Process for hydrogenating functionalized polymer and products thereof

Abstract: A process for producing a hydrogenated and acidic functional­ ized polymer from a polymer initially containing either ethylenic unsaturation or both aromatic and ethylenic unsaturation comprising the steps of: (a) incorporating one or more precursors of an acidic functional group into the starting polymer; (b) hydrogenating the product from step (a) so as to convert at least a portion of the ethylenic unsaturation initially contained in said polymer; (c) converting at least a portion of the precursors incorporated in the hydrogenated polymer from step (b) to the corresponding acidic functional group; and (d) recovering a product containing acidic functionality which is at least partially hydrogenated.

Description: This invention relates to a process for preparing hydrogenated and functionalized polymers and to the hydrogenated products thus obtained. More particularly, this invention relates to a process for preparing hydrogenated polymers which contain acidic functional groups which otherwise might interfere in a hydrogenation step and to the hydrogenated products containing such functional groups. There are several well known advantages associated with the use of an acidic functionalized, particularly a carboxylated, and hydrogenated polymer. For instance, they may be beneficially employed as a modifier in compositions containing thermosetting resins or various engineering thermoplastics, due to their superior compatibility, stability and weatherability over unfunctionalized polymers. It has, heretofore, been expedient to first partially hydrogenate the ethylenically unsaturated polymer and then functionalize the same, for example by an ENE-type reaction wherein an ethylenically unsaturated functionalizing agent, particularly a dicarboxylic acid, is grafted onto a polymer at a carbon atom which is allylic to the ethylenically unsaturation in the polymer; via free-radical grafting; or by first metallating the polymer, and then reacting the metallated sites with a carboxylating agent such as CO₂. Once the ethylenically unsaturated polymer has been hydrogenated, however, the processes which can be used for functionalization are reduced. It will, of course, be appreciated that to the extent that the hydrogenated polymer contains a significant amount of residual ethylenic unsaturation, any of the techniques heretofore noted could be used. If the hydrogenation of the ethylenic unsaturation has, however, been completed or substantially completed, incorporation of functionality via the so-called ENE reaction as well as by free-radical addition of an ethylenically unsaturated functionalizing agent across an ethylenically unsaturated site is no longer possible. Functionalization may, of course, be accomplished in selectively hydrogenated copolymers containing aromatic unsaturation using the process described in U.S. Patent No. 4,145,298 but metallation of such a polymer followed by reaction with a functionalizing agent will incorporate the functionality exclusively into the aromatic portion of the polymer. This process is, of course, frequently used today and polymeric compositions containing such functionalized polymers do offer several advantages. More recently, however, the desirability of having at least some acidic functionality in the elastic portion of the polymer has been discovered. Functionalization may also be accomplished by a process as described in U.S. Patent Nos. 4,329,438; 4,578,429; and 4,628,072, a process believed to impart functionality into the elastomeric portion of such hydrogenated polymers by free-radical grafting of an ethylenically unsaturated compound onto the polymer. Such free-radical grafting, however, results in degradation of the polymer. When the polymer is a block copolymer containing, for example, terminal polymeric blocks comprising monoalkenyl aromatic hydrocarbon monomer units and a central polymer block containing conjugated diolefin monomer units, which block would be elastic, cleavage of the block copolymer within the elastomeric (central) block can destroy or at least reduce the advantages otherwise associated with the use of such a polymer. Also, when the process of U.S. Patent No. 4,578,429 is used to incorporate the desired functionality, the functionality is believed to be concentrated at a limited number of sites as oligomers of the monomer unit used as a source of the functional group rather than distributed somewhat uniformly along the polymer chain. Moreover, the amount of functionality incorporated into the polymer with this particular process is difficult to control and the length of the oligomer is generally longer than that which would be incorporated into an unsaturated polymer due to the reduced number of sites available for reaction. In light of this, the need for an improved process for preparing hydrogenated polymers containing acidic functional groups that interfere with the more commonly used hydrogenation producing a hydrogenated and acidic functionalized polymer from a block copolymer comprising at least one polymeric block containing predominantly monoalkenyl aromatic hydrocarbon monomer units and at least one polymeric block containing primarily conjugated diolefin monomer units, comprising the steps of: (a) incorporating one or more precursors of an acidic functional group selected from a metal salt, ester, amide or carbonate into the starting polymer; (b) hydrogenating the product from step (a) so as to convert at least 50% of the ethylenic unsaturation initially contained in said polymer; (c) converting at least a portion of the precursors incorporated in the hydrogenated polymer from step (b) to the corresponding acidic functional group; and (d) recovering a product containing acidic functionality which is at least partially hydrogenated. catalyst, particularly a process wherein at least some such functionality can be incorporated into an elastomeric portion of the polymer without degrading the same, and for the products thereof is believed to be readily apparent. It has now been discovered that the foregoing and other disadvantages of the prior art processes for preparing hydrogenated and acidic functionalized polymers can be avoided, or at least significantly reduced, with the process of this invention. It is, therefore, an object of this invention to provide a process for preparing a hydrogenated polymer containing acidic functional groups which would interfere with the hydrogenation if such functional groups were present during such hydrogenation. It is another object of this invention to provide such a process which will yield hydrogenated polymers containing at least some functionality reasonably uniformly distributed in that portion of the polymer initially containing the ethylenic unsaturation. The foregoing and other objects and advantages will become apparent from the description of the invention set forth hereinafter and from the examples contained therein. In accordance with the present invention, the foregoing and other objects and advantages are accomplished by a process for Any of the processes known for incorporating an acidic functional group precursor into an ethylenically unsaturated polymer may be used in the first step of the process of this invention. Such processes include incorporation of the desired acidic functional group into the polymer and thereafter converting the acidic functional group to a precursor, which precursor will at least not interfere with the hydrogenation reaction to the same extent as the desired acidic functional group, and which precursor can then be converted back to the desired acidic functional group after the hydrogenation is completed, or incorporation of a suitable precursor directly into the polymer. As indicated more fully hereinafter, the precursor obtained by converting an acidic functional group may, but need not, be the same as the precursor incorporated directly into the polymer. For convenience, the precursors to which an acidic functional group may be converted so as to permit hydrogenation as well as precursors which may be incorporated directly will both be referred to herein as a functional group precursor or an acidic functional group precursor. After the functional group precursor has been incorporated into the polymer, any of the processes known in the prior art for effecting hydrogenation of an ethylenically unsaturated polymer may be used to effect the desired degree of hydrogenation in the process of the instant invention. As indicated heretofore, the present invention relates to a process for preparing hydrogenated polymers which contain acidic functional groups which could interfere with the hydrogenation reaction if present in the polymer during hydrogenation with certain catalysts and to the polymeric products of such a process. When the polymer initially contains only ethylenic unsaturation, the functionality will be distributed within that portion of the polymer containing such unsaturation. When the polymer contains both ethylenic and aromatic unsaturation, the functionality may be contained exclusively in that portion of the polymer containing the ethylenic unsaturation before hydrogenation or may be distributed throughout the polymer; i.e., partly in that portion of the polymer containing the ethylenic unsaturation before the hydrogenation and partly in that portion of the polymer containing aromatic unsaturation. Hydrogenation of the polymer may be accomplished with any of those hydrogenation processes known in the prior art although the merits of the process of this invention is most evident when the desired acidic functional groups would interfere with the hydrogenation such as when a catalyst prepared by combining a metal alkyl or hydride with a compound containing an iron group metal; viz., iron, cobalt or nickel, is used. In general, any polymer containing ethylenic unsaturation or both aromatic and ethylenic unsaturation may be functionalized and hydrogenated using the process of this invention, and, hydrogenation of either of these polymers may be partial or substantially complete. Polymers containing both aromatic and ethylenic unsaturation may also, of course, be selectively hydrogenated so as to convert (saturate) a significant portion of the ethylenic unsaturation while converting little or no aromatic unsaturation. As is well known, polymers containing both aromatic and ethylenic unsaturation can be prepared by copolymerizing one or more polyolefins, particularly a diolefin, with one or more alkenyl aromatic hydrocarbon monomers. The copolymers may, of course, be random, tapered, block or a combination of these. When the double bonds in the polyolefin are separated by three or more carbon atoms, the ethylenic unsaturation incorporated into the polymer will be contained in a branch extending outwardly from the main polymer chain but when the polyolefin is conjugated at least a portion of the ethylenic unsaturation incorporated into the polymer may be contained in the polymer backbone. As is well known, polymers containing ethylenic unsaturation or both aromatic and ethylenic unsaturation may be prepared using free-radical, cationic and anionic initiators or polymerization catalysts. Such polymers may be prepared using bulk, solution or emulsion techniques. In any case, the polymer containing at least ethylenic unsaturation will, generally, be recovered as a solid such as a crumb, a powder, a pellet or the like. Polymers containing ethylenic unsaturation and polymers containing both aromatic and ethylenic unsaturation are, of course, available commercially from several suppliers and these commercially available polymers can be functionalized and hydrogenated with the process of this invention. While any of the polymers containing only ethylenic unsaturation or both aromatic and ethylenic unsaturation known in the prior art may be processed in accordance with the present invention, the use of a polymer prepared in solution is particularly expedient since functionalization and hydrogenation could be accomplished immediately after preparation of the polymer while the polymer remains in solution. As is well known, polymers of conjugated diolefins and copolymers of one or more conjugated diolefins and one or more alkenyl aromatic hydrocarbon monomers are frequently prepared in solution using anionic polymerization techniques. The present invention will, then, be described by reference to such polymers. It will, however, be appreciated that any polymer containing only ethylenic unsaturation or both aromatic and ethylenic unsaturation could be modified by incorporating desired acidic functional groups or a precursor thereof and then processed in accordance with the process of this invention. In general, when solution anionic techniques are used, conjugated diolefin polymers and copolymers of conjugated diolefins and alkenyl aromatic hydrocarbons are prepared by contacting the monomer or monomers 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 n wherein: R is an aliphatic, cycloaliphatic, aromatic or alkyl-substituted aromatic hydrocarbon radical having from 1 to 20 carbon atoms; and n is an integer of 1 to 4. Conjugated diolefins which may be polymerised anionically include those conjugated diolefins containing from 4 to 12 carbon atoms such as 1,3-butadiene, isoprene, piperylene, methylpentadiene, phenylbutadiene, 3,4-dimethyl-1,3-hexadiene and 4,5-diethyl-1,3-octadiene. Conjugated diolefins containing from 4 to 8 carbon atoms are preferred for use in such polymers. Alkenyl aromatic hydrocarbons which may be copolymerized include vinyl aryl compounds such as styrene, various alkyl-substituted styrenes, alkoxy-substituted styrenes, vinyl naphthalene and alkyl-substituted vinyl naphthalenes. 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 straight-and branched-chain hydrocarbons such as pentane, hexane, heptane and octane, as well as, alkyl-substituted derivatives thereof; cycloaliphatic hydrocarbons such as cyclopentane, cyclohexane and cycloheptane, as well as, alkyl-substituted derivatives thereof; aromatic and alkyl-substituted aromatic hydrocarbons such as benzene, naphthalene, toluene and xylene; hydrogenated aromatic hydrocarbons such as tetralin and decalin; halogenated hydrocarbons, particularly halogenated aromatic hydrocarbons, such as chlorobenzene and chlorotoluene; linear and cyclic ethers such as methyl ether, methyl ethyl ether and tetrahydrofuran; ketones such as methyl ketone (acetone), methyl ethyl ketone and ethyl ketone (3-pentanone). Conjugated diolefin polymers and conjugated diolefin-alkenyl aromatic copolymers which may be hydrogenated and functionalized in the present invention include those copolymers described in U.S. Patent Nos. 3,135,716; 3,150,209; 3,496,154; 3,498,960; 4,145,298 and 4,238,202. Conjugated diolefin-alkenyl aromatic hydrocarbon copolymers which may be functionalized and hydrogenated in accordance with this invention also include block copolymers such as those described in U.S. Patent Nos. 3,231,635; 3,265,765 and 3,322,856. In general, linear and branched block copolymers which may be functionalized and hydrogenated in accordance with the present invention include those which may be represented by the general formula: A z -(B-A) y -B x wherein: A is a linear or branched polymeric block comprising predominantly monoalkenyl aromatic hydrocarbon monomer units; B is a linear or branched polymeric block containing predominantly conjugated diolefin monomer units: x and z are, independently, a number equal to 0 or 1; y is a whole number ranging from 0 to 15, and the sum of x+z+y ≧ 2 . Polymers which may be treated in accordance with this invention also include coupled and radial block copolymers such as those described in U.S. Patent Nos. 4,033,888; 4,077,893; 4,141,847; 4,391,949 and 4,444,953. More particularly, coupled and radial block copolymers which may be treated in accordance with the present invention include those which may be represented by the general formula: [B x -(A-B) y -A z ] n -C-P n′ wherein: A, B, x, y and z are as previously defined; n and n′ are, independently, numbers from 1 to 100 such that n+n′ ≧ 3 : C is the core of the coupled or radial polymer formed with a polyfunctional coupling agent: and Each P is the same or a different polymer block or polymer segment having the general formula: B′ x′ -(A′-B'') y′ -A'' z′ wherein: A'' is a polymer block containing predominantly monoalkenyl aromatic hydrocarbon monomer units: B′ is a polymer block containing predominantly conjugated diolefin monomer units: A′-B'' is a polymer block containing monoalkenyl aromatic hydrocarbon monomer units (A′) and conjugated diolefin monomer units (B''), the A′-B'' monomers units may be random, tapered or block and when A′-B'' is block, the A′ block may be the same or different from A'' and B'' may be the same or different from B′; x′ and z′ are, independently, numbers equal to 0 or 1; and y′ is a number from 0 to 15, with the proviso that the sum of x′+y′+z ≧ 1 . The radial polymers may, then, be symmetric or asymmetric. In general, the initial incorporation of a functional group which will be converted to a suitable functional group precursor or the direct incorporation of a suitable precursor may be accomplished when the polymer is in solution or in the molten state depending partly upon the process actually used to incorporate the functional group or functional group precursor and partly upon preference. In this regard, it should be noted that when the functional group to be converted to a suitable precursor, or the functional group precursor that is to be incorporated directly into the polymer, is incorporated via to the so-called ENE reaction or via free-radical addition across a carbon-carbon double bond, either process (solution or molten state) is satisfactory. When the polymer is in the molten state, however, means capable of imparting high mechanical shear, such as an extruder, will, generally, be used to effect the desired reaction to incorporate the function group to be converted or to directly incorporate a suitable precursor. When the functional group to be converted to a suitable precursor or the precursor incorporated directly is incorporated via techniques such as metallation followed by reaction with a suitable electrophile, on the other hand, incorporation will, preferably, be accomplished with the polymer in solution. Of the several processes available for incorporation of a functional group or functional group precursor, those processes tending to incorporate a single function group or functional group precursor unit at each site of incorporation with minimal coupling of the polymer such as the process using the so-called ENE reaction and the process involving metallation followed by reaction with an electrophile are preferred. When a functional group to be converted to a suitable precursor is incorporated into the polymer, conversion of the functional group to the precursor will also, generally, be accomplished with the polymer in solution. In general, any of the solvents known to be useful for preparing such polymers in solution may be used to effect these reactions or conversions. Similarly, hydrogenation of the ethylenically unsaturated polymers in accordance with the present invention will be accomplished with the polymer in solution. In general, any of the solvents useful in preparing the polymer may be used to effect the hydrogenation. The solution of polymer and solvent, when a solution is used in any step of the process of this invention, will generally contain from 1 wt% to 30 wt% polymer and from 99 wt% to 70 wt% solvent when the conversion and hydrogenation are completed. In general, the process of this invention may be used to produce hydrogenated polymers containing any acidic functional group which would, if dissolved in water, yield a hydrogen ion concentration within the range from 1x10⁻¹ to 1x10⁻⁵ (a pH of 1 to 5). The process of this invention could, of course, also be used to incorporate functional groups which are acids capable of yielding solutions having higher pH's but use of the process of this invention with such functional groups would not be necessary since these higher pH functional groups would not, generally, interfere with direct hydrogenation of the polymer with the hydrogenation catalysts useful in the process of this invention. The process of this invention is, then, particularly useful for the production of polymers containing organic acid functionality such as carboxyl functionality and aromatic hydroxyl functionality and inorganic acid functionality such as sulphonic acid functionality and phosphoric acid functionality. Incorporation of these functionalities into a polymer containing ethylenic unsaturation is, of course, well within the ordinary skill of the art and a detailed discussion of processes useful for such incorporation will not be included herein. Nonetheless, the principle processes commonly used for such incorporation will be briefly summarized hereinafter. When the polymer is to be carboxylated and the carboxyl groups then converted to a suitable precursor or a carboxyl group, the polymer may be carboxylated using any of the processes known in the prior art to be effective for carboxylating such polymers. For example, an unsaturated monofunctional or polyfunctional carboxylic acid or anhydride such as acrylic acid or anhydride or maleic acid or maleic anhydride can be grafted onto the polymer chain at carbon atoms allylic to ethylenic unsaturation using the so-called ENE reaction as taught in U.S. Patent Nos. 4,292,414; 4,308,353 and 4,427,828. As is well known, the so-called ENE reaction may be accomplished with the polymer in solution or in the molten state. The ENE reaction will, generally, be accomplished at a temperature within the range from 100 °C to 400 °C in the absence of free-radicals or free-radical initiators. When this technique is used with polymers containing both ethylenic and aromatic unsaturation the incorporated carboxyl groups will be contained exclusively in that portion of the polymer containing the ethylenic unsaturation. Carboxyl functionality may also be incorporated into the polymer by free-radical addition of an unsaturated carboxylic acid or anhydride across an ethylenic double bond contained in the polymer. Free-radical grafting may be accomplished thermally, generally at temperatures within the range from 150 °C to 300 °C, or in the presence of a free-radical initiator, generally at temperatures within the range from 50 °C to 300 °C. As is also well known, this grafting reaction may be accomplished with the polymer in solution or in the molten state. When this technique is used, the carboxyl groups will again be contained exclusively in that portion of the polymer containing the ethylenic unsaturation. In general, any of the ethylenically unsaturated carboxylic acids and/or anhydrides known in the prior art to be subject to the ENE reaction or graftable onto ethylenically unsaturated polymers may be used to incorporate the carboxyl functionality into the polymers which may be hydrogenated with the process of the present invention. The carboxylic acid and/or anhydride may be monofunctional such as acrylic, methacrylic, cinnamic, crotonic and isocrotonic or polyfunctionals such as maleic, fumaric, itaconic, citraconic and mesaconic. Carboxyl functionality may further be incoporated onto the ethylenically unsaturated polymer by first metallating the polymer, reacting the metallated polymer with a carboxylating agent such as CO₂ and thereafter contacting the reaction product with a proton donor as taught in U.S. Patent No. 3,976,628. As is well known, carboxylation of the polymer via metallation of the polymer will, generally, be accomplished with the polymer in solution. As is known in the prior art, this process produces an intermediate product wherein at least a portion of the carboxyl functionality is present as a carboxyl group precursor. This intermediate product may be hydrogenated before the carboxyl group precursor is converted to the carboxylic acid group. It generally will be advantageous however, to convert any or at least a portion of the acid groups formed in the intermediate product as a result of the reaction with CO₂ to a salt group before effecting the hydrogenation. While any of the processes known in the prior art may be used to incorporate the functional group or the functional group precursor, those processes tending to incorporate a single unit at each site of incorporation with minimal coupling and providing novel and advantageous block copolymers, which form another aspect of the invention are preferred. As indicated above, it has now been discovered that certain acidic functional groups contained in a polymer also containing ethylenic unsaturation significantly inhibit hydrogenation of the ethylenic unsaturation at least when catalysts reactive with such groups are used. It is, then, necessary to convert the acid functional group or groups to a different functional group precursor which will not interfere with the hydrogenation reaction, or at least which intereferes less than the certain acidic functional groups. While the acidic functional group might be converted to any number of groups which would interfere with the hydrogenation less than the acidic group itself, conversion to a relatively neutral group such as a metal salt, an ester and an amide is most effective. Aromatic hydroxyl functionality may also be converted to a carbonate but cannot be converted to an amide. In general, and as indicated above, conversion of acidic functional groups to acid functional group precursors will be accomplished with the polymer in solution. In general, when an acid group is converted to a precursor that is a metal salt, any metal cation could be used to form the salt so long as the metal cation actually used will not be displaced from the salt by one or more of the metals used to prepare the catalyst, particularly the metal in the reducing component, and so long as the metal or metal compound used as a source of the metal ion does not react or complex with the acid group so as to gel or otherwise crosslink or couple the polymer segments. Displacement will, of course, general, be avoided when the salt is prepared with the same metal as is contained in the metal alkyl or hydride used to prepare the catalyst. Use of the same metal to prepare the salt as is contained in the reducing component used to prepare the catalyst is, therefore, preferred. Moreover, while, in general, any metal could be used, it appears that any metal cation will, to some extent, inhibit or impair the hydrogenation reaction. While the reasons for this impairment are not completely clear and while the inventor does not wish to be bound by any particular theory, it is believed that the impairment is at least in some way associated with an interaction between the polymer bound functional group precursor, particularly the metal cation thereof, and one of the components, particularly the reducing component, used to prepare the catalyst or a product of any reaction occurring between these components. Such interaction is particularly apparent when the functional group precursor is capable of complexing with a metal used in the preparation of the hydrogenation catalyst. For example, a polymer containing ethylenic unsaturation and precursors that are lithium carboxylate functional groups would be expected to complex with either the aluminium reactant or a reaction product thereof, when a catalyst prepared by combining a nickel carboxylate and an aluminium trialkyl is used to effect hydrogenation. The potential reaction with the Al trialkyl can be illustrated by the following equation: P-CO₂Li+Al(R)₃ ---> Li⁺[(R)₃AlO₂C-P]⁻ wherein: P is a polymer segment; P-CO₂Li is the polymer segment P having a single, for illustrative purposes, functional group precursor attached thereto; and R is an alkyl group. Obviously, if the metal in the functional group precursor were the same as the metal in the reducing component used to prepare the catalyst, complexing would not occur. Complexing can also be avoided, or at least minimized, even when different metals are used, by selecting a combination of metals which are not prone to complexing. In general, and as is well known in the prior art, carboxyl groups may be converted to metal salts by reaction of the carboxyl group with an active metal (Groups I-A and II-A) in its elemental state or basic compound of essentially any metal such as a metal hydroxide, a metal alkyl and a metal hydride. The reference to Groups I-A and II-A relates to Groups I-A and II-A of the Periodic Table of the Elements. All such reference to these and other groups herein is by reference to the Periodic Table of the Elements as arranged by Mendeleev and published in Kirk-Othmer, Encyclopedia of Chemical Technology, Second Edition, 8:94. In general, such reaction may be accomplished at a temperature within the range from 20 °C to 60 °C at essentially any pressure. In general, the active metal and the basic metal compound will be used at or near the stoichiometric amount required to convert all carboxyl groups so as to avoid the incorporation of a significant excess of reagent into the polymer solution. To the extent that an excess amount is added, however, it will, generally, be expedient to remove such excess prior to hydrogenation so as to avoid possible interference with the hydrogenation reaction. In general, when a carboxyl group is converted to an ester as the functional group precursor, essentially any monoalcohol or monoepoxide could be reacted with the carboxyl group. To minimize possible steric hinderance, however, aliphatic alcohols containing from 1 to 10 carbon atoms will, advantageously, be used. When the carboxyl group is converted to an amide as the functional group precursor, essentially any inorganic acid halide may be reacted with the carboxyl group and the resulting acyl halide then reacted with ammonia. Alternatively, the carboxyl group may be converted to a quaternary ammonium salt, by reaction with ammonia or a primary or secondary amine, and the quaternary ammonium salt then converted to the amide by heating. In each of these conversions, care will, generally, be exercised so as to avoid the use of excess reagent and, when the reagent would interfere with a subsequent hydrogenation, any excess reagent will be removed. These conversions will be accomplished at conditions well known in the prior art. Again, these conversions will, generally, be accomplished in a suitable solvent. It will, of course, be appreciated that when the ethylenically unsaturated elastomer is first functionalized using the ENE reaction or free-radical grafting and the functional groups then converted to a functional group precursor, all or at least substantially all of the functional groups will be incorporated into that portion of the polymer containing the ethylenic unsaturation. As indicated before, there are end use applications for carboxylated polymers wherein such distribution of the carboxyl groups appear to be advantageous. There may, however, be other end use applications wherein it would be advantageous to have carboxyl groups distributed in both an elastomeric portion of a polymer such as a block copolymer containing ethylenic unsaturation and a plastic portion containing aromatic unsaturation. Such distribution may, then, be accomplished by first metallating the polymer, reacting the metallated polymer with a carboxylating agent such as CO₂ and then reacting the carboxylated polymer with a proton donor as taught in U.S. Patent no. 3,976,628. When the polymer thus treated contains both aromatic and ethylenic unsaturation, the carboxyl groups will be distributed in both sections proportionately to the relative amount of aromatic rings and ethylenic unsaturation contained in the polymer. As suggested above, the product obtained by reacting the metallated polymer with the carboxylating agent will be a polymer containing at least a portion of the carboxyl functionality as a carboxylic acid metal salt group, the remainder being as the acid group, and in some cases at least may be directly hydrogenated depending largely upon the number of acid groups contained therein. These salt precursor groups, like the carboxyl groups, will be proportionately distributed in the aromatic and elastomeric portions of the polymer. Aromatic hydroxyl functionality may be incorporated into a polymer containing both aromatic and ethylenic unsaturation by preparing the polymer with a compound containing an aromatic hydroxyl group such as a hydroxy-substituted styrene or by grafting such compounds onto the polymer. Inorganic acid functionality can be incorporated into a polymer containing ethylenic unsaturation or both aromatic and ethylenic unsaturation by preparing the polymer with a compound containing an inorganic acid group such as styrene sulphonate or by grafting such a compound onto the polymer and by direct sulphonation of the polymer with acyl sulphates. As is well known, the reactions may be accomplished at temperatures within the range from 50 °C to 200 °C. In general, direct sulphonation occurs stoichiometrically. As a result, the polymer will, generally, be contacted with a stoichiometric amount of the reagent required to impart the desired amount of functionality or an amount just slightly in excess of the stoichiometric amount. In general, the functional groups imparted via direct sulphonation will be incorporated into that portion of the polymer containing the ethylenic unsaturation. Each of these functional groups can be converted to a satisfactory precursor using known technology. For example, the aromatic hydroxyl functional group can be converted to an ester group by reaction with a carboxylic acid or a carboxylic acid halide or to a carbonate by reaction with phosgene or an alkyl carbonate such as methyl carbonate. The inorganic acid functional groups may be converted to salt groups by reaction with a metal hydroxide or esterified by reaction with alcohols or suitable alkyl halides. After the functional group precursors have been incorporated into a polymer containing ethylenic unsaturation or both aromatic and ethylenic unsaturation, the polymer will next be hydrogenated so as to convert (saturate) at least a portion of the ethylenic unsaturation in the polymer. As indicated before, the maximum amount of ethylenic unsaturation that may be converted (saturated) will vary with the particular carboxylic acid precursor actually used as well as the catalyst actually selected, and particularly the nature of the metal atom contained in the reducing component used to prepare the catalyst. In any case, however, it will be possible to convert (saturate) at least 50% of the ethylenic unsaturation initially contained in the polymer and catalyst components and acidic functional group precursors can be selected which will permit conversion (saturation) of up to at least 90% to 95% of the ethylenic unsaturation initially contained in the polymer. To the extent that it is desirable to convert at least a portion of the aromatic unsaturation contained in a polymer containing both aromatic and ethylenic unsaturation, the amount of aromatic unsaturation that may be converted will depend, firstly, on whether the aromatic unsaturation contains a functional group precursor and, if it does, secondly, on the particular functional group precursor incorporated and the particular catalyst used to effect the hydrogenation. It will, of course, be appreciated that if the aromatic portion of the polymer does not contain a precursor, hydrogenation of the aromatic unsaturation will not be affected and whether hydrogenation of the aromatic unsaturation is effected will be controlled by processes well known in the prior art. In this regard, the relative selectivity of various catalysts used for hydrogenating polymer containing both aromatic and ethylenic unsaturation are well known. The amount of aromatic unsaturation actually converted will, then, depend primarily upon the particular catalyst selected, the concentration thereof used during hydrogenation and the hydrogenation conditions actually used. The amount of aromatic unsaturation actually converted when the aromatic portion of the precursors will, generally, be less than the amount of ethylenic unsaturation converted, primarily because the ethylenic unsaturation is generally more easily hydrogenated than the aromatic unsaturation. The hydrogenation or selective hydrogenation of the polymer may be accomplished using any of the several hydrogenation processes known in the prior art, such as those taught, for example, in U.S. Patent Nos. 3,494,942; 3,634,594; 3,670,054; 3,700,633 and Re. 27,145. In general, the processes known in the prior art and useful in the present invention for hydrogenating polymers containing ethylenic unsaturation and for hydrogenating or selectively hydrogenating polymers containing aromatic and ethylenic unsaturation, involve the use of a suitable catalyst, particularly a catalyst or catalyst precursor comprising an iron group metal atom. In the processes described in the foregoing patents, a catalyst is prepared by combining an iron group metal, particularly nickel or cobalt, compound with a suitable reducing agent such as an aluminium alkyl. The preferred iron group metal compounds are carboxylates and alkoxides. Various chelates and salts of sulphur-containing hydrocarbyl acids and partial ester thereof such as taught in U.K. Patent No. 1,030,306 are also useful in the process of this invention. Also, while aluminium alkyls are the preferred reducing agents, it is known in the prior art that alkyls and hydrides of metals of Groups I-A, II-A and III-B of the Periodic Table of the Elements are effective reducing agents, particularly lithium, magnesium and aluminium. In general, the iron group metal compound will be combined with Group I-A, II-A or III-B metal alkyl or hydride at a concentration sufficient to provide Group I-A, II-A and/or III-B metal to iron group metal atomic ratio within the range from 0.1:1 to 20:1, preferably from 1:1 to 10:1. As indicated in the foregoing patents, the hydrogenation catalyst is generally prepared by combining the iron group metal compound and the reducing agent in a suitable solvent or diluent at a temperature within the range from 20 °C to 60 °C before the catalyst is fed to the hydrogenation reaction. Satisfactory results can, however, frequently be obtained by feeding the catalyst components separately into the reactor. In practising the process of the present invention, water may, and preferably will be, present when the components used to prepare the catalyst are combined. When water is present, water will be present at a concentration within the range from 0.3 to 1.3 moles of water per mole of iron group metal compound. The water may, then, be conveniently combined with the iron group metal compound before it is combined with the metal alkyl or hydride used to prepare the catalyst. In general, the hydrogenation will be accomplished in a suitable solvent at a temperature within the range from 20 °C to 80 °C and at a hydrogen partial pressure within the range from 6.9 MPa (100 psig) to 344.7 MPa (5,000 psig), preferably 6.9 MPa to 68.9 MPa. Catalyst concentrations within the range from 50 ppm (wt) to 500 ppm (wt) of iron group metal based on total solution are generally used and contacting at hydrogenation conditions is generally continued for a period of time within the range from 60 to 240 minutes. After the hydrogenation is completed, the hydrogenation catalyst and catalyst residue will, generally, be separated from the polymer. Separation of the catalyst and catalyst residue may be accomplished using processes well known in the prior art; however, separation by washing with an aqueous acid solution is preferred. Essentially any acid, organic and inorganic, may be used to effect separation of the catalyst and catalyst residue. Interestingly, when an aqueous acid solution is used to separate the catalyst from a polymer containing a metal salt as the functional group precursors, the metal salt will be simultaneously converted to the corresponding carboxylic acid group. After the hydrogenation has been completed and when the functional group precursors were not converted to the desired acidic functional group during the catalyst separation step, the hydrogenated polymer containing the functional group precursors may then be treated to either form or restore the desired acidic functional group. As indicated above, conventional technology may be used to effect conversion of the functional group precursor to the acidic functional group. For example, when the functional group precursor is a metal salt, the salt may be converted to the acid by contacting the polymer, and hence, the salt group with a proton donor such as an organic or inorganic acid. Generally, acids such as acetic acid, citric acid, dilute sulphuric acid and dilute hydrochloric acid are particularly effective. This conversion is readily accomplished at ambient conditions. When the functional group precursor is an ester, an amide or a carbonate, on the other hand, the conversion will be accomplished via hydrolysis. Generally, the hydrolysis may be accomplished in the presence of either an acidic or basic catalyst. When a basic catalyst is used, however, it will, frequently, be necessary to contact the resulting product with a proton donor so as to convert the metal salt formed by reaction of the basic catalyst with the acidic functional group. In general, the conversion of an ester, an amide or carbonate functional group precursor to the desired acidic functional group via hydrolysis will be accomplished at a temperature within the range from 100 °C to 350 °C in an inert atmosphere. After conversion of the functional group precursor to the corresponding acidic functional group has been completed, the (selectively) hydrogenated polymer containing acidic functionality may be recovered from solution as a crumb using techniques well known in the prior art. For example, the dissolved polymer may be precipitated by adding a suitable non-solvent to the solution. Suitable non-solvents include alcohols and ketones. Preferably, however, the polymer will be recovered by contacting the solution with steam or water and the solvent is then separated via distillation. After the polymer has been recovered as a crumb, the same may be treated to separate any entrained impurities introduced as a result of the hydrogenation and functionalization unless these impurities have been previously separated. The (selectively) hydrogenated, acid functionalized polymer of this invention may be used in any of the end use applications known in the prior art for such polymers. Suitable end uses, then, include use as an impact modifier, as a viscosity index improvers such as dispersant-viscosity index improvers, as a tie layer or as a tie layer component and as a component in adhesive compositions. In a preferred embodiment of the present invention, a block copolymer comprising at least one block containing monoalkenyl aromatic hydrocarbon monomer units and at least one block comprising conjugated diolefin monomer units will be modified by incorporating a functional group or a functional group precursor using a technique designed to incorporate a single group or precursor at each of the sites of incorporation. More preferably, the polymer will be metallated using a lithium alkyl. The active metal sites incorporated into the polymer will then be converted to carboxyl functional groups by reaction with CO₂ to impart the carboxyl functionality and the polymer then contacted with LiOH to convert at least a portion of the carboxyl groups contained in the polymer to the salt. Thereafter, the polymer is selectively hydrogenated so as to convert (saturate) at least 80%, more preferably at least 90%, of the ethylenic unsaturation initially contained in the polymer without converting a significant portion, e.g., less than 25%, more preferably less than 5%, of the aromatic unsaturation contained in the polymer. Also, at least a portion of the metal salt groups is then converted to the corresponding carboxylic acid group. In the preferred embodiment, the monoalkenyl aromatic hydrocarbon polymer blocks will have a weight-average molecular weight within the range from 1,000 to 125,000 and the conjugated diolefin polymer blocks will have a weight-average molecular weight within the range from 10,000 to 450,000. Most preferably, the ethylenically unsaturated polymer will contain a singly polystyrene block and a single polybutadiene block. In the preferred embodiment, the polymer will be metallated so as to incorporate a sufficient number of metal sites to permit the production of a polymer containing, on average, from 1 to 50 carboxylic acid groups per polymer chain. In the preferred embodiment, the hydrogenation catalyst will be prepared by combining an iron group metal carboxylate containing a metal selected from the group consisting of nickel and cobalt and from 5 to 30 carbon atoms, with a metal alkyl containing a metal selected from Group I-A of the Periodic Table of the Elements, most preferably lithium. In the preferred embodiment, the iron group metal carboxylate will be combined with from 0.5 moles to 0.75 moles of water per mole of carboxylate. In the preferred embodiment, the iron group metal compound will be combined with the Group I-A metal alkyl during preparation of the catalyst at a concentration sufficient to provide a Group I-A metal atom to iron group metal atom ratio with the range from 1:1 to 10:1. In the preferred embodiment, the catalyst will be prepared in cyclohexane and the hydrogenation will be completed in a mixed tetrahydrofuran/cyclohexane solvent. The hydrogenation will be completed at a temperature within the range from 40 °C to 80 °C at a hydrogen partial pressure within the range from 6.9 MPa to 68.9 MPa, most preferably at a hydrogenation partial pressure within the range from 34.5 MPa to 48.3 MPa. During the hydrogenation, from 50 ppm (wt) to 200 ppm (wt) iron group metal, based on total solution, will be present. The polymer will be contained in the solution at a concentration within the range from 1 wt% to 30 wt%, based on combined polymer and solvent. In a most preferred embodiment, the catalyst will be prepared by combining a nickel 2-ethylhexanoate with a lithium alkyl wherein the alkyl group contains from 1 to 5 carbon atoms. The preferred polymer will have a single functional group unit at each site of functionalization and the functional groups will be randomly distributed in those portions (blocks) of the polymer containing the groups. Having thus broadly described the present invention and a preferred and most preferred embodiment thereof, it is believed that the same will become even more apparent by reference to the following examples. It will be appreciated, however, that the examples are presented solely for purposes of illustration and should not be construed as limiting the invention unless limitations illustrated therein are incorporated into the claims appended hereto. EXAMPLE 1 In this example, a catalyst prepared by combining nickel 2-ethylhexanoate containing 0.5 moles of H₂O per mole of nickel carboxylate and s-butyl lithium was used to hydrogenate two different styrene-butadiene block copolymers. Both of the block copolymers contained carboxylic acid functionality, said functionality being present as a mixture of acid and salt groups, with one of the two polymers containing significantly less acid sites than the other. Both of the polymers tested were prepared by metallating a styrene-butadiene diblock copolymer and then reacting the metallated polymer with CO₂. The first polymer tested was, in effect, the reaction product obtained by reacting CO₂ with the metallated polymer while the second polymer tested was the product obtained by contacting this reaction product with sufficient LiOH to convert a substantial portion of the carboxyl groups to the Li salt. The first of the polymers tested, then, contained the carboxyl functionality primarily as an acid group while the second polymer had a reduced amount of the carboxyl functionality present as the acid. The staring block polymer for both of these products contained polystyrene blocks having a number-average molecular weight of 12,400 and polybutadiene blocks having a weight-average molecular weight of 66,200. The starting polymer; i.e., the polymer prior to metallation and carboxylation, had, on average, 973 ethylenic unsaturations per polymer chain. The metallation was accomplished by contacting a solution of the polymer in cyclohexane with s-butyllithium in the presence of tetra methylethylene diamine, at a temperature of 60 °C for 10 minutes. Initially, 16.07 moles of s-butyllithium were added per mole of polymer. After the metallation was completed, a portion of the metallated polymer gel was combined with dry ice contained in tetrahydrofuran at room temperature. The contacting with CO₂ was continued for 45 minutes. After the CO₂ treatment was completed, the carboxylated polymer which polymer contained 0.38 wt% carboxyl functionality (as acid and salt) was recovered as a crumb by precipitation with steam/water. Analysis revealed than 64% of the carboxyl functionality was present as the acid, while 36% of the acid functionality was present as the lithium salt. About 33% (wt) of the polymer coupled during the reaction with CO₂ and dimers, trimers and tetramers were identified. 67% (wt) remained uncoupled. Analysis of the carboxylated polymer product using deuterium NMR techniques also indicated that 54 wt% of the carboxyl functionality was incorporated in the polybutadiene blocks of the polymer while 46 wt% was incorporated into polystyrene blocks. A first portion of this carboxylated polymer was next dissolved in a blend containing 77 wt% cyclohexane and 23 wt% tetrahydrofuran at a concentration of 4.6 wt%, based on total solution, and then contacted with hydrogen at a partial pressure of 51.0 MPa and an initial temperature of 45 °C in the present of a catalyst prepared by combining nickel 2-ethylhexanoate and s-butyllithium separately in cyclohexane at a maximum temperature of 47 °C. As indicated above, the nickel 2-ethylhexanoate contained 0.5 moles of water per mole of nickel 2-ethylhexanoate. During hydrogenation, the temperature rose to 83 °C. The amount of nickel 2-ethylhexanoate and s-butyllithium actually combined was controlled such that the mixture contained one atom of nickel per 6 atoms of lithium. The catalyst was added to the cyclohexane/tetrahydrofuran polymer solution in an amount sufficient to provide 70 parts, by weight, of nickel per million parts, by weight, of polymer solution. Contacting during the hydrogenation reaction was continued for 180 minutes. Following the hydrogenation the hydrogenated product was contacted with acetic acid to convert at least a significant portion of the lithium salt to the corresponding carboxylic acid group. Analysis of the product indicated that 75% of the ethylenic unsaturation originally contained in the carboxylated polymer was converted or hydrogenated during the hydrogenation reaction. A second portion of the carboxylated polymer recovered as a crumb was dissolved in tetrahydrofuran and then contacted with an aqueous solution of LiOH so as to convert a significant portion of the carboxyl groups to the corresponding Li salt group. After this contacting was completed, analysis of the polymer indicated that 6% of the carboxyl functionality was present as the acid while 94% was present as the lithium salt. A portion of this polymer was then hydrogenated at the same conditions and with a catalyst identical to that which was used in the previous run. After the hydrogenation was completed, analysis indicated that 87% of the ethylenic unsaturation originally contained in the polymer was converted or saturated. As will be apparent from these results, increasing the portion of carboxyl functionality present in the salt form increases the extent of hydrogenation. EXAMPLE 2 In this example, a carboxylated polymer was prepared from a diblock copolymer identical to that used in Example 1 and the carboxylated polymer was prepared in the same manner as was used in Example 1 except that the amount of s-butyllithium used during the metallation step was increased sufficiently to produce a carboxylated polymer containing 0.67 wt% combined carboxyl functionality. Analysis of the polymer obtained as a crumb indicated that 50% of the carboxyl functionality was present as the acid with the remainder present as a Li salt. About 55% (wt) of the polymer coupled during the carboxylation step while 45% (wt) remained uncoupled. The carboxylated polymer was next reacted with lithium hydroxide in the same manner as summarized in Example 1 and then hydrogenated with a catalyst prepared by combining nickel 2-ethylhexanoate and triethyl aluminium. After the polymer was reacted with the LiOH, 7% of the carboxyl functionality remained in the acid form with the remaining 93% present as a Li salt. The polymer containing principally lithium salt groups was hydrogenated at a hydrogen partial pressure of 51.7 MPa at a temperature ranging from 42 °C to 80 °C for 180 minutes in the presence of a catalyst prepared by combining nickel 2-ethylhexanoate and triethyl aluminium. The catalyst was prepared by combining the nickel 2-ethylhexanoate and the triethyl aluminium separately in cyclohexane at ambient temperature for 10-15 minutes. Again, the nickel 2-ethylhexanoate contained 0.5 moles of water per mole of nickel 2-ethylhexanoate. The amount of nickel 2-ethylhexanoate and triethyl aluminium combined was sufficient to provide a mixture containing one mole of nickel per 2.3 moles of aluminium. After the catalyst components were combined, a sufficient amount of the cyclohexane suspension was added to the polymer to provide 70 parts (wt) of nickel per million parts (wt) of polymer solution. After the hydrogenation was completed, the hydrogenated product was contacted with acetic acid to convert at least a significant portion of the salt groups to the carboxylic acid groups. Analysis of the hydrogenated product obtained in this Example indicated that 55% of the ethylenic unsaturation originally contained in the polymer was converted or saturated. Further analysis also indicated that the amount of combined carboxyl functionality (acid and salt) in the polymer after conversion of the lithium salt was identical to that contained in the original polymer (0.67 wt%). COMPARATIVE EXAMPLE In this example, a polymer identical to that reacted with lithium hydroxide in Example 2 and containing 0.67 wt% carboxyl functionality was hydrogenated at the same conditions and with a catalyst identical to that used in Example 2 except that the polymer was present at a concentration of 12 wt%, based on total solution, during hydrogenation. Following the hydrogenation, analysis indicated that 16% of the ethylenic unsaturation originally contained in the polymer was converted or hydrogenated. While the present invention has been described and illustrated by reference to particular embodiments thereof, it will be appreciated by those of ordinary skill in the art that the same lends itself to variations not necessarily described or illustrated herein. For this reason, then, reference should be made solely to the appended claims for purposes of determining the true scope of the present invention.

Claims: A process for producing a hydrogenated and acidic functionalized polymer from a block copolymer comprising at least one polymeric block containing predominantly monoalkenyl aromatic hydrocarbon monomer units and at least one polymeric block containing primarily conjugated diolefin monomer units, comprising the steps of: (a) incorporating one or more precursors of an acidic functional group selected from a metal salt, ester, amide or carbonate into the starting polymer; (b) hydrogenating the product from step (a) so as to convert at least 50% of the ethylenic unsaturation initially contained in said polymer; (c) converting at least a portion of the precursors incorporated in the hydrogenated polymer from step (b) to the corresponding acidic functional group; and (d) recovering a product containing acidic functionality which is at least partially hydrogenated. A process as claimed in claim 1, wherein said monoalkenyl aromatic hydrocarbon is styrene. A process as claimed in claim 1, wherein said conjugated diolefin is butadiene. A process as claimed in any of claims 1 to 3, wherein the hydrogenation is accomplished in the presence of a catalyst prepared by combining a compound containing an iron group metal such as cobalt and nickel with a reducing agent such as an alkyl or hydride of a metal selected from groups I-A, II-A and III-B of the Periodic Table of the Elements. A process as claimed in claim 4, wherein the compound containing the iron group metal is an alkoxide or carboxylate. A process as claimed in claim 4 or 5, wherein the reducing agent is an alkyl or a hydride of lithium, magnesium or aluminium. A process as claimed in claim 1 wherein said precursor is a metal salt. A process as claimed in claim 7 wherein the metal in said metal salt is of the same group as the metal in the reducing agent. As process as claimed in any of claims 1 to 8, wherein at least a portion of said precursors are incorporated into that portion of said polymer initially containing ethylenic unsaturation. A polymer obtainable by a process as disclosed in any of claims 1 to 9 comprising acidic functionality in the portion of said polymer initially containing ethylenic unsaturation as well as in the portion of the polymer containing aromatic unsaturation and wherein the acidic functionality is present as a single unit at each site of incorporation. The polymer as claimed in claim 10 wherein said acidic functionality is a carboxylic acid group. The polymer as claimed in claim 10, wherein a starting block copolymer comprises at least a monoalkenyl aromatic hydrocarbon polymer block having a weight average molecular weight within the range from 1,000 to 125,000 and at least one conjugated diene polymer block, having a weight average molecular weight within the range from 10,000 to 450,000.

Inventors: GOODWIN DAN E, POTTICK LORELLE ANN, WILLIS CARL LESLEY, GOODWIN, DAN E., POTTICK, LORELLE ANN, WILLIS, CARL LESLEY
Applicants: SHELL INT RESEARCH, SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1989
Main classification: C08F8
IPC codes: C08C19, C08F8