Abstract:
Disclosed is a thermally stable liquid negative developer comprising an organic liquid carrier, a pigment, a stabilizing gel on the borderline of solubility in the carrier, a latex which imparts a fixative function to the developer, and a two component charge control agent. The charge control agent consists of a first polymer, soluble in the carrier, having a basic character because of the inclusion of pyrrolidone or hydroxylated alkyl groups, and a second polymer, insoluble or on the borderline of solubility in the carrier, having an acid character because of the inclusion of free halogenated groups, and containing a minor amount of carrier soluble moieties. The two components may constitute separate ingredients, or either or both components may be incorporated into the structure of other developer components. Thus, the basic component may be included in the gel, and the acid component included in the latex. The image density of copies produced with the developer remains at optimum levels although the developer is subjected to elevated temperatures in storage or use.

Description:
BACKGROUND OF THE INVENTION 
     This invention relates to electrostatic developer compositions. More particularly, it relates to liquid developer compositions of improved storage and thermal stability. 
     Conventional liquid negative developers for use in electrostatic copying machines consist of an organic nonpolar liquid carrier having a low dielectric constant and a high resistivity containing a toner comprising a solid particulate resinous fixative and a pigment or pigment system. A charge control agent and one or more substances for enhancing the shelf-life of the composition and for maintaining the various solid components as a homogeneously dispersed phase are also included. When a substrate containing a latent electrostatic image is brought into contact with the developer composition, charged components of the developer are attracted preferentially to the oppositely charged latent image and subsequently fixed, typically by the application of heat to evaporate the carrier, to produce a permanent visible image. 
     In an ideal developing composition, the fixative and pigment should be intimately associated, of uniform small particle size, and should be uniformly charged. This would result in uniform depletion of the toner as images are developed sequentially and in uniform density of the successively produced copies. In practice, this ideal property of developing compositions has been difficult to achieve. The static charge imparted to the solid particles in such a composition by the charge control agent is typically a function of the chemical properties of the agent and the toner particles and of the surface area of the particles. 
     Known negative charge agents for liquid developer systems consist of polymers that contain large amounts of electron accepting groups (acid character) such as halogens, e.g., polyvinyl chloride and chlorinated polyethylenes, polypropylenes, or polyisoprenes. These associate with the resinous fixer and pigment components in the developer. In an electric field the charge agent and associated pigment and fixer (latex) take on a net negative charge and migrate to anodic areas of the latent image-bearing substrate. 
     The use of a separate polymeric component of this type as a charge control agent has an adverse effect on the stability of the developer with respect to changes in temperature in use or storage. More particularly, if the developer is subjected to a temperature substantially above room temperature, the solubility of the charge control agent in the carrier is increased. It has been discovered that this has the effect of allowing the polymer to relax thereby reducing steric hindrance to the uptake of negative charge, with the result that the electronegativity of the developer increases. When such a developer is used the resulting image exhibits a halo effect, that is, the edges of the image taper off to background rather than exhibit a sharp cut-off. Furthermore, upon cooling the developer back down to the temperature at which it is designed to operate, the charge control agent tends to separate itself from other components resulting in a deleterious reduction in homogeneity. 
     The majority of liquid developer compositions contain vehicle-soluble charge control agents, and since the charge control agent is depleted to a lesser extent than the fixative and pigment, as successive copies are produced the net charge on particles remaining in the developer varies in a complicated way resulting in variations in the image density of the successively produced copies. While this depletion effect can be substantially reduced by employing a carrier insoluble charge control agent such as those disclosed in copending U.S. application, Ser. No. 109,393 filed Jan. 3, 1980, now U.S. Pat. Nos. 4,306,009, and 103,544 filed Dec. 13, 1979, now abandoned, developers using such an approach are nevertheless subject to the thermal instability problem noted above. 
     SUMMARY OF THE INVENTION 
     The developer and imaging process of this invention substantially reduce the foregoing problems by virtue of the novel charge control agent composition of a nature hereinafter described. Broadly, the improvements in depletion properties and thermal stability of developers manufactured in accordance with the teachings disclosed herein may be traced to an intimately associated two-component polymeric mixture which serves a charge control function. The two components may constitute separate ingredients, or either or both of the components may be incorporated into the structure of other developer components. The two-component mixture includes a carrier-soluble component comprising moieties of a weakly basic character such as hydroxylated alkyl groups or pyrrolidone, and a carrier insoluble component which comprises some carrier soluble moieties and moieties of an acidic character such as halogen groups, preferably chloride groups. The polymers together form a non-aqueous dispersion which, because of the inclusion of the carrier soluble components, is relaxed in the carrier at storage and use temperatures and is resistant both to temperature change induced losses of homogeneity and to changes in the negative charge carrying properties of the charge control agent. 
     Broadly, the developer of the invention comprises an organic liquid carrier having a resistivity greater than 10 9  ohm-cm and a dielectric constant less than 3, a pigment (or pigment system), a stabilizing gel on the borderline of solubility in the carrier, a latex, and a dual component charge control agent comprising a mixture of a first polymer, soluble in the carrier, containing multiple moieties of basic character, and a second polymer, insoluble or on the borderline of solubility in the carrier, containing multiple halogenated moieties of acid character and at least a minor amount of carrier soluble moieties. The first polymer may be added as a separate ingredient, but preferably is designed to have a dispersion stabilizing function, i.e., constitutes a portion of the structure of the gel or a &#34;gelatex&#34; of the type disclosed herein. The second polymer, in addition to its role in providing charge control, preferably constitutes a portion of the structure of the latex, or fixative, component of the developer. 
     The first polymer making up the charge control agent mix may comprise a major amount of monomer units 
     (A) having the structural formula: ##STR1## and a minor amount of monomer units (B) having the structural formula: ##STR2## and/or: ##STR3## where R is CH 3  or H, Z is a hydrocarbon chain having 8-20 carbon atoms (soluble in the carrier), and Y is a hydroxylated alkyl group. A suitable monomer (A) is lauryl methacrylate. A suitable monomer (B) is hydroxypropyl methacrylate and/or vinyl pyrrolidone. Preferably, polymer units A and B are copoylymerized together with a monomer having a polymerization reaction rate intermediate that of lauryl methacrylate and hydroxypropyl methacrylate such as butyl methacrylate. It is also preferred to include a divinyl monomer in the reaction mixture to produce a multiply branched, covalently crosslinked polymer structure. A suitable divinyl compound for this purpose is ethylene glycol dimethacrylate. The currently preferred copolymer comprises, by weight, between about 0.5% and 2.5% monomer units B. This component may be present in the developer composition as a separate component in addition to the latex and stabilizers. Alternatively it may comprise the gel component of a gelatex of a nature hereinafter described. 
     The second polymer in the two-component charge control agent comprises a minor amount of carrier-soluble monomer (C) such as monomer units having the structural formula: ##STR4## a minor amount of monomer units (D) for imparting acidic properties to the polymer such as halogenated dienes having 3-4 carbon atoms (e.g., chlorinated isoprene) or halogenated vinyl compounds, and a major amount of carrier-insoluble monomer units (E) having the structural formula: ##STR5## wherein R is H or CH 3 , Z is a hydrocarbon chain having a 8-20 carbon atoms, and A is: ##STR6## where n is 1-6. Preferred halogenated vinyl compounds (D) include compounds having the structural formula: ##STR7## wherein R is H or CH 3 , G is chloride or bromide, and B is H, alkyl having 1-6 carbon atoms, halogenated alkyl having 1-6 carbon atoms, phenyl, lower alkyl (C 1  -C 6 ) substituted phenyl, or acyl chloride or bromide. Acryloyl chloride, methacryloyl chloride, cinnamoyl chloride, crotonyl chloride, fumaryl chloride, and mixtures thereof may be used. 
     The preferred carrier-insoluble monomer units (E) are methyl and/or methyl and butyl methacrylate. 
     Broadly, about 0.1% to 5% of the total weight solids in the developer should comprise hydroxylated alkyl or pyrrolidone monomer units, and about 0.1% to 30% should comprise halogenated acid character monomer units. When a separate gel is employed and the second, chlorinated component functions both as a charge control agent and a latex, the preferred ranges of basic polymer units and acid polymer units of the type disclosed herein are 0.3%-1.2% and 0.6%-1.3%, respectively. In the developer embodiment employing gelatex, the preferred ranges are 1.4%-3.2% for the basic monomer units, and 5%-21% for the chlorinated monomer units. 
     It is an object of the invention to provide a liquid negative developer composition having a novel and improved charge control agent. Another object is to provide a developer composition which is resistant to time and temperature change-induced alterations in charge control properties. Another object is to produce a liquid negative developer of improved storage stability. Yet another object is to provide a developer of the type described and an imaging process which is characterized by improved image density depletion properties as successive copies are produced. These and other objects and features of the invention will be apparent of the following description and from the claims. 
    
    
     DESCRIPTION 
     Broadly, the several objects of the instant invention are accomplished by providing a liquid developer which essentially consists of a carrier or vehicle, a pigment or pigment system, a gel which comprises a resinous material on the borderline of solubility in the vehicle at the temperature of use and also has an affinity for the latex, a latex, and a resinous charge control agent comprising a mixture of two copolymers which have a significant affinity for each other. The two-component charge control agent comprises a mixture of a first polymer, soluble in the carrier, which contains multiple hydroxylated alkyl groups or pyrrolidone groups, and a second polymer, insoluble in the carrier, comprising a minor amount of carrier soluble moieties and multiple groups having moieties of acid character, i.e., halogens. 
     The carriers useful in the composition of the invention are nonpolar solvents or solvent systems of the type conventionally used in prior art liquid developers. The carrier will have a resistivity greater than about 10 9  ohm-cm and a dielectric constant less than about 3. As known to those skilled in the art, it will be characterized by an evaporation rate suitable for rapid, e.g., two second, evaporations from the substrate to be developed when exposed to temperatures below which paper is charred. It will preferably be free of aromatic liquids and other excessively toxic or corrosive components. Also, as is known, it should have a viscosity low enough to permit rapid migration of particles which are attracted to the electrostatically charged image to be developed. Typically, the viscosity of the vehicle may range between about 0.5 and 2.5 centipoise at room temperature. 
     Nonlimiting examples of suitable carriers include petroleum fractions which are substantially odorless, relatively inexpensive, and commercially available such as those sold by Humble Oil and Refining Company under the trademarks ISOPAR G, ISOPAR H, ISOPAR K, and ISOPAR L. These materials comprise various mixtures of about C 8  -C 16  hydrocarbons. 
     The pigment or pigment system employed in the composition of the invention is also conventional. The preferred method of imparting color to the toner particles is to use a fine solid particulate pigment in combination with one or more dyes which associate with the composition&#39;s resinous components. Carbon black particles in the submicron range are preferred, but powdered metals and metal oxides may also be used. Various dyes of recognized utility in imparting color to vinyl resins may be used in combination with the particulate pigment. The presently preferred pigment system for use in the composition of the invention comprises Printex 140u, a carbon black sold by Degussa Inc. having a mean particle size of 0.029 microns, plus alkali blue (BASF Wyandotte), monarch green (Herculese Inc.), and cromophtal red (Ciba-Giegy). 
     A polymeric gel which stabilizes the developer dispersion is also included therein. The gel is designed to be both compatible with the vinyl components of the latex and to be on the borderline of solubility-insolubility in the organic nonpolar carrier. It comprises, as an essential component, a polymer or a copolymer containing a major amount of monomer units selected from the group consisting of C 8  -C 20  esters of acrylic or methacrylic acid. This developer component has a molecular weight in the range of 10 3  to about 10 6  and swells when mixed with non-polar organic carriers of the type described above. Such C 8  -C 20  alkyl esters may be homopolymerized or copolymerized with each other or various other vinyl type monomers. Nonlimiting examples of suitable comonomers include vehicle insoluble monomers such as lower alkyl esters of acrylic and methacrylic acids, provided that the ratio of the monomers is low enough such that solvation of the resulting copolymer in the vehicle is assured. Other useful compounds include glycidyl methacrylate or acrylate, crotonic, maleic, atropic, fumaric, itaconic, and citraconic acids, acrylic, methacrylic, and maleic, anhydrides, acrylonitrile, methacrylonitrile, acrylamide, hydroxy ethyl methacrylate and acrylate, hydroxy propyl methacrylate and acrylate, dimethyl amino methyl methacrylate and acrylate, allyl alcohol, cinnamic acid, methallyl alcohol, propargyl alcohol, and mono and dimethyl maleate and fumarate. 
     Suitable methods of synthesizing gels of the type described above for use in the developer system of the invention are set forth below. 
     PREPARATION OF SOLUBLE MULTIPOLYMER GEL PRECURSORS 
     A. 800 g of lauryl methacrylate and 3.54 g of benzoyl peroxide are added to 1.3 liters of Isopar G in a 5 liter flask where the temperature is maintained between 80° and 95° and allowed to react for 6 hours under a nitrogen atmosphere to form a lauryl methacrylate homopolymer. The overall reaction concentration is about 40%, and about a 95% conversion to the polymer is achieved. 
     B. The procedure of A is repeated except that 40 g of glycidyl methacrylate is included in the reaction flask and a 20:1 poly (lauryl-glycidyl) methacrylate copolymer is produced. Less than about 10% of the originally added monomers remain unreacted. 
     C. The procedure of B is repeated. Next, 40 g of methacrylic acid and 0.54 g hydroquinone are added to the polymer solution and the solution is maintained at about 93° C. for 12-15 hours to form a small amount of hydroquinone-methacrylic acid complex. 
     D. The procedure of C is repeated except that 20 g of acrylic acid are substituted for the 40 grams of methacrylic acid. A 20:1 poly (lauryl-glycidyl) methacrylate copolymer and a complex of hydroquinone and acrylic acid are produced. Polymer yield is on the order of 90+%. 
     E. The procedure of C is repeated except that 10 g of crotonic acid are substituted for the 40 grams of methacrylic acid. A 20:1 poly (lauryl-glycidyl) methacrylate copolymer and a complex of hydroquinone and crotonic acid are produced. Polymer yield is on the order of 90+%. 
     F. The procedure of C is repeated except that 20 g of methacrylic acid is substituted for the 40 grams of methacrylic acid. A 20:1 poly (lauryl-glycidyl) methacrylate copolymer and a complex of hydroquinone and methacrylic acid are produced. 
     GEL PREPARATION 
     G. 40 g of methacrylic acid and 0.5 g of hydroquinone are added to 1 liter of Isopar G and maintained at about 90° C. for about 10 hours. Next, 40 grams of lauryl methacrylate, 18 g methyl methacrylate, and 0.5 g benzoyl peroxide are added to the reaction flask to initiate polymerization. Polymerization is continued for five hours to produce a methacrylic acid-lauryl methacrylate-methyl methacrylate terpolymer. The terpolymer solution/dispersion is added to about 100 grams of soluble precursor A and ball milled to produce a substantially homogeneous gel on the borderline of solubility in Isopar G. 
     H. The procedure of G is repeated except that 100 g of soluble precursor B is substituted for precursor A. After ball milling for 10 hours, a substantially homogeneous gel on the borderline of solubility in Isopar G is produced. 
     I. 102 g (dry weight) of soluble precursor C is mixed with 18 g methyl methacrylate, 0.3 g benzoyl peroxide, and 900 ml of Isopar G and reacted in a 2 liter flask under a nitrogen atmosphere for 5 hours. A gel is formed which is on the borderline of solubility in Isopar G at room temperature. Substantially no free monomer can be detected in the reaction flask. 
     J. The procedure of I is repeated except that 100 g of precursor D is substituted for precursor C. A gel similar in properties to that described in section I is produced. 
     K. The procedure of I is repeated except that 100 g of precursor E is substituted for precursor C. A gel similar in properties to that described in section I is produced. 
     L. 84 g (dry weight) of a precursor similar to precursor C, except that only 10 grams of methacrylic acid are added after polymerization of the lauryl-glycidyl copolymer, are added to 36 grams methyl methacrylate and 0.3 g benzoyl peroxide in 900 ml Isopar G. The mix is maintained under a nitrogen atmosphere for 5 hours at a temperature of less than 80° C. A viscous gel is produced, and less than about 4% unreacted polymer can be found in the reaction flask. 
     M. 90 g (dry weight) of precursor F are added to 30 g methyl methacrylate and 0.3 g benzoyl peroxide in 900 ml Isopar G. The mix is maintained under a nitrogen atmosphere for 5 hours at a temperature of less than about 80° C. A viscous, but less gelled polymer is produced with about 93% conversion. 
     When using a gel of the type set forth above, the charge control agent components are synthesized separately in a two-stage polymerization. Preferably, the first polymer (basic character) is synthesized first, and the second polymer (acid character) which also serves as the latex component is thereafter synthesized in the presence of the first. The two component charge control agent mixtures may be produced as follows: 
     A carrier-soluble polymer containing plural weakly basic moieties, preferably in the range of 0.5% to about 2.5% by weight, is prepared from the following ingredients in, e.g., Isopar G. 
     1. A major amount of monomer having the formula: ##STR8## where R is H or CH 3  and n is 8-20 (carrier-soluble moiety) 
     2. A minor amount of monomer having the formula: ##STR9## where R is H or CH 3  and m may be 1-20 but is preferably 2 or 3 (basic moiety) 
     3. A minor amount of cross-linker having the formula: ##STR10## where R is H or CH 3 , P is 2 or 3, and R 1  is a carbon chain having 2-20 carbon atoms and may contain aromatic rings or oxygen containing moieties. 
     4. A minor amount of a monomer having the formula: ##STR11## where R is H or CH 3  and q is 3-6 (monomer of reaction rate intermediate 1 and 2) and 
     5. a free-radical initiator catalyst such as benzoyl peroxide, azobis isobutyronitrile, etc. 
     After formation of this polymer, which is soluble (preferably) or on the borderline of solubility in the carrier (depending on relative quantities of 1 vs. 2, 3, and 4 employed), the second polymer (carrier-insoluble or partially insoluble component) is prepared, preferably in the same reaction flask, from the following ingredients. 
     6. A minor amount of monomer 1 and monomers 3 or 4 or both (set forth above) to provide carrier-soluble moieties. 
     7. A minor amount of a monomer having the formula: ##STR12## where R is H or CH 3 , G is chloride or bromide, and B is H, alkyl, or Halogenated alkyl having 1-6 carbon atoms, phenyl, lower alkyl substituted phenyl, or acyl halide, or monomer 7 may consist of a halogenated monomer such as chlorostyrene or 3-chloro-1-butene. 
     8. A major amount of a monomer having the formula: ##STR13## where R is H or CH 3  and K is --COOC L  H 2L+1  (L=1-6), ##STR14## or phenyl. 
     9. a catalyst such as set forth in No. 5 above. 
     Ingredient 6 imparts partial solubility in the carrier. Ingredients 3 and 4 have reaction rates intermediate that of ingredients 1, 7 and 8 and promote complete polymerization. 
     This component contained multiple moieties of acid character (halogens), preferably chlorides, in about 0.5% to 4.0% by weight. Monomeric acids such as carboxylic, sulfonic, etc., form weak and unacceptably charged non-aqueous dispersions and should be avoided. 
     Specific examples of suitable charge control agent are set forth below: 
     EXAMPLES OF PREPARATION OF TWO-COMPONENT CHARGE CONTROL PREPARATION 
     The following ingredients are added to 5 liter flasks equipped with thermometers, stirrers, reflux condensers, and an N 2  inlet to prepare the carrier soluble basic character component. 
     
         ______________________________________I-a200    g      Lauryl methacrylate (LMA)24     g      Hydroxypropyl methacrylate (HPMA)2      g      Ethylene glycol dimethacrylate (EGDMA)760    g      Isopar G, and1.0    g      Benzoyl peroxide (BP)II-a200    g      LMA22     g      Hydroxyethyl methacrylate10     g      Butyl methacrylate (BMA)1.0    g      Azobis isobutyronitrile (AIBN)440    g      Isopar GIII-a200    g      LMA24     g      HPMA2.0    g      EGDMA1.0    g      BP760    g      Isopar GIV-a200    g      LMA11     g      HPMA2.0    g      EGDMA1.0    g      BP600    g      Isopar GV-a200    g      LMA11     g      HPMA2.0    g      EDGMA1.0    g      BP600    g      Isopar GVI-a200    g      LMA24     g      HPMA2.0    g      EGDMA1.0    g      BP600    g      Isopar G______________________________________ 
    
     Each of the reaction mixtures are heated to 90° C. while purging with N 2  for about 4 hours. The contents of the flasks are then cooled and the acid character component, which also serves as a latex, is prepared by adding to the respective flasks: 
     
         ______________________________________I-b1540     g        Isopar G430      g        Methyl methacrylate (MMA)40       g        LMA20       g        BMA26       g        Acryloyl Chloride (ACl)1.8      g        Azobis isobutyronitrile (AIBN)II-b1360     g        Isopar G430      g        MMA40       g        LMA20       g        BMA26       g        ACl1.8      g        AIBNIII-b1450     g        Isopar G216      g        MMA20       g        LMA10       g        BMA12       g        Methacryloyl chloride (MACl)1.0      g        BPIV-b1540     g        Isopar G430      g        Styrene Monomer (SM)40       g        LMA20       g        BMA22       g        Cinnamoyl Chloride (CCl)1.8      g        AIBNV-b1540     g        Isopar G380      g        Vinyl Acetate (VA)40       g        2-ethyl hexyl acrylate (EHA)26       g        Crotonyl Chloride1.8      g        AIBNVI-b1540     g        Isopar G380      g        VA40       g        EHA20       g        Fumaryl Chloride1.8      g        AIBN______________________________________ 
    
     Each of the reaction flasks is heated to about 70° C. while purging with nitrogen for 4 hours. The product is an opaque white non-aqueous dispersion containing the following weight percent solids (approximate): 
     
         ______________________________________I     II          III   IV        V   VI______________________________________22    27          16    18        16  18______________________________________ 
    
     In place of or in addition to stabilizing gels of the type set forth above, the developer of the invention may include a gelatex of the type set forth in copending application Ser. No. 109,393. The gelatex comprises a mixture of polymers which act as a fixitive and dispersant. It consists of a carrier-insoluble vinyl polymeric latex and a multiply branched vinyl polymeric gel framework which physically entraps or entangles the carrier insoluble polymer and is itself slightly soluble or on the borderline of solubility in the carrier. If the multiply branched component of the gelatex is synthesized to include a minor amount of moieties of basic character such as pyrrolidone or hydroxylated alkyl, it serves the dual roles of stabilizing the developer and providing the basic component of the charge control agent. When using such a gelatex (basic polymer constituent included), the polymer of acidic character is separately synthesized and then blended with the gelatex. Alternatively, the insoluble latex component of the gelatex may be synthesized to include halogenated groups, in which case no separate acidic polymer need be added. 
     Methods of making a gelatex wherein a basic component (vinly pyrrolidone) is included in the structure are set forth below. 
     MULTIPOLYMER PREPARATION 
     Multipolymers at about 40% solids are prepared by copolymerizing the monovinyl monomers and cross-linkers listed in Tables 1, 2, and 3. The reactions are conducted using azobis isobutyronitrile or benzoyl peroxide (as indicated) in Isopar G under a nitrogen atmosphere for about six hours after reaching 80° C. The data set forth are given in parts by weight unless otherwise specified. The reaction products are translucent solutions which exhibit the Tyndall effect, indicating that the gel is on the borderline of solubility. 
     
                                           TABLE I__________________________________________________________________________  Multipolymer NumberIngredient  1   2   3   4   5   6   7   8__________________________________________________________________________Lauryl-meth-acrylate  672.75      673 673.25              673.5                  688.25                      688.5                          697.75                              698Vinyl-Pyrroli-done   75  75  75  75  60  60  50  50Ethylene-dimeth-acrylate  2.25      2   1.75              1.5 1.75                      1.5 2.25                              2AcrylicAcidDioctyl-maleateDimethylamino-ethylmeth-acrylateAIBN.sup.1  3.75      3.75          3.75              3.75                  3.75                      3.75                          3.75                              3.75% polymerrecovery  95.5      92.5          92.7              94.3                  95.1                      93.7                          94.5                              95.2Reactionconc. (%)  40  40  40  40  40  40  40  40__________________________________________________________________________ .sup.1 Azobis isobutyronitrile 
    
     
                       TABLE II______________________________________Multipolymer NumberIngredient   9       10     11   12   13   14   15   16______________________________________Lauryl-meth-acrylate   698.25  698.5  695  696  697  696  697  696Vinyl-Pyrroli-done    50      50     50   50   50   50   50   50Ethylene-dimeth-acrylate   1.75    1.5    2    2    2    2    2    2AcrylicAcid                   3    2    1    2    1    3Dioctyl-maleateDimethylamino-ethylmeth-acrylateAIBN.sup.1   3.75    3.75   4.25 4    3.75 3.75 4.25 3.75% polymerrecovery   94.5    94.7   93.9 91.2 90.4 89.1 92.4 92.2Reactionconc. (%)   40      40     40   40   40   40   40   40______________________________________ .sup.1 Azobis isobutyronitrile 
    
     
                       TABLE III______________________________________  Multipolymer NumberIngredient    17      18      19    20    21    22______________________________________Lauryl-meth-acrylate 705     706     696   707.5 710   275Vinyl-Pyrroli-done     40      40      40    37.5  35    20Ethylene-dimeth-acrylate 5       2       2     5     5     0.6AcrylicAcid             2       2Dioctyl-maleate                  10Dimethyl-amino-ethylmeth-acrylate                             4AIBN.sup.1    3.75    4       4     3.75  3.75  1.5% polymerrecovery 90.3    92.0    92.5  90.3  91.3  86.8Reactionconc. (%)    40      40      40    40    40    40______________________________________ .sup.1 Azobis isobutyronitrile 
    
     GELATEX PRODUCTION 
     The gel polymers dispersed in isopar produced as set forth above are used as a reaction medium to conduct a latex polymerization. The amount and identity of the various monomers used and other data pertinent to the reaction are set forth below. These reactions are conducted in about 580 g Isopar G under a nitrogen atmosphere for about five hours after the reaction medium reaches 80° C. The product form described as a &#34;VIS GLT&#34; is preferred. Data are given in parts by weight unless otherwise specified. The resulting gelatex compositions comprise an opaque, viscous latex. 
     
                       TABLE IV______________________________________  Gelatex NumberIngredient    1      2      3    4    5    6    7    8______________________________________multipolymerused fromexample  1      2      3    4    5    6    7    8multipolymerconc. (%solids)  38.5   37.4   37.5 38.0 38.25                                 38.5 38.1 38.4multipolymerused (wet)    165    283.4  282  278  277  303  306  276(dry)    63.5   106    106  105.7                            106  116.6                                      116.6                                           106Methylmethacrylate    54     90     90   90   90   99   99   90Methacrylicacid     2.4    4      4    4    4    4.4  4.4  4Ethylene di-methacrylateCellolyn.sup.3WaxAIBN.sup.1    0.35   0.75   0.75 0.75B.sub.2 O.sub.2.sup.2            0.5  0.55 0.55 0.5% recovery      94.1   95.3 97.2      97.8 88.0 97.8ReactionConc. (%)    15     30     30   30   30   30   30   30Form.sup.4    GEL    VIS    VIS  VIS  GEL  VIS  VIS  VIS           GLT    GLT  GLT       GLT  GLT  GLT______________________________________ .sup.1 Azobis Isobutyronitrile .sup.2 Benzolyl peroxide .sup.3 hydroxylated wood rosin .sup.4 GEL = formation of gel  little turbidity  VIS GLT = more viscous, turbid, preferred gelatex compositions 
    
     
                       TABLE V______________________________________  Gelatex NumberIngredient    9      10     11   12   13   14   15   16______________________________________multipolymerused fromexample  9      10     11   12   13   14   15   16multipolymerconc. (%solids)  38.1   38.2   37.8 37.6 37.35                                 36.9 37.7 37.2multipolymerused (wet)    278    278    841  423  851.4                                 288  844  301(dry)    106    106    317.9                       159  318  106.2                                      318.1                                           112Methylmethacrylate    90     90     270  135  270  90   270  80Methacrylicacid     4      4      12   6    12   4    12   8Ethylene di-methacrylateCellolyn.sup.3WaxAIBN.sup.1      0.7B.sub.2 O.sub.2.sup.2    0.6           1.41 0.7  1.5  0.47 1.41 0.43% recovery    94.6   93.7   100.0                       93.8 100.0     100.0                                           99.3ReactionConc. (%)    30     30     30   18.8 30   30   25   30Form.sup.4    VIS    VIS    VIS  VIS  VIS  VIS  VIS  VIS    GLT    GLT    GLT  GLT  GLT  GLT  GLT  GLT______________________________________ .sup.1 Azobis Isobutyronitrile .sup.2 Benzolyl peroxide .sup.3 hydroxylated wood rosin .sup.4 GEL = formation of gel  little turbidity VIS GLT = more viscous, turbid, preferred gelatex compositions 
    
     
                       TABLE VI______________________________________    Gelatex NumberIngredient 16B    17     18   19   20   21   22______________________________________multipolymerused fromexample    16B    17     18   19   20   21   22multipolymerconc. (% solids)      37.2   37.3   37.7 37.2 37.4 37.2 35multipolymerused (wet) 298    284    281.2                         341.9                              284  285  191(dry)      110.8  105.9  106  127.2                              106.2                                   106  66.85Methylmethacrylate      80     90     90   108  90   90   57Methacrylicacid       8      4      4    4.8  4    4    2.5Ethylenedimethacrylate      0.5Cellolyn.sup.3                               23Wax                                          23AIBN.sup.1                                   0.5B.sub.2 O.sub.2.sup.2      0.43   0.47   0.5  0.5  0.47 0.47% recovery 98.2          99.7 99.8      88.6 86.1ReactionConc. (%)  30     20     25   25   30   22   22Form.sup.4 VIS    GEL    VIS  VIS  GEL  VIS  GEL      GLT           GLT  GLT       GLT______________________________________ .sup.1 Azobis Isobutyronitrile .sup.2 Benzolyl peroxide .sup.3 Hydroxylated Wood Rosin  (Herculese) .sup.4 GEL = formation of gel  little turbidity  VIS GLT = more viscous, turbid, preferred gelatex compositions 
    
     As a result of these reactions there are produced turbid (opaque) gelatex compositions comprising highly branched and cross-linked, vinyl pyrrolidone containing copolymer gels which act as a matrix for carrier-insoluble linear (or branched in the case of example 16B) latex polymers. The molecular weights of the polymers vary widely between about 10 3  to about 10 5 , with the soluble component on average in the 10 4  -10 5  molecular weight range. 
     If a gelatex of the type set forth above is used in place of the gel, then material prepared as described below may be used as the second polymer of acidic character. (Alternatively, materials I-VI (set forth above), but omitting basic components I-a through VI-a may be used.) To produce the acidic component for use in gelatex-type compositions, chlorine containing polymers e.g., polyvinyl chloride (homopolymers or multipolymers), polychloroprene, or chlorinated polyethylene, polypropylene, polyisoprene, etc., are grafted with a monomer or a combination of monomers of the type; ##STR15## where R is H or CH 3 , F is COOC n  H n+1  where n is 1-20, preferably 4-12, --OCOCH 3 , or phenyl. The chlorine containing monomer units preferably constitute 50-95% of the second component, most preferably 70-90%. This component is insoluble or partially soluble in the carrier. It may be prepared as follows 
     EXAMPLE A 
     To a 5 l flask equipped with a thermometer, stirrer, reflux condenser, and N 2  inlet is added: 
     
         ______________________________________433 g         Toluene740 g         chlorinated poly (isoprene)         (Parlon S-5, Hercules, Inc.)______________________________________ 
    
     The polyisoprene is dissolved with heat (to ≈60° C.) if necessary. Thereafter, the following materials are added to the flask: 
     
         ______________________________________260 g         Lauryl Methacrylate (LMA)4.0 g         Benzoyl Peroxide (BP)______________________________________ 
    
     The reaction mixture is heated to 85° C. while purging with N 2 . The temperature is maintained at 85° C. for 4 hours, during which time the color of the reaction mixture changes from dark brown to golden yellow. Next, 520 g Toluene are added with vigorous stirring, followed by slow addition of 1600 g of a gelatex (≈25% solids). 
     The toluene is then removed by vacuum and heat (≈100° C.), and the liquid content is made up with Isopar G. 
     
         ______________________________________Final Product           2064 g solids                 60.6% acid character polymer 41.3% gelatex                19.3%______________________________________ 
    
     EXAMPLE B 
     The procedure of example A is repeated, except that the 260 g LMA is replaced with 87 g of LMA and 44 g of butyl methacrylate (BMA). 
     EXAMPLE C 
     To a 5 l flask equipped with a thermometer, stirrer, reflux condenser, and N 2  inlet is added: 
     
         ______________________________________583 g       Toluene675 g       Parlon 10P (chlorinated       polypropylene from Hercules, Inc.)______________________________________ 
    
     The polypropylene is dissolved with heat (to ≈60° C.) if necessary. Thereafter, the following materials are added to the flask: 
     
         ______________________________________135 g            Butyl acrylate (BA)4.5 g            BP______________________________________ 
    
     The reaction mixture is then heated to 85° C. while purging with N 2 . The temperature is maintained at 85° C. for 4 hours, during which time the color of the reaction mixture changes from dark brown to golden yellow. Next, 975 g of toluene are added with vigorous stirring, followed by slow addition of 1125 g of a gelatex (25% solids). 
     The toluene is then removed by vacuum and heat (≈100° C.), and the liquid content is made up with Isopar G. 
     
         ______________________________________Final product           2188 g solids                 44.4% acid character polymer 31.6% gelatex                12.8%______________________________________ 
    
     EXAMPLE D 
     To a 5 l flask equipped with a thermometer, stirrer, reflux condenser and N 2  inlet is added: 
     
         ______________________________________530 g       Cyclohexanone490 g       Geon 652 (vinylidene chloride/       vinyl chloride from B. F. Goodrich       Chem. Co. supplied as a latex       which is dried in a vac oven at       80° C.)______________________________________ 
    
     The chlorinated copolymer is dissolved with heat (≈60° C.) if necessary. Thereafter the following materials are added to the flask: 
     
         ______________________________________   189 g         BA   4.2 g         BP______________________________________ 
    
     The reaction mixture is then heated to 85° C. while purging with N 2 . The temperature is maintained at 85° C. for 4 hours, during which time the color of the reaction mixture changes from dark brown to golden yellow. Next, 564 g methylethyl ketone (MEK) are added with virorous stirring, followed by slow addition of 1050 g of a gelatex (25% solids) and 518 g of Isop H. 
     The MEK and cyclohexanone are then removed with vacuum and heat (≈100° C.), and the liquid content is made up with Isopar G. 
     
         ______________________________________Final product           1975 g solids                 41% acid character polymer 27.7% gelatex                13.3%______________________________________ 
    
     Developer concentrates having improved storage and thermal stability capable of producing upwards of 10,000 copies of uniform image density may be produced from the foregoing ingredients by adding to Isopar G the following ingredients so that a dispersion containing 20-25% by weight solids is produced. 
     
         ______________________________________Ingredient             Parts by Weight______________________________________Pigment.sup.1          40-60Two-component charge control (I-VI)                  50-70(component I-b to VI-b serve as latex)Gel G, H, I, J, K, L, or M                  40-70Wood rosin.sup.2       15-25Wax.sup.3              15-25______________________________________ 
    
     A preferred composition consists of, as parts by weight solids: 
     
         ______________________________________Ingredient             Parts by Weight______________________________________Pigment.sup.1          50Two-component charge control (I-VI)                  60Gel G, H, I, H, K, L, or M                  50Wood rosin.sup.2       20Wax.sup.3              20______________________________________ .sup.1 36 parts printex 140u, 8 parts monarch green, 4 parts alkali blue, 2 parts cromophtal red. .sup.2 Cellolyn 21 (Herculese). .sup.3 FT150 (purified parrafin). 
    
     The ingredients are blended by ball milling for 20 hours in Isopar G (20% solids). 
     A developer embodying the invention using gelatex may be prepared by ball milling the following ingredients (parts by weight) in Isopar G (20% solids) for 20 hours. 
     
         ______________________________________Ingredient        Parts by Weight______________________________________Pigment.sup.1     40-60Gelatex (1-22)     60-100Acid Character Polymer.sup.2             20-40Wood Rosin.sup.3  10-30Wax.sup.4         10-30______________________________________ 
    
     Preferred developers of this type consist of the following ingredients in the following parts by weight: 
     
         ______________________________________               Parts by WeightIngredient            A     B______________________________________Pigment.sup.1         50    50Gelatex (2)           85    72Acid Character Polymer.sup.2                 25    38Wood Rosin.sup.3      20    20Wax.sup.4             20    20______________________________________ .sup.1 36 parts printex 140u (carbon black), 8 parts monarch green, 4 parts alkali blue, 2 parts cromophtal red. .sup.2 Poly LMA -- chloroisoprene produced as disclosed in Example A. .sup.3 Cellolyn 21 .sup.4 FT150 (purified parrafin). 
    
     Developers made as set forth above have been subjected to standard testing procedures in an effort to assess their storage and thermal stability. 
     Centrifuge tests are performed by adding 80 ml. of developer concentrate to centrifuge tubes and subjecting the tubes to high gravity in a centrifuge apparatus. This simulates the long term settling properties of the developer normally experienced in the field. Rating of results are as follows 1. Sedimentation--This is the amount of material that will settle to the bottom of the container. The numerical ratings refer to the percent settled with 0, indicating no settling, and 5, indicating 100% settling. 
     2. Consistency--this is a subjective rating of the softness or hardness of the material that settles during the centrifuge testing. 1 refers to a very soft cake and 5 refers to a very hard cake. 
     3. Redispersibility--This is a subjective rating of the redispersibility of the sediment. A rating of 1 indicates that simple hand shaking of the centrifuge tube will completely redisperse the sediment while a rating of 5 indicates that the sediment is hard packed and will not redisperse. 
     The lower the ratings in each of these categories, the more stable the developer in storage. 
     Set forth below are the results of centrifuge tests performed on the developers of this invention and commercially available liquid negative developers. 
     
         ______________________________________Centrifuge Evaluation     Sedimentation              Consistency                        Redispersibility______________________________________Prior ArtDevelopers  3-5        2-5       3-5DevelopersDisclosed herein       1-2        1-2       1-3______________________________________ 
    
     The cyclic temperature test is performed by subjecting the developer to cyclic temperature variations of room temperature to 125° F. and then evaluating the change in viscosity of the developers over time. This simulates the aging properties of the developer experienced during shipping and warehousing. A decrease from its initial viscosity indicates that the developer is not well stabilized and that precipitation or flocculation of solids is occurring. A substantial (greater than 10 cps) increase in viscosity indicates that the developer is gelling and will cause problems in use. A continued increase in viscosity will render the developer unfit for its intended use. 
     In the chart below, initial viscosity is the viscosity obtained before testing. Oven viscosity is the viscosity obtained after repeated heating and cooling (cooled to room temperature before reading), and aged viscosity is the viscosity obtained after an additional 24 hours. In the ideal developer, all three measurements would be identical. 
     Set forth below are the results of cyclic temperature tests performed on the developers of this invention and commercially available liquid negative developers. 
     
         ______________________________________Cyclic Temperature Evaluation    Initial Vis.              Oven Vis. Aged Vis.______________________________________Prior ArtDevelopers 16          30        80DevelopersDisclosed Herein      15          20        20______________________________________ 
    
     Other embodiments are within the following claims.