PAINTABLE ADHESION PROMOTER SYSTEM FOR POLYVINYL CHLORIDE PLASTISOLS

Abstract: Disclosed is an improved plastisol composition comprising a finely-­ divided vinyl chloride polymer, filler, a primary plasticizer, and a polyaminoamide-polyimidazoline adhesion promoter. The improvement for overcoating said plastisol with an acid catalyzed topcoat comprises a plasticizer/promoter phase which comprises said primary plasticizer, said adhesion promoter, and an effective amount of a secondary plasticizer non­ ionic solvent effective in solvating the adhesion promoter in the plasticizer/promoter phase. The plasticizer/promoter phase is pre-formed for addition with the remaining ingredient for the plastisol composition.

Description: The present invention relates to plastisols in general and in particular to improved adhesion promoter systems for polyvinyl chloride (PVC) plastisols. The present invention concerns a plastisol composition according to the pre-characterizing portion of claim 1 and a method for making a plastisol composition according to the pre-characterizing portion of claim 8. The present invention also concerns a method for coating to a metal substrate according to claim 15. Vinyl chloride homopolymers (PVC) and copolymers are widely used for the protection of metallic surfaces against corrosion, for adhering thin sheet metal constructions, and for sealing welded seams, particularly in the automotive industry. Such coatings principally are applied in the form of plasticized vinyl chloride polymers (plastisols) by a variety of techniques. Depending upon the viscosity of the PVC plastisol, its utilization can be characterized as a sealant, caulk, coating, adhesive, or other function. Since resistance to corrosion is a prime prerequisite in dealing with metal parts, the PVC plastisol should adhere to the metal part with a fair degree of tenacity; otherwise, oxidation undercutting would result. Despite the ability to control the texture of the plastisol by suitable fillers and the color by the addition of suitable tinctorial pigments, often the PVC plastisol must be overcoated with a high performance, e.g. acrylic, topcoat, especially in automotive uses of the PVC plastisol. Uniformity in visual appearance dictates such overcoating requirement typically. Another requirement of the PVC plastisol is that it be curable at short, low bake cycles. In fact, successful plastisols and organisols in the automotive industry are being called on today to be curable, dry to the touch, at baking temperatures of less than 149°C (300°F), e.g. about 135°C (275°F), with oven residence times of about 20-30 minutes. Energy costs dictate such low temperature, short baking cycles. Further, successful plastisol and organisol formulations must be economic and expel a minimum of atmospheric pollutants. While a variety of adhesion promoters have been proposed for PVC plastisols and organisols, most have suffered from a variety of drawbacks including cost, insufficient film flexibility, or the like. One class of adhesion promoters which appears to exhibit a good balance between cost, flexibility, and low temperature bake characteristics are polyaminoamide-polyimidazoline adhesion promoters, such as set forth in US-A-4 146 520. Such adhesion promoters have enabled the formulation of advantageous PVC plastisols and organisols which can be baked at temperatures as low as about 121°C (250°F). Unfortunately, the plastisols and organisols containing such polyaminoamide-polyimidazoline adhesion promoters are not readily overcoated with acid-catalyzed topcoats, especially high performance acid catalyzed acrylic automobile finishes. It is theorized that the amine value of the adhesion promoters interacts and renders ineffectual the acid catalyst in the topcoat, thus resulting in tacky films. While reduction of the level of the adhesion promoter can overcome such topcoat tackiness, loss of adhesion also can occur at such low adhesion promoter levels. Thus, there is a need in the art to enable the utilization of polyaminoamide-polyimidazoline adhesion promoters in low bake PVC plastisol and organisol compositions, yet provide the ability to overcoat such plastisols with acid catalyzed topcoats. The plastisol composition of the present invention is defined according to the characterizing portion of claim 1. The method of making the plastisol composition of the present invention is defined according to the characterizing portion of claim 8. The plastisol composition according to claim 1 is used in a method for coating a metal substrate according to claim 15. According to a preferred embodiment of the invention the adhesion promoter ranges from between 1 and 10 weight parts per 100 weight parts of the vinyl chloride polymer. For coating a metal substrate according to the present invention the proportion of the secondary plasticizer ranges preferentially from between 10 and 70 weight parts, said primary plasticizer ranges from between 20 and 200 weight parts, and said promoter ranges from between 1 and 10 weight parts, all weight parts based on 100 weight parts of said vinyl chloride polymer. The present invention is addressed to the need in the art to retain advantageous low bake properties of PVC plastisols and their requisite good adhesion to metal, yet still be able to be coated wet-on-dry or wet-on-wet by acid catalyzed topcoats. Accordingly, the present invention is directed to plastisol compositions comprising finely-divided vinyl chloride polymer, filler, a primary plasticizer, and a polyaminoamide-polyimidazoline adhesion promoter. The improvement of the present invention comprises a plasticizer/promoter phase comprising said primary plasticizer, said adhesion promoter, and an effective amount of a secondary plasticizer nonionic solvent effective in solvating said adhesion promoter in said plasticizer/promoter phase wherein the plasticizer/promoter phase is preformed for addition with the remaining ingredients of the plastisol composition. Suitable nonionic secondary plasticizer solvents include aromatic solvents and polyalkylene glycol ether solvents which are effective in solvating the polyaminoamide-polyimidazoline adhesion promoters. Another aspect of the present invention involves the method for formulating the improved plastisol compositions wherein the plasticizer/promoter phase comprising the primary plasticizer, the adhesion promoter, and the secondary plasticizer nonionic solvent is pre-formed and then such phase added to the remaining ingredients of the plastisol composition. Advantages of the present invention include the retention of low bake characteristics of the plastisol and the excellent adhesion characteristics of the plastisol. A further advantage is the ability to overcoat the plastisol wet-on-dry or wet-on-wet with an acid catalyzed topcoat (i.e. "paintability", for present purposes) which is dry to the touch at lower bake temperatures of 121°C-182°C (250°-360°F), for example. A further advantage is the ability to exhibit the foregoing advantageous characteristics while retaining the flexibility of controlling the rheological characteristics of the plastisol. A further advantage is an improved plastisol composition which exhibits excellent controlled age characteristics. These and other advantages will be readily apparent to those skilled in the art based upon the disclosure contained herein. The polyaminoamide-polyimidazoline adhesion promoters are set forth in US-A-4,146,520. Such adhesion promoters include condensation products formed between a polymerized fatty acid mixture and an excess of polyalkylene polyamine. Such adhesion promoters additionally include the foregoing condensation product further reacted with an aldehyde, a ketone, or an epoxy compound. While not intending to be bound by theory, it appears that a significant quantity of the adhesion promoter migrates to the surface of the cured plastisol While such migration does not adversely impair the performance of the plastisol, it does adversely affect the curability of acid catalyzed topcoats which then are applied to the wet (wet-on-wet) or dry (i.e. wet-on-dry) plastisol. It is believed that the amine value of the adhesion promoter reacts with the acid catalyst in the topcoat which means that the topcoat will not be fully cured at the recommended bake temperatures of about 150°C (300°F) or thereabouts. As noted above, such undesirable interaction can be mostly obviated by a reduction of the amount of adhesion promoter in the plastisol, though such reduction compromises the degree of adhesion achievable, so that this alternative is not commercially viable. The same holds true for increasing the amount of acid catalyst in the acid catalyzed topcoat. One way of viewing the result of the invention is that the adhesion promoter is rendered more compatible or homogeneous in the plastisol so that it does not overconcentrate at the film surface. Accordingly, appropriate secondary plasticizer solvents or diluents should be effective in solvating the polyaminoamide-polyimidazoline adhesion promoters. Next, such secondary plasticizer solvents should be non-ionic. Solvents rich in amine value, for example, should be avoided even though they may effectively solvate the adhesion promoters as such solvents only contribute to the problem being solved. Accordingly, nonionic solvents are recommended. Suitable nonionic solvents which solvate the adhesion promoter include aromatic solvents and polyalkylene glycol ether solvents. By "solvate", we mean that a clear, stable solution results upon the mixing of the nonionic solvent and the adhesion promoter, typically at room temperature though moderate heating may be employed. Suitable such nonionic solvents include, for example, monoisopropyl biphenyl, diethylene glycol monoethyl ether, diisopropyl biphenyl, phenylxylyl ethane, butylated biphenyl and mixtures thereof. The proportion of the secondary plasticizer solvent is adjusted to accomplish its function in the formulation. Often, this means between 10 and 70 phr (weight parts per 100 weight parts of PVC resin) nonionic solvent is used. The remaining ingredients in the plastisol are conventional and include finely-divided polyvinyl chloride homopolymers or vinyl chloride copolymers, and often blends thereof. The primary plasticizer most often will be an alkyl phthalate such as dihexyl phthalate (DHP) diisodecyl phthalate (DIDP). Alternatively, the primary plasticizer may be an alkyl adipate (e.g. di(2-ethyl hexyl) adipate). The plasticizer typically will range from 20 to 200 phr (weight parts per 100 weight parts of PVC resin). Additionally the plastisol will contain a filler for control of rheology, control of cost, and the like. Suitable fillers include, for example, calcium carbonate, glass (including hollow glass spheres), talc, chalk, barium sulfate, and the like. The fillers certainly affect paintability of the plastisol, though with the invention more flexibility in filler utilization is gained. The proportion of filler can range up to about 300 phr and the optimum will vary depending upon the type of PVC and plasticizer, and the rheology desired. Finally, thixotropic agents can be added to achieve certain plastisol rheologies and such agents include, for example, fumed silica, bentonite, metallic fatty acid soaps. Thixotropic agents typically are added in the range of about 1-5 phr. In order to maximize the paintability of the plastisol (i.e. ability to coat the plastisol with an acid catalyzed topcoat), it has been determined that a pre-blend of adhesion promoter, primary plasticizer, and nonionic secondary plasticizer solvent should be made. Such plasticizer/promoter blend then is added to the remaining ingredients for forming the plastisol. Apparently, the formation of the plasticizer/plastisol blend is more effective in compatibilizing the adhesion promoter in the plastisol or "pushing" the plasticizer into the PVC particles. Regardless of the mechanism involved, it has been determined that paintability of plastisol becomes a routine achievement when the plasticizer/promoter blend is initially formed in making the plastisol composition. The plastisol is dryable or curable at very low bake temperatures ranging on down to 121°-135°C (250°-275°F). The plastisol either can be baked and then topcoated (wet-on-dry) or the plastisol can be applied followed by the topcoat wherein both coatings then are cured in a single bake (wet-on-wet). In automotive applications, the plastisol typically is drawn down or applied onto a metal subsrate which has been primed with a corrosion-inhibiting coating. Typical topcoats include high performance acrylic topcoats which are cured by conventional acid catalysts. The following examples show how the present invention has been practiced but should not be construed as limiting. All percentages and proportions are by weight unless expressly indicated. EXAMPLES EXAMPLE 1 The efficacy of polyaminoamide-polyimidazoline adhesion promoters in PVC plastisol formulations was demonstrated on the following general formulation. Ingredient Amount (wt.-parts) Occidental 6482 (regist. TM) 60 Borden VC265 (regist. TM) 40 Dihexyl phthalate (DHP) 62.5 Diisodecyl phthalate (DIDP) 62.5 CaCO₃ 250 Varying levels of adhesion promoter were utilized as follows: Formulation No. Wt. Parts 204-65-1 10.17 204-65-2 7.13 204-65-3 4.75 204-65-4 3.56 204-65-5 2.38 204-65-6 1.19 204-65-7 0.59 The adhesion promoter was Euretek (registered TM) 580 polyaminoamide adhesion promoter (amine value of 190, manufactured under US-A-4,146,520, Sherex Chemical Company, Inc., Dublin, Ohio). Brookfield viscosity measurements were taken on each formulation initially and thereafter at various intervals of time. The following data was recorded. Advantageously, the viscosity should stabilize over time. The above-tabulated data demonstrates such viscosity stability. Each formulation was drawn down (0.50 mm (0.020 inch) coating) on primed steel panels (Uni-Prime coated panels, PPG Industries, used in all examples) and baked for 20 minutes at 121° C. Each coating had good adhesion to the panels except for 204-65-7, indicating that the promoter level was too low. The coated panels then were coated with a white enamel paint (an automotive topcoat based on melamine and a hydroxyl-acrylic resin with an acid catalyst, supplied by PPG Industries, Pittsburgh, Pa.) The topcoated panels were baked at 121°C for 30 minutes. All samples were slightly tacky and eventually intercoat adhesion was lost (about 50 days). This demonstrates the difficulties encountered in curing an acid catalyzed topcoat over a primer high in amine value. Thus, while metal adhesion and controlled age viscosity were good, paintability was lacking. EXAMPLE 2 Plasticizer studies extended to various blends in order to retain control age viscosity but improve paintability. The basic formulation studied was as follows: Ingredient* Amount (wt.-parts) Occidental 6482™ 60 Borden VC265™ 40 CaCO₃ 100 Talc 20 Silica 1 Euretek™ 580 promoter 3.21phr Talc - Mistron ZCS grade talc, Cypress Industrial Minerals Silica - Cab-O-Sil® brand fumed silica, Cabot Corporation. Promoter- phr is weight parts per hundred weight parts of PVC. The various plasticizer/promoter phases evaluated are set forth below: Formulation No. 204-88 (wt.-parts) Ingredient 1 2 3 4 5 6 DIHP 50 50 50 50 50 50 DHP 10 20 25 50 50 100 Monoisopropyl biphenyl 40 30 25 -- -- 40 In formulations 1-3 and 5, the promoter was added to the plasticizer mix slightly warmed until homogeneous. In formulations 4 and 6, the promoter was added after the plastisol was made. Age viscosity measurements were taken as set forth below. Coatings on primed steel panels 0.50 mm (0.20 inch thickness) were baked at 121°C for 20 minutes. All films adhered well except No. 204-88-5 (control). The acid catalyst topcoat of Example 1 was applied over the cured plastisols and baked at 121°C for 30 minutes (wet-on-dry). Nos. 1-3 were dry while Nos. 4 and 5 were slightly tacky. Thus, the paintability of the plastisol had been improved by the addition of the secondary plasticizer solvent, monoisopropyl biphenyl. The amount of secondary plasticizer solvent appeared to be a bit low in Nos. 2 and 3, so that the formulation of this example appears to require at least about 40 weight parts of monoisopropyl biphenyl in order for paintability to be realized. EXAMPLE 3 The basic formulation of Example 2 (Table 4) was studied again at higher levels of monoisopropyl biphenyl: 50 wt.-parts for 204-96-1 and 70 wt.-parts for 204-96-2. Again, the technique of blending the adhesion promoter into the plasticizer blend prior to making the plastisol was utilized. The age viscosity data recorded is set forth below. Each plastisol exhibited good adhesion to the steel panels (bake protocol of 121°C for 20 minutes). The acid catalyzed topcoat of Example 1 was applied wet-on-dry and wet-on-wet with baking at 121°C for 30 minutes for both. The topcoat was not tacky for both systems. Note the slightly increased secondary solvent levels used compared to Example 2. Thus, the ability to achieve paintability while retaining adhesion to metal has been achieved. EXAMPLE 4 The following formulations were studied. Formulation No. 204-147 Ingredient (wt-parts) 1 2 Occidental 6482™ 60 60 Borden VC265™ 40 40 CaCO₃ 200 200 Talc 10 10 DIDP 60 60 Monoisopropyl biphenyl 40 40 Euretek 580 promoter™ 3 3 The plasticizer/promoter blend of No. 1 was mixed at room temperature and then added to the plastisol. The plasticizer/promoter blend of No. 2 was mixed at 72°C and then added to the plastisol. The effects of temperature during the formulating, thus, were being studied. Both plastisols were coated on steel panels and subjected to wet-on-dry and wet-on-wet topcoating as in Example 3. No apparent performance difference between the two formulations observed. EXAMPLE 5 Various secondary plasticizer solvents were studied utilizing the basic formulation of Example 2. The various plasticizer blends studied are set forth below: Formulation No. 204-98 Ingredient (wt.-parts) 1 2 3 DIDP 50 50 50 DHP 10 10 10 Butylated biphenyl 40 -- -- Diisopropyl biphenyl -- 40 -- Phenylxylyl ethane -- -- 40 The plasticizer/promoter blends were made and then added to the remaining ingredients, as described above. Age viscosity data are set forth below. The formulations were coated and cured on steel panels (121°C for 20 minutes) and topcoated wet-on-dry and wet-on-wet as in the previous examples. Again, good adhesion to the substrates was achieved. The wet-on-dry topcoats also were tack free while the wet-on-wet topcoats were very slightly tacky. Thus, the efficacy of additional aromatic secondary plasticizer solvents is demonstrated. EXAMPLE 6 The following formulations were made as described above. Formulation no. 204-116 Ingredient (wt.-parts) 1 2 3 4 Occidental 6482™ 60 60 60 60 Borden VC265™ 40 40 40 40 CaCO₃ 200 200 200 200 DIDP 60 60 60 30 DHP -- -- -- 30 Euretek 580 promoter™ 5 3 3 3 Monoisopropyl biphenyl 40 40 -- -- Diethylene glycol monoethyl ether -- -- 40 40 Control age viscosity data recorded is set forth below. The plastisols were coated on panels (121°C for 20 minutes) and topcoated wet-on-dry as described in the previous examples. Again, good substrate adhesion was achieved. The topcoats were dry for Nos. 2, 3, and 4, and only very slightly tacky for No. 1. Again, the low temperature paintability of the inventive plastisols is demonstrated. EXAMPLE 7 Additional studies of the ether secondary plasticizer solvent were undertaken on the following formulations. Formulation No. 204-98 Ingredient (wt.-parts) 1 2 3 Occidental 6482™ 60 60 60 Borden VC265™ 40 40 40 CaCO₃ 200 200 200 DIDP 90 80 105 Diethylene glycol monoethyl ether 10 20 20 Euretek 580 promoter™ 3 3 3 Control age viscosity data is set forth below. Good adhesion to steel panels again was achieved. The wet-on-dry topcoats (121°C for 30 minutes) also were dry. The efficacy of the ether secondary plasticizer solvent again is demonstrated. EXAMPLE 8 Formulation No. 204-118-1 (Example 7) was evaluated again along with an equivalent formulation which used a different adhesion promoter (No. 2) at the same level: Euretek® 555 polyaminoamide-polyimidazoline adhesion promoter (amine value of 380; Gardner color of 12; 8.1 lb/gal. at 82.2°C; Viscosity profile (Brookfield LVT, spindle 34) of 17,000 mPa·s at 43.3°C, 13,000 mPa·s at 48.9°C, 9,000 mPa·s at 54.5°C, 4,000 mPa·s at 60.0°C, and 2,800 mPa·s at 65.6°C; Sherex Chemical Company, Inc., Dublin, Ohio). The control age viscosity data recorded is set forth below. Panel coatings and wet-on-dry acid catalyzed topcoats were applied as in the previous examples. Good panel adhesion was achieved. The topcoat on Formulation No. 204-118-1 was dry while the topcoat on Formulation No. 204-126-2 was only slightly tacky. EXAMPLE 9 The following formulations were made: Formulation No. 204-120 Ingredient (wt.-parts) 1 2 3 Occidental 6482™ 60 60 60 Borden VC265™ 40 40 40 CaCO₃ 200 200 200 DIDP 90 80 55 Diethylene glycol monoethyl ether 10 20 20 Euretek 580 promoter™ 3 3 3 Control age viscosity data is set forth below. Viscosity (mPa·s) No. RPM Initial 1 day 10 days 21 days 1 2.5 108,800 158,400 334,400 318,400 5 66,600 96,800 212,800 203,200 10 43,300 61,600 137,600 131,200 20 30,000 41,600 92,800 90,800 R 3.63 3.81 3.60 3.51 yield 2,110 3,080 6,080 5,760 2 2.5 20,400 44,000 225,600 249,600 5 13,400 27,600 136,800 150,400 10 10,200 18,900 86,800 10,800 20 7,850 13,800 56,600 71,200 R 2.60 3.19 3.99 3.51 yield 350 820 4,440 4,960 3 2.5 22,800 40,000 313,600 304,000 5 19,000 32,200 217,600 202,400 10 16,300 26,100 110,400 137,600 20 14,700 22,950 81,400 102,800 R 1.55 1.83 3.85 2.96 yield 190 490 4,800 5,080 Spindle #6 for Initial and 1 day; Spindle #7 'for all other samples. Panel and topcoat testing revealed that good panel adhesion still was present but that the wet-on-dry topcoats (121°C for 30 minutes) were slightly tacky. The reason for the dimunition in performance of this butyl ether solvent compared to the ethyl ether version is not understood presently. EXAMPLE 10 The following formulations were made. Formulation No. 204 Ingredient* (wt.-parts) 103-1 103-2 105-1 105-2 138-1 138-2 Occidental 6482™ 60 60 60 60 60 60 Borden VC265™ 40 40 40 40 40 40 CaCO₃ 100 100 100 100 200 200 Talc 20 20 20 20 -- -- Silica 1 1 1 1 -- -- DIDP 30 20 50 30 90 80 DHP 30 20 25 30 -- -- Monoisopropyl biphenyl 20 30 -- -- -- -- Propylene glcyol dibenzoate 20 30 -- -- -- -- Ethyl toluene sulfon amide (ortho and para isomer mixture) -- -- 25 40 -- -- Ethoxylated nonyl phenol -- -- -- -- 10 20 While the aromatic ester, the sulfonamide, and the nonyl phenol solvents all solvated the adhesion promoter, wet-on-dry paintability was lacking. Ester solvents appear not to be beneficial due to postulated undesirable interaction with other ingredients. The sulfonamide solvent adds more amine value to the plastisol which is not desirable for achieving cure of the acid catalyzed topcoat. The ethoxylated nonyl phenol solvent should have functioned properly according to current understanding of the invention. Perhaps different levels or degrees of ethoxylation will enable this solvent,to function as plastisol.

Claims: A plastisol composition comprising finely-divided vinyl chloride polymer, filler, a primary plasticizer, and a polyaminoamide-polyimidazoline adhesion promoter, wherein for overcoating said plastisol with an acid catalyzed topcoat said composition comprises a plasticizer/promoter phase comprising said primary plasticizer and said adhesion promoter, characterized in that said plasticizer/promoter phase comprises in addition an effective amount of a secondary plasticizer nonionic solvent effective in solvating said adhesion promoter in said plasticizer/promoter phase, said plasticizer/promoter phase being preformed for addition with the remaining ingredients of the plastisol composition. The plastisol composition of claim 1 characterized in that said secondary plasticizer nonionic solvent ranges from between 10 to 70 weight parts per 100 weight parts of said vinyl chloride polymer. The plastisol composition of claim 1 characterized in that said primary plasticizer ranges from between 20 and 200 weight parts per 100 weight parts of said vinyl chloride polymer. The plastisol composition of claim 1 characterized in that said adhesion promoter ranges from between 1 and 10 weight parts per 100 weight parts of said vinyl chloride polymer. The plastisol composition of claim 1 characterized in that said secondary plasticizer nonionic solvent is selected from the group consisting of monoisopropyl biphenyl, diethylene glycol monoethyl ether, diisopropyl biphenyl, phenylxylyl ethane, butylated biphenyl, and mixtures thereof. The plastisol composition of claim 1 characterized in that it contains more than one of said vinyl chloride polymer. The plastisol composition of claim 1 characterized in that it additionally comprises a thixotropic agent ranging from between 1 and 5 weight parts per 100 weight parts of said vinyl chloride polymer. A method for making a plastisol composition which comprises: (a) forming a plasticizer/promoter phase comprising a primary plasticizer, a polyaminoamide-polyimidazoline adhesion promoter, (b) blending said plasticizer/promoter phase with a finely-divided vinyl chloride polymer and a filler to make said plastisol composition characterized by the addition during step (a) to the plasticizer/promoter phase of an effective amount of a secondary plasticizer nonionic solvent effective in solvating said adhesion promoter in said plasticizer/promoter phase. The method of claim 8 characterized in that said secondary plasticizer nonionic solvent ranges from between 10 to 70 weight parts per 100 weight parts of said vinyl chloride polymer. The method of claim 8 characterized in that said primary plasticizer ranges from between 20 and 200 weight parts per 100 weight parts of said vinyl chloride polymer. The method of claim 8 characterized in that said adhesion promoter ranges from between 1 and 10 weight parts per 100 weight parts of said vinyl chloride polymer. The method of claim 8 characterized in that said secondary plasticizer nonionic solvent is selected from the group consisting of monoisopropyl biphenyl, diethylene glycol monoethyl ether, diisopropyl biphenyl, phenylxylyl ethane, butylated biphenyl, and mixtures thereof. The method of claim 8 characterized in that it contains more than one of said vinyl chloride polymer. The method of claim 8 characterized in that it additionally comprises a thixotropic agent ranging from between 1 and 5 weight parts per 100 weight parts of said vinyl chloride polymer. A method for coating a metal substrate which comprises: (a) applying a plastisol composition; (b) applying an acid-catalyzed topcoat over said plastisol compostion; and (c) heating said coated metal substrate to cure said plastisol composition and said topcoat, characterized in applying as said plastisol composition, the plastisol composition of claims 1-7. The method of claim 15 characterized in that said plastisol composition on said metal substrate is heated for its curing prior to applying said topcoat thereto. The method of claims 15 and 16 characterized in that the proportion of secondary plasticizer ranges from between 10 and 70 weight parts, said primary plasticizer ranges from between 20 and 200 weight parts, and said promoter ranges from between 1 and 10 weight parts, all weight parts based on 100 weight parts of said vinyl chloride polymer.

Inventors: WOZNIAK, DON STEVEN
Applicants: SHEREX CHEMICAL COMPANY, INC.
Application year: 1987
Main classification: C08J3
IPC codes: C08L27, C08L79, C09D5, C09J127, C09D127, C08K5, C08J3