US20060263415A1 - Production of beta-glucans and mannans - Google Patents

Production of beta-glucans and mannans Download PDF

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US20060263415A1
US20060263415A1 US11/418,922 US41892206A US2006263415A1 US 20060263415 A1 US20060263415 A1 US 20060263415A1 US 41892206 A US41892206 A US 41892206A US 2006263415 A1 US2006263415 A1 US 2006263415A1
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glucan
yeast
cell walls
mannan
mannans
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Joseph Sedmak
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Sensient Flavors LLC
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    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K36/00—Medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicines
    • A61K36/06—Fungi, e.g. yeasts
    • A61K36/062—Ascomycota
    • A61K36/064—Saccharomycetales, e.g. baker's yeast
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K10/00—Animal feeding-stuffs
    • A23K10/10—Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K10/00—Animal feeding-stuffs
    • A23K10/10—Animal feeding-stuffs obtained by microbiological or biochemical processes
    • A23K10/14—Pretreatment of feeding-stuffs with enzymes
    • A—HUMAN NECESSITIES
    • A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23K—FODDER
    • A23K20/00—Accessory food factors for animal feeding-stuffs
    • A23K20/10—Organic substances
    • A23K20/163—Sugars; Polysaccharides
    • 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
    • A23L29/206—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin
    • A23L29/244—Foods or foodstuffs containing additives; Preparation or treatment thereof containing gelling or thickening agents of vegetable origin from corms, tubers or roots, e.g. glucomannan
    • 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
    • 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
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/72—Cosmetics or similar toiletry preparations characterised by the composition containing organic macromolecular compounds
    • A61K8/73—Polysaccharides
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/96—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution
    • A61K8/97—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution from algae, fungi, lichens or plants; from derivatives thereof
    • A61K8/9728—Fungi, e.g. yeasts
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61K—PREPARATIONS FOR MEDICAL, DENTAL OR TOILETRY PURPOSES
    • A61K8/00—Cosmetics or similar toiletry preparations
    • A61K8/18—Cosmetics or similar toiletry preparations characterised by the composition
    • A61K8/96—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution
    • A61K8/99—Cosmetics or similar toiletry preparations characterised by the composition containing materials, or derivatives thereof of undetermined constitution from microorganisms other than algae or fungi, e.g. protozoa or bacteria
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P17/00—Drugs for dermatological disorders
    • A61P17/04—Antipruritics
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P29/00—Non-central analgesic, antipyretic or antiinflammatory agents, e.g. antirheumatic agents; Non-steroidal antiinflammatory drugs [NSAID]
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61P—SPECIFIC THERAPEUTIC ACTIVITY OF CHEMICAL COMPOUNDS OR MEDICINAL PREPARATIONS
    • A61P3/00—Drugs for disorders of the metabolism
    • A61P3/02—Nutrients, e.g. vitamins, minerals
    • 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
    • A61P37/08—Antiallergic agents
    • A—HUMAN NECESSITIES
    • A61—MEDICAL OR VETERINARY SCIENCE; HYGIENE
    • A61Q—SPECIFIC USE OF COSMETICS OR SIMILAR TOILETRY PREPARATIONS
    • A61Q19/00—Preparations for care of the skin
    • 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
    • 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
    • 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
    • C08B37/006—Heteroglycans, i.e. polysaccharides having more than one sugar residue in the main chain in either alternating or less regular sequence; Gellans; Succinoglycans; Arabinogalactans; Tragacanth or gum tragacanth or traganth from Astragalus; Gum Karaya from Sterculia urens; Gum Ghatti from Anogeissus latifolia; Derivatives thereof
    • C08B37/0087—Glucomannans or galactomannans; Tara or tara gum, i.e. D-mannose and D-galactose units, e.g. from Cesalpinia spinosa; Tamarind gum, i.e. D-galactose, D-glucose and D-xylose units, e.g. from Tamarindus indica; Gum Arabic, i.e. L-arabinose, L-rhamnose, D-galactose and D-glucuronic acid units, e.g. from Acacia Senegal or Acacia Seyal; Derivatives thereof
    • C—CHEMISTRY; METALLURGY
    • C12—BIOCHEMISTRY; BEER; SPIRITS; WINE; VINEGAR; MICROBIOLOGY; ENZYMOLOGY; MUTATION OR GENETIC ENGINEERING
    • C12P—FERMENTATION OR ENZYME-USING PROCESSES TO SYNTHESISE A DESIRED CHEMICAL COMPOUND OR COMPOSITION OR TO SEPARATE OPTICAL ISOMERS FROM A RACEMIC MIXTURE
    • C12P19/00—Preparation of compounds containing saccharide radicals
    • C12P19/04—Polysaccharides, i.e. compounds containing more than five saccharide radicals attached to each other by glycosidic bonds

Definitions

  • This invention relates to ⁇ -glucan/mannan preparations and to methods for their preparation.
  • the invention relates to preparations, including ⁇ -(1,3/1,6) glucan and mannan, produced from microorganisms including, but not limited, to yeasts.
  • Glucan is a generic term referring to an oligo- or polysaccharide composed predominantly or wholly of the monosaccharide D-glucose. Glucans are widely distributed in nature, and are particularly important for their role in maintaining the structural integrity of bacterial, yeast, and plant cells. For example, glucan, in combination with other polysaccharides such as mannan and chitin, is responsible for the shape and mechanical strength of the cell wall. Glucans typically accounts for approximately 40% to 50% of the weight of the cell wall in these cells.
  • the D-glucose units may be linked together in a variety of ways.
  • glucans with (1,3), (1,4), (1,6) and (1,2) linkages are all known.
  • the variety of linkages possible means that glucans are normally highly branched compounds. Many forms are possible as a result of this highly variable manner in which this individual glucose units can be joined as well as the overall steric shape of the parent molecule.
  • a common glucan is ⁇ -(1,3)-linked glucopyranose (commonly referred to as ⁇ -glucan).
  • Cell walls of several species include ⁇ -(1,3)-linked glucopyranose coupled with ⁇ -(1,6)-linked glucopyranose.
  • the cell wall of Saccharaomyces cerevisiae is primarily composed of ⁇ -linked glucan, which is mainly a backbone of ⁇ -(1-3)-linked glucose units, with a minor component of inter and intra molecular branching via ⁇ -(1-6)-linkages.
  • glucans Because of their chemical properties, glucans have found a wide variety of uses in the chemical, food and pharmaceutical industries. For example, they may be useful as viscosity imparting agents, emulsifiers, fibers, films, coating substances, supports for affinity chromatography and gel electrophoresis, in cell culture media, as filter pads, and in cement. They are also widely used as food thickeners and as a source of dietary fiber, and as carriers and coating agents in pharmaceutical products. Glucans have been shown to have immunopharmacological activity in humans and animals. For example, strong immunostimulation and protection against pathogenic microorganisms have been demonstrated in shrimp, fish, poultry, swine, cattle, rabbits, mice, rats and humans.
  • Yeast ⁇ -glucans may stimulate the innate (non-specific) immune response of vertebrates and invertebrates via interaction with the Toll-like receptor Dectin-1. Such binding stimulates the production of active oxygen species in macrophages and enhances their phagocytosis and killing of microorganisms. These stimulated immune cells also produce cytokins which can circulate throughout the animal and interact with other immune cells to enhance the immune status of the animal.
  • Mannan is a polymer composed of mannose units.
  • mannan is associated with protein in both the external surface of the yeast cell wall, as a muscigenous polysaccharide, and in the inner cell membrane. It generally accounts for about 20-50% of the dry weight of the cell wall.
  • Mannan is linked to a core-peptide chain as an oligomer or polymer.
  • the complex contains about 5-50% proteins.
  • Oligomeric mannan is bonded directly to serine and threonine, whereas polymeric mannan is bonded to aspargine via N-acetylglucosamine.
  • the mannose units are linked by ⁇ -1,6, ⁇ -1,2 and ⁇ -1,3-linkages.
  • Mannan-oligosaccharides can be released from yeast cell walls by proteolytic action.
  • the released MOS can effectively bind to bacterial pathogens of the intestinal tract and block their ability to colonize the intestinal tract.
  • E. coli, Salmonella spp. and Vibrio cholera have proteins on their surface (lectins) which bind specifically to the mannose sugar residues of the MOS.
  • FIG. 1 is a flowchart of one embodiment of a process for production of ⁇ -glucan/mannan preparations in accordance with the present invention.
  • FIG. 2 is a flowchart of another embodiment for process for production of ⁇ -glucan/mannan preparations in accordance with the present invention.
  • the present invention provides a method for processing yeast cells using the steps of autolyzing the yeast cells to release yeast cell walls, incubating the yeast cell walls with an exogenous protease, separating the yeast cell walls into a glucan-enriched component and a mannan enriched component, and ultrafiltering the mannan-enriched component to form a filtrate and a retentate.
  • the invention provides a method for processing yeast cells using the steps of autolyzing the yeast cells at a temperature of 40° C. to 65° C. to release yeast cell walls, incubating the yeast cell walls with an exogenous protease at a pH of 9 to 10, and incubating the protease-treated cell walls with an enzyme such as an amylase, lipase or a combination thereof.
  • the invention provides a composition comprising ⁇ -mannans, wherein at least 85% (w/w) of the total ⁇ -mannans have a molecular weight of 10,000 Da or more.
  • inventions include animal feeds, food supplements, pharmaceuticals, cosmetics and neutraceuticals that comprise glucans or mannans made by methods of the invention.
  • the invention provides a process that produces insoluble cell wall preparations enriched in ⁇ (1,3) and ⁇ (1,6) glucans and a soluble fraction enriched in mannans.
  • the process in accordance with the present invention includes an autolysis step of a source of cell walls, for example, yeast, such as brewer's yeast or baker's yeast, followed by an enzymatic digestion step.
  • the enzymatic digestion is carried out using a high-pH protease.
  • the enzymatic digestion is carried out using a combination of enzymes, such as a high-pH protease, an amylase, glucoamylase and/or lipase.
  • the enzymatic digestion is carried out using a high-pH protease followed by one or more other enzymes, such as amylase, glucoamylase and/or lipase.
  • the invention provides a cell wall preparation that is enriched ⁇ -(1,3) and ⁇ -(1,6) glucans, and in another embodiment, a soluble fraction enriched in mannans.
  • any numerical range recited herein includes all values from the lower value to the upper value. For example, if a concentration range is stated as 1% to 50%, it is intended that values such as 2% to 40%, 10% to 30%, or 1% to 3%, etc., are expressly enumerated in this specification. These are only examples of what is specifically intended, and all possible combinations of numerical values between the lowest value and the highest value enumerated are to be considered to be expressly stated in this application.
  • ⁇ -glucan/mannan preparations can be prepared from microorganisms, such as yeast, using a simple autolysis process, at slightly acidic/near-neutral pH and only moderately elevated temperature. Autolysis is followed by an enzymatic digestion.
  • the enzymatic step utilizes a high pH protease (e.g., Protex 6L available from Genencore International or from fermentation of Bacillus lichenformis ), typically about 0.05%-1% by weight, at an alkaline pH, and elevated temperature.
  • a high pH protease e.g., Protex 6L available from Genencore International or from fermentation of Bacillus lichenformis
  • Suitable yeast species as a source of ⁇ -glucans/mannans include, but are not limited to, yeast strains of Saccharomyces cerevisiae (including baker's yeast strains and brewer's yeast strains), Kluyveromyces fragilis , and Candida strains, such as Candida utilis , and combinations thereof.
  • yeast strains of yeast which are suitable sources of ⁇ -glucans/mannans include, but are not limited to, Saccharomyces delbruekii, Saccharomyces rosei, Saccharomyces microellipsodes, Saccharomyces carlsbergensis, Schizosaccharomyces pombe, Kluyveromyces lactis, Kluyveromyces polysporus, Candida albicans, Candida cloacae, Candida tropicalis, Candida guilliermondii, Hansenula wingei, Hansenula arni, Hansenula henricii, Hansenula Americana and combinations thereof. These yeast strains can be produced using culture in food grade nutrients either by batch fermentation or continuous fermentation.
  • microorganisms including, but are not limited to, bacteria, fungi, and plants, for example, unicellular algae, have been reported in the art as a source of ⁇ -glucans/mannans.
  • Other microorganisms which may be useful in the invention as sources of ⁇ -glucans and/or mannans include, but are not limited to, bacteria, such as Alkaligenes , especially Alkaligenes faecalis Var.
  • Non-microorganisms such as plants, may also be useful in the invention as sources of ⁇ -glucans and/or mannans.
  • the process in accordance to the present invention relates to the generation of cell wall preparations enriched in ⁇ -(1,3)- and ⁇ -(1,6)-glucan content and mannan content, produced from microorganisms including, but not limited to, yeast.
  • the process includes a first step of autolysis of yeast, e.g., brewer's yeast, (typically a 7% to 18%, particularly a 10% to 17%, and more particularly a 8% to 12% or 13% to 16% solids slurry).
  • the autolysis may suitably be carried out at a pH of at least 4, particularly at least 4.5, and more particularly at least 5.
  • the yeast is then separated, suitably by centrifugation, to produce an extract, and a cell wall stream of low ⁇ -glucan content.
  • a further step treats the cell wall stream with an enzyme including, but not limited to, a protease, e.g., an alkaline protease, at a pH of at least 8.5, particularly at least 9, and more particularly at least 9.2.
  • the pH may also suitably be less than 10.5, particularly less than 10, and even more particularly less than 9.8.
  • the protease treatment may suitably be carried out at a temperature of at least 45° C., particularly at least 50° C., more particularly at least 53° C.
  • This ⁇ -(1,3/1,6) cell wall product is then dried, e.g., spray dried, which results in aggregation of the product to particles of about 100-300 microns or larger.
  • the mannan extract is then subjected to a 10,000 molecular weight ultrafiltration to yield a high-molecular weight retentate that is enriched in mannan.
  • Live yeast are subjected to autolysis in a process in which endogenous yeast enzymes break down and solubilize some yeast macromolecules.
  • Soluble extract is separated from insoluble yeast cell walls by centrifugation.
  • the cell walls are then treated with a high-pH protease to further remove protein from the cell walls, and subsequently also remove the mannan which is attached to the cell wall protein.
  • the ⁇ -glucan enriched cell walls are then separated from the secondary extract by centrifugation. Mannan, which has a high molecular weight, can be further purified and concentrated by passing the secondary extract through a 10,000 Da ultrafilter.
  • the autolysis may suitably be carried out for at least 10 hours, particularly at least 16 hours, and more particularly at least 24 hours.
  • the autolysis may suitably be carried out for less than 100 hours, particularly less than 48 hours, and even more particularly less than 36 hours.
  • the yeast is then separated, suitably by centrifugation, to produce an extract, and a cell wall stream of low ⁇ -glucan content.
  • a further step treats the cell wall stream with enzymes.
  • the enzymatic step utilizes first a high pH protease at an alkaline pH, for example, at a pH of at least 8.5, particularly at least 9, and more particularly at least 9.2.
  • the pH may also suitably be less than 10.5, particularly less than 10, and even more particularly less than 9.8.
  • the protease treatment may suitably be carried out at a temperature of at least 45° C., particularly at least 50° C., more particularly at least 53° C.
  • the protease treatment may suitably be carried out at a temperature of less than 70° C., particularly less than 65° C., and more particularly less than 60° C., and even more particularly less than 57° C.
  • the protease treatment may be suitably carried out for at least 5 hours, particularly at least 8 hours, more particularly at least 10 hours, even more particularly at least 12 hours.
  • the protease treatment may be suitably carried out for less than 48 hours, particularly less than 36 hours, more particularly less than 24 hours, and even more particularly less than 18 hours.
  • the pH may suitably range from at least 3.5, particularly from at least 4, and even more particularly from at least 4.5.
  • the pH may also suitably range from less than 7, particularly less than 6, and even more particularly less than 5.5.
  • the temperature for carrying out the incubation with glucoamylase, amylase and/or lipase may suitably range from at least 40° C., particularly at least 45° C. more particularly at least 50° C. and even more particularly at least 53° C.
  • the temperature may also suitably range from less than 70° C., particularly less than 65° C., more particularly less than 60° C., and even more particularly less than 58° C.
  • the incubation with the amylase and/or a lipase is suitably carried out at a pH of 4 to 7 and a temperature of 50° to 65° C. for approximately 4 to 10 hours.
  • the amylase may digest residual alpha-glucans such as glycogen that may still reside with the cell wall.
  • the lipase may degrade cell wall membranes enriched with lipids and fats.
  • the cell wall stream may then be separated by centrifugation to produce a secondary extract enriched with mannan, and a cell wall product enriched in ⁇ -glucans.
  • the cell wall product may be dried, e.g., spray dried.
  • the secondary mannan extract may be passed through an ultrafilter, such as a 10,000 Da ultrafilter, a 50,000 Da ultrafilter, or a 100,000 Da ultrafilter to enrich the mannan content of the retentate.
  • the preparations of the invention may be dried by any suitable process including, but not limited to, freeze-drying, roller drum drying, oven-drying, spray-drying, ring-drying, and combinations thereof and/or dried using film-forming equipment, and either may be used without further processing, or may be milled using any suitable technique.
  • the high-pH protease may have an optimum proteolytic activity at a pH above 7.
  • Suitable proteases include, but are not limited to, those obtained from Actinidia chinensis, Ananas comosus, Aspergillus spp. (e.g. A. niger, A. niger var. awamori, A. oryzae, A. sojae, A. melleus ), Bacillus spp. (e.g. B. subtilis, B. alcalophilus, B. amyloliquefaciens, B. halodurans, B. lentus, B. licheniformis, B. stearothermophilus, B.
  • Actinidia chinensis e.g. A. niger, A. niger var. awamori, A. oryzae, A. sojae, A. melleus
  • Bacillus spp. e.g. B. subtilis
  • thermoproteolyticus Carica papya, Cryphonectria parasitica, Endothia parasitica, Ficus glabrata, Kluyveromyces lactis, Penicillum citrinum, Rhizomucor miehei, Rhizopus niveus , from calf, goat or ox stomachs or porcine pancreases, and combinations thereof.
  • Suitable proteases may include, but are not limited to, commercially available enzymes such as subtilisin Carlsberg, subtilisin BPN′, subtilisin Novo, subtilisin 309, subtilisin 147 and subtilisin 168, AlcalaseTM, SavinaseTM, PrimaseTM, DuralaseTM, DurazymTM, EsperaseTM, and KannaseTM (available from Novo Nordisk A/S); MaxataseTM, MaxacalTM, MaxapemTM, OptimaseTM, ProperaseTM, PurafectTM, Purafect OxPTM, FN2TM, and FN3TM (available from Genencor International Inc.); and ValidaseTM AFP, ValidaseTM FP Concentrate, ValidaseTM FP 500, ValidaseTM FP II, ValidaseTM TSP Concentrate, Alkaline Protease Concentrate, Bromelain (available from Valley Research, South Bend, Ind.), and combinations thereof.
  • commercially available enzymes
  • Suitable amylases include those of plant, animal, bacterial or fungal origin, and combinations thereof.
  • Amylases include, but are not limited to, glucoamylases or ⁇ -amylases obtained from Bacillus spp., (e.g., B. licheniformis, B. amyloliquefaciens, B. subtilis, B. stearothermophilus ), Aspergillus oryzae, Aspergillus niger, Aspergillus niger var. awamori, Microbacterium imperiale, Thermomonospora viridis , barley malt ( Hordeum spp.), porcine pancreas ( Sus spp.), and combinations thereof.
  • Bacillus spp. e.g., B. licheniformis, B. amyloliquefaciens, B. subtilis, B. stearothermophilus
  • Aspergillus oryzae Aspergill
  • amylases examples include, but are not limited to, commercially available amylases such as Glucoamylase Concentrate, DuramylTM, TermamylTM, FungamylTM and BANTM (available from Novo Nordisk A/S); RapidaseTM and PurastarTM (available from Genencor International Inc.); and ValidaseTM BAA, ValidasemTM HT340L, ValidaseTM FAA, ValidaseTM AGS, ValidaseTM GA, ValidaseTM RGA (available from Valley Research, South Bend, Ind.), and combinations thereof.
  • the amylase may be suitably used at a final concentration of at least 0.001%, particularly at least 0.01% and even more particularly at least 0.02%.
  • the amylase may be suitably used at a final concentration of less than 0.1%, particularly less than 0.05%, and even more particularly less than 0.1%.
  • Lipases useful in the invention include, but are not limited to, lipases from Humicola (synonym Thermomyces ), e.g. from H. lanuginosa ( T. lanuginosus ), H. insolens , a Pseudomonas lipase , e.g. from P. alcaligenes or P. pseudoalcaligenes, P. cepacia, P. stutzeri, P. fluorescens, Pseudomonas sp. strain SD 705, P. wisconsinensis , a Bacillus lipase , e.g. from B. subtilis, B. stearothermophilus or B.
  • lipase enzymes include, but are not limited to, LipolaseTM and Lipolase UltraTM (Novo Nordisk A/S), and Fungal Lipase 8000 and Pancreatic Lipase 250 (available from Valley Research, South Bend, Ind.).
  • the product resulting from autolysis of the yeast cells suitably also comprises, at least 20%, particularly at least 23% and more particularly at least 25% protein of the total product on a dry solids basis.
  • the product also suitably comprises less than 45%, particularly less than 40% and more particularly less than 35% protein of the total product on a dry solids basis.
  • the product resulting from autolysis of the yeast cells suitably comprises at least 20%, particularly at least 23% and more particularly at least 25% total glucans of the total product on a dry solids basis.
  • the product also suitably comprises less than 45%, particularly less than 40% and more particularly less than 35% total glucans of the total product on a dry solids basis.
  • the product resulting from autolysis of the yeast cells suitably comprises, at least 5%, particularly at least 7% and more particularly at least 10% alpha-glucans of the total product on a dry solids basis.
  • the product also suitably comprises less than 20%, particularly less than 18% and more particularly less than 15% alpha-glucans of the total product on a dry solids basis.
  • the product resulting from autolysis of the yeast cells suitably comprises, at least 7%, particularly at least 10% and more particularly at least 12% beta-glucans of the total product on a dry solids basis.
  • the product also suitably comprises less than 22%, particularly less than 20% and more particularly less than 18% beta-glucans of the total product on a dry solids basis.
  • the product resulting from autolysis of the yeast cells suitably comprises, at least 5%, particularly at least 7% and more particularly at least 10% mannans of the total product on a dry solids basis.
  • the product also suitably comprises less than 20%, particularly less than 18% and more particularly less than 15% mannans of the total product on a dry solids basis.
  • the enriched ⁇ -(1,3/1,6) glucan product cell wall product is characterized, for example, as at least 50%, at least 55%, at least 60% or at least 65% ⁇ -(1,3/1,6) glucan with a protein content of less than 20%, less than 15%, or less than 10%.
  • the enriched mannan product (secondary mannan extract) may be characterized as containing at least 50%, particularly at least 55% and even more particularly at least 57% mannan.
  • the enriched mannan product may also be characterized as containing less than 70%, particularly less than 68%, and even more particularly less than 65% mannan.
  • the enriched mannan product may be also characterized as containing at least 25%, particularly at least 27%, and more particularly at least 29% protein.
  • the enriched mannan product may be also characterized as containing less than 35%, particularly less than 32%, and more particularly less than 30% protein.
  • the ultrafiltration step may be carried out by forcing an extract produced from the processes described herein, such as a secondary mannan extract, through an ultrafilter under pressure.
  • the ultrafilter comprises one or more semi-permeable membranes.
  • the semi-permeable membrane or ultrafilter may have a molecular weight cut-off of, for example, at least 8,000 Da, particularly at least 10,000 Da, more particularly at least 25,000 Da, even more particularly at least 50,000 Da, still more particularly at least 100,000 Da, and yet still more particularly at least 150,000 Da.
  • the ultrafilter may have a molecular weight cut of any value between those recited herein including, but not limited to, a molecular weight cut off of at least 15,000 Da, 20,000 Da, 30,000 Da, 40,000 Da, 60,000 Da, 70,000 Da, 80,000 Da, 90,000 Da, 110,000 Da, 120,000 Da, 130,000 Da and 140,000 Da.
  • Suitable ultrafilter membranes include, but are not limited to, hollow fiber membranes available from A/G Technology Corp, Needham, Mass.
  • At least 80% (w/w), particularly at least 85% (w/w), and more particularly at least 90% (w/w) of the total secondary mannans in the retentate following filtration of a secondary mannan extract may have a molecular weight above the molecular weight cut off of the filter used. For example, if a 10,000 Da cut off is used with a secondary mannan extract, typically at least 80% (w/w), particularly at least 85% (w/w), and more particularly at least 90% (w/w) of the total mannans in the retentate may have a molecular weight above 10,000 Da.
  • a 50,000 Da cut off is used with a secondary mannan extract, typically at least 80% (w/w), particularly at least 85% (w/w), and more particularly at least 90% (w/w) of the total mannans in the retentate may have a molecular weight above 50,000 Da.
  • a 100,000 Da cut off is used with a secondary mannan extract, typically at least 80% (w/w), particularly at least 85% (w/w), and more particularly at least 90% (w/w) of the total mannans in the retentate may have a molecular weight above 100,000 Da.
  • a 150,000 Da cut off is used with a secondary mannan extract, typically at least 80% (w/w), particularly at least 85% (w/w), and more particularly at least 90% (w/w) of the total mannans in the retentate may have a molecular weight above 150,000 Da.
  • the ultrafiltration step may optionally include passing the mannan extract through two or more ultrafilters of different molecular weight cut offs.
  • the final retentate comprises an enriched mannan product wherein a majority of mannans have a molecular weight falling between the molecular weight cut-offs of the ultrafilters.
  • at least 80% (w/w), particularly at least 85% (w/w), and more particularly at least 90% (w/w) of the total mannans of the final retentate may suitably have a molecular weight between the molecular weight cut-offs of the ultrafilters.
  • the secondary mannan extract which results from separation from the glucan enriched product following enzymatic treatment of autolyzed cell walls is characterized, for example, from 15% to 50% mannan, 20% to 30% protein, and 20% to 25% other components.
  • the retentant may comprise at least 50%, particularly at least 52%, more particularly at least 55% and even more particularly at least 60% mannan.
  • the retentate may comprise less than 70%, particularly less than 65%, and more particularly less than 62% mannan.
  • the retentate may further comprise at least 10%, particularly at least 12%, more particularly at least 15% and even more particularly at least 17% protein.
  • the retentate may further comprise less than 33%, particularly less than 30%, and more particularly less than 22% protein.
  • the preparations in accordance with the present invention are contemplated to be of value in, e.g., food supplements, pharmaceuticals (e.g., improving immune response), cosmetics, animal feeds, and neutraceuticals.
  • an animal feed may suitably contain 1 to 10 g of preparation/kg feed.
  • the preparation may be comprise at least 0.01%, particularly at least 0.02%, more particularly at least 0.05%, and even more particularly at least 0.1% and less than 5%, particularly less than 2%, more particularly less than 0.5%, and even more particularly less than 0.3% of the total weight of the feed, on a weight/weight basis.
  • Suitable animal feeds include, but are not limited to, cattle, horse, swine, poultry, fish (e.g., crustacean, shellfish), bird and pet (e.g., cat, dog) feeds.
  • a liquid composition may contain 0.1%-1% by weight of the preparation in accordance with the present invention.
  • Preparations according to the invention may also be used in a plant protection composition together with an agriculturally acceptable carrier, and optionally an agriculturally acceptable nutrient, herbicide or pesticide.
  • the enriched beta-glucan fractions made according to the present invention may suitably be used as immune stimulators in animal and human foods, pharmaceuticals or emollients, agents to reduce cholesterol, and thickening agents in foods and beverages.
  • the beta glucan may be suitably present at a concentration (w/w) of at least 0.05%, particularly at least 0.1% and more particularly at least 0.5%, and less than 10%, particularly less than 5% and more particularly less than 2%.
  • the beta-glucan fractions made according to the present invention may be used to treat eczema, for example, by incorporation into a cream, lotion or emollient.
  • Eczema encompasses various inflamed skin conditions, including atopic dermatitis (“atopic eczema”), and affects about 10% to about 20% of the world population during childhood. Eczema appears to be an abnormal response of the body's immune system.
  • mannan-enriched products made according to the present invention.
  • mannan products may be used in the animal feed industry, having advantageously the ability to bind mycotoxins and also pathogenic bacteria, preventing bacteria from colonizing the intestinal tract.
  • the invention provides, among other things, enriched preparations of ⁇ -glucans and mannans, utilizing processes of relatively mild process conditions.
  • the insoluble cell wall fraction was washed three times with a volume of water equal to the volume of extract removed.
  • the washed cell wall fraction was condensed to 15.4% solids, the pH was adjusted to 7.0 with hydrochloric acid and the fraction was spray dried.
  • a portion of the extract from the Protex 6L treatment (corresponding to the 20 extract shown in FIG. 1 ) was condensed to 28.3% solids, the pH was adjusted to 7.0 and the extract was spray dried.
  • the remainder of the 2° extract was ultrafiltered using a UFP-10-C-6A 10,000 NMWC hollow fiber membrane (available from A/G Technology Corp, Needham, Mass.).
  • the high molecular weight enriched mannan retentate was adjusted to pH 7.0 and spray dried.
  • the 3° extract (filtrate) was adjusted to pH 7.0, condensed and spray dried.
  • composition of the products resulting from this process were analyzed using the following techniques: protein was determined using a LECO protein determinator (LECO Corp., St. Joseph, Mich.); total glucans, alpha-glucans and beta-glucans were measured using Megazyme International Mushroom and Yeast Beta-glucan kit (available from Megazyme International, Wicklow, Ireland); mannans were determined by acid hydrolysis of carbohydrates and linked spectrophotometric assay for free mannose, using hexokinase, glucose-6-phosphate dehydrogenase, phosphoglucose isomerase and phosphomannose isomerase; fat was determined using the methanol-chloroform extraction method of Blich, E. G. and Dyer, W. J. Can.
  • the heated material was separated with a Westfalia bowl separator (available from Westfalia Separator, Inc., Northvale, N.J.). Most of the extract (shown as the 2° extract in FIG. 2 ) was condensed and spray dried. A portion of the 2° extract was ultrafiltered using a UFP-10-C-6A 10,000 NMWC hollow fiber membrane (available from A/G Technology Corp, Needham, Mass.). The retentate and the filtrate were condensed and spray dried. The spray dried products were analyzed according to the techniques described in Example 1. The results are presented in Table 2. The cell wall fraction was water washed by centrifugation, condensed and spray dried. TABLE 2 Characterization of Products made according to Process Depicted in FIG.
  • the data of table 3 indicate that when glucoamylase is added before the Protex 6L, as in Vessel 1, then the cell walls are not sufficiently altered to permit the glucoamylase to access and digest the large molecular weight ⁇ -glucan (glycogen) that is trapped inside the cell walls following the autolysis of brewer's yeast.
  • adding protease prior to the glucoamylase permitted the glucoamylase to access and digest the ⁇ -glucan, and to release substantially more glucose. This is the case, even though the glucoamylase in vessel 1 had a longer time (14 hours) to work at pH 5.0 than the glucoamylase of Vessel 2 (4 hours). Therefore, for optimal removal of glycogen/ ⁇ -glucan from brewer's yeast cell walls, the alkaline protease Protex 6L should be added before the glucoamylase.
  • Pigs fed the treatment diet were significantly heavier on day 14 and there was a tendency for the pigs to show increased in weight for the 28 days.
  • a highly purified yeast cell wall product of Saccharomyces cerevisiae is produced o the process described in Example 2. It has a high concentration of ( ⁇ -1,3/1,6) product is G.R.A.S. (Generally Recognized as Safe) by the FDA.
  • the product to supplement in a wide variety of foods with a high quality natural source of ( ⁇ -1,3/1,6) glucan. This biologically active material has been shown to stimulate the immune wide range of animals.
  • the composition and characteristics of the product are ble 7.
  • Standard chicken feed (without antibiotics) either containing 1 g/Kg of the enriched mannan ultrafiltration retentate of Example 1, or containing no enriched mannan (control), is fed daily to broiler chickens for two weeks.
  • the broiler chickens (both the control and the mannan fed groups) are then given an oral inoculation of a strain of Salmonella pathogenic for the chickens.
  • the chickens are continued on their respective diets, and mortality and morbidity are monitored for one month.
  • Beta-Glucan Enriched Product of Examples 1 or 2 in Tiger Vietnamese silk Cultivation
  • a select group of children suffering from eczema that is not responsive to current accepted skin lotion treatments is treated with a lotion containing a 1% suspension of the enriched ⁇ -glucan product of Example 2.
  • the lotion is applied twice daily.
  • the skin is evaluated weekly by a dermatologist for improvement of lesions and pain.
  • the ⁇ -glucan lotion is expected to decrease the lesions associated pain and quickens the healing of the lesions.
  • the yeast beta-glucan extract from Example 2 is added at 0.5% (w/w) and 1% (w/w) to cookies, snack bars and bakery items.
  • the beta-glucan supplemented cookies, snack bars and bakery items contain fewer calories than cookies, snack bars and bakery items not containing beta-glucan.
  • the beta glucans are expected to stimulate the innate immune system of the intestinal tract and benefit the immune status of the consumer.
US11/418,922 2005-05-05 2006-05-05 Production of beta-glucans and mannans Abandoned US20060263415A1 (en)

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CA2607004A1 (en) 2006-11-16
US20100190872A1 (en) 2010-07-29
CA2912012C (en) 2018-05-29
BRPI0611535A8 (pt) 2017-03-28
JP2008541700A (ja) 2008-11-27
CA2912012A1 (en) 2006-11-16
EP1877447A1 (en) 2008-01-16
CN101184780A (zh) 2008-05-21
CN101184780B (zh) 2012-10-03
EP1877447B1 (en) 2016-12-21
US8753668B2 (en) 2014-06-17
WO2006121803A1 (en) 2006-11-16

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