EP1855866A1 - Article contenant un polypropylene et un polyurethanne thermoplastique - Google Patents

Article contenant un polypropylene et un polyurethanne thermoplastique

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Publication number
EP1855866A1
EP1855866A1 EP06708424A EP06708424A EP1855866A1 EP 1855866 A1 EP1855866 A1 EP 1855866A1 EP 06708424 A EP06708424 A EP 06708424A EP 06708424 A EP06708424 A EP 06708424A EP 1855866 A1 EP1855866 A1 EP 1855866A1
Authority
EP
European Patent Office
Prior art keywords
plasma
thermoplastic polyurethane
polypropylene
article
din
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Withdrawn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
EP06708424A
Other languages
German (de)
English (en)
Inventor
Klaus Hilmer
Leo Hoffmann
Simon Amesöder
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.)
BASF SE
Original Assignee
BASF SE
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Filing date
Publication date
Application filed by BASF SE filed Critical BASF SE
Publication of EP1855866A1 publication Critical patent/EP1855866A1/fr
Withdrawn legal-status Critical Current

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Classifications

    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/06—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material
    • B32B27/08—Layered products comprising a layer of synthetic resin as the main or only constituent of a layer, which is next to another layer of the same or of a different material of synthetic resin
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16—Making multilayered or multicoloured articles
    • B29C45/1657—Making multilayered or multicoloured articles using means for adhering or bonding the layers or parts to each other
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16—Making multilayered or multicoloured articles
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C59/00—Surface shaping of articles, e.g. embossing; Apparatus therefor
    • B29C59/14—Surface shaping of articles, e.g. embossing; Apparatus therefor by plasma treatment
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B32—LAYERED PRODUCTS
    • B32B—LAYERED PRODUCTS, i.e. PRODUCTS BUILT-UP OF STRATA OF FLAT OR NON-FLAT, e.g. CELLULAR OR HONEYCOMB, FORM
    • B32B27/00—Layered products comprising a layer of synthetic resin
    • B32B27/30—Layered products comprising a layer of synthetic resin comprising vinyl (co)polymers; comprising acrylic (co)polymers
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16—Making multilayered or multicoloured articles
    • B29C45/1657—Making multilayered or multicoloured articles using means for adhering or bonding the layers or parts to each other
    • B29C2045/166—Roughened surface bonds
    • B29C2045/1662—Roughened surface bonds plasma roughened surface bonds
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29C—SHAPING OR JOINING OF PLASTICS; SHAPING OF MATERIAL IN A PLASTIC STATE, NOT OTHERWISE PROVIDED FOR; AFTER-TREATMENT OF THE SHAPED PRODUCTS, e.g. REPAIRING
    • B29C45/00—Injection moulding, i.e. forcing the required volume of moulding material through a nozzle into a closed mould; Apparatus therefor
    • B29C45/16—Making multilayered or multicoloured articles
    • B29C45/1676—Making multilayered or multicoloured articles using a soft material and a rigid material, e.g. making articles with a sealing part
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
    • Y10T428/00—Stock material or miscellaneous articles
    • Y10T428/249921—Web or sheet containing structurally defined element or component

Definitions

  • the invention relates to articles containing without chemical adhesion promoter adhesively bonded thermoplastic polyurethane and polypropylene, preferably articles containing articles based on thermoplastic polyurethane adhesively bonded to articles based on polypropylene.
  • "Without chemical adhesion promoters” means that there is no further component (adhesion promoter) between the thermoplastic polyurethane and the polypropylene, ie no component which differs from the polypropylene and the thermoplastic polyurethane, in particular no adhesive
  • the articles according to the invention are thus not based on a mixture comprising polypropylene and thermoplastic polyurethane, nor does the invention relate to processes for the production of an article comprising thermoplastic polyurethane and polypropylene plasma-treating the surface of a polypropylene article and then bringing the thermoplastic polyurethane preferably in molten state into contact with the plasma-treated surface, preferably by means of injection molding
  • Em relates to the invention thus available articles containing thermoplastic polyurethane
  • Thermoplastics are plastics that remain thermoplastic when repeatedly heated and cooled in the temperature range typical of the material for processing and application.
  • thermoplastic is meant the property of a plastic to soften in a typical temperature range for him repeatedly in the heat and to harden on cooling and be repeatedly formed in the softened state by flowing as a molded part, extrudate or forming part to semifinished or articles.
  • Thermoplastics are widely used in the art and are in the form of fibers, sheets, films, moldings, bottles, jackets, packaging, etc.
  • thermoplastics For many applications, it is desirable to combine various thermoplastics in one article. The reasons for this are due to the different requirements that are placed on the surface, eg with regard to the feel and appearance on the one hand and on the other hand on the strength or rigidity and functionality (seals) of the article.
  • adhesive combination of various thermoplastics it is known in the case of multicomponent injection molding, for example two-component injection molding ( ⁇ 2-component injection molding), to bond various plastics adhesively together by direct injection molding.
  • the composite element should be characterized by an efficient and effective production and the best possible adhesion without the use of adhesion promoters.
  • thermoplastically processable plastic which is excellently suitable as a carrier material, ie the polypropylene, is adhesively bonded directly to a thermoplastic which is very noble in look and feel, here thermoplastic polyurethane.
  • a composite element between polypropylene and thermoplastic polyurethane has hitherto not been known and in particular is not accessible without chemical adhesion promoters.
  • This combination of materials precisely because of their direct adhesive bond, ie without the use of chemical adhesion promoters, solvents, in particular adhesives, opens up new hitherto unknown qualitative refinement possibilities for many applications.
  • thermoplastic polyurethane offers the advantage of a noble haptic, whereby in addition an optically complex surface can be represented, because TPU has a very good imaging performance of tool surfaces.TTP continues to be characterized by a very low surface contamination and can color over color concentrates in wide Ranges are varied. according to the invention, articles in which the thermoplastic polyurethane is the visible surface.
  • the articles according to the invention are preferably a multicomponent injection-molded article, preferably two-component injection-molded articles, i. Articles made in multi-component, preferably two-component injection molding.
  • Two-component injection molding is well known and widely described for other material combinations.
  • a component is injected into a mold and then molded onto the second components.
  • the insertion of a component, preferably a polypropylene-based article, into a tool and subsequent injection molding to the plasma-treated surface of the polypropylene article may alternatively be performed.
  • thermoplastic polyurethane is preferably a thermoplastic polyurethane with a Shore hardness of 45 A to 80 A, a tensile strength according to DIN 53504 greater than 15 MPa, a tear strength according to DIN 53515 greater than 30 N / mm and abrasion according to DIN 53516 of less than 250 mm 3 .
  • the articles according to the invention are also distinguished in particular by the excellent adhesion between the polypropylene and the thermoplastic polyurethane. Preference is therefore given in particular to articles in which the peel resistance according to DIN DIN EN 1464 is at least 1 N / mm, preferably at least 2 N / mm.
  • Another object was to develop the most efficient and effective method by which the articles shown in the introduction can be produced, in particular with simple means of adhesive bonding can be achieved.
  • thermoplastic polyurethane and polypropylene preferably articles containing without chemical adhesion promoter adhesively bonded thermoplastic polyurethane and polypropylene
  • the surface of a polypropylene article is plasma-treated and then the thermoplastic polyurethane, preferably in the molten state, with the plasma-treated surface in contact, preferably injection molded by injection molding.
  • the second component is thus applied by means of injection molding to the plasma-treated surface of the first components, in particular injection-molded.
  • the method according to the invention ie the adhesion promotion by means of plasma treatment, in generally known Method for the thermoplastic processing of plastics used.
  • the plasma treatment can be applied to the surface of an extruded plastic film onto which the other plastic is subsequently extruded or preferably injection-molded.
  • the one plastic preferably the polypropylene
  • the other plastic preferably the thermoplastic polyurethane
  • the surface of the polypropylene will be plasma-treated and then thermoplastic polyurethane applied by injection molding on the plasma-treated surface of the polypropylene, preferably spray.
  • the two-component injection molding wherein in two-component injection molding preferably in a single injection mold in a first step with polypropylene produces a first injection molded body, then the surface of this first injection molded body and then thermoplastic polyurethane by injection molding on the plasma-treated surface of the first injection molding applies, preferably sprayed.
  • the plasma treatment is well known and shown for example in the cited documents.
  • Apparatuses for plasma treatment are, for example, at Plasmatreat GmbH, Bisamweg 10, 33803 Steinhagen and TIGRES. Gerstenberg GmbH, Mühlenbach 12, 25462 Rellingen available.
  • a plasma in a plasma source by means of high voltage discharge, bring this plasma by means of a plasma nozzle with the surface of the one component, preferably the polypropylene in contact and the plasma source at a distance between 2 mm and 25 mm at a speed between 0.1 m and at 400 m / min, preferably between 0.1 m / min and 200 m / min, more preferably between 0.2 m / min and 50 m / min, relative to the surface of the component that is being plasma treated.
  • the plasma is preferably transported by a gas flow along the discharge path onto the surface of the thermoplastic material to be treated.
  • the plasma treatment preferably lasts between 1 ms and 100 s.
  • gases oxygen, nitrogen, carbon dioxide and mixtures of the aforementioned gases, preferably air, in particular compressed air can be used.
  • the gas flow can be up to 2 rr ⁇ Vh per nozzle.
  • the working frequency can be between 10 and 30 kHz.
  • Electrode voltage can be between 5 and 10 kV. There are standing or rotating plasma nozzles into consideration. Surface temperature of the component may be between 5 ° C and 250 0 C, preferably between 5 ° C and 200 0 C.
  • thermoplastics are well known and described in particular manifold for polypropylene and thermoplastic polyurethane.
  • principle of two-component (2-component) injection molding is shown in Figure 2 in Simon Amesöder et al., Kunststoffe international 9/2003, pages 124 to 129.
  • the temperature during the injection molding of thermoplastic polyurethane is preferably between 140 and 250 ° C., more preferably between 160 and 230 ° C. TPUs are preferably processed as gently as possible. The temperatures can be adjusted according to hardness.
  • the peripheral speed during plasticizing is preferably less than or equal to 0.2 m / s, the back pressure is preferably between 30 to 200 bar.
  • the injection speed is preferably as low as possible in order to keep shear stress low.
  • the cooling time is preferably sufficiently long to choose, wherein the emphasis is preferably 30 between 80% of the injection pressure.
  • the molds are preferably heated to between 30 and 70 ° C.
  • the sprue is preferably chosen at the strongest point of the component. In the case of surface overmoulding, an injection point cascade can be used.
  • the temperature during the injection molding of polypropylene is preferably between 200 and 300 ° C., more preferably between 220 and 275 ° C.
  • the machine temperatures may preferably be from 220 to 300 0 C, the feed preferably at 30-50 0 C.
  • the injection pressure is typically at 600-1800 bar.
  • the postpressure is preferably maintained at 30-60% of the injection pressure.
  • Plasticizing is preferred with up to 1.3 m / s peripheral speed of the screw, but can be carried out particularly preferably only so fast that the plasticizing process is completed during the cooling time.
  • the dynamic pressure to be used may preferably be between 50 and 200 bar.
  • the sprue can preferably take place at the strongest point of the component.
  • polypropylene well-known polypropylene can be used.
  • Polypropylene is described for example in Römpp Chemie Lexikon, 9th edition, page 3566 ff., Georg Thieme Verlag, Stuttgart. Particular preference is given to polymers which have the following structural unit: - [CHCH 3 ) -CH 2 ] n -, where n is preferably chosen such that the polymer has a molecular weight, preferably weight-average molecular weight, preferably between 150000 g / mol and 600000 g / mol.
  • Corresponding polypropylene (PP) is commercially available.
  • polypropylene are mixtures which include, for example, polypropylene together with other thermoplastics, e.g. other polyolefins such as polyethylene containing, preferably mixtures in which the content of polypropylene at least 50 wt .-%, more preferably at least 90 wt .-%, in particular 100 wt .-% is.
  • polypropylene is particularly preferred, i.e., most preferably, the polypropylene is not used in admixture with other polymers.
  • TPUs Thermoplastic polyurethanes, also referred to herein as TPUs, and methods for their preparation are well known.
  • TPUs are prepared by reacting (a) isocyanates with (b) isocyanate-reactive compounds, usually having a molecular weight (M w ) of 500 to 10,000, preferably 500 to 5000, particularly preferably 800 to 3000 and (c) chain extenders having a molecular weight of 50 to 499, optionally in the presence of (d) catalysts and / or (e) conventional additives.
  • organic isocyanates it is possible to use generally known aliphatic, cycloaliphatic, araliphatic and / or aromatic isocyanates, for example tri-, tetra-, penta-, hexa-, hepta- and / or octamethylene diisocyanate, Methyl pentamethylene diisocyanate 1, 5, 2-ethyl-butylene diisocyanate-1,4, pentamethylene diisocyanate-1, 5, butylene diisocyanate 1, 4, 1-iso-cyanato-3,3, 5-trimethyl-5-isocyanato-methylcyclohexane (isophorone diisocyanate, IPDI), 1, 4- and / or 1,3-bis (isocyanatomethyl) cyclohexane (HXDI), 1,4-cyclohexane diisocyanate, 1 Methyl 2,4- and / or 2,6-cyclohexane diis
  • aliphatic isocyanates are also preferred, as is indicated at the beginning, particularly preferably isocyanato-SSS-trimethyl- ⁇ -isocyanato-methyl- cyclohexane (isophorone diisocyanate, IPDI) and / or hexamethylene diisocyanate (HDI), especially hexamethylene diisocyanate.
  • IPDI isophorone diisocyanate
  • HDI hexamethylene diisocyanate
  • isocyanate (a) prepolymers which have free isocyanate groups.
  • the NCO content of these prepolymers is preferably between 10 and 25%.
  • the prepolymers can offer the advantage that, due to the pre-reaction in the preparation of the prepolymers, a shorter reaction time is required in the production of the TPU.
  • isocyanate-reactive compounds for example polyesterols, polyetherols and / or polycarbonatediols, which are usually also grouped under the term "polyols", with molecular weights between 500 and 8000 , preferably 600 to 6000, in particular 800 to less than 3000, and preferably an average functionality to isocyanates of 1, 8 to 2.3, preferably 1, 9 to 2.2, in particular 2.
  • Polyether polyols are preferably used, for example those the basis of generally known starter substances and customary alkylene oxides, for example ethylene oxide, propylene oxide and / or butylene oxide, preferably polyetherols based on propylene oxide-1, 2 and ethylene oxide and in particular polyoxytetramethylene glycols.
  • the polyetherols have the advantage that they have a higher hydrolysis stability than polyesterols.
  • low-unsaturated polyetherols are understood as meaning, in particular, polyether alcohols having a content of unsaturated compounds of less than 0.02 meg / g, preferably less than 0.01 meg / g.
  • Such polyether alcohols are usually prepared by addition of alkylene oxides, in particular ethylene oxide, propylene oxide and mixtures thereof, to the above-described diols or triols in the presence of highly active catalysts.
  • highly active catalysts are, for example, cesium hydroxide and multimetal cyanide catalysts, also referred to as DMC catalysts.
  • DMC catalysts A frequently used DMC catalyst is zinc hexacyanocobaltate.
  • the DMC catalyst can be left in the polyether alcohol after the reaction, usually it is removed, for example by sedimentation or filtration.
  • polybutadiene diols having a molecular weight of 500-10,000 g / mol, preferably 1,000-5,000 g / mol, in particular 2,000-3,000 g / mol, can be used.
  • TPUs which have been prepared using these polyols can be crosslinked by irradiation after thermoplastic processing. This leads eg to a better burning behavior.
  • a polyol it is also possible to use mixtures of different polyols.
  • chain extenders (c) it is possible to use generally known aliphatic, araliphatic, aromatic and / or cycloaliphatic compounds having a molecular weight of 50 to 499, preferably 2-functional compounds, for example diamines and / or alkanediols having 2 to 10C -Atomen in the alkylene radical, in particular 1, 3-propanediol, butanediol-1, 4, hexanediol-1, 6 and / or di-, tri-, tetra-, penta-, hexa-, hepta-, octa-, nona- and or Dekaalkylen- glycols having 3 to 8 carbon atoms, preferably corresponding oligo- and / or
  • Polypropylene glycols although mixtures of chain extenders can be used.
  • components a) to c) are difunctional compounds, i. Diisocyanates (a), difunctional polyols, preferably polyetherols (b) and difunctional chain extenders, preferably diols.
  • Suitable catalysts which in particular accelerate the reaction between the NCO groups of the diisocyanates (a) and the hydroxyl groups of the constituent components (b) and (c) are the tertiary amines known and customary in the prior art, e.g. Triethylamine, dimethylcyclohexylamine, N-methylmorpholine, N, N'-dimethylpiperazine, 2- (dimethylaminoethoxy) ethanol, diazabicyclo- (2,2,2) octane and the like, and in particular organic metal compounds such as titanic acid esters, iron compounds such as e.g. Iron (Ul) acetylacetonate, tin compounds, e.g.
  • Triethylamine dimethylcyclohexylamine, N-methylmorpholine, N, N'-dimethylpiperazine, 2- (dimethylaminoethoxy) ethanol, diazabicyclo- (2,2,2) octane and the
  • the catalysts are usually used in amounts of from 0.0001 to 0.1 parts by weight per 100 parts by weight of polyhydroxyl compound (b).
  • component (e) in addition to catalysts (d) can the constitutional components (a) to (c) and conventional auxiliaries and / or additives (e) are added.
  • auxiliaries and / or additives include blowing agents, surface-active substances, fillers, nucleating agents, lubricants and mold release agents, dyes and pigments, antioxidants, for example against hydrolysis, light, heat or discoloration, inorganic and / or organic fillers, flame retardants, reinforcing agents and plasticizers, metal deactivators.
  • component (e) also includes hydrolysis protectants such as, for example, polymeric and low molecular weight carbodiimides.
  • the thermoplastic polyurethane in the materials according to the invention particularly preferably contains melamine cyanurate, which acts as a flame retardant.
  • meltamine cyanurate is preferred in an amount between 0.1 and 60 wt .-%, particularly preferably between 5 and 40 wt .-%, in particular between 15 and 25 wt .-% used, each based on the total weight of the TPU.
  • the thermoplastic polyurethane contains triazole and / or triazole derivative and antioxidants in an amount of 0.1 to 5 wt .-% based on the total weight of the thermoplastic polyurethane.
  • antioxidants are generally suitable substances which inhibit or prevent unwanted oxidative processes in the plastic to be protected. In general, antioxidants are commercially available.
  • antioxidants are sterically hindered phenols, aromatic amines, thiosynergists, organophosphorus compounds of the trivalent phosphorus, and Hlashd Amine Light Stabilizers.
  • sterically hindered phenols are found in Plastics Additives Handbook, th edition 5, H. Zweifel, ed, Hanser Publishers, Kunststoff, 2001 ([1]), and S.98-107 S.116-121.
  • aromatic amines can be found in [1] p.107-108.
  • thiosynergists are given in [1], p.104-105 and p.112-113.
  • phosphites can be found in [1], p.109-112.
  • hindered amine light stabilizers are given in [1], p.123-136. to
  • the antioxidants in particular the phenolic antioxidants, have a molecular weight of greater than 350 g / mol, particularly preferably greater than 700 g / mol and a maximum molecular weight of ⁇ 10,000 g / mol, preferably ⁇ 3,000 g / mol. Furthermore, they preferably have a melting point of less than 180 0 C. Further, preferably used antioxidants, which are a- morph or liquid. Also, as component (i), mixtures of two or more antioxidants can be used.
  • chain regulators usually having a molecular weight of from 31 to 3000.
  • Such chain regulators are compounds which have only one isocyanate-reactive functional group, such as.
  • monofunctional alcohols monofunctional amines and / or monofunctional polyols.
  • Chain regulators can generally be used in an amount of 0 to 5, preferably 0.1 to 1, parts by weight, based on 100 parts by weight of component b), and fall by definition under component (c).
  • the structural components (b) and (c) can be varied in relatively wide molar ratios.
  • Molecular ratios of component (b) to total chain extenders (c) of 10: 1 to 1:10, in particular from 1: 1 to 1: 4 have proven useful, the hardness of the TPU increasing with increasing content of (c) increases.
  • the thermoplastic polyurethane preference is given to using soft plasticizer-free thermoplastic polyurethane, preferably having a hardness of up to 90 Shore A, in particular for haptic and optical applications. In wear and shock protection applications, all TPUs up to 80 Shore D are suitable. In hydrolysis-sensitive applications, ether TPUs are to be preferred.
  • thermoplastic polyurethane preferably has a number-average molecular weight of at least 40,000 g / mol, particularly preferably at least 80,000 g / mol, in particular at least 120,000 g / mol.
  • thermoplastic polyurethane has a Shore hardness of 45 A to 80 A, a tensile strength according to DIN 53504 of greater than 15 MPa, a tear strength according to DIN 53515 of greater than 30 N / mm and an abrasion according to DIN 53516 of less than 250 mm 3 has.
  • TPUs Due to their particularly good adhesion TPU according to WO 03/014179 are preferred.
  • the following statements up to the examples relate to these particularly preferred TPUs.
  • These TPUs adhere particularly well, since the processing temperatures are higher than with other "conventional" TPUs with comparable hardnesses and can achieve the best adhesive strengths under these conditions.
  • These particularly preferred TPUs are preferably obtainable by reacting (a) isocyanates with ( diols b1) polyesterdiols having a melting point greater than 15O 0 C, (b2) polyether and / or polyester diols, each having a melting point of less than 15O 0 C and a molecular weight of 501 to 8000 g / mol and optionally (c) diols having a molecular weight of 62 g / mol to 500 g / mol.
  • thermoplastic polyurethanes in which the molar ratio of diols (c) having a molecular weight of from 62 g / mol to 500 g / mol to component (b2) is less than 0.2, especially is preferably 0.1 to 0.01.
  • thermoplastic polyurethanes in which the polyester diols (b1), which preferably have a molecular weight of from 1000 g / mol to 5 000 g / mol have the following structural unit (I):
  • R 1 carbon skeleton having 2 to 15 carbon atoms, preferably an alkylene group having 2 to 15 carbon atoms and / or a bivalent aromatic radical having 6 to 15 carbon atoms, particularly preferably having 6 to 12 carbon atoms
  • R 2 optionally branched-chain alkylene group having 2 to 8 carbon atoms, preferably 2 to 6, particularly preferably 2 to 4 carbon atoms, in particular -CH 2 -CH 2 - and / or -CH 2 -CH 2 -CH 2 -CH 2 -CH 2 -,
  • R 3 optionally branched-chain alkylene group having 2 to 8 carbon atoms, preferably 2 to 6, particularly preferably 2 to 4 carbon atoms, in particular -CH 2 -CH 2 - and / or -CH 2 -CH 2 -CH 2 -CH 2 -,
  • X an integer from the range 5 to 30.
  • the preferred melting point and / or the preferred molecular weight mentioned above relate to the structural unit (I) shown.
  • melting point in this document means the maximum of the melting peak of a heating curve which was measured using a commercially available DSC apparatus (for example DSC 7 / Perkin-Elmer Co.).
  • the molecular weights given in this document represent the number average molecular weights in [g / mol].
  • thermoplastic polyurethanes can preferably be prepared by reacting a, preferably high molecular weight, preferably semicrystalline, thermoplastic polyester with a diol (c) and then the reaction product of (i) containing (b1) polyester diol having a melting point greater than 15O 0 C.
  • diol together with (b2) polyetherdiols and / or polyesterdiols, each having a melting point of less than 15O 0 C and a molecular weight of 501 to 8000 g / mol and, if appropriate, further (c) diols having a molecular weight of 62 to 500 g / mol with (a) isocyanate, if appropriate in the presence of (d) catalysts and / or (e) auxiliaries.
  • the molar ratio of the diols (c) having a molecular weight of from 62 g / mol to 500 g / mol to the component (b2) is preferably less than 0.2, preferably from 0.1 to 0.01.
  • step (i) While the hard phases are made available to the end product by step (i) by the polyester used in step (i), the use of component (b2) in step (ii) results in the buildup of the soft phases.
  • the preferred technical teaching is that polyesters having a pronounced, well crystallizing hard phase structure are preferably melted in a reaction extruder and first degraded with a low molecular weight diol to give shorter polyesters having free hydroxyl end groups. In this case, the original high crystallization tendency of the polyester is retained and can then be used to obtain TPU with advantageous properties when the reaction proceeds rapidly, as there are high tensile strength values, low abrasion values and due to the high and narrow melting range high heat resistance and low compression set.
  • preferably high molecular weight, partially crystalline, thermoplastic polyesters are degraded with low molecular weight diols (c) under suitable conditions in a short reaction time to rapidly crystallizing polymer.
  • Ester diols (b1) which in turn are then incorporated with other polyester diols and / or polyether diols and diisocyanates in high molecular weight polymer chains.
  • thermoplastic polyester used ie before the reaction (i) with the diol (c), preferably has a molecular weight of 15000 g / mol to 40,000 g / mol and preferably a melting point of greater than 16O 0 C, more preferably of 170 0 C. to 260 0 C on.
  • starting material ie as polyester, which in the step (i) preferably in the molten state, particularly preferably at a temperature of 23O 0 C to 28O 0 C, preferably for a duration of 0.1 min to 4 min, particularly preferably 0, 3 to 1 min with the diol (s) (c) is reacted, generally known, preferably high molecular weight, preferably partially crystalline, thermoplastic polyesters, for example in granular form, can be used.
  • Suitable polyesters are based, for example, on aliphatic, cycloaliphatic, araliphatic and / or aromatic dicarboxylic acids, for example lactic acid and / or terephthalic acid, and aliphatic, cycloaliphatic, araliphatic and / or aromatic dialcohols, for example ethanediol-1,2-butanediol-1,4 and / or hexanediol-1, 6.
  • polyesters used are: poly-L-lactic acid and / or polyalkylene terephthalate, for example polyethylene terephthalate, polypropylene terephthalate, polybutylene terephthalate, in particular polybutylene terephthalate.
  • thermoplastic polyester is preferably melted at a temperature of 18O 0 C to 27O 0 C.
  • reaction (i) with the diol (c) is preferably carried out at a temperature of 23O 0 C to 280 0 C, preferably 24O 0 C to 28O 0 C by.
  • diol (c) in step (i) for reaction with the thermoplastic polyester and optionally in step (ii) generally known diols having a molecular weight of 62 to 500 g / mol can be used, for example, the later mentioned, for example ethylene glycol , 1, 3-propanediol, 1, 4-butanediol, 1, 5-pentanediol, 1, 6-hexanediol, heptanediol, octanediol, preferably butane-1, 4-diol and / or ethane-1, 2-diol.
  • the weight ratio of the thermoplastic polyester to the diol (c) in the step (i) is usually 100: 1, 0 to 100: 10, preferably 100: 1, 5 to 100: 8.0.
  • the reaction of the thermoplastic polyester with the diol (c) in the reaction step (i) is preferably carried out in the presence of customary catalysts, for example those which are described later. Preference is given to using catalysts based on metals for this reaction.
  • the reaction in step (i) is preferably carried out in the presence of from 0.1 to 2% by weight of catalysts, based on the weight of diol (c).
  • the reaction in the presence of such catalysts is advantageous in order to be able to carry out the reaction in the available short residence time in the reactor, for example a reaction extruder.
  • Suitable catalysts for this reaction step (i) are: tetrabutyl orthotitanate and / or tin (II) dioctoate, preferably tin dioctoate.
  • the polyesterdiol (b1) as the reaction product from (i) preferably has a molecular weight of from 1000 g / mol to 5000 g / mol.
  • the melting point of the polyester diol as the reaction product of (i) is preferably 15O 0 C to 26O 0 C, in particular 165 to 245 ° C, ie that the reaction product of the thermoplastic polyester with the diol (c) in step (i) compounds having said melting point contains, which are used in the subsequent step (ii).
  • the reaction product of the TPU therefore has free hydroxyl end groups and is preferably further processed in the further step (ii) to the actual product, the TPU.
  • the reaction of the reaction product from step (i) in step (ii) is preferably carried out by adding a) isocyanate (a) and (b2) polyether diols and / or polyester diols each having a melting point of less than 15O 0 C and a molecular weight of 501 to 8000 g / mol and optionally further diols (c) having a molecular weight of 62 to 500, (d) catalysts and / or (e) auxiliaries to the reaction product of (i).
  • the reaction of the reaction product with the isocyanate takes place via the hydroxyl end groups formed in step (i).
  • the reaction is preferably carried out in the step (ii) at a temperature of 190 to 25O 0 C for a period preferably from 0.5 to 5 min, particularly preferably 0.5 to 2 minutes, preferably in a reactive extruder, more preferably in the same Reaction extruder, in which also the step (i) was carried out.
  • the reaction of step (i) may take place in the first housings of a conventional reaction extruder and later, ie later housings, after the addition of components (a) and (b2), the corresponding implementation of step (ii) are carried out.
  • the first 30 to 50% of the length of the reaction extruder may be used for step (i) and the remaining 50 to 70% used for step (ii).
  • the reaction in step (ii) is preferably carried out with an excess of the isocyanate groups to the isocyanate-reactive groups.
  • the ratio of the isocyanate groups to the hydroxyl groups is preferably 1: 1 to 1.2: 1, more preferably 1.02: 1 to 1.2. 1.
  • reaction extruder a generally known reaction extruder.
  • reaction extruders are described by way of example in the company publications by Werner & Pfleiderer or in DE-A 2 302 564.
  • the preferred method is preferably carried out in such a manner to that in the first case of a reaction extruder at least one thermoplastic polyester, for example polybutylene terephthalate, dosed, and at temperatures preferably between 180 0 C to 270 0 C, preferably from 240 0 C to 270 0 C is melted, in a following housing a diol (c), for example butanediol, and preferably a transesterification catalyst, at temperatures between 240 ° C to 280 ° C the polyester through the diol (c) to Polyesteroli- gomeren with hydroxyl end groups and molecular weights between 1000 to
  • thermoplastic polyurethanes 5000 g / mol degrades, in a subsequent housing isocyanate (a) and (b2) to isocyanate-reactive compounds having a molecular weight of 501 to 8000 g / mol and optionally (c) diols having a molecular weight of 62 to 500, (d) catalysts and / or (e) added to auxiliaries and then at temperatures of 190 to 250 0 C, the construction of the preferred thermoplastic polyurethanes.
  • step (ii) with the exception of (c) diols having a molecular weight of from 62 to 500, contained in the reaction product of (i), no (c) diols having a molecular weight of from 62 to 500 are fed.
  • the reaction extruder preferably has neutral and / or backward-promoting kneading blocks and recycling elements in the region in which the thermoplastic polyester is melted, and in the region in which the thermoplastic polyester is reacted with the diol, preferably screw mixing elements, toothed disks and / or tooth mixing elements Combination with return conveyor elements.
  • the clear melt is usually fed by means of a gear pump underwater granulation and granulated.
  • thermoplastic polyurethanes show optically clear, single-phase melts which rapidly solidify and, owing to the semi-crystalline polyester hard phase weak opaque to form white-opaque moldings.
  • the rapid solidification behavior is a decisive advantage over known formulations and production processes for thermoplastic polyurethanes.
  • the rapid solidification behavior is so pronounced that even products with a hardness of 50 to 60 Shore A can be processed by injection molding with cycle times of less than 35 seconds.
  • no TPU-typical problems such as sticking or blocking of the films or hoses occur.
  • the proportion of the thermoplastic polyester in the final product is preferably 5 to 75 wt .-%.
  • the preferred thermoplastic polyurethanes particularly preferably comprise products of the reaction of a mixture comprising 10 to 70% by weight of the reaction product of (i), 10 to 80% by weight (b2) and 10 to 20% by weight (a), wherein the weights are based on the total weight of the mixture comprising (a), (b2), (d), (e) and the reaction product of (i).
  • the preferred thermoplastic polyurethanes preferably have a hardness of Shore 45 A to Shore 78 D, more preferably 50 A to 75 D.
  • thermoplastic polyurethanes preferably have the following structural unit (II):
  • R 1 carbon skeleton having 2 to 15 carbon atoms, preferably an alkylene group having 2 to 15 carbon atoms and / or an aromatic radical having 6 to 15 carbon atoms,
  • R 2 optionally branched-chain alkylene group having 2 to 8 carbon atoms, preferably 2 to 6, particularly preferably 2 to 4 carbon atoms, in particular -CH 2 -CH 2 - and / or -CH 2 -CH 2 -CH 2 -CH 2 -,
  • R 3 radical, which is characterized by the use of polyether diols and / or polyester diols each having molecular weights between 501 g / mol and 8000 g / mol as (b2) or by the use of alkanediols having 2 to 12 carbon atoms for the reaction with diisocyanates reveals
  • X an integer from the range 5 to 30
  • n an integer from the range 5 to 20.
  • the radical R 1 is defined by the isocyanate used, the radical R 2 defined by the reaction product of the thermoplastic polyester with the diol (c) in (i) and the radical R 3 by the starting components (b2) and optionally (c) the production of TPU.
  • the PP XM1 TO1 component was subjected to a plasma treatment with the Elastollan® TPU prior to injection molding, after which the TPU was injected directly.
  • the adhesion to the plasma-treated surface is permanently so high that the components can not be separated without destructive component (specimen) deformation.
  • the same appearance is shown by MOPLEN, HiFax and Adstif polypropylene grades from BASELL.

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  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Mechanical Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Plasma & Fusion (AREA)
  • Injection Moulding Of Plastics Or The Like (AREA)
  • Laminated Bodies (AREA)
  • Manufacture Of Macromolecular Shaped Articles (AREA)

Abstract

L'invention concerne un article contenant un polyuréthanne thermoplastique et un polypropylène liés par adhérence sans agent adhésif chimique.
EP06708424A 2005-02-22 2006-02-21 Article contenant un polypropylene et un polyurethanne thermoplastique Withdrawn EP1855866A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE200510008261 DE102005008261A1 (de) 2005-02-22 2005-02-22 Artikel enthaltend Polypropylen und thermoplastisches Polyurethan
PCT/EP2006/060148 WO2006089893A1 (fr) 2005-02-22 2006-02-21 Article contenant un polypropylene et un polyurethanne thermoplastique

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EP1855866A1 true EP1855866A1 (fr) 2007-11-21

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US (1) US20090042007A1 (fr)
EP (1) EP1855866A1 (fr)
JP (1) JP2008531331A (fr)
KR (1) KR20070110383A (fr)
CN (1) CN101128305A (fr)
DE (1) DE102005008261A1 (fr)
WO (1) WO2006089893A1 (fr)

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KR20090082270A (ko) * 2006-11-16 2009-07-29 바스프 에스이 롤러 베어링
DE102007051112A1 (de) 2007-10-24 2008-08-28 Bayer Materialscience Ag Verbundelemente und ein Verfahren zu ihrer Herstellung
DE102010047248B4 (de) * 2010-10-04 2017-01-05 Fresenius Medical Care Deutschland Gmbh Fluidführende medizintechnische Funktionseinrichtung mit Sensorankoppelabschnitt, medizintechnische Behandlungsvorrichtung sowie Verfahren
DE102014216283B4 (de) * 2014-07-28 2022-12-08 Max Rehberger Vorrichtung zur Vermeidung von Pflanzenwuchs um eine Verkehrseinrichtung
CN105058932A (zh) * 2015-07-30 2015-11-18 广东天安新材料股份有限公司 一种表面装饰材料
CN114147931B (zh) * 2020-09-07 2024-03-29 一道新能源科技股份有限公司 一种光伏组件用浮体的加工方法
JP2024176813A (ja) 2023-06-09 2024-12-19 豊田合成株式会社 積層体及び積層体の製造方法

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US20010040316A1 (en) * 1999-10-28 2001-11-15 Stewart David M.H. Method of making polyurethane composite materials
DE10138298A1 (de) * 2001-08-10 2003-02-27 Basf Ag Thermoplastische Polyurethane
WO2003071839A1 (fr) * 2002-02-20 2003-08-28 Matsushita Electric Works, Ltd. Dispositif et procédé de traitement au plasma
DE10308727B3 (de) * 2003-02-28 2004-06-09 Krauss-Maffei Kunststofftechnik Gmbh Verbundbauteil mit teilbeweglichen Elementen und Verfahren zu dessen Herstellung
DE10309989A1 (de) * 2003-02-28 2004-09-16 Hüttlin, Herbert, Dr.h.c. Tunnelförmige Vorrichtung zum Behandeln von partikelförmigem Gut
DE10333197A1 (de) * 2003-07-22 2005-02-10 Krauss-Maffei Kunststofftechnik Gmbh Verfahren zur Herstellung eines Kunststoff-Verbundbauteils

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KR20070110383A (ko) 2007-11-16
US20090042007A1 (en) 2009-02-12
DE102005008261A1 (de) 2006-08-24
JP2008531331A (ja) 2008-08-14
CN101128305A (zh) 2008-02-20
WO2006089893A1 (fr) 2006-08-31

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