Classifications

• • C—CHEMISTRY; METALLURGY
  • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
  • C09J—ADHESIVES; NON-MECHANICAL ASPECTS OF ADHESIVE PROCESSES IN GENERAL; ADHESIVE PROCESSES NOT PROVIDED FOR ELSEWHERE; USE OF MATERIALS AS ADHESIVES
  • C09J153/00—Adhesives based on block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Adhesives based on derivatives of such polymers
  • C09J153/02—Vinyl aromatic monomers and conjugated dienes
  • C09J153/025—Vinyl aromatic monomers and conjugated dienes modified

Definitions

• the present invention relates to adhesive compositions for protective films and to protective films, in particular protective films containing an adhesive layer on a flexible substrate, such as a thin substrate of a polyolefm, polyamide or a polyester.
• Protective film is a pressure sensitive adhesive tape or sheet intended for temporary application onto a surface, to protect that surface from adhesion of dust and/or from damage.
• Examples of surfaces to be protected by protective films are synthetic resin boards, decorative laminated sheets and metal plates.
• Protective films are e.g. used to protect the coated metal surface of cars during assembly of the car and transport from the manufacturing plant to car dealers.
• protective films must be tacky enough and have enough holding power to stick to a variety of surfaces; must be stable enough not to quickly deteriorate under the influence of UV; and must be easily removable from the surface it is protecting, without leaving any traces of adhesive.
• EP 0 519 278 A2 describes an automotive paint film - protective sheet comprising a substrate having formed on one side thereof a rubber-based pressure-sensitive adhesive having a dynamic modulus of from 2x10 ⁇ to 7x10 ⁇ dyne/cm ⁇ .
• the pressure-sensitive adhesives described therein consist essentially of an A-B-A block copolymer, wherein A is a styrene block and B is a hydrogenated butadiene block, a hydrogenated tackify g resm, and optionally an acrylic polymer.
• a disadvantage of the protective films described herein is that the pressure sensitive adhesive is too tacky which makes it difficult to remove the protective film or to manually apply the protective film.
• a further disadvantage is that the pressure sensitive adhesive composition is difficult tc handle. This makes application of the protective film cumbersome.
• the protective film is prepared by coating a solution or melt of the pressure sensitive adhesive onto a substrate. It would be desirable if a pressure sensitive adhesive composition would be found that can be co-extruded with the substrate .
• US 5,427,850 describes a protective film consisting essentially of an A-B-A block copolymer, wherein A is a styrene block and B is an optionally hydrogenated butadiene or isoprene block; a tackifymg resm and a polyolefm selected from low density polyethylene, linear low density polyethylene, medium density polyethylene, high density polyethylene and an ethylene- ⁇ -olefin copolymer wherein said polyolefm has a melt index of 0.1 to 30 g/10 mm. and less than 1.0% by weight of the polyolefm can be extracted m n-pentane.
• m order to achieve this commercially available polyolefm is first subjected to an extraction treatment prior to use m the preparation of adhesive compositions for protective films.
• the present invention relates to an adhesive composition
• an adhesive composition comprising: (I) a block copolymer containing at least two poly (monovmyl aromatic hydrocarbon) blocks and at least one hydrogenated poly (conjugated diene) block; (n) 20 to 80 parts by weight of an at least partially hydrogenated tackifymg resm per 100 parts by weight of block copolymer; (in) 0 to 40 parts by weight of aromatic resm per 100 parts by weight of block copolymer;
• rhe present invention relates to a process for preparing pellets containing the above adhesive composition.
• the process involves use of a, preferably twin-screw, extruder and an underwater pelletizer.
• the present invention relates to a process for preparing pellets containing an adhesive composition
• a process for preparing pellets containing an adhesive composition comprising: (l) dry-blending a block copolymer containing at least two poly (monovmyl aromatic hydrocarbon) blocks and at least one hydrogenated poly (conjugated diene) block, or a blend of the block copolymer with up to 25 parts by weight of plasticiser per 100 parts by weight of block copolymer, with 20 to 80 parts by weight of an at least partially hydrogenated tackifymg resm per 100 parts by weight of block copolymer, 10 to 60 parts by weight of a polybutene-1 per 100 parts by weight of block copolymer, and optionally up to 40 parts by weight of aromatic res per 100 parts by weight of block copolymer to obtain a dry-blend;
• the present invention relates to a process for preparing pellets containing an adhesive composition
• a process for preparing pellets containing an adhesive composition comprising: (l) adding a block copolymer containing at least two poly (monovmyl aromatic hydrocarbon) blocks and at least one hydrogenated poly ( con ugated diene) block, or a blen ⁇ of the block copolymer with up to 25 parts by weight of plasticiser per 100 parts DV weight of block copolymer; 20 to 80 parts by weignt of an at least partially hydrogenated tackifymg resm per 100 parts by weight of block copolymer; 10 to 60 parts by weight of a polybutene-1 per 100 parts by weight of block copolymer, and optionally up to 40 parts by weight of aromatic res per 100 parts by weight of block copolymer to separate feed inlet openings in an extruder; ( ⁇ ) blending and extruding the components in the extruder to obtain an extrudate;
• the present invention relates to a protective film comprising an adhesive layer and a substrate layer, wherein the adhesive layer comprises :
• the present invention relates to a process for preparing a protective film by co-extrusion of an extrudable substrate layer and an adhesive layer as defined herein, which process comprises feeding an adhesive composition to form the adhesive layer to a first extruder and feeding the substrate composition to form the substrate layer to a second extruder, melting the adhesive composition and the substrate composition and conveying the substantially molten adhesive composition and substrate composition with the first and second extruder respectively, at the same time to a die m hydraulic communication with the first and second extruder and co-extrud g a film comprising the adhesive layer and the substrate layer.
• the die is preferably a multi-manifold die.
• the extrusion process downstream of the first and second extruder is typically a cast film process or a blown film process. Both processes are well known in the art and have been described the Encyclopedia of Chemical Technology (Kirk-Othmer) , 1996, volume 19, in the chapter on plastic processing, pages 290-316, which pages are herein incorporated by reference.
• the present invention relates to articles containing a protective film as defined herein.
• the block copolymer (l) may be linear or radial, including linear triblock copolymers (ABA) , multi-armed block copolymers ((AB) n X), asymmetric block copolymers, such as ( (AB) n X (B' ) m , with A representing a monovmyl aromatic hydrocarbon polymer block, B and B' representing a hydrogenated conjugated diene polymer block, n being an integer of 2 or higher, preferably from 2 to 6, m being an integer of at least 1, preferably from 1 to 4, and X representing tne residue of a coupling agent.
• the block copolymer may contain up to 40% by weight, relative to the tota..
• block copolymer of a diolock copolymer AB preferably up to 30% by weight, more preferably up to 25% by weight. If it is desired that tne block copolymer (I) contains an amount of diblock copolymer, the latter is typically present in an amount of at least 5% by weight, preferably at least 10% by weight of the block copolymer (I) .
• the diblock copolymer apparent molecular weight is m the range of from 40,000 to 180,000, more preferably m the range of from 60,000 to 150,000.
• the block copolymer (I) may, for example, be prepared by coupling at least two diblock copolymer molecules AB together. As the coupling efficiency is not 100%, the block copolymer (l) will contain uncoupled diblock copolymer.
• the block copolymer (I) may however also consist of a blend of block copolymers, one being a diblock copolymer.
• the coupling agent may be any di- or polyfunctional coupling agent known m the art, for example, dibromoethane, silicon tetrachloride, diethyl adipate, divmylbenzene, dimethyldichlorosilane, methyl dichlorosilane .
• Particularly preferred in such a preparation route is the use of non-halogen containing coupling agents, for example gamma-glycidoxypropyl- t ⁇ methoxysilane, and diglycidylether of bisphenol A.
• the block copolymer to be used in the compound of the present invention may be prepared by any method known in the art including the well known full sequential polymerisation method, optionally in combination with re-initiation, and the coupling method, as illustrated in e.g. U.S. Patents Nos . 3,231,635; 3,251,905; 3,390,207; 3,598,887 and 4,219,627 and EP 0413294 A2 , EP 0387671 Bl, EP 0636654 Al, and WO 94/22931.
• the resultant block copolymer is hydrogenated in accordance with any one of the known methods (for example, the method as disclosed m U.S. Patent 3,700,633 which is herein incorporated by reference) to obtain the hydrogenated block copolymer (i) .
• the hydrogenated block copolymer (1) to be used in the present invention typically at least 80%, preferably at least 90%, more preferably at least 95% of the double bonds in the conjugated diene block (s) is hydrogenated.
• the hydrogenation degree can be analysed using the nuclear magnetic resonance (NMR) method.
• the mono-vinyl aromatic monomer is typically selected from styrene, C ] _-C4 alkylstyrene and Cj_-C4 dialkyl- styrene, m particular styrene, ⁇ -methylstyrene, o-methylstyrene or p-methylstyrene, 1 , 3-d ⁇ methylstyrene, p-tert . -butylstyrene or mixtures thereof, most preferably styrene.
• the conjugated diene monomer is typically a conjugated diene monomer containing from 4 to 8 carbon atoms, such as 1 , 3-butad ⁇ ene, 2-methyl-l , 3-butad ⁇ ene (isoprene), 2 , 3-d ⁇ methyl-l , 3-butad ⁇ ene, preferably butadiene or isoprene or mixtures thereof, most preferably butadiene.
• the 1,2-vmyl content of a butadiene block prior to hydrogenation is typically at least 25% by weight.
• the 1,2-vmyl content is n the range of from 30 to 90% by weight, more preferably from 35 to 80% by weight .
• polar compounds such as ethers, ammes and other Lewis bases and more in particular those selected from the group consisting of dialkylethers of glycols.
• Most preferred modifiers are selected from dialkyl ether of ethylene glycol containing the same or different terminal alkoxy groups and optionally bearing an alkyl substituent on the ethylene radical, such as monoglyme, diglyme, diethoxyethane, 1, 2-d ⁇ ethoxy-propane, l-ethoxy-2 , 2-tert- butoxyethane, of which 1 , 2-d ⁇ ethoxypropane is most preferred .
• the content of monovmyl aromatic hydrocarbon of the final block copolymer is preferably m the range of from 5 to 45% by weight, and more preferably 10 to 25% by weight, based on the total block copolymer.
• the total apparent molecular weight of the block copolymer is preferably in the range from 70,000 to 310,000, e.g. from 160,000 to 300,000 g/mol.
• Tackifymg resms are well known to those skilled in the art and a wide variety of different tackifymg resms is available commercially.
• the tackifymg resm to be used in the present invention is at least partially hydrogenated and is preferably a partially or fully hydrogenated hydrocarbon resm.
• the (partially) hydrogenated tackifymg resm preferably has an unsaturation index (U x ) of up to 22%, more preferably of up to 20%.
• the unsaturation index is determined by ⁇ - ⁇ NMR according to the procedure outlined in Canadian patent specification CA 1337218, incorporated herein by reference .
• the tackifymg resm preferably has a softening point as determined by the Ring and Ball method (ASTM E28) m the range of from 75 to 140 °C, say of from 75 to 125 °C, more preferably 80 to 105 °C.
• the tackifymg resm is a fully hydrogenated hydrocarbon resm.
• a fully hydrogenated hydrocarbon resm typically has an unsaturation index of less than 5%.
• the tackifymg resm is present in an amount from 20 to 80 parts by weight (pbw) per 100 parts by weight of block copolymer.
• An adhesive composition containing less than 20 pbw will not have sufficient tack and a composition containing more than 80 pbw will be too tacky and will be difficult to coextrude.
• the tackifymg resm is present in an amount from 25 to 65 pbw, more preferably from 30 to 55 pbw, per 100 parts by weight of block copolymer.
• the polybutene-1 typically has a crystallmity of less than 80%. Crystallmity is determined with wide- angle X-ray diffraction after 7 days. Preferably, the crystallmity is in the range from 0 to 60%.
• the polybutene-1 is preferably a polybutene-1 copolymer .
• the polybutene-1 (polybutylene) referred to herein is one butene-1 polymer containing from 80% preferably from 95% and more preferably from 97% by weight of isotactic portions.
• the weight average molecular weight typically may range from 60,000 to 1,000,000 g/mol, determined by Gel Permeation
• Suitable poly-1-butenes also have a density of from 0.875 to 0.925, preferably from 0.890 to 0.920.
• Suitable poly-1- butenes have melt flow indices in the range of from 0.05 to 400, preferably 0.05 to 300, more preferably from 0.1 to 200, even more preferably from 0.2 to 20, and most preferably from 0.4 to 5 dg/mm, as determined by ASTM D- 1238 Condition E, at 190 °C and 2.16 kg.
• the intrinsic viscosity of the poly-1-butene may range from 0.07, preferably from 7 at 130 °C in "decalin" (decahydro- naphthalene) .
• poly-1-butene polymers including their methods of preparation, and their properties are known in the art.
• An exemplary reference containing additional information on polybutylene is U.S. Patent No. 4,960,820 which is herein incorporated by reference.
• a poly-1-butene polymer (PB) usable herein is either a butene-1 homopolymer or a copolymer. If a butene-1 copolymer is used, the non-butene comonomer content is from 1 to 50 mole%, preferably from 1 to 30 mole% of either ethylene, propylene, or an alpha olefin having from 5 to 8 carbon atoms.
• the poly-1-butenes can be modified to increase surface activity by reaction with, for example, maleic anhydride.
• Suitable poly-1-butenes can be obtained, for example, in accordance with Ziegler-Natta low-pressure polymerization of butene-1, e.g. by polymerizing butene-1 with catalysts of T1CI3 or T1CI3-AICI3 and A1(C H5)2C1 at temperatures of 10-100 °C, preferably 20-40 °C, e.g. according to the process described in DE-A-1 , 570, 353. It can also be obtained, for example by using T ⁇ Cl -MgCl2 catalysts . High melt indices are obtainable by further processing the polymer by peroxide cracking, thermal treatment or irradiation to induce scissions leading to a higher melt flow material.
• PB-8310 and PB-0300 are particularly suitable polymers.
• PB-8310 is a copolymer of butene-1 and 6 mole% ethylene, with a melt index of 3.0 g/10 mm. at 190 °C and 2.16 kg, a crystallmity of 34% and a density of 0.895.
• PB-0300 is a homopolymer of butene-1, with a melt index of 4.0 g/10 mm. at 190 °C and 2.16 kg, a crystallmity of 55% and a density of 0.915.
• the polybutene-1 homopolymer typically has a crystallmity of at least 30o by weight when measured witn wide-angle X-ray diffraction after 7 days, but preferably less than 70% by weight.
• the polybutene-1 is typically present m an amount from 5 to 60 parts by weight (pbw) per 100 parts by weight of block copolymer.
• An adhesive composition containing less than 5 pbw will not have a stable peel adhesion strength. Rather, the peel adhesion will increase upon ageing.
• a composition containing more than 60 pbw will have a too low peel adhesion.
• the polyolefm is present m an amount from 8 to 40 pbw, more preferably from 10 to 30 pbw, per 100 parts by weight of block copolymer.
• Plasticisers are well known to those skilled in the art. Typically, the hardness of polymer compound is decreased by adding a plasticiser. The plasticiser is typically substantially compatible with at least the hydrogenated conjugated diene block (s) of the block copolymer (a) .
• plasticisers commonly used include oil, preferably naphthemc or paraffmic oil, more preferably paraffmic oil.
• plasticisers which may be used m the compound of the invention are, oligomers of randomly or sequentially polymerised styrene and conjugated diene, oligomers of conjugated diene, such as butadiene or isoprene, liquid polybutene-1, and ethylene-propylene-diene rubber, all having a weight average molecular weight in the range from 300 to 35,000, preferably from 300 to 25,000, more preferably from 500 to 10,000.
• the adhesive composition may further comprise a poly (monovmyl aromatic block) compatible resm.
• a poly (monovmyl aromatic block) compatible resm Such resms are well known to those skilled m the art. Examples of suitable resms include coumarone- dene resm, polymdene resm, poly(methyl indene* resm, polystyrene resm, vmyltoluene-alphamethylstyrene resm, alphamethylstyrene resm and polyphenylene ether, particular poly (2 , 6-d ⁇ methyl-l , 4-phenylene ether).
• Poly (monovmyl aromatic hydrocarbon) compatible resms are e.g. sold under the tradenames HERCURES, ENDEX, KRISTALLEX, NEVCHEM and PICCOTEX.
• the adhesive composition preferably further comprises a dusting agent in an amount from 0.1 to 10% by weight, more preferably from 0.2 to 5% by weight, basis the total composition .
• the dusting agent is a very fine powder having on average a particle size between 1 nm and 100 ⁇ m, preferably between 5 nm and 10 ⁇ m.
• an adhesive composition which is free flowing can be obtained.
• the term "free flowing adhesive composition” refers to an adhesive composition of the present invention which contains a dusting agent and in which the particles of the composition do not adhere to one another.
• any such fine powder may be employed but it is preferred that a polyolefm, such as polyethylene, silica, talc or calcium carbonate powder is used.
• Examples of commercially available silica powders include, but are not limited to, AEROSIL R972 (average particle size about 16 nm) , AEROSIL 200
• the dusting agent is typically used m an amount of from 0.05 to 10% by weight, preferably from 0.1 to 5% oy weight, based on total weight of the compositio .
• the adhesive composition may further comprise from 0 to 100 parts by weight of filler per 100 parts by weight of block copolymer.
• suitable fillers include silica and calcium carbonate.
• the adhesive composition may contain one or more auxiliary components such as stabilisers, flame retardants, anti- blocking agents and anti-slippmg agents. These components are typically present in an amount from 0.1 to
• the present invention further relates to a process for preparing pellets containing the above adhesive composition.
• the process involves use of an extruder and an underwater pelletizer.
• the extruder is a twin-screw extruder, more preferably a co-rotating twin-screw extruder.
• Underwater pelletizers are well known to those skilled in the art and are available commercially. Other pelletizers such as face cutters and strand granulators have been found to be less suitable as use of face cutters or strand granulators does not result n uniform pellet size distributions. Furthermore, most of the adhesive compositions have the tendency to agglomerate in a face cutter or stick to the knives of a strand granulator, preventing easy production of these adhesive compositions in pellet form.
• the present invention further relates to protective films consisting essentially of an adhesive layer and a substrate layer. If desired, the adhesive layer may further be covered with a protective laminated sheet such as siliconised paper.
• the substrate layer is preferably an extrudable substrate layer. Examples include polyolefms such as polyethylene, polypropylene and copolymers of polyethylene and polypropylene.
• Pellets containing an adhesive composition were prepared by first dry-blending a block copolymer, a hydrogenated tackifymg resm, a polyolefm and an antioxidant in a tumbler mixer for 30 minutes.
• the dry- blend thus obtained was fed into a MARIS (trademark) single port twin-screw extruder fitted with a GALA (trademark) underwater pelletizer.
• a detergent and an antifoammg agent TEGO anti foam 1488 0.01% by weight m HORDEMER PE03 soap was added to the pelletizer water to avoid agglomeration of the wet pellets (TEGO and HORDEMER are trademarks) .
• the wet pellets were dried by centrifugal drier with dry air flow. Talc was added as a dusting agent.
• KRATON G1657 which is a linear block copolymer having two terminal styrene blocks and one hydrogenated butadiene midblock (KRATON is a trademark) .
• KRATON G1657 is a coupled block copolymer containing 30 wt% diblock copolymer. The polystyrene content is 13 wt%.
• polystyrene-1 copolymers PB8310 and PB0300 marketed by Montell.
• REGALIT ⁇ R101 (REGALITE is a trademark) .
• REGALITE R101 is a hydrogenated hydrocarbon resm having a softening point of 99 °C.
• the antioxidant used m the Examples is tetrakis- ethylene- (3, 5-d ⁇ -tert ⁇ ary-butyl-4-hydroxy-hydrocmna- mate)methane, marketed as IRGANOX 1010 (IRGANOX is a trademark) .
• compositions 1 and 2 were free-flowing pellets .
• compositions 1 and 2 were co-extruded with polyethylene in a 40 mm single screw co-extruder having a Length/Diameter ratio of 27. The compression ratio was 1.5.
• a two-layer protective film was co-extruded at a temperature ranging from 100 °C (inlet) to 150 °C (outlet) .
• the protective film consisted of a 25 ⁇ m adhesive layer and a 75 ⁇ m polyethylene substrate layer.
• the polyethylene used for the substrate was LDPE ex. DSM with a Melt Index (polyethylene condition) of 4.4.
• the films 1 and 2, containing adhesive compositions 1 or 2 respectively, were laminated on the adhesive side with silicomsed paper for easy handling.

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• Chemical & Material Sciences (AREA)
• Chemical Kinetics & Catalysis (AREA)
• Organic Chemistry (AREA)
• Adhesives Or Adhesive Processes (AREA)
• Adhesive Tapes (AREA)
• Extrusion Moulding Of Plastics Or The Like (AREA)
• Materials For Medical Uses (AREA)

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• 2000
  • 2000-06-09 WO PCT/EP2000/005408 patent/WO2000077118A1/en not_active Ceased
  • 2000-06-09 JP JP2001503960A patent/JP4829446B2/ja not_active Expired - Fee Related
  • 2000-06-09 BR BRPI0011472-3A patent/BR0011472B1/pt not_active IP Right Cessation
  • 2000-06-09 ES ES00935203T patent/ES2223527T3/es not_active Expired - Lifetime
  • 2000-06-09 DE DE60014073T patent/DE60014073T2/de not_active Expired - Lifetime
  • 2000-06-09 EP EP00935203A patent/EP1185597B1/en not_active Expired - Lifetime
  • 2000-06-09 AT AT00935203T patent/ATE277140T1/de not_active IP Right Cessation
  • 2000-06-09 AU AU50777/00A patent/AU5077700A/en not_active Abandoned

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