Styrene-isoprene-styrene block copolymer composition for low viscosity low application temperature hot melt adhesives

Abstract: A low viscosity low application temperature hot melt adhesive which contains a predominantly branched styrene-isoprene-styrene block copolymer composition comprised of linear polymeric blocks wherein the polystyrene block molecular weight is greater than 12,000, the polystyrene content is 35% or less by weight of the block copolymer composition and the molecular weight of the block copolymer composition and the coupling efficiency are chosen so that the melt viscosity of the adhesive made with the composition is less than 3100 cps.

Description: This invention relates to a novel block copolymer composition for use in low viscosity low application temperature hot melt adhesives. More particularly, it relates to predominantly branched styrene-isoprene-styrene block copolymer compositions comprised of linear polymeric blocks and adhesives made using such compositions. It is known that a block copolymer can be obtained by an anionic copolymerization of a conjugated diene compound and an alkenyl arene compound by using an organic alkali metal initiator. Block copolymers have been produced which comprise primarily those having a general structure A―B and A―B―A wherein the polymer blocks A comprise thermoplastic polymer blocks of alkenyl arenes such as polystyrene, while block B is a polymer block of a conjugated diene such as polyisoprene. The proportion of the thermoplastic blocks to the elastomeric polymer block and the relative molecular weights of each of these blocks is balanced to obtain a rubber having unique performance characteristics. When the content of the alkenyl arene is small, the produced block copolmer is a so-called thermoplastic rubber. In such a rubber, the blocks A are thermodynamically incompatible with the blocks B resulting in a rubber consisting of two phases - a continuous elastomeric phase (blocks B) and a basically discontinuous hard, glass-like plastic phase (blocks A) called domains. Since the A-B-A block copolymers have two A blocks separated by a B block, domain formation results in effectively locking the B blocks and their inherent entanglements in place by the A blocks and forming a network structure. These domains act as physical crosslinks anchoring the ends of many block copolymer chains. Such a phenomenon allows the A-B-A rubber to behave like a conventionally vulcanized rubber in the unvulcanized state and is applicable for various uses. For example, these network forming polymers are applicable for use in adhesive formulations; as mouldings of shoe soles, etc.; impact modifier for polystyrene resins and engineering thermoplastics; modification of asphalt; etc. Styrenic block copolymers are widely used to make hot melt adhesives for a wide variety of uses including diaper assembly. Hot melt adhesives based on styrenic block copolymers such as KRATON thermoplastic rubber (KRATON is a trade mark) provide excellent adhesion to non-polar substrates such as polyethylene which are commonly used in diaper manufacture. Additionally, such styrenic block copolymer based adhesives maintain adhesion in elasticity demanding applications such as disposable diapers. Relatively low styrene content (from 15% to 24%) styrene-isoprene-styrene block copolymers are known to be useful for adhesives for such applications. New improvements have necessitated the development of new hot melt adhesives for use in the manufacture of disposable diapers. Diaper manufacturers now use thinner gauge polyethylene to manufacture diapers. Not only does thinner gauge polyethylene produce a more esthetically pleasing diaper but it also represents significant cost savings. However, as the gauge of the polyethylene is decreased, the likelihood of burn through of these thin layers has increased. In the past, the lower limit on the operating temperature has been defined by the temperature at which the hot melt adhesive could be applied with sufficiently low viscosity for even and proper application. Such temperatures were in the range of 149 °C to 177 °C. The industry would like to operate at from about 121° to about 149 °C. Thus, it is clear that there is a need for a hot melt adhesive which is characterised by sufficiently low viscosity for proper application in diaper manufacture at these lower temperatures to help prevent burn through of the thinner gauge polyethylene used in the new diaper assemblies. There are new commercial products which purport to satisfy this need. However, these commercial products do not provide the balance of adhesive performance properties which is provided by the present invention, i.e., a melt viscosity of less than 3100 cps at a temperature of 177 °C and a shear adhesion failure temperature (SAFT) of greater than 71 °C. The present invention provides block copolymer compositions which can be used to make adhesives satisfying these criteria. Accordingly the present invention relates to branched styrene-isoprene block copolymer compositions of the formula (SI) 3 X, wherein S is a linear poly(styrene) block and I is a linear poly(isoprene) block and X represents the residue of a trivalent coupling agent substantially free of tetravalent coupling agent residues, to be used in low viscosity - low application temperature hot melt adhesives which have a melt viscosity of less than 3100 cps at a temperature of 177 °C and a SAFT of greater than 71 °C, said block copolymers characterised in that; (a) the polystyrene block molecular weight must be greater than 12,000. (b) the polystyrene content must be 35% or less by weight of the block copolymer composition and (c) the molecular weight and coupling efficiency of the block copolymer composition must fall to the left of line A-A in Figure 1, representing a graph of the coupling efficiency versus the molecular weight of the overall composition. The present invention also encompasses a low viscosity, low application temperature hot melt adhesive, comprising the above block copolymer composition and a tackifying resin. The branched SIS block copolymers, having three linear arms, can be prepared by methods which are in principle know in the art. As is well known, polymers containing both aromatic and ethylenic unsaturation can be prepared by copolymerizing one or more polyolefins, particularly a diolefin, such as isoprene, with one or more alkenylaromatic hydrocarbon monomers, such as styrene. Polymers of conjugated diolefins and copolymers of one or more conjugated diolefins and one or more alkenyl aromatic hydrocarbon monomers such as predominantly branched SIS block copolymers are normally prepared in solution using anionic polymerization techniques. The predominantly branched block copolymers have three arms with the following structure: (SI)3 In general, when solution anionic techniques are used, the initial SI block copolymers are prepared by contacting the mononers to be polymerized simultaneously or sequentially with an organoalkali metal compound in a suitable solvent at a temperature within the range from -150 °C to 300 °C, preferably at a temperature within the range from 0 °C to 100 °C. Particularly effective anionic polymerization initiators are organolithium compounds having the general formula: RLi p wherein: R is an aliphatic, cycloaliphatic, aromatic or alkyl-substituted aromatic hydrocarbon radical having from 1 to 20 carbon atoms; and p is an integer of 1 to 4. Preferably, sec.-butyllithium is used for the initial block copolymers to be coupled. In general, any of the solvents known in the prior art to be useful in the preparation of such polymers may be used. Suitable solvents, then, include for example cycloaliphatic hydrocarbons such as cyclopentane, cyclohexane, cycloheptane and the like, as well as, alkyl-substituted derivatives thereof; aromatic and alkyl-substituted aromatic hydrocarbons such as benzene, naphthalene, toluene, xylene and the like; hydrogenated aromatic hydrocarbons such as tetralin, decalin and the like; linear and cyclic ethers such as methyl ether, methyl ethyl ether, tetrahydrofuran and the like. As described in U.S. Patent No. 4,096,203, usually the styrene is contacted with the initiator. Next, the living polymer in solution is contacted with isoprene. The result living polymer has a simplified structure S-I-Li. It is at this point that the living polymer is coupled. There are a wide variety of coupling agents that can be employed. Any polyfunctional coupling agent which contains three reactive sites can be employed. Examples of the types of compounds which can be used include those, which have been described in U.S. Patent Nos. 3,595,941; 3,468,972; 3,135,716; 3,078,254, and 3,594,452 From European patent application no. 0171225 it was known to prepare coupled alkenyl aromatic compound - conjugated block copolymer and pressure sensitive adhesive composition containing the same. The block copolymers having the structure: [(A-B)m] n X or [(A-B-A 1 )m] n X wherein A and A 1 represents the same or different poly(alkenylaromatic) blocks and B represents a poly(conjugated diene) block and X represents the residue of a tin-containing coupling agent and the residue of a non-tin-containing coupling agent, m is an integer of 1 of more and n is an integer from 2 to 6 corresponding to the functionality of X. In particular in example 6 in table 2 a mixture of tetra-armed and three armed coupled block copolymers were prepared by using tin tetrachloride and dichloromethylsilane, wherein the poly(styrene) blocks had a molecular weight of 16000 and the poly(isoprene) blocks had a molecular weight of 37000 and the average total molecular weight was 159.000. When the coupling agent has three reactive sites, such as trisnonylphenylphosphite (TNPP), the polymer will have a branched structure, such as: (SI) 3 x For the preparation of the present block copolymers predominantly branched, a coupling agent with three reactive sites must be used. Preferred coupling agents which can be used include trisnonylphenylphosphite (TNPP), trimethoxy phosphite and triethoxy phosphite, of which TNPP being the most preferred. In the prior art, such as that exemplified by U.S. Patent Nos. 3,595,941 and 3,468,972, the effort was always made to select the particular coupling agent or reaction conditions that resulted in the highest coupling efficiency. High coupling efficiency is desired herein in order to produce strong adhesive compositions. Coupling efficiency is defined as the number of molecules of coupled polymer divided by the number of molecules of coupled polymer plus the number of molecules of uncoupled polymer. Thus, when producing an SIS branched polymer according to the present invention, the coupling efficiency is shown by the following relationship: # of Molecules of SIS # of molecules of SIS plus SI Coupling efficiency can be determined theoretically from the stoichiometric quantity of coupling agent required for complete coupling or coupling efficiency can be determined by an analytical method such as gel permeation chromatography, as was known from e.g. U.S. Patent No. 4,096,203, teaching that the coupling efficiency could be controlled from 20% to 80%, preferably 30% to 70%. It is also within the scope of the present invention to prepare the desired copolymers having the desired SAFT-value by blending polymers from processes of differing coupling efficiency. It was found that, if the coupling efficiency of the block copolymers is too low, i.e., less than 60%, the SAFT may fall below 71 °C. This coupling efficiency is controlled by a number of methods as disclosed in U.S. patent No. 4,096,203, columns 3 and 4. Following the coupling reaction or when the desired coupling efficiency has been obtained, the product is neutralized such as by the addition of terminators, e.g. water, alcohol or other reagents, for the purpose of removing the lithium radical forming the nucleus for the condensed polymer product. The product is then recovered such as by coagulation utilizing hot water or steam or both. As discussed above, for certain new applications in the diaper industry, it has been determined that an adhesive formulation must exhibit good adhesion and have a melt viscosity of less than 3100 cps at 177 °C and a shear adhesion failure temperature (SAFT) of greater than 71 °C. The present invention provides block copolymers and an adhesive which satisfies these requirements. The composition is a predominantly branched SIS block copolymer composition which is comprised of linear polymeric blocks. In order to achieve the standards set forth above, the compositions and adhesives of the present invention must have the following characteristics: (1) a polystyrene block molecular weight (PS MW) of greater than 12,000; (2) a polystyrene content (PSC) of 35% or less; and (3) an overall molecular weight (M s - styrene equivalent molecular weight) and coupling efficiency which fall to the left of line A-A in Figure 1. It has been determined that if the above compositions do not have the above characteristics, then the adhesion, melt viscosity and SAFT criterion cannot be met. However, if the composition does have the above characteristics, then the adhesion, melt viscosity and SAFT criterion are satisfied. Figure 1 is a plot of coupling efficiency versus overall molecular weight based on data from the examples. The line A-A represents a contour line of constant melt viscosity of 3100 cps. If a point is to the right of this line, the melt viscosity will be too high. The shaded area to the left of the line represents the area of operability. If the polystyrene content is greater than 35%, the adhesion of the adhesives made from the composition is poor. Generally, for high SAFT, large styrene blocks are necessary, thus necessitating at least 12,000 PS MW to achieve an SAFT of 71 °C or greater. If the PS MW is greater than 14,000, an SAFT of 75 °C or more can be achieved which will allow the adhesive to exhibit higher creep resistance. A relatively narrow range of operable compositions is defined herein since the characteristics are interrelated. Thus, the PS must be greater than 12,000 for a desired SAFT but cannot be too high because then either the PSC or the overall molecular weight will be too high. The PSC cannot be too low or the PS MW will be too low. The concentration of the initiator can be regulated to control the molecular weight of the overall composition and of the polystyrene blocks. Generally, the initiator concentration is in the range of 0.25 to 50 millimoles per 100 grams of monomer. The required initiator level frequently depends upon the solubility of the initiator in the hydrocarbon diluent. The ratio of the initiator to the monomer determines the block size, i.e. the higher the ratio of initiator to monomer the smaller the molecular weight of the block. Methods of controlling the molecular weights of the blocks and the overall polymer are quite well known. For instance, such are disclosed in U.S. Patent 3,149,182, which states that the amount of monomer can be kept constant and different molecular weights can be achieved by changing the amount of initiator or the amount of initiator can be kept constant and different molecular weights can be achieved by varying the amount of the monomer, and in U.S. 3,231,635 and many others. A typical block copolymer composition within the scope of the present invention, having a coupling efficiency of 90%, a polystyrene block molecular weight of 15,000, a polystyrene content of 30% and an overall molecular weight of 183,000, was prepared by polymerizing styrene with sec.-butyllithium as initiator at a monomer to initiator molar ratio of 144 to 1 and then completing the polymerization, polymerizing isoprene at a monomer to initiator molar ratio of 283 to 1 and then completing the polymerization and finally coupling the living polymer obtained by means of TNPP in an amount of 0.8% by weight based on the weight of the polymer. It is necessary to add an adhesion promoting or tackifying resin that is compatible with the elastomeric conjugated diene block. A common tackifying resin is a diene-olefin copolymer of piperylene and 2-methyl-2-butene having a softening point of 95 °C. This resin is available commercially under the tradename Wingtack 95 and is prepared by the cationic polymerization of 60% piperylene, 10% isoprene, 5% cyclopentadiene, 15% 2-methyl-2-butene and 10% dimer, as taught in U.S. Patent No. 3,577,398. Other tackifying resins of the same general type may be employed in which the resinous copolymer comprises 20-80 weight percent of piperylene and 80-20 weight percent of 2-methyl-2-butene. The resins normally have softening points (ring and ball) between 80 °C and 115 °C. Other adhesion promoting resins which are also useful in the compositions of this invention include hydrogenated rosins, esters of rosins, polyterpenes, terpenephenol resins and polymerized mixed olefins. To obtain good thermo-oxidative and color stability, it is preferred that the tackifying resin be a saturated resin, e.g., a hydrogenated dicyclopentadiene resin such as Escorez 5000 series resin (Escorez is a trade mark) made by Exxon or a hydrogenated polystyrene or polyalphamethylstyrene resin such as Regalrez resin (Regalrez is a trade mark) made by Hercules. The amount of adhesion promoting resin employed varies from 20 to 400 parts by weight per hundred parts rubber (phr), preferably between 100 to 350 phr. The selection of the particular tackifying agent is, in large part, dependent upon the specific block copolymer employed in the respective adhesive composition. In the manufacture of disposable articles such as diapers, sanitary napkins and bed pads, there is the additional consideration of having a substantially white or clear adhesive composition. The adhesive composition of the instant invention may contain plasticizers, such as rubber extending plasticizers, or compounding oils or liquid resins. Rubber compounding oils are well-known in the art and include both high saturates content oils and high aromatics content oils. Preferred plasticizers are highly saturated oils, e.g. Tufflo 6056 oil (Tufflo is a trade mark) made by Arco. The amounts of rubber compounding oil employed in the invention composition can vary from 0 to 100 phr, and preferably between 0 to 60 phr. Optional components of the present invention are stabilizers which inhibit or retard heat degradation, oxidation, skin formation and colour formation. Stabilizers are typically added to the commercially available compounds in order to protect the polymers against heat degradation and oxidation during the preparation, use and high temperature storage of the adhesive composition. Additional stabilizers known in the art may also be incorporated into the adhesive composition. These may be for protection during the life of the disposable article against, for example, oxygen, ozone and ultra-violet radiation. However, these additional stabilizers should be compatible with the essential stabilizers mentioned herein-above and their intended function as taught herein. The adhesive compositions of the present invention are typically prepared by blending the components at an elevated temperature, preferably between 130 °C and 200 °C, until a homogeneous blend is obtained, usually less than three (3) hours. Various methods of blending are known to the art and any method that produces a homogeneous blend is satisfactory. The resultant adhesives may then preferably be used in a wide variety of product assembly applications. A particularly preferred application is their use in bonding polyethylene or polypropylene substrates to tissue, non-wovens or other polyethylene or polypropylene substrates using techniques involving multiple dispositions of small quantities of the adhesives according to conventional "multi-line" or "multi-dot" type constructions. Although the procedures used to manufacture these disposable constructions vary depending upon the particular manufacturer, the adhesive is generally extruded in lines (or dots) at regularly spaced intervals along the length of the article. The adhesive may be applied at temperatures as low as 121 °C. An additional advantage of the adhesive of the present invention is that it can be effectively applied by spraying. The adhesive is usually applied to the polyethylene or polypropylene backing and subsequently the combination is mated with an absorbent inner core and tissue or non-woven liner. Another important advantage of the compositions of the present invention is that they give much higher strength than similarly made linear polymers which also meet the industry standards. This is shown in the examples in Table 2. In the following examples, the coupling efficiency was determined by the method described above. The melt viscosity was measured in centipoise-seconds (cps) by using a Brookfield Thermocell viscometer at 177 °C. The SAFT was measured by 1" x 1" Mylar to Mylar lap joint with a 1 kg weight. SAFT measures the temperature at which the lap shear assembly fails under load. The molecular weights were determined by gel permeation chromatography as styrene equivalent molecular weight. The polystyrene content was determined by infrared spectroscopy. A series of predominantly branched SIS block copolymers comprised of linear polymeric blocks were made and analyzed (samples 1-10). For comparative purposes, one commercially available product which is currently being touted for use in low temperature low viscosity applications was also analyzed (A). This is also thought to be a branched SIS block copolymer comprised of linear polymeric blocks but it can be seen that it does not meet the specifications of the present invention. The block copolymer compositions were made according to the procedure discussed above. The coupling agent was TNPP. They were used to make adhesives by blending 25% polymer with 60% tackifying resin (Escorez 5300) and 15% plasticizer (Tufflo 6056). The formulations were stabilized with 1 phr of Irganox 1010 (Irganox is a trade mark). Samples 1, 3 and 8-10 are all acceptable since they meet all of the criteria stated above. Samples 2, 4 and 5 are all unacceptable since their melt viscosity is too high - see that they all appear to the right of line A-A in Figure 1. Samples 6 and 7 are unacceptable because their PSC is more than 35% and thus the adhesion is poor. The competitive material fails because its SAFT is much too low as a result of the polystyrene block molecular weight being below 12,000. Table 2 compares the tensile properties of Samples 8, 9 and 10 with a similarly made linear SIS block copolymer. Stress at 100% is the stress in bar at 100% strain. Tensile strength is the ultimate strength at break in bar. E B is the elongation % at break. All test results were performed on an Instron tester. It can be seen that the tensile strength of the branched polymers is considerably greater than the tensile strength of the linear polymer. Tensile Properties Sample C.E. (%) PSC (%) Stress @ 100% Tensile Strength EB (%) Linear 84 30 11.7 165.5 1050 Branched 8 87 33 21.0 265.5 1000 9 77 30 11.4 220.7 1025 10 72 29 14.8 200.0 1050

Claims: Claims for the following Contracting States : BE, DE, DK, FR, GB, IT, NL, SE Branched block copolymers according to the formula (SI)3X, wherein S is a linear poly(styrene) block and I is a linear poly(isoprene) block, and X represents the residue of a trivalent coupling agent substantially free of tetravalent coupling agent residues, to be used in low viscosity low application temperature hot melt adhesives, which have a melt viscosity of less than 3100 cps at a temperature of 177°C and a SAFT of greater than 71°C, said block copolymers characterised in that: (a) the polystyrene block molecular weight is greater than 12,000; (b) the polystyrene content range is 35% or less by weight of the block copolymer composition; and (c) the overall molecular weight of the block copolymer and the coupling efficiency are chosen to fall in the area to the left of A-A in Figure 1. Branched block copolymers according to claim 1, wherein the polystyrene block molecular weight is greater than 14,000. Branched block copolymers according to claims 1 and 2, characterised in that X is the residue of trisnonylphenyl phosphite, trimethoxy phosphite or triethoxy phosphite. Branched block copolymers according to claim 3 characterised in that X is the residue of tris nonyl phenyl phosphite. A diaper adhesive composition comprising the block copolymers of claims 1-4, and from 20 to 400 parts by weight, per 100 parts by weight of the block copolymer, of a tackifying resin which is compatible with the poly(isoprene) blocks. Claims for the following Contracting State : ES Process for preparing branched block copolymers according to the formula (SI) 3X, wherein S is a linear poly(styrene) block and I is a linear poly(isoprene) block, and X represents the residue of a trivalent coupling agent substantially free of tetravalent coupling agent residues, in a known manner, which block copolymers are to be used in low viscosity low application temperature hot melt adhesives, which have a melt viscosity of less than 3100 cps at a temperature of 177°C and a SAFT of greater than 71°C, said block copolymers characterised in that: (a) the polystyrene block molecular weight is greater than 12,000; (b) the polystyrene content range is 35% or less by weight of the block copolymer composition; and (c) the overall molecular weight of the block copolymer and the coupling efficiency are chosen to fall in the area to the left of A-A in Figure 1. Process for preparing branched block copolymers according to claim 1, wherein the polystyrene block molecular weight is greater than 14,000. Process for preparing branched block copolymers according to claims 1 and 2, characterised in that X is the residue of trisnonylphenyl phosphite, trimethoxy phosphite or triethoxy phosphite. Process for preparing branched block copolymers according to claim 3 characterised in that X is the residue of tris nonyl phenyl phosphite. Process for preparing diaper adhesive composition in a known manner, wherein the composition comprises the block copolymers of claims 1-4, and from 20 to 400 parts by weight, per 100 parts by weight of the block copolymer, of a tackifying resin which is compatible with the poly(isoprene) blocks.

Inventors: CHIN STEVEN SOOHYUN, CHIN, STEVEN SOOHYUN
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1991
Main classification: C08F297
IPC codes: C08F297, C09J153