by delivering an antioxidant; and any combination of the above benefits. In some aspects, the one or more health benefits may be selected from promoting brain health; promoting healthy aging of brain; delivering antioxidant nutrients to the brain; managing oxidative stress in the brain; and any combination of the above benefits.

Also described herein are methods of increasing IPA in the gastrointestinal tract and/or serum of a subject in need thereof, comprising administering to the subject an effective amount of a composition described herein.

Also described herein are methods for optimizing the gut-brain axis of a healthy nervous system by reducing neuroinflammation and neurodegeneration in a subject in need thereof, comprising administering to the subject an effective amount of a composition described herein.

Also described herein are methods for treating, ameliorating, or preventing a disease in a subject having or at risk of having the disease, the method comprising administering to the subject an effective amount of a composition described herein. In some aspects, the disease can be an intestinal disease, a metabolic disorder, an inflammatory condition, or an immune disorder. In some aspects, the disease can be metabolic syndrome, insulin resistance, insulin sensitivity, prediabetes, diabetes, anxiety, depression, autism, hypertension, irritable bowel syndrome, metabolic abnormalities, stress-related disorders, neurological diseases (such as parkinson's disease), Inflammatory Bowel Disease (IBD), crohn's disease, cardiac disease, or neurological disorders (such as multiple sclerosis).

Examples and data

The following data and examples are provided to help illustrate the invention described herein. The exemplified compositions are given for illustrative purposes only and are not to be construed as limiting the invention, as many variations are possible without departing from the spirit and scope of the invention. All parts, percentages and ratios herein are by weight unless otherwise indicated.

Production of IPA and its derivatives

The fermentation medium was first prepared according to the formula in table 2.

Table 2: fermentation Medium 1

Composition (I)	amount/1L
		Resazurin (0.01% w/v stock solution)	1.00ml
K2HPO4	2.00g
		KH2PO4	2.00g
MgCl26H2O	0.20g
		(NH4)2SO4	5.00g
NaHCO3 (10% w/v stock solution)	25.00mL
		Cysteine hydrochloride (5% w/v stock solution)	10.00mL
L-glycine	0.0751g
		L-valine	0.1172g
L-leucine	0.1312g
		L-isoleucine	0.1312g
L-methionine	0.1492g
		L-histidine	0.1552g
L-arginine	0.1742g
		L-phenylalanine	0.1652g
L-tyrosine	0.1812g
		L-tryptophan	0.2042g
Solution of trace elements1	10.00mL
		Vitamin solution2	10.00mL
Softened water	Proper amount of

¹Trace mineral supplementMD-TMS^TM(commercially available from ATCC (Manassas, Va.).

²Vitamin supplementMD-VS^TM(commercially available from ATCC (Manassas, Va.).

All ingredients except the amino acid, trace element solution and vitamin solution were mixed and heated to 121 ℃ for 30-40 minutes with stirring. The mixture is allowed to cool for about 10-20 minutes, and then the amino acid, trace element solution, and vitamin solution are added. Prior to the addition of the amino acid, an amino acid solution was prepared by dissolving all the amino acids listed in table 2 in a 100mL aliquot of the cooling medium and filter sterilized.

Clostridium sporogenes ATCC15579(C. sponogenes) was grown anaerobically at 36 ℃ for 24 hours in 10mL peptone yeast glucose ("PYG") medium (commercially available from Sigma-Aldrich (St. Louis, Mo.). A10 mL aliquot of the 24 hour culture (approximately 1 × E8CFU/mL) was centrifuged at 10,0000 × g for 5 minutes. The supernatant was removed and the spore-forming clostridium pellet was resuspended in 10mL saline to wash the bacteria. The samples were then centrifuged at 10,000 Xg for 5 minutes. The supernatant was removed and the spore-forming clostridium pellet was resuspended in 10mL saline to form an inoculum preparation.

100 μ l inoculum was anaerobically transferred to 10mL fermentation medium in duplicate. After preparation, the tubes were transferred to a 36 ℃ cabinet in an anaerobic chamber for 24-28 hours. After incubation, the tubes were removed from the chamber and centrifuged at 8,000 × g for 10 minutes. The supernatant was removed and filtered through a 0.2 μm syringe filter into a sterile glass tube.

Then, the supernatant was collectedA 3mL aliquot of the solution was transferred to a lyophilization vial. Food-grade 5%100 starch (commercially available from Ingredion (Westchester, IL)) was added to the vials. The samples were then lyophilized. First, in the heat treatment step, the vial was held at 20 ℃ for 30 minutes, then at 0 ℃ for 80 minutes, and then at-25 ℃ for 60 minutes. Freezing was carried out at-25 ℃ (-50 ℃ C. condenser) and under vacuum of 200 mTorr. Next, in the drying step, the vial was held at-25 ℃ and 200mTorr for a total of about 1800 to about 1830 minutes, then the temperature was raised to 4 ℃ and the vial was held at 4 ℃ and 200mTorr for 60 minutes. After lyophilization, the fermentation broth powder was subjected to IPA analytical measurement according to IPA measurement method described below. 150 μ M pure IPA in fermentation medium was used as a control. The results are in table 3 below.

TABLE 3.

Components	Amount (mg/g fermented product)	Standard deviation of
			Indole-3-propionic acid	0.308	0.011
Indole-3-propenoic acid	0.002	0.000
			Tryptophan	0.492	0.020
Indole-3-lactic acid	0.058	0.002

It was found that IPA and its derivatives can be produced by bacterial fermentation in defined fermentation media and lyophilization of the supernatant. IPA, indole-3 acrylic acid, indole-3-lactic acid and tryptophan were detected in the fermentation powder. It was found that starch did not inhibit IPA recovery.

Fermentation medium

After demonstrating the concept that IPA and other indole derivatives can be produced by bacterial fermentation (table 3), different fermentation media were tested to assess whether levels of IPA and other derivatives production could be increased. Fermentation medium a contained the same formulation as medium 1 with added glucose, fermentation medium B was the same formulation as medium a but contained tryptophan as the only amino acid, and fermentation medium C contained the same formulation as medium 1 but with 10-fold amino acids. Fermentation media A, B and C were prepared according to the recipe in Table 4. These media were compared to fermentation medium 1 described in table 2 above.

Table 4: fermentation medium

Composition (I)	Medium A	Medium B	Medium C
				Resazurin (0.01% w/v stock solution)	1.00mL	1.00mL	1.00mL
K2HPO4	2.00g	2.00g	2.00g
				KH2PO4	2.00g	2.00g	2.00g
MgCl26H2O	0.20g	0.20g	0.20g
				(NH4)2SO4	5.00g	5.00g	5.00g
NaHCO3 (10% w/v stock solution)	25.00mL	25.00mL	25.00mL
				Cysteine hydrochloride (5% w/v stock solution)	10.00mL	10.00mL	10.00mL
L-glycine	0.0751g	0	0.7510g
				L-valine	0.1172g	0	1.1720g
L-leucine	0.1312g	0	1.3120g
				L-isoleucine	0.1312g	0	1.3120g
L-methionine	0.1492g	0	1.4920g
				L-histidine	0.1552g	0	1.5520g
L-arginine	0.1742g	0	1.7420g
				L-phenylalanine	0.1652g	0	1.6520g
L-tyrosine	0.1812g	0	1.8120g
				L-tryptophan	0.2042g	0.2042g	2.0423g
Solution of trace elements1	10.00mL	10.00mL	10.00mL
				Vitamin solution2	10.00mL	10.00mL	10.00mL
Glucose stock solution (500mM)	40mL	40.00mL	0
				Softened water	Proper amount of	Proper amount of	Proper amount of

¹Trace oreSubstance supplementMD-TMS^TM(commercially available from ATCC (Manassas, Va.).

²Vitamin supplementMD-VS^TM(commercially available from ATCC (Manassas, Va.).

All ingredients except the amino acid, glucose stock solution, trace element solution and vitamin solution were mixed and heated to 121 ℃ for 30-40 minutes with stirring. The mixture is allowed to cool for about 10-20 minutes, and then the amino acid, glucose stock solution, trace element solution, and vitamin solution are added. Prior to the addition of the amino acids, amino acid solutions were prepared by dissolving all the amino acids listed in table 4 in 100mL aliquots of cooling medium and filter-sterilizing.

Clostridium sporogenes ATCC15579(C. sponogenes) was grown anaerobically at 36 ℃ for 24 hours in 10mL peptone yeast glucose ("PYG") medium (commercially available from Sigma-Aldrich (St. Louis, Mo.). A10 mL aliquot of the 24 hour culture (approximately 1 × E8CFU/mL) was centrifuged at 10,0000 × g for 5 minutes. The supernatant was removed and the spore-forming clostridium pellet was resuspended in 10mL saline to wash the bacteria. The samples were then centrifuged at 10,000 Xg for 5 minutes. The supernatant was removed and the spore-forming clostridium pellet was resuspended in 10mL saline to form an inoculum preparation.

100 μ l inoculum was anaerobically transferred to 10mL fermentation medium in duplicate. After preparation, the tubes were transferred to a 36 ℃ cabinet in an anaerobic chamber for 24-28 hours. After incubation, the tubes were removed from the chamber and centrifuged at 8,000 × g for 10 minutes. The supernatant was removed and filtered through a 0.2 μm syringe filter into a sterile glass tube. The supernatant was then subjected to IPA analytical measurement according to the IPA measurement method described below. The results are in table 5 below.

TABLE 5.

It was surprisingly found that the addition of glucose to the growth medium (fermentation medium a) significantly improved IPA yield compared to the growth medium without glucose (fermentation medium 1). Growth medium containing glucose and tryptophan as the only amino acids (fermentation medium B) reduced IPA and derivative yields. It was also found that increasing the amino acid concentration (fermentation medium C) significantly reduced IPA compared to fermentation medium 1.

Examples

Composition (I)	Example 6	Example 7	Example 8	Example 9
						By weight%	By weight%	By weight%	By weight%
Fermented product	60.0	65.0	85.0	80.0
					Microcrystalline cellulose	30.0	9.0	14.0	10.0
Maltodextrin	9.0	25.0	0	9.0
					Magnesium stearate	1.0	1.0	1.0	1.0

Examples 1-9 can be prepared according to the following procedure.

Preparation of fermentation Medium

The fermentation medium 1 can be prepared by mixing all the ingredients listed in table 2 except for the amino acid, trace element solution and vitamin solution. The medium can be sterilized by heating to 121 ℃ for 30-40 minutes under stirring. The medium may then be cooled for about 10-20 minutes before the amino acids, trace element solution and vitamin solution are added. Prior to addition of the amino acid, an amino acid solution can be prepared by dissolving the amino acid in a 100mL aliquot of the cooling medium and filter sterilizing. The medium can then be handled and stored under sterile conditions until use.

Alternatively, fermentates of examples 1-9 may be prepared using fermentation medium A. Fermentation medium a can be prepared by mixing all the ingredients listed in table 4 except for the amino acid, glucose stock solution, trace element solution and vitamin solution. The medium can be sterilized by heating to 121 ℃ for 30-40 minutes under stirring. The medium may then be cooled for about 10-20 minutes, and then the amino acids, glucose stock solution, trace element solution, and vitamin solution are added. Prior to addition of the amino acid, an amino acid solution can be prepared by dissolving the amino acid in a 100mL aliquot of the cooling medium and filter sterilizing. The medium can then be handled and stored under sterile conditions until use.

Bacterial preparation

Clostridium sporulatum ATCC15579(c. sponogenes) was grown anaerobically at 36 ℃ in peptone yeast glucose ("PYG") medium, commercially available from Sigma-Aldrich (st. louis, MO). An aliquot of the 24 hour culture (approximately 1xE8CFU/mL) can be centrifuged to produce a pellet. The supernatant can be removed and the spore-forming clostridium pellet can be resuspended in saline to wash the bacteria. The sample may then be centrifuged again. The supernatant can be removed and the spore-forming clostridium pellet resuspended in saline to form an inoculum preparation.

Preparation of fermentation products

The spore-forming Clostridium inoculum preparation can be anaerobically transferred to a fermentation medium to form a bacterial solution. The fermentation can be carried out in a suitably sized fermenter at 36 ℃ until maximum growth is achieved.

To prepare a ferment in which the bacteria are removed, the fermented bacterial solution may be centrifuged to remove the bacteria and the supernatant may be collected. Optionally, the supernatant may be passed through a combination of reverse osmosis, tray drying, microfiltration and nanofiltration to reduce the water content prior to drying. The resulting concentrated liquid may be mixed with mannitol and starch as dehydrating agents. The supernatant may then be spray dried to produce a powdered fermentation containing IPA. Alternatively, the supernatant may be sprayed into liquid nitrogen to produce frozen beads. The frozen beads may be dried by lyophilization and then ground to produce a powdered fermentation containing IPA.

To prepare a fermentation containing bacteria, the fermented bacterial solution may be inactivated by heating or by treatment with proteolytic enzymes. The resulting solution may be mixed with mannitol and starch as dehydrating agents. The solution may then be spray dried to produce a powdered fermentation containing IPA. Alternatively, the solution can be sprayed into liquid nitrogen to produce frozen beads. The frozen beads may be dried by lyophilization and then ground to produce a powdered fermentation containing IPA.

The powdered fermentation containing IPA may be weighed and loaded into a powder blender such as a properly sized "V" blender. Microcrystalline cellulose (USP) and maltodextrin (USP), if present in the formulation, may be separately screened, weighed and loaded into a powder blender. Blending may be performed until a homogeneous blend of fermentate and excipients is obtained, typically mixing may be performed for 100 and 500 revolutions. Magnesium stearate (USP) may be sieved and loaded into a powder blender. Magnesium stearate can be incorporated into the ferment powder by blending, typically less than 100 turns.

The final blend can be loaded into a powder feed hopper of a rotary encapsulator equipped with a capsule polisher. Gelatin or hydroxypropyl methylcellulose capsules may be loaded into a capsule hopper. The capsules can be filled with the final blend and polished. Alternatively, the final blend can be loaded into a pouch filler equipped with a pouch sealer, and can be loaded with pouch material. The pouch can be filled and sealed.

IPA measuring method

Biological samples were subjected to protein precipitation by adding 300 μ L MeOH to 100 μ L samples. Vortex the sample and use a bench top centrifuge such as a Beckman CoulterX15R (rotor SX4750A) or equivalent instrument was centrifuged at 3000rpm for 10 minutes to pellet the protein and other precipitates. mu.L of the supernatant was transferred to a 96-well deep-well plate along with 30. mu.L of 10ng/mL indole-3-propionic acid-2, 2-d2(IPA-d2) and 150. mu.L water. For samples in other matrices (including but not limited to bacterial cell culture filtrate and fermentates), samples were subjected to 1000-fold dilution with 10% aqueous MeOH. 30 μ L of 10ng/mL IPA-d2 was added to 300 μ L of the diluted sample. IPA and IPA-d2 in the separated/diluted samples were subjected to gradient High Performance Liquid Chromatography (HPLC) analysis on a Waters Atlantis T3 column (from Waters Corp. (Milford, MA)) or equivalent column (2.1mm x 50mm, 3 μm particles), with 0.1% aqueous formic acid as mobile phase a and 0.1% acetonitrile solution of formic acid as mobile phase B. Detection and quantitation was achieved by tandem mass spectrometry operating under Multiple Reaction Monitoring (MRM) MS/MS conditions (m/z 190.1 → 130.0 for IPA and m/z 192.1 → 130.0 for IPA-d 2). A regression curve was constructed by plotting the response (peak area IPA/peak area IPA-d2) of each standard versus concentration using IPA calibration Standards (STD) prepared in 10% MeOH in water. By two (1/x)²) The regression curve determines the concentration of IPA in the sample by interpolation.

Combination of

1. A method of producing indole-3-propionic acid and other indole derivatives, comprising: adding a bacterium having a nucleic acid sequence with at least 80% homology to the nucleic acid sequence of SEQ ID NO. 1 to a liquid fermentation medium to form a bacterial solution; fermenting the bacterial solution under anaerobic conditions at 36 ℃; adding a dehydrating agent; and dehydrating to obtain a fermentation broth powder comprising indole-3-propionic acid and other indole derivatives.

2. The method of paragraph a, further comprising centrifuging the fermented bacterial solution to form a supernatant and a bacterial pellet; taking out the supernatant; and adding a dehydrating agent to the supernatant.

3. The method of paragraph a or B, wherein the fermentate powder comprises 0.1 to 20mg/g indole-3-propionic acid.

4. The method of any of paragraphs a to C, wherein the fermentate powder comprises from 0.1 to 20mg/g of other indole derivatives.

5. The method of any of paragraphs a-D, wherein the fermentation medium comprises water, an amino acid composition, salts, minerals, and optionally carbohydrates.

6. The method of any of paragraphs a-E, further comprising homogenizing prior to the dehydrating step.

7. The method of any of paragraphs a to F, wherein the dehydrating step is spray drying.

8. The method of any of paragraphs a to G, wherein the dehydrating step is freeze-drying.

9. A composition, comprising: a ferment comprising indole-3-propionic acid of bacterial origin; and excipients, carriers and/or diluents.

10. The composition of paragraph I, wherein the composition comprises 0.01 to 10% indole-3-propionic acid, by weight of the composition.

11. The composition of paragraph I or J, wherein the composition further comprises an indole derivative selected from the group consisting of indole-3-acetic acid, indole-3-acrylic acid, indole-3-lactic acid, and combinations thereof.

12. The composition of any one of paragraphs I to K, wherein the composition further comprises one or more bacteria selected from the group consisting of: bifidobacterium bifidum (Bifidobacterium bifidum), Bifidobacterium breve (Bifidobacterium breve), Bifidobacterium infantis (Bifidobacterium infantis), Bifidobacterium longum (Bifidobacterium longum), Streptococcus cremoris (Streptococcus cremoris), Streptococcus diacetylactis (Streptococcus diacetobacter), Streptococcus lactis (Streptococcus lactis), Streptococcus thermophilus (Streptococcus thermophilus), Lactobacillus acidophilus (Lactobacillus acidophilus), Lactobacillus bifidus (Lactobacillus bifidus), Lactobacillus bulgaricus (Lactobacillus bulgaricus), Lactobacillus casei (Lactobacillus casei), Lactobacillus delbrueckii (Lactobacillus delbrueckii), Lactobacillus crispatus (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus casei), Lactobacillus casei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei (Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei (Lactobacillus), Lactobacillus paracasei, Lactobacillus), Lactobacillus paracasei, Lactobacillus (Lactobacillus), Lactobacillus (Lactobacillus paracasei (Lactobacillus), Lactobacillus (Lactobacillus paracasei, Lactobacillus), Lactobacillus (Lactobacillus), Lactobacillus paracasei, Lactobacillus), Lactobacillus (, Lactobacillus salivarius, Lactobacillus thermophilus, Lactococcus lactis, Clostridium sporogenes, Streptococcus anaerobiosis, Clostridium cadaveris, Clostridium bold, and combinations thereof.

13. The composition of paragraph L, comprising from 1xe 3 Colony Forming Units (CFU) to 1xe 11CFU of the one or more bacteria.

14. The composition of any of paragraphs I-M, wherein the fermentate further comprises tryptophan.

15. A method of promoting brain health, comprising administering to an individual in need thereof a composition according to paragraph I.

The dimensions and values disclosed herein are not to be understood as being strictly limited to the exact numerical values recited. Rather, unless otherwise specified, each such dimension is intended to mean both the recited value and a functionally equivalent range surrounding that value. For example, a dimension disclosed as "40 mm" is intended to mean "about 40 mm".

The values disclosed herein as being "at the end of a range" should not be construed as being strictly limited to the exact numerical values recited. Conversely, unless otherwise specified, each numerical range is intended to mean both the recited value and any real number within the range, including integers. For example, a range disclosed as "1 to 10" is intended to mean "1, 2, 3, 4, 5, 6,7, 8, 9, and 10", and a range disclosed as "1 to 2" is intended to mean "1.1, 1.2, 1.3, 1.4, 1.5, 1.6, 1.7, 1.8, 1.9, and 2".

Each document cited herein, including any cross referenced or related patent or patent application and any patent application or patent to which this application claims priority or its benefits, is hereby incorporated by reference in its entirety unless expressly excluded or otherwise limited. The citation of any document is not an admission that it is prior art with any disclosure of the invention or the claims herein or that it alone, or in combination with any one or more of the references, teaches, suggests or discloses any such invention. Further, to the extent that any meaning or definition of a term in this document conflicts with any meaning or definition of the same term in a document incorporated by reference, the meaning or definition assigned to that term in this document shall govern.

While particular embodiments of the present invention have been illustrated and described, it would be obvious to those skilled in the art that various other changes and modifications can be made without departing from the spirit and scope of the invention. It is therefore intended to cover in the appended claims all such changes and modifications that are within the scope of this invention.