WO2008140744A1 - Particulate-soluble glucan preparation - Google Patents

Particulate-soluble glucan preparation Download PDF

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Publication number
WO2008140744A1
WO2008140744A1 PCT/US2008/005914 US2008005914W WO2008140744A1 WO 2008140744 A1 WO2008140744 A1 WO 2008140744A1 US 2008005914 W US2008005914 W US 2008005914W WO 2008140744 A1 WO2008140744 A1 WO 2008140744A1
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WO
WIPO (PCT)
Prior art keywords
glucan
particulate
soluble
composition
solution
Prior art date
Application number
PCT/US2008/005914
Other languages
French (fr)
Inventor
Donald J. Cox
Original Assignee
Biopolymer Engineering, Inc. Dba Biothera, Inc.
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Biopolymer Engineering, Inc. Dba Biothera, Inc. filed Critical Biopolymer Engineering, Inc. Dba Biothera, Inc.
Priority to EP08754267.6A priority Critical patent/EP2155000A4/en
Priority to BRPI0811274-6A2A priority patent/BRPI0811274A2/en
Priority to UAA200912721A priority patent/UA101617C2/en
Priority to CA2690918A priority patent/CA2690918C/en
Priority to JP2010507462A priority patent/JP5562837B2/en
Priority to CN200880014957.4A priority patent/CN101711112B/en
Priority to MX2009012070A priority patent/MX2009012070A/en
Priority to AU2008251847A priority patent/AU2008251847B2/en
Priority to KR1020147023009A priority patent/KR101665216B1/en
Publication of WO2008140744A1 publication Critical patent/WO2008140744A1/en

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    • C—CHEMISTRY; METALLURGY
    • C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08B—POLYSACCHARIDES; DERIVATIVES THEREOF
    • C08B37/00—Preparation of polysaccharides not provided for in groups C08B1/00 - C08B35/00; Derivatives thereof
    • C08B37/0006—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid
    • C08B37/0024—Homoglycans, i.e. polysaccharides having a main chain consisting of one single sugar, e.g. colominic acid beta-D-Glucans; (beta-1,3)-D-Glucans, e.g. paramylon, coriolan, sclerotan, pachyman, callose, scleroglucan, schizophyllan, laminaran, lentinan or curdlan; (beta-1,6)-D-Glucans, e.g. pustulan; (beta-1,4)-D-Glucans; (beta-1,3)(beta-1,4)-D-Glucans, e.g. lichenan; Derivatives thereof
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/385—Concentrates of non-alcoholic beverages
    • A23L2/39—Dry compositions
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/38—Other non-alcoholic beverages
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L2/00—Non-alcoholic beverages; Dry compositions or concentrates therefor; Their preparation
    • A23L2/52—Adding ingredients
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L29/00—Foods or foodstuffs containing additives; Preparation or treatment thereof
    • A23L29/20—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents
    • A23L29/269—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of microbial origin, e.g. xanthan or dextran
    • A23L29/271—Curdlan; beta-1-3 glucan; Polysaccharides produced by agrobacterium or alcaligenes
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
    • A23L33/20—Reducing nutritive value; Dietetic products with reduced nutritive value
    • A23L33/21—Addition of substantially indigestible substances, e.g. dietary fibres
    • A23L33/22—Comminuted fibrous parts of plants, e.g. bagasse or pulp
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L5/00—Preparation or treatment of foods or foodstuffs, in general; Food or foodstuffs obtained thereby; Materials therefor
    • A23L5/51—Concentration
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/20—Agglomerating; Granulating; Tabletting
    • A23P10/22—Agglomeration or granulation with pulverisation of solid particles, e.g. in a free-falling curtain
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23P—SHAPING OR WORKING OF FOODSTUFFS, NOT FULLY COVERED BY A SINGLE OTHER SUBCLASS
    • A23P10/00—Shaping or working of foodstuffs characterised by the products
    • A23P10/40—Shaping or working of foodstuffs characterised by the products free-flowing powder or instant powder, i.e. powder which is reconstituted rapidly when liquid is added
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K31/00—Medicinal preparations containing organic active ingredients
    • A61K31/70—Carbohydrates; Sugars; Derivatives thereof
    • A61K31/715—Polysaccharides, i.e. having more than five saccharide radicals attached to each other by glycosidic linkages; Derivatives thereof, e.g. ethers, esters
    • A61K31/716—Glucans
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P31/00—Antiinfectives, i.e. antibiotics, antiseptics, chemotherapeutics
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P35/00—Antineoplastic agents
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P37/00—Drugs for immunological or allergic disorders
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P43/00—Drugs for specific purposes, not provided for in groups A61P1/00-A61P41/00
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H1/00—Processes for the preparation of sugar derivatives
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07H—SUGARS; DERIVATIVES THEREOF; NUCLEOSIDES; NUCLEOTIDES; NUCLEIC ACIDS
    • C07H3/00—Compounds containing only hydrogen atoms and saccharide radicals having only carbon, hydrogen, and oxygen atoms
    • C07H3/04—Disaccharides
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
    • A23V2250/00—Food ingredients
    • A23V2250/50—Polysaccharides, gums
    • A23V2250/502—Gums
    • A23V2250/5034—Beta-Glucan

Definitions

  • the present invention relates to a particulate-soluble ⁇ -glucan. More particularly, the present invention relates to an improved method and composition of particulate-soluble ⁇ -glucan.
  • Glucans are generally described as polymers of glucose and are derived from yeast, bacteria, fungi and plants such as oats and barley. Glucans containing a ⁇ (l-3)- linked glucopyranose backbone are known to have biological activity, specifically, they have been shown to modulate the immune system and more recently to induce hematopoietic stem and progenitor cell (HSPC) mobilization.
  • HSPC hematopoietic stem and progenitor cell
  • Particulate ⁇ -glucan is solubilized in an acidic solution at elevated temperature and pressure.
  • the resulting soluble ⁇ -glucan may be further clarified and purified using, for example, centrifugation and/or chromatographic techniques.
  • the resulting product even when comprised of high molecular weight glucans, can be dried to a powder and subsequently re-solubilized.
  • FIGS. 1-4 are RI traces and data transformations graphs of particulate-soluble ⁇ -glucan samples.
  • FIG. 5 is a graphic representation of TNFa production induced by various ⁇ - glucans. DETAILED DESCRIPTION OF THE INVENTION
  • the starting material used in the present invention is particulate, or insoluble, ⁇ -glucan, produced by any method.
  • the particulate ⁇ -glucan starting material may range in size from whole glucan particles down to submicron-sized particles.
  • the level of impurities within the starting material may also vary. However, as the level of impurities within the starting material increases, the amount of soluble glucan recovered decreases.
  • suitable starting material is WGP 3-6 ® from Biothera.
  • any of a number of source of b-glucan can be used for the present invention.
  • sources are yeast, barely, oats, mushrooms and other fungi, etc.
  • the particulate ⁇ -glucan is treated with acid under pressure and elevated temperature to produce soluble ⁇ -glucan.
  • pelleted, particulate ⁇ — glucan is resuspended and mixed in a sealable reaction vessel in a buffer solution and brought to pH 3.6. Buffer reagents are added such that every liter, total volume, of the final suspension mixture contains about 0.61 g sodium acetate, 5.24 ml glacial acetic acid and 430 g pelleted, particulate ⁇ -glucan.
  • the vessel is purged with nitrogen to remove oxygen and increase the pressure within the reaction vessel.
  • the pressure inside the vessel is brought to 35 PSI, and the suspension is heated to about 135°C for up to about 5.5 hours. It was found that under these conditions the ⁇ -glucan will solubilize. As the temperature decreases from 135°C, the amount of solubilization also decreases.
  • Hazardous chemicals that have previously been used include, for example, flammable VOCs such as ether and ethanol, very strong acids such as formic acid and sulphuric acid and caustic solutions of very high pH.
  • the present process is not only safer, but, by reducing the number of different chemicals used and the number of steps involved, is more economical.
  • An additional advantage of the present process is that the length of the above treatment controls the molecular weight of the resulting particulate-soluble ⁇ -glucan.
  • pill-soluble ⁇ -glucan may be in any of the soluble, particulate or re-solubilized forms.
  • the length of treatment time is inversely related to the resulting molecular weight size. In other words, as the treatment time increases, the resulting average molecular weight of the particulate-soluble ⁇ -glucan decreases. This principal is illustrated in the following.
  • N is the number of molecules of molecular weight M 1 .
  • FIG. 1 includes panels A and B.
  • Panel A is a refractive index (RI) trace of the 60 min. sample.
  • panel B a section of the data generated in panel A was transformed and plotted on the graph shown.
  • Curve 10 represents the transformed raw data.
  • Curve 12 represents the cumulative percentage of specific molecular weights. Molecular weight was determined by a standard curve generated with dextran of known size (data not shown).
  • FIG. 2 Data generated from the 90 min. sample is shown in FIG. 2.
  • FIG. 3 Data generated from the 120 min. sample is shown in FIG. 3. Panel A and panel B, with curves 18 and 20, correspond to the panels A and B of FIG. 1.
  • FIG. 4 Data generated from the 240 min. sample is shown in FIG. 4.
  • particulate-soluble glucan may be more useful for specific applications. For example, when applied topically, molecules of smaller molecular weight may better penetrate skin. Larger molecular weight molecules, on the other hand, may be better suited for oral administration. Therefore, the ability to easily control the average size of the glucan molecules offers a significant competitive advantage.
  • the exact duration of heat treatment is typically determined experimentally by sampling reactor contents. Various tests may be performed such as gel permeation chromatography (GPC) analyses. The process maximizes the yield of particulate-soluble material that meets specific specification profiles and impurity levels. Once the ⁇ -glucan is solubilized, the mixture is cooled to stop the reaction.
  • GPC gel permeation chromatography
  • the particulate-soluble ⁇ -glucan may be washed and utilized at this point, however, for pharmaceutical applications further purification is typically performed. Any combination of one or more of the following steps may be used to further purify and/or clarify the particulate-soluble ⁇ -glucan. Other means known in the art may also be used if desired. Suitable means include, for example, centrifugation or continuous-flow centrifugation, which eliminates a significant amount of lipid impurities.
  • the inclusion of lipids within the particulate-soluble ⁇ -glucan may increase its effectiveness against certain infectious diseases or enhancing the immune system.
  • the process presented here provides a means to effectively control and vary the amount of lipid in the particulate-soluble ⁇ -glucan composition.
  • the particulate-soluble ⁇ -glucan may be filtered.
  • the material is filtered through a 0.2 ⁇ m filter.
  • Chromatography may also be used for purification.
  • the particulate-soluble ⁇ -glucan may be conditioned at some point in preparation for chromatography. For example, if a chromatographic step includes hydrophobic interaction chromatography (HIC), the particulate-soluble ⁇ -glucan can be conditioned to the appropriate conductivity and pH with a solution of ammonium sulphate and sodium acetate. A suitable solution is 3.0 M ammonium sulfate, 0.1 M sodium acetate, which is used to adjust the pH to 5.5.
  • HIC hydrophobic interaction chromatography
  • Another chromatographic step that may be utilized is gel permeation chromatography (GPC). Multiple chromatography cycles may be needed to ensure that the load does not exceed the capacity of the column.
  • GPC gel permeation chromatography
  • the particulate-soluble ⁇ -glucan is purified and ready for use.
  • the particulate-soluble ⁇ -glucan that is generally collected has an average molecular weight > 1,000,000 Da, with a high polydispersity.
  • An advantage of this particulate-soluble ⁇ - glucan product, especially in the high molecular weight ranges such as over a million Daltons (Da) is that the product can be spray dried to a powder form and then subsequently re-solubilized in solutions of pH about 5 and higher — essentially from weakly acidic to strongly basic.
  • re-solubilization occurs at temperatures as low as about room temperature ( ⁇ 25°C). Depending on the final concentration after re- solubilization and the solvent used, the time and temperature requirements for re- solubilization will vary.
  • the product's ability to re-solubilize makes it ideal for creating an instantized form of ⁇ -glucan suitable for, for example, instant drink powders.
  • particulate- soluble ⁇ -glucan in dry form is re-wet to achieve a moisture content of about 9%-12%, which forms an agglomerate.
  • a surfactant, such as lecithin is added to the agglomerate via a two-fluid nozzle.
  • the concentration of surfactant will vary depending on the surfactant used and the conditions and solvent into which the product will be finally dissolved.
  • the agglomerate is then run through three stages of a fluid bed drier. The first stage heats the product, the second stage conditions the product and the third stage cools the product. The resulting product is sifted to form the instantized product.
  • a second dry-form soluble ingredient such as table sugar or salt (NaCl).
  • a second dry-form soluble ingredient such as table sugar or salt (NaCl).
  • 200 mg of powdered, particulate-soluble ⁇ -glucan and about 0.5 to about 1.0 g of sucrose crystals were mixed and ground in a mortor bowl for about 2-3 minutes. The mixture was added to 500 mis of room temperature water and shook vigorously. The particulate-soluble ⁇ - glucan re-solubilized. An identical experiment was carried out with NaCl with the same result.
  • the particulate-soluble ⁇ -glucan product may be used for any of a number of applications.
  • Particulate-soluble ⁇ -glucan is ideal for use as a nutritional supplement, a food ingredient, a cosmetic ingredient and a pharmaceutical product for use in humans and agricultural/companion/exotic animals.
  • Typical foods in which the dry or wet forms of particulate-soluble ⁇ -glucan may be added include, for example, cereals and cereal products, baked goods and baking mixes, beverages and beverage bases, dairy product analogs such as soy milk, milk and milk products, plant protein products, processed fruits and fruit juices, soft candy, soup and soup mixes, yogurt, bottled water and drinks, nutrition bars, etc.
  • dairy product analogs such as soy milk, milk and milk products, plant protein products, processed fruits and fruit juices, soft candy, soup and soup mixes, yogurt, bottled water and drinks, nutrition bars, etc.
  • Various masking agents and other additives may be added to improve the flavor and texture if necessary.
  • the particulate-soluble ⁇ -glucan in its liquid form, can be used to make edible films.
  • a thin layer of liquid product is dried by any of a number of means known in the art.
  • Additives may be added to the liquid product to create films of various textures or to make them more or less pliable.
  • the films are useful as carriers for pharmaceutical or supplement products.
  • various masking agents can be added to improve the flavor of the film.
  • the particulate-soluble ⁇ -glucan product may also be more efficacious than prior art particulate ⁇ -glucan.
  • the product may be more effective against infectious diseases or cancer. Increased efficacy may be in terms of better uptake, better immune system enhancement, decreased dosing regiments, etc.
  • in vitro studies showed that the particulate-soluble ⁇ -glucan does not induce TNF ⁇ from human peripheral blood mononuclear cells (PBMC) at concentrations up to 300 ⁇ g/mL.
  • PBMC peripheral blood mononuclear cells
  • human PBMC were cultured in cRPMI medium containing 5% heat-inactivated FCS. Cells were stimulated with various beta glucans (all endotoxin free), TLR7/8 agonist, or vehicle.
  • the beta glucans were used at various concentrations. After overnight incubation at 37 0 C, 5% CO 2 , cell-free supernatants were collected, stored at -2O 0 C until cytokine analysis by ELISA. The results from three replicates are shown in FIG. 5. As evidenced by the graph, whole glucan particles stimulate TNF ⁇ production, while the particulate-soluble product does not. Because TNF ⁇ is a major cytokine involved in an inflammatory response, the particulate-soluble product is not expected to induce an inflammatory response.

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Abstract

Particulate β-glucan is solubilized at elevated pressure and temperature to form particulate-soluble β-glucan. The particulate-soluble beta-glucan is capable of being dried to a powder form and subsequently re-solubilized.

Description

PARTICULATE-SOLUBLE GLUCAN PREPARATION
BACKGROUND OF THE INVENTION
This application claims the benefit of U.S. Provisional Application No. 60/916,690, entitled SOLUBLE GLUCAN PREPARATION, filed May 8, 2007.
The present invention relates to a particulate-soluble β-glucan. More particularly, the present invention relates to an improved method and composition of particulate-soluble β-glucan.
Glucans are generally described as polymers of glucose and are derived from yeast, bacteria, fungi and plants such as oats and barley. Glucans containing a β(l-3)- linked glucopyranose backbone are known to have biological activity, specifically, they have been shown to modulate the immune system and more recently to induce hematopoietic stem and progenitor cell (HSPC) mobilization.
In the past, a high quality soluble β-glucan was expensive to produce. The expense made it cost prohibitive as a nutritional supplement or food ingredient, for example. Therefore, there is a need for an improved soluble β-glucan.
SUMMARY OF THE INVENTION
Particulate β-glucan is solubilized in an acidic solution at elevated temperature and pressure. The resulting soluble β-glucan may be further clarified and purified using, for example, centrifugation and/or chromatographic techniques. The resulting product, even when comprised of high molecular weight glucans, can be dried to a powder and subsequently re-solubilized.
BRIEF DESCRIPTION OF THE DRAWINGS
FIGS. 1-4 are RI traces and data transformations graphs of particulate-soluble β-glucan samples.
FIG. 5 is a graphic representation of TNFa production induced by various β- glucans. DETAILED DESCRIPTION OF THE INVENTION
The starting material used in the present invention is particulate, or insoluble, β-glucan, produced by any method. The particulate β-glucan starting material may range in size from whole glucan particles down to submicron-sized particles. The level of impurities within the starting material may also vary. However, as the level of impurities within the starting material increases, the amount of soluble glucan recovered decreases. One example of suitable starting material is WGP 3-6® from Biothera.
Any of a number of source of b-glucan can be used for the present invention. Examples of such sources are yeast, barely, oats, mushrooms and other fungi, etc. The particulate β-glucan is treated with acid under pressure and elevated temperature to produce soluble β-glucan. To begin, pelleted, particulate β— glucan is resuspended and mixed in a sealable reaction vessel in a buffer solution and brought to pH 3.6. Buffer reagents are added such that every liter, total volume, of the final suspension mixture contains about 0.61 g sodium acetate, 5.24 ml glacial acetic acid and 430 g pelleted, particulate β-glucan. The vessel is purged with nitrogen to remove oxygen and increase the pressure within the reaction vessel.
Typically, the pressure inside the vessel is brought to 35 PSI, and the suspension is heated to about 135°C for up to about 5.5 hours. It was found that under these conditions the β-glucan will solubilize. As the temperature decreases from 135°C, the amount of solubilization also decreases.
It should be noted that this temperature and pressure are optimized for the embodiment just described. Optimization and adjustment of temperatures and pressures may be required if any of the reaction conditions and/or reagents are altered.
The increased pressure and temperature imparts advantages over prior art processes for solubilizing β-glucan by virtually eliminating the use of hazardous chemicals from the process. Hazardous chemicals that have previously been used include, for example, flammable VOCs such as ether and ethanol, very strong acids such as formic acid and sulphuric acid and caustic solutions of very high pH. The present process is not only safer, but, by reducing the number of different chemicals used and the number of steps involved, is more economical. An additional advantage of the present process is that the length of the above treatment controls the molecular weight of the resulting particulate-soluble β-glucan. As the term is used throughout, "particulate-soluble β-glucan" may be in any of the soluble, particulate or re-solubilized forms. The length of treatment time is inversely related to the resulting molecular weight size. In other words, as the treatment time increases, the resulting average molecular weight of the particulate-soluble β-glucan decreases. This principal is illustrated in the following.
Four samples were collected from a batch of particulate-soluble β-glucan suspension at various time-points (60, 90, 120 and 240 min.) during the above-described process. The molecular weights of the samples were determined by size exclusion chromatography against dextran molecular weight markers. The results are summarized in Table 1.
TABLE 1
Figure imgf000004_0003
Figure imgf000004_0001
♦ ♦weight average molecular weight calculated by:
Figure imgf000004_0002
where N, is the number of molecules of molecular weight M1.
***z-averaged molecular weight, which is based on the volume of the polymer chains.
As evidenced by the above data, the particulate β-glucan slowly begins to breakdown with the largest average size occurring at about 90 min. After the 90 min. time-point, the average size decreases. Time-point specific data is shown in FIGS. 1-4. FIG. 1 includes panels A and B. Panel A is a refractive index (RI) trace of the 60 min. sample. In panel B, a section of the data generated in panel A was transformed and plotted on the graph shown. Curve 10 represents the transformed raw data. Curve 12 represents the cumulative percentage of specific molecular weights. Molecular weight was determined by a standard curve generated with dextran of known size (data not shown).
Data generated from the 90 min. sample is shown in FIG. 2. Panel A and panel B, with curves 14 and 16, correspond to the panels A and B of FIG. 1.
Data generated from the 120 min. sample is shown in FIG. 3. Panel A and panel B, with curves 18 and 20, correspond to the panels A and B of FIG. 1.
Data generated from the 240 min. sample is shown in FIG. 4. Panel A and panel B, with curves 22 and 24, correspond to the panels A and B of FIG. 1.
Specific sizes of particulate-soluble glucan may be more useful for specific applications. For example, when applied topically, molecules of smaller molecular weight may better penetrate skin. Larger molecular weight molecules, on the other hand, may be better suited for oral administration. Therefore, the ability to easily control the average size of the glucan molecules offers a significant competitive advantage.
The exact duration of heat treatment is typically determined experimentally by sampling reactor contents. Various tests may be performed such as gel permeation chromatography (GPC) analyses. The process maximizes the yield of particulate-soluble material that meets specific specification profiles and impurity levels. Once the β-glucan is solubilized, the mixture is cooled to stop the reaction.
The particulate-soluble β-glucan may be washed and utilized at this point, however, for pharmaceutical applications further purification is typically performed. Any combination of one or more of the following steps may be used to further purify and/or clarify the particulate-soluble β-glucan. Other means known in the art may also be used if desired. Suitable means include, for example, centrifugation or continuous-flow centrifugation, which eliminates a significant amount of lipid impurities.
In some instances, the inclusion of lipids within the particulate-soluble β-glucan may increase its effectiveness against certain infectious diseases or enhancing the immune system. The process presented here provides a means to effectively control and vary the amount of lipid in the particulate-soluble β-glucan composition.
Alternatively or in addition to, the particulate-soluble β-glucan may be filtered. In one embodiment, the material is filtered through a 0.2 μm filter. Chromatography may also be used for purification. The particulate-soluble β-glucan may be conditioned at some point in preparation for chromatography. For example, if a chromatographic step includes hydrophobic interaction chromatography (HIC), the particulate-soluble β-glucan can be conditioned to the appropriate conductivity and pH with a solution of ammonium sulphate and sodium acetate. A suitable solution is 3.0 M ammonium sulfate, 0.1 M sodium acetate, which is used to adjust the pH to 5.5.
Another chromatographic step that may be utilized is gel permeation chromatography (GPC). Multiple chromatography cycles may be needed to ensure that the load does not exceed the capacity of the column. At this point, the particulate-soluble β-glucan is purified and ready for use. The particulate-soluble β-glucan that is generally collected has an average molecular weight > 1,000,000 Da, with a high polydispersity. An advantage of this particulate-soluble β- glucan product, especially in the high molecular weight ranges such as over a million Daltons (Da), is that the product can be spray dried to a powder form and then subsequently re-solubilized in solutions of pH about 5 and higher — essentially from weakly acidic to strongly basic. In addition, re-solubilization occurs at temperatures as low as about room temperature (~25°C). Depending on the final concentration after re- solubilization and the solvent used, the time and temperature requirements for re- solubilization will vary. The product's ability to re-solubilize makes it ideal for creating an instantized form of β-glucan suitable for, for example, instant drink powders. Briefly, particulate- soluble β-glucan in dry form is re-wet to achieve a moisture content of about 9%-12%, which forms an agglomerate. A surfactant, such as lecithin, is added to the agglomerate via a two-fluid nozzle. The concentration of surfactant will vary depending on the surfactant used and the conditions and solvent into which the product will be finally dissolved. The agglomerate is then run through three stages of a fluid bed drier. The first stage heats the product, the second stage conditions the product and the third stage cools the product. The resulting product is sifted to form the instantized product.
Another way to form an instantized product is through the addition of a second dry-form soluble ingredient such as table sugar or salt (NaCl). In one example, 200 mg of powdered, particulate-soluble β-glucan and about 0.5 to about 1.0 g of sucrose crystals were mixed and ground in a mortor bowl for about 2-3 minutes. The mixture was added to 500 mis of room temperature water and shook vigorously. The particulate-soluble β- glucan re-solubilized. An identical experiment was carried out with NaCl with the same result.
The particulate-soluble β-glucan product, whether in its solubilized, powdered or re-solubilized form, may be used for any of a number of applications. Particulate-soluble β-glucan is ideal for use as a nutritional supplement, a food ingredient, a cosmetic ingredient and a pharmaceutical product for use in humans and agricultural/companion/exotic animals.
Typical foods in which the dry or wet forms of particulate-soluble β-glucan may be added include, for example, cereals and cereal products, baked goods and baking mixes, beverages and beverage bases, dairy product analogs such as soy milk, milk and milk products, plant protein products, processed fruits and fruit juices, soft candy, soup and soup mixes, yogurt, bottled water and drinks, nutrition bars, etc. Various masking agents and other additives may be added to improve the flavor and texture if necessary.
In its liquid form, the particulate-soluble β-glucan can be used to make edible films. A thin layer of liquid product is dried by any of a number of means known in the art. Additives may be added to the liquid product to create films of various textures or to make them more or less pliable. The films are useful as carriers for pharmaceutical or supplement products. Here again, various masking agents can be added to improve the flavor of the film.
The particulate-soluble β-glucan product may also be more efficacious than prior art particulate β-glucan. For example, the product may be more effective against infectious diseases or cancer. Increased efficacy may be in terms of better uptake, better immune system enhancement, decreased dosing regiments, etc. To this end, in vitro studies showed that the particulate-soluble β-glucan does not induce TNFα from human peripheral blood mononuclear cells (PBMC) at concentrations up to 300 μg/mL. Specifically, human PBMC were cultured in cRPMI medium containing 5% heat-inactivated FCS. Cells were stimulated with various beta glucans (all endotoxin free), TLR7/8 agonist, or vehicle. The beta glucans were used at various concentrations. After overnight incubation at 370C, 5% CO2, cell-free supernatants were collected, stored at -2O0C until cytokine analysis by ELISA. The results from three replicates are shown in FIG. 5. As evidenced by the graph, whole glucan particles stimulate TNFα production, while the particulate-soluble product does not. Because TNFα is a major cytokine involved in an inflammatory response, the particulate-soluble product is not expected to induce an inflammatory response.
While this invention has been shown and described with references to particular embodiments, it will be understood by those skilled in the art that various changes in form and detail may be made therein without departing from the spirit and scope of the invention encompassed by the appended claims.

Claims

1. A composition comprising a particulate-soluble β-glucan capable of being dried to powder form and then being re-solubilized in a solution having a pH of about 5 or more.
2. The composition of claim 1 wherein the particulate-soluble β-glucan is derived from yeast.
3. The composition of claim 1 wherein the particulate-soluble b-glucan is instantized.
4. The composition of claim 3 and further comprising: a second dry-form soluble ingredient.
5. The composition of claim 1 wherein a temperature of the solution is about room temperature or higher.
6. A composition comprising a particulate-soluble b-glucan solubilized in a solution, the solution being any of range from weakly acidic to strongly basic.
7. The composition of claim 6 wherein the solution has a temperature ranging from about room temperature to about 6O0C.
8. The composition of claim 6 wherein the solution is a beverage for human and/or animal consumption.
9. A composition comprising a particulate-soluble β-glucan capable of being dried to powder form and then being re-solubilized in a solution having a temperature of about 250C or more.
10. A composition comprising a particulate-soluble b-glucan, the composition being either a liquid or dry form, the dry form being capable of re-solubilization in a liquid that has a pH of about 5 or greater.
11. The composition of claim 10 wherein the particulate-soluble b-glucan has an average molecular weight of over about 1,000,000 Da.
PCT/US2008/005914 2007-05-08 2008-05-08 Particulate-soluble glucan preparation WO2008140744A1 (en)

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