NL2011591C2

NL2011591C2 - A radial styrenic block copolymer and an improved latex comprising water and said radial styrenic block copolymer.

Info

Publication number: NL2011591C2
Application number: NL2011591A
Authority: NL
Inventors: Wouter Jong
Original assignee: Kraton Polymers Us Llc
Priority date: 2013-10-11
Filing date: 2013-10-11
Publication date: 2015-04-14

Description

Description A radial styrenic block copolymer and an improved latex comprising water and said radial styrenic block copolymer

Technical Field [0001] The current invention concerns a radial styrenic block copolymer and an improved latex comprising water, and the radial styrenic block copolymer dispersed therein. Moreover, it concerns a process for preparing articles by coagulation dipping from the improved latex. It also concerns the dipped goods so produced.

Background Art [0002] The majority of commercial surgical gloves are still manufactured from natural rubber latex (NRL). However, NRL can lead to Type I allergic reactions, including risk of anaphylactic shock. In the race to reduce patient and medical staff allergy risks, a growing number of hospitals aim to eliminate products made from NRL, including surgical gloves. Drawbacks of NRL, including odor, and adverse allergic (Type I) reactions, led to the development of synthetic alternatives. However, replacement of NRL surgical gloves by synthetic alternatives has caused in the past some concerns regarding comfort and protection.

[0003] Needed today are surgical gloves with excellent properties in the following areas: tensile strength, modulus, and puncture resistance. The new surgical gloves should offer mechanical properties and protection that is at least comparable to NRL gloves. Moreover, the surgical gloves should preferably be superior to NRL gloves in terms of comfort (which is a balance of strength and modulus).

[0004] Similar demands are made with respect to other dipped goods, such as condoms.

[0005] Vulcanization is a chemical process for converting rubber or related polymers into more durable materials via the addition of a curing system such as sulphur or equivalent vulcanizers in combination with additives that modify the kinetics of the vulcanizer, known as accelerators. From WO 2013/025440 articles with enhanced tensile strength and comfort are known, that are prepared from a latex comprising water, a styrenic block copolymer and a vulcanizer, by a process which comprises coating a surface with the latex to obtain a film and vulcanizing the same. The styrenic block copolymer has 2 or more poly(vinyl aromatic) blocks and at least one block of polymerized conjugated diene, wherein the styrenic block copolymer has a weight average molecular weight of 150,000 to 250,000, the poly(vinyl aromatic) blocks have a weight average molecular weight ranging from 9,000 to 15,000, and the content of poly(vinyl aromatic) blocks in the styrenic block copolymer ranges from 8 to 15 %wt, based on the total styrenic block copolymer. The preferred styrenic block copolymer that is used in the experiments is a linear styrenic block copolymer.

[0006] This reference also provides a latex comprising such a styrenic block copolymer and a vulcanizer, as well as a styrenic block copolymer that is particularly suitable for use in such a latex. Excellent mechanical properties are achieved with this latex/vulcanizer system. Moreover, the gloves prepared from the artificial latex excel in comfort. On the other hand, there is an increasing demand for dipped goods that are free of products used as vulcanizers and accelerators. Vulcanizers and accelerators on the one hand provide strength, but on the other hand may act as allergens, causing sensibilisation.

[0007] WO2013025440 teaches to use a vulcanizer. The latex may in theory be used without vulcanizer. However, those that have tried to use the latex of WO2013025440 without vulcanizer found out that the strength is then insufficient unless this system is annealed at a temperature of between 100-130 °C, preferably about 120 °C. Annealing at a higher temperature causes damage to the film. Moreover, they found that the latex used without vulcanizer when annealed at the appropriate annealing temperature suffers from a phenomenon referred to as "ballooning". Ballooning is a permanent deformation of the film. There is no solution provided in the prior art with respect of this problem.

[0008] In US 5500469 an artificial latex comprising a stable aqueous colloidal dispersion of a preformed multiblock copolymer prepared using a sulfate of an ethoxylated phenol as a dispersing and stabilizing agent is described. This composition is particularly suitable for preparing articles such as gloves or condoms that are free of vulcanizers. The multiblock copolymer has the formula: A-B-Ym -(B-A)n wherein each A is independently a polymer block of an alkenyl aromatic hydrocarbon, the total A being at least 5 weight percent of the total weight of the polymer; wherein Y is the remnant of a multifunctional coupling agent; m is 0 or 1; n is an integer from 1 to 5, preferably 1 to 3, more preferably 1; and B comprises a polymer block of a conjugated diene. The polymer illustrated in US5500469 is an SIS (styrene-isoprene-styrene) block copolymer containing 18% styrene and 82% isoprene and having a weight average molecular weight of about 130,000. Unfortunately, this polymer does not provide the superior comfort known from WO2013025440. In other words, although this reference identified a broad range of multiblock copolymers as suitable, it did not disclose specific block copolymers with excellent comfort that can be used without vulcanizer and that does not suffer from ballooning when annealed.

[0009] In US 5563204 an aqueous dispersion is claimed which is capable of forming a free-standing, coherent, elastomeric, solid film which, after drying and annealing at 80 °C for 30 minutes, demonstrates a tensile strength of about 11.0 MPa or greater. It is suggested to use one or more block copolymer(s) corresponding to the formula A-B-Xm-(B-A)n, wherein each A polymer block consists essentially of a monovinylidene aromatic monomer, having a weight average molecular weight from about 8,000 to about 15,000 Daltons, each B polymer block consists essentially of a conjugated diene and, optionally, a monovinylidene aromatic monomer having a weight average molecular weight from about 30,000 to about 200,000 Daltons, X is the remnant of a multifunctional coupling agent, m is 0 or 1, and n is an integer from 1 to 5, [0010] In example 1 of this reference a film of an SIS block copolymer is prepared and the tensile strength at break is tested. In example 2 of this reference a radial block copolymer is used. There is no improvement when replacing a linear block copolymer by a radial block copolymer. Ballooning at this temperature does not occur and is not discussed. The latter is not surprising, as the annealing is carried out at a relatively low temperature; a temperature that is too low to provide sufficient strength when using styrenic block copolymers with relatively small endblocks.

[0011] It may therefore be concluded that the prior art broadly describes latices based on linear and branched block copolymers, but that there is no clear teaching how to prepare a vulcanizer-free latex with excellent comfort that can be annealed to provide sufficient strength without suffering from ballooning.

[0012] In US2005020773 Improved adhesives are provided through the use of styrenic radial block copolymers, containing at least 40 wt % diblock copolymers, the adhesives have improved adhesive properties and a reduced elastic behaviour under die-cutting conditions. No latices are disclosed.

[0013] The inventor set out to find a styrenic block copolymer and a latex comprising water and said styrenic block copolymer that may be used without vulcanizer, and that combines superior comfort, softness and strength without suffering from ballooning.

Summary of invention [0014] Accordingly the invention provides a new radial styrenic block copolymer as defined in claim 1 and an improved latex comprising said block copolymer(s) as defined in claim 10. Moreover, it provides a process for preparing dipped goods that includes an annealing step. Finally, it provides dipped goods as defined in claim 14, that exhibit superior comfort, softness and strength, without use of vulcanizers and/or accelerators and without suffering from ballooning.

Brief description of drawings [0015] The photo in Figure 1 illustrates surgical gloves made from latices that are annealed at a temperature of 120 °C. The middle glove is made from the linear block copolymer of WO2013025440. The glove provides the expected comfort. Flowever, it suffers from excessive ballooning. The surgical gloves in Figure 2 are made in accordance with the present invention. No ballooning occurs.

Description of embodiments [0016] The synthesis of styrenic block copolymers is known since the early 60’ s of the last century. An early example is US 3149182 .

[0017] The first step of the synthesis involves contacting styrene or a similar alkenyl aromatic hydrocarbon and an initiator, typically an organomonolithium compound in the presence of an inert diluent thereby forming a living polymer compound having the simplified structure A-Li. A is therefore composed for at least 90 mol% of an alkenyl aromatic hydrocarbon. The alkenyl aromatic hydrocarbon is preferably styrene. Other useful alkenyl aromatic hydrocarbons from which the A blocks may be formed include alphamethyl styrene, tertbutyl styrene, vinyl piperidine and other ring alkylated styrenes as well as mixtures of the same. Minor amounts of other anionically copolymerizable monomers may be included.

[0018] The inert diluent may be an aromatic or naphthenic hydrocarbon, e.g., benzene or cyclohexane, which may be modified by the presence of an alkene or alkane such as pentenes or pentanes. Specific examples of suitable diluents include n-pentane, n-hexane, isooctane, cyclohexane, toluene, benzene, xylene and the like.

[0019] The initiators that are reacted with the alkenyl aromatic hydrocarbon in step one of the synthesis are represented by the formula RLi; wherein R is an aliphatic, cycloaliphatic, or aromatic radical, or combinations thereof, preferably containing from 2 to 20 carbon atoms per molecule. Exemplary of these organomonolithium compounds are ethyllithium, n-propyllithium, isopropyllithium, n-butyllithium, sec-butyllithium, tert-octyllithium, n-decyllithium, n-eicosyllithium, phenyllithium, 2-naphthyllithium, 4-butylphenyllithium, 4-tolyllithium, 4-phenylbutyllithium, cyclohexyllithium, 3,5-di-n-hepthylcyclohexyllithium, 4 -cyclopentylbutyllithium, and the like. The alkyllithium compounds are preferred for employment according to this invention, especially those wherein the alkyl group contains from 3 to 10 carbon atoms. A much preferred initiator is sec-butyllithium. See US 3231635 . The concentration of the initiator can be regulated to control molecular weight. Generally, the initiator concentration is in the range of about 0.25 to 50 millimoles per 100 grams of monomer although both higher and lower initiator levels can be used if desired. The required initiator level frequently depends upon the solubility of the initiator in the hydrocarbon diluent. These polymerization reactions are usually carried out at a temperature in the range of -50 to +150 °C and at pressures which are sufficient to maintain the reaction mixture in the liquid phase.

[0020] Next, the living polymer in solution is contacted with a single conjugated diene or mixture of conjugated dienes, forming a polymer block B. B is therefore composed for at least 90 mol% of one or more conjugated dienes. Other copolymerizable monomers may be included. Preferred dienes include butadiene and isoprene. A much preferred diene is isoprene. Thus, preferably each polymer block B is composed for at least 90 mol% of isoprene. In a further preferred embodiment, the living polymer is first contacted with isoprene and last contacted with butadiene, whereby at least one butadiene unit is at the end of the living polymer. The resulting living polymer has a simplified structure A-B-Li. It is at this point that the living polymer may be coupled.

[0021] The radial styrenic block copolymer of the present invention has a relatively high degree of branching (DoB), being greater than 3. There are a wide variety of polyfunctional coupling agents with a functionality of 3 and greater that can be employed. Examples of the types of compounds which can be used include the polyepoxides, polyisocyanates, polyimines, polyaldehydes, polyketones, polyanhydrides, polyesters, polyhalides, and the like. These compounds can contain two or more types of functional groups such as the combination of epoxy and aldehyde groups, isocyanate and halide groups, and the like. Many suitable types of these polyfunctional compounds have been described in US 3595941, US 3468972, US 3135716, US 3078254 and US 3594452. A preferred coupling agent is gamma-glycidoxypropyltrimethoxysilane (GPTS).

[0022] Coupling efficiency (CE) 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. 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. In the present invention coupling efficiency is greater than 90%, preferably from 92% to almost 100%.

[0023] The typical coupling conditions include a temperature of between about 60 and about 80 °C, and sufficient pressure to maintain the reactants in a liquid phase.

[0024] Following the coupling reaction the product may be 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.

[0025] The block copolymers produced by the process of this invention will have a simple structure A-B-Y-(B-A)n wherein each A is independently a polymer block composed for at least 90 mol% of an alkenyl aromatic hydrocarbon; the content of A by weight of the total weight of the polymer (PSC) is in the range of 8-15 % ; Y is the remnant of a coupling agent having a functionality greater than 2; the degree of branching (DoB) is n+1, wherein n is an integer from 2 to 5, preferably 2 to 4; each B is independently a polymer block composed for at least 90 mol% of one or more conjugated dienes; the styrenic block copolymer has a coupling efficiency (CE) of at least 90%;

each A block independently has a weight average molecular weight (MW A) ranging from 9,000 to 15,000, and

each B Block independently has a weight average molecular weight (MW B) ranging from 75,000 to 150,000.

[0026] The radial styrenic block copolymer may comprise a small amount of uncoupled block copolymer. The uncoupled polymer has the AB structure. As indicated, the A block is a block mainly composed of polymerized alkenyl aromatic hydrocarbon and the B block is a block is mainly composed of polymerized conjugated diene or dienes. For the purposes of the present invention, the expression mainly indicates that no more than 10 mole%, preferably less than 5 mole% of copolymerizable monomers may be present.

[0027] The average molecular weights of each of the blocks is important. Polymers having relatively large blocks A will give gloves that are strong, even without vulcanization, but relatively inflexible. The comfort of such gloves will be inferior to that of NR gloves. Polymers having relatively small blocks will be inferior in terms of strength and protection. This is particularly important in the absence of vulcanizers.

[0028] The blocks A preferably have average molecular weights between about 10,000 and about 12,000. The blocks B preferably have average molecular weights between about 80,000 and about 120,000. The average molecular weights of the alkenyl aromatic hydrocarbon polymer end blocks are determined by gel permeation chromotography, whereas the alkenyl aromatic hydrocarbon polymer content of the block copolymer is measured by infrared spectroscopy of the finished block polymer. The weight percentage of the A blocks in the finished block polymer should be between 8 and 15%, preferably 10% and 12% by weight.

[0029] As indicated above, the present invention also provides a latex comprising water and the new radial styrenic block copolymer (s). The latex should contain little or no vulcanizers and/or accelerators. However, it may comprise various other additives such as oils, co-solvents, waxes, colorants, tackifiers, fillers, release agents, anti-blocking agents and other conventional additives.

[0030] For the preparation of the synthetic latex anionic, cationic or non-ionic surfactants or combinations thereof may be used. The surfactant is present in a sufficient amount to emulsify the styrenic block copolymer (or copolymers if a combination of block copolymers is used). To produce a synthetic latex, the styrenic block copolymer, usually in the form of a solution in an organic solvent (also referred to as a cement), is dispersed in water using a suitable surfactant or a combination of surfactants and the organic solvent is removed. A suitable procedure is disclosed in, e.g., US 3238173 .

[0031] For the preparation of thin walled rubber articles preferably a synthetic latex is used having a solids content of from 20 to 80%, more preferably of from 25 to 70% by weight. Most preferably the synthetic latex has a solids content of from 30 to 65% by weight.

[0032] The present invention also specifically provides for dipped goods that have been obtained by the process described above. Such goods are thin walled rubber articles such as gloves, catheters or condoms.

[0033] To prepare a thin walled rubber article from the latex, such as a film, a suitable surface is coated with the latex and the water thereafter removed by evaporation. A second or further layer may be provided in the same manner to achieve thicker films. The film resulting from the foregoing procedure is dried by any suitable technique. Heating is typically used, with preferred temperatures for drying and subsequent annealing varying from 25 to 130 °C. In the current invention, the annealing temperature is preferably within the range of 100-130 °C, more preferably about 120 °C.

[0034] To prepare a dipped article, a similar process is used, wherein a mould is dipped into the latex, in a preferred embodiment of the process for making a thin walled article, the mould is dipped into the latex. The dip-coated mould is then removed from the latex and dried. The mould may be dip coated more than once in the same latex. In an alternative process a mould is dip-coated in a first latex, followed by (air) drying and dip-coating in a second latex and so forth. In this way balloons, and condoms may be made. In a different embodiment, the mould may be dipped in a dispersion of a coagulant, the coagulant on the surface of the mould may be dried, and subsequently, the mould is dipped into the rubber latex. The latter manner is especially used for the manufacture of gloves.

Example [0035] Additional features and advantages of the present invention are described in the following examples.

Test methods: [0036] Molecular weights were determined by GPC (Gel Permeation Chromatography) using a calibration curve based on mono-dispersed polystyrene standards such as is done according to ASTM 3536. The molecular weight of polymers measured using GPC so calibrated are styrene equivalent molecular weights. The styrene equivalent molecular weight may be converted to true molecular weight when the styrene content of the polymer and the vinyl content of the diene segments are known. The detector used is preferably a combination ultraviolet and refractive index detector.

[0037] Tests for physical properties were performed using ASTM D412 (92), die C. All tests were performed on an Instron 4465 tensile machine. Since the Young's modulus (at 0% elongation) of the very soft and flexible materials that were obtained in the experiments appeared very difficult to measure, the modulus of the synthetic latices at low elongation (between 5 and 15 mm) was measured and the result was called "10% Young's modulus".

[0038] Complex modulus was determined by performing Dynamic Mechanical measurement according to ISO 6721-1 1994. All tests were performed on a Rheometrics Spectrometer series II.

Example 1 [0039] Polymerization of polymer according to the invention was performed in a 40 liter stirred stainless steel reactor. 19.5 kg dry cyclohexane was transferred into the reactor and heated to 50° C. 76 ml of a 0.44M s-butyllithium solution was added. 300 g of styrene was added to the reactor and after 1 hour 2400 g of isoprene was slowly added (100 g/min) and the temperature was maintained at 60°C. 45 minutes after the isoprene addition the temperature was increased to 70° C and 2.4 ml of gamma-glycidoxypropyltrimethoxysilane was added. After 30 minutes 2 ml methanol was added to terminate the reaction.

[0040] Results:

Block A MW: 12,000;

Block B MW: 92,000; PSC: 11%;

DoB: 3.0, and CE: 94%

Example 2 [0041] A series of latices were formed from various linear and radial poly(styrene-b-isoprene-b-styrene) block copolymers A to J. The block copolymers are described in the Tables 1 and 2 below. “ MW A” in Table 1 refers to the polystyrene block that is formed first. This is the weight average molecular weight. MW B refers to the polyisoprene block that is formed thereafter, typically it is calculated by dividing the molecular weight of the finished block copolymer by the average degree of branching (DoB), and subtracting MW A. (living) poly(styrene-b-isoprene) polymers before coupling. PSC refers to the content by weight of the A blocks. CE refers to the coupling efficiency, where f.s. refers to full sequential: a block copolymer that is made without coupling and with a theoretical CE of 100% (MW B in Table 1 for full sequential polymers is calculated by using a fictive DoB of 2).

[0042]

Table 1

[0043]

Table 2

[0044] The radial block copolymer according to the invention, is polymer H. Polymer A is similar to the polymer of US 5500469. Polymer B is the commercial polymer, Kraton® D1161). Polymers C and D were made with methyltrimethoxysilane. Polymer E is similar to the polymer of WO 2013/025440. Polymers G and I were made with GPTS. Polymer J is similar to the polymer of US 2005/020773, made with bistrimethoxysilylethane. Other comparative examples were included to show the effect of branching, coupling efficiency, polystyrene content, and size of the A blocks.

[0045] The latices contained 30 % by weight of the block copolymer. No vulcanizers or accelerators were added. Other components included an anionic surfactant and an anti-oxidant. Test specimens were prepared by first dipping stainless steel plates in a coagulant solution and, after drying, in the polymer latex. The objective was to form a uniform layer of the latex as it precipitated onto the plates. The films were annealed in an oven at about 120 °C for 15 minutes.

[0046] The films were then tested on tensile strength, softness and ballooning. The results are described in the Tables 3 and 4 below. “ TS” refers to tensile strength (MPa). When greater than 20 MPa this is considered good(+). “ 10% Y” refers to the 10% Young’ s modulus (MPa). This parameter is a measure for softness. When smaller than 0.25 MPa this is considered good (+). Ballooning is inspected visually . When no deformities and/or loss of dimensional stability are seen this is considered good (+). “ C. Mod.” refers to complex modulus (Pas) as described in ASTM D4092-07 A complex modulus at 120°C of 2 x 105 Pas or higher results in no ballooning and is considered good (+).

[0047]

Table 3

[0048]

Table 4

Conclusions [0049] As is clear from the above results, having a balance of strength, softness, comfort, lack of ballooning and without the presence of vulcanizers/accelerators is hard to achieve. Surprisingly, block copolymers within a very narrowly defined range in terms of branching, coupling efficiency, polystyrene content and molecular weight exist that excel in these properties.

Clauses 1. A radial styrenic block copolymer of the general formula: A-B-Y-(B-A)n wherein - each A is independently a polymer block composed for at least 90 mol% of an alkenyl aromatic hydrocarbon; - the content of A by weight of the total weight of the polymer (PSC) is in the range of 8-15 % ; - Y is the remnant of a coupling agent having a functionality greater than 2; - the degree of branching (DoB) is n+1, wherein n is an integer from 2 to 5, preferably 2 to 4; - each B is independently a polymer block composed for at least 90 mol% of one or more conjugated dienes; - the styrenic block copolymer has a coupling efficiency (CE) of at least 90%; - each A block independently has a weight average molecular weight (MW A) ranging from 9,000 to 15,000, and - each B Block independently has a weight average molecular weight (MW B) ranging from 75,000 to 150,000. 2. The radial styrenic block copolymer of claim 1, wherein each B is a polymer block composed for at least 90 mol% of isoprene. 3. The radial styrenic block copolymer of claim 2, wherein at least one B comprises at most 10 mol% butadiene with at least 1 butadiene unit directly connected to the remnant of the coupling agent Y. 4. The radial styrenic block copolymer of claim 1 to 3, wherein each A is a polymer block composed for at least 90 mol% of styrene. 5. The radial styrenic block copolymer of any one of claims 1 to 4, wherein Y is the remnant of gamma-glycidoxypropyltrimethoxysilane. 6. The radial styrenic block copolymer of any one of claims 1 to 5, wherein the styrenic block copolymer has a coupling efficiency in the range of 92 to about 100%. 7. The radial styrenic block copolymer of any one of claims 1 to 6, wherein the total A is in the range of 9-12 % by weight of the total weight of the polymer. 8. The radial styrenic block copolymer of any one of claims 1 to 7, wherein each A block independently has a weight average molecular weight ranging from 10.000 to 12.000. 9. The radial styrenic block copolymer of any one of claims 1 to 8, wherein each B block independently has a weight average molecular weight ranging from 80.000 to 120.000. 10. An artificial latex comprising water and one or more styrenic block copolymers as defined in any one of claims 1-9 dispersed in said water in an amount of 20 to 80 % by weight of the combination of water and styrenic block copolymer and further comprising 0 to 0.2 parts by weight per hundred parts by weight of the combination of water and styrenic block copolymer of a vulcanizer and/or an accelerator. 11. The artificial latex of claim 10, comprising said one or more styrenic block copolymers in an amount of 50 to 70, preferably of 55 to 65 % by weight of the combination of water and styrenic block copolymer. 12. A process for preparing articles by coagulation dipping from the artificial latex according to any one of claims 10 to 11, wherein a film is made from the latex and said film is allowed to dry and wherein said film is annealed for at least 10 minutes at an annealing temperature within the range of 100-130 °C. 13. The process of claim 12, wherein said film is annealed at about 120 °C. 14. Dipped goods comprising a film composed of the radial styrenic block copolymer of any one of claims 1 to 9, and 0 to 0.2 parts by weight per 100 parts by weight of the styrenic block copolymer of remnants of a vulcanizer and/or an accelerator.

Claims

A radial styrene-containing block copolymer of the general formula: A-B-Y- (B-A) n wherein - each A is independently a polymer block consisting of at least 90 mole% of an alkenyl aromatic hydrocarbon; - the content of A by weight relative to the total weight of the polymer (PSC) is in the range of 8-15%; - Y is the remainder of a coupling agent with a functionality greater than 2; - the degree of branching (DoB) is n + 1, wherein n is an integer from 2-5, preferably from 2-4; - each B is independently a polymer block consisting of at least 90 mol% of one or more conjugated dienes; - The styrene-containing block copolymer has a coupling efficiency (CE) of at least 90%; - Each block A independently has a weight average molecular weight (MW A) in the range of 9,000 to 15,000, and - Each block B independently has a weight average molecular weight (MW B) in the range of 75,000 to 150,000.

The radial styrene-containing block copolymer according to claim 1, wherein each B is a polymer block consisting of at least 90 mol% isoprene.

The radial styrene-containing block copolymer according to claim 2, wherein at least one B contains at most 10 mol% butadiene with at least 1 butadiene unit directly connected to the remainder of the coupling agent Y.

The radial styrene-containing block copolymer according to claims 1 to 3, wherein each A is a polymer block consisting of at least 90 mole% styrene.

The radial styrene-containing block copolymer according to any of claims 1 to 4, wherein Y is the remainder of gamma-glycidoxypropyl trimethoxysilane.

The radial styrene-containing block copolymer according to any of claims 1 to 5, wherein the styrene-containing block copolymer has a coupling efficiency in the range of 92 to about 100%.

The radial styrene-containing block copolymer according to any of claims 1 to 6, wherein the total A is in the range of 9-12% of the weight relative to the total weight of the polymer.

The radial styrene-containing block copolymer according to any of claims 1-7, wherein each block A independently has a weight average molecular weight in the range of 10,000-12,000.

The radial styrene-containing block copolymer according to any of claims 1-8, wherein each block B independently has a weight-average molecular weight in the range of 80,000-120,000.

An artificial latex comprising water and one or more styrene-containing block copolymers as defined in any one of claims 1-9 dispersed in said water in an amount of 20 to 80% by weight of the combination of water and the styrene-containing block copolymer and further 0 to 0.2 parts by weight of a vulcanizing agent and / or an accelerator per hundred parts by weight of the combination of water and styrene-containing block copolymer.

The artificial latex according to claim 10, comprising said one or more styrene-containing block copolymers in an amount of 50 to 70, preferably 55-65% by weight of the combination of water and styrene-containing block copolymer.

A method of preparing articles by dipping and coagulating the artificial latex according to any of claims 10-11, wherein a film is made from the latex and the film can dry and wherein said film undergoes heat treatment for at least 10 minutes at a temperature in the range of 100-130 ° C.

The method of claim 12, wherein said film undergoes heat treatment at about 120 ° C.

Dipped goods comprising a film consisting of a radial styrene-containing block copolymer according to any of claims 1-9, and 0 to 0.2 parts by weight of residues of a vulcanizer and / or an accelerator per 100 parts by weight of the styrene-containing block copolymer.