EP1713857A1 - High-frequency-weldable polymer mixture and processes for using the same - Google Patents

High-frequency-weldable polymer mixture and processes for using the same

Info

Publication number
EP1713857A1
EP1713857A1 EP05707268A EP05707268A EP1713857A1 EP 1713857 A1 EP1713857 A1 EP 1713857A1 EP 05707268 A EP05707268 A EP 05707268A EP 05707268 A EP05707268 A EP 05707268A EP 1713857 A1 EP1713857 A1 EP 1713857A1
Authority
EP
European Patent Office
Prior art keywords
copolymer
heterophasic
lomin
mfr
content
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Withdrawn
Application number
EP05707268A
Other languages
German (de)
French (fr)
Inventor
Kai Torsdal
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Borealis Technology Oy
Original Assignee
Borealis Technology Oy
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Borealis Technology Oy filed Critical Borealis Technology Oy
Priority to EP05707268A priority Critical patent/EP1713857A1/en
Publication of EP1713857A1 publication Critical patent/EP1713857A1/en
Withdrawn legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/10Homopolymers or copolymers of propene
    • C08L23/14Copolymers of propene
    • C08L23/142Copolymers of propene at least partially crystalline copolymers of propene with other olefins
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C65/00Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor
    • B29C65/02Joining or sealing of preformed parts, e.g. welding of plastics materials; Apparatus therefor by heating, with or without pressure
    • B29C65/04Dielectric heating, e.g. high-frequency welding, i.e. radio frequency welding of plastic materials having dielectric properties, e.g. PVC
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29CSHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C66/00General aspects of processes or apparatus for joining preformed parts
    • B29C66/70General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material
    • B29C66/71General aspects of processes or apparatus for joining preformed parts characterised by the composition, physical properties or the structure of the material of the parts to be joined; Joining with non-plastics material characterised by the composition of the plastics material of the parts to be joined
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B32LAYERED PRODUCTS
    • B32BLAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00Layered products comprising a layer of synthetic resin
    • B32B27/32Layered products comprising a layer of synthetic resin comprising polyolefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J5/00Manufacture of articles or shaped materials containing macromolecular substances
    • C08J5/18Manufacture of films or sheets
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2019/00Use of rubber not provided for in a single one of main groups B29K2007/00 - B29K2011/00, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/04Polymers of ethylene
    • B29K2023/08Copolymers of ethylene
    • B29K2023/083EVA, i.e. ethylene vinyl acetate copolymer
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2023/00Use of polyalkenes or derivatives thereof as moulding material
    • B29K2023/10Polymers of propylene
    • B29K2023/12PP, i.e. polypropylene
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2077/00Use of PA, i.e. polyamides, e.g. polyesteramides or derivatives thereof, as moulding material
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0085Copolymers
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B29WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29KINDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/0088Blends of polymers
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08JWORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
    • C08J2323/00Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers
    • C08J2323/02Characterised by the use of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Derivatives of such polymers not modified by chemical after treatment
    • C08J2323/10Homopolymers or copolymers of propene
    • C08J2323/14Copolymers of propene
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L23/00Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers
    • C08L23/02Compositions of homopolymers or copolymers of unsaturated aliphatic hydrocarbons having only one carbon-to-carbon double bond; Compositions of derivatives of such polymers not modified by chemical after-treatment
    • C08L23/04Homopolymers or copolymers of ethene
    • C08L23/08Copolymers of ethene
    • C08L23/0807Copolymers of ethene with unsaturated hydrocarbons only containing more than three carbon atoms
    • C08L23/0815Copolymers of ethene with aliphatic 1-olefins
    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L77/00Compositions of polyamides obtained by reactions forming a carboxylic amide link in the main chain; Compositions of derivatives of such polymers

Definitions

  • the present invention is directed to high-frequency-weldable polymer mixture, processes for using the same and to sheets or molded articles containing said polymer mixture.
  • the present invention relates to PP grades with high frequency welding properties and to processes for using the same in blow moulding, sheet extrusion, sheet calendaring, blown film, coating, cast film, injection moulding and fibre to none woven for automotive interior.
  • plastics parts can be welded in a high- frequency field.
  • thermoplastic parts in the form of sheets or molded articles to be connected are heated to the required welding temperature in the capacitor field of a high-frequency voltage source without an auxiliary die.
  • the sheets are seam-welded (overlapping seams welded so as to withstand shearing stress or peeling stress) .
  • High-frequency-weldable materials are, above all, thermoplastics with polar groups, i.e., plastics with molecules, atoms or side groups that cause a charge transfer in the molecule (dipoles) .
  • polar groups i.e., plastics with molecules, atoms or side groups that cause a charge transfer in the molecule (dipoles) .
  • the polar groupings carry out oscillations corresponding to the excitation frequency.
  • the oscillations lead to heat development in the thermoplastic.
  • the dielectric loss factor is generally used as a characteristic value for the transformation of electric field energy into heat.
  • the sheets are not connected along the entire surface. Welding is generally restricted to line-type or frame-type contours and heating is restricted to the respective welding web region.
  • polyolefins cannot be processed in this way.
  • polyolefin films or sheets generally are sealed by applying external heat directly to the portions that must be sealed.
  • the seal cycles are longer and the seals thus obtained are non- uniform and of poor quality, when compared with the seal cycles of a radio-frequency apparatus and the seals thereby obtained.
  • EP-A-0 406 568 describes a polypropylene-polyamide molded compound which, in addition to a polypropylene ho opolymer and/or a polypropylene copolymer and a polyamide, contains an olefinic unsaturated carboxylic acid and/or an olefinic unsaturated carboxylic acid derivative.
  • Said EP-A-0 406 568 contains no reference to the high-frequency weldability of the described molded compound.
  • DE-A-41 42 271 describes molded articles which contain essentially polyolefins, polyamides and adhesion promoters or bonding agents.
  • the bonding agent is preferably a copolymer of styrene and ethylene butylene blocks grafted with maleic anhydride.
  • Said propylene-polyamide compounds have the disadvantage that they have a low dielectric loss factor at room temperature, as a result of which they can only absorb small amounts of energy in the high-frequency alternating field. Therefore, a disadvantageously high energy input and high welding power are required for welding this material.
  • the dielectric loss factor increases sharply as the heating of the material caused by the absorption of energy in the high-frequency field increases, resulting in a significant drop in the breakdown voltage or dielectric strength and an increased risk of dielectric breakdown. This leads to an increased reject rate.
  • copolymers of ethylene and vinyl acetate are high-frequency-weldable.
  • JP-A- 06287362 discloses a high-frequency weldable mixture of polyolefins with ethylene vinyl acetate copolymers (EVA) .
  • EVA ethylene vinyl acetate copolymers
  • molded articles made from mixtures of this kind have only a limited thermal dimensional stability. Sheets made from such mixtures with a high EVA content tend to stick together at elevated temperatures.
  • EP- Al-0 688 821 discloses a crystalline propylene homopolymer or copolymer, and certain amounts of an elasto eric olefin copolymer soluble in xylene at ambient temperature, which elastomeric olefin copolymer contains less than 40% by weight of ethylene and has an intrinsic viscosity from 1.5 to 4 dl/g which is compounded with a minor amount of at least one polymer capable of developing heat by absorption of radio-frequency electromagnetic radiation.
  • Another polymer mixture which is alleged to have a sufficient high-frequency weldability and further properties is described in EP-A1-0 849 324.
  • said high-frequency-weldable polymer mixture is containing a complex mixture copolymers of ethylene with co-monomers selected from vinyl esters of saturated carboxylic acids, including alkyl acrylates and -methacrylates, and ethylene homopolymers, ethylene copolymers, propylene homopolymers and/or propylene copolymers with grafted units of unsaturated carboxylic acids, dicarboxylic acids, their esters and/or anhydrides.
  • PVC In some technical fields, especially in the field of car interiors, PVC is the most commonly used plastic. PVC is currently the dominating polymer used in artificial leather applications due to it's combination of properties. The car industry has built on these properties and thus it is difficult to replace PVC by other polymers.
  • thermoplastic alloy composition comprising a blend of polypropylene copolymers, polyamide, ethylene propylene rubber, ethylene methyl acrylate, processing aid and wax is very useful for coating to carriers with hot mill calenders or extruders on both sides as high frequency weldable skin for auto interior items like luggage roller-shades, sun-visors, soft pockets, seat upholstery, gearstick stocking, tarpaulins for new car protection, industrial web and carriers.
  • the present invention is directed to a thermoplastic alloy composition
  • a thermoplastic alloy composition comprising a blend of polypropylene copolymers, polyamide, ethylene propylene rubber and optionally further ingredients like fillers, additives etc.
  • the composition comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 1-40% and having a MFR 0.1-15 g/10min; (b) 1-80 wt.-% of a heterophasic PP copolymer having a C 2 content of 1-40% and having a MFR 0.2-15 g/lOmin; (c) 20-35 wt.-% of a polyamide, (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer, whereby the weight percentages add up to 100 wt.-%.
  • the thermoplastic alloy composition comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 5-35% and having a MFR 0.1-15 g/lOmin; (b) 1-80 wt.-% of a heterophasic PP copolymer having a C 2 content of 1-35% and having a MFR 0.2-14 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; whereby the weight percentages add up to 100 wt.-%.
  • a processing aid and/or 0.5-15% preferably 0.1-10 wt.-%, more preferably 0.1-5 wt.-% of a lubricant can be contained in the inventive composition.
  • the inventive composition if it is intended for use in a blow-moulding process, comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 1-40% and having a MFR 0.1-2.0 g/lOmin; (b) 20-80 wt.-% of a heterophasic PP copolymer having a C 2 content of 1-40% and having a MFR 0.2-2.0 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; and (e) 1-10 wt.-% of a processing aid; whereby the weight percentages add up to 100 wt.-%.
  • the inventive composition if it is not used for a blow-moulding process but is intended to be used in a sheet extrusion process or a blown-film process, comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 1-40% and having a MFR 0.1-2.0 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C 2 content of 1-40% and having a MFR 0.2-2.0 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid. whereby the weight percentages add up to 100 wt.-%.
  • the inventive composition if it is intended to be used in a coating and castfilm process or an injection moulding process, comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 10-40% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C 2 content of 1-40% and having a MFR 5-14 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of a elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid. whereby the weight percentages add up to 100 wt.-%.
  • the inventive composition if it is intended to be used in a calendering process comprises additionally a lubricant as compound (f) .
  • the thermoplastic alloy composition comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 1-40% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C 2 content of 1-40% and having a MFR 5-14 g/lOmin; (c) 20-35 wt .
  • thermoplastic alloy composition if it is intended for use in a calendering process, comprises: (a) 10-50 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 5-35% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C 2 content of 5-35% and having a MFR 5-14 g/lOmin; (c) 20-30 wt.-% of a polyamide; (d) 15-25 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; and . (f) 0.1-10 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%.
  • thermoplastic alloy composition if it is intended for use in a calendering process, comprises: (a) 10-35 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 10-30% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C 2 content of 10-30% and having a MFR 5-14 g/lOmin; (c) 20-30 wt.-% of a polyamide; (d) 15-25 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; and (f) 0.1-5 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%.
  • the above mentioned polyolefin composition is convertible into sheets, films, fibers, and other moldable products that are sealable with dielectric heat generated by radio- frequencies and are free of gel-like and surface irregularities. Moreover, said composition has superior physical-mechanical properties, flexibility in particular. Consequently, the sheets and films obtained from the composition of the present invention are particularly useful for use in packaging, as well as for other applications that require high flexibility, softness and dielectric heat sealability, in particular for calendaring and embossing methods .
  • thermoplastic alloy composition comprises the following components in further preferred ranges:
  • component (a) 10-70 wt.-%, preferably 10-50 wt.-%, most preferably 10-35 wt.-% of a random-heterophasic PP-copolymer having a C 2 content of 1 to 40%, preferably 5 to 35% and having a MFR 0.1-15 g/lOmin, preferably 0.1-14 g/lOmin, more preferably 0.1-10 g/lOmin is used in accordance with the teachings of the invention.
  • Said random-heterophasic PP copolymer is preferably a soft raheco which is, alone, suitable for use on conventional blown film lines. It has very good tear and impact strength and excellent heat sealing characteristics.
  • Said random-heterophasic PP copolymer is very soft due to the high molecular weight and mixable with the other grades in the recipe that is needed for a flexible skin. At the same time, the low temperature properties are excellent with soft surface. Said random-heterophasic PP copolymer is easy to process and has a smooth surface from die that is easy to emboss, mangle for glossiness or to stretch even to thin film.
  • the abbreviation "MFR" used in the invention means "Melt Flow Rate" of the respective compound at 230 °C and 2.16 kg load and was determined according to ISO 1133.
  • component (b) 1-80 wt.-%, preferably 20-70 wt.-%, most preferably 30-50 wt.-% of a heterophasic PP copolymer having a C 2 content of 1 to 40%, preferably 5 to 35 wt.-% and having a MFR of 0.2 to 15 g/lOmin, preferably 0.2 to 14 g/lOmin, more preferably 0.2 to 10 g/lOmin is used.
  • a product with higher MFR should be chosen, e.g. 5-14 g/lOmin. This component is part of the body and the MFR should vary with the application. The component could be used in various weight percentages, depending on the intended product and processing method.
  • Said heterophasic PP copolymer is preferably a high molecular weight, low melt flow rate polypropylene block copolymer having a high impact strength, good softness, low emission and easy to mix with other grades.
  • polyamides are used as component (c) .
  • the employed polyamide can be an amorphous or partially crystalline polyamide, wherein partially crystalline polyamides are preferred because of their thermal dimensional stability.
  • the polyamide preferably has a molecular weight of at least approximately 1000, preferably at least 5000.
  • the polyamides can be produced by polycondensation of equimolar amounts of saturated dicarboxylic acids with 4 to 12 carbon atoms, preferably 6 to 12 carbon atoms, per molecule with a diamine containing 4 to 12 carbon atoms per molecule. Suitable polyamides can also be produced by ring-opening polymerization of lactams .
  • polyamides examples include polyhexamethylene adipic acid amide (Nylon 6,6), polyhexamethylene sebacic acid amide (Nylon 6,10), polyhexamethylene dodecane dicarboxylic acid amide (Nylon 6,12), poly- ⁇ -caprolactam (Nylon 6) or polylauric acid lactam.
  • polyamides which have been produced by copolycondensation of at least two of the above-mentioned polymers or their synthesis components can also be used.
  • the polyamides are preferably linear and have a melting point above approximately 200 °C.
  • the polyamide content is approximately 20 to 35 percent by weight, preferably approximately 20 to 30 percent by weight.
  • Durethan obtainable from Dupont can be used as component (c) .
  • an elastomeric C2-C8-copolymer preferably with 20 to 25% octene, melt flow index like 0.75 to 1.25 dg/min at 100°C/2.16 kg and density of 0.867 - 0.873 g/cm 3 is used.
  • Said copolymer is an ethylene-octene copolymer that provides excellent flow properties and imparts good heat aging, compression set and weather resistance properties. Furthermore, said polymer balances stiffness and ductility, producing a higher modulus PP copolymer mixture.
  • said polymer mixture made with said copolymer (d) maintain their integrity in high-impact applications, even at -30°C. Combined with good flowability and part fill, this integrity allows downgauging to thinner parts, helping to reduce material and part costs.
  • the elastomeric C2-C8-copolymer content is approximately 15 to 35 percent by weight, preferably approximately 15 to 25 percent by weight.
  • Said melt flow index at 190 °C at 2.16 kg load was measured according to ASTM D1238, while the density was determined according to ISO 1183 if not otherwise indicated.
  • a processing aid is here intended to serve as compatibilisator for the other ingredients of the mixture.
  • Said processing aids are polymers which are mainly used to improve the performance of the polyolefins and other thermoplastics. Impact resistance properties of these plastics at low and ambient temperatures are enhanced by the incorporation of said processing aid polymers. Also, said polymers permit the compatibilisation of some of the other compounds which are dissimilar plastics to allow combinations of properties that could not be achieved otherwise .
  • polymers consisting of block segments of styrene monomer units and rubber monomer units can be used.
  • the most common structures are the linear A-B-A block types: styrene-butadiene-styrene (SBS) , styrene- isoprene-styrene (SIS) , styrene-ethylene/butylene-styrene type (SEBS) or styrene-ethylene/propylene-styrene (SEPS) .
  • SBS styrene-butadiene-styrene
  • SIS styrene-isoprene-styrene
  • SEBS styrene-ethylene/butylene-styrene type
  • SEPS styrene-ethylene/propylene-styrene
  • A-B-A type polymers there are specialized polymers of the radial (A-B)n type: (styrene-butadiene) n or (styrene-isoprene) n, and diblock (A-B) type: styrene- butadiene (SB) , styrene-ethylene/propylene (SEP) and styrene- ethylene/butylene (SEB) .
  • SB styrene-butadiene
  • SEP styrene-ethylene/propylene
  • SEB styrene- ethylene/butylene
  • component (f) 0.1-15 wt.-%, preferably 0.1-10 wt.-%, more preferably 0.1-5 wt.-% of a lubricant or mixtures thereof are compounded with the polymer components.
  • a lubricant conventional lubricants for improving the processability can be used as release and antiblocking agent for polyolefins flow promotion, internal lubricant and antiblocking and slip agent.
  • Component (f) is an aid for release of the molten polymer from the hot mills when the polymer is processed on a calander. Several waxes can be used whereby blooming and also odour are sometimes co-effects that must be avoided. Depending on the choice of the component (f) the amount can vary in the defined range.
  • composition of the present invention can contain additives commonly used in polymer materials, such as stabilizers, pigments and fillers.
  • processing PP grades on high frequency welding machines where the inventive compositions are to be used in the current PVC machinery is dependent of the polymer choice.
  • the HF-welding properties in this grade are solved within the grade recipe according to the invention.
  • composition according to the invention can be mentioned softness, low stress whitening, melt strength, elongation, impact, tear resistance, bond to substrate, grain retention, fogging, emission, and odour.
  • a further important characteristic of the inventive composition is that, after processing the grade in extruders, the composition can afterwards be assembled by confectioning in high frequency welding machines (27000 Hz) .
  • High-frequency in the sense of the present invention means applying a high-frequency alternating field with high intensity to the thermoplastic composition, whereby the polar groupings of the thermoplastic composition carry out oscillations corresponding to the excitation frequency produced during the process in the high-frequency welding machines. This oscillation of the polar groups leads to heat development in the thermoplastic.
  • the frequency to be used for this process ranges from about 1 to about 30 MHz, wherein 27 MHz, especially 27.12 MHz, is the most common welding frequency.
  • the production of the grade is done with a conventional compounding extruder, e.g. a twin screw extruder, and with loss in weight feeders with remote adjusting device to the complete process computer. Rising the temperature over 250 °C in middle part of the extruder for then to decrease again to 230 °C before cooling to pelletizing leads to an improved homogenisation of the polymers in the molten state.
  • a conventional compounding extruder e.g. a twin screw extruder
  • composition of the invention is also suitable for preparing a moulded article wherein at least one layer comprises the inventive composition of the kind being particularly suitable for blow moulding as claimed.
  • the present invention also refers to an article made of or coated with a layer comprising the inventive composition.
  • a layer comprising the inventive composition.
  • said layer is coated with a method making use of a high frequency welding process.
  • heterophasic block PP-copolymer BA202E, KSR4525, supplied by Borealis As polyamid: Durethan B30, supplied by Bayer
  • Marklube 280 supplied by Cromton or Licolube
  • MFR values for the polymers are as follows: MFR (230*C, 2.16 kg) SA233CF: 0,8 SD233CF: 7,0 BA202: 0,3
  • Sheets were made on a Kuhne-line GA3/900.
  • the barrel temperatures were set to 180 and up to 220 °C, and the die range from 220 to 250°C.
  • the films are made on an Ankutec FBA/AO/300/30 with a temperature of 190 to 240 °C on the barrel, die gap of 1 mm, blow-up ratio 3:1.
  • 0.3 mm thick films is made on a Kuhne-line GA3/900.
  • the barrel temperatures are set to 220 and up to 260 °C and then the die to 230 to 250°C.
  • the chill roll temperature is 25°C, line speed 8 m/min and using an air knife.
  • a Nestal 300 machine was used. A temperature of 220 to 260 °C on the barrel and a rather low injection speed was used. Tool temperatures was 15 to ' 30°C dependent of the shape.
  • Vanfree vam 1 wt . %
  • the thickness of the sheet or foil can vary from 2.0mm and down to 0.005mm. Welding of sheets being thicker than 0.5mm demand a stronger effect than for PVC. Preheating of the sheet may be used to speed up the process .
  • the typical thickness is 0.2 to 0.5mm for example to sun-visors with insert and welded ends.
  • the typical thickness is 0.2 to 0.5mm as inserts or pockets for interior.
  • a blown film can typical be blown from 0.020 to 0.5mm, but in this inventive application as liners, barrier and laminates it will preferably be from 0.05 to 0.5mm.
  • the grades can be used for coating of carriers like fabric, textiles, none woven, paper, foils or other substrates.
  • the products can be used for preparing artificial leather or roller shades, for seat or furniture upholstery, for pockets and soft mirrors in applications in doors or facia panels.
  • tarpaulins and roofing can be made, using the inventive PP grade.
  • Injection moulded parts of this grade can typically be attachments lugs, fixing devices or embossed labels for HF welding. None woven sheet for HF welding is actual as reinforcing carriers, backing for stitchery and seat skin. Also filters for person and product protection can be welded with this technique.
  • the inventive composition for example as sheets, can be processed by using the following HF welding method.
  • composition prepared as described above was converted into a sheet with a thickness of 200 to 500 micrometers by extruding it at 230°-250°C through a flat die extruder.
  • the resulting sheets have been test welded with a radio frequency sealing apparatus with a heatable electrode operating at 27 MHz and equipped with a pressure tool.
  • the welding begins when the ampere meter starts to indicate current. For this machine above, it increases from 0.25 up to 0.4 amp.
  • the press is adjusted to only force the molten polymer sheets together, and keep it until the weldzone is frozen. Using a sheet thickness of 0.3mm will lead to good welding results which are sufficiently strong to not be torn apart in the weldzone. Breakage happens besides the weldzone, and the strength is depending of the sheet or notches in the weld edges. As it is clear thicker sheets and moulded articles can also be processed, but need more power and longer time is needed. Accordingly, thinner films and fibres need less power and time.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Manufacturing & Machinery (AREA)
  • Crystallography & Structural Chemistry (AREA)
  • Materials Engineering (AREA)
  • Compositions Of Macromolecular Compounds (AREA)

Abstract

New High-frequency-weldable polymer mixtures, processes for using the same and to sheets or molded articles containing said polymer mixture are described. In more detail, the present invention relates to PP grades with high frequency welding properties and to processes for using the same in blow moulding, sheet extrusion, blown film, coating, calendaring, cast film, injection moulding and fibre to none woven for automotive interior.

Description

High-frequency-welda le polymer mixture and processes for using the same
The present invention is directed to high-frequency-weldable polymer mixture, processes for using the same and to sheets or molded articles containing said polymer mixture. In more detail, the present invention relates to PP grades with high frequency welding properties and to processes for using the same in blow moulding, sheet extrusion, sheet calendaring, blown film, coating, cast film, injection moulding and fibre to none woven for automotive interior.
Technological background
It is known that plastics parts can be welded in a high- frequency field. In this case, thermoplastic parts in the form of sheets or molded articles to be connected are heated to the required welding temperature in the capacitor field of a high-frequency voltage source without an auxiliary die. The sheets are seam-welded (overlapping seams welded so as to withstand shearing stress or peeling stress) .
High-frequency-weldable materials are, above all, thermoplastics with polar groups, i.e., plastics with molecules, atoms or side groups that cause a charge transfer in the molecule (dipoles) . When a thermoplastic of this kind enters a high-frequency alternating field, the polar groupings carry out oscillations corresponding to the excitation frequency. The oscillations lead to heat development in the thermoplastic. The dielectric loss factor is generally used as a characteristic value for the transformation of electric field energy into heat. As a rule, the sheets are not connected along the entire surface. Welding is generally restricted to line-type or frame-type contours and heating is restricted to the respective welding web region.
However, because of their non-polar character, polyolefins cannot be processed in this way. In fact, polyolefin films or sheets generally are sealed by applying external heat directly to the portions that must be sealed. However, the seal cycles are longer and the seals thus obtained are non- uniform and of poor quality, when compared with the seal cycles of a radio-frequency apparatus and the seals thereby obtained.
In order to be able to weld polyolefins in the high-frequency field also, U.S. Pat. No. 3.336.173 proposes mixing in polyamides with the polyolefins. However, molded articles made from such materials have the disadvantage that the obtained weld seams do not have adequate strength or that tearing occurs next to the weld seam.
A different solution is disclosed in EP-A-0 406 568 that describes a polypropylene-polyamide molded compound which, in addition to a polypropylene ho opolymer and/or a polypropylene copolymer and a polyamide, contains an olefinic unsaturated carboxylic acid and/or an olefinic unsaturated carboxylic acid derivative. Said EP-A-0 406 568 contains no reference to the high-frequency weldability of the described molded compound.
DE-A-41 42 271 describes molded articles which contain essentially polyolefins, polyamides and adhesion promoters or bonding agents. The bonding agent is preferably a copolymer of styrene and ethylene butylene blocks grafted with maleic anhydride. Said propylene-polyamide compounds have the disadvantage that they have a low dielectric loss factor at room temperature, as a result of which they can only absorb small amounts of energy in the high-frequency alternating field. Therefore, a disadvantageously high energy input and high welding power are required for welding this material.
On the other hand, the dielectric loss factor increases sharply as the heating of the material caused by the absorption of energy in the high-frequency field increases, resulting in a significant drop in the breakdown voltage or dielectric strength and an increased risk of dielectric breakdown. This leads to an increased reject rate.
Further, it is known that copolymers of ethylene and vinyl acetate are high-frequency-weldable. For example, JP-A- 06287362 discloses a high-frequency weldable mixture of polyolefins with ethylene vinyl acetate copolymers (EVA) . However, molded articles made from mixtures of this kind have only a limited thermal dimensional stability. Sheets made from such mixtures with a high EVA content tend to stick together at elevated temperatures.
A further HF-weldable polymer composition is described in EP- Al-0 688 821. Said EP-A1-0 688 821 discloses a crystalline propylene homopolymer or copolymer, and certain amounts of an elasto eric olefin copolymer soluble in xylene at ambient temperature, which elastomeric olefin copolymer contains less than 40% by weight of ethylene and has an intrinsic viscosity from 1.5 to 4 dl/g which is compounded with a minor amount of at least one polymer capable of developing heat by absorption of radio-frequency electromagnetic radiation. Another polymer mixture which is alleged to have a sufficient high-frequency weldability and further properties is described in EP-A1-0 849 324. According to said EP-A1-0 849 324, said high-frequency-weldable polymer mixture is containing a complex mixture copolymers of ethylene with co-monomers selected from vinyl esters of saturated carboxylic acids, including alkyl acrylates and -methacrylates, and ethylene homopolymers, ethylene copolymers, propylene homopolymers and/or propylene copolymers with grafted units of unsaturated carboxylic acids, dicarboxylic acids, their esters and/or anhydrides.
In some technical fields, especially in the field of car interiors, PVC is the most commonly used plastic. PVC is currently the dominating polymer used in artificial leather applications due to it's combination of properties. The car industry has built on these properties and thus it is difficult to replace PVC by other polymers.
Some other polymers have typically been able to compete with PVC in some properties, but have failed to compete in other properties. In that respect, the combination of both being calenderable and weldable with high frequency techniques - which has been possible for PVC - has been difficult to obtain.
In the last years, the car industry has invested both financially and intellectually in hot mill calendering for the production of foil, sheet or skin, and in high frequency welding units in the confectioning of the final products for car interiors. However, satisfying results with other polymers to replace PVC have not been obtained. It is therefore the need for plastics, preferably on polyolefin basis, having improved HF welding characteristics.
Surprisingly, it has been found out by the inventors that said requirements could be met by a specific polymer composition. According to the inventors, a thermoplastic alloy composition comprising a blend of polypropylene copolymers, polyamide, ethylene propylene rubber, ethylene methyl acrylate, processing aid and wax is very useful for coating to carriers with hot mill calenders or extruders on both sides as high frequency weldable skin for auto interior items like luggage roller-shades, sun-visors, soft pockets, seat upholstery, gearstick stocking, tarpaulins for new car protection, industrial web and carriers.
Therefore, the present invention is directed to a thermoplastic alloy composition comprising a blend of polypropylene copolymers, polyamide, ethylene propylene rubber and optionally further ingredients like fillers, additives etc. In more detail, the composition comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR 0.1-15 g/10min; (b) 1-80 wt.-% of a heterophasic PP copolymer having a C2 content of 1-40% and having a MFR 0.2-15 g/lOmin; (c) 20-35 wt.-% of a polyamide, (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer, whereby the weight percentages add up to 100 wt.-%.
In a preferred embodiment of the present invention, the thermoplastic alloy composition comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 5-35% and having a MFR 0.1-15 g/lOmin; (b) 1-80 wt.-% of a heterophasic PP copolymer having a C2 content of 1-35% and having a MFR 0.2-14 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; whereby the weight percentages add up to 100 wt.-%.
Optionally, 1-10 wt.-% of a processing aid and/or 0.5-15%, preferably 0.1-10 wt.-%, more preferably 0.1-5 wt.-% of a lubricant can be contained in the inventive composition.
Preferably, the inventive composition, if it is intended for use in a blow-moulding process, comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR 0.1-2.0 g/lOmin; (b) 20-80 wt.-% of a heterophasic PP copolymer having a C2 content of 1-40% and having a MFR 0.2-2.0 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; and (e) 1-10 wt.-% of a processing aid; whereby the weight percentages add up to 100 wt.-%.
Preferably, the inventive composition, if it is not used for a blow-moulding process but is intended to be used in a sheet extrusion process or a blown-film process, comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR 0.1-2.0 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C2 content of 1-40% and having a MFR 0.2-2.0 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid. whereby the weight percentages add up to 100 wt.-%.
Preferably, the inventive composition, if it is intended to be used in a coating and castfilm process or an injection moulding process, comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 10-40% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C2 content of 1-40% and having a MFR 5-14 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of a elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid. whereby the weight percentages add up to 100 wt.-%.
In a preferred embodiment, the inventive composition, if it is intended to be used in a calendering process comprises additionally a lubricant as compound (f) . Therefore, the thermoplastic alloy composition comprises: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C2 content of 1-40% and having a MFR 5-14 g/lOmin; (c) 20-35 wt . -% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; and (f) 0.1-15 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%. In a particular preferred embodiment the thermoplastic alloy composition, if it is intended for use in a calendering process, comprises: (a) 10-50 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 5-35% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C2 content of 5-35% and having a MFR 5-14 g/lOmin; (c) 20-30 wt.-% of a polyamide; (d) 15-25 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; and .(f) 0.1-10 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%.
In an especially preferred embodiment the thermoplastic alloy composition if it is intended for use in a calendering process, comprises: (a) 10-35 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 10-30% and having a MFR 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP copolymer having a C2 content of 10-30% and having a MFR 5-14 g/lOmin; (c) 20-30 wt.-% of a polyamide; (d) 15-25 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; and (f) 0.1-5 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%.
The above mentioned polyolefin composition is convertible into sheets, films, fibers, and other moldable products that are sealable with dielectric heat generated by radio- frequencies and are free of gel-like and surface irregularities. Moreover, said composition has superior physical-mechanical properties, flexibility in particular. Consequently, the sheets and films obtained from the composition of the present invention are particularly useful for use in packaging, as well as for other applications that require high flexibility, softness and dielectric heat sealability, in particular for calendaring and embossing methods .
In more detail, the thermoplastic alloy composition comprises the following components in further preferred ranges:
As component (a), 10-70 wt.-%, preferably 10-50 wt.-%, most preferably 10-35 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1 to 40%, preferably 5 to 35% and having a MFR 0.1-15 g/lOmin, preferably 0.1-14 g/lOmin, more preferably 0.1-10 g/lOmin is used in accordance with the teachings of the invention. Said random-heterophasic PP copolymer is preferably a soft raheco which is, alone, suitable for use on conventional blown film lines. It has very good tear and impact strength and excellent heat sealing characteristics. Said random-heterophasic PP copolymer is very soft due to the high molecular weight and mixable with the other grades in the recipe that is needed for a flexible skin. At the same time, the low temperature properties are excellent with soft surface. Said random-heterophasic PP copolymer is easy to process and has a smooth surface from die that is easy to emboss, mangle for glossiness or to stretch even to thin film. The abbreviation "MFR" used in the invention means "Melt Flow Rate" of the respective compound at 230 °C and 2.16 kg load and was determined according to ISO 1133.
As component (b) , 1-80 wt.-%, preferably 20-70 wt.-%, most preferably 30-50 wt.-% of a heterophasic PP copolymer having a C2 content of 1 to 40%, preferably 5 to 35 wt.-% and having a MFR of 0.2 to 15 g/lOmin, preferably 0.2 to 14 g/lOmin, more preferably 0.2 to 10 g/lOmin is used. For fiber and injection moulding, a product with higher MFR should be chosen, e.g. 5-14 g/lOmin. This component is part of the body and the MFR should vary with the application. The component could be used in various weight percentages, depending on the intended product and processing method. Said heterophasic PP copolymer is preferably a high molecular weight, low melt flow rate polypropylene block copolymer having a high impact strength, good softness, low emission and easy to mix with other grades.
As component (c) , polyamides are used. The employed polyamide can be an amorphous or partially crystalline polyamide, wherein partially crystalline polyamides are preferred because of their thermal dimensional stability. The polyamide preferably has a molecular weight of at least approximately 1000, preferably at least 5000. The polyamides can be produced by polycondensation of equimolar amounts of saturated dicarboxylic acids with 4 to 12 carbon atoms, preferably 6 to 12 carbon atoms, per molecule with a diamine containing 4 to 12 carbon atoms per molecule. Suitable polyamides can also be produced by ring-opening polymerization of lactams . Examples of suitable polyamides include polyhexamethylene adipic acid amide (Nylon 6,6), polyhexamethylene sebacic acid amide (Nylon 6,10), polyhexamethylene dodecane dicarboxylic acid amide (Nylon 6,12), poly-ε-caprolactam (Nylon 6) or polylauric acid lactam. Further, polyamides which have been produced by copolycondensation of at least two of the above-mentioned polymers or their synthesis components can also be used. The polyamides are preferably linear and have a melting point above approximately 200 °C. The polyamide content is approximately 20 to 35 percent by weight, preferably approximately 20 to 30 percent by weight. As example, Durethan obtainable from Dupont can be used as component (c) .
As component (d) , an elastomeric C2-C8-copolymer, preferably with 20 to 25% octene, melt flow index like 0.75 to 1.25 dg/min at 100°C/2.16 kg and density of 0.867 - 0.873 g/cm3 is used. Said copolymer is an ethylene-octene copolymer that provides excellent flow properties and imparts good heat aging, compression set and weather resistance properties. Furthermore, said polymer balances stiffness and ductility, producing a higher modulus PP copolymer mixture. In addition, said polymer mixture made with said copolymer (d) maintain their integrity in high-impact applications, even at -30°C. Combined with good flowability and part fill, this integrity allows downgauging to thinner parts, helping to reduce material and part costs. The elastomeric C2-C8-copolymer content is approximately 15 to 35 percent by weight, preferably approximately 15 to 25 percent by weight.
Said melt flow index at 190 °C at 2.16 kg load was measured according to ASTM D1238, while the density was determined according to ISO 1183 if not otherwise indicated.
As component (e) , 1-10 wt.-% of a processing aid is here intended to serve as compatibilisator for the other ingredients of the mixture. Said processing aids are polymers which are mainly used to improve the performance of the polyolefins and other thermoplastics. Impact resistance properties of these plastics at low and ambient temperatures are enhanced by the incorporation of said processing aid polymers. Also, said polymers permit the compatibilisation of some of the other compounds which are dissimilar plastics to allow combinations of properties that could not be achieved otherwise .
As preferred processing aids, polymers consisting of block segments of styrene monomer units and rubber monomer units can be used. The most common structures are the linear A-B-A block types: styrene-butadiene-styrene (SBS) , styrene- isoprene-styrene (SIS) , styrene-ethylene/butylene-styrene type (SEBS) or styrene-ethylene/propylene-styrene (SEPS) . In addition to the A-B-A type polymers, there are specialized polymers of the radial (A-B)n type: (styrene-butadiene) n or (styrene-isoprene) n, and diblock (A-B) type: styrene- butadiene (SB) , styrene-ethylene/propylene (SEP) and styrene- ethylene/butylene (SEB) . Melt flow of 14-28 g/lOmin (230°C- 5kg), Melanic Anhydride, Bound 1.4-2.0 w%, Specific Gravity 0.91 g/cc.
As component (f) , 0.1-15 wt.-%, preferably 0.1-10 wt.-%, more preferably 0.1-5 wt.-% of a lubricant or mixtures thereof are compounded with the polymer components. As said lubricant, conventional lubricants for improving the processability can be used as release and antiblocking agent for polyolefins flow promotion, internal lubricant and antiblocking and slip agent. Component (f) is an aid for release of the molten polymer from the hot mills when the polymer is processed on a calander. Several waxes can be used whereby blooming and also odour are sometimes co-effects that must be avoided. Depending on the choice of the component (f) the amount can vary in the defined range.
In addition to the above components, the composition of the present invention can contain additives commonly used in polymer materials, such as stabilizers, pigments and fillers.
In accordance with the invention, various recipes on the basis of the inventive composition can be provided for various applications. As it can be easily understood from the skilled man, the application machines for the products need the right viscosity and demands of the mechanical- and physical properties that are required can be achieved with the right combination of the mentioned products.
Furthermore, processing PP grades on high frequency welding machines where the inventive compositions are to be used in the current PVC machinery is dependent of the polymer choice. The HF-welding properties in this grade are solved within the grade recipe according to the invention.
As key properties for the composition according to the invention can be mentioned softness, low stress whitening, melt strength, elongation, impact, tear resistance, bond to substrate, grain retention, fogging, emission, and odour.
As a clear advantage compared to PVC is the reduced density of the product giving weight saving potentials, good ageing properties and accepted recycle systems.
A further important characteristic of the inventive composition is that, after processing the grade in extruders, the composition can afterwards be assembled by confectioning in high frequency welding machines (27000 Hz) .
"High-frequency" in the sense of the present invention means applying a high-frequency alternating field with high intensity to the thermoplastic composition, whereby the polar groupings of the thermoplastic composition carry out oscillations corresponding to the excitation frequency produced during the process in the high-frequency welding machines. This oscillation of the polar groups leads to heat development in the thermoplastic. The frequency to be used for this process ranges from about 1 to about 30 MHz, wherein 27 MHz, especially 27.12 MHz, is the most common welding frequency.
The production of the grade is done with a conventional compounding extruder, e.g. a twin screw extruder, and with loss in weight feeders with remote adjusting device to the complete process computer. Rising the temperature over 250 °C in middle part of the extruder for then to decrease again to 230 °C before cooling to pelletizing leads to an improved homogenisation of the polymers in the molten state.
The composition of the invention is also suitable for preparing a moulded article wherein at least one layer comprises the inventive composition of the kind being particularly suitable for blow moulding as claimed.
Consequently, the present invention also refers to an article made of or coated with a layer comprising the inventive composition. Preferably, said layer is coated with a method making use of a high frequency welding process. Examples
Depending on the specific uses, various preparation methods for molded articles can be used and the respective inventive composition can be adapted to said specific uses within the specified ranges as claimed.
All the used starting materials of the following examples are commercially available and indicated as follows:
As random-heterophasic PP-copolymer: SA233CF and SD233CF, supplied by Borealis
As heterophasic block PP-copolymer: BA202E, KSR4525, supplied by Borealis As polyamid: Durethan B30, supplied by Bayer
As elastomeric C2-C8-copolymer : Engage 8100, supplied by
DuPont Dow Elastomers
As lubricant: Marklube 280, supplied by Cromton or Licolube
FA 1, supplied by Clariant As processing aid: Kraton 1901X, supplied by Kraton or
Vanfree VAM, supplied by Vanderbilt Company
However, these compounds are exemplary only and not intended to limit the invention, as other products/compounds can be used, respectively.
The MFR values for the polymers are as follows: MFR (230*C, 2.16 kg) SA233CF: 0,8 SD233CF: 7,0 BA202: 0,3
KSR 4525: 7,0 Example 1
As a recipe composition for Blowmoulding of the polyolefin block:
SA233CF 13wt.%
BA202E 40wt.%
Engage 8100 25wt.%
Durethan B30 20wt.%
Kraton 1901X 2wt.%
An Uniloy MSA/S blow moulding machine was used with a temperature of 160 to 200 °C on the barrel and keeping a melt temperature in the range of 205-220 °C.
Example 2
As a recipe composition for Sheet extrusion of the polyolefin block:
SD233CF 13wt.%
KSR4525 40wt.%
Engage 8100 25wt.%
Durethan B30 20wt.%
Kraton 1901X 2wt.%
Sheets were made on a Kuhne-line GA3/900. The barrel temperatures were set to 180 and up to 220 °C, and the die range from 220 to 250°C.
Example 3
As a recipe composition for Blown film extrusion of the polyolefin block: SA233CF 13wt.%
BA202E 40wt.%
Engage 8100 25wt.%
Durethan B30 20wt.%
Kraton 1901X 2wt.%
The films are made on an Ankutec FBA/AO/300/30 with a temperature of 190 to 240 °C on the barrel, die gap of 1 mm, blow-up ratio 3:1.
Example 4
As a recipe composition for Coating and Castfilm extrusion of the polyolefin block:
SD233CF 13wt. g, . o
KSR4525 40wt. Q. - "O
Engage 8100 25wt. g, . *o
Durethan B30 20wt. Q. o
Kraton 1901X 2wt. g. . Ό
0.3 mm thick films is made on a Kuhne-line GA3/900. The barrel temperatures are set to 220 and up to 260 °C and then the die to 230 to 250°C. The chill roll temperature is 25°C, line speed 8 m/min and using an air knife.
Example 5
As a recipe composition for Injection Moulding of the polyolefin block:
SD233CF 13wt.%
KSR4525 40wt.%
Engage 8100 25wt.%
Durethan B30 20wt.% Kraton 1901X 2wt.%
A Nestal 300 machine was used. A temperature of 220 to 260 °C on the barrel and a rather low injection speed was used. Tool temperatures was 15 to'30°C dependent of the shape.
Example 6
As a recipe composition for Sheet calendering of the polyolefin block:
SA233CF 29 wt . %
KSR4525 18 wt . %
Engage 8100 25 wt . %
Durethan B30 20 wt . % Kraton 1901X 2 wt . %
Marklube 280 1.5 wt . %
Vanfree vam 1 wt . %
Schwabenthan Polymix 150P calendering machine was used. The temperature was 161°C.
Preparation
For soft sheet and easy welding, the thickness of the sheet or foil can vary from 2.0mm and down to 0.005mm. Welding of sheets being thicker than 0.5mm demand a stronger effect than for PVC. Preheating of the sheet may be used to speed up the process .
The various requirements for the sheets and moulded articles and applications thereof are explained below.
As blow molded part, the typical thickness is 0.2 to 0.5mm for example to sun-visors with insert and welded ends. As extruded sheet, the typical thickness is 0.2 to 0.5mm as inserts or pockets for interior. A blown film can typical be blown from 0.020 to 0.5mm, but in this inventive application as liners, barrier and laminates it will preferably be from 0.05 to 0.5mm.
For coating, the grades can be used for coating of carriers like fabric, textiles, none woven, paper, foils or other substrates. The products can be used for preparing artificial leather or roller shades, for seat or furniture upholstery, for pockets and soft mirrors in applications in doors or facia panels. Also tarpaulins and roofing can be made, using the inventive PP grade. Injection moulded parts of this grade can typically be attachments lugs, fixing devices or embossed labels for HF welding. None woven sheet for HF welding is actual as reinforcing carriers, backing for stitchery and seat skin. Also filters for person and product protection can be welded with this technique.
According to a preferred embodiment, the inventive composition, for example as sheets, can be processed by using the following HF welding method.
The composition prepared as described above was converted into a sheet with a thickness of 200 to 500 micrometers by extruding it at 230°-250°C through a flat die extruder. The resulting sheets have been test welded with a radio frequency sealing apparatus with a heatable electrode operating at 27 MHz and equipped with a pressure tool.
The sealing conditions were as follows:
Machine: FIAB, Type 2002, Series no. 1068, 27MHz, 2 kW Tool: 300mm x 5mm brass with Teflon tape. Base: table covered with Mylar or Teflon tape Parameters : Tuning wave. 80-90% Welding Time 7sec. Holding time after is also 7sec. Pressure 1.5 bar Sheet thickness 0.2-0.5mm
After start, the welding begins when the ampere meter starts to indicate current. For this machine above, it increases from 0.25 up to 0.4 amp. The press is adjusted to only force the molten polymer sheets together, and keep it until the weldzone is frozen. Using a sheet thickness of 0.3mm will lead to good welding results which are sufficiently strong to not be torn apart in the weldzone. Breakage happens besides the weldzone, and the strength is depending of the sheet or notches in the weld edges. As it is clear thicker sheets and moulded articles can also be processed, but need more power and longer time is needed. Accordingly, thinner films and fibres need less power and time.

Claims

Claims
1. A thermoplastic alloy composition comprising a blend of polypropylene copolymers, polyamide, ethylene propylene rubber and optionally further ingredients like fillers, additives, comprising: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.1-15 g/lOmin; (b) 1-80 wt.-% of a heterophasic PP block copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.2-15 g/lOmin; (c) 20-35 wt.-% of a polyamide, (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; whereby the weight percentages add up to 100 wt.-%.
2. A thermoplastic alloy composition according to claim 1, comprising: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 5-35% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.1-15 g/lOmin; (b) 1-80 wt.-% of a heterophasic PP block copolymer having a C2 content of 5-35% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.2-14 g/lOmin; (c) 20-35 wt.-% of a polyamide, (d) 15-35 wt.-% elastomeric C2-C8-copolymer; whereby the weight percentages add up to 100 wt.-%.
3. A thermoplastic alloy composition according to claim 1 or 2, comprising additionally 1-10 wt.-% of a processing aid and/or 0.5-15 wt.-%, preferably 0.1-10 wt.-%, more preferably 0.1-5 wt.-% of a lubricant.
4. A thermoplastic alloy composition according to claim 1 or 2, comprising additionally 1-10 wt.-% of a processing aid and/or 0.1-10 wt.-% of a lubricant.
5. A thermoplastic alloy composition according to claim 1 or 2, comprising additionally 1-10 wt.-% of a processing aid and/or 0.1-5 wt.-% of a lubricant.
6. The thermoplastic alloy composition according to claim 1 suitable for use in a blow-moulding process, comprising: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.1-2.0 g/lOmin; (b) 20-80 wt.-% of a heterophasic PP block copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.2-2.0 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; and (e) 1-10 wt.-% of a processing aid; whereby the weight percentages add up to 100 wt.-%.
7. The thermoplastic alloy composition according to claim 1 suitable for use in a sheet extrusion process or a blown film process, comprising: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.1-2.0 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP block copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 0.2-2.0 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; and (e) 1-10 wt.-% of a processing aid; whereby the weight percentages add up to 100 wt.-%.
8. The thermoplastic alloy composition according to claim 1 suitable for use in a coating and/or castfilm process or an injection moulding process, comprising: (a) 10-70 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP block copolymer having a C2 content of 1-40% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 5-14 g/lOmin; (c) 20-35 wt.-% of a polyamide; (d) 15-35 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; whereby the weight percentages add up to 100 wt.-%.
The thermoplastic alloy composition according to claim 6 suitable for use in a calendering process, comprising additionally as compound (f) 0.1-15 wt.-% of a lubricant,
10. The thermoplastic alloy composition of claim 1 suitable for use in a calendering process, comprising: (a) 10-50 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 5-35% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP block copolymer having a C2 content of 5-35% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 5-14 g/lOmin; (c) 20-30 wt.-% of a polyamide; (d) 15-25 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt . -% of a processing aid; and (f) 0.1-10 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%.
11. The thermoplastic alloy composition of claim 1 suitable for use in a calendering process, comprising: (a) 10-35 wt.-% of a random-heterophasic PP-copolymer having a C2 content of 10-30% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 2.0-15 g/lOmin; (b) 1-60 wt.-% of a heterophasic PP block copolymer having a C2 content of 10-30% and having a MFR (at 230°C and 2,16 kg load according to ISO 1133) of 5-14 g/lOmin; (c) 20-30 wt.-% of a polyamide; (d) 15-25 wt.-% of an elastomeric C2-C8-copolymer; (e) 1-10 wt.-% of a processing aid; and (f) 0.1-5 wt.-% of a lubricant; whereby the weight percentages add up to 100 wt.-%.
12. Sheet or film comprising the composition of any of claims 1 to 5 and 7 to 11.
13. Moulded article wherein at least one layer comprises the composition of any of claims 1 to 6 and 8.
14. Use of the composition of any of claims 1 to 11 in a high frequency welding process.
15. Article made of or coated with a layer comprising the composition of any of claims 1 to 11.
16. Article according to claim 15 wherein the layer is coated with a method making use of a high frequency welding process.
17. Use of a thermoplastic alloy composition according to claim 6 in a blow-moulding process.
18. Use of a thermoplastic alloy composition according to claim 7 in a sheet extrusion process or a blown film process .
19. Use of a thermoplastic alloy composition according to claim 8 in a coating and/or castfilm process or an injection moulding process.
20. The use according to claim 19, said composition comprising additionally as compound (f) 0.1-15 wt.-% of a lubricant.
21. Use of the thermoplastic alloy composition of claim 10 in a calendering process.
2. Use of the thermoplastic alloy composition of claim 11 in a calendering process.
EP05707268A 2004-02-09 2005-02-08 High-frequency-weldable polymer mixture and processes for using the same Withdrawn EP1713857A1 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
EP05707268A EP1713857A1 (en) 2004-02-09 2005-02-08 High-frequency-weldable polymer mixture and processes for using the same

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
EP04002801A EP1561782A1 (en) 2004-02-09 2004-02-09 High-frequency-weldable polymer mixture and processes for using the same
PCT/EP2005/001271 WO2005075557A1 (en) 2004-02-09 2005-02-08 High-frequency-weldable polymer mixture and processes for using the same
EP05707268A EP1713857A1 (en) 2004-02-09 2005-02-08 High-frequency-weldable polymer mixture and processes for using the same

Publications (1)

Publication Number Publication Date
EP1713857A1 true EP1713857A1 (en) 2006-10-25

Family

ID=34673696

Family Applications (2)

Application Number Title Priority Date Filing Date
EP04002801A Withdrawn EP1561782A1 (en) 2004-02-09 2004-02-09 High-frequency-weldable polymer mixture and processes for using the same
EP05707268A Withdrawn EP1713857A1 (en) 2004-02-09 2005-02-08 High-frequency-weldable polymer mixture and processes for using the same

Family Applications Before (1)

Application Number Title Priority Date Filing Date
EP04002801A Withdrawn EP1561782A1 (en) 2004-02-09 2004-02-09 High-frequency-weldable polymer mixture and processes for using the same

Country Status (2)

Country Link
EP (2) EP1561782A1 (en)
WO (1) WO2005075557A1 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1878560A1 (en) * 2006-07-12 2008-01-16 Basf Aktiengesellschaft Plastic-rubber composite and method of manufacturing thereof
EP2331321B1 (en) * 2008-09-29 2013-01-16 Borealis AG Polyolefin composition
DE102013113120B4 (en) * 2013-11-27 2023-06-29 Loparex Germany Gmbh & Co. Kg Foil for labels and cover strips
WO2017009193A1 (en) * 2015-07-13 2017-01-19 Sabic Global Technologies B.V. Composition comprising heterophasic propylene copolymer

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
DE4142271A1 (en) * 1991-12-20 1993-06-24 Danubia Petrochem Deutschland High-frequency welding of polyolefin-polyamide moulded prods. - with addn. of coupling agent, esp. maleic anhydride-grafted olefin (co)polymer, to improve HF welding and mechanical properties
DE19653590C2 (en) * 1996-12-20 1998-10-15 Benecke Kaliko Ag High-frequency weldable polymer mixture
ES2176554T3 (en) * 1997-05-16 2002-12-01 Advanced Elastomer Systems METHOD FOR WELDING WITH HIGH FREQUENCY ELASTOMEROS NON-POLAR THERMOPLASTICS.
EP1283242A1 (en) * 2001-08-03 2003-02-12 Amcor Flexibles Transpac N.V. Blends of heterophasic polypropylene block copolymers for making films

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
See references of WO2005075557A1 *

Also Published As

Publication number Publication date
WO2005075557A1 (en) 2005-08-18
EP1561782A1 (en) 2005-08-10

Similar Documents

Publication Publication Date Title
US8057910B2 (en) Toughened thermoplastic polyamide compositions
EP1605002A1 (en) Hydrogenated diene copolymer, polymer composition, and molded object
JP2008511721A (en) Thermoformable propylene polymer composition
KR20180085649A (en) Thermoplastic polyolefin sheet being capable of displaying and touch-sensing
EP1713857A1 (en) High-frequency-weldable polymer mixture and processes for using the same
US6162865A (en) High-frequency-weldable polymer mixture
US20150175788A1 (en) Blends of ethylene copolymers with high-frequency weldability
KR102106711B1 (en) Polyolefin Resin Composition for a Sealant Layer of a Peelable Film and Peelable Film Comprising a Sealant Layer Prepared Therefrom
WO2022186038A1 (en) Resin composition for adhesion and method for producing same, thermoplastic resin composition and method for producing same, adhesive sheet, laminate, and molded body made of synthetic resin
JP4732749B2 (en) Thermoplastic resin composition, molded article and use thereof
JP4254251B2 (en) Polyolefin film and product comprising the same
JPH07329260A (en) Heat sealable stretched laminated film
US20220145051A1 (en) Thermoplastic olefin composition
JPH0866990A (en) Composite molded body and its manufacture
JP2003342429A (en) Polypropylene resin composition and its application
KR100544398B1 (en) Polypropylene composition provided by the calendering process for decoration sheet and method for preparing polypropylene film and sheet using the same
JPH09111061A (en) Thermoplastic resin composition
JPH07179624A (en) Surfacing sheet and laminate prepared therefrom
KR20050123255A (en) Composition of thermoplastic
JP2011094038A (en) Elastomer composition for producing melt-extended product containing distribution-controlled block polymer, and film
JP2673128B2 (en) Multi-layer blow molded product
JP2011148872A (en) Elastomer composition comprising acid-modified polymer for manufacturing melt-spread item, and film
CN114286842A (en) Polyolefin-based composition modified by silane
JP4894236B2 (en) Thermoplastic resin composition and method for producing the same
JP2004346086A (en) Polyethylene terephthalate resin composition

Legal Events

Date Code Title Description
PUAI Public reference made under article 153(3) epc to a published international application that has entered the european phase

Free format text: ORIGINAL CODE: 0009012

17P Request for examination filed

Effective date: 20060809

AK Designated contracting states

Kind code of ref document: A1

Designated state(s): AT BE BG CH CY CZ DE DK EE ES FI FR GB GR HU IE IS IT LI LT LU MC NL PL PT RO SE SI SK TR

DAX Request for extension of the european patent (deleted)
17Q First examination report despatched

Effective date: 20090513

STAA Information on the status of an ep patent application or granted ep patent

Free format text: STATUS: THE APPLICATION IS DEEMED TO BE WITHDRAWN

18D Application deemed to be withdrawn

Effective date: 20090924