Method of making hydroxyaryl-functionalized interpolymer by free radical initiated polymerization

Abstract

Radical polymerization techniques can be used to polymerize monomers that include a class of hydroxyaryl compounds so as to provide polymers that exhibit desirable properties including, but not limited to, reduced hysteresis. Compositions such as vulcanizates in which such polymers can be utilized and products such as tire components that incorporate and/or are manufactured from such compositions also are provided.

Claims

1. A method for providing an ethylenically unsaturated polymer that comprises multiple hydroxyaryl functional groups, said method comprising radically initiating polymerization of a plurality of monomers that comprises at least one polyene, at least one C.sub.8-C.sub.20 vinyl aromatic compound and at least one compound defined by general formula (I),
CH.sub.2CHR.sup.1(I) where R.sup.1 is an aryl group having from 2 to 5 OR substituents with R being a protecting group which is non-reactive during said polymerization but which can be removed by a process that does not destroy or react with ethylenic unsaturation in said ethylenically unsaturated polymer, said polymer comprising from 1 to 12 B mer resulting from incorporation of said at least one compound defined by general formula (I), at least three of said B mer constituting a contiguous block, said at least one C.sub.8-C.sub.20 vinyl aromatic compound providing 20 to 50% of the constituent mer units of said polymer.

2. The method of claim 1 wherein said plurality of monomers comprises one or more types of dienes.

3. The method of claim 1 wherein said one or more types of dienes comprises at least one type of conjugated diene.

4. The method of claim 3 further comprising reacting said polymer with a heteroatom-containing compound so as to provide terminal functionalization to said polymer.

5. The method of claim 2 further comprising reacting said polymer with a heteroatom-containing compound so as to provide terminal functionalization to said polymer.

6. The method of claim 1 wherein the resulting polymer is substantially linear.

7. The method of claim 6 further comprising reacting said polymer with a heteroatom-containing compound so as to provide terminal functionalization to said polymer.

8. The method of claim 1 wherein said radically initiated polymerization employs a peroxide-based initiator.

9. The method of claim 1 wherein said radically initiated polymerization employs a radical initiator, chain transfer agent, emulsifier and, optionally, a stabilizer.

10. The method of claim 1 further comprising reacting said polymer with a heteroatom-containing compound so as to provide terminal functionalization to said polymer.

11. The method of claim 1 wherein said plurality of monomers are provided in an aqueous medium.

12. The method of claim 1 further comprising hydrolyzing each of said OR substituents so as to provide hydroxyl groups.

13. The method of claim 1 wherein said contiguous block is no more than six polymer chain atoms from a terminus of said ethylenically unsaturated polymer.

14. The method of claim 1 wherein said aryl group is a phenyl group.

15. The method of claim 14 wherein said phenyl group comprises OR substituents at its 3 and 4 ring positions.

16. The method of claim 1 wherein each R independently is a trialkylsiloxy, acetal, tert-butyl ether, or 2-methoxyethoxy ether group.

17. The method of claim 1 wherein mer from said at least one polyene and from said at least one C.sub.8-C.sub.20 vinyl aromatic mer are randomly distributed.

Description

DESCRIPTION OF ILLUSTRATIVE EMBODIMENTS

(1) As apparent from the foregoing Summary, the method can involve any of a variety of possible permutations or combinations thereof, and the resulting polymer can be characterized in a variety of ways. Generally, the polymer includes polyene mer and one or more of the aforedescribed B mer units. In at least certain embodiments, the polymer also can include directly bonded pendent aromatic groups.

(2) The following describes the production and use of a polymer that includes at least one B mer, i.e., a unit that includes a pendent aryl, preferably phenyl, group with at least one directly bonded hydroxyl and/or OR group. Where more than one B mer unit is present, they can be non-adjacent to each other or can constitute a block of the polymer. In some embodiments, a block of B units can be within ten, eight, six, four, or even two polymer chain atoms from a terminus of the polymer. In some of the described embodiments, the resulting polymer includes multiple A mer, i.e., alkene units (some or all of which can be derived from one or more types of dienes, particularly one or more types of conjugated dienes, e.g., 1,3-butadiene), and optionally multiple C mer, i.e., units that include a pendent aryl group, particularly a phenyl group. Each of the A, B and C mer can result from incorporation of ethylenically unsaturated monomers. In addition or alternatively, the polymer can include mer from other types of ethylenically unsaturated monomers such as vinyl aromatic monomers.

(3) The A mer typically result from incorporation of polyenes, particularly trienes (e.g., myrcene) and dienes, particularly C.sub.4-C.sub.12 dienes and even more particularly conjugated dienes such as 1,3-butadiene, 1,3-pentadiene, 1,3-hexadiene, 2,3-dimethyl-1,3-butadiene, 2-ethyl-1,3-butadiene, 2-methyl-1,3-pentadiene, 3-methyl-1,3-pentadiene, isoprene, 4-methyl-1,3-pentadiene, 2,4-hexadiene, and the like. Some or all of the A mer can be derived from one or more types of dienes, particularly one or more types of conjugated dienes, e.g., 1,3-butadiene. In some embodiments, essentially all (i.e., at least 95%) of the polyenes can be dienes, particularly conjugated dienes.

(4) Polyenes can incorporate into polymeric chains in more than one way. Especially for tire tread applications, controlling this manner of incorporation can be desirable, and techniques for achieving this control are discussed below. A polymer chain with an overall 1,2-microstructure, given as a numerical percentage based on total moles of polyene, of from about 8 to about 80%, optionally from about 15 to 65%, can be desirable for certain end use applications. A polymer that has an overall 1,2-microstructure of no more than about 50%, preferably no more than about 45%, more preferably no more than about 40%, even more preferably no more than about 35%, and most preferably no more than about 30%, based on total moles of polyene, is considered to be substantially linear.

(5) The polymer chain also can include pendent aromatic groups, which can be provided by C mer, particularly those derived from vinyl aromatics, particularly the C.sub.8-C.sub.20 vinyl aromatics such as, e.g., styrene, -methyl styrene, p-methyl styrene, the vinyl toluenes, and the vinyl naphthalenes. When used in conjunction with one or more polyenes, C mer can constitute from about 1 to about 70%, from about 10 to about 60%, or from about 20 to about 50% of the polymer chain; random microstructure can provide particular benefit in, for example, rubber compositions used in the manufacture of tire treads. Where a block interpolymer is desired, C units can constitute from about 1 to about 90%, generally from about 2 to about 80%, commonly from about 3 to about 75%, and typically about 5 to about 70% of the polymer chain.

(6) Exemplary interpolymers include those in which one or more conjugated dienes are used to provide the A units, i.e., polydienes; among these, 1,3-butadiene can be one of several or the only polydiene employed. Where C units are desired, they can be provided from styrene so as to provide, for example, SBR. In each of the foregoing types of exemplary interpolymers, one or more B units also are included.

(7) B units include a pendent aryl group which includes one or more directly bonded hydroxyl groups, preferably at least 2 hydroxyl groups. Because the H atoms of hydroxyl groups are active and can interfere with certain polymerization processes, the one or more B units can be provided from compounds that include R groups, i.e., groups that are non-reactive in the types of conditions utilized when polymerizing ethylenically unsaturated monomers but which later can be removed, typically by hydrolysis or similar reaction, so as to provide the desired hydroxyl groups. The particular type(s) of protecting group(s) employed should not interfere with the polymerization process, and the de-protection process employed to provide hydroxyl groups should not destroy or otherwise react with ethylenic unsaturation in the polymer resulting from the presence of A units. A non-limiting class of useful protecting groups is trialkylsiloxy groups, which can be provided by reacting hydroxyl groups with a trialkylsilyl halide. While the following examples employ Cert-butyldimethylsiloxyl groups, others such as acetal, tert-butyl ether, 2-methoxyethoxy ether, and the like also can be used.

(8) The number of hydroxyl and/or OR groups on the aryl, typically phenyl, group of each B unit need not be the same. Where the number is the same, the hydroxyl or OR groups need not be at the same position(s) on those rings. Using a phenyl group as a representative aryl group, relative to the point of attachment of the phenyl group to the polymer chain, a single hydroxyl or OR group can be located ortho, meta, or para on the phenyl ring, while multiple hydroxyl or OR groups can be provided 2,3-, 2,4-, 2,5-, 2,6-, 3,4-, 3,5-, 3,6-, 2,3,4-, 2,3,5-, etc., on the phenyl ring.

(9) B units typically are provided from vinyl aromatic compounds that include one or more hydroxyl and/or hydroxyl-producing groups directly attached to their aryl, typically phenyl, rings. Such compounds can be represented by the general formula
CH.sub.2CHR.sup.1(I)
where R.sup.1 is an aryl group, specifically a phenyl group or two or more fused aromatic rings, that includes n hydroxyl or OR groups with 1n5 and each R independently being the type of protecting group described above, (Although each R need not be identical, ease and simplicity typically result in a single type of R moiety being used in a given compound.) The hydroxyl or OR groups can be substituents of the same ring of R.sup.1 or can be substituents of different rings and, where R.sup.1 contains three or more hydroxyl or OR groups, two of them can be substituents of one ring with the other(s) being substituent(s) of other ring(s). In one embodiment, two hydroxyl or OR groups can be at the 3 and 4 positions of the same ring within the aryl group, preferably a phenyl group. Where R.sup.1 is other than a phenyl group and includes more than one hydroxyl OR group and where the hydroxyl or OR groups are on more than one ring, at least two of the hydroxyl or OR groups preferably are least somewhat proximate, i.e., directly bonded to ring C atoms that are separated by no more than 4, preferably 3, and even more preferably 2, other ring atoms.

(10) The number of B units typically is small relative to the number of other units; a relatively small number of B units has been found to provide a satisfactory level of desired properties, with further improvements in those properties not necessarily being proportional to the number of B units present. This relatively small number can be expressed in a number of ways. For example, the weight percentage of the final polymer attributable to B units commonly is less than 2%, more commonly from about 0.1 to about 1.5%, and typically from about 0.2 to about 1.0%. The percentage of B mer relative to the total number of mer in the polymer commonly is less than 1%, more commonly from about 0.01 to about 0.75%, and typically from about 0.05 to about 0.5%. The total number of B units in a given polymer generally is from 1 to several dozen, commonly from 1 to 12, more commonly from 1 to 10, and most commonly from 1 to 5.

(11) The B units can be separated from one another, or two or more B units can be contiguous along the polymer chain. (While the ordinarily skilled artisan understands how to synthesize random and block interpolymers, each is discussed in some detail below.) Further, the B units can incorporated near the beginning of the polymerization, near the end of the polymerization, or at any one or more intermediate points; in the first two of the foregoing possibilities, a B unit can be provided within 6 chain atoms of, within 2 units of, adjacent to a terminus of the polymer, or as a terminal unit, either alone or as part of a block.

(12) Based on the foregoing description of the relative amounts of B mer and C mer in the resulting interpolymers, the interpolymer can contain from about 99% to about 28% A met, from about 90% to about 38% A mer or from about 80% to about 48% A mer (for a random interpolymer) or about 99% to about 8% A mer, from about 98 to about 18% A mer, from about 97% to about 23% A mer or from about 95% to about 28% A mer (for a block interpolymer). The remainder of this description focuses on radical polymerization techniques for providing interpolymers of the type just described. The terms radical polymerization and free radical polymerization are used interchangeably herein.

(13) Under conventional radical polymerization conditions, emulsion or suspension polymerization can be conducted utilizing a polymerization initiator at a temperature ranging from 10 C. to 200 C., preferably from 0 C. to 100 C. Preferably the radical polymerization is an emulsion polymerization.

(14) The polymerization initiator used in the radical polymerization may be any of the conventional radical polymerization initiators which include, for example, organic peroxides such as benzoyl peroxide, lauryl peroxide, tert-butyl hydroperoxide, cumene hydroperoxide, p-methane hydroperoxide, di-tert-butyl peroxide, dicumyl peroxide and the like. Additionally, radical polymerization initiators can include peracids and esters thereof such as peracetic acid and potassium persulfate, peroxides such as lauryl peroxide and benzoyl peroxide, and azo compounds such as 2,2-azobisisobutyronitrile, and a mixture thereof. Any of these radical polymerization initiators may be used alone or in combination of two or more.

(15) Other types of living free radical polymerizations can provide a high degree of control over the composition, architecture, phase morphology and microstructure of polymers produced according to the disclosure. These types of free radical polymerizations are described in a variety of references, including U.S. Pat. No. 6,992,156 the disclosure of which is incorporated herein by reference. Such polymerizations include Atom Transfer Radical Polymerization (ATRP), Nitroxide Mediated Polymerization (NMP), Reversible Addition Fragmentation Transfer (RAFT), Degenerative Transfer (DT) as well as other polymerization reaction Stable Free Radicals (SFR). Due to the living nature of these types of radical polymerizations, additional or other further functionality can be incorporated into the resulting polymers.

(16) A chain transfer agent such as mercaptans including tert-dodecylmercaptan, n-dodecylmercaptan and the like, carbon tetrachloride, thioglycols, diterpene, terpinolene, .gamma.-terpinene and the like may also be used in combination.

(17) An emulsifier employed in an emulsion polymerization may, for example, be an anionic surfactant, a nonionic surfactant, a cationic surfactant as well as an amphoteric surfactant and the like. A fluorine-based surfactant may also be employed. Any of these emulsifiers may be used alone or in combination of two or more.

(18) A suspension stabilizer employed in a suspension polymerization may, for example, be polyvinyl alcohol, sodium polyacrylate, hydroxyethyl cellulose and the like. Any of these suspension stabilizers may be used alone or in combination of two or more.

(19) In an emulsion or a suspension polymerization, monomers, a radical polymerization initiator and the like may be charged all to the reaction vessel at once, or they may be added continuously or intermittently over the period of the reaction. The polymerization may be performed in an oxygen-free reaction vessel at 0 to 80 C. with changing temperature, stirring condition or the like as desired during the reaction. The polymerization may be of a continuous system or a batch system.

(20) Polymerization can be conducted at any of a wide range of pressures, although the polymerization typically is conducted under a pressure at which all of the monomers can be maintained in the liquid phase, Higher pressures can be utilized as needed or desired, typically by pressurizing the reactor with a gas that is inert to the polymerization reaction.

(21) The polymerization can be agitated, and the reaction allowed to proceed for a period of time sufficient to result in the formation of the desired polymer, usually from about 0.01 to about 48 hours, commonly from about 0.02 to about 36 hours, and typically from about 0.05 to about 24 hours.

(22) Where the B units are desired to be located preferentially at one or more points along the polymer chain, one or more compounds as represented by formula (I) can be staged so as to incorporate at the desired location(s). Where the other types of monomers are essentially depleted (i.e., polymerized), staged delivery of the formula (I)-type compounds can result in a block of B units which, if no additional monomers are charged to the polymerization vessel, can result in a terminal B block. Alternatively, the polymerization can be started with only formula (I)-type compounds present so as to form an initial block of B units followed by addition of other types of monomers designed to provide other types of units, either in a random or block manner.

(23) Polymers that include one or more B units, regardless of whether randomly distributed or provided as a block, may have improved cold flow properties relative to similar polymers not containing B units. The level of improvement may scale with the number of B units present, although the correlation is not necessarily linear and is impacted by the position (e.g., near a chain end versus mid-chain) and the proximity (e.g., random versus block) of the B units.

(24) After a desired degree of conversion has been reached, the resulting polymer latex can be stabilized, steam stripped to remove any unreacted monomer, coagulated using inorganic acid and chemical aids and washed and dried.

(25) Where such additional or other functionality is desired to enhance interaction with particulate filler, a living polymer can be further functionalized by reaction with an appropriate terminating reagent, coupling agent and/or linking agent. The ordinarily skilled artisan is familiar with numerous examples of terminal functionalities that can be provided through this type of post-polymerization functionalization. For additional details, the interested reader is directed to any of U.S. Pat. Nos. 4,015,061, 4,616,069, 4,935,471, 5,153,159, 5,149,457, 5,196,138, 5,329,005, 5,496,940, 5,502,131, 5,567,815, 5,610,227, 5,663,398, 5,786,441, 6,812,295, 7,153,919, etc., as well as references cited in these patents and later publications citing these patents; see also U.S. Patent Publ. Nos. 2007/0149744, 2007/0037956, 2007/0078232, 2008/0027171 and the like.

(26) Reaction of most types of functionalizing compounds with living polymers can be performed relatively quickly (a few minutes to a few hours) at moderate temperatures (e.g., 0 to 75 C.). Although not always necessary, quenching can be conducted by stirring the polymer and an active hydrogen-containing compound, such as an alcohol or acid, for up to about 120 minutes at temperatures of from about 25 to about 150 C.

(27) During polymerization and any optional post-polymerization functionalization, the anaerobic conditions typically present in the polymerization vessel are such that essentially all R moieties remain. Ensuring that most, if not all, of these are converted to hydrogen atoms typically is desirable to enhance interactivity between the functionalized polymer and particulate filler (when the polymer is used in filled compositions). While functionalizing reaction conditions (or the conditions involved in quenching and processing, described below) might be sufficient to hydrolyze some of the R.sup.2 groups, a separate hydrolysis reaction designed to ensure complete conversion to H atoms can be utilized. The ordinarily skilled artisan is aware of a variety of potentially useful hydrolyzing reactions, although one exemplary route is set forth below in the examples.

(28) During the foregoing processing and/or the compounding described below, some of the hydroxyl groups created by de-protection of the B units might undergo further reaction, e.g., with other functional groups present in the compound.

(29) Polymers made according to radical techniques generally have a number average molecular weight (M.sub.n) of up to about 1,000,000 Daltons. In certain embodiments, the M.sub.n can be as low as about 2000 Daltons; in these and/or other embodiments, the M.sub.n advantageously can be at least about 10,000 Daltons or can range from about 10,000 to about 500,000 Daltons or from about 20,000 to about 350,000 Daltons. Often, the M.sub.n is such that a polymer sample exhibits a gum Mooney viscosity (ML.sub.4/100 C.) of from about 2 to about 150, more commonly from about 2.5 to about 125, even more commonly from about 5 to about 100, and most commonly from about 10 to about 75.

(30) The resulting polymer can be utilized in a tread stock compound or can be blended with any conventionally employed tread stock rubber including natural rubber and/or non-functionalized synthetic rubbers such as, e.g., one or more of homo- and interpolymers that include just polyene-derived mer units (e.g., poly(butadiene), poly(isoprene), and copolymers incorporating butadiene, isoprene, and the like), SBR, butyl rubber, neoprene, EPR, EPDM, acrylonitrile/butadiene rubber (NBR), silicone rubber, fluoroelastomers, ethylene/acrylic rubber, EVA, epichlorohydrin rubbers, chlorinated polyethylene rubbers, chlorosulfonated polyethylene rubbers, hydrogenated nitrile rubber, tetrafluoroethylene/propylene rubber and the like. When a functionalized polymer(s) is blended with conventional rubber(s), the amounts can vary from about 5 to about 99% of the total rubber, with the conventional rubber(s) making up the balance of the total rubber. The minimum amount depends to a significant extent on the degree of hysteresis reduction desired.

(31) Amorphous silica (SiO.sub.2) can be utilized as a filler. Silicas are generally classified as wet-process, hydrated silicas because they are produced by a chemical reaction in water, from which they are precipitated as ultrafine, spherical particles. These primary particles strongly associate into aggregates, which in turn combine less strongly into agglomerates. Highly dispersible silica is any silica having a very substantial ability to de-agglomerate and to disperse in an elastomeric matrix, which can be observed by thin section microscopy.

(32) Surface area gives a reliable measure of the reinforcing character of different silicas; the Brunauer, Emmet and Teller (BET) method (described in J. Am. Chem. Soc., vol. 60, p. 309 et seq.) is a recognized method for determining surface area. BET surface area of silicas generally is less than 450 m.sup.2Jg, and useful ranges of surface include from about 32 to about 400 m.sup.2/g, about 100 to about 250 m.sup.2Jg, and about 150 to about 220 m.sup.2/g.

(33) The pH of the silica filler is generally from about 5 to about 7 or slightly over, preferably from about 5.5 to about 6.8.

(34) Some commercially available silicas which may be used include Hi-Sil 215, Hi-Sil 233, and Hi-Sil 190 (PPG Industries, Inc.; Pittsburgh, Pa.). Other suppliers of commercially available silica include Grace Davison (Baltimore, Md.), Degussa Corp. (Parsippany, N.J.), Rhodia Silica Systems (Cranbury, N.J.), and J. M. Huber Corp. (Edison, N.J.).

(35) Silica can be employed in the amount of about 1 to about 100 phr, preferably in an amount from about 5 to about 80 phr. The useful upper range is limited by the high viscosity that such fillers can impart.

(36) Other useful fillers include all forms of carbon black including, but not limited to, furnace black, channel blacks and lamp blacks. More specifically, examples of the carbon blacks include super abrasion furnace blacks, high abrasion furnace blacks, fast extrusion furnace blacks, fine furnace blacks, intermediate super abrasion furnace blacks, semi-reinforcing furnace blacks, medium processing channel blacks, hard processing channel blacks, conducting channel blacks, and acetylene blacks; mixtures of two or more of these can be used. Carbon blacks having a surface area (EMSA) of at least 20 m.sup.2/g, preferably at least about 35 m.sup.2Jg, are preferred; surface area values can be determined by ASTM D-1765 using the CTAB technique. The carbon blacks may be in pelletized form or an unpelletized flocculent mass, although unpelletized carbon black can be preferred for use in certain mixers.

(37) The amount of carbon black can be up to about 50 phr, with about 5 to about 40 phr being typical. When carbon black is used with silica, the amount of silica can be decreased to as low as about 1 phr; as the amount of silica decreases, lesser amounts of the processing aids, plus silane if any, can be employed.

(38) Elastomeric compounds typically are filled to a volume fraction, which is the total volume of filler(s) added divided by the total volume of the elastomeric stock, of about 25%; accordingly, typical (combined) amounts of reinforcing fillers, i.e., silica and carbon black, is about 30 to 100 phr.

(39) When silica is employed as a reinforcing filler, addition of a coupling agent such as a silane is customary so as to ensure good mixing in, and interaction with, the elastomer(s). Generally, the amount of silane that is added ranges between about 4 and 20%, based on the weight of silica filler present in the elastomeric compound.

(40) Coupling agents can have a general formula of A-T-G, in which A represents a functional group capable of bonding physically and/or chemically with a group on the surface of the silica filler (e.g., surface silanol groups); T represents a hydrocarbon group linkage; and G represents a functional group capable of bonding with the elastomer (e.g., via a sulfur-containing linkage). Such coupling agents include organosilanes, in particular polysulfurized alkoxysilanes (see, e.g., U.S. Pat. Nos. 3,873,489, 3,978,103, 3,997,581, 4,002,594, 5,580,919, 5,583,245, 5,663,396, 5,684,171, 5,684,172, 5,696,197, etc.) or polyorganosiloxanes bearing the G and A functionalities mentioned above. An exemplary coupling agent is bis[3-(triethoxysilyl)propyl]-tetrasulfide.

(41) Addition of a processing aid can be used to reduce the amount of silane employed. See, e.g., U.S. Pat. No. 6,525,118 for a description of fatty acid esters of sugars used as processing aids. Additional fillers useful as processing aids include, but are not limited to, mineral fillers, such as clay (hydrous aluminum silicate), talc (hydrous magnesium silicate), and mica as well as non-mineral fillers such as urea and sodium sulfate. Preferred micas contain principally alumina, silica and potash, although other variants are also useful. The additional fillers can be utilized in an amount of up to about 40 phr, typically up to about 20 phr.

(42) Other conventional rubber additives also can be added. These include, for example, process oils, plasticizers, anti-degradants such as antioxidants and antiozonants, curing agents and the like.

(43) All of the ingredients can be mixed using standard equipment such as, e.g., Banbury or Brabender mixers. Typically, mixing occurs in two or more stages. During the first stage (often referred to as the masterbatch stage), mixing typically is begun at temperatures of about 120 to about 130 C. and increases until a so-called drop temperature, typically about 165 C., is reached.

(44) Where a formulation includes silica, a separate re-mill stage often is employed for separate addition of the silane component(s). This stage often is performed at temperatures similar to, although often slightly lower than, those employed in the masterbatch stage, i.e., ramping from about 90 C. to a drop temperature of about 150 C.

(45) Reinforced rubber compounds conventionally are cured with about 0.2 to about 5 phr of one or more known vulcanizing agents such as, for example, sulfur or peroxide-based curing systems. For a general disclosure of suitable vulcanizing agents, the interested reader is directed to an overview such as that provided in Kirk-Othmer, Encyclopedia of Chem. Tech., 3d ed., (Wiley Interscience, New York, 1982), vol. 20, pp. 365-468. Vulcanizing agents, accelerators, etc., are added at a final mixing stage. To ensure that onset of vulcanization does not occur prematurely, this mixing step often is done at lower temperatures, e.g., starting at about 60 to about 65 C. and not going higher than about 105 to about 110 C.

(46) The relevant teachings of all patent documents mentioned above are incorporated herein by reference.