BACKGROUND

The present invention is directed to a composition which can produce, inter alia, elastomeric microcellular foam, preferably polyurethane foam having improved and well-balanced mechanical properties. Polyurethane is a polymer composed of organic units joined by carbamate (urethane) links. Polyurethane is typically produced by the reaction of a polyisocyanate with a polyol. Polyurethanes are used in the manufacture of high-resilience foam seating, rigid foam insulation panels, micro- cellular foam seals and gaskets, durable elastomeric wheels and tires, automotive suspension bushings, electrical potting compounds, high performance adhesives, surface coatings and sur- face sealants, synthetic fibers, carpet underlay, hard-plastic parts, condoms, and hoses and so on.

For elastomeric microcellular foam, preferably polyurethane foam, usually, split tear is an important, yet difficult to improve property, especially under fixed foam density. Actions usually have been done on changing formulation substantially. However, in such cases, other physical properties are often compromised.

For example, in Journal of Cellular Plastics, 36, pp 286 (2000), Sawai et. al. has shown the relationship between stress F, proportional constant C, resin strength f cell diameter dand foam density p in the case of brittle transmission of crack for polyurethane foam:

According to the formula above, to increase the split tear, there are a few ways: 1_) to increase the resin strength for the resin without foaming, which is usually achieved by using polyester polyol instead of polyether polyol, however, the use of polyester polyol will lead to poor hydroly- sis resistance, reducing the life time of footwear foam; and 2) to increase density of foam, however, for a fixed shape/volume of midsole, this will lead to heavier finished product, which is unacceptable to the consumer; 3) to increase the cell diameter when the density and resin strength is fixed, however, it is impossible to increase cell diameter without influence on other properties negatively. In short, so far there is no effective way to increase the split tear and pre- serving the original mechanical properties at the same time. Therefore, there is a need to find a system so that good split tear could be achieved without compromising other physical properties. SUMMARY OF THE INVENTION

The present inventor has found that, using lactam as an additive, it is possible to significantly increase mechanical properties of elastomeric microcellular foam, preferably polyurethane foam, such as split tear, without substantially compromising other physical properties.

The present inventor has also found that the effect of lactam is more apparent with silicon oil present in the composition to produce the elastomeric microcellular foam, preferably polyurethane foam.

The present inventor has also found that the present invention is particularly useful when poly- tetrahydrofuran is present in the inventive composition to produce polyurethane foam, either as the sole polyol or as one of the polyols in the composition. DETAILED DESCRIPTIONS

The present invention discloses a composition to produce elastomeric microcellular foam, preferably polyurethane foam, which comprise: a polyisocyanate, a compound with at least two groups reactive toward isocyanates, preferably a polyol, so that the remaining substructure of the compound is connected with the polyisocyanate, a lactam, a surfactant, and a blowing agent.

POLYISOCYANATE. The polyisocyanates used in the present invention are those conventionally used in the preparation of polyurethane foams and can be either monomeric polyisocyanate or polyisocyanate prepolymer.

The monomeric polyisocyanates used in the present invention, preferably monomeric diisocyanate, can be exemplified by aromatic diisocyanates such as toluene diisocyanate (TDI) and/or methylene diphenyl diisocyanate (MDI). Aliphatic and/or cycloaliphatic isocyanates, such as 1 ,6- hexamethylene diisocyanate (HDI), 1 -isocyanato-3-isocyanato-methyl-3,5,5-trimethyl- cyclohexane (isophorone diisocyanate, IPDI), and/or 4,4'-diisocyanato dicyclohexylmethane (H12MDI or hydrogenated MDI) can also be used. It is also possible to use mixtures of the polyisocyanates. The polyisocyanate prepolymer can be obtainable by reacting an excess of isocyanates with one or more compounds having at least two groups reactive toward isocyanates, preferably hydroxyl groups and/or amino groups, at temperatures of for example 30 to 100°C. The NCO content of polyisocyanate prepolymers of the invention is preferably from 10 to 33% by weight in polyisocyanates. Note that the compound having at least two groups reactive toward isocyana- tes used in the formation of the polyisocyanate prepolymer can be the same or different from the compound having at least two groups reactive toward isocyanates in the formation of the elastomeric microcellular foam, preferably polyurethane foam.

The compound with at least two groups reactive toward isocyanates, so that the remaining substructure of the compound is connected with the polyisocyanates. The compound is preferably polyol.

POLYOL. The polyols used in the present invention are those conventionally used in the preparation of polyurethane foams. The most commonly used polyols are those referred to as po- lyether polyols and/or polyester polyols. However, the polyol used in the composition of the present invention can be replaced by any compounds having at least two groups reactive toward isocyanates, such as -OH, -SH, -IMH2, -COOH, and -CH2-acidic groups, although the reaction products with said polyisocyanates are no longer what is typically referred to as polyurethane. For example, when the polyol is replaced with a compound with two -IMH2 groups, polyurea is obtained. The acidic groups of -CH2-acidic groups could be used common acidic groups, such as -H2PO4, -HCO3, and/or -COOH. The implementation of the present invention using such compound in the place of polyols can be envisioned by those skilled in the art.

The polyether polyols used in the inventive composition can be obtained by known processes, for example via anionic or cationic polymerization of alkylene oxides with the addition of at least one starter molecule comprising from 2 to 8, preferably from 2 to 6, and particularly preferably from 2 to 4, reactive hydrogen atoms, in the presence of a catalyst. The catalyst to produce polyether polyol can be, in the case of anionic polymerization, alkali metal hydroxides, such as sodium hydroxide or potassium hydroxide, or alkali metal alcoholates, such as sodium methoxi- de, sodium ethoxide, potassium ethoxide, and/or potassium isopropoxide, or, in the case of ca- tionic polymerization, Lewis acids, such as antimony pentachloride, boron trifluoride etherate, and/or bleaching earth. Other catalysts that can be used are double-metal cyanide compounds, known as DMC catalysts. The alkylene oxides used preferably comprise one or more compounds having from 2 to 4 carbon atoms in the alkylene moiety, e.g. tetrahydrofuran, ethylene oxide, propylene 1 ,2-oxide, butylene 1 ,2-oxide or butylene 2,3-oxide, in each case alone or in the form of a mixture, and preferably propylene 1 ,2-oxide and/or ethylene oxide, in particular propylene 1 ,2-oxide. Examples of starter molecules that can be used are ethylene glycol, diet- hylene glycol, glycerol, trimethylolpropane, pentaerythritol and/or sugar derivatives, such as sucrose, hexitol derivatives, such as sorbitol, methylamine, ethylamine, isopropylamine, butyla- mine, benzylamine, aniline, toluidine, toluenediamine, naphthylamine, ethylenediamine, diethyl- enetriamine, 4,4'-methylenedianiline, 1 ,3-propanediamine, 1 ,6-hexanediamine, ethanolamine, diethanolamine, triethanolamine, and also other di- or polyhydric alcohols, or di- or polybasic amines.

Polyester polyols used in the inventive composition can be obtained by known processes, for example by the polycondensation of multifunctional carboxylic acids and polyols, such as adipic acid and 1 ,4-butanediol. The polyester polyols used are preferably produced via condensation of polyhydric alcohols having from 2 to 12 carbon atoms, e.g. ethylene glycol, diethylene glycol, butanediol, trimethylolpropane, glycerol, or pentaerythritol, with polybasic carboxylic acids having from 2 to 12 carbon atoms, e.g. succinic acid, glutaric acid, adipic acid, suberic acid, azel- aic acid, sebacic acid, decanedicarboxylic acid, maleic acid, fumaric acid, phthalic acid, isoph- thalic acid, terephthalic acid, and the isomers of naphthalenedicarboxylic acids, or their anhydrides.

It is also possible to use mixtures of the polyether polyols and/or polyester polyols, even mixture of one or more polyether polyols and one or more polyester polyols, of course.

The level of the polyol in the present invention could be chosen from the conventional level of elastomeric microcellular polyurethane foam, preferably is 71 -99.7% by weight, more preferably is 80-98% by weight, based on the total weight of component A. POLYTETRAHYDROFURAN POLYOL. In a preferred embodiment, the polyol at least comprises polytetrahydrofuran. In other words, said polytetrahydrofuran can be either the sole polyol in the inventive composition, or as one of the polyols in the inventive composition. The polytetrahydrofuran polyols of the present invention are those conventionally used in the preparation of polyurethane foams and are preferably those with average Mn of 140 to 3500, more preferably 650 to 2000.

SURFACTANT. The composition of the present invention may also comprise surfactant, such as polydimethylsiloxane-polyoxyalkylene block copolymers, silicon oils, nonylphenol ethoxyla- tes, and other organic compounds. Surfactant are applied in the foaming system to regulate the sell structure and/or stabilize the foam, it also can be termed as stabilizer in some other occasion. SILICON OIL. In a preferred embodiment, the inventive composition comprises silicon oil as surfactant. Said silicon oil is preferably polysiloxane and polyether-polydimethylsiloxane copolymer, more preferably polyether-polydimethyl siloxane copolymer. Silicon oil can be either one specific kind of silicon oil or mixture thereof. It is possible to use additional surfactant other then said silicon oil.

The level of the silicon oil can be either that commonly used in the art; however, it is also possible to add additional silicon oils to the inventive composition so that the level of silicon oil is made higher. Specifically, the level of silicon oil can be 0.1 -4%, preferably 0.5-4%, more preferably 0.5-2%, most preferably 0.5-1 %, or 1 -2% by weight, based on the total weight of component A (see below for the definition of components A and B).

The silicon oil used in the present invention can be either the silicon oil used as surfactant in the art; however, it is also possible to be added as an additional or alternative ingredient separately.

OTHER INGREDIENTS. Other known, conventional ingredients, many of them optional, can be used in the inventive composition to produce polyurethane foam. Typical examples are catalysts, blowing agents, chain extenders and crosslinkers.

CATALYST. The composition of the present invention may comprise catalysts to accelerate various reactions. Factors affecting catalyst selection include balancing three reactions: uretha- ne (polyol+isocyanate, or gel) formation, the urea (water+isocyanate, or "blow") formation, or the isocyanate trimerization reaction (e.g., using potassium acetate, to form isocyanurate rings). Well known polyurethane catalysts include tertiary amine, alkyl tin carboxylates, oxides and mercaptides oxides and amines.

BLOWING AGENT. In order to produce polyurethane forms, a blowing agent which produced gas during the polymerization of the urethane is added to the composition of the present inven- tion. The normally used blowing agent is physical blowing agents which has low melting point and transform from liquid to gas when temperature increased during reaction, such as HFO (hydrofluoronated olefins), and/or chemical blowing agents which produce gas via reacting with isocyanate groups, such as water. CHAIN EXTENDER AND CROSSLINKER. The composition of the present invention may also comprise chain extenders and crosslinkers such as ethylene glycol, 1 ,4-butanediol (1 ,4-BDO or BDO), 1 ,6-hexanediol, cyclohexane dimethanol and hydroquinone bis(2-hydroxyethyl) ether (HQEE), alkyl tin carboxylates, triethylenediamine (TEDA, or DABCO, 1 ,4- diazabicyclo[2.2.2]octane), dimethylcyclohexylamine (DMCHA), and dimethylethanolamine (DMEA), and dibutyltin dilaurate.

The level of the catalyst, the blowing agent, the chain extender and the crosslinker could be chosen from the conventional level of elastomeric microcellular foam, preferably is 0.1 -10% by weight, more preferably is 3-7% by weight, based on the total weight of component A. LACTAM. The present inventor has found that, using lactam as an additive, it is possible to significantly increase mechanical properties such as split tear, without compromising other physical properties.

Lactam of the present invntion can be the compound of the following formula:

wherein X is a CH group, R is an hydrogen, m is an integer of 0 or an integer of 1 , 2, 3, 4, 5, 6, 7, 8 or 9, or

X is a nitrogen atom, R is a C1 to C18 alkyl group, a C7 to C15 aralkyl group or a pyridine group, which is optionally substituted with C1 to C6 alkyl groups, m is 3.

Lactam that can be used in the present invention includes butyrolactam, valerolactam, caprolactam, 1 -N-Methyl-hexyhydro-1 ,4-diazapinon-(3), 1 -N-Ethyl-hexahydro-1 ,4-diazepinon-(3), 1 -N- Propyl-hexahydro-1 ,4-diazepinon-(3). Preferred lactam is ε-caprolactam. The level of lactam in the composition is 0.1 to 15%, preferably 0.2 to 5% by weight based on the total weight of component A (see below for the definition of components A and B).

Lactam used in the present invention can be obtained commercially. For example, ε- caprolactam. is available from BASF or Ningbo Huajia Chemical Co. Ltd. as chemical reagents.

In a preferred embodiment, lactam and said surfactant, preferably silicon oil can be used in combination. The level of the lactam in the present invention is preferable 0.1 -15% by weight, more preferable is 0.5-5.5% by weight, based on the total weight of component A.

FORMULA. Each of the ingredients in the composition of the present invention, particularly lactam, silicon oil and polytetrahydrofuran, can be one specific compound, or a blend of more than one compounds.

Respective chemicals are available commercially. For example, silicon oil is available from Air Product or DEGUSSA GOLDSCHMIDT as Dabco series or Tegostab series. Polytetrahydro- furan is available from BASF, Mitsubishi Group under the trade name Polytetrahydrofuran 2000, PTMEG 2000.

In the production of the elastomeric microcellular foam, preferably polyurethane foam of the present invention, the full formula of the composition in the present invention is used as two components, namely components A and B, wherein component A comprises the compound with at least two groups reactive toward isocyanates, preferably a polyol, the lactam, the surfactant, the blowing agent and other optional additives such as chain extender, catalysts, i.e. component A comprises all the ingredients in the composition except polyisocyanates. While component B is polyisocyanate, unless specified otherwise. The two components are prepared in advance and mixed together to produce the polyurethane foam of the present invention. An isocyanate index, in short "index", which is a measure for the excess isocyanate used relative to the theoretical amount, is required. The index can be calculated as the molar ratio of isocyanate group in component B to the groups reactive toward isocyanates in component A (in the case of polyol, hydroxyl group) multiplied by 100.

A typical formula of the inventive composition and ranges of the respective ingredients are listed below. It is apparent that those skilled in the art can fine-tune the exact level of ingredients as needed, as long as there is no significant negative impact made to the properties of the product. The levels are based on the weight of the component in which it is added to the composition of the present invention. Note that the weight of 1 part by weight of component A is not necessaries the same as that of 1 part by weight of component B. All the ingredients in components A and B should add up to 100 parts, respectively. Component Ingredient Broadest range Preferred range A B (parts by wt) (parts by wt)

A Polyol 71 -99.7 80-98

A Lactam 0.1 -15 0.5-5.5

A Surfactant 0.1 -4 0.5-1 .6

A Additives (catalyst, chain extender, 0.1 -10 3-7

crosslinker, blowing agent, etc.)

B Polyisocyanate 100 100

The present invention is further directed to a process to produce an elastomeric microcellular foam, preferably polyurethane foam, from the inventive composition. The production process per se can be known, wherein premixed component A comprising the compound with at least two groups reactive toward isocyanates, preferably polyol, the surfactant, the blowing agent and other optional additives, and component B comprising isocyanate, at a certain index, are injected into a mold where the two components are mixed and reacts into an elastomeric microcellular foam, preferably polyurethane foam. The mold could be either at room temperature or preheated. The index can be optimized to achieve better properties.

According to the present invention, split tear of microcellular foam polyurethane can be increased significant by adding a minor amount of lactam, and other physical properties have not been compromised. Furthermore, according to the present invention, an even better performance can be achieved using the combination of lactam and silicon oil. In other words, in the inventive formula, lactam and silicon oil produces a synergistic effect leading to better performance. As the amounts of lactam and silicon oil are small, the cost for such advantage is insignificant. The advantage of the present invention can be demonstrated using polyether polyol, such as polytetrahydrofuran.

The present invention also provides flexibilities in the optimization of index. For those formulas with polytetrahydrofuran as the sole polyol or at least of one type of polyol (wherein more than one type of polyol is used in the formula), it is usually difficult to optimize the index to a value close to 100. Such index is less preferred as it means there will be unreacted isocyanate group or the functional group used to react with the isocyanate group in the foam produced. It was found that the index value can be easily tuned to a value closer to 100 in the presence of lactam, preferably ε-caprolactam.

The present invention also provides flexibilities to improve the mechanical strength of po- lyurethane microcellular foam material in which polytetrahydrofuran or polytetrahydrofuran hybrid with polyether polyol/polyester polyol plays as the polyol of target polyurethane system. This enables the obtainment of a flexible formula of the inventive composition.

INDUSTRIAL APPLICATION

Potential applications of the invention include but are not limited to footwear foam, synthetic leather, and other elastomeric foam applications

EXAMPLES

MEASUREMENT OF PHYSICAL PROPERTIES. Split tear is measured according to SATRA TM65, which is a test used to assess the split tear strength of cellular materials. When conducting a test, rectangular specimens are split for part of their length, parallel to the top and bottom faces and through mid-thickness. This produces two tongues which are clamped into the jaws of the tensile tester. During the test, the jaws are separated at a specified rate and the maximum force needed to propagate the split is recorded. The tests are conducted with sample thickness of 10 mm.

Free rise density is determined by placing the polyurethane foam-forming reaction mixture into a paper cup immediately before foaming, and, after fully foamed and cured, removing the foam outside the paper cup, weight the polyurethane foam in the paper cup, and dividing the weight of the polyurethane foam by the volume of cup.

Article density is the density of molded polyurethane foam plates/samples with over packing ratio above 1 .0.

Hardness (Asker C) is measurement according to ASTM D2240, with distance between the test point and the edge of the test specimen at least 13 mm, and the points are spaced at least 5 mm. The test was run on a HPE ll-Asker C electronic durometer. The test result is calculated by testing 5 point, then give a range as final result (such as: 50-56). Rebound is tested according to ASTM D2632, with the test specimen placed vertically. The downside of the test specimen was used. A GT-7042-v1 Vertical Rebound test machine was used. The test result was obtained by running the test for six times and recording the last three results.

FORMULA OF THE COMPOSITION. Materials used are listed below:

Polyol 1 Polytetrahydrofuran having an OH number of 56 mg KOH/g

Polyol 2 Polyether polyol based on glycerol, propylene oxide and ethylene oxide, having an OH number of 27 mg KOH/g and a viscosity of 1225 mPas at 25°C.

Polyol 3 Polyester polyol based adipic acid, monoethylene glycol and butanediol, having an OH number of 56 mg KOH/g.

Polyol 4 Polyether polyol based on propane-1 ,2-diol, propylene oxide and ethylene oxide, having an OH number of 29.5 mg KOH/g and a viscosity of 760 mPas at 25°C.

Polyol 5 Polyester polyol based adipic acid, monoethylene glycol and butanediol, having an OH number of 56 mg KOH/g and a viscosity of 625 mPas at 75°C.

Chain Exten1 ,4-butanediol

der 1

Chain ExtenMonoethylene glycol

der 2

Chain ExtenDiethyltoluenediamine

der 3

Crosslinker 1 Trifunctional crosslinker with an OH number of 1603 mg KOH/g.

Water Distilled water prepared in lab

Silicon oil 1 Polyether polydimethylsiloxane copolymer with Mn of 3.3x10 ³ from Evonik

Silicon oil 2 Mixture of octamethylcyclotetrasiloxane and poly-siloxane from Momentive

Silicon oil 3 Polysiloxane based silicone surfactant from Air Products

Caprolactam Organic compound with the formula (CH ₂ )5C(0)NH from BASF SE

Catalyst 1 Lupragen N203 ^® from BASF Polyurethanes

Catalyst 2 Delayed action catalyst based on 1 ,4-Diazabicyclo[2.2.2]octane (DABCO)

Catalyst 3 Catalyst based on 1 ,8- Diazabicyclo (5.4.0)undec-7-ene from Evonik

Catalyst 4 Catalyst based on bismuth

Isocyanate 1 4,4'-MDI

Isocyanate 2 4,4'-MDI and carbodiimide-modified 4,4'-MDI Isocyanate 3 Isocyanate prepolymer based on Isocyanate 1 , Isocyanate 2 with polyol 1 and an NCO content of 18%;

Isocyanate 4 Isocyanate prepolymer based on Isocyanate 1 , Isocyanate 2 with polyol 5 and an NCO content of 18%;

Isocyanate 5 Isocyanate prepolymer based on Isocyanate 2 with polyol 4 and an NCO content of 19%.

Isocyanates 3, 4 and 5 are prepolymers. Unlike monomeric Isocyanates 1 and 2 which can be used as received, prepolymers must be prepared in advance. To do so, a 2 L 4-neck flask equipped with a blade stirrer, a thermometer, nitrogen inlet means was initially charged with defined amount of monomeric isocyanates and was heated to 60°C. At 60°C, defined amount of monomeric polyol was added in 30 minutes under agitation. After all components had been added, the mixture was heated to a temperature of 80°C and stirred at 80°C for 2 hours followed by cooling down to room temperature and determination of the prepolymer's NCO value 24 hours later.

The respective amounts of monomeric polyisocyanates and polyols are listed below.

PROCESS TO PRODUCE POLYURETHANE FOAM. The full formula of the composition of the present invention is divided into two packages, packages A and B. Package B is made by weighting the specified amount of polyisocyanate in a glove box under dry nitrogen protection. Package A is made by weighting the specified amounts of all other ingredients and mixed at room temperature. The elastomeric microcellular polyurethane foam of the invention is prepared by either manual trial or machine trial.

In a manual trail, components A and B are manually mixed at a predefined index with a stirrer at room temperature, and then pour in to 50°C mold, followed by demolding after 7 minutes. In a machine trial, a Hai Feng or Green Machine device is used. Components A and B are preheated to defined temperatures, followed by injecting to 50°C mold, and demolding after 7 minutes. For a machine trial, optimized index (opt) is determined by a "drop test". The test consists of indenting a needle on the foam under a defined load at a particular time. The indentation is measured after a certain time (usually 15 seconds of indentation). It's necessary to vary the start time of indentation to see the maximum variation in deflection: It usually occurs 5-10 seconds after the pinch time. The pinch time (PT) is the time from start of pouring/injection of the material till the polyurethane foam gets cured developing sufficient strength. It is usually determined by pinching the foam by nails till the foam is strong enough to resist the peeling. It determines the state of curing of the foam. The pinch time is the indication of the demolding time. Higher the pinch time longer the demolding time and vice versa. The indentation is usually measured in mm on application of a defined load. The minimum indentation value gives the op- timum ratio thus the best foam.

EXAMPLE 1

This example shows the impact of lactam on properties of polyurethanes.

The example shows that the presence of caprolactam can significantly increases split tear without reducing hardness and rebound (which is a key property for polyurethane foam's application as shoe sole). EXAMPLE 2

This example shows the impact of silicon oil on properties of polyurethanes in the absence of lactam. Increasing amount of silicon oil is added in component A.

The experiment example shows that application of certain silicon oil can also slightly improve split tear without sacrificing other properties, such as hardness, high resilience. However, it can cause the increases of free rise density, which is not good for application as low density foam. Therefore, using silicon oil to increase split tear has to compromise the density. As stated in description section, using silicon oil to increase split tear will lead to heavier finished product, which is unacceptable to the consumer. EXAMPLE 3

This example shows the impact of the combination of lactams and silicon oil on properties of polyurethanes.

Polyurethane foam is produced in low pressure polyurethane casting machine. Experiment on injection machine shows the similar results. It can be seen that presence of the combination of caprolactam and silicon oil increases split tear significantly without reducing rebound. This demonstrates the synergistic effect between caprolactam and silicone oil without impact to free rise density of the polyurethane system. The test was repeated at higher silicon oil level.

^* Polyurethane foam is produced in low pressure polyurethane casting machine. Experiment on injection machine shows the similar results.

It can be seen that, under higher silicon oil level, split tear strength is even further improved without increasing free rise density or decreasing rebound significantly. This means that the synergistic effect is even higher under higher silicon oil level. This shows the possibility of achieving even better split tear at low free rise density. EXAMPLE 4

This example demonstrates the capability of improving mechanical properties of polyester polyol based polyurethane in the presence of lactams. The polyisocyanate in component B is an prepolymer of polyisocyanate and polyester polyol, with polyester polyol at 18 mol% base on the amount of polyisocyanate, calculated by the amount of hydroxyl groups and isocyanate groups. That is, the polyisocyanate prepolymer is prepared by reacting an excess of the isocya- nates with polyester polyols. In another experiment, a mixture of polyether polyol and polyester polyol is used in component A to demonstrate the impact of lactams on mechanical properties of hybrid A component systems. It can be seen that, when there is a mixture of polytetrahydrofuran and polyester polyol in the polyurethane structure, caprolactam is improving split tear without compromising rebound.

Formula (parts

4A 4B 4C 4D 4E 4G by wt)

Polyol 1 93.8 93.8 96.8 92.8 91.8 87.8

Polyol 3 5 5

Chain Exten¬

3 3

der 1

Crosslinker 1 0.3 0.3 0.3 0.3 0.3 0.3

Silicon oil 1 0.5 0.5 0.5 0.5 0.5 0.5

Catalyst 1 1 .2 1 .2 1 .2 1 .2 1 .2 1 .2

Water 1 .2 1 .2 1 .2 1 .2 1 .2 1 .2

Caprolactam 0 4 0 4 0 4

Temperature

of Components 30/25 30/25 30/25 30/25 30/25 30/25 A and B (°C)

Isocyanate Isocyanate Isocyanate Isocyanate Isocyanate Isocyanate Isocyanate

4 4 3 3 3 3

Index / / / / / /

Cream time (s) 14 9 16 10 16 1 1

Full rise time

63 58 73 70 78 54 (s)

Free density

155 132 196 158 192 152

(g/L)

Article density

300 301 300 300 300 300

(g/L)

Hardness (As-

42-45 45-45 45-47 45-47 50-50 50-51 ker C)

Rebound resi¬

51 48 64 61 64 60 lience (%)

Split tear

strength 1 .86 2.04 2.68 2.95 2.64 3.08

(N/mm)