Title of Invention

POLYMER COMPOSITIONS COMPRISING SYNDIOTACTIC POLYPROPYLENE AND THERMOPLASTIC ELASTOMER

Abstract Polymer composition comprising a thermoplastic elastomer including styrene and isoprene and/or vinylisoprene units (SI) and a syndiotactic polypropylene (s-PP).
Full Text

SYNDIOTATIC POLYPROPYLENE COMPOSITION COMPRISING A THERMOPLASTIC ELASTOMER
The present invention relates to a polymer composition comprising a thermoplastic elastomer; to a film or tube comprising a layer including such a composition and to specific applications thereof.
Articles intended for medical applications must meet not only conventional requirements, such as good mechanical strength or low cost, but also requirements - extremely strict - peculiar to this specific field of application, such as, for example, requirements relating to the biocompatibility properties of the said articles, their ability to be subjected to a sterilization treatment, their flexibility, their transparency , their weldability, their impact strength (including as regards containers filled with liquid), the amount of substances which migrates (for example in medical (fatty) liquids) or can be extracted (for example, with hexane and/or purified water) and in some cases, their barrier properties.
Until now, commercially available articles for medical use, for example infusion or blood bags, and bags intended for the conservation of medical related fluids, have been based on vinyl chloride polymers, for example on PVC. Although having several advantages, this type of polymer, however, has certain disadvantages, such as the need to incorporate high amounts of stabilizers therein for the purpose of improving its thermal stability or to incorporate high amounts of plasticizers therein for the purpose of obtaining sufficient flexibility. There is therefore a market demand for articles for medical applications which are devoid of chlorinated polymers.
To get such articles, it is known to start from polyolefin-based films and to weld these together (or on themselves) in order to make bags or pouches. It is more specifically known to use polypropylene (PP) based films which include additives in order to improve some of the above mentioned properties. Such additives are often elastomers used to improve the transparency and flexibility of the PP resins. An example of such elastomers are those including styrene and isoprene and/or vinylisoprene units (hereafter called "SP resins), hydrogenated or not. Among those, styrene-vinylisoprene-styrene block copolymers (SVIS) and styrene-isoprene-butadiene-styrene (SIBS) are preferred because they have an improved compatibility with PP resins, especially when they are at least

partially hydrogenated However, after a while (or after a heat treatment like heat sterilisation), it appears that films made of PP and SI resins loose their transparency, which would indicate that some phase separation appears after long term use/storage.
The applicant found that surprisingly, when choosing a syndiotactic polypropylene resin (s-PP), this long term phase separation tends to disappear. Another advantage of using s-PP over "conventional" i-PP is its lower melting point (130°C versus 165°C) which allows welding at lower temperature, while still allowing steam sterilisation at the classical temperature of 121°C
Accordingly, the present invention relates to a polymer composition comprising a SI and a s-PP.
The SI resin used in the composition according to the present invention is generally a triblock copolymer having two polystyrene outer blocks and a midblock including isoprene and eventually other monomers and which may be partially or fully hydrogenated The term "partially hydrogenated" means that there are still some unsaturated isoprene units left in the structure. Usually, in commercial hydrogenated SI resins, there are about 5 wt% dienes (insaturations) left or less, preferably 1 wt% or less, and most preferably, 0.5wt% or less. Fully or almost fully hydrogenated resins are preferred for stability reasons.
Examples of such resins are those commercialised by KURARAY under the trade name HYBRAR. These resins include till about 40% (in-weight) of styiene which forms blocks linked together by blocks made of vinyMsoprene-co-polyisoprene. Grades 5127 and 5125 are non-hydrogenated while grade 7125 is hydrogenated Hydrogenated SVIS resins like HYBRAR 7125 are preferred.
Other examples of such SI resins are styrene-isoprene-butadiene-styrene resins (SEBS). Examples of such resins which give good results are those commercialised under the name KRATON** G-1730, RP-6924 and RP-6917. These resins are fully or almost fully hydrogenated (i.e. they have less than 0.2 wt% of insaturations left).
The s-PP according to the present invention may be a homopolymer or a copolymer of propylene with up to 30% of a C2-Q comonomer, preferably ethylene. It preferably is a polyolefin of controlled crystallinity as described in WO 00/61062. It preferably shows a softening point (or **Vicat Point**) of less than 121°C (measured according to ASTM Standard D1525), at least after having been processed in appropriate conditions (which are described in WO 00/061062, incorporated herein by reference), even if the producer of the resin

announces higher values. The s-PP according to the present invention thus preferably exhibit the distinguishing feature that their crystallinity can be easily reduced during their processing. This ready control of the crystallinity is advantageous in the content of the invention, in so far as it makes it possible to confer a reduced crystallinity on these s-PP resins, provided that appropriate processing conditions are used, thus increasing the transparency and the flexibility of the whole structure.
The polydispersity of the s-PP according to the present invention is advantageously less than 8 and preferably less than 4. This characteristic reflects a low dispersion of the molecular masses, which increases the separation between the melting temperature ranges and softening temperature ranges and thus makes it possible to have a more effective action on the crystallinity during the processing.
Furthermore, the melt flow index of the s-PP used is advantageously less than 12 g/10 min, preferably less than 10 g/10 min and most preferably less than 8 g/10 min (measured according to ASTM Standard D1238, under the conditions 190°C/2.16 kg for the polymere of ethylene and the copolymers of butene and under the conditions 230°C/2.16 kg for the polymers of propylene and the homopolymers of butene).
In the composition according to the present invention, the s-PP is generally present in an amount of 30% or more, or even^40% or more (in weight compared with the total weight of the blend). On the other hand, the SVIS content of fee blend is generally of 5% or more, or even 10% or more. Generally, the s-PP is present in amount of 95% or less, or even 90% or less, while on the other hand, the SVIS is generally present in amount of 70% or less, or even 60% or less.
The composition according to the present invention may include other polymers and/or usual additives like pigments, stabilizers ... Especially when it is intended to be welded, it may comprise at least one not very crystalline or amoiphous polyolefin chosen between ethylene-vinyl acetate (EVA), ethylene-methyl acrylate (EMA), etbylene-ethyl acrylate (EEA) or ethylene-butyl acrylate (EBA) copolymers. Among the last mentioned copolymers, only those which exhibit a content of comonomer(s) of at least 9% naturally come into consideration as additional constituents. The concentration of these copolymers is generally equal to or higher than 0.05% (in weight with relation to the entire composition), and preferably higher than 0.1%. It is generally equal to or lower than 15%, preferably than 10% and most preferably than 5%. A mixture of EVA

an EMA, preferably in a total amount of at least 0.1%, or even at least 1%, but not exceeding 5%, gives good results. It makes it namely possible to make welds with very reproducible peel strengths, which is very useful for making items with a peelable seal, like multi-chamber bags or pouches including a permanent, outer seal and at least one peelable seal.
The composition according to the present invention may easily be processed in any kind of object, from a flat one (like a film or sheet) to a three dimensional one {UKQ a container or a tube), and either into a monolayer structure or into a multilayer one.
Preferably, the present invention relates to a film or a tube comprising at least one layer including the above described composition.
The term "film" is used to denote a thin, flat structure (in the case of cast films for instance) or a tubular one (in the case of blown films for instance) which generally has a thickness of 1000 \irn or less, preferably 500 \na or less, or even 250 Jim or less. In practice, a thickness of 90 (ira or more is suitable, or even 140 pm or more. The term "tube" is used to denote a tubular structure which generally has a wall-thickness of 200 \im or more, preferably 500 \im or more. In practice, this thickness is often lower than 2500 nm. Such tubes can serve as a port member for a medical packaging unit (like for instance a container, pouch, bag and the like).
Preferably, the composition described above is used in a multilayer structure (film or tube) which includes several layers providing specific properties like barrier properties, sealability etc. In a preferred embodiment, the composition is included in the sealing layer of the structure (film or tube). By "sealing layer" is meant a layer which actually melts during welding (either permanent or peelable seals), which is usually a surface layer and has in general the lowest melting point of the structure. It is namely so that the SI resin (as being a thermoplastic elastomer with glass transition temperatures below 0°C) is soft at ambient temperatures or above and that the s-PP ha£ a rather low melting point so that their mixture shows excellent sealability. In this embodiment, as already explained above, the sealing layer preferably comprises additionally EVA and/or EMA, in the amounts specified above, but preferably equal to or less than 5% in weight in order not to loose transparency.
Multilayer structures (like films or tubes) according to the present invention may include at least one barrier layer comprising resins like EVOH, PA, polyester, LCP (liquid crystal polymer),... or their mixtures. In a preferred

embodiment, pure EVOH is used as barrier resin, more particularly an EVOH with an ethylene content in the range between 20 and 45 mol%, preferably between 25 and 40 mol% and most preferably around 30 mol% this to withstand steam sterilization at 121°C/250 °F. A suitable commercial grade of EVOH is Kuraray EVAL™ 101B (27 mol% ethylene). In another preferred embodiment, EVOH is mixed/blended with polyamide (PA) to improve barrier properties at higher humidity. Examples of such PA resins are PA 11 or PA 12 (for instance Rilsan^ or Rilsan^A from Atofina), PA6/66 (for instance Capron® CF120 ZI from BASF) or FDA 21 CFR 177.1500 and EU directive 2007/72/EC compliant PA6 (like for instance Capron® from BASF, Durethan® T40 from Bayer) or PA 6/12 (Zytel18* from Dupont). The ones which have a melting point (measured by DSC {endotherm peak temperature}) around 200°C are preferred. The ones having a Vicat softening temperature (ISO306 50N;120°C/h) below 150°C are preferred as well to gain some flexibility. Yet in another preferred embodiment, a layer of EVOH is combined with at least one layer of a suitable PA (PA11,12, 6, 6/66, 612 and the like) as mentioned above in order to get maximum transparency in combination with high barrier properties. For medium barrier films a layer of a suitable PA (PA113 12, 6, 6/66, 612 and the like) may be included
To adhere polyolefin containing layers to such barrier layers, tie layers like for instance maleated thermoplasts (Bynel® from Dupont, Admer® from Mitsui, Orevac® from Atofina, Priex8* from Solvay,...) and/or thermoplastic elastomers (Rraton® FG 1901, FG 1921, FG 1924) are used. Of particular interest is a maleated s-PP eventually blended/mixed with a maleated thermoplastic elastomer.
According to one embodiment, the film includes as barrier layer, a layer including a cyclic olefin resin (COP) which may be a thermoplastic or an elastomer, or a mixture of both. This allows to get better barrier properties against the migration of alcohols, acids and water (or vapour).
The term "COP" is understood to mean a homo- or a copolymer of a C5 to C12 cyclic monomer and/or di-cyclic monomer (dimer), which may bear side chains so as to reach a total of 5 to 30 C. Cycloolefin copolymers in general consist besides the cyclic monomer of a C3 to C10 olefin monomer. They are in general amorphous or semi cristallin plastics whose softening points and glass transition temperatures (Tg) can be adjusted over a wide temperature range by varying the proportion of comonomer. Those having a cyclic monomer content above approximately 20 wt% are relatively brittle and have a Tg above room

temperature. TTiose having a cyclic olefin content below approximately 20 wt% are having a Tg below room temperature and are therefore elastomeric in nature (having an elongation at break of at least 50%). Of particular interest are those having a cyclic olefin content of at least 40 wt%, preferably of 50 wt% or more and most preferably those having a cyclic olefin content of 60 wt% or more and those having a cyclic olefin content of 20 wt% or less or 2% or more. Of particular interest are the ones with a Tg of 121 °C or more while they are steam sterilisable and the ones having a cyclic olefin content of less than 20 wt% while they show some cristallinity and thus having a melting point, which is advantageous for sealing and other heat treatments. The applicant found that surprisingly, when mixing a COP with a high Tg and one with a low Tg, certain properties in terms of flexibility, transparency, sterilisability and sealabilty, which are most wanted in the art for medical applications could be combined.
The basic cyclic monomer unit can be cyclopentene, cyclohexene, norbornene, dicyclopentadiene, tetracyclododecene or methyhetracyclododecene. It is preferably norbornene :


or cyclic, like in dicyclopentadiene (which is in fact norbomene with a cyclopentadiene side chain) :

The olefin is advantageously efhylene. The COP is preferably a homo- or copolymer of norbornene with or without side chains; it is more preferably either a homopolymer of norbomene (with or without side chains, but preferably with cyclopentadiene as side chain, i.e. it is preferably a homqpolymer of dicyclopentadiene), or a copolymer of norbomene (with or without side chains) and ethylene. In the latter case, the content of ethylene is advantageously between 80 and 98 wt% or below 60 wt%.
According to this embodiment, the COP may be blended with another polymer or with a hydrogenated hydrocarbon. Advantageously, the COP is blended with s-PP in order to make the film/tube more tough and ductile and impact and puncture resistant, easy to weld and to steam sterilise, but other thermoplastic polymers/elastomers and hydrocarbons may be used as well to dilute/ blend the COP. These are advantageously chosen from not very crystalline or amorphous polyolefins or hydrocarbons like the SI resins described above or those of the following types :
- olefinic copolymers composed of at least two C2 to C10 alkenes, comprising
at least 60% by weight of ethylene and/or of propylene and/or of butene but
not comprising more than 90% by weight of the same comonomer, or from
- olefinic copolymers comprising ethylene and/or propylene and/or butene and
from 10 to 40% by weight of one or more different comonomers which are
preferably chosen from C5 to C1o olefins [for instance copolymers of ethylene
and 1 -octene in an amount such to have linear low density polyethylene
(LLDPE), very low density polyethylene (VLDPE) or ultra low density
polyethylene (ULDPE)] and carboxylic acid or ester groups, for example
vinyl acetate, methyl, ethyl or butyl acrylate and methyl methacrylate, or
carbon monoxide, or from

- elastomeric copolymeis or terpolymers with blocks of styrene and of one or
more olefins (for example, copolymers of the styrene-butadiene-styrene
(SBS), styrene-ethylene-butylene-styrene (SEBS) or styrene-ethylene-
propylene-styrene type (SEPS), and the like), or from
- highly branched homopolymers [for example, low density polyethylene
(LDPE) or medium density polyethylene (MDPE)] or from
- hydrogenated hydrocarbons like paraffin or paraffinic oil.
Advantageously, the COP comprising layer comprises at least one resin chosen between SI resins, styrene-ethylene-butylene-styrene (SEBS), eventually including styrene-etbylene-butylene (SEB), styrene-ethylene-propylene-styrene (SEPS), eventually including styrene-ethylene-propyiene (SEP), and etbylene-1-octene copolymers (preferably made by metallocene technology). SI resins, SEBS and/or SEPS are preferred because they allow to make both permanent seals and pealable seals (at a lower temperature) and because they improve its impact strength. The total concentration of these resins is generally equal to or higher than 1 % (in weight with relation to the entire layer composition), and preferably equal to or higher than 5%. It is generally equal to or lower than 39%, preferably than 30%.
Since COP resins are sensitive to grease, even in low amounts such as when touching or manipulating it, the COP comprising layer according to this preferred embodiment of the present invention is advantageously an internal layer, comprised in between two other layers. One of these layers may be the SI and s-PP comprising layer.
The films/tubes according to the present invention may also include a high melt temperature (>130°C), flexible, transparent outer layer (i.e. a layer on the outside of the structure, on the other side of the sealing layer). This layer may comprise a thermoplastic polyester elastomer (TPE) and/or PEBA (polyester block amide copolymers). TPE resins are composed of alternating hard poly-1,4-butanediol and/or poly(alkylene oxide)glycol, terephthalate acid or 1,4-cyclohexane-dicarboxylate and 1,4-cyclohexane-dimefhanol block copolymers connected by ether and ester linkages. Examples of such TPEs are ECDEL® resins (PCCE or polycyclohexane dicarboxylic acid - cyclohexane dimethanol -elastomer or copolyester based on 1,4-cyclohexanedicarboxylic acid, 1,4* cyclohexanedimethanol, and poly (oxytetxamethylene) glycol) commercialised by Eastman, HYTREL® resins from Dupont, LOMOD® resins from GE and RITEFLEX® resins from Celanese. PEBA resins are composed of polyamide

blocks and at least a block of poly(alkylene oxide). Such resins are for example commercialized by Atofina chemicals PEBAX®.
The above mentioned outer layer of the film according to the present invention may also comprise an SI or SEES, SBS,... resin (i.e. block copolymers having outer blocks of styrene and a midblock comprising at least one polyoleftn or isoprene, as described above) to reduce sticking of the film to itself when stored (folded or rolled up) and/or to its packaging.
Besides the sealing layer, barrier layer and outer layers mentioned above, the films/tubes according to the invention may include at least one additional internal layer, with a melting point in between those of the sealing and outer layers and including similar polymers (chosen between one or more of SI resins, s-PP, other PP resins, elastomers,.. .). F°r instance, it may be of interest from an economical point of view to include a layer made of scraps (i.e. production waste of films/tubes according to the present invention), as internal layer in the films/tubes described above. Whatever the number of layers, it is generally interesting to have a melting point gradient in the structure, in which the layer with the lowest melting point being the sealing layer.
According to an embodiment of the present invention, the multilayer structure (film or tube) described above comprises a more than 40% in weight of metallocene technology PO resins from which at least 30 wt% PP resins (either syndiotactic or isotactic, either homo- or copolymer, for instance with ethylene). The choice of PO resins obtained through metallocene catalyst technology improves the purity (content of extractibles and catalytic residues) of the entire structure. These metallocene PP resins are preferably s-PP and/or i-PP.
Films according to the present invention may be fully or partially (partially meaning with a window) embossed (i.e. may carry a pattern in relief) by any known technique in order to prevent blocking.
Films according to the present invention are very easy to weld and can therefore very conveniently be used to make bags. Accordingly, the present invention also relates to a bag made by welding a film as described above. Preferably, this bag is a multi-chamber bag including at least one permanent, outer seal and at least one peelable seal. By permanent seal is meant a seal which cannot be peeled easily manually and which generally shows a peel strength of at least 2000 N/m (according to ASTM/ISO F88), or even at least 3000 N/m, while a peelable seal is a seal easy to peel manually and which generally shows a peel strength of less than 2000 N/m. The optimal temperature, pressure and welding time ranges to respectively get a permanent and a peelable seal with a given

structure can very easily be determined by one of ordinary skiU in the art, using a few experiments. Generally, permanent and peelable seals are made using hot gas or hot tool welding, the latter being preferred.
The films, tubes and bags according to the present invention may be used for any application were their above mentioned properties are valuable. The medical field is such an application area. Bags according to the present invention are indeed particularly suitable for containing medical fluids like dialysis, infusion, nutrition,... solutions.
Finally, the polymer composition according to the present invention can also advantageously be used in injection moulded articles. It is namely so that in most application area of the above mentioned film and bag, the latter have to be connected to some kind of apparatus (like a perfusion or dialysis apparatus for instance) and to perform this connection, often connecting parts are used, which are generally made by injection moulding. In order to have a complete system of the same polymer ingredients, and to benefit of the advantages thereof as set forth above, these injection moulded articles advantageously include the same polymer composition as the one described above.
The following examples serve to illustrate the invention. In those examples, the following polymer grades were used (s means syndiotactic; i means isotactic):
• s-PP is grade 1251 from Totalpetrochemicals with MFI 2 according to ASTM
Dl 238 and made by using a metallocene catalyst.
• Hydrogenated SI block copolymer is grade Hybrar 7125 from Kuraray.
• EVA1 has MFI is around 3 and about 18 wt%VA.
• EVA2 has MFI 2 according to ASTMD1238 190°C 2.16 kg and 18 %VA.
• EMA has 16 % MA with MFI 0.3 according to ASTM D1238 190°C 2.16 kg.
• i-PPl is grade HD601CF from Borealis.
• i-PP2 has MFI around 5.6, made by using a metallocene catalyst
• i-PP3 has MFI of 5 according to ASTM D 1238.
• i-PP4 has MFI around 2.
• i-PPEl Random Flexible Copolymer is grade SD233CF from Borealis.
• i-PPE2 Random Flexible Copolymer elastomeric is grade Vistamaxx ® 1100
from Exxonmobile, made by using a metallocene catalyst
• i-PPE3 Random Flexible Copolymer elastomeric is grade Versify® 2300
from Dow.
• i-PP copolymer is grade RD208CF from Borealis.
• COP1 has MFI of 30 (ISO 1133,260 °C, 2,16 kg)

• C0P2 has MFI of 13 (ISO 1133, 260 ° C, 2,16 kg)
• COP3 has at least 80 wt% of Ethylene.
The haze and the clarity of the films were measured as total luminous transmittance according to ASTM D1003.
The films were made by means of coextiusion (flat die and feedblock), each layer having its own independent single screw extruder (diameter 60 and 45 mm and length of the barrel of 25 D). The temperature settings on the die, feedblock and adapters were around 210 °C. The temperature settings on the cylinder are ranging from 150 to 210 °C, depending on the polymer used. Single layer tubes were made using a 45mm single screw extruder. The tubes were made using an annular die. Extrusion temperature was around 210°C. The bags were made by hot tool welding of these films with the tubes under the following conditions : temperature is between 120 up to 150°C, pressure is 6 bar, welding time is 1.4 seconds for the circumferential weld The tubes were preheated at 80°C. Steam sterilization was performed at 121 °C for 30 minutes using a steam autoclave as described in applicable USP and / or EP guidelines. Comparative example 1 :
A multilayer film including the following layers was coextruded : layer A (Outer layer 40 microns) comprising a blend of 50 wt % i-PPl with 50 wt % of i-PP2, layer B (middle layer 110 microns) consisting of i-PP 75 wt % random flexible1 i-PPEl copolymer and 25 wt % of i-PP2 and layer C (sealing layer* 40 microns) consisting of a blend of i-PP copolymer 75 weight %, SEBS 25 weight %. The total thickness of the film was 190 microns. A bag of this film showed permanent circumferential seal at a welding temperature of 148°C. The haze of the film after sterilization with steam was 23 %. Comparative example 2:
A multilayer film including the following layers was coextruded : Layer A (outer layer): blend of 90 wt % i-PPl and 10 wt % SEBS. Layer Bl : i-PP3 (100 wt %).
Layer B2 : blend made of 75 wt % i-PP3 and 25 wt % SEBS. Layer C (sealing layer): blend made of 75 wt % i-PP3 and 22 wt % SEBS and 2 wt % EVA1 and 1 wt % EMA.
The total thickness of the film was 200 micron, with a layer Bl of 40 micron. Its haze after sterilization was 26 %. Comparative example 3 :

A multilayer film including the following layers was coextruded. Layer A (Outer layer 40 microns) comprising 100 wt % i-PPl. Layer B (sealing layer) consisting of 50 wt % random flexible i-PPEl copolymer and 50 wt % of i-PP4. The total thickness of the film was 200 microns. A bag of this film showed permanent circumferential seal at a welding temperature of 148°C. Haze of the film after sterilization with steam was 30 %. Example 4 :
A film according to the present invention including the following layers was coextruded Layer A (Outer layer 40 microns) comprising a blend of
50 % i-PPl with 50 % of i-PP2. Layer B (middle layer 110 microns) consisting
of 75 wt % random flexible i-PPEl copolymer and 25 wt % of i-PP2. Layer C
(sealing layer 40 microns) consisting of a blend of s-PP 75 wt %, hydrogenated
51 block copolymer 25 weight %. The total thickness of the film was
190 microns. A bag of this film showed permanent circumferential seal at a welding temperature of 135°C. Haze of the film after sterilization with steam was 14%. Example 5 :
A film according to the present invention including the following layers was coextruded : Layer A (outer layer): blend of 90 wt % i-PPl and 10 wt % SEBS.
Layer Bl : i-PP3 (100 wt %)
Layer B2 : blend made of 75 wt % s-PP and 25 wt % hydrogenated SI block copolymer.
Layer C (sealing layer): blend made of 75 wt % S-PP3 and 22 wt % hydrogenated SI block copolymer and 2 wt % EVA1 and 1 wt % EMA. The total thickness of the film was 200 micron, with layers A and Bl both of 40 micron. Its haze after sterilization was 5 %. A bag of this film showed permanent circumferential seal at a welding temperature of 135°C Example 6:
A film according to the present invention including the following layers was coextruded : Layer A (outer layer): blend of 90 wt % i-PPl and 10 wt % SEBS.
Layer Bl : blend of 45 wt % COP1 and 40 wt % COP2 and 15 wt % s-PP. Layer B2 : blend made of 75 wt % s-PP and 25 wt % hydrogenated SI block copolymer.

Layer C (sealing layer): blend made of 75 wt % S-PP3 and 22 wt % hydrogenated SI block copolymer and 2 wt % EVA2 and 1 wt % EMA. The total thickness of the film was 200 micron, with a layers A and Bl both of 40 micron. Its haze after sterilization was 6 %. A bag of this film showed permanent circumferential seal at a welding temperature of 135°C Example 7 :
A film according to the present invention including the following layers, was coextruded. Layer A (Outer layer 40 microns) comprising 100 wt % i-PPl. Layer B consisting of a blend of 50 wt % s-PP and 50 wt % of a hydrogenated SI block copolymer. Layer C (sealing layer) consisting of 50 wt % random flexible i-PPEl copolymer and 50 wt % of i-PP4. The total thickness of the film was 200 microns. A bag of this film showed permanent circumferential seal at a welding temperature of 148°C. Haze of the film after sterilization with steam was 25 %. Example 8 :
A film according to the present invention including the following layers, was coextruded. Layer A (Outer layer 40 microns) comprising 100 wt % i-PPl. Layer B consisting of a blend of 50 wt % s-PP and 50 wt % of a hydrogenated SI block copolymer. Layer C (sealing layer) consisting of 50 wt % random flexible i«PPE2 copolymer and 50 wt % of i-PP4. The total thickness of the film was 200 microns. A bag of this film showed permanent circumferential seal at a welding temperature of 148°C. Haze of the film after sterilization with steam was 15%. Example 9 :
A film according to the present invention including the following layers, was coextruded. Layer A (Outer layer 40 microns) comprising 100 wt % i-PPl. Layer B consisting of a blend of 50 wt % s-PP and 50 wt % of a hydrogenated SI block copolymer. Layer C (sealing layer) consisting of 50 wt % random flexible i-PPE3 copolymer and 50 wt % of i-PP4. The total thickness of the film was 200 microns. A bag of this film showed permanent circumferential seal at a welding temperature of 148°C. Haze of the film after sterilization with steam was 19 %. Example 10:
A film according to the present invention including the following layers, was coextruded. Layer A (Outer layer 40 microns) comprising 100 wt % i-PPl. Layer B consisting of a blend of 25 wt % s-PP and 25 wt % of a hydrogenated SI

block copolymer, 25 wt % of random flexible i-PPE2 copolymer and 25 wt % of
i-PP4. Layer C (sealing layer) consisting of 70 wt % random flexible i-PPE2
copolymer and 30 wt % of i-PP4. The total thickness of the film was
200 microns. A bag of this film showed permanent circumferential seal at a
welding temperature of 142°C. Haze of the film after sterilization with steam
was 19%.
Comparative example 11 :
A multilayer film including the following layers was coextruded. Layer A (Outer layer 40 microns) comprising a blend of 50 % i-PPl with 50 % of i-PP. Layer B : 75 wt % i-PPEl and 25 % wt hydrogenated SI block copolymer. Layer C : comprising a blend as described in WO03/097739 consisting of 85 wt % COP3 and 15 wt % of s-PP. The haze after sterilization was 17 %. Example 12:
A film according to the present invention including the following layers, was coextruded. Layer A (Outer layer 40 microns) comprising a blend of 50 % i-PPl wilh 50 % of i-PP. Layer B : Layer B consisting of a blend of 25 wt % s-PP and 25 wt % of a hydrogenated SI block copolymer, 25 wt % of random flexible i-PPE2 copolymer and 25 wt % of i-PP4. Layer C : comprising a blend as described in WO03/097739 consisting of 85 wt % COP3 and 15 wt % of s-PP. The haze after sterilization was 6 %. Example 13:
A film according to the present invention including the following layers, was coextruded. Layer A (Outer layer 40 microns) comprising a blend of 50 % i-PPl with 50 % of i-PP. Layer B : Layer B consisting of a blend of 75 wt % s-PP and 25 wt % of a hydrogenated SI block copolymer. Layer C : comprising of COP3. The haze before sterilization was 4 %.







CLAIMS
1 - Polymer composition comprising a thermoplastic elastomer including
styrene and isoprene and/or vinylisoprene units (SI) and a syndiotactic
polypropylene (s-PP).
2 - Polymer composition according to claim 1, in which the SI is at least
partially hydrogenated.
3 - Multilayer structure at least one layer including a polymer composition
according to claim 1 or 2.
4 - Multilayer structure to the preceding claim, which is a multilayer film
or tube and in which fee layer including the polymer composition according to
claim 1 or 2 is the sealing layer.
5 - Film or tube according to the preceding claim, in which the sealing
layer comprises additionally EVA and/or EMA.
6 - Film or tube according to any of claims 4 or 5, having at least one
barrier layer comprising resins like EVOH (ethylene vinlyl alcool copolymer),
PA (polyamide), polyester, LCP (liquid crystal polymer) or mixtures thereof, or a
cyclic olefin polymer (COP).
7 - Film or tube according to any of claims 4 to 6, having an outer layer
comprising a thermoplastic polyester elastomer (TPE) and/or a PEBA (polyester
block polyamide).
8 - Film or tube according to any of claims 4 to 7, which comprises a major
more than 40 % in weight of metallocene technology PO (polyolefin) resins from
which at least 30 wt % PP (polypropylene) resins.
9 - Bag made by welding a film according to any of claims 3 to 8.
10 - Injection moulded article comprising a polymer composition
according to any of claims 1 or 2.


Documents:

2783-CHENP-2006 AMENDED CLAIMS 09-11-2011.pdf

2783-CHENP-2006 AMENDED PAGES OF SPECIFICATION 09-11-2011.pdf

2783-CHENP-2006 FORM-1 09-11-2011.pdf

2783-CHENP-2006 FORM-3 09-11-2011.pdf

2783-CHENP-2006 FORM-3 31-01-2012.pdf

2783-CHENP-2006 OTHER PATENT DOCUMENT 09-11-2011.pdf

2783-CHENP-2006 AMENDED CLAIMS 04-04-2012.pdf

2783-CHENP-2006 CORRESPONDENCE OTHERS 18-03-2011.pdf

2783-CHENP-2006 CORRESPONDENCE OTHERS 31-01-2012.pdf

2783-CHENP-2006 CORRESPONDENCE OTHERS 04-04-2012.pdf

2783-CHENP-2006 CORRESPONDENCE OTHERS 15-03-2012.pdf

2783-CHENP-2006 CORRESPONDENCE OTHERS 20-04-2012.pdf

2783-CHENP-2006 EXAMINATION REPORT REPLY RECEIVED 09-11-2011.pdf

2783-CHENP-2006 FORM-13 28-11-2007.pdf

2783-chenp-2006-abstract.pdf

2783-chenp-2006-claims.pdf

2783-chenp-2006-correspondnece-others.pdf

2783-chenp-2006-description(complete).pdf

2783-chenp-2006-form 1.pdf

2783-chenp-2006-form 3.pdf

2783-chenp-2006-form 5.pdf

2783-chenp-2006-pct.pdf


Patent Number 252894
Indian Patent Application Number 2783/CHENP/2006
PG Journal Number 23/2012
Publication Date 08-Jun-2012
Grant Date 07-Jun-2012
Date of Filing 28-Jul-2006
Name of Patentee RENOLIT AG
Applicant Address Horchheimer Strasse 50, 67547 Worms
Inventors:
# Inventor's Name Inventor's Address
1 KARSTEN, Petrus Havikshoek, 27, NL-1602 DL ENKHUIZEN
2 MULKENS, Edmond Kennedyboulevard 412 Noord-Holland, NL-1931XG EGMOND AAN ZEE
PCT International Classification Number C08L25/10,23/10,A61J1/00,C08L53/02
PCT International Application Number PCT/EP2005/050370
PCT International Filing date 2005-01-28
PCT Conventions:
# PCT Application Number Date of Convention Priority Country
1 04100347.6 2004-01-30 EUROPEAN UNION