WO1993020140A1 - Biodegradable polymer compositions - Google Patents

Biodegradable polymer compositions Download PDF

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Publication number
WO1993020140A1
WO1993020140A1 PCT/US1993/002821 US9302821W WO9320140A1 WO 1993020140 A1 WO1993020140 A1 WO 1993020140A1 US 9302821 W US9302821 W US 9302821W WO 9320140 A1 WO9320140 A1 WO 9320140A1
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WO
WIPO (PCT)
Prior art keywords
composition according
starch
acid
composition
group
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PCT/US1993/002821
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English (en)
French (fr)
Inventor
Gerd Borchers
Ingo Dake
Jean-Pierre Sachetto
Olivier Mauzac
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Parke-Davis & Company
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Application filed by Parke-Davis & Company filed Critical Parke-Davis & Company
Priority to JP5517564A priority Critical patent/JPH07505433A/ja
Publication of WO1993020140A1 publication Critical patent/WO1993020140A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L3/00Compositions of starch, amylose or amylopectin or of their derivatives or degradation products
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L2201/00Properties
    • C08L2201/06Biodegradable
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L93/00Compositions of natural resins; Compositions of derivatives thereof
    • C08L93/02Shellac

Definitions

  • the present invention relates to biodegradable compositions capable of being formed by heat and pressure into articles having good dimensional stability and physical properties.
  • compositions comprise a starch and/or a derivative of starch and at least one compound, preferably obtainable from a natural source, which compound comprises at least one component having a molecular weight of less than 2,000 and which has at least one carboxyl group and at least one hydroxyl group.
  • said composition further contains one or more compounds selected from the group consisting of hydrophilic and/or hydrophobic polymers.
  • composition comprising the combination, under conditions sufficient to ensure uniform melt formation, of: (a) starch and/or a starch derivative, and (b) at least one compound which comprises at least one component having a molecular weight of less than 2,000 and which has at least one carboxyl group and at least one hydroxyl group.
  • said compound is obtained from a natural source.
  • a compound obtainable from a "natural source” is meant a biosynthesised material which is extracted, secreted or otherwise obtained from prokaryotic or eukaryotic organisms including micro-organisms, plants, animals and insects.
  • Such definition embraces also the products obtained from the processing (biological or otherwise) , of such material.
  • oils for example, are compounds obtainable from a natural source according to this present definition.
  • Said composition preferably further contains item (c) - viz one or more compounds selected from the group consisting of hydrophilic and/or hydrophobic polymers.
  • Item (a) of the composition is preferably a native starch as derived from potatoes, rice, tapioca, corn, pea, rye, oats, wheat, maize or barley or a derivative of such a starch, for example an ether or ester derivative, preferably an ester derivative, as described herein below.
  • the starch ester may be a mixed ester, i.e. having different kinds of ester groups attached to the same molecule, as are obtained for example by reaction of starch with a mixed acid anhydride or a mixture of different acid anhydrides.
  • a mixed acid anhydride may be for example an acid anhydride made from acetic acid and propionic acid; a mixture of different acid anhydrides may be for example a mixture of acetic acid anhydride and propionic acid anhydride.
  • the degree of substitutior (DS) of the starch derivative of item (a) is preferably . tween CM and 3.0, preferably about 0.8 to about 2.1 and most preferably from about 0.8 to about 1.5.
  • the equilibrium moisture content at . about 25°C and at a relative humidity of about 50% is preferably less than about 12% by weight of the moistened starch derivative.
  • the compound (item b of the composition) may be present in the composition in an amount of up to about 10% by weight with respect to that of the total composition.
  • the at least one component present in the compound may have between about 3 and about 25 carbon atoms, and may comprise between 1 and about 10 carboxyl groups and between 1 and about 10 hydroxyl groups. In a particularly preferred embodiment of the compound, at least two such components are present, at least one of which may be alicyclic and comprise a methanoazulene ring.
  • a preferred embodiment of the present invention includes a composition comprising item (a) and item (b) as defined above, and item (c) - viz at least one polymer selected from the group consisting of hydrophilic and/or hydrophobic polymers. Item (a) and item (b) and optionally item (c) when combined provide a composition which yields products with enhanced transparency.
  • composition may contain further additives.
  • the present invention refers to compositions comprising the combination, under conditions sufficient to ensure uniform melt formation, of: (a) starch and/or a starch derivative, and (b) at least one compound which comprises at least one component having a molecular weight of less than 2,000 and which has at least one carboxyl group and at least one hydroxyl group.
  • the present invention relates to finished articles made from said compositions or said melts.
  • the present invention refers to the use of a compound which comprises at least one component having a molecular weight of less than 2,000 and which has at least one carboxyl group and at least one hydroxyl group as a processing aid in the manufacture of a composition
  • a composition comprising (a) a starch and/or a derivative of a starch, and optionally (c) one or more compounds selected from the group consisting of hydrophilic and/or hydrophobic polymers.
  • compositions according to the present invention may be powdery mixtures of their components or in the form of a melt or in the form of solid shaped articles or, for example, in pre-extruded forms such as granulates or pellets.
  • compositions When in the form of a melt, the compositions may be further processed into shaped articles by use of any known process, such as: injection molding, compression molding, filming, blow molding, vacuum forming, thermoforming, extrusion, co- extrusion, foaming, and combinations thereof.
  • the present invention further refers to a method of preparation of a melt of a composition according to this invention, comprising:
  • compositions comprising the combination, under conditions sufficient to ensure uniform melt formation, of: (a) starch and/or a starch derivative, and (b) at least one compound which comprises at least one component having a molecular weight of less than 2,000 and which has at least one carboxyl group and at least one hydroxyl group.
  • the present invention also refers to compositions comprising the combination, under conditions sufficient to ensure uniform melt formation, of (a) a starch and/or a derivative of a starch, (b) at least one compound which comprises at least one component having a molecular weight of less than 2,000 and which has at least one carboxyl group and at least one hydroxyl group, and (c) at least one polymer selected from the group consisting of hydrophilic and/or hydrophobic polymers.
  • the starch which is present in the composition of the present invention is of vegetable origin and may be obtained, for example, from potatoes, rice, tapioca, corn, pea, rye, oats, wheat, maize and barley.
  • the starch has an amylose content, by weight, of up to about 65%, more preferably of up to about 45%, and most preferably between about 30% about 35%.
  • the lower limit for the amylose content of the starch preferably is about 10 to about 15%, likewise by weight.
  • the starch is a high amylose variety having an amylose content, by weight, of between about 70% and about 95%, and more preferably of between about 75% and about 85%.
  • Item (a) may also be a derivative of a starch whereby the starch to be derivatized may be obtained for example from potatoes, rice, tapioca, corn, pea, rye, oats, and/or wheat.
  • Said derivative of starch may have an amylose content, by weight, of up to about 65%, more preferably of up to about 45%, and most preferably between about 30% about 35%.
  • the lower limit for the amylose content of the starch derivative preferably is about 10 to about 15%, likewise by weight.
  • the starch from which the derivative is obtained is a high amylose starch having an amylose content, by weight, of between about 70% and about 95%, preferably between about 75% and about 85%.
  • Item (a) of the composition when in the form of a starch derivative, may be an ether or ester, and preferably is an ester derivative.
  • the starch ester may be a mixed ester comprising at least two different types of alkylcarbonyl groups (i.e. of different lengths) in the same molecule and as such may be of the kind as obtained by reaction of starch with a mixed anhydride or with a mixture of different acid anhydrides.
  • such mixed starch esters comprise at least two members selected from the group consisting of acetate, propionate, butyrate, pentanoate, hexanoate, heptanoate and octanoate residues bound to a common starch molecule.
  • Particularly preferred starch diesters comprise both acetate and propionate groups or both acetate and butyrate groups or both propionate and butyrate groups or both pentanoate and butyrate groups bound to a common starch molecule.
  • the ratio of the types of ester groups comprised by the starch ester may vary greatly, but preferably is in the range of about 1:1 to about 1:20.
  • ether derivatives are alkyl ethers or hydroxyalkylethers of starch, such as the methyl ether, propyl ether, butyl ether, hydroxyethyl ether or hydroxypropyl ether wherein the starch is substituted to a degree of about 0.1 to about 3, and preferably is substituted to a degree of between 0.1 and 2.1.
  • ester derivatives are the methyl esters, butyl esters or propyl esters of starch wherein the starch is substituted to a degree of about 0.1 to about 2.1.
  • Particularly preferred are the ester derivatives of starch such as the acetates and propionates, and most particularly preferred are the starch propionates.
  • the degree of substitution (DS) of the starch is from about 0.1 to about 2.1.
  • Preferred is a DS of about 0.5 to about 1.8, and preferably from about 0.8 to about less than 1.5 which preferably is 1.4.
  • the preferred DS for starch acetates is from about 0.7 to about 1.8 and most preferred is a DS of from about 0.9 to about 1.5.
  • the preferred DS for starch propionates is from about 0.5 to about 1.6 and preferably from about 0.7 to about 1.4.
  • the compound (item b) may be present in the composition in an amount of up to 10% by weight with respect to that of the total composition, and more preferably is likewise present in an amount of between about 1% and 5%.
  • the compound is most preferably present in the composition in an amount of about 2 to 3% by weight with respect to that of the total composition.
  • the at least one component present in the compound may have the general formula: A(OH) y (COOH) z ; wherein: A is a saturated or unsaturated aliphatic or alicyclic moiety comprising at least 3 and preferably less than about 25 carbon atoms; y is greater than or equal to 1 and less than or equal to about 10; and- z is greater than or equal to 1 and less than or equal to about 10.
  • A comprises from about 10 to about 20 carbon atoms, and it is more preferred that it comprises from about 11 to about 15 carbon atoms.
  • the component may comprise 2 or more hydroxyl groups and/or two or more carboxyl groups. It is more preferred that the component comprises 2 or 3 hydroxyl and 2 or 3 carboxyl groups, and it is most preferred that the sum of the carboxyl and hydroxyl groups in the compound does not exceed about 8, being typically between about 4 and about 6.
  • Suitable such components include lactic acid, citric acid, 2-hydroxy valeric acid, 2-hydroxy caprylic acid, 16-hydroxy palmitic acid; 9,10-dihydroxy palmitic acid; 9,10-dihydroxy stearic acid; 2,3-dihydroxy stearic acid; 2-hydroxy stearic acid; 3-hydroxy stearic acid; 10-hydroxy stearic acid; 11- hydroxy stearic acid; 12-hydroxy stearic acid; and 9,10,12-trihydroxy stearic acid.
  • at least two components are present, each of which may have a molecular weight of from about 100 to about 1000.
  • At least one of the components present in the compound may be alicyclic.
  • Such an alicyclic component may comprise a methanoazulene ring.
  • the compound comprises dodecahexanoic acid, such as aleuritic acid, and an hydroxylated-methanoazulene-containing carboxylic acid, such as shellolic acid, jalaric acid or laksholic acid, and preferably a mixture of such compounds.
  • a compound which comprises shellolic acid and aleuritic acid is shellac, obtainable from MHP Shellac GmbH of Repsoldstrasse 4, D- 2000, Hamburg, Germany. Where shellac is present in the composition as item (b) it is preferred that it is substantially 100% micronised and possesses an average particle size of below about 80um.
  • composition according to this invention may further comprise in an amount of up to 50%, and preferably up to 30% by weight of the total composition one or more compounds selected from the group consisting of hydrophilic polymers.
  • hydrophilic polymers includes water-soluble and/or water-swellable polymers.
  • This group includes a large number of known polymers such as water-soluble celluloses such as: alkylcelluloses, hydroxyalkylcelluloses and hydroxyalkylalkylcelluloses, such as: methylcellulose, hydroxymethylcellulose, hydroxyethylcellulose, hydroxypropylcellulose, hydroxy- ethylmethylcellulose, hydroxypropylmethylcellulose, hydroxybutylmethylcellulose, cellulose esters and hydroxyalkylcellulose esters such as: cellulose acetylphthalate (CAP) , Hydroxypropylmethyl-cellulose (HPMCP) ; carboxyalkylcelluloses, carboxyalkyl-a- lkylcelluloses, carboxyalkylcellulose esters such as: carboxymethylcellulose and their alkali-metal salts; water-soluble or water-swellable synthetic polymers such as: poly(acrylic acids) and their salts and essentially water soluble poly(acrylic acid) esters, poly(methacrylic acids) and their salts and essentially water-soluble poly
  • the alkenol homopolymer is preferably a polyvinyl alcohol which has a degree of hydrolysis of from about 80 mol% to about 100 mol% and preferably from about 88 mol% to about 99 mol% and most preferably from about 96 mol% to about 98 mol%.
  • the number average molecular weight ranges preferably are from about 15,000 to about 250,000, and more preferably from about 26,000 to about 120,000. Most preferred is a molecular weight ranging from about 40,000 to about 80,000.
  • the composition contains pre-treated polyvinyl alcohol in the form of a melt, obtained previously by adding sufficient energy to polyvinyl alcohol to melt it and substantially eliminate crystallinity in the melt. It is particularly preferred that such crystallinity is substantially completely eliminated.
  • Alkenol copolymers as mentioned above are preferably synthetic copolymers containing vinyl alcohol units as well as aliphatic units as are obtained by copolymerization of vinyl esters, preferably vinyl acetate with monomers preferably ethylene, propylene, isobutylene and/or styrene with subsequent partial or complete hydrolysis of the vinyl ester group. These polymers comprise a sufficient hydroxyl group content such that they remain at least water- swellable within the definition as given herein.
  • composition according to this invention may further comprise in an amount up to 60 %, preferably in an amount up to 35% and most preferably in an amount up to 25% by weight of the total composition one or more hydrophobic thermoplastic polymers as item (c) , which is a substantially water-insoluble thermoplastic polymer.
  • Such a water-insoluble polymer dissolves in water in an amount of less than 25 grams per 100 grams of the dry polymer, preferably in an amount of less than 15 grams per 100 grams of dry polymer when immersed in water at room temperature.
  • thermoplastic polymers examples include polyolefines, such as polyethylene, polyisobutylenes, polypropylenes, vinylpolymers such as poly(vinyl chloride) , poly(vinyl acetates), polystyrenes; polyacrylonitriles; polyvinylcarbazoles; substantially water-insoluble poly(acrylic acid) esters or poly(methacrylic acid) esters; polyacetals (POM); polycondensates such as polyamides, thermoplastic polyesters, polycarbonates, polyurethanes, poly(alkylene terephthalates) ; polyarylethers; thermo ⁇ plastic polyimides; but also poly(hydroxybutyrate) (PHB) , poly(hydroxybutyrate-co-hydroxyvalerate) and high molar-mass, substantially water-insoluble poly(alkylene oxides) such as polymers of ethylene oxide and propylene oxide as well as their copolymers are included.
  • POM poly(hydroxybutyrate)
  • thermoplastic copolymers of the different kinds known such as ethylene/vinyl acetate-copolymers (EVA) ; ethylene/vinyl alcohol-copolymers (EVOH) ; ethylene/ethyl acrylate-copolymers (EEA) ; ethylene- acrylic acid copolymers (EAA) ; ethylene/methyl acrylate-copolymers (EMA); ABS - copolymers; sty- rene/acrylonitrile-copolymers (SAN) ; as well as their mixtures.
  • EVA ethylene/vinyl acetate-copolymers
  • EVA ethylene/vinyl alcohol-copolymers
  • EAA ethylene/ethyl acrylate-copolymers
  • EAA ethylene- acrylic acid copolymers
  • EAA ethylene/methyl acrylate-copolymers
  • EMA ethylene/methyl acrylate-copolymers
  • ABS - copolymers sty- ren
  • hydrophobic thermoplastic polymers are those with a set processing temperature within the range of about 95°C to about 210°C, preferably within the range of about 95°C to about 190°C.
  • polymers containing polar groups such as hydroxyl, ether-, acid, ester or urethane groups.
  • Such polymers include, for example, copolymers of ethylene, propylene or isobutylene such as ethylene/vinyl acetate-copolymers (EVA) , ethylene/vinyl alcohol-copolymers, ethylene/ ethyl acrylatecopolymers (EEA) , ethylene/methacrylate- copolymers (EMA) , polyure- thane-copolymers, styrene/acrylonitrile-copolymers (SA ⁇ ) ; polyacetals (POM) and their mixtures as mentioned above.
  • the synthetic polymer may contain the usual known additives for processing.
  • the composition according to the present invention may have a relatively low water content.
  • Said water content is preferably below 15%, more preferably below 12% and most preferably below 8% by weight of the total composition. Accordingly, if necessary, the moisture content of the composition is reduced either before mixing the components or during the melt formation process. It is possible for example to initiate melt formation of the composition in a vented extruder and to evaporate the moisture from the melt by vacuum just before the melt is extruded.
  • the present invention further refers to a method of preparation of a melt of a composition according to this invention, comprising:
  • Item (a) may be mixed with item (b) and optionally with item (c) and further additives as defined herein in any desired sequence. It is preferred to mix all the components of the composition with all the intended additives to form the final composition, which may then be heated to form a uniform melt. Of course, other sequences , may be more appropriate.
  • compositions according to the invention are mixed together in a form as to obtain a free flowing powder, which is useful for continuous processing.
  • This powder is fed to the hopper of an extruder and is processed to form a melt which may subsequently be dried.
  • the melt may then be either granulated or further processed into shaped articles.
  • it is suitably heated in a screw and barrel of an extruder for a time sufficient to enable uniform melt formation.
  • the temperature is preferably within the range of 100°C to 220°C, and more preferably within the range of from 160 to 200°C, the precise temperature being dependent up on the type and nature of the composition used.
  • the composition preferably is heated in an extruder, and preferably in a vented extruder for optionally drying the composition as explained above.
  • Pressures created in such a volume correspond to the vapour pressure of the most volatile material present which may be water at the used temperature. It will be appreciated that pressures may be applied or generated, as is known to be possible in the use of said screw and barrel.
  • the preferred applied and/or generated pressures are in the range of pressures which occur in extrusion and are known per se,being up to about 150 x 10 5 N/m , preferably up to about 75 x 10 5 N/m 2 and most preferably up to about 50 x 10 5 N/m 2 .
  • the granular mixture is heated to a temperature which is generally within the range of about 120 to 220°C, preferably within the range of about 120 to 190°C and most preferably within the range of about 130 to 190°C.
  • the minimum pressures under which the melts are formed correspond to the vapour pressures produced by the compositions at said temperatures. These pressures are recommended even if a substantially anhydrous composition is used. Ranges of pressures suitable for extrusion processes are from zero to about 150 x 10 5 N/m 2 , preferably from zero to about 75 x 10 ⁇ N/m 2 and most preferably from zero to about 50 x 10 5 N/m 2 . ressures used in injection molding may exceed 150 x 10 ⁇ N/m 2 .
  • the composition comprises at least one member selected from the group consisting of extenders, fillers, lubricants, mold release agents, other plasticisers, flame- retardants, stabilisers and colouring agents.
  • extenders are gelatin, vegetable proteins such as sunflower protein, soybean proteins, cotton seed proteins, peanut proteins or rape seed proteins. Such extenders may optionally be added in any desired amount up to and including 20 %, preferably within the range of 3 % to 10 % based on the total weight of the composition.
  • Suitable fillers include, for example, oxides of magnesium, aluminum, silicon, and titanium.
  • the fillers are present in the composition at a concentration of up to about 20% by weight, and preferably between about 3.0 and about 10%, by weight, based on the total weight of the composition.
  • the lubricants include stearates of aluminum, calcium, magnesium, and tin, as well as the free acid and magnesium silicate, silicones and substances such as lecithin, and mono and diglycerides, which for the purpose of the present invention function in like manner.
  • the particularly preferred lubricants are stearic acid or lecithin, which are present in the composition in amounts of up to 3%, preferably in an amount of 1%, and most preferably are present in the composition in an amount 0.6% by weight with respect to that of the composition.
  • plasticisers include low molecular weight poly(alkylene oxides), such as, for example, poly(ethylene glycols), poly(propylene glycols) , poly(ethylene-propylene glycols) , such as, for example, glycerol; pentaerythritol; propylene glycol; sorbitol; sodium diethylsulfosucc ate; phosphatides of which lecithin is preferred.
  • plasticisers are preferably present in the composition at a concentration of between about 0.5% and about 15% by weight, and more preferably between about 0.5% and about 5% by weight, based on the weight of all of the components, including the water therein.
  • the sum of all the plasticisers in the composition does not exceed about 25% by weight, and most preferably does not exceed about 20% by weight, based on the total weight of the composition.
  • composition may further comprise flame retardants which, for example, comprise phosphorous, sulphur and halogens, or mixtures thereof.
  • Suitable phosphorous-containing flame retardants include diethyl-N,N-bis (2-hydroxyethyl) aminomethyl phosphonate; dimethyl methylphosphonate; phosphonic acid, methyl-, dimethylester, polymer with oxirane and phosphorous oxide; aliphatic phosphate/phosphonate oligomers; tributyl phosphate; triphenyl phosphate; tricresyl phosphate; 2- ethylhexyl diphenyl phosphate; and tributoxyethyl phosphate. These retardants are available from Akzo Chemicals Inc. of 300 South Riverside Plaza, Chicago, Illinois, USA.
  • phosphorous-containing retardants include: guanidinium phosphate which can be obtained from Chemie Linz GmbH of St Peter strasse 25, A-4021, Linz, Austria; (hydroxypropyl) sec.butyl phosphine oxide which can be obtained from the Chemical Products Group of FMC Corporation, 2000 Market Street, Philadelphia, Pennsylvania 19103, USA; and the following compounds obtainable from Albright and Wilson, Americas Inc, of P.O.
  • polypropoxylated dibutyl pyrophosphoric acid a mixture of phosphonic acid, methyl- , (5-ethyl-2-methyl-1,3,2-dioxaphosphorinan-5-yl)methyl ethyl ester., P-oxide and phosphonic acid, methyl-, bis [(5- ethyl-2-methyl-l,3,2-dioxaphosphorinan-5-yl)methyl] ester, P,P -dioxide as sold under the trade name Amgard V19; ammonium polyphosphate; ethylendiamine polyphosphate; melamine phosphate; dimelamine phosphate; and microencapsulated red phosphorous.
  • ammonium polyphosphate and ethylendiamine polyphosphate are used as flame retardants, it is preferred that they are buffered with disodium orthophosphate so that they are thereby less corrosive to the equipment used for processing the composition comprising them.
  • Suitable sulphur containing-retardants include: guanidinium sulfate obtainable from Chemie Linz GmbH at the address given above; ammonium sulfate; ammonium sulfamate; and tetrakis (hydroxymethyl) phosphonium sulfate; all of which may be obtained from the American Cyanamid Company, of One Cyanamid Plaza, Wayne, New Jersey, 07470, USA.
  • the particularly preferred flame retardants are ammonium polyphosphate and/or ethylenediamine polyphosphate, guanidinium phosphate, ammonium sulphate and/or guanidinium sulfate.
  • the above mentioned flame retardants are present in the composition in an amount of from 0.5 to about 15%, preferably from about 1.5 to 8%, and most preferably from 2 to 5%, all percentages being by weight with -'•spect to that of the total composition.
  • Stabilisers include antioxidants such as thiobisphenols, alkylidenbisphenols, secondary aromatic amines; stabilisers against photo-decomposition, such as, for example, uv absorbers and quenchers; hydroperoxide decomposers; free radical scavengers, and anti-microbial agents.
  • Colouring agents include known azo dyes, organic or inorganic pigments, or colouring agents of natural origin.
  • Inorganic pigments are preferred, such as the oxides of iron or titanium, these oxides being present in the composition at a concentration of between about 0.01 and about 10% by weight, and preferably present at a concentration of between about 0.05 and about 3% by weight, based on the total weight of the composition.
  • Most preferably the colouring agents are present in the composition in an amount of about 0.03 to about 0.07% by weight with respect to the total composition.
  • Still further substances which may be added to the composition include animal or vegetable fats, preferably in their hydrogenated forms, especially those which are solid at room temperature.
  • Such fats preferably have a melting point of at least 50 °C and include triglycerides of C12-, C14-, C16-and C18- fatty acids.
  • the total concentration of said fats, mono-, di- glycerides and phosphatides may be up to 5% by weight, based on the total weight of the composition.
  • Still further compounds which may be added to, or present in the composition include boron-containing compounds, particularly so when the composition is formed into films, sheets or fibres. The presence of such compounds in the composition yields articles which have improved transparency. Young's modulus and tear strength.
  • the preferred boron-containing compounds are boric acid, metaboric acid, alkali and alkaline earth metal salts, borax and derivatives thereof. Said compounds may be present in the composition in an amount of between 0.002 and 0.4%, by weight with respect to that of the composition, and preferably are present at a concentration of between about 0.01 and 0.3%, likewise by weight.
  • Inorganic salts of alkali or alkaline earth metals may be additionally present in the composition in an amount of between 0.1 and 5% by weight with respect to that of the total composition.
  • the presence of such salts in the composition still further improves the Young's modulus, transparency and tear strength of articles made from the composition.
  • compositions according to this invention form thermoplastic melts on heating under conditions as described herein.
  • Such melts can be processed like conventional thermoplastic materials, using, for example, injection molding, blow molding, extrusion and coextrusion (rod, pipe and film extrusion) , compression molding, to produce known articles.
  • the articles include bottles, sheets, films, packaging materials, pipes, cups, rods, laminated films, sacks, bags, pharmaceutical capsules, granules or powders.
  • compositions according to this invention may also be used as carrier materials for active substances, and may be mixed with active ingredients such as pharmaceuticals and/or agriculturally active compounds s h as insecticides or pesticides for sustained release applications of these ingredients.
  • active ingredients such as pharmaceuticals and/or agriculturally active compounds s h as insecticides or pesticides for sustained release applications of these ingredients.
  • the resulting extruded materials can be granulated or worked to fine powders.
  • the thus adjusted starch is fed into the entry port of a twin screw extruder (Leistritz model LSM 34) having screws co-rotating in a horizontal cylindrical barrel and an outlet die mounted at the discharge end of the extruder, opposite its entry port.
  • the starch composition is then heated to a temperature of between 160 and 180°C for about 20 to 120 seconds at a suitable pressure necessary to avoid the formation of water vapour at said temperature.
  • the pelletized melted starch mix is conditioned to a moisture content of about 12%, and then fed into the entry port of an injection molding machine suitable for the production of tensile test pieces.
  • Said test pieces are injection molded at a pressure is 1,300 bar, and temperature of 175°C.
  • the thus molded test piece has a hazy appearance.
  • Example 1 is repeated except that shellac is added to the starch composition in an amount of 2% by weight with respect to that of the starch. Test pieces similar to those of Example 1 are produced but at a lower injection molding pressure of 950 bar. The thus produced test piece has a slightly hazy appearance in comparison with that obtained for the test piece from Example 1.
  • Example 2 is repeated except that the shellac is added to the starch composition in an amount of 8% by weight with respect to that of the starch.
  • Test pieces similar to those of Example 1 are produced at an injection molding pressure of 500 bar. The thus produced test piece has a slightly hazy appearance in comparison with that obtained for the test piece from Example 1.
  • Examples 1 to 3 are repeated except that the maize starch is replaced by starch acetate wherein the degree of substitution is between 1 and 1.4. Results similar to those of Examples 1-3 are obtained.
  • the presence of the shellac in the starch blend thus enables articles to be injection molded therefrom at pressures lower than those required in the absence of the shellac for a constant temperature.
  • articles may be injection molded from the starch compositions comprising shellac at a relatively reduced temperature. This capacity to blend the starch compositions under less energetic conditions is especially advantageous when the starch compositions contains relatively heat labile components, such as flame retardants.
  • Example 5 From Example 5 it can be seen that easily de-moldable articles having good dimensional stability are produced when the water content of the composition is relatively low, but only if the injection molding pressure is relatively high (1250 bar) .
  • Example 7 of the Table it can be seen from Example 7 of the Table, however, that the addition of shellac to the composition enables the preparation at relatively low pressures (950 bar) of injection molded articles which are easily de-molded, have a low water content and which exhibit good dimensional stability.
PCT/US1993/002821 1992-03-31 1993-03-26 Biodegradable polymer compositions WO1993020140A1 (en)

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PCT/US1993/002821 WO1993020140A1 (en) 1992-03-31 1993-03-26 Biodegradable polymer compositions

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WO1994014886A1 (de) * 1992-12-19 1994-07-07 Metraplast H. Jung Gmbh Zusammensetzung für einen werkstoff, insbesondere für eine spritzgussmasse
WO1995033450A1 (en) * 1994-06-07 1995-12-14 Alko Group Ltd. Starch acetate composition with modifiable properties, method for preparation and usage thereof
DE4424419A1 (de) * 1994-07-12 1996-01-18 Naturalis Ag Verfahren zum Herstellen von kompostierbaren Formkörpern aus vorwiegend pflanzlichen Rohstoffen und Komponentengemisch hierfür
EP1321264A1 (de) * 2001-12-17 2003-06-25 Wolfram Lihotzky-Vaupel Verfahren zur Herstellung von Granulat
EP1321279A1 (de) * 2001-12-17 2003-06-25 Wolfram Lihotzky-Vaupel Verfahren zur Extrusion sowie dadurch herstellbarer Formkörper
WO2003051613A1 (de) * 2001-12-17 2003-06-26 Hb-Feinmechanik Gmbh Co Kg Verfahren zur herstellung von formkörpern
WO2008071712A1 (en) * 2006-12-12 2008-06-19 Novamont S.P.A. Biodegradable material for injection molding and articles obtained therewith
EP2046885A1 (de) * 2006-08-04 2009-04-15 Plantic Technologies Limited Abformbares biologisch abbaubares polymer
US8435354B2 (en) 2005-10-11 2013-05-07 The Procter & Gamble Company Water stable compositions and articles comprising starch and methods of making the same
KR20160040201A (ko) * 2013-08-05 2016-04-12 토르시투라 파다나 에스.피.에이. 방염 특성을 갖는 셀룰로스 기재 및 관련 제조 방법
EP3359469B1 (de) 2016-02-01 2019-04-10 Norbert Kuhl Sauerstoffdichter lebensmittelbehälter
DE202018106080U1 (de) * 2018-10-24 2020-01-27 Andreas Lübcke Trinkhalm

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US5656292A (en) * 1994-06-07 1997-08-12 Alko Group Ltd. Composition for pH dependent controlled release of active ingredients and methods for producing it

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WO1992014782A1 (en) * 1991-02-20 1992-09-03 Novamont S.P.A. Biodegradable polymeric compositions based on starch and thermoplastic polymers

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EP0344118A2 (de) * 1988-05-26 1989-11-29 Warner-Lambert Company Polymerzusammensetzung
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Cited By (24)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO1994014886A1 (de) * 1992-12-19 1994-07-07 Metraplast H. Jung Gmbh Zusammensetzung für einen werkstoff, insbesondere für eine spritzgussmasse
WO1995033450A1 (en) * 1994-06-07 1995-12-14 Alko Group Ltd. Starch acetate composition with modifiable properties, method for preparation and usage thereof
US5667803A (en) * 1994-06-07 1997-09-16 Oy Polymer Corex Kuopio Ltd. Starch acetate composition with modifiable properties, method for preparation and usage thereof
DE4424419A1 (de) * 1994-07-12 1996-01-18 Naturalis Ag Verfahren zum Herstellen von kompostierbaren Formkörpern aus vorwiegend pflanzlichen Rohstoffen und Komponentengemisch hierfür
EP1321264A1 (de) * 2001-12-17 2003-06-25 Wolfram Lihotzky-Vaupel Verfahren zur Herstellung von Granulat
EP1321279A1 (de) * 2001-12-17 2003-06-25 Wolfram Lihotzky-Vaupel Verfahren zur Extrusion sowie dadurch herstellbarer Formkörper
WO2003051613A1 (de) * 2001-12-17 2003-06-26 Hb-Feinmechanik Gmbh Co Kg Verfahren zur herstellung von formkörpern
WO2003051597A1 (de) * 2001-12-17 2003-06-26 Wolfram Lihotzky-Vaupel Verfahren zur herstellung von granulat
WO2003051607A1 (de) * 2001-12-17 2003-06-26 Wolfram Lihotzky-Vaupel Verfahren zur extrusion sowie dadurch herstellbarer formkörper
EP1338405A1 (de) * 2001-12-17 2003-08-27 Wolfram Lihotzky-Vaupel Verfahren zur Herstellung von Formkörpern aus natürlichen Polymeren
US8435354B2 (en) 2005-10-11 2013-05-07 The Procter & Gamble Company Water stable compositions and articles comprising starch and methods of making the same
EP2046885A4 (de) * 2006-08-04 2012-02-29 Plantic Technologies Ltd Abformbares biologisch abbaubares polymer
EP2046885A1 (de) * 2006-08-04 2009-04-15 Plantic Technologies Limited Abformbares biologisch abbaubares polymer
US8697245B2 (en) 2006-08-04 2014-04-15 Plantic Technologies Ltd. Mouldable biodegradable polymer
WO2008071712A1 (en) * 2006-12-12 2008-06-19 Novamont S.P.A. Biodegradable material for injection molding and articles obtained therewith
US8809423B2 (en) 2006-12-12 2014-08-19 Novamont S.P.A. Biodegradable material for injection molding and articles obtained therewith
KR20160040201A (ko) * 2013-08-05 2016-04-12 토르시투라 파다나 에스.피.에이. 방염 특성을 갖는 셀룰로스 기재 및 관련 제조 방법
KR102255811B1 (ko) 2013-08-05 2021-05-25 토르시투라 파다나 에스.피.에이. 방염 특성을 갖는 셀룰로스 기재 및 관련 제조 방법
EP3359469B1 (de) 2016-02-01 2019-04-10 Norbert Kuhl Sauerstoffdichter lebensmittelbehälter
EP3411436B1 (de) 2016-02-01 2019-09-18 Norbert Kuhl Sauerstoffdichter kunststoff, verfahren zur herstellung, verwendung und daraus hergestelltes verpackungsmaterial
EP3597565A1 (de) 2016-02-01 2020-01-22 Martin Wassmer Sauerstoffdichter kunststoff und daraus hergestelltes verpackungsmaterial
US11578200B2 (en) 2016-02-01 2023-02-14 Norbert Kuhl Oxygen-tight food container
US11753536B2 (en) 2016-02-01 2023-09-12 Norbert Kuhl Oxygen-tight plastic, and packaging material produced therefrom
DE202018106080U1 (de) * 2018-10-24 2020-01-27 Andreas Lübcke Trinkhalm

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