WO1991015542A1 - Starch-based degradable plastic containing polypropylene glycol - Google Patents

Starch-based degradable plastic containing polypropylene glycol Download PDF

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Publication number
WO1991015542A1
WO1991015542A1 PCT/US1991/002361 US9102361W WO9115542A1 WO 1991015542 A1 WO1991015542 A1 WO 1991015542A1 US 9102361 W US9102361 W US 9102361W WO 9115542 A1 WO9115542 A1 WO 9115542A1
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starch
average
ppg
sample
degradable plastic
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PCT/US1991/002361
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French (fr)
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John S. Peanasky
John M. Long
Richard P. Wool
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Agri-Tech Industries, Inc.
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Publication of WO1991015542A1 publication Critical patent/WO1991015542A1/en

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    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/06Polyethene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • 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
    • C08L3/02Starch; Degradation products thereof, e.g. dextrin
    • 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
    • C08L2205/00Polymer mixtures characterised by other features
    • C08L2205/03Polymer mixtures characterised by other features containing three or more polymers in a blend
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815Copolymers of ethene with aliphatic 1-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/12Polypropene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L71/00Compositions of polyethers obtained by reactions forming an ether link in the main chain; Compositions of derivatives of such polymers
    • C08L71/02Polyalkylene oxides

Definitions

  • This invention relates generally to plastics and, more particularly, to degradable plastics containing starch and polyethylene with selected additives for producing enhanced mechanical properties.
  • Plastic products make up a substantial proportion of the solid wastes that are disposed of each year.
  • FIGURE 1 is a graph showing the percentage of accessed starch, as determined through acid hydrolysis, versus the volume percentage of starch in various
  • FIGURE 2 is a graph of average tensile modulus versus volume percent of polypropylene glycol (PPG) for several experimental samples containing starch,
  • FIGURE 3 is a graph of average yield stress versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weights
  • FIGURE 4 is a graph of average ultimate stress versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weights
  • FIGURE 5 is a graph of average elongation to break versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weights.
  • FIGURE 6 is a graph of average fracture energy versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weiglits
  • FIGURE 7 is a graph representation of tensile modulus for various samples containing starch and PPG in combination with high density polyethylene (HDPE), linear low density polyethylene (LLDPE) or polypropylene (PP).
  • HDPE high density polyethylene
  • LLDPE linear low density polyethylene
  • PP polypropylene
  • FIGURE 8 is a graph representation of yield stress for various samples containing starch and PPG in combination with HDPE, LLDPE or PP.
  • FIGURE 9 is a graph representation of ultimate stress for various samples containing starch and PPG in combination with HDPE, LLDPE or PP.
  • FIGURE 10 is a graph representation of elongation to break for varrious samples containing starch, PPG and HDPE, LLDPE or PP.
  • FIGURE 11 is a graph representation of fracture energy for various samples containing starch, PPG and HDPE, LLDPE or PP.
  • FIGURE 12 is a graph of change in mass/initial mass versus time for various samples used in a soil degradation study of samples containing polyethylene, starch and PPG.
  • FIGURE 13 is a graph of concentration of components (s) to C-O stretch band versus time for various samples used in the soil degradation study.
  • PPG polypropylene glycol
  • blended starch and polyethylene compounds exhibit measurably improved
  • the starch concentration comprises roughly 30% or more, by volume, of the starch and polyethylene blend (hereinafter all percentages will be by volume unless specifically indicated). It is believed that the 30% concentration represents a critical and surprising "percolation threshold" at which the starch forms a fully connected substructure within a given starch and polyethylene component. This results in a majority of the starch in the manufactured component being accessible to bioorganisms and environmental chemical action. This level of starch leads further to more rapid degradation than would occur at concentrations below the percolation threshold where a fully connected starch lattice does not normally exist.
  • the percolation threshold of approximately 30% starch has been experimentally verified through acid hydrolysis techniques. The results of this verification are illustrated graphically in FIG. 1. As shown therein, the percentage of accessible starch, as determined through acid hydrolysis techniques, increases sharply between substantially 20% and 36% starch, with substantially 50% of the starch being accessible at a starch concentration of approximately 30%.
  • the preferred concentration of PPG is between about 1 and 3% by volume. This range of concentration achieves the desired improvement in physical properties without exhibiting the characteristics of excess PPG loading, such as an odor and oily feel. It will be appreciated that known ultra violet degradation enhancers can also be added to enhance degradation of the compounds in the presence of ultra violet light.
  • PPG lubricants in starch-containing polyethylene compounds to achieve unique mechanical properties has been demonstrated through experiment (see Example) .
  • the benefits derived from the use of PPG and its lubricating effects are observed in a wide range of PE/starch formulations.
  • the use of PPG appears to be most beneficial in PE/starch compounds having starch
  • PPG has been shown to be the critical starch level for significant biodegradability.
  • the use of PPG provides useful, flexible materials containing high starch levels and that are suitable for the manufacture of a wide range of plastic products with greatly enhanced biodgradability.
  • Examples 1 through 8 verify the existence of the percolation threshold through acid hydrolysis techniques.
  • low density polyethylene (LDPE) supplied by Quantum Chemical Company was mixed with cornstarch, supplied by Cargill Inc., in starch concentrations ranging from 5 to 60 volume
  • each of these samples was refluxed in hydrochloric acid.
  • the color of the solution was noticeably amber, indicating the presence of hydroxymethylfuranose formed through acid hydrolysis of the starch component of each sample, the acid solution was replaced with fresh solution. This process was repeated over a period of 24 to 72 hours until no visually
  • This sample consisted of 95% polyethylene and 5% starch.
  • the percentage of accessible starch as determined through acid hydrolysis was approximately 5%.
  • This sample consisted of 85% polyethylene and 15% starch.
  • the percentage of accessible starch as determined through acid hydrolysis was approximately 4%.
  • This sample consisted of 75% polyethylene and 25% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 14%.
  • This sample consisted of 70% polyethylene and 30% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 35%.
  • This sample consisted of 65% polyethylene and 35% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 76%.
  • This sample consisted of 50% polyethylene and 50% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 96%.
  • Tare weights of the starch and PE were measured using the Mettler Balance. PPG was added to the tared starch using the transfer pipette.
  • the PE was introduced to the mixing bowl of the Brabender Plasti-Corder at 140°C and 60rpm and allowed to melt. Once melting was achieved, as determined by having reached a peak torque value, the starch/PPG mixture was added.
  • Torque and temperature data were recorded for each run using the Brabender software and were stored on disk in CPM format.
  • the data on the CPM disks were read usiny the uniform-PC software in an IBM PC/AT and stored in DOS ASCII format.
  • the plates were compression molded in window frame molds (4 inches by 4 inches) using the Carver Press operating at a temperature of 140°C. Molding runs
  • Dogbone samples were cut for tensile tests using the ASTM D-412 half size cutting die. The thickness of the samples was measured with a micrometer using the method described by ASTM D-638. Thickness among the samples varied from 1.8 milJimeters to 2.2 millimeters. All samples were placed in the grips of the MTS 812 at room temperature and elongated at a rate of 5 millimeters per minute. Data were collected using an IBM analog to digital data acquisition board and stored in DOS ASCII format. For each sample, the tensile modulus (PSI), yield stress (PSI), ultimate stress (PSI), elongation to break and fracture energy were determined.
  • PSI tensile modulus
  • PSI yield stress
  • PSI ultimate stress
  • elongation to break and fracture energy were determined.
  • This sample consisted of 100% Chemplex 3404B LDPE and served as a control. This sample exhibited an average modulus of 14844, and average yield stress of 1108, an average ultimate stress of 1608, an average elongation to break of 6.10 and an average fracture energy of 8038.
  • This sample exhibited an average modulus of 7613.28, and average yield stress of 464.10, an average ultimate stress of 592.35, and average elongation to break of 1.744 and an average fracture energy of 912.61.
  • This sample exhibited an average modulus of 5147.54, and average yield stress of 316.90, an average ultimate stress of 473.37, and average elongation to break of 2.10 and an average fracture energy of 867.76.
  • This sample exhibited an average modulus of 14371.41, and average yield stress of 537.23, an average ultimate stress of 610.5591, and average elongation to break of 1.32 and an average fracture energy of 750.88.
  • This sample consisted of 35% Chemplex 3404B LDPE, 63% potato starch and 2% Aldrich 20,233-9 PPG having a molecular weight of 2000.
  • the resulting sample exhibited an average modulus of 2716.94, and average yield stress of 173.71, an average ultimate stress of 271.25, an average elongation to break of 1.31 and a fracture energy of
  • This sample consisted of 35% Chemplex 3404B LDPE, 63% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425.
  • the resulting sample exhibited an average modulus of 2813.54, and average yield stress of 180.72, an average ultimate stress of 284.22, an average elongation to break of 1.61 and a fracture energy of
  • This sample consisted of 40% Chemplex 3404B LDPE, 58% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425.
  • the resulting sample exhibited an average modulus of 3599.19, and average yield stress of 250.36, an average ultimate stress of 357.82, an average elongation to break of 1.56 and a fracture energy of
  • This sample consisted of 60% Chemplex 3404B LDPE, 38% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425.
  • the resulting sample exhibited an average modulus of 6542.78, and average yield stress of 530.08, an average ultimate stress of 611.88, an average elongation to break of 1.15 and a fracture energy of
  • This sample consisted of 50% Chemplex 3404B LDPE, 48% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425.
  • the resulting sample exhibited an average modulus of 4746.73, an average yield stress of 341.76, an average ultimate stress of 481.21, an average elongation to break of 1.70 and a fracture energy of
  • This sample consisted of 25% cornstarch in combination with 75% Chemplex 3404B LDPE.
  • the resulting sample exhibited an average modulus of 14170, and average yield stress of 739, and average ultimate stress of 942, and average elongation to break of 2.57 and an average fracture energy of 2279.
  • This sample consisted of 40% cornstarch in combination with 60% Chemplex 3404B LDPE.
  • the resulting sample exhibited an average modulus of 22539, and average yield stress of 653, and average ultimate stress of 665, and average elongation to break of .738 and an average fracture energy of 448.
  • This sample consisted of 65% cornstarch in combination with 65% Chemplex 3404B LDPE.
  • the resulting sample was too brittle to be cut into dog bones and hence could not be tested for mechanical properties.
  • This sample consisted of 25% potato starch in combination with 75% Chemplex 3404B LDPE.
  • the resulting sample exhibited an average modulus of 10540, and average yield stress of 773, and average ultimate stress of 855, and average elongation to break of 1.19 and an average fracture energy of 936.
  • This sample consisted of 40% potato starch in combination with 60% Chemplex 3404B LDPE.
  • the resulting sample exhibited an average modulus of 9626, and average yield stress of 510, and average ultimate stress of 650, and average elongation to break of 1.34 and an average fracture energy of 798.
  • This sample consisted of 65% potato starch in combination with 35% Chemplex 3404B LDPE.
  • the resulting sample exhibited an average modulus of 6840, and average yield stress of 187, and average ultimate stress of 311, and average elongation to break of 1.15 and an average fracture eneryy of 324.
  • Texaco Jeffamine M-2070 a monofunctional copolymer of predominentaly PEG with some PPG and having a molecular weight of 2070.
  • This sample was prepared using 60% Chemplex 3404B LDPE, 39% cornstarch and 1% Dow voranol 235-044 (3800 MW) .
  • This sample exhibited an average modulus of 8931, an average yield stress of 442, an average ultimate stress of 600, an average elongation to break of 1.47 and an average fracture energy of 801.
  • This sample was prepared using 60% Chemplex 3404B LDPE, 39% cornstarch and 1% Dow voranol 222-056(2000 MW). This sample exhibited an average modulus of 8652, an average yield stress of 433, an average ultimate stress of 605, an average elongation to break of 1.47 and an average fracture energy of 801.
  • This sample was prepared using 60% Chemplex 3404B LDPE, 37% cornstarch and 3% Dow voranol 222-056(2000 MW). This sample exhibited an average modulus of 6712, an average yield stress of 407, an average ultimate stress of 576, an average elongation to break of 1.42 and an average fracture energy of 728.
  • This sample was prepared using 60% Chemplex 3404B LDPE, 39% cornstarch and 1% Dow voranol 232-023(7200 MW). This sample exhibited an average modulus of 10116, an average yield stress of 497, an average ultimate stress of 626, an average elongation to break of 1.58 and an average fracture energy of 911.
  • This sample was prepared using 60% Chemplex 3404B LDPE, 37% cornstarch and 3% Dow voranol 232-023(720 MW). This sample exhibited an average modulus of 7380, an average yield stress of 375, an average ultimate stress of 570, an average elongation to break of 1.50 and an average fracture energy of 761.
  • This sample was prepared usiny 40% high density polyethelyene (Olin 506 supplied by Dow Chemical) in combination with 60% cornstarch. A mixing temperature of 160°C was used to compensate for the higher melting point of the HDPE relative to the LDPE used in the earlier examples.
  • This sample which contained no PPG and hencer served as a control exhibited an unmeasurable modulus, a yield stress of 850, an ultimate stress of 906, an
  • This sample was prepared using 40% HDPE (Olin 506), 58% cornstarch and 2% aldrich 20,230-4 PPG having a molecular weight of 425.
  • the mixing temperature was 160°C, and the resulting sample exhibited a modulus of 10584, a yield stress of 487, an ultimate stress of 653, an elongation to break of 5.2 and a fracture energy of 3003.
  • This sample was prepared using 40% linear low density polyeththylene (Norlin GA 502-010 M8NN26) and 60% cornstarch. The sample was mixed at 160°C to compensate for the higher melting point of LLDPE relative to LDPE. The resulting sample, which served as a control, exhibited a modulus of 19680, a yield stress of 596, an ultimate stress of 631, an elongation to break of 2.97 and a fracture energy of 1396.
  • This sample was prepared using 40% polypropylene (T.O. plastics 109-2050-250) and 60% cornstarch. The sample was mixed at 200°C to compensate for the higher melting point of PP relative to LDPE. The resulting sample, which served as a control, exhibited an
  • This sample was prepared using 40% PP (T.O.
  • plastics 109-2050-250 plastics 109-2050-250), 58% cornstarch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425.
  • the sample was mixed at 200°C and exhibited a modulus of 13673, a yield stress of 605, an ultimate stress of 807, an
  • Soils were obtained from farmland top-soil in March before planting. They were sifted with 1/8" screen to remove clumps, plant debris and macroorganisms. The soil, at a depth of three inches, was placed in a plastic box measuring 15"xl0"x6.5", which was lined with stanless steel cloth to allow air circulation. The soils were kept moist but not wet with deionized water and stored in a room at ambient temperature (70-78F) and humidty
  • This environment provides a broad variety of fungi and bacteria to permit aerobic degradation of anturally biodegradable materials in a reasonalbe time frame, typically less than 1 year.
  • Thin films (1-3 mils) of plastic material were buried in a 4x5 array at a depth of 2 inches. Samples were removed once per month for evaluation of mass change and Fourier Transform Infra Red (FTIR) spectroscopic analysis of chemical changes.
  • FTIR Fourier Transform Infra Red
  • Figure 12 shows the mass change as a function of time of burial in soils up to 200 days for each of the samples A, B and C. Rapid degradation occured for the satrch containing samples in the first 50 days when about 40% of the weight was lost and proceeded more slowly thereafter.
  • the PPG containing material exhibited a slightly faster rate initially and degraded at about the same rate as the starch and LDPE material.
  • the control material, pure PE, showed a slight decrease in mass.

Abstract

A degradable plastic which contains starch and polypropylene glycol. High starch percentages can be combined with conventional plastics, such as polyethylene, by using polypropylene glycol to produce biodegradable materials with enhanced mechanical properties for the plastic product.

Description

STARCH-BASED DEGRADABLE PLASTIC
CONTAINING POLYPROPYLENE GLYCOL SPECIFICATION BACKGROUND OF THE INVENTION
This invention relates generally to plastics and, more particularly, to degradable plastics containing starch and polyethylene with selected additives for producing enhanced mechanical properties.
Plastic products make up a substantial proportion of the solid wastes that are disposed of each year.
Because many plastics degrade extremely slowly, plastics disposal is a major problem, particularly in advanced, consumer oriented societies.
One possible solution to the plastic disposal problem lies in the development of naturally degradable plastics. Various proposed formulations for degradable plastics are based on the mixture of polyethylene with cornstarch. Although such mixtures can show greatly enhanced degradability over pure polyethylene, this often is obtained at the expense of other important mechanical properties, such as strength and flexibility. As a general rule, compositions containing a higher percentage of starch degrade faster than compositions containing less starch. However, higher starch concentrations tend to exhibit substantially reduced strength and flexibility, thereby limiting their usefulness. At present, there exists no starch and polyethylene based plastic that exhibits a good balance of meaningful degradability in combination with useful and practical mechanical
properties.
In view of the foregoing, it is a general object of the present invention to provide a new and improved starch-based degradable plastic.
It is a further object of the present invention to provide a starch-based degradable plastic and method of manufacture that exhibits meaningful degradability in combination with useful and practical mechanical
properties.
It is a still further object of the present invention to provide a starch-based degradable plastic having the degradability characteristics of a high starch concentration compound in combination with the strength and flexibility characteristics of a low starch
concentration compound.
BRIEF DESCRIPTION OF THE DRAWINGS
The features of the present invention which are believed to be novel are set forth with particularity in the appended claims. The invention, together with the further objects and advantages thereof, may best be understood by reference to the following description taken in conjunction with the accompanying drawings wherein like reference numerals identify like elements, and wherein:
FIGURE 1 is a graph showing the percentage of accessed starch, as determined through acid hydrolysis, versus the volume percentage of starch in various
starch/polyethylene mixtures.
FIGURE 2 is a graph of average tensile modulus versus volume percent of polypropylene glycol (PPG) for several experimental samples containing starch,
polyethylene and PPGs of various molecular weights.
FIGURE 3 is a graph of average yield stress versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weights
FIGURE 4 is a graph of average ultimate stress versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weights
FIGURE 5 is a graph of average elongation to break versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weights.
FIGURE 6 is a graph of average fracture energy versus volume percent PPG for various samples containing polyethylene, starch and PPGs of various molecular weiglits
FIGURE 7 is a graph representation of tensile modulus for various samples containing starch and PPG in combination with high density polyethylene (HDPE), linear low density polyethylene (LLDPE) or polypropylene (PP).
FIGURE 8 is a graph representation of yield stress for various samples containing starch and PPG in combination with HDPE, LLDPE or PP.
FIGURE 9 is a graph representation of ultimate stress for various samples containing starch and PPG in combination with HDPE, LLDPE or PP.
FIGURE 10 is a graph representation of elongation to break for varrious samples containing starch, PPG and HDPE, LLDPE or PP.
FIGURE 11 is a graph representation of fracture energy for various samples containing starch, PPG and HDPE, LLDPE or PP.
FIGURE 12 is a graph of change in mass/initial mass versus time for various samples used in a soil degradation study of samples containing polyethylene, starch and PPG.
FIGURE 13 is a graph of concentration of components (s) to C-O stretch band versus time for various samples used in the soil degradation study.
DESCRIPTION OF THE PREFERRED EMBODIMENT
In one aspect of the present invention there is provided a degradable plastic compound blended from
polyethylene (PE), starch and polypropylene glycol (PPG) in liquid form as an interfacial additive. It is believed that the PPG acts as an interfacial lubricant which
lubricates contact points between starch and starch, starch and PE, as well as between PE and PE. This results in degradable plastics that have relatively high starch concentrations but that nevertheless exhibit improved strength and flexibility characteristics compared with similar compounds lacking the critical interfacial additive. Additional details and examples of the
advantage of the PPG type additive will be described hereinafter. As used herein, "relatively high" starch concentrations are those that result in commercially significant improvement in degradation characteristics as compared against materials containing substantially pure polyethylene.
In accordance with another aspect of the invention, it has been determined that blended starch and polyethylene compounds exhibit measurably improved
degradation characteristics when the starch concentration comprises roughly 30% or more, by volume, of the starch and polyethylene blend (hereinafter all percentages will be by volume unless specifically indicated). It is believed that the 30% concentration represents a critical and surprising "percolation threshold" at which the starch forms a fully connected substructure within a given starch and polyethylene component. This results in a majority of the starch in the manufactured component being accessible to bioorganisms and environmental chemical action. This level of starch leads further to more rapid degradation than would occur at concentrations below the percolation threshold where a fully connected starch lattice does not normally exist.
The percolation threshold of approximately 30% starch has been experimentally verified through acid hydrolysis techniques. The results of this verification are illustrated graphically in FIG. 1. As shown therein, the percentage of accessible starch, as determined through acid hydrolysis techniques, increases sharply between substantially 20% and 36% starch, with substantially 50% of the starch being accessible at a starch concentration of approximately 30%.
In accordance with the invention related to PPG additive, it has been discovered that the addition of the PPG to the blended starch and polyethylene results in a noticeable improvement in a balance of the properties of strength and flexibility of the resulting compound.
Without being limited in the scope of the claims, it is believed that, without the presence of PPG, the lack of adhesion between the polyethylene and the starch results in the ready formation of microvoids at the poles of the starch granules when the combined starch and PE undergoes uniaxial extension. As the extension increases, the microvoids coalesce until the material fails. As the starch concentration is increased and approaches the percolation threshold, the microvoids coalesce at lower extensions in proportion to the size of an invading cluster representing the accessible starch. Accordingly, when complete connectivity through the material is achieved by increasing starch concentration to the
percolation threshold, the strength and flexibility of the material deteriorates. A nonlimiting explanation is that the addition of PPG retards the coalescence of these voids by lubrication. In the final stages of deformation prior to material failure, crack initiation and crack growth may be delayed via an energy dissipation mechanism aided by the presence of PPG.
The substantial, beneficial effects of the addition of PPG have been observed at starch concentration as high as 63% by volume. In addition, the beneficial effects of the addition of PPG have been observed at PPG levels as low as at least 0.5% by volume. The beneficial effects of the addition of PPG have also been observed at PPG concentrations as great as 10% by volume although it is believed that PPG concentrations in excess of 3% by volume merely result in an excess of PPG with little corresponding improvement in overall mechanical
properties. The preferred concentration of PPG is between about 1 and 3% by volume. This range of concentration achieves the desired improvement in physical properties without exhibiting the characteristics of excess PPG loading, such as an odor and oily feel. It will be appreciated that known ultra violet degradation enhancers can also be added to enhance degradation of the compounds in the presence of ultra violet light.
Various polypropylene glycols having molecular weights between 403 and 5000 have been investigated. The addition of PPG substantially enhanced the physical properties of the starch and polyethylene blend. For example, compounds which contained no PPG and could not even survive being cut into dogbone samples, could, with the addition of as little as 0.5% PPG be cut into such samples and tested.
In addition to PPG, various related copolymers of PPG and polyethylene glycol (PEG), as well as PPGs having ends capped with PEG, have been investigated as
additives.
In addition to low density polyethylene, the efficacy of PPG as an additive in starch-based degradable compositions has also been demonstrated in compositions containing high density polyethylene (HDPE), linear low density polyethylene (LDPE) and polypropylene (PP) in place of LDPE.
The use of PPG lubricants in starch-containing polyethylene compounds to achieve unique mechanical properties has been demonstrated through experiment (see Example) . The benefits derived from the use of PPG and its lubricating effects are observed in a wide range of PE/starch formulations. The use of PPG appears to be most beneficial in PE/starch compounds having starch
concentrations above the percolation threshold level of approximately 30 volume percent. This percolation
threshold has been shown to be the critical starch level for significant biodegradability. The use of PPG provides useful, flexible materials containing high starch levels and that are suitable for the manufacture of a wide range of plastic products with greatly enhanced biodgradability.
Further features, advantages and characteristics of the invention are demonstrated in the examples that follow. These examples are meant to be illustrative of the inventions and are not intended to limit the scope thereof .
EXAMPLES
Verification Of Percolation Threshold
The following Examples 1 through 8 verify the existence of the percolation threshold through acid hydrolysis techniques. In these examples, low density polyethylene (LDPE) supplied by Quantum Chemical Company was mixed with cornstarch, supplied by Cargill Inc., in starch concentrations ranging from 5 to 60 volume
percent. The fractional volume of starch p, in these blends was determined using the formula,
p = 1/[1 + yqs/xqp] where x and y are the weight fractions of starch and PE, and qs and qp are the densities of starch and PE, respectively. The density of starch was determined using pycnometry. Melt blending was performed in a Brabender Data Processing Plasti-Corder Model PL2000 with a 350cc capacity mixing head attachment. Samples were mixed at 140°C and 60rpm for 30 minutes. The blends were then compression molded into plates of thickness 0.05-0.2 inches using 5 inch by 5 inch window frame molds. Samples were cut from this plate using an ASTM D-412c (D-638IV) half size dogbone cutter.
Following preparation, each of these samples was refluxed in hydrochloric acid. When the color of the solution was noticeably amber, indicating the presence of hydroxymethylfuranose formed through acid hydrolysis of the starch component of each sample, the acid solution was replaced with fresh solution. This process was repeated over a period of 24 to 72 hours until no visually
detectable color change in the solution was noted. The samples were then removed to deionized water for about 72 hours. The water solution was changed every 6 to 5 hours. The samples were then placed under vacuum in an oven at 60°C for another 72 hours, and then removed to a dessicator under vacuum for two months. At the end of two months, a final weight was obtained. The loss of weight experienced by each sample provides an indication of the accessable starch in each sample.
EXAMPLE ONE
This sample consisted of 95% polyethylene and 5% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 5%.
EXAMPLE TWO
This sample consisted of 85% polyethylene and 15% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 4%.
EXAMPLE THREE
This sample consisted of 75% polyethylene and 25% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 14%.
EXAMPLE FOUR
This sample consisted of 70% polyethylene and 30% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 35%.
EXAMPLE FIVE
This sample consisted of 67.5% polyethylene and
32.5% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 58%.
EXAMPLE SIX
This sample consisted of 65% polyethylene and 35% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 76%.
EXAMPLE SEVEN
This sample consisted of 60% polyethylene and 40% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 94%. EXAMPLE EIGHT
This sample consisted of 50% polyethylene and 50% starch. The percentage of accessible starch as determined through acid hydrolysis was approximately 96%.
Examples Including Addition of PPG
The following examples demonstrate the efficacy of PPG in significantly improving the strength and flexibility characteristics of blended polyethylene and starch.
A number of samples containing various
combinations of starch, polyethylene and PPG were prepared and tested. For each combination, a total of six samples were prepared and tested for tensile (Young's) modulus, yield stress, ultimate stress, elongation to break and fracture energy. The various combinations, and the average test result data for the combinations are
summarized in Tables 1, 2, and 3 below.
Figure imgf000012_0001
Figure imgf000013_0001
Figure imgf000014_0001
The following material processing equipment, raw materials and data processing equipment and software were used in preparing and testing the samples:
Material Processing Equipment Used:
1. Mettler Balance Model PM4600
2. Pasteur Transfer Pipettes, 5.75 inch
3. Brabender Data Processing Plasti-Corder Model PL2000 350cm Cubed Mixing Head with Roller Blades
4. Brabender Data Processing Plasti-Corder
Model PL331 350cm Cubed Mixing Head with roller Blades
5. Carver Laboratory Hotpress Model M25
6. Custom Scientific Instrument Half Size Dogbone Cutter, ASTM D-412c (D-638IV)
7. MTS 812 Series with Hydraulically
Driven Actuator
Raw Materials:
1. LDPE Chemplex 3404B
2. Unmodified cornstarch from Cargill
Corporation
3. Food grade potato starch from Western Polymer Corp.
4. Aldrich 20, 230-4 PPG-Molecular weight 425
5. Aldrich 20, 232-0 PPG-Molecular weight 1000
6. Aldrich 20, 233-9 PPG-Molecular weight 2000
Data Processing Equipment and Software:
1. IBM PC/AT
2. IBM PS2 Model 80
3. HP7475A Six Pen Plotter 4. Uniform-PC from Micro Solutions
Computer Products
5. Graphing equipment computer software
from Golden Software, Inc.
Each of the samples was prepared as follows:
Tare weights of the starch and PE were measured using the Mettler Balance. PPG was added to the tared starch using the transfer pipette.
The PE was introduced to the mixing bowl of the Brabender Plasti-Corder at 140°C and 60rpm and allowed to melt. Once melting was achieved, as determined by having reached a peak torque value, the starch/PPG mixture was added.
Mixing continued for 15 minutes and a plateau torque and temperature was achieved a few minutes after loading the raw materials. The blends were then removed from the mixing head attachment and cut into pieces
approximately 1/4 inch in diameter using scissors. The resulting "pellets" were wrapped in aluminum foil and set aside for a minimum of two days before molding into plates.
Torque and temperature data were recorded for each run using the Brabender software and were stored on disk in CPM format. The data on the CPM disks were read usiny the uniform-PC software in an IBM PC/AT and stored in DOS ASCII format.
The plates were compression molded in window frame molds (4 inches by 4 inches) using the Carver Press operating at a temperature of 140°C. Molding runs
consisted of a 450 second heating period, and a 450 second molding period at 20,000 pounds force (1300 PSI0). After the molding period, the press was cooled to room
temperature prior to releasing slowly the pressure. The plastic was removed from the molds using a utility knife.
Dogbone samples were cut for tensile tests using the ASTM D-412 half size cutting die. The thickness of the samples was measured with a micrometer using the method described by ASTM D-638. Thickness among the samples varied from 1.8 milJimeters to 2.2 millimeters. All samples were placed in the grips of the MTS 812 at room temperature and elongated at a rate of 5 millimeters per minute. Data were collected using an IBM analog to digital data acquisition board and stored in DOS ASCII format. For each sample, the tensile modulus (PSI), yield stress (PSI), ultimate stress (PSI), elongation to break and fracture energy were determined.
Some of the more notable combinations shown in
Tables 1, 2, and 3 are discussed in greater detail below:
EXAMPLE NINE
This sample consisted of 100% Chemplex 3404B LDPE and served as a control. This sample exhibited an average modulus of 14844, and average yield stress of 1108, an average ultimate stress of 1608, an average elongation to break of 6.10 and an average fracture energy of 8038.
EXAMPLE TEN
This sample was prepared using 75% Chemplex
3404B LDPE, 23% cornstarch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. This sample exhibited an average modulus of 9809, an average yield stress of 1029, an average ultimate stress of 1036, an average elongation to break of 1.39 and an average fracture energy of 1252.
EXAMPLE ELEVEN
This sample was prepared using 60% Chemplex
3404BH LDPE, 35% cornstarch and 5% Aldrich 20,232-0 PPG having a molecular weight of 1000. This sample exhibited an average modulus of 7613.28, and average yield stress of 464.10, an average ultimate stress of 592.35, and average elongation to break of 1.744 and an average fracture energy of 912.61.
EXAMPLE TWELVE
This sample was prepared using 60% Chemplex
3404B LDPE, 30% cornstarch and 10% Aldrich 20,232-0 PPG having a molecular weight of 1000. This sample exhibited an average modulus of 6963.99, and average yield stress of 478.30, an average ultimate stress of 586.52, and average elongation to break of 1.24 and an average fracture energy of 646.61.
EXAMPLE THIRTEEN
This sample was prepared using 50% Chemplex
3404B LDPE, 48% cornstarch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. This sample exhibited an average modulus of 5147.54, and average yield stress of 316.90, an average ultimate stress of 473.37, and average elongation to break of 2.10 and an average fracture energy of 867.76.
EXAMPLE FOURTEEN
This sample was prepared using 60% Chemplex
3404B LDPE, 39.5% cornstarch and 0.5% Aldrich 20,230-9 PPG having a molecular weight of 2000. This sample exhibited an average modulus of 14371.41, and average yield stress of 537.23, an average ultimate stress of 610.5591, and average elongation to break of 1.32 and an average fracture energy of 750.88.
The following examples demonstrate the efficacy of PPG as an additive in starch and polyethylene blends containing a starch other then cornstarch. In the
following examples, potato starch was used.
EXAMPLE FIFTEEN
This sample consisted of 35% Chemplex 3404B LDPE, 63% potato starch and 2% Aldrich 20,233-9 PPG having a molecular weight of 2000. The resulting sample exhibited an average modulus of 2716.94, and average yield stress of 173.71, an average ultimate stress of 271.25, an average elongation to break of 1.31 and a fracture energy of
300.66.
EXAMPLE SIXTEEN
This sample consisted of 35% Chemplex 3404B LDPE,
61.5% potato starch and 3.5% Aldrich 20,233-9 PPG having a molecular weight of 2000. The resulting sample exhibited an average modulus of 2393.66, and average yield stress of 156.94, an average ultimate stress of 243.97, an average elongation to break of 1.05 and a fracture energy of
215.30.
EXAMPLE SEVENTEEN
This sample consisted of 35% Chemplex 3404B LDPE, 63% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The resulting sample exhibited an average modulus of 2813.54, and average yield stress of 180.72, an average ultimate stress of 284.22, an average elongation to break of 1.61 and a fracture energy of
388.01,
EXAMPLE EIGHTEEN
This sample consisted of 60% Chemplex 3404B LDPE,
38% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The resulting sample exhibited an average modulus of 8690.58, and average yield stress of 600.95, an average ultimate stress of 639.02, an average elongation to break of 1.28 and a fracture energy of
767.44.
EXAMPLE NINETEEN
This sample consisted of 40% Chemplex 3404B LDPE, 58% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The resulting sample exhibited an average modulus of 3599.19, and average yield stress of 250.36, an average ultimate stress of 357.82, an average elongation to break of 1.56 and a fracture energy of
481.60.
EXAMPLE TWENTY
This sample consisted of 60% Chemplex 3404B LDPE, 38% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The resulting sample exhibited an average modulus of 6542.78, and average yield stress of 530.08, an average ultimate stress of 611.88, an average elongation to break of 1.15 and a fracture energy of
636.80. EXAMPLE TWENTY-ONE
This sample consisted of 50% Chemplex 3404B LDPE, 48% potato starch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The resulting sample exhibited an average modulus of 4746.73, an average yield stress of 341.76, an average ultimate stress of 481.21, an average elongation to break of 1.70 and a fracture energy of
715.66.
The following examples consist of polyethylene in combination with starch without the addition of any PPG additive. These examples serve as controls to demonstrate the effectiveness of the PPG additive.
EXAMPLE TWENTY-TWO
This sample consisted of 25% cornstarch in combination with 75% Chemplex 3404B LDPE. The resulting sample exhibited an average modulus of 14170, and average yield stress of 739, and average ultimate stress of 942, and average elongation to break of 2.57 and an average fracture energy of 2279.
EXAMPLE TWENTY-THREE
This sample consisted of 40% cornstarch in combination with 60% Chemplex 3404B LDPE. The resulting sample exhibited an average modulus of 22539, and average yield stress of 653, and average ultimate stress of 665, and average elongation to break of .738 and an average fracture energy of 448.
EXAMPLE TWENTY-FOUR
This sample consisted of 65% cornstarch in combination with 65% Chemplex 3404B LDPE. The resulting sample was too brittle to be cut into dog bones and hence could not be tested for mechanical properties.
EXAMΓLE TWENTY-FIVE
This sample consisted of 25% potato starch in combination with 75% Chemplex 3404B LDPE. The resulting sample exhibited an average modulus of 10540, and average yield stress of 773, and average ultimate stress of 855, and average elongation to break of 1.19 and an average fracture energy of 936.
EXAMPLE TWENTY-SIX
This sample consisted of 40% potato starch in combination with 60% Chemplex 3404B LDPE. The resulting sample exhibited an average modulus of 9626, and average yield stress of 510, and average ultimate stress of 650, and average elongation to break of 1.34 and an average fracture energy of 798.
EXAMPLE TWENTY-SEVEN
This sample consisted of 65% potato starch in combination with 35% Chemplex 3404B LDPE. The resulting sample exhibited an average modulus of 6840, and average yield stress of 187, and average ultimate stress of 311, and average elongation to break of 1.15 and an average fracture eneryy of 324.
Addition of PPG And PEG Copolymers and
PEG Capped PPGS
The following examples demonstrate the efficacy of, copolymers of PPG and PEG, and the efficacy of PPGs having ends capped with PEG, in improving the strength and flexiblity characteristics of blended polyethylene and starch.
In the examples that follow, the following additives were utilized:
1. Dow Voranol 235-044, a trifunctional copolymer of PPG and PEG having a molecular weight of 3800.
2. Texaco Jeffamine M-2070, a monofunctional copolymer of predominentaly PEG with some PPG and having a molecular weight of 2070.
3. Dow Voranol 222-056, a PEG end capped PPG copolymer having a homogeneous backbone and a
molecular weight of 2000. Between 10 and 20% of the chains are capped with ethylene oxide rather polypylene oxide. 4. Dow Voranol 232-023, a trifunctional additive having between 10 and 20% of the chains capped with ethylene oxide and having a molecular weight of 7200.
The samples considered in the following examples were prepared and tested according to the procedures utilized in connections with Examples 9 through 27 above.
EXAMPLE TWENTY-EIGHT
This sample was prepared using 60% Chemplex 3404B LDPE, 39% cornstarch and 1% Dow voranol 235-044 (3800 MW) . This sample exhibited an average modulus of 8931, an average yield stress of 442, an average ultimate stress of 600, an average elongation to break of 1.47 and an average fracture energy of 801.
EXAMPLE TWENTY-NINE
This sample was prepared using 60% Chemplex 3404B
LDPE, 37% cornstarch and 3% Dow voranol 235-044 (3800 MW). This sample exhibited an average modulus of 6858, an average yield stress of 409, an average ultimate stress of 577, an average elongation to break of 1.39 and an average fracture energy of 715.
EXAMPLE THIRTY
This sample was prepared using 60% Chemplex 3404B LDPE, 39% cornstarch and 1% Dow voranol 222-056(2000 MW). This sample exhibited an average modulus of 8652, an average yield stress of 433, an average ultimate stress of 605, an average elongation to break of 1.47 and an average fracture energy of 801.
EXAMPLE THIRTY-ONE
This sample was prepared using 60% Chemplex 3404B LDPE, 37% cornstarch and 3% Dow voranol 222-056(2000 MW). This sample exhibited an average modulus of 6712, an average yield stress of 407, an average ultimate stress of 576, an average elongation to break of 1.42 and an average fracture energy of 728.
EXAMPLE THIRTY-TWO
This sample was prepared using 60% Chemplex 3404B LDPE, 39% cornstarch and 1% Dow voranol 232-023(7200 MW). This sample exhibited an average modulus of 10116, an average yield stress of 497, an average ultimate stress of 626, an average elongation to break of 1.58 and an average fracture energy of 911.
EXAMPLE THIRTY-THREE
This sample was prepared using 60% Chemplex 3404B LDPE, 37% cornstarch and 3% Dow voranol 232-023(720 MW). This sample exhibited an average modulus of 7380, an average yield stress of 375, an average ultimate stress of 570, an average elongation to break of 1.50 and an average fracture energy of 761.
Replacement of LDPE with HDPE,
LLDPE or PP
The beneficial affects of PPG as an additive have also been noted in connection with compounds containing starch in combination with HDPE, LLDPE or PP. Except where specifically noted, the samples considered in the following examples were prepared and tested according to the procedures utilized in connection with examples 9 through 27 above. The results of these studies are shown in FIGS. 7 through 11.
EXAMPLE THIRTY-FOUR
This sample was prepared usiny 40% high density polyethelyene (Olin 506 supplied by Dow Chemical) in combination with 60% cornstarch. A mixing temperature of 160°C was used to compensate for the higher melting point of the HDPE relative to the LDPE used in the earlier examples. This sample, which contained no PPG and hencer served as a control exhibited an unmeasurable modulus, a yield stress of 850, an ultimate stress of 906, an
elongation to break of 0.11 and a fracture energy of 55.
EXAMPLE THIRTY-FIVE
This sample was prepared using 40% HDPE (Olin 506), 58% cornstarch and 2% aldrich 20,230-4 PPG having a molecular weight of 425. The mixing temperature was 160°C, and the resulting sample exhibited a modulus of 10584, a yield stress of 487, an ultimate stress of 653, an elongation to break of 5.2 and a fracture energy of 3003.
EXAMPLE THIRTY-SIX
This sample was prepared using 40% linear low density polyeththylene (Norlin GA 502-010 M8NN26) and 60% cornstarch. The sample was mixed at 160°C to compensate for the higher melting point of LLDPE relative to LDPE. The resulting sample, which served as a control, exhibited a modulus of 19680, a yield stress of 596, an ultimate stress of 631, an elongation to break of 2.97 and a fracture energy of 1396.
EXAMPLE THIRTY-SEVEN
This sample was prepared using 40% LLDPE (Norlin
GA 502-010 M8NN26), 58% cornstarch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The sample was mixed at 160°C and exhibited a modulus of 4116, a yield stress of 238, an ultimate stress of 557, an elongation to break of 6.69 and a fracture energy of 2748.
EXAMPLE THIRTY-EIGHT
This sample was prepared using 40% polypropylene (T.O. plastics 109-2050-250) and 60% cornstarch. The sample was mixed at 200°C to compensate for the higher melting point of PP relative to LDPE. The resulting sample, which served as a control, exhibited an
unmeasurable modulus, a yield stress of 1302, an ultimate stress of 1512, an elongation to break of 0.04 and a fracture energy of 19.
EXAMPLE THIRTY-NINE
This sample was prepared using 40% PP (T.O.
plastics 109-2050-250), 58% cornstarch and 2% Aldrich 20,230-4 PPG having a molecular weight of 425. The sample was mixed at 200°C and exhibited a modulus of 13673, a yield stress of 605, an ultimate stress of 807, an
elongation to break of 1.68 and a fracture energy of 1251. Soil Degradation Studies
Soils were obtained from farmland top-soil in March before planting. They were sifted with 1/8" screen to remove clumps, plant debris and macroorganisms. The soil, at a depth of three inches, was placed in a plastic box measuring 15"xl0"x6.5", which was lined with stanless steel cloth to allow air circulation. The soils were kept moist but not wet with deionized water and stored in a room at ambient temperature (70-78F) and humidty
(37-90%). This environment provides a broad variety of fungi and bacteria to permit aerobic degradation of anturally biodegradable materials in a reasonalbe time frame, typically less than 1 year.
Thin films (1-3 mils) of plastic material were buried in a 4x5 array at a depth of 2 inches. Samples were removed once per month for evaluation of mass change and Fourier Transform Infra Red (FTIR) spectroscopic analysis of chemical changes.
The samples considered in the investigation were as follows:
A: 36% cornstarch; 4% PPG (Registry No. 25322-G9-4); 60% LDPE by volume
B: 40% cornstarch; 60% LDPE
C: 100% LDPE
Figure 12 shows the mass change as a function of time of burial in soils up to 200 days for each of the samples A, B and C. Rapid degradation occured for the satrch containing samples in the first 50 days when about 40% of the weight was lost and proceeded more slowly thereafter. The PPG containing material exhibited a slightly faster rate initially and degraded at about the same rate as the starch and LDPE material. The control material, pure PE, showed a slight decrease in mass.
Figure 13 shows the change of the C-O-C
stretching vibration in the infrared spectrum near
960-1190cm-1. This vibration is largely due to starch but also has other contributions. The results are similar to those of Figure 7. The data suggest that the starch is first removed during the initial rapid degradation (up to 50 days) and that the remaining material degrades more slowly.
While particular embodiments of the
invention has been shown and described, it will be obvious of those skilled in the art that changes and modifications may be made without departing from the invention in its broader aspects, and, therefore, the aim in the appended claims is to cover all such changes and modifications as fall within the true spirit and scope of the invention.

Claims

WE CLAIM :
1. A degradable plastic composition comprising by volume starch, low density polyethylene and at least about 0.5% polypropylene glycol.
2. A degradable plastic composition as defined in Claim 1 wherein said polypropylene glycol comprises substantially 0.5% or more by volume of degradable plastic composition.
3. A degradable plastic composition as defined in Claim 1 wherein said polypropylene glycol comprises between substantially 0.5% and 3.0% by volume of said degradable plastic composition.
4. A degradable plastic composition as defined in Claim 1 wherein said polypropylene glycol has a
molecular weight of substantially 425.
5. A degradable plastic composition as defined in Claim 1 wherein said starch comprises substantially 30% or more by volume of said degradable plastic compound.
6. A degradable plastic compound as defined in Claim 5 wherein said degradable plastic compound contains between substantially 0.5% and substantially 10% by volume of said polypropylene glycol.
7. A degradable plastic composition as defined in Claim 1 wherein said starch is cornstarch.
8. A degradable plastic composition as defined in Claim 1 wherein said starch is potato starch.
9. A degradable plastic composition comprising polyethylene, starch and polypropylene glycol, said starch comprising substantially 30% or more by volume of said composition and said polypropylene glycol comprising substantially 0.5% or more by volume of said composition.
10. A degradable plastic composition as defined in Claim 9 wherein said polypropylene glycol has a
molecular weight of substantially 425.
11. A degradable plastic compound as defined in Claim 9 wherein said degradable plastic compound wherein said polypropylene glycol comprises no more than
substantially 3.0% by volume of said degradable plastic compound.
12. A degradable plastic compound as defined in Claim 11 wherein said starch comprises cornstarch.
13. A degradable plastic compound as defined in Claim 11 wherein said starch comprises potato starch.
PCT/US1991/002361 1990-04-06 1991-04-05 Starch-based degradable plastic containing polypropylene glycol WO1991015542A1 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1074435C (en) * 1999-06-22 2001-11-07 沈阳南阳经贸集团有限公司 Polynary degradable resin composition and its preparation process
CN1074778C (en) * 1997-07-17 2001-11-14 田长澄 Degradeable plastic and plant composite material and its preparation
CN1081203C (en) * 1999-02-11 2002-03-20 天津丹海股份有限公司 Preparation of mother material for biodegradable plastics
CN1114653C (en) * 2000-01-12 2003-07-16 李小鲁 Biologically degradable resin composition and its preparation and application
WO2011081827A1 (en) * 2009-12-30 2011-07-07 Samsin USA, LLC Biodegradable plastic, environmentally friendly cable made therewith, and environmentally friendly headset
CN106167556A (en) * 2016-07-13 2016-11-30 蚌埠市华科机电有限责任公司 A kind of degradable modified plastic particles

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850862A (en) * 1972-07-28 1974-11-26 Union Carbide Corp Blends of a biodegradable thermoplastic dialkanoyl polymer and a naturally occurring biodegradable product
US4218350A (en) * 1977-09-16 1980-08-19 Coloroll Limited Shaped synthetic polymers containing a biodegradable substance
GB2214918A (en) * 1988-02-03 1989-09-13 Warner Lambert Co Polymeric materials made from destructurized starch and at least one synthetic thermoplastic polymeric material

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3850862A (en) * 1972-07-28 1974-11-26 Union Carbide Corp Blends of a biodegradable thermoplastic dialkanoyl polymer and a naturally occurring biodegradable product
US4218350A (en) * 1977-09-16 1980-08-19 Coloroll Limited Shaped synthetic polymers containing a biodegradable substance
GB2214918A (en) * 1988-02-03 1989-09-13 Warner Lambert Co Polymeric materials made from destructurized starch and at least one synthetic thermoplastic polymeric material

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
KIRK-OTHMER, "ENCYCLOPEDIA OF CHEMICAL TECHNOLOGY", Volume 18, Published 1982, by JOHN WILEY AND SONS, See page 633. *

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1074778C (en) * 1997-07-17 2001-11-14 田长澄 Degradeable plastic and plant composite material and its preparation
CN1081203C (en) * 1999-02-11 2002-03-20 天津丹海股份有限公司 Preparation of mother material for biodegradable plastics
CN1074435C (en) * 1999-06-22 2001-11-07 沈阳南阳经贸集团有限公司 Polynary degradable resin composition and its preparation process
CN1114653C (en) * 2000-01-12 2003-07-16 李小鲁 Biologically degradable resin composition and its preparation and application
WO2011081827A1 (en) * 2009-12-30 2011-07-07 Samsin USA, LLC Biodegradable plastic, environmentally friendly cable made therewith, and environmentally friendly headset
US8722775B2 (en) 2009-12-30 2014-05-13 Samsin USA, LLC Environmentally friendly cable
CN106167556A (en) * 2016-07-13 2016-11-30 蚌埠市华科机电有限责任公司 A kind of degradable modified plastic particles

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