PERMEABLE POLYMER FILM
Films especially suitable for the packaging of fresh foodstuff, like salad and vegetables, due to their valuable balance of high permeability to oxygen and optimal permeability to water vapour, comprising at least one layer A) and at least one layer B), wherein the layer A) comprises a copolymer of propylene with hexene-1 containing from 3 to 9% by weight of recurring units derived from hexene-1, said copolymer having a melting temperature from 125° C. to 143° C., and the layer B) comprises a polyolefin composition containing (all percentages being by weight): a) 10-40% of one or more propylene homopolymers or copolymers containing over 85% of propylene and having a fraction insoluble in xylene at room temperature greater than 80%; and b) 60-90 of one or more copolymers of ethylene with α-olefin(s), containing ethylene in a quantity from 20 to 80%, and having solubility in xylene at room temperature greater than 70%.
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The present invention relates to a polymer film especially suitable for the packaging of fresh foodstuff, like salad and vegetables.
It is well known that polypropylene films, and particularly biaxially oriented polypropylene films (BOPP), are widely used for the packaging of foodstuff using automatic machines. In fact the said films are characterized by a particular good balance of processability (“machinability”), optical and mechanical properties, and low permeability to gases, in particular oxygen and carbon dioxide, and water vapour.
However for the packaging of fresh foods, in particular vegetables, greater gas transmission rates are necessary. As a matter of fact, the metabolic activity of vegetable cells continues also after these foods are harvested, cleaned and cut into pieces; therefore the cells still “breathe”, consuming the oxygen and emitting carbon dioxide and water vapour. In a closed package this process quickly results in changes of the atmosphere inside the package, making it unsuitable for the continuation of the metabolic activity and favourable for the development of undesired micro-organisms.
Monolayer and multilayer films suitable for packaging fresh produce items that continue to respire after they are harvested are described in U.S. Pat. No. 6,348,271. The films therein described are characterized by the presence of at least one layer of a propylene resin composition comprising a propylene polymer component and up to 70% by weight of an ethylene/propylene copolymer. Additional layers made of propylene polymers can be present.
In such document it is explained that, to avoid excessive drying of the packaged foodstuff, the water vapour transmission rate should not be greater than 50 g/m2*day. On the other hand, a high oxygen transmission rate would be desirable, but an increase of oxygen transmission rate can easily raise the water vapour transmission rate to excessively high values. In particular, in the examples of U.S. Pat. No. 6,348,271 it is shown that at an oxygen transmission rate value of around 6000 nmol/m2*s*100 kPa, corresponding to around 3000 cm3 (STP)/m2*day, measured at 1 atmosphere pressure difference, the vapour transmission rate becomes as high as 60 g/m2*day.
It has now been found that a particularly good balance of oxygen and water vapour transmission rate is achieved by combining at least one film layer comprising a specific propylene copolymer with another layer comprising a polyolefin composition containing a propylene polymer and a propylene/ethylene copolymer with high solubility in hydrocarbon solvents.
Due to its valuable properties, the said propylene copolymer provides valuable film performances, in particular a valuable balance of resistance to solvents (low amounts of fraction soluble in organic solvents, in particular hydrocarbons), ink and dye printability and heat sealability, as it makes it possible to seal the film at advantageously low temperatures.
Thus the present invention provides a multilayer film comprising at least one layer A) and at least one layer B), wherein the layer A) comprises a copolymer (i) of propylene with hexene-1 containing from 3 to 9% by weight, preferably from 5 to 9% by weight, more preferably from 6 to 9% by weight, in particular from 6.5 to 9% by weight, of recurring units derived from hexene-1, said copolymer having a melting temperature from 125° C. to 143° C., preferably from 128° C. to 143° C., and the layer B) comprises a polyolefin composition (ii) containing (all percentages being by weight):
a) 10-40%, preferably 20-40%, more preferably 25-38%, of one or more propylene polymers selected from propylene homopolymers copolymers of propylene with ethylene or a CH2═CHR α-olefin, where R is a C2—C8 alkyl radical, and copolymers of propylene with ethylene and said CH2═CHR α-olefin, said copolymers containing over 85% of propylene and having a fraction insoluble in xylene at room temperature greater than 80%; and
b) 60-90%, preferably 60-80%, more preferably 62-75%, of one or more copolymers of ethylene with propylene or a CH2═CHR α-olefin, where R is a C2—C8 alkyl radical, or a combination thereof, and optionally minor quantities of a diene, said copolymers containing ethylene in a quantity from 20 to 80%, preferably from 20 to 40%, more preferably from 20 to 38%, and having solubility in xylene at room temperature greater than 70%, preferably greater than 80%;
the amounts of (a) and (b) being referred to the total weight of (a) and (b).
For room temperature, a temperature of 25° C. is meant.
In particular, the films of the present invention can have a A)/B) or a A)/B)/A) structure, wherein layers A) and B) are as above defined.
From the above definitions it is clear that the term “copolymer” includes polymers containing more than one kind of comonomers, such as terpolymers.
The said amounts of hexene-1 units are referred to the total weight of the copolymer (i).
The said melting temperature values for the copolymer (i) are determined by differential scanning calorimetry, according to ISO 11357-3, with a heating rate of 20° C./minute.
Recurring units derived from other comonomers, selected in particular from ethylene and CH2═CHR1 α-olefins where RI is a C2—C8 alkyl radical, hexene-1 excluded, can be present in copolymer (i), provided that the final properties of the copolymer are not substantially worsened. Examples of the said CH2═CHRI α-olefins are butene-1, 4-methyl-1-pentene, octene-1. Among the said other comonomers, ethylene is preferred.
Indicatively, the total amount of recurring units derived from comonomer(s) different from propylene and hexene-1 in copolymer (i) is from 0.5 to 2% by weight, preferably from 0.5 to 1.5% by weight, referred to the total weight of the copolymer.
Moreover, the copolymer (i) is semicrystalline, as it has a crystalline melting point, and typically has a stereoregularity of isotactic type.
Preferably, said copolymer (i) exhibits at least one of the following features:
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- a solubility in xylene at room temperature equal to or lower than 25% by weight, preferably equal to or lower than 20% by weight;
- Isotacticity Index equal to or higher than 97%, determined as mm triads using 13C-NMR;
- a molecular weight distribution expressed by the Mw/Mn ratio, measured by GPC, (Gel Permeation Chromathograpy), from 4 to 7.
In particular, the copolymer (i) has preferably a Melt Flow Rate (MFR, measured according to ISO 1133, 230° C./2.16 kg, i.e. at 230° C., with a load of 2.16 kg) from 0.1 to 10 g/10 min., more preferably from 0.1 to 5 g/10 min., in particular from 0.1 to 3 g/10 min.
Such copolymer (i) can be obtained with polymerization processes carried out in the presence of stereospecific Ziegler-Natta catalysts supported on magnesium dihalides. By properly dosing the molecular weight regulator (preferably hydrogen), the said preferred Melt Flow Rate values and melting temperature values are obtained, when the amount of recurring units derived from hexene-1 is within the above said range of from 3 to 9% by weight, preferably from 5 to 9% by weight.
The polymerization process, which can be continuous or batch, is carried out following known techniques and operating in liquid phase, in the presence or not of inert diluent, or in gas phase, or by mixed liquid-gas techniques. It is preferable to carry out the polymerization in gas phase.
Polymerization reaction time, pressure and temperature are not critical, however it is best if the temperature is from 20 to 100° C. The pressure can be atmospheric or higher.
As previously mentioned, the regulation of the molecular weight is carried out by using known regulators, hydrogen in particular.
The said stereospecific Ziegler-Natta polymerization catalysts comprise the product of the reaction between:
1) a solid component, containing a titanium compound and an electron-donor compound (internal donor) supported on magnesium dihalide (preferably chloride);
2) an aluminum alkyl compound (cocatalyst); and, optionally,
3) an electron-donor compound (external donor).
Said catalysts are preferably capable of producing homopolymers of propylene having an isotactic index higher than 90% (measured as weight amount of the fraction insoluble in xylene at room temperature).
The solid catalyst component (1) contains as electron-donor a compound generally selected among the ethers, ketones, lactones, compounds containing N, P and/or S atoms, and mono-and dicarboxylic acid esters.
Catalysts having the above mentioned characteristics are well known in the patent literature; particularly advantageous are the catalysts described in U.S. Pat. No. 4,399,054 and European patent 45977.
Particularly suited among the said electron-donor compounds are phthalic acid esters and succinic acid esters.
Suitable succinic acid esters are represented by the formula (I):
wherein the radicals R1 and R2, equal to or different from each other, are a C1—C20 linear or branched alkyl, alkenyl, cycloalkyl, aryl, arylalkyl or alkylaryl group, optionally containing heteroatoms; the radicals R3 to R6 equal to or different from each other, are hydrogen or a C1—C20 linear or branched alkyl, alkenyl, cycloalkyl, aryl, arylalkyl or alkylaryl group, optionally containing heteroatoms, and the radicals R3 to R6 which are joined to the same carbon atom can be linked together to form a cycle.
R1 and R2 are preferably C1—C8 alkyl, cycloalkyl, aryl, arylalkyl and alkylaryl groups. Particularly preferred are the compounds in which R1 and R2 are selected from primary alkyls and in particular branched primary alkyls. Examples of suitable R1 and R2 groups are methyl, ethyl, n-propyl, n-butyl, isobutyl, neopentyl, 2-ethylhexyl. Particularly preferred are ethyl, isobutyl, and neopentyl.
One of the preferred groups of compounds described by the formula (I) is that in which R3 to R5 are hydrogen and R6 is a branched alkyl, cycloalkyl, aryl, arylalkyl and alkylaryl radical having from 3 to 10 carbon atoms. Another preferred group of compounds within those of formula (I) is that in which at least two radicals from R3 to R6 are different from hydrogen and are selected from C1—C20 linear or branched alkyl, alkenyl, cycloalkyl, aryl, arylalkyl or alkylaryl group, optionally containing heteroatoms. Particularly preferred are the compounds in which the two radicals different from hydrogen are linked to the same carbon atom. Furthermore, also the compounds in which at least two radicals different from hydrogen are linked to different carbon atoms, that is R3 and R5 or R4 and R6 are particularly preferred.
Other electron-donors particularly suited are the 1,3-diethers, as illustrated in published European patent applications EP-A-361 493 and 728769.
As cocatalysts (2), one preferably uses the trialkyl aluminum compounds, such as Al-triethyl, Al-triisobutyl and Al-tri-n-butyl.
The electron-donor compounds (3) that can be used as external electron-donors (added to the Al-alkyl compound) comprise the aromatic acid esters (such as alkylic benzoates), heterocyclic compounds (such as the 2,2,6,6-tetramethylpiperidine and the 2,6-diisopropylpiperidine), and in particular silicon compounds containing at least one Si—OR bond (where R is a hydrocarbon radical). Examples of the said silicon compounds are those of formula Ra1Rb2Si(OR3)c, where a and b are integer numbers from 0 to 2, c is an integer from 1 to 3 and the sum (a+b+c) is 4; R1, R2, and R3 are alkyl, cycloalkyl or aryl radicals with 1-18 carbon atoms optionally containing heteroatoms.
Thexyltrimethoxysilane (2,3-dimethyl-2-trimethoxysilyl-butane) is particularly preferred. Other preferred silicon compounds are diisopropyl dimethoxy silane and dicyclopentyl dimethoxysilane.
The previously said 1,3-diethers are also suitable to be used as external donors. In the case that the internal donor is one of the said 1,3-diethers, the external donor can be omitted.
The catalysts may be precontacted with small quantities of olefin (prepolymerization), maintaining the catalyst in suspension in a hydrocarbon solvent, and polymerizing at temperatures from room to 60° C., thus producing a quantity of polymer from 0.5 to 3 times the weight of the catalyst.
The operation can also take place in liquid monomer, producing, in this case, a quantity of polymer up to 1000 times the weight of the catalyst.
Examples of the said CH2═CHR α-olefins where R is a C2—C8 alkyl radical, present in the composition (ii), are butene-1, pentene-1, 4-methyl-pentene-1, hexene-1, and octene-1. Butene-1 is preferred.
Whenever present, the amount of diene in component (b) of the composition (ii) is preferably from 1 to 10% by weight with respect to the total weight of component (b). Examples of dienes are butadiene, 1,4-hexadiene, 1,5-hexadiene, and ethylidene-1-norbornene.
Preferably the intrinsic viscosity of the fraction soluble in xylene at room temperature of the composition (ii) is from 2 to 4 dl/g.
Examples of composition (ii) are described in published European patent application EP-A-0472946 and in WO03/011962, whose content is incorporated in this patent application for reference purposes.
The polyolefin composition (ii) can be prepared by mixing the previously prepared components (a) and (b) in the fluid state, i.e., at temperatures greater than their softening or melting point, or, more preferably, by sequential polymerization in two or more stages. It is preferred to carry out the polymerization processes for the preparation of the single components or of the polyolefin composition (ii) (sequential polymerization) in the presence of a highly stereospecific Ziegler-Natta catalyst. In particular, the Ziegler-Natta catalysts described in detail in connection with the preparation of the copolymer (i) of propylene with hexene-1 of layer A) can be used for the preparation of the polyolefin composition (ii) as well. Whenever desirable for balancing the mechanical and gas transmission properties of the film of the present invention, the film layer B) can comprise a blend of the polyolefin composition (ii) with a copolymer of propylene with hexene-1 falling within the definition of the copolymer (i).
Preferred relative amounts are from 30% to 70% by weight of polyolefin composition (ii) and from 30% to 70% by weight of the said copolymer (i). Such amounts are referred to the total weight of the polyolefin composition (ii) and of the copolymer (i).
All the film layers may also contain the additives that are commonly used for the film manufacturing, and especially for the films used for packaging applications with automatic machines, such as anti-oxidants, process stabilizers, slip agents, antistatic agents, antiblock agents.
Independently from the structure of the film, the overall film thickness is preferably from 9 to 100 microns, the thickness of the layer(s) A) is preferably from 0.5 to 15 microns, and that of the layer(s) B), typically used as inner layer(s), is from 9.5 to 99.5 microns.
The said films are produced by using processes well known in the art.
In particular, extrusion processes can be used.
In said extrusion processes the polymer materials to be used for the various layers are molten in different extruders and extruded through a narrow die slit. Subsequent from the exit from the die, the material can be cooled, heated and optionally oriented in several ways or in combination. Examples of such processes are cast, blown, extrusion coating, uniaxially oriented, simultaneous biaxially oriented, and sequential biaxially oriented film processes.
Specific examples of such processes are the blown film and BOPP processes hereinbelow explained.
Blown Film
The molten polymer materials are forced through a circular shaped die.
The extrudate which is drawn off has the shape of a tube, which is inflated by air to form a tubular bubble. The bubble is cooled and collapsed before winding-up.
The blown film process is preferred for the preparation of the film of the present invention.
BOPP
The molten polymer materials are forced continuously through a narrow die. The extruded molten material is pulled away from the die and cooled, then heated again and stretched both in the Machine Direction (MD) and in the Transverse Direction (TD). After the stretching process, the film is cooled and then wound-up.
The following examples are given to illustrate, not to limit, the present invention.
The following analytical methods have been used to determine the properties reported in the present application.
Hexene-1 Content and Isotacticity
Determined by 13C-NMR spectroscopy.
13C-NMR spectra are acquired on a Bruker DPX-600 spectrometer operating at 150.91 MHz in the Fourier transform mode at 120° C.
The samples are dissolved in 1,1,2,2-tetrachloroethane-d2 at 120° C. with a 8% wt/v concentration. Each spectrum is acquired with a 90° pulse, 15 seconds of delay between pulses and CPD (WALTZ 16) to remove 1H-13C coupling. About 1500 transients are stored in 32 K data points using a spectral window of 6000 Hz.
The peak of the Propylene CH is used as internal reference at 28.83 ppm.
The evaluation of diad distribution and the composition is obtained from Saa using the following equations:
PP=100 Sαα (PP)/Σ
PH=100 Sαα (PH)/Σ
HH=100 Sαα (HH)/Σ
Where Σ=Σ Sαα
[P]=PP+0.5 PH
[H]=HH+0.5 PH
Ethylene Content
Via InfraRed analysis.
The spectrum of a pressed film of the polymer is recorded in absorbance vs. wavenumbers (cm−1). The following measurements are used to calculate the ethylene content:
a) Area (At) of the combination absorption bands between 4482 and 3950 cm−1 which is used for spectrometric normalization of film thickness.
b) Area (AC2) of the absorption band due to methylenic sequences (CH2 rocking vibration) after a proper digital subtraction of an isotactic polypropylene (IPP) reference spectrum. The range 660 to 790 cm−1 is used for both heterophasic and/or random copolymers.
Melt Flow Rate (MFR, 230° C., 2.16 kg)
ISO 1133, 230° C./2.16 kg.
Intrinsic Viscosity
Measured in tetrahydronaphthalene at 135° C.
Determination of Solubility in Xylene at Room Temperature (% by Weight)
2.5 g of polymer are dissolved in 250 ml of xylene, at 135° C., under agitation. After 20 minutes, the solution is cooled to 25° C. under stirring, and then it is allowed to settle for 30 minutes. The precipitate is filtered with filter paper; the solution is evaporated under a nitrogen current, and the residue dried under vacuum at 80° C. until constant weight. The weight percentage of polymer soluble in xylene at room temperature is then calculated. The percent by weight of polymer insoluble in xylene at room temperature is considered the isotactic index of the polymer. This value corresponds substantially to the isotactic index determined by extraction with boiling n-heptane, which by definition constitutes the isotactic index of polypropylene.
Propylene Copolymers: Determination of Melting Temperature
The melting temperature is determined using the following procedure according to ISO 11357 Part 3.
Differential scanning calorimetric (DSC) data is obtained using a DSC Q1000 TA Instruments. Samples weighing approximately 6-8 mg are sealed in aluminum sample pans.
The samples are subjected to a first heating run from 5° C. to 200° C. with a heating rate of 20° C./minute, and kept at 200° C. under isothermal conditions for 5 minutes. Then the samples are cooled from 200° C. to 5° C. with a cooling rate of 20° C./minute, and kept at 5° C. under isothermal conditions for 5 minutes, after which they are subjected to a second heating run from 5° C. to 200° C. with a heating rate of 20° C./minute. The melting temperature is the temperature of the highest melting peak obtained in the second heating run.
MWD and
MWD and particularly the ratio
The solution is filtered through a 0.45 μm Teflon membrane. The filtrate (concentration 0.08-1.2g/l injection volume 300 is subjected to GPC. Monodisperse fractions of polystyrene (provided by Polymer Laboratories) are used as standard. The universal calibration for butene-1 polymers is performed by using a linear combination of the Mark-Houwink constants for PS (K=7.11×10-5dl/g; a=0.743) and PB(K=1.18×10-4dl/g; α=0.725).
MEASUREMENTS ON FILMS
Oxygen Transmission (OTR)
Measured on a Mocon OX-TRAN 2/21 unit, commercially available from Mocon, Inc., according to ASTM D3985 at 23° C., 0% relative humidity (RH), and 100% O2.
Water Vapor Transmission (WVTR)
Measured on a Mocon PERMATRAN W3/33 unit, commercially available from Mocon, Inc. according to ASTM F 1249 at 37.8° C. and 90% relative humidity (RH).
Puncture Resistance and Deformation
Determined from the energy required to puncture the film with a plunger (50 mm, diameter of 4 mm) with a rate of 20 mm/min, followed by measuring the deformation.
Tensile Modulus
Determined according to ASTM D882, both in the machine direction (MD) and in the transverse direction (TD).
PRODUCTS USED IN THE WORKING EXAMPLES
Three layer films are prepared using the hereinafter described polymer materials.
Layers A)
Preparation of the Copolymers (i)
Two copolymers of propylene with hexene-1, hereinafter called Copolymer 1 and Copolymer 2, are prepared as follows.
The solid catalyst component used in polymerization is a highly stereospecific Ziegler-Natta catalyst component supported on magnesium chloride, containing about 2.2% by weight of titanium and diisobutylphthalate as internal donor, prepared by analogy with the method described in WO03/054035 for the preparation of catalyst component A.
Catalyst System and Prepolymerization Treatment
Before introducing it into the polymerization reactor, the solid catalyst component described above is contacted at 15° C. for about 6 minutes with aluminum triethyl (TEAL) and thexyltrimethoxysilane (2,3 -dimethyl-2-trim ethoxysilyl-butane), in a TEAL/thexyltrimethoxysilane weight ratio equal to about 7 and in such quantity that the TEAL/solid catalyst component weight ratio be equal to about 6.
The catalyst system is then subjected to prepolymerization by maintaining it in suspension in liquid propylene at 20° C. for about 20 minutes before introducing it into the polymerization reactor.
Polymerization
The polymerization is carried out in a gas phase polymerization reactor by feeding in a continuous and constant flow the prepolymerized catalyst system, hydrogen (used as molecular weight regulator), propylene and hexene-1 in the gas state.
The main polymerization conditions are:
The polymer particles exiting the reactor are subjected to a steam treatment to remove the reactive monomers and volatile substances, and then dried.
The resulting copolymers have the following properties:
Layer B)
The material used to prepare the layer B) is a polyolefin composition (ii) having a MFR of 0.6 g/10 min. and comprising (weight percentages):
A) 32% of a crystalline propylene random copolymer containing 3.5% of ethylene and about 6% of a fraction soluble in xylene at room temperature, and having an intrinsic viscosity [η] of 1.5 dl/g;
B) 68% of an ethylene/propylene copolymer containing 27% of ethylene, having solubility in xylene at room temperature of 89% by weight.
The intrinsic viscosity of the fraction soluble in xylene at room temperature of the total composition is of 3.2 dl/g.
Such composition has been prepared by a sequential polymerization process in the presence of a stereospecific Ziegler-Natta catalyst supported on magnesium dichloride.
Examples 1 and 2 Preparation of the FilmsBefore using them to prepare films, the said two copolymers of propylene with hexene-1 are both extruded with 500 ppm by weight of Dynamar FX5911 and 750 ppm by weight of NA 21, thus obtaining the final products COPO-1, resulting from extrusion with the said additives of Copolymer 1, and COPO-2, resulting from extrusion with the said additives of Copolymer 2.
Dynamar™ FX5911 is a fluoropolymer sold by 3M for use as processing aid.
NA 21™ is a nucleating agent based on aluminum-hydroxy-bis[2,2′-methylene-bis(4,6-di-t-butylphenyl)phosphate], sold by Asahi Denka K. K.
The said extrusions with Dynamar FX5911 and NA 21 are carried out in a co-rotating twin screw three lobs profile extruder (ZSK58 type, length/diameter ratio of 28, manufactured by Coperion) under nitrogen atmosphere in the following conditions:
Rotation speed: 260 rpm;
Extruder output: 160 kg/hour;
Melt temperature: 250-260° C.
The three layer films are prepared on a Kiefel three layer coextrusion line.
The final film thickness of the films is approximately 30 micron, with a structure A/B/A wherein the thickness of each layer A) amounts to 30% of the total thickness and the thickness of layer B) to the remaining 40%.
The film of Example 1 is prepared by using COPO-1 for both the two layers A) and the above described polyolefin composition (ii) for layer B). The film of Example 2 is prepared by using COPO-2 for both the two layers A) and the above described polyolefin composition (ii) for layer B).
In the said Kiefel coextrusion blown-film line, the screw length/screw diameter ratios are 60 mm/24 xD for all three A, B and C extruders. No IBCS system (Internal Bubble Cooling System) is used. During the extrusion trials, the melt is extruded through an annular die with a diameter of 200 mm and a quite narrow gap (1.2 mm for the trials). At the exit from the die, the melt tube is subjected to intensive air cooling, immediately blown up to about three times the diameter of the die and stretched in the direction of the flow.
The main operating conditions in Examples 1 and 2 are:
-
- Barrel temperature: 230-230-230-230° C.;
- Adaptor temperature: 235-235-240-240° C.;
- Die temperature: 240° C.;
- Screw speed: 90 rpm for Extruder B (B layer), 53 rpm for both A&C extruders (A & C side layers);
- Blow-up ratio: 3.1;
- Total line throughput: 125-132 kg/h.
The properties of the so obtained films are reported in Table 1.
Claims
1. A film comprising at least one layer A) and at least one layer B), wherein the layer A) comprises a copolymer (i) of propylene with hexene-1 containing from 3 to 9% by weight, preferably from 5 to 9% by weight, more preferably from 6 to 9% by weight, in particular from 6.5 to 9% by weight, of recurring units derived from hexene-1, said copolymer having a melting temperature from 125° C. to 143° C., preferably from 128° C. to 143° C., and the layer B) comprises a polyolefin composition (ii) containing (all percentages being by weight): the amounts of (a) and (b) being referred to the total weight of (a) and (b).
- a) 10-40%, preferably 20-40%, more preferably 25-38%, of one or more propylene polymers selected from propylene homopolymers, copolymers of propylene with ethylene or a CH2═CHR α-olefin, where R is a C2—C8 alkyl radical, and copolymers of propylene with ethylene and said CH2═CHR α-olefin, said copolymers containing over 85% of propylene and having a fraction insoluble in xylene at room temperature greater than 80%; and
- b) 60-90%, preferably 60-80%, more preferably 62-75%, of one or more copolymers of ethylene with propylene or a CH2═CHR α-olefin, where R is a C2—C8 alkyl radical, or a combination thereof, and optionally minor quantities of a diene, said copolymers containing ethylene in a quantity from 20 to 80%, preferably from 20 to 40%, more preferably from 20 to 38%, and having solubility in xylene at room temperature greater than 70%, preferably greater than 80%;
2. The film of claim 1, having a A)/B) or A)/B)/A) structure.
3. The film of claim 1, having an overall thickness from 9 to 100 microns.
4. The film of claim 1, prepared by using a blown film process.
5. The film of claim 1, wherein the copolymer (i) has a Melt Flow Rate (MFR, measured according to ISO 1133, 230° C./2.16 kg) from 0.1 to 10 g/10 min., more preferably from 0.1 to 5 g/10 min., in particular from 0.1 to 3 g/10 min.
6. The film of claim 1, wherein the intrinsic viscosity of the fraction soluble in xylene at room temperature of the composition (ii) is from 2 to 4 dl/g.
7. Food packaging items comprising the film of claim 1.
Type: Application
Filed: Dec 8, 2011
Publication Date: Sep 26, 2013
Applicant: BASELL POLIOLEFINE ITALIA S.R.L. (Milano)
Inventors: Michele Grazzi (Casaglia (FE)), Andrea Felisati (Ferrara), Giampaolo Pellegatti (Boara (FE))
Application Number: 13/991,754
International Classification: B65D 81/28 (20060101);
