WO1989010381A1 - Biologically decomposable composition - Google Patents
Biologically decomposable composition Download PDFInfo
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- WO1989010381A1 WO1989010381A1 PCT/FI1989/000075 FI8900075W WO8910381A1 WO 1989010381 A1 WO1989010381 A1 WO 1989010381A1 FI 8900075 W FI8900075 W FI 8900075W WO 8910381 A1 WO8910381 A1 WO 8910381A1
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- biopolymer
- composition
- synthetic polymer
- starch
- film
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L101/00—Compositions of unspecified macromolecular compounds
Definitions
- the present invention relates to a biologically decomposable composition, comprising a composition consisting of a biopolymer and at least one synthetic polymer, the composition further including a material causing in certain conditions disintegration of the chains of the synthetic polymer and/or the synthetic polymer of the composition having been treated in a manner that the chains of the synthetic polymer disintegrate in certain conditions.
- EP-230143 discloses a synthetic polymer decomposing agent which is sensitive to light.
- the additive disintegrates polyethene chains as the composition is exposed to light.
- polyethylene will be decomposed as it is exposed to the effect of light for a lengthy period of time.
- the above deals particularly with mechanisms for chopping the synthetic polymer in a biologically decompos able composition.
- this can be effected either by means of an additive incorporated in a composition for cutting off in certain conditions the chains of a synthetic polymer or by treating the synthetic polymer itself in a manner that the polymer chains break in certain conditions. It is natural that a combination of the above factors can be utilized.
- the most important reason for these treatments is that certain synthetic polymers, such as polyethylene polymer, do not decompose microbiologically.
- the synthetic polymer surrounds starch particles (biopolymer).
- biopolymer contained therein consists of starch particles which have a relatively large, size and a relatively small reactive surface.
- the large biopolymer particles considerably impair the strength characteristics of a film.
- decomposition of such compounds is very slow because of small active surface area.
- An object of this invention is to provide a biologically decomposable composition which to the maximum extent overcomes the weaknesses of prior known compositions.
- a biologically decomposable composition of the invention is mainly characterized in that the biopolymer is ezymatically modified.
- the advantage gained by the invention can be clearly seen e.g. when the biopolymer used is starch.
- Starch can be enzymatically modified so that the surface of starch particles is only partially hydrolyzed.
- partial hydrolysis on the surface of a particle around he diminishing core develops a dextrine chain layer which has the effect that, in theory, the particle "dissolves" without any boundary surface in a synthetic polymer, such as polyethylene.
- a synthetic polymer such as polyethylene
- the particle size of a biopolymer can be adjusted as desired. In principle, this means that the actual core of a particle diminishes especially when starch is used and around the core there is grown a dextrine chain layer. Thus, the amount of biopolymer in relation to synthetic polymer can be increased without impairing the mechanical properties of a composition. This is due to the fact that the enzymatically modified biopolymer sort of dissolves in synthetic polymer.
- the biopolymer treating enzyme remains as stable on the surface of biopolymer particles in partial hydrolysis. The enzyme is activated by the action of water, whereby the starch dissolves and it is a microbiologically readily available source of energy.
- the enzymatic ally modified biopolymer can be dried so it can be readily mixed within synthetic polymer granulate and extruded into a plastic film.
- one preferred biopolymer is starch.
- An enzymatic modification on starch according to the invention can be preferably effected with alfa-amylase, e.g. ⁇ -1,4 glucan-4 clucan-hydrolase: (E.C. 3.2.1.1.) particularly with heat-resistant alfaamylase.
- alfa-amylase e.g. ⁇ -1,4 glucan-4 clucan-hydrolase: (E.C. 3.2.1.1.) particularly with heat-resistant alfaamylase.
- a characteristic feature of heat-resistant alfa-mylase is that its action activates as temperature is rising and the thermal denaturation of an enzyme protein is very slow as it is bound to substrate (starch).
- the alfa-amylase enzyme remains bound to its substrate as high as at 180oC, i.e. for example at polyethylene film production temperature, for a sufficiently long period of time so as not to be destroyed in the production of film.
- Another preferred biopolymer is cellulose.
- the enzyme used for its enzymatic modification is cellulase, e.g. 1,4- ⁇ -D-glucan cellobiohydrolase: (E.C. 3.2.1.91.), especially a cellulase that form cellodextrines.
- the invention is further illustrated in the accompanying drawing showing diagrammatically the effect of the enzymatic modification of biopolymer particle on the structure of such particle.
- the top of fig. 1 (2) shows biopolymer particles prior to modification and as they would be incorporated e.g. in a film-making process in the prior art solutions.
- the bottom (b) of fig. 1 shows biopolymer particles obtained by enzymatic modification. Both groups of particles are provided with vertical lines on either side thereof for describing the boundary surfaces of e.g. a produced plastic film.
- the biopolymer particle forms in the resulting film a cavity which significantly decreases the overall strength of a film at this point.
- a modified biopolymer particle whose core is relatively small and which consists of members, such as dextrine chains (in the case of starch), branching off the core, does not produce a similar cavity effect on a plastic film and, thus, the strength impairing effect of a biopolymer composition is substantially lesser.
- fig. 1 shows one advantage of the invention, namely the fact, especially when starch is used, the dextrine chains extend at least in certain places all the way to the surface of a film providing for water a kind of capillary duct system directly inside the composition.
- Enzymatically modified rice starch and polyethylene were mixed with each other at a ratio of 1:1.
- This mixture was melt stirred by means of a co-kneeter type of extruder from Buss AG (model MDK/E46 11D; screw length 506 mm; diameter 46 mm; screw temperature from forward end 140°C, 140°C, 140°C, 140°C).
- the melt mix ture of melt polyethylene and modified starch was finally compressed through the orifices (7 orifices, diameter 3 mm) at the end of the extruder and sliced by means of a cutter into a water basin by means of a cutter operating immediately downstream of the orifices and dried to form a master batch granulate.
- biopolymers rice starch, cellulose and modified cellulose
- master batches containing 50 % of biopolymer were used to prepare master batches containing 50 % of biopolymer.
- Film-blowing was effected by means of a Luigi Bandera ⁇ niblock type of 1 -screw film-blowing extruder (screw length 1125 mm; diameter 45 mm; compression ratios 2,57:1 and 2.24:1; nozzle diameter 150 mm; nozzle slit 1 mm).
- the film-blowing conditions were as follows: temperatures from forward end of screw (set values) 130°C, 140°C, 140°C, 140°C, 140°C and 140°C; temperature of melt appr. 160°C; speed of rotation of screw 79 rpm; running speed 8-10 min and,blowing ratio 1.8.
- the above-described film-blowing extruder was used with varying biopolymer additions (1.5 - 6.0 % as dry) to preparepolyethylene films by employing a polyethylene grade whose melt index was 1.2 and density 0.922.
- the thicknesses of such manufactured films varied within the range of 70-90 ⁇ m (tables 1 and 2).
- Table 1 indicates how the enzymatic modification of a biopolymer improves the mechanical strength properties of a film compared with polyethylene having enzymatically unmodified biopolymer added therein.
- a 3 % addition provides a 30 % improvement in tensile strength, 20 % in elongation and appr. 22 % in drop value.
- a film of modified rice starch is 5 um thinner than a film of rice starch (RT).
- the change of particle size due to modification is also clearly seen in table 1 as the mean particle size of starch diminishes to about one fifth of the original.
- the enzymatic modification provides similar improvements.
- the improvement in tensile strength by virtue of modification is appr. 24 %, in elongation nearly 20 % and in drop value more than 20 %.
- the particle size diminishes by virtue of modification to about half from the original.
- EMRT enzymatically modified rice starch
- EMS enzymatically modified cellulose
- the mean particle size of biopolymer is determined with Malvern 2600 device in aqueous phase.
- Table 2 indicates the effect of an increase in the amount of biopolymer on the mechanical strength properties of a polyethylene film.
- modified rice starch provides for mechanically stronger film properties compared to original rice starch (RT).
- the difference between EMRT and RT increases dramatically as the amount of biopolymer in a polyethylene film increases.
- the difference between EMRT and RT varies within the range of 6-12 % in favour of EMRT while a 6 % addition of biopolymer increases the difference in mechanical strength properties to the range of 30-96 % in favour of EMRT.
- modified rice starch When modified rice starch was added in a polyethylene film (1.5 - 6.0 %), its mechanical strength properties were impaired only by 20 % while the similar additions of rice starch impaired the values considerably more, i.e. 60 %.
- KS/PS 300/550 330/610 240/520 350/610 200/370 260/500
- Tests were effected according to ASTM standard, STM G 21-70 1980. The test was effected with 100 ⁇ 80 mm sized test specimens which were incubated in glass Petri dishes (150 ⁇ 150 ⁇ 25 mm) for 4 weeks at 28°C. Sufficient relative air humidity in the incubation space was secured by placing a vessel containing saturated KNO 3 -solution (Rh 92 %) on the incubator floor. The controls used were test specimens that were not sterilized and not treated with mould suspension. The organic nature of mould suspension was checked with standardized test dishes. The mould-formation of plastics was observed at one-week intervals. The test fungi were as follows
- test specimens The mould-formation of test specimens was rated visually and microscopically as follows:
- the enclosed table 3 shows that the mould-formation in a compsition having enzymatically modified rice starch was more vigorous than with a polyethylene film having unmodified rice starch added therein. TABLE 3 The average mould-formation of test specimens
- EMRT enzymatically modified rice starch
- UV photosensitive component
- a biologically decomposable composition of the invention can also be processed into a product by the application of other processes prior known in plastics manufacturing, such as injection moulding, blowing technique, extrusion moulding, vacuum moulding, rotational casting or various foaming techniques.
- plastics manufacturing such as injection moulding, blowing technique, extrusion moulding, vacuum moulding, rotational casting or various foaming techniques.
- the examples deal with blown films for the reason that the manufacturing of a thin-walled film is in technical sense most demanding, particularly in view of the workability of a biologically decomposablw composition.
- plastics manufacturing techniques can be applied which facilitate the manufacturing of an end product at such temperatures that an enzymatically modified biopolymer maintains its characteristics promoting the decomposition of a composition in certain conditions.
- the upper limit temperature range can be considered to be 220-250°C.
- the synthetic polymer comprises polyethylene.
- polyoleophines overall are included in those synthetic polymers that can be employed in a composition of the invention.
- the agents belonging in the group of polyoleophines include e.g. HD-polyethylene, LD-polyethylene and polypropylene.
- polystyrene is a synthetic polymer suitable for a biologically decomposable composition of the invention.
- rice starch provides for the besz comparative results in unmodified form.
- corn starch etc. can be used as a biopolymer of the invention.
- Enzymatic modification makes it possible to reduce their particle size as desired.
- starch it can be said that enzymatic modification provides for such a particle size distribution in which the mean particle size is smaller than 10 ⁇ m.
- cellulose it can be said that enzymatic modification provides for such a particle size distribution in which the mean particle size is smaller than 20 ⁇ m (fig. 1).
Abstract
The invention relates to a biologically decomposable composition, comprising a composition consisting of a biopolymer and a synthetic polymer, the composition further including a material causing in certain conditions disintegration of the chains of the synthetic polymer and/or the synthetic polymer of the composition being treated in a manner that the chains of the synthetic polymer disintegrate in certain conditions. The biopolymer is enzymatically modified.
Description
Biologically decomposable composition
The present invention relates to a biologically decomposable composition, comprising a composition consisting of a biopolymer and at least one synthetic polymer, the composition further including a material causing in certain conditions disintegration of the chains of the synthetic polymer and/or the synthetic polymer of the composition having been treated in a manner that the chains of the synthetic polymer disintegrate in certain conditions.
This type of biologically decomposable composition is disclosed e.g. in GB Patent Specifications 1 487 050, 1 485 833 and in US Patent Specification 4 337 181. In this case, to a biologically decomposable composition is added some self-oxidizing agent containing at least one double-bond which, when contacted with a metal salt, produces reactions as a consequence of which the composition decomposes when placed in the ground. In the cited publication, the biopolymer used is starch. However, the use of starch as set forth in the cited publication is highly unfavourable especially when the purpose is to provide films having a good tensile strength but at the same time biologically decomposable characteristics.
Publication EP-230143 discloses a synthetic polymer decomposing agent which is sensitive to light. The additive disintegrates polyethene chains as the composition is exposed to light. Thus, polyethylene will be decomposed as it is exposed to the effect of light for a lengthy period of time.
The above deals particularly with mechanisms for chopping the synthetic polymer in a biologically decompos
able composition. Thus, this can be effected either by means of an additive incorporated in a composition for cutting off in certain conditions the chains of a synthetic polymer or by treating the synthetic polymer itself in a manner that the polymer chains break in certain conditions. It is natural that a combination of the above factors can be utilized. The most important reason for these treatments is that certain synthetic polymers, such as polyethylene polymer, do not decompose microbiologically. For example, in a composition disclosed in GB Patent Specification 1 485 833, the synthetic polymer surrounds starch particles (biopolymer). A consequence of this is that the organisms decomposing starch particles are not able to make at least a direct contact with starch, since said organisms do not penetrate the layer of synthetic polymer. Thus, the disintegration of the polymer chains of such layer of synthetic polymer is extremely essential, so that the organisms capable of cooperation with biopolymer can make contact with biopolymer. Hence, especially starch particles turn gradually into glucose as a result of microbial actions. The resulted glucose is used by microbes as a source of carbon and energy. The hydrocarbon chains chopped from a synthetic polymer, such as polyethylene, can serve as a source of carbon and energy for the microbes.
Thus, for the above reasons, it is essential to incorporate in a biologically decomposable composition and/ or its synthetic polymer a "triggering" factor which decomposes the synthetic polymer.
A problem with biologically decomposable compositions of the prior art is, however, that the biopolymer contained therein consists of starch particles which have
a relatively large, size and a relatively small reactive surface. When manufacturing plastic films, for example, the large biopolymer particles considerably impair the strength characteristics of a film. In addition, decomposition of such compounds is very slow because of small active surface area.
An object of this invention is to provide a biologically decomposable composition which to the maximum extent overcomes the weaknesses of prior known compositions. In order to accomplish this object, a biologically decomposable composition of the invention is mainly characterized in that the biopolymer is ezymatically modified.
The advantage gained by the invention can be clearly seen e.g. when the biopolymer used is starch. Starch can be enzymatically modified so that the surface of starch particles is only partially hydrolyzed. In partial hydrolysis, on the surface of a particle around he diminishing core develops a dextrine chain layer which has the effect that, in theory, the particle "dissolves" without any boundary surface in a synthetic polymer, such as polyethylene. when such a composition is exposed to conditions favourable to decomposition, the polymer chains of a synthetic polymer disintegrate e.g. as a result of the action of UV-light, whereby the particlly dissolved starch together with pieces of the chains of a synthetic polymer provides a culture medium favourable to microbes. The glucose, which first develops from dextrines in biological suggession, brings over a relatively fast-growing microbism. That collects near the synthetic polymer also other growth factors which, when starch is used up, are also required by those microorganisms which use as their
source of carbon the carbon chains formed from a chopped synthetic polymer. As an example there is shown the following diagram, wherein the biopolymer is enzymatically modified starch and the synthetic polymer is a polyethylene film comprising a structure decomposing it in UV-light
One of the most significant advantages gained by the invention is that by means of enzymatic modification the particle size of a biopolymer can be adjusted as desired. In principle, this means that the actual core of a particle diminishes especially when starch is used and around the core there is grown a dextrine chain layer. Thus, the amount of biopolymer in relation to synthetic polymer can be increased without impairing the mechanical properties of a composition. This is due to the fact that the enzymatically modified biopolymer sort of dissolves in synthetic polymer. The biopolymer treating enzyme remains as stable on the surface of biopolymer particles in partial hydrolysis. The enzyme is activated by the action of water, whereby the starch dissolves and it is a microbiologically readily available source of energy. The enzymatic
ally modified biopolymer can be dried so it can be readily mixed within synthetic polymer granulate and extruded into a plastic film.
As pointed out above, one preferred biopolymer is starch. An enzymatic modification on starch according to the invention can be preferably effected with alfa-amylase, e.g. α-1,4 glucan-4 clucan-hydrolase: (E.C. 3.2.1.1.) particularly with heat-resistant alfaamylase. A characteristic feature of heat-resistant alfa-mylase is that its action activates as temperature is rising and the thermal denaturation of an enzyme protein is very slow as it is bound to substrate (starch). The alfa-amylase enzyme remains bound to its substrate as high as at 180ºC, i.e. for example at polyethylene film production temperature, for a sufficiently long period of time so as not to be destroyed in the production of film.
Another preferred biopolymer is cellulose. The enzyme used for its enzymatic modification is cellulase, e.g. 1,4- β-D-glucan cellobiohydrolase: (E.C. 3.2.1.91.), especially a cellulase that form cellodextrines.
The invention is further illustrated in the accompanying drawing showing diagrammatically the effect of the enzymatic modification of biopolymer particle on the structure of such particle. The top of fig. 1 (2) shows biopolymer particles prior to modification and as they would be incorporated e.g. in a film-making process in the prior art solutions. Furthermore, the bottom (b) of fig. 1 shows biopolymer particles obtained by enzymatic modification. Both groups of particles are provided with vertical lines on either side thereof for describing the boundary surfaces of e.g. a produced
plastic film. As shown in the top figure, the biopolymer particle forms in the resulting film a cavity which significantly decreases the overall strength of a film at this point. On the other hand, a modified biopolymer particle, whose core is relatively small and which consists of members, such as dextrine chains (in the case of starch), branching off the core, does not produce a similar cavity effect on a plastic film and, thus, the strength impairing effect of a biopolymer composition is substantially lesser. Thus, it is possible to produce considerably stronger films with the same amount of biopolymer or to increase the amount of biopolymer without, however, impairing the strength characteristics of a film. In addition, fig. 1 shows one advantage of the invention, namely the fact, especially when starch is used, the dextrine chains extend at least in certain places all the way to the surface of a film providing for water a kind of capillary duct system directly inside the composition.
The following examples illustrate the manufacturing technique of a composition of the invention and results of the tests performed with the composition.
Enzymatic modification of biopolymer
EXAMPLE 1 Partial hydrolysis of starch
At the initial stage of modification 600 g (dry matter) of rice starch was suspended in a cold CaCl2-solution containing 800 mg calcium/1 liter water. pH of the suspension was adjusted to 6,5. Temperature of the suspension was raised to 60ºC with continuous agitation. A high temperature alfa-amylase enzyme produced e.g. by Bacillus licheniformis was added such an amount
in 25 ml that the mean particle size of rice starch decreased within 30 minutes from 30 urn to below 10 μm. Suspension was cooled and cold-dried. The cold-dried enzyme-modified mass was ground e.g. in a mortar. The particle size distribution was determined e.g. with Malvem 2600 device for finding out a sufficient enzyme content.
EXAMPLE 2 Partial hydrolysis of cellulose
For modification, 300 g (dry matter) ofcrystalline cellulose was suspended in cold water. pH of the suspension was adjusted to 4,5. Temperature of the suspension was raised ro 50ºC with continuous stirring. ion. A cellubiohydrolase produced by Trichoderma reesei was added such an amount in 25 ml that the mean particle size of cellulose decreased within 30 minutes from 40 um to below 20 μm Suspension was cooled and cold-dried. The particle size distribution was determined e.g. with Malvem 2600 device for finding out a sufficient enzyme content.
The effect of enzymatic modification on the particle size is illustrated in the accompanying figure 2.
Preparation of biopolymer master batch and filmblowing
Enzymatically modified rice starch and polyethylene (film-blowing grade: melt index 1.8 and density 0.922} were mixed with each other at a ratio of 1:1. This mixture was melt stirred by means of a co-kneeter type of extruder from Buss AG (model MDK/E46 11D; screw length 506 mm; diameter 46 mm; screw temperature from forward end 140°C, 140°C, 140°C, 140°C). The melt mix
ture of melt polyethylene and modified starch was finally compressed through the orifices (7 orifices, diameter 3 mm) at the end of the extruder and sliced by means of a cutter into a water basin by means of a cutter operating immediately downstream of the orifices and dried to form a master batch granulate.
In a similar fashion, the other biopolymers (rice starch, cellulose and modified cellulose) were used to prepare master batches containing 50 % of biopolymer.
Film-blowing was effected by means of a Luigi Bandera ϋniblock type of 1 -screw film-blowing extruder (screw length 1125 mm; diameter 45 mm; compression ratios 2,57:1 and 2.24:1; nozzle diameter 150 mm; nozzle slit 1 mm). The film-blowing conditions were as follows: temperatures from forward end of screw (set values) 130°C, 140°C, 140°C, 140°C, 140°C and 140°C; temperature of melt appr. 160°C; speed of rotation of screw 79 rpm; running speed 8-10 min and,blowing ratio 1.8.
The above-described film-blowing extruder was used with varying biopolymer additions (1.5 - 6.0 % as dry) to preparepolyethylene films by employing a polyethylene grade whose melt index was 1.2 and density 0.922. The thicknesses of such manufactured films varied within the range of 70-90 μm (tables 1 and 2).
Table 1 indicates how the enzymatic modification of a biopolymer improves the mechanical strength properties of a film compared with polyethylene having enzymatically unmodified biopolymer added therein.
With rice starch, a 3 % addition provides a 30 % improvement in tensile strength, 20 % in elongation and
appr. 22 % in drop value. In addition, a film of modified rice starch (EMRT) is 5 um thinner than a film of rice starch (RT). The change of particle size due to modification is also clearly seen in table 1 as the mean particle size of starch diminishes to about one fifth of the original.
Also with another biopolymer, i.e. with cellulose, the enzymatic modification provides similar improvements. The improvement in tensile strength by virtue of modification is appr. 24 %, in elongation nearly 20 % and in drop value more than 20 %. Also with cellulose, the particle size diminishes by virtue of modification to about half from the original.
TABLE 1
The effect of enzymatic modification of biopolymer (starch, cellulose) on the mechanical properties of a polyethylene film (pe-film)
The amount of Tensile strength Elongation Drop Mean part. Film
Biopolymer biopolymer in pe-film KS/PS KS/PS value size of thickness dry matter % (MPa) (%) (g) biopolymer (μ) (μm)
RT 3.0 15.1/13.5 310/530 115 28.5 80
EMRT 3.0 18.8/17.9 370/640 140 6.0 75 S 4.5 12.7/10.7 280/500 95 36.9 90 EMS 4.5 15.9/13.1 340/570 115 18.2 90
RT = rice starch
EMRT = enzymatically modified rice starch
S = cellulose
EMS = enzymatically modified cellulose
Tensile strength and elongation measured with Instron device (model 1026) and results are given in accordance with the following standards:
Tensile strength KS = direction of film ASTM D882 PS = transverse direction "
Elongation " Drop value ASTM D1709
The mean particle size of biopolymer is determined with Malvern 2600 device in aqueous phase.
Table 2 indicates the effect of an increase in the amount of biopolymer on the mechanical strength properties of a polyethylene film.
With all different concentrations (1.5 - 6.0 %) the modified rice starch (EMRT) provides for mechanically stronger film properties compared to original rice starch (RT).
The difference between EMRT and RT increases dramatically as the amount of biopolymer in a polyethylene film increases. For example, with a 1.5 % addition , the difference between EMRT and RT varies within the range of 6-12 % in favour of EMRT while a 6 % addition of biopolymer increases the difference in mechanical strength properties to the range of 30-96 % in favour of EMRT.
When modified rice starch was added in a polyethylene film (1.5 - 6.0 %), its mechanical strength properties were impaired only by 20 % while the similar additions of rice starch impaired the values considerably more, i.e. 60 %.
It can be summarized from table 2 that by virtue of the enzymatic modification of biopolymer it is possible to add in a polyethylene film up to 3 times more biopolymer (see table 2 RT 1.5 % and EMRT 4.5 %) to obtain the same mechanical strength properties for the film as those obtained by the addition of untreated biopolymer.
In table 2 with all dry matter contents of biopolymer, the EMRT film is 5-10 μm thinner than a corresponding RT film.
TABLE 2
The effect of the amount of biopolymer on the mechanical strength properties of a polyethylene film
RT EMRT RT EMRT RT EMRT
1.5 % 1.5 % 4.5 % 4.5 % 6,0 % 6.0 %
(dry matter) (dry matter) (dry matter) (dry matter) (dry matter) (dry matter)
Tensile strength
KS/PS 16.5/14.7 17.4/16.2 13.7/11.6 16.3/16.5 12.1/8.4 15.0/16.5
(MPa)
KS/PS 300/550 330/610 240/520 350/610 200/370 260/500
MPa)
Drop test n (g) 125 140 95 130 70 110
Film thickness 80 70 85 75 85 80
(urn)
Mould-formation tests
Tests were effected according to ASTM standard, STM G 21-70 1980. The test was effected with 100 × 80 mm sized test specimens which were incubated in glass Petri dishes (150 × 150 × 25 mm) for 4 weeks at 28°C. Sufficient relative air humidity in the incubation space was secured by placing a vessel containing saturated KNO3-solution (Rh 92 %) on the incubator floor. The controls used were test specimens that were not sterilized and not treated with mould suspension. The organic nature of mould suspension was checked with standardized test dishes. The mould-formation of plastics was observed at one-week intervals. The test fungi were as follows
Aspergillus niger ATCC 9142
Penicillium funiculosum ATCC 11797
Chaetomium globosum Chg K25
Aureobasidium pullulans PULL U2
The mould-formation of test specimens was rated visually and microscopically as follows:
0 no growth
1 less than 10 % of surface area
2 10 - 30 % of surface area
3 30 - 60 % of surface area
4 60 - 100 % of surface area
The enclosed table 3 shows that the mould-formation in a compsition having enzymatically modified rice starch was more vigorous than with a polyethylene film having unmodified rice starch added therein.
TABLE 3 The average mould-formation of test specimens
Test soecimen 1 week x 2 weeks x 3 weeks x 4 weeks x
LD-polyethylene 0 , 3 1 1 1
LD-polyethylene +
RT 14 % 0,7 1,7 2 2
LD-polyethylene + EMRT 14 % 1 1,3 2 2,7
LD-polyethvlene +
EMRT 10 % + UV 3 % 1,3 2,3 2,7 3,3
RT = rice starch
EMRT = enzymatically modified rice starch
UV = photosensitive component (Sarmalyte 24000)
It should be appreciated that a biologically decomposable composition of the invention can also be processed into a product by the application of other processes prior known in plastics manufacturing, such as injection moulding, blowing technique, extrusion moulding, vacuum moulding, rotational casting or various foaming techniques. The examples deal with blown films for the reason that the manufacturing of a thin-walled film is in technical sense most demanding, particularly in view of the workability of a biologically decomposablw composition. Generally speaking, such plastics manufacturing techniques can be applied which facilitate the manufacturing of an end product at such temperatures
that an enzymatically modified biopolymer maintains its characteristics promoting the decomposition of a composition in certain conditions. The upper limit temperature range can be considered to be 220-250°C.
In the examples, the synthetic polymer comprises polyethylene. It should be obvious to a person skilled in the art that polyoleophines overall are included in those synthetic polymers that can be employed in a composition of the invention. The agents belonging in the group of polyoleophines include e.g. HD-polyethylene, LD-polyethylene and polypropylene. It is obvious to a skilled person that e.g. polystyrene is a synthetic polymer suitable for a biologically decomposable composition of the invention.
Furthermore, the examples deal with rice starch for the reason that, in unmodified condition, they have the smallest particle size of all known starches. Thus, rice starch provides for the besz comparative results in unmodified form. It is self-evident that also corn starch etc. can be used as a biopolymer of the invention. Enzymatic modification makes it possible to reduce their particle size as desired. As far as starch is concerned, it can be said that enzymatic modification provides for such a particle size distribution in which the mean particle size is smaller than 10 μm. As for cellulose, it can be said that enzymatic modification provides for such a particle size distribution in which the mean particle size is smaller than 20 μm (fig. 1).
Claims
1. A biologically decomposable composition, comprising a composition consisting of a biopolymer and a synthetic polymer, the composition further including a material causing in certain conditions disintegration of the chains of the synthetic polymer and/or the synthetic polymer of the composition having been treated in a manner that the chains of the synthetic polymer disintegrate in certain conditions, c h a r a c t e r i z e d in that the biopolymer is enzymatically modified.
2. A biologically decomposable composition as set forth in claim 1, the biopolymer comprising starch, c h a r a c t e r i z e d in that the enzymatic modification of starch is effected with alfa-amylase, especially with heat-resistant alfa-amylase.
3. A biologically decomposable composition as set forth in claim 1, the biopolymer comprising cellulose, c h a r a c t e r i z e d in that the enzymatic modification of cellulose is effected with cellulase, especially with cellodextrines-forming cellulase.
4. A biologically decomposable composition as set forth in claim 2, c h a r a c t e r i z e d in that the mean particle size of enzymatically modified starch is smaller than 10 um.
5. A biologically decomposable composition as set forth in claim 3, c h a r a c t e r i z e d in that the mean particle size of enzymatically modified cellulose is smaller than 20 um.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FI881965 | 1988-04-27 | ||
FI881965A FI881965A (en) | 1988-04-27 | 1988-04-27 | BIOLOGISKT NEDBRYTBAR SAMMANSAETTNING. |
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Publication Number | Publication Date |
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WO1989010381A1 true WO1989010381A1 (en) | 1989-11-02 |
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PCT/FI1989/000075 WO1989010381A1 (en) | 1988-04-27 | 1989-04-24 | Biologically decomposable composition |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0421413A1 (en) * | 1989-10-05 | 1991-04-10 | Biodata Oy | Biologically degradable film and method of preparation the same |
EP0421415A1 (en) * | 1989-10-05 | 1991-04-10 | Biodata Oy | Biologically degradable cover film and method of preparation the same |
US5095054A (en) * | 1988-02-03 | 1992-03-10 | Warner-Lambert Company | Polymer compositions containing destructurized starch |
DE4202414A1 (en) * | 1992-01-16 | 1993-08-05 | Nien Made Enterprise Co | JALOUSIELAMELLE AND METHOD FOR PRODUCING THE SAME |
WO1998002046A1 (en) * | 1996-07-15 | 1998-01-22 | Kalle Nalo Gmbh & Co. Kg | Moulded articles of cellulose hydrate with enzymatically modified surface |
WO2016198650A1 (en) * | 2015-06-12 | 2016-12-15 | Carbios | Masterbatch composition comprising a high concentration of biological entities |
US10287561B2 (en) | 2014-10-21 | 2019-05-14 | Carbios | Polypeptide having a polyester degrading activity and uses thereof |
US10385183B2 (en) | 2014-05-16 | 2019-08-20 | Carbios | Process of recycling mixed PET plastic articles |
US10508269B2 (en) | 2015-03-13 | 2019-12-17 | Carbios | Polypeptide having a polyester degrading activity and uses thereof |
US10626242B2 (en) | 2014-12-19 | 2020-04-21 | Carbios | Plastic compound and preparation process |
US10717996B2 (en) | 2015-12-21 | 2020-07-21 | Carbios | Recombinant yeast cells producing polylactic acid and uses thereof |
US10767026B2 (en) | 2016-05-19 | 2020-09-08 | Carbios | Process for degrading plastic products |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0032802A1 (en) * | 1980-01-17 | 1981-07-29 | THE GOVERNMENT OF THE UNITED STATES OF AMERICA as represented by the Secretary Department of Commerce | Flexible, self-supporting and biodegradable films and their production |
SE454444B (en) * | 1981-06-23 | 1988-05-02 | Roquette Freres | PROCEDURE FOR PREPARING A TEMPOR PROTECTIVE COATING OF A FORM |
-
1988
- 1988-04-27 FI FI881965A patent/FI881965A/en not_active Application Discontinuation
-
1989
- 1989-04-24 WO PCT/FI1989/000075 patent/WO1989010381A1/en unknown
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0032802A1 (en) * | 1980-01-17 | 1981-07-29 | THE GOVERNMENT OF THE UNITED STATES OF AMERICA as represented by the Secretary Department of Commerce | Flexible, self-supporting and biodegradable films and their production |
SE454444B (en) * | 1981-06-23 | 1988-05-02 | Roquette Freres | PROCEDURE FOR PREPARING A TEMPOR PROTECTIVE COATING OF A FORM |
Cited By (18)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5095054A (en) * | 1988-02-03 | 1992-03-10 | Warner-Lambert Company | Polymer compositions containing destructurized starch |
EP0421413A1 (en) * | 1989-10-05 | 1991-04-10 | Biodata Oy | Biologically degradable film and method of preparation the same |
EP0421415A1 (en) * | 1989-10-05 | 1991-04-10 | Biodata Oy | Biologically degradable cover film and method of preparation the same |
US5316847A (en) * | 1989-10-05 | 1994-05-31 | Biodata Oy | Biologically degradable films comprising enzyme-coated bio-degradable polymer particles |
DE4202414A1 (en) * | 1992-01-16 | 1993-08-05 | Nien Made Enterprise Co | JALOUSIELAMELLE AND METHOD FOR PRODUCING THE SAME |
WO1998002046A1 (en) * | 1996-07-15 | 1998-01-22 | Kalle Nalo Gmbh & Co. Kg | Moulded articles of cellulose hydrate with enzymatically modified surface |
US6761944B1 (en) | 1996-07-15 | 2004-07-13 | Kalle Nalo Gmbh & Co. Kg | Moulded articles of cellulose hydrate with enzymatically modified surface |
US10385183B2 (en) | 2014-05-16 | 2019-08-20 | Carbios | Process of recycling mixed PET plastic articles |
US10287561B2 (en) | 2014-10-21 | 2019-05-14 | Carbios | Polypeptide having a polyester degrading activity and uses thereof |
US10626242B2 (en) | 2014-12-19 | 2020-04-21 | Carbios | Plastic compound and preparation process |
US10508269B2 (en) | 2015-03-13 | 2019-12-17 | Carbios | Polypeptide having a polyester degrading activity and uses thereof |
WO2016198650A1 (en) * | 2015-06-12 | 2016-12-15 | Carbios | Masterbatch composition comprising a high concentration of biological entities |
US10723848B2 (en) | 2015-06-12 | 2020-07-28 | Carbios | Masterbatch composition comprising a high concentration of biological entities |
US11198767B2 (en) | 2015-06-12 | 2021-12-14 | Carbios | Process for preparing a biodegradable plastic composition |
US11802185B2 (en) | 2015-06-12 | 2023-10-31 | Carbios | Masterbatch composition comprising a high concentration of biological entities |
US10717996B2 (en) | 2015-12-21 | 2020-07-21 | Carbios | Recombinant yeast cells producing polylactic acid and uses thereof |
US10767026B2 (en) | 2016-05-19 | 2020-09-08 | Carbios | Process for degrading plastic products |
US11377533B2 (en) | 2016-05-19 | 2022-07-05 | Carbios | Process for degrading plastic products |
Also Published As
Publication number | Publication date |
---|---|
FI881965A0 (en) | 1988-04-27 |
FI881965A (en) | 1989-10-28 |
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