Linear copolymers having pendant peroxycarbonate ester functionality, their synthesis and use
United States Patent 1191 Crawford Apr. 22, 1975 1 1 LINEAR COPOLYMERS HAVING PENDANT PEROXYCARBONATE ESTER FUNCTIONALITY. THEIR SYNTHESIS AND USE [75] Inventor: James E. Crawford, Adrian, Mich.  
 [73] Assignee: Owens-Illinois, Inc., Toledo, Ohio [22] Filed: .Ian. 15, 1973 [21] Appl. No.: 323,994  
  Related U.S. Application Data [63] Continuation of Ser. No. 177,115, Sept. l. 1971.  
 [ 2] U.S. C1. ..260/77.5 R; 204/159.23; 260/DIG. 28; 260/80 P; 260/82.l;  
 260/88.1 PC; 260/95 R; 260/96 R;  
  260/78.5 T; 260/92.8 W [51] Int. Cl C08I 1/60; C08f 27/12; C070 69/60 [58] Field of Search 260/78.5 T. 80 P, 88.] PC. 260/. 453 R, 453 P, 610 D, DIG. 28, 463  
 [56] References Cited UNITED STATES PATENTS 3.022.281 2/1962 Smith 260/92.8 3.108.093 10/1963 Pajctkowski et a1 260/89.5 3,326,859 6/1967 Sciner 260/72 3,499,919 3/1970 Gerritsen et a1. 260/453 3.592.948 7/1971 Bal&#39;ford ct a1. 260/453 3.652.524 3/1972 Lewis 260/928 3.657.312 4/1972 DAngclo 260/463 FOREIGN PATENTS OR APPLICATIONS 1.041.088 9/1966 United Kingdom OTHER PUBLICATIONS Graft Copolymerization with Perester Side Groups: Smets et al.: Journal of Polymerscience: Vol. 54, pp. 65-81 (1961).  
 Synthesis of Peroxide Esters of Aliphatic Dibasic Acids: Yurzhenko et al.: Journal of Organic Chem. of the U.S.S.R. Vol. 1, Jan-Apr., pp. 689-691 (1964).  
 Primary Examiner-Joseph L. Schofer Assistant E.raminer.1ohn Kight, III  
 Attorney, Agent, or F irm-Robert F. Rywalski Edward J. Holler [57] ABSTRACT 24 Claims, No Drawings LINEAR COPOLYMERS HAVING PENDANT PEROXYCARBONATE ESTER FUNCTIONALITY. THEIR SYNTHESIS AND USE This is a continuation of a application Ser. No. 177.115. Filed Sept. 1.197l.  
 BACKGROUND OF THE INVENTION This invention is directed toward a process for the preparation of multifunctional peroxycarbonate esters. the peroxycarbonate ester products of this process, and a method for initiation of free radical polymerization of ethylenically unsaturated monomers.  
  Olefinic and vinyl monomers are generally recognized to respond to four types of initiators: (a) free radical; (b) cationic; (c) anionic; and (d) coordination. Probably the most common and widely accepted method for the initiation of polymerization of ethylenically unsaturated monomers involves the use of free radicals. Free radical polymerization ordinarily involves the generation of a monomer radical through an interaction of the monomer with an initiator compound. the propagation of the monomer radical chain and the termination of the polymer chain either through the exhaustion of monomer or by disproportionation, Flory. P. 1.. Journal American Chemical Society. 59:241 (1937). The class of compounds most widely used as initiators in the generation of monomer free radicals in the above type of synthesis are the peroxides.  
  The peroxide and hydroperoxides of the type which can be employed in the initiation of free radical polymerization of ethylenically unsaturated compounds can be prepared by any one of a number of standard methods. see Kirk and Othmer, Encyclopedia of Chemical Technology. 2nd Edition, Volume 14. pp. 776-794.  
 Unfortunately. peroxides generated by standard methods of preparation ordinarily yield highly concentrated products which are subject to destabilization upon storage. resulting in the formation of explosive mixtures.  
  My invention is the discovery of a process for the preparation of multifunctional peroxycarbonate ester compounds. Unlike the conventional processes used in the preparation of peroxides. the process of this invention is adaptable to the in situ generation of the peroxycarbonate ester in a suspension. solution or emulsion polymerization system. A further advantage of these initiator compounds of my invention resides in their ability to impart greater stability to the polymers whose polymerization they initiate. The polymeric segments of these initiator compounds, which become integrated into the polymer chain during the polymerization process. may also affect other physical properties of the polymer. depending upon their concentration relative to the polymer. This invention also includes the polymeric products of this process and the method for the initiation of free radical polymerization of ethylenically unsaturated compounds utilizing the multifunctional peroxycarbonate esters as the initiators in these polymerization systems.  
 SUMMARY OF THE INVENTION This invention is a process for the preparation multifunctional peroxycarbonate esters from an acid salt of a linear copolymer and a carbonate comprising mixing the acid salt of the linear copolymer of the formula 2 leanh wherein M is CH CH with R being CH at R is H.  
 or phenyl a is CH OR&#34; with R&#34; being alkyl of l to 4 carbon atoms. R is H. F. --Cl, Br or CH,, M2 lS I I R R where. 2; R and R are independently selected from H.  
 F. Cl.  
 9-0H or E- R&#39;&#34; with R&#39; being CH or -C H R and R are independently selected from -H.  
 F. Cl.  
  g- H, g- R phenyl or (N02 Ci. X)3- d.  
  with R&#34; being alkyl of l to 8 carbon atoms.  
  X is halogen. and a is an integer from 0 to 3 n1 is l to 1000 n is l to 1000. and q is 4 to 1000 with in excess of 4 moles per linear copolymer chain to stoichiometric quantities of a carbonate of the formula wherein R is alkyl of l to 7 carbon atoms. alkenyl of l to 4 carbon atoms. aryl or substituted aryl, and  
  X is halogen in a reaction medium. comprising water or mixtures of water and lower alkyl alcohols under oxidizing conditions at temperatures ranging from about ]C. to that temperature immediately below the thermal decomposition point of the multifunctional peroxycarbonate ester for an interval of about I to 60 minutes.  
  In the preferred process of this invention, the reactants are salts of ethylene-acrylic acid copolymers, styrenemaleic anhydride, vinyl ether-maleic anhydride. and carbonates such as ethylene chlorocarbonate or ethylchlorocarbonate. Ordinarily. in those processes in which the reactants do not combine spontaneously at or near room temperature, the reaction temperature of the sytem should preferably be kept about to C. below the thermal decomposition point of the peroxycarbonate ester.  
  Further embodiments of this invention include a method for the initiation of the free radical polymerization of ethylenically unsaturated monomers and the peroxycarbonate ester compounds of the following structural formula wherein with R being CH C H R is H.  
  II II 0 O or phenyl R is H. CH;,, OR&#34;  
 with R&#34; being alkyl of l to 4 carbon atoms,  
  R, is H, -F, Cl, Br or ---CH,, M., is  
 where,  
 R and R are independently selected from H.  
 F. Cl.  
  with R&#39; being CH or C H R is H, -F, Cl,  
  II ll 0 O phenyl or 0L ID with R&#34; being alkyl of l to 8 carbon atoms X is halogen a is an integer from O to 3 R is alkyl of l to 7 carbon atoms, alkenyl of 1 to 4 carbon atoms, aryl or halo-substituted aryl,  
 m is l to 1000 n is l to 1000, and  
 q is 4 to 1000 DESCRIPTION OF THE INVENTION INCLUDING PREFERRED EMBODIMENTS PREPARATION OF PEROXYCARBONATE ESTERS The peroxycarbonate ester product of the process of this invention is a linear copolymer having a degree of polymerization ranging from about 4 to about 1000 and pendant peroxycarbonate ester moieties extending from the backbone of the copolymer in a random or regular sequence depending upon the specific arrangement of the various monomers in the copolymer.  
  The peroxycarbonate ester compounds of this invention are prepared by the reaction of an acid salt ofa linear copolymer with a carbonate in an aqueousreaction medium under oxidizing conditions.  
 REACTANTS Copolymer Salt The copolymer salt reactant of the process of this invention can itself be prepared by reaction of an acid functional copolymer with the free cations in a basic aqueous solution. The conversion of the acid functional group(s) of the copolymer to the corresonding salt can be brought about by first dissolving the copolymer in an aqueous solution containing a base. such as sodium hydroxide. The concentration of the base with respect to the copolymer should be carefully adjusted in order to insure some solubility of the acid functional copolymer. Addition of base in excess of that amount required to establish a solubility equilibrium will result in various undesirable side reactions upon the subsequent addition of the carbonate. This generation of carboxylate ions from the corresponding carboxylic acid follows well known acid dissociation patterns, Roberts and Caserio, Basic Principles of Urganic Chemislr Chapter 16, W. A. Benjamin, IIKL,  
 New York (I965).  
  The acid functional copolymers which dissociate in basic aqueous solutions to form the corresponding salt reactant of this process are themselves prepared by standard polymerization techniques. The various methods used in the preparation of the copolymers of the acid salt reactants of the process of this invention are well known and described in the literature. Sorenson and Campbell, Preparative Methods of Polymer Chemistry, lnterscienee Publishers Inc., New York (1962).  
  The relative arrangement of the monomeric components in the backbone of the copolymer salt reactants of the process of this invention will, of course. be determined by the relative reactivity ratios of the monomers used in the preparation of the specific copolymer. For example, preparation of copolymers from two monomers whose corresponding free radicals prefer to react exclusively with its opposite number in the polymerization system. will yield a copolymer having a regularly alternating arrangement of monomeric components along its backbone, irrespective of the relative proportions of each monomer in the monomer feed. The free radical polymerization of ethylene with fumaric acid or maleic anhydride is representative of the preparation of alternating copolymer salt reactants of this invention. In sharp contrast. the preparation of copolymers from monomers which do not prefer to react exclusively with the other monomers in the system, will result in copolymers having their monomeric components randomly arranged along their respective backbones. In those instances where the disparity between the relative reactivity ratios of the monomers is great, the resulting copolymer will have a correspondingly disparate ratio of one monomer to the other. The preparation of copolymers from monomers having different reactivity ratios can, to some degree, be controlled by controlling the relative concentration of the monomers in the reaction system. The kinetics of copolymerization fo monomers having similar and widely varying reactivity ratios has been studied extensively, and the technical literature is replete with articles fully describing such phenomenon. See F. W. Billmeyer. Textbook of Polymer Science, Chapter 1 l, lnterscienee Publishers. New York (I966) and accompanying bibliography. Copolymer salts prepared from ethylene-acrylic acid copolymers are illustrative of the random copolymerzation of monomers having disparate reactivity ratios.  
  The acid functional copolymers which can be used in the preparation of the salt reactants of the process of this invention can be represented by the following structural formula -c-on or c-dw II II o o R being C H R2 iS H,  
  \t n O O or phenyl R3 IS H, &#34;CH3, OR  
  with R&#34; being alkyl of l to 4 carbon atoms, R, is H, F. Cl, -Br or CH;;  
  I I R R where.  
 R and R are independently selected from H, --F. -Cl,  
  with R&#39; being CH;; or C H R and R are independently&#39;selected from H,  
 F, Cl,  
 (migh ok with R&#34; being alkyl of l to 8 carbon atoms. X is halogen. and a is an integer from 0 to 3 m is l to I000 n is I to 1000 q is 4 to 1000 Copolymers having the above structural formula which can be used in the preparation of the copolymer salt reactant of the process of this invention are the copolymers of ethylene-acrylic acid, ethylene-maleic anhydride, butadiene-acrylic acid, styrene-acrylic acid, styrene-maleic anhydride and vinyl ethermaleic anhydride.  
  The preferred salt reactants of the process of this invention are prepared from copolymers of ethyleneacrylic acid, styrene-maleic anhydride and vinyl ethermaleic anhydride.  
  Carbonate The carbonate reactant of the process of this invention can be represented by the following strucural formula phenyl or where.  
 R is alkyl of l to 7 carbon atoms, alkenyl of l to 4 carbon atoms. aryl or substituted aryl, and  
 X is halogen Carbonates of the above formula which can be used in the synthesis of the peroxycarbonate esters of this invention are ethyl and ethylene chlorocarbonate. propylchlorocarbonate. methylchlorocarbonate. their corresponding isomers and derivatives. Steric hinderance of the copolymer salt tends to indirectly limit both the size of the substituents and the degree of substitution on the carbonate reactant with which it is to react. Carbonates that are substituted with lower alkyl radicals l to 2 carbon atoms) or with aryl and substituted aryl radicals (where the degree of secondary substitution on the aryl radical is similarly limited). appear to be more sterically compatible in reaction with the various copolymer salts than more extensively substituted carbonate compounds and are. therefore. preferred in the process of this invention.  
 OXlDIZlNG AGENT The oxidizing agents which can be used in the process of this invention are the peroxides. the hydroperoxides and ozone; with hydrogen peroxide being the preferred agent of this process.  
  In those instances where ozone is selected as the oxidizing agent of choice. the ozone can be prepared simultaneous with the contacting of the reactants in separate vessels. Once generated. the ozone is bubbled through the reaction medium containing the reactants of this process.  
  In certain instances. the peroxycarbonate ester product of this invention can itself be used as an oxidizing agent for the preparation of additional peroxycarbonate ester compounds.  
 REACTION MEDIUM The reaction medium for the process of this invention can be water or mixtures of water and lower alkyl alcohols (e.g. methyl or ethyl) in any proportion.  
  In those instances in which the peroxycarbonate ester is to be generated in a polymerizing medium (suspension or emulsion systems). the reaction medium may also contain certain other materials indigenous to these systems. For example. suspension polymerization systems routinely contain dispersants to insure suspension of the monomer during polymerization. and. therefore, reaction media of this invention can also be expected to contain such typical dispersants as hydroxyethyl cellulose. hydromethyl cellulose. methyl cellulose, polyvinyl acetate. polyvinyl alcohol and gelatin, as well as other standard additives.  
 PROCESS The peroxycarbonate esters of this invention can be prepared by the reaction of a linear copolymer salt of the type previously described, with in excess of4 moles per copolymer chain to stoichiometric quantities of a carbonate under oxidizing conditions at temperatures ranging from about l5C. to temperatures as high as 200C.  
  The concentration of carbonate relative to acid salt of the linear copolymer is based on the degree of peroxycarbonate ester functionality requisite to effectively initiate polymerization of ethylenically unsaturated monomers. ln most instances. an amount of excess of 4 such functional groups per polymer chain will suffice to achieve the desired initiator activity where customary quantities of such compounds are used to initiate polymerization. The range of concentrationof carbonate relative to the acid salt of the linear copolymer in the process of this invention can. therefore. range from in excess of 4 moles per linear copolymer chain to stoichiometric quantities.  
  The temperature required to shift the equilibrium of the reaction mass in favor of peroxycarbonate ester formation varies directly with the particular combination of reactants in the system. In some instances. the reactants combine so&#39;rapidly at room temperatures, that the system must be chilled and maintained at about 1 5C. in order to contain and maintain control of such reaction. In sharp contrast, where the copolymer salts are only slightly soluble in their reaction medium. elevated temperatures, often as high as 100C. are required to shift the equilibrium of the reaction system in favor of peroxycarbonate ester formation. Often at such elevated temperatures. the boiling point of the reaction medium is exceeded, and. therefore, the system must be pressurized to keep the fluid media of the system from evaporating.  
  With limited exception, the thermal decomposition point of most of the peroxycarbonate ester compounds of this invention fall within the temperature range of about 30 to 100C. In the preferred processes of this invention. the reaction temperature of the system should range from about l0 to l5C. below thermal decomposition point of the peroxycarbonate ester being prepared.  
  The order of addition of the reactants to the reaction medium does not appear to be of critical importance nor does it appear necessary to agitate the reaction system in order to cause combination of the reactants. Howevensome agitation may prove helpful to facilitate such combination and thereby reduce reaction time.  
  The volume of reaction medium relative to the concentration of the reactants will vary depending upon whether or not the peroxycarbonate ester is to be generated in situ in a polymerization system or whether it is to be prepared independent of such system. In the former case, the concentration of the peroxycarbonate ester initiator in such a polymerization system will not ordinarily exceed 1% based on the volume of the reaction medium in the system. Whereas, the preparation of the peroxycarbonate ester independent of such a polymerization will ordinarily involve substantially less reaction medium. especially where the solubility of the copolymer permits the use of less. The volume of reaction medium in this latter instance can often be equivalent to the volume of reactants in the system and will seldom exceed about two fold the volume of such reactants.  
  ln those circumstances where the peroxycarbonate ester is to be generated in situ and subsequently initiate free radical polymerization of the ethylenically unsaturated monomer. the copolymer salt can be first generated in the reaction vessel. and then reacted with the carbonate and oxidizing agent. It may be advisable in certain instances. not to add the other components of the polymerization system to the reaction vessel until after the peroxycarbonate ester has been formed. in order to avoid destabilization of the peroxide groups of the peroxycarbonate ester. Subsequent to formation of this initiator compound. the various other components of the polymerization system can be freely added without risk of destabilization.  
  Where the peroxycarbonate ester is generated independent ofa polymerization system. it can be separated from the reaction medium by starving the system of solvent and thereby precipitating the polymer. In most instances the peroxycarbonate ester is separated by evaporation of a reaction medium under a vacuum or by simple filtration techniques.  
  Formation of the peroxycarbonate ester in situ in a polymerization system can proceed in the manner described above with the only minor variant being the composition of the reaction medium. Once the peroxycarbonate ester has been formed, the monomer can then be added and the system subsequently heated to a temperature at or above which the peroxycarbonate ester decomposes to form free radicals which in turn initiate free radical polymerization of the monomer. The monomer can also be added to the polymerization system containing a linear copolymer salt and a carbonate prior to the generation of the peroxycarbonate ester. if the synthesis of the peroxycarbonate ester is carried out at temperatures at or above the thermal decomposition point of such compound. the peroxycarbonate ester will immediately decompose upon formation to form free radicals. These free radicals will then combine, as they are formed. with monomer and form monomer chain radicals.  
  The rate of polymerization of the monomer within the system will vary directly with the square root of initiator concentration and the temperature of the system. Under normal reaction conditions. the concentration of monomer chain radicals within such a polymerization system will assume a steady state&#34;. such that the rate of their disappearance through termination will equal their rate of formation. activation The peroxycarbonate esters of this invention are also sensitive to photochemical destabilization upon exposurer to ultra violet (UV) light. Of course. the specific wavelength which can most efficiently cause decomposition of the peroxycarbonate ester to free radicals will shift with the variations in absorption of the specific peroxycarbonate ester; each such compound having a greater sensitivity to certain wavelengths of light. The amount of UV energy required to activate, decompose or destabilize the covalent bonds of the peroxide groups in the peroxycarbonate ester will also be dependent upon the relative stability of the peroxide functional group. Activation. decomposition or destabilization of the initiator compound of the process of this invention can occur over a broad band of UV wavelengths; however. the interval required for such activation will be most abbreviated at wavelengths of greater absorption.  
  Both the wavelength of the activating light source and interval required for exposure to such irradiation can be determined by simple experimental techniques. if such data is not so available in the technical literature.  
  The concentration of initiator free radicals in the polymerization system can also be controlled by the decomposition of the initiator prior to the addition of the monomer. However. an unusually high concentration of initiator radicals within a polymerization system will ordinarily result in formation of polymers having a very low degree of polymerizaton.  
  The amount of peroxycarbonate ester compound. therefore. needed to effectively initiate free radical polymerization of ethylenically unsaturated monomer will vary with the relative reactivity of the monomer. the temperature of the particular polymerization system and the presence or absence of monomer during clecomposition of the initiator compound.  
 PHYSICAL PROPERTIES AND UTILITY The peroxycarbonate esters of this invention are linear copolymers having a degree of polymerization from about 4 to about 1000. The degree of polymerization and the respective molecular weights of these copolymers can be calculated by vapor pressure osmometry or other standard techniques. The frequency and arrangement of pendant peroxycarbonate ester functionality will of course vary with the random or alternating arrangement of the monomers in the polymeric chain.  
  Since the peroxycarbonate esters of the invention readily undergo thermal and photochemical degradation to form free radicals, they are highly effective as a source ofinitiator compound in the polymerization of olefinic and vinyl monomers in emulsion, solution, suspension and bulk polymerization systems. These peroxycarbonate esters are also highly effective in the initiation of the cross-linking of linear polymer chains and can themselves serve as a link between such adjacent polymeric chains. The peroxycarbonate esters themselves are also useful in the formation of highly branched polymer structures.  
  The following examples further exemplify the process, compositions and methods of this invention. Parts and percentages where appearing in such examples are by weight unless otherwise stipulated.  
 EXAMPLE I Five parts ofa 25 weight percent solution ofa sodium salt of ethylene-acrylic acid copolymer (4:1 ratio) are added to a three neck flask containing 1600 parts water. 24 parts of a 5 percent solution of hydroxyethylcellulose and 0.6 parts of a 50 percent aqueous solution of hydrogen peroxide. The above ingredients are mildly agitated until the solution is uniformly mixed. After the copolymer is uniformly dispersed throughout the aqueous solution. 0.5 parts of ethylchlorocarbonate is added. The ethylchlorocarbonate and copolymer react quite rapidly to form the multifunctional peroxycarbonate ester product. The multifunctional peroxycarbonate ester is separated from the reaction mass by filtration. washed and air dried. The peroxycarbonate ester can now be added to a reactor containing ethylenically unsaturated monomer. or the monomer can be added directly to the above reaction mass containing the multifunctional peroxide.  
  In the latter type of situation. the reactor containing the multifunctional peroxycarbonate ester is first purged with nitrogen, sealed and then 400 parts by weight vinyl chloride monomer added. The reactor is heated to F. with agitation for a period of about 4 /2 hours. The reaction product, polyvinyl chloride. is separated from the reaction mass by filtration. washed with distilled water and air dried.  
 EXAMPLE ll Following the general procedure of Example 1, a multifunctional peroxycarbonate ester is prepared from stoichiometric amounts of a sodium salt of a vinyl ether-maleic anhydride copolymer and ethylchlorocarbonate.  
 EXAMPLE 111 Following the general procedure of Example I. a multifunctional peroxycarbonate ester is prepared from stoichiometric amounts of a sodium salt of a styrenemaleic anhydride copolymer and ethylchlorocarbonate.  
 EXAMPLE IV Following the general procedure of Example I. a multifunctional peroxycarbonate ester is prepared from stoichiometric amounts of a sodium salt of a ethylenemaleic anhydride copolymer and ethylchlorocarbonate.  
 EXAMPLE V Following the general procedure of Example I. a multifunctional peroxycarbonate ester is prepared from stoichiometric amounts of a sodium salt of a styreneacrylic acid copolymer (4 to 1 ratio) and ethylchlorocarbonate.  
 EXAMPLE Vl Following the general procedure of Example I. a multifunctional peroxycarbonate ester is prepared from stoichiometric amounts of a sodium salt of a vinyl ether-maleic anhydride copolymer and ethyclorocarbonate.  
 What is claimed is:  
  l. A process for the preparation of a linear copolymer having pendant peroxycarbonate ester functionality from an acid salt of a linear copolymer and a carbonate. which comprises:  
 mixing the acid salt of a linear copolymer of the for- CH-C- or -CH -C=CHCH where.  
 R is H,  
 or phenyl R3 H, CH3, OR  
  with R&#34; being alkyl of l to 4 carbon atoms. R; is H. -F. Cl. Br or CH;; M2 is where. R and R are independently selected from H. F. Cl,  
 10 C-OH or -C-OR&#34;&#39; n v n 0 0 H with R being CH or -C H R and R; are independently selected from H F, Cl.  
  C-OH, -c-o u u 0 0 phenyl or with R being an alkyl of l to 8 carbon atoms.  
  a is 0 to 3. and X is a halogen m is l to 1000 n is l to 1000 q is 4 to 1000 with a carbonate of the formula R -O-E-X wherein R is an alkyl of l to 7 carbon atoms, alkenyl of l to 4 carbon atoms, aryl or substituted aryl. and X is halogen in a reaction medium, comprising water or mixtures of water and lower alkyl alcohols and in the presence of hydrogen peroxide or ozone at temperatures ranging from about l5C. to 200C. so as to form said linear copolymer having pendant peroxycarbonate ester functionality.  
  2. The process as defined in claim 1, wherein the linear copolymer salt is derived from an ethylene-acrylic acid copolymer.  
 3. The process as defined in claim 1, wherein the linanhydride copolymer.  
  4. The process as defined in claim 1, wherein the linear copolymer salt is derived from a styrene-acrylic acid copolymer.  
  5. The process as defined in claim 1, wherein the linear copolymer salt is derived from a styrene-maleic anhydride copolymer.  
  6. The process as defined in claim 1, wherein the linear copolymer salt is derived from a vinyl ether-maleic anhydride copolymer.  
  7. The process as defined in claim I wherein the carbonate is ethylene chlorocarbonate.  
 &#39; ear copolymer salt is derived from an ethylene-maleic 8. The process as defined in claim 1, wherein the carbonate is ethylchlorocarbonate.  
  9. The process as defined in claim 1 wherein hydrogen peroxide is employed.  
  10. The process as defined in claim 1. wherein the mixture of acid salt of a linear copolymer and carbonate are heated to a temperature about 150C. below the thermal decomposition point of the multifunctional peroxycarbonate ester.  
  ll. A method for the initiation of free radical polymerization of ethylenically unsaturated monomers with a peroxycarbonate ester. comprising:  
 a. contacting an ethylenically unsaturated monomer in an aqueous medium with an effective polymerization initiating amount ofa linear copolymer having pendant peroxycarbonate ester functionality produced in accordance with the process of claim 1 b. generating free radicals by destabilization of peroxide groups of said linear copolymer having pendant peroxycarbonate ester functionality.  
  12. The method for the initiation of free radical polymerization as defined in claim 11, wherein free radicals are generated by thermal destabilization of the peroxide groups of the peroxycarbonate ester by heating at temperatures sufficient to cause cleavage of peroxide bonds.  
  13. The method for initiation of free radical polymerization as defined in claim 11, wherein free radicals are generated by photochemical destabilization of the peroxide groups of the peroxycarbonate ester by exposure to ultra violet light for an interval sufficient to cause cleavage of peroxide bonds.  
  [4. The method for the initiation of free radical polymerization as defined in claim 11, wherein the peroxycarbonate ester is the product of the reaction ofa stoichiometric amount of a linear copolymer salt of ethyleneacrylic acid and a stoichiometric amount of ethylchlorocarbonate.  
  15. The method for the initiation of free radical polymerization as defined in claim 11, wherein the peroxycarbonate ester is the product of the reaction of a stoichiometric amount of a salt of an ethylene-maleic anhydride copolymer and a stoichiometric amount of ethylchlorocarbonate.  
  16. The method for the initiation of free radical polymerization as defined in claim 11, wherein the peroxycarbonate ester is the product of the reaction of a stoichiometric amount ofa salt ofa styrene-acrylic acid copolymer and a stoiehiometric amount of ethylchlorocarbonate.  
 17. The method for the initiation of free radical polymerization as defined in claim 11, wherein the peroxycarbonate ester is the product of the reaction of a stoichiometric amount of a salt of a styrene-maleic anhydride copolymer ad a stoichiometric amount of ethylchlorocarbonate.  
  18. The method for the initiation of free radical polymerization as defined in claim 11, wherein the peroxycarbonate ester is the product of the reaction of a stoichiometric amount of a salt of a vinyl ether-maleic anhydride copolymer and a stoichiometric amount of ethylchlorocarbonate.  
 19. As a composition of matter a linear copolymer &#39;having pendant peroxycarbonate ester functionality said composition being the product of the process of claim 1.  
  20. The composition of claim 19 wherein said acid salt of a linear copolymer is an acid salt of a linear copolyer of acrylic acid with ethylene or styrene.  
  21. The composition of claim 19 wherein acid salt of a linear copolymer is an acid salt of a linear copolymer of maleic anhydride with styrene, ethylene, or vinyl ether. I  
  22. A method for the preparation of a linear copolymer having pendant peroxycarbonate ester functionality capable of initiating free radical polymerization which comprises reacting in a aqueous medium an acid salt of a linear copolymer having pendant acid functionality with a carbonate of the formula wherein R is an alkyl of l to 7 carbon atoms, alkenyl of l to 4 carbon atoms, aryl or substituted aryl. and X is halogen. and wherein said reacting is done in the presence of ozone or hydrogen peroxide at a temperature and for a time sufficient to form said linear copolymer having pendant peroxycarbonate ester functionallty.  
  23. As a composition of matter the reaction product of claim 22.  
  24. In a method for the initiation of free radical polymerization of ethylenically unsaturated compounds wherein a free-radical polymerizable, ethylenically unsaturated monomer is polymerized in the presence of peroxy. free-radical initiator. the improvement wherein said initiator is a linear copolymer having pendant peroxycarbonate ester functionality produced in accordance with a method of claim 22.  
  UNITED STATES PATENT OFFICE CERTIFICATE OF CORRECTION 5 PATENT NO. 5,879,555  
 DATED April 22, 1975 INVENTOR(S) James E. Crawford It is certified that error appears in the above-identified patent and that said Letters Patent p are hereby corrected as shown below:  
 Column 1, line 62 after &#34;preparation&#34; insert of Column 5, line 34, &#34;0&#34; should be of Column 6, line 10, before the formula &#34;B B insert 7-- M is Column 7, line 59, &#34;of&#34; should be in Column 9, at about line 30, delete &#34;activation&#34; after end of sentence.  
  Claim 10, column 15, line &#39;7, 150 C. should be 15 C.  
 Claim 20, column 14, line 18, &#34;copolyer&#34; should be copolymer Signed and Scaled this p Thirty-first Day-0F August 1976 Arrest:  
 p RUTH c. MASON c. MARSHALL DANN Arlesrrng Officer Commissioner oflarems and Trademarks