POWDER COATINGS

Abstract

At least a two-layer protective coating system including: (a) a layer of a fusion bonded epoxy, and (b) a layer of a spray-dried protective powder coating disposed on at least a portion of the top surface of the fusion bonded epoxy layer (a), said powder coating being cured to form a protective coating on at least a portion of the fusion bonded epoxy layer; a process for preparing the above two-layer protective coating system; a substrate such as a metal pipe coated with the above two-layer protective coating system; and a process for producing a coated article such as a coated metal pipe using the above two-layer protective coating system.

Claims

1. A waterborne polyolefin dispersion formulation for preparing a powder coating comprising (i) a base polymer, (ii) a polymeric coupling agent; (iii) a neutralizing agent; (iv) a fluid medium; and (v) optionally, a polymeric performance improving agent.

2. A process for preparing a waterborne polyolefin dispersion formulation for preparing a powder coating comprising admixing: (i) a base polymer, (ii) a polymeric coupling agent; (iii) a neutralizing agent; (iv) a fluid medium; and (v) optionally, a polymeric performance improving agent.

3. A sprayable powder coating composition having a uniform particle size distribution comprising a particulate material made from the formulation of claim 1, wherein the particle size distribution of the particulate material is from about 20 to about 300 microns.

4. A coating system comprising: (a) a layer of a fusion bonded epoxy, and (b) a layer of a spray dried protective powder coating disposed on at least a portion of the top surface of the fusion bonded epoxy layer (a), said powder coating being cured to form a protective coating on at least a portion of the fusion bonded epoxy layer; and wherein the spray dried protective powder coating layer is prepared from a waterborne polyolefin dispersion comprising: (i) a base polymer, (ii) a polymeric coupling agent; (iii) a neutralizing agent; (iv) a fluid medium; and (v) optionally, a polymeric performance improving agent.

5. A coated substrate comprising a metallic substrate having at least a portion of the top surface of the substrate coated with the coating system of claim 4.

6. The coating system of claim 4, wherein the waterborne polyolefin dispersion includes an epoxy resin or an epoxy resin in a waterborne dispersion.

7. The coating system of claim 6, wherein the epoxy resin dispersion comprises (i) an epoxy resin and (ii) a stabilizing agent.

8. The coating system of claim 4, wherein the coating system has an impact resistance of from about 100 inch-lbs to about 160 inch-lbs as measured on a 32 mil steel panel; and a damage tolerance of from 0 holiday to about 1 holiday as measured using a holiday tester following cooling to 32 C.

9. The coating system of claim 4, wherein the coating system has an overall film thickness of from about 350 microns to about 700 microns; wherein the fusion bonded epoxy layer has a thickness of from about 200 microns to about 400 microns; and wherein the protective powder coating layer has a thickness of from about 150 microns to about 300 microns.

10. A process for preparing a two-layer protective coating system comprising the steps of adjoining: (a) a layer of a fusion bonded epoxy, and (b) a layer of a spray-dried protective powder coating; wherein the layer of spray-dried protective powder coating is disposed on at least a portion of the top surface of the fusion bonded epoxy layer (a), said powder coating being cured to form a protective coating on at least a portion of the fusion bonded epoxy layer.

11. A process for preparing a two-layer protective coating system on a substrate comprising the steps of: (A) providing a layer of a fusion bonded epoxy on a substrate; (B) preparing a waterborne polyolefin dispersion; (C) preparing a powder from the waterborne polyolefin dispersion; (D) applying the powder on at least a portion of the fusion bonded epoxy layer; and (E) curing the polyolefin powder over the fusion bonded epoxy layer.

12. A process of claim 11, wherein the substrate is a metal pipe.

13. A process for preparing a hybrid polyolefin powder comprising the steps of: (1) preparing a polyolefin dispersion, (2) preparing an epoxy dispersion, (3) blending the polyolefin dispersion and the epoxy dispersion, and (4) spray dry blending the polyolefin dispersion and the epoxy dispersion.

14. The process of claim 13, further including adding a second polymer resin (e.g., epoxy), a curing catalyst, a pigment, or mixtures thereof to the polyolefin dispersion and/or the epoxy dispersion.

Description

BRIEF DESCRIPTION OF THE DRAWINGS

[0023] For the purpose of illustrating the present invention, the drawings show a form of the present invention which is presently preferred. However, it should be understood that the present invention is not limited to the embodiments shown in the drawings.

[0024] FIG. 1 is a cross-sectional side view of one embodiment of the present invention showing a portion of a two-layered structure of the coating of the present invention disposed on the surface of a substrate such as steel.

[0025] FIG. 2 is a graphical illustration showing the representative particle size distribution for the dispersion of Example 5 of the present invention.

[0026] FIG. 3 is a scanning electron microscopy (SEM) image of a polyolefin dispersion and epoxy blend powder of Example 15 of the present invention which illustrates the typical powder morphology made via the process of the present invention.

[0027] FIG. 4 is a graphical illustration showing the representative particle size distribution for a polyolefin dispersion powder of Example 19 of the present invention.

[0028] FIG. 5 is a graphical illustration showing the representative particle size distribution for the dispersion of Example 1 of the present invention.

DETAILED DESCRIPTION

[0029] Holiday, in relation to an anticorrosive surface coating, herein means a discontinuity in coating, including one or more of the following: when a part of the surface remains uncoated; a defect such as an area of insufficient coating film thickness; a pinhole within the coating; a crack within the coating; or an improper adhesion or bonding of the coating.

[0030] Damage tolerance herein, with reference to a coating, means that the coating is able to withstand minimum impact resistance and flexibility requirements as described by the Canadian Standard Association as System B1 and System B2 in the standard Z245.21-10 for plant-applied external polyethylene coatings for steel pipe. Impact resistance herein, with reference to a coating, means no holidays are detected after a minimum of 3.0 J/mm is applied to the coating as per Clause 12.12., Clause 12.2.3 (d), and Clause 12.2.3 (e) of CSA Z245.20.

[0031] A sufficient amount of epoxy functionality herein means that enough epoxy groups are available to react with the FBE primer to form a covalent bond.

[0032] Readily applied herein, with reference to an FBE primer, means that the FBE primer is not fully cured before the powder coating of the present invention is applied onto the FBE primer; and therefore, is easily applied to the FBE primer.

[0033] Sprayable herein means that the particle size and distribution of the present invention coating composition is such that the composition can be sprayed using standard or conventional powder coating equipment for pipes.

[0034] Hybrid powders herein means powders consisting of more than one polymer dispersion (e.g., POD and epoxy dispersions), or a combination of polymer dispersions and organic/inorganic fillers/pigments (e.g., a combination of POD, epoxy dispersion, and TiO.sub.2 pigment).

[0035] In one broad scope, the present invention includes at least a two-layer protective coating system including: (a) a layer of a fusion bonded epoxy having a top surface and a bottom surface, and (b) a layer of a spray-dried protective powder coating disposed on at least a portion of the top surface of the fusion bonded epoxy layer (a).

[0036] With reference to FIG. 1, there is shown one embodiment of the present invention coating structure comprising a multi-layer composite structure or sheet member, indicated by general numeral 10, which is bonded to the surface of a substrate 20 such as a steel pipe. The multi-layer structure 10 includes at least one layer of a fusion bonded epoxy layer 11; and one or more layers of a waterborne polyolefin dispersion powder coating surface layer 12 bonded to at least a portion of the top surface of the fusion bonded epoxy layer 11. The layers 11 and 12 are bonded together as shown in FIG. 1 to make up the multi-layer composite structure or sheet member 10.

[0037] As aforementioned with reference to FIG. 1, the first layer 11 of the present invention coating system includes (a) a layer of a fusion bonded epoxy (FBE). The FBE coating (also referred to as a fusion-bond epoxy powder coating or as FBE coating), is an epoxy-based powder coating that is used in various applications, for example, to protect steel pipe used in pipeline construction from corrosion.

[0038] FBE coatings are thermoset polymer coatings prepared by curing a curable epoxy resin coating composition. The name fusion-bond epoxy is due to resin crosslinking and the application method, which is different from conventional curing of an epoxy resin formulation. For example, the resin and hardener components, incorporated into a dry powder FBE composition, remain unreacted at storage conditions (for example, typically, a packaged FBE product is shipped and stored at temperatures not to exceed about 27 C.) or as recommended by the FBE supplier. Then, when the FBE composition is used at typical coating application temperatures (for example, from about 180 C. to about 250 C.), the powder contents melt and transform into a liquid form. The liquid FBE composition, when applied onto the surface of a substrate such as a steel surface, wets and flows onto the surface of the substrate forming a liquid film on the surface of the substrate; and soon thereafter, the liquid FBE film becomes a solid coating by chemical cross-linking, assisted by heat. This process is known as fusion bonding.

[0039] As a protective coating, there are various types of FBE coatings made from various coating formulations depending on the requirements of a coating application. Typically, the FBE coating is used as one part or layer in a multi-layer coating structure. The FBE coating can also have different properties depending on the requirements for a particular coating application.

[0040] FBE coatings and methods of preparing FBE coatings are further described, for example, in WO 2010096345 and WO 2005023941, incorporated herein by reference.

[0041] Generally, the FBE layer of the at least two-layer coating structure of the present invention may have a thickness of from about 50 microns (m) to about 1 millimeters (mm) in one embodiment; from about 100 m to about 0.5 mm in another embodiment; and from about 200 m to about 0.4 mm in still another embodiment

[0042] As aforementioned with reference to FIG. 1, the second layer 12 of the present invention coating system includes (b) a layer of a spray-dried protective powder coating. Generally, the protective powder coating layer of the at least two-layer coating structure may have a thickness of from about 50 m to about 5.0 mm in one embodiment; from about 200 m to about 2.5 mm in another embodiment; and from about 500 m to about 1.0 mm in still another embodiment. In a preferred embodiment, the spray-dried protective powder coating layer of the present invention can be prepared from a waterborne polyolefin dispersion.

[0043] As discussed herein, the coating composition, that is, the polyolefin dispersion (POD) of the present invention includes (a) from about 40 weight percent (wt %) to about 80 wt % of a base polymer; (b) from about 10 wt % to about 30 wt% of a polymeric stabilizing agent; (c) from about 5 wt % to about 15 wt % of a polymeric coupling agent; (d) from 0 wt % to about 35 wt% of a polymeric performance improving agent; (e) a neutralizing agent of a concentration sufficient to partially or fully neutralize the polymeric stabilizing agent; and (f) a fluid medium, where the wt % values are based on the total weight of the base polymer, the polymeric stabilizing agent, the polymeric coupling agent, and, when present, the polymeric performance improving agent. As used herein, this total weight of the base polymer, the polymeric coupling agent, the polymeric stabilizing agent, and, when present, the polymeric performance improving agent may be referred to as the solid content of the coating composition. The wt % values provided herein are based on the total weight of the solid content of the coating composition and sum to a value of 100 wt %.

[0044] The polyolefin dispersion of the present disclosure includes from about 40 wt % to about 80 wt % of a base polymer, where the wt % is based on the total weight of the solid content, as defined herein, of the coating composition. All individual values and sub-ranges from about 40 wt % to about 80 wt % are included herein and disclosed herein; for example, the wt % can be from a lower limit of about 40 wt %, about 45 wt % or about 50 wt % to an upper limit of about 70 wt %, about 75 wt %, or about 80 wt %. For example, the coating composition may comprise from about 40 wt % to about 75 wt.%, or from about 40 wt % to about 70 wt %, or from about 45 wt % to about 80 wt %, or from about 45 wt % to about 75 wt %, or from about 45 wt % to about 70 wt %, or from about 50 wt % to about 80 wt %, or from about 50 wt % to about 75 wt %, or from about 50 wt % to about 70 wt % of the base polymer, based on the total weight of the solid content of the coating composition. The polyolefin dispersion can include at least one or more of the base polymers. For example, the polyolefin dispersion can include two or more base polymers, as discussed herein. Therefore, as used herein, a base polymer or the base polymer can be substituted with two or more base polymers.

[0045] The base polymer can be selected from the group consisting of a non-functionalized ethylene polymer, a non-functionalized propylene polymer, a non-functionalized propylene/ethylene copolymer, and combinations thereof. For example, the base polymer may include two or more of the non-functionalized polymers discussed herein. As used herein, non-functionalized means the absence of a reactive polar group on the polymer.

[0046] The non-functionalized ethylene polymer can be selected from the group consisting of polyethylene, an ethylene-copolymer and any combination thereof. Examples of the ethylene-copolymer can include non-functionalized propylene/ethylene copolymers. The propylene/ethylene copolymers may include propylene-ethylene alternating copolymers. Examples of such non-functionalized ethylene polymers and non-functionalized propylene/ethylene random and block copolymers include, but are not limited to, VERSIFY DP-4000.01; VERSIFY 4200, VERSIFY 4000, VERSIFY 3200, VERSIFY 3000, and VERSIFY 3300, all available from The Dow Chemical Company; ENGAGE 8407 available from The Dow Chemical Company; INFUSE 9807 available from The Dow Chemical Company; Vistamaxx propylene-based elastomers (available from ExxonMobil Chemical); commercially available high density polyethylene such as, but are not limited to, DMDA-8007 NT 7 (melt index: 8.3, density: 0.965), DMDC-8910 NT 7 (melt index: 10, density: 0.943), DMDA-1210 NT 7 (melt index 10, density 0.952), HDPE 17450N (melt index 17, density 0.950), DMDA-8920 NT 7 (melt index 20, density 0.954), DMDA 8940 NT 7 (melt index 44, density 0.951), DMDA-8950 NT 7 (melt index 50, density 0.942), DMDA-8965-NT 7 (melt index 66, density 0.952), DMDA-8940 HDPE (melt index of approximately 40-48 g/10 min), all available from The Dow Chemical Company; and mixtures thereof.

[0047] Exemplary non-functionalized ethylene polymers can also include homogeneous polymers, such as for example the polymers described in U.S. Pat. No. 3,645,992; high density polyethylene (HDPE), such as for example the HDPE described in U.S. Pat. No. 4,076,698; heterogeneously branched linear low density polyethylene (LLDPE); heterogeneously branched ultra-low linear density polyethylene (ULDPE); homogeneously branched, linear ethylene/alpha-olefin copolymers; homogeneously branched, substantially linear ethylene/alpha-olefin polymers, which can be prepared, for example, by processes disclosed in U.S. Pat. Nos. 5,272,236 and 5,278,272, the disclosures of which are incorporated herein by reference; and high pressure, free radical polymerized ethylene polymers and copolymers such as low density polyethylene (LDPE) or ethylene vinyl acetate polymers (EVA); and mixtures thereof. The non-functionalized ethylene polymer has a crystalline melting point of from about 100 C. to about 230 C. Other values are possible, where the crystalline melting point is measured by calorimetry measurements.

[0048] In one embodiment, an example of the non-functionalized propylene polymer can include, but is not limited to, 6D43 Polypropylene (available from Braskem Corp.). Generally, the non-functionalized propylene polymer can be characterized as having substantially isotactic propylene sequences. Substantially isotactic propylene sequences means that the sequences have an isotactic triad (mm) measured by .sup.13C NMR of greater than about 0.85; in the alternative, greater than about 0.90; in another alternative, greater than about 0.92; and in another alternative, greater than about 0.93. Isotactic triads are well-known in the art and are described in, for example, U.S. Pat. No. 5,504,172 and WO00/01745, which refers to the isotactic sequence in terms of a triad unit in the copolymer molecular chain determined by .sup.13C NMR spectra.

[0049] Other examples of the base polymer include, but are not limited to, ethylene ethyl acrylate copolymer, ethylene methyl methacrylate, ethylene butyl acrylate, and combinations thereof.

[0050] The base polymer can have a density of at least about 0.88 grams/mole as measured by ASTM D972. Specific examples of the densities of such base polymers can include, but are not limited to, a density in the range of from about 0.88 grams/mole to about 1.0 grams/mole or from about 0.88 grams/mole to about 0.98 grams/mole. The base polymer has a crystalline melting point of at least 100 C. as measured using Differential Scanning Calorimetry (DSC).

[0051] The coating composition further includes a polymeric stabilizing agent to promote the formation of a stable dispersion during the formation of the coating composition. The polymeric stabilizing agent may preferably be an external stabilizing agent. The coating composition may include for example, from about 10 wt % to about 30 wt % of the polymeric stabilizing agent, based on the total weight of the solid content, as defined herein, of the coating composition. The coating composition can also include for example from about 5 wt % to about 50 wt % of the polymeric stabilizing agent, based on the total weight of the solid content, as defined herein, of the coating composition. All individual values and sub-ranges from about 5 wt % to about 50 wt % of the polymeric stabilizing agent are included herein and disclosed herein; for example, the wt % can be from a lower limit of about 5 wt %, about 10 wt % or about 15 wt % to an upper limit of about 30 wt %, about 40 wt % or about 50 wt %. For example, the coating composition may comprise from about 5 wt % to about 40 wt %, or from about 5 wt % to about 30 wt %, or from about 10 wt % to about 30 wt %, or from about 10 wt % to about 40 wt %, or from about 10 wt % to about 50 wt %, or from about 15 wt % to about 30 wt %, or from about 15 wt % to about 40 wt%, or from about 15 wt % to about 50 wt % of the polymeric stabilizing agent, based on the total weight of the solid content of the coating composition. The coating composition may also comprise from about 20 wt % to about 24 wt % of the polymeric stabilizing agent, based on the total weight of the solid content of the coating composition.

[0052] The polymeric stabilizing agent can have an acid number of equal to or greater than about 100 in one embodiment; greater than about 110 in another embodiment; or greater than about 140 in still another embodiment. The polymeric stabilizing agent can be a polar polymer, for example, including a polar group as either a comonomer or grafted monomer. In some embodiments, the polymeric stabilizing agent can include one or more polar polyolefins, for example, having a polar group as either a comonomer or grafted monomer. Acid Number values (the amount of KOH in mg KOH/g polymer required to neutralize acid functionality when measured by titration) can be measured according to ASTM D-1386.

[0053] Examples of polymeric stabilizing agents include, but are not limited to, ethylene-acrylic acid and ethylene-methacrylic acid copolymers having a functionality in a range of from about 10 wt % to about 25 wt %. Functionality values (the amount of functional monomer expressed as weight percent of the resin) can be determined by ASTM D 4094 or equivalent. Examples of such polymeric stabilizing agents include those available under the trademarks PRIMACOR, such as PRIMACOR 5980i or PRIMACOR 5990i, both commercially available from The Dow Chemical Company; NUCREL, commercially available from E.I. DuPont de Nemours; ESCOR commercially available from ExxonMobil Chemical Company and described in U.S. Pat. Nos. 4,599,392, 4,988,781, and 5,938,437, each of which is incorporated herein by reference in its entirety; and mixtures thereof. Other ethylene-carboxylic acid copolymer may also be used. Examples of other polymeric stabilizing agents useful in the present invention may include products under the trade name CERAMER from Baker-Hughes Company, such as CERAMER 1608; and PA-18 polyanhydride copolymer from Chevron-Phillips Company; and mixtures thereof. Those having ordinary skill in the art will recognize that a number of other useful polymers may also be used as the polymeric stabilizing agent.

[0054] The coating composition further includes a polymeric coupling agent. The polymeric coupling agent can help in forming the coating composition, for example, the coupling agent can help provide a more uniform dispersion, and/or improve properties of a cured coating composition. The coating composition includes for example from about 5 wt % to about 15 wt % of the polymeric coupling agent, based on the total weight of the solid content, as defined herein, of the coating composition. All individual values and subranges from about 5 wt % to about 15 wt % of the polymeric coupling agent are included herein and disclosed herein; for example, the wt % can be from a lower limit of about 5 wt % or about 6 wt % to an upper limit of about 8 wt %, about 9 wt % or about 15 wt %. For example, the coating composition may comprise from about 5 wt % to about 8 wt %, or from about 5 wt % to about 9 wt %, or from about 5 wt % to about 15 wt %, or from about 6 wt % to about 8 wt %, or from about 6 wt % to about 9 wt %, or from about 6 wt % to about 15 wt % of the polymeric coupling agent, based on the total weight of the solid content of the coating composition.

[0055] The polymeric coupling agent can have a melt viscosity of less than about 80 Pascal-seconds (Pa-s) at 150 C. in one embodiment; less than about 40 Pa-s at 150 C. in another embodiment; less than about 20 Pa-s at 150 C. in still another embodiment; or less than about 10 Pa-s at 150 C. in yet another embodiment. Melt viscosity can be determined by DIN 53019 or ASTM D-1986, e.g., measurement of wax viscosity using a Brookfield rotational viscometer. For a number of embodiments, the polymeric coupling agent can have an acid number of less than about 100.

[0056] The polymeric coupling agent can include a modified, for example, functionalized, polymer, such as a functionalized polyolefin. For example, the polymeric coupling agent can be selected from the group consisting of a functionalized polypropylene, a functionalized polyethylene homopolymer, a copolymer that has been modified with carboxylic acid groups, a copolymer that has been modified with anhydride groups, and any combination thereof. The polymeric coupling agent can also be selected from a low molecular weight compound having reactive polar groups. Examples of the polymeric coupling agent include, but are not limited to, modified olefin polymers. The modified olefin polymers can include graft copolymers and/or block copolymers, such as propylene-maleic anhydride graft copolymer. Examples of groups that can modify the polymer include, but are not limited to, acid anhydrides, carboxylic acids, carboxylic acid derivatives, primary and secondary amines, hydroxyl compounds, oxazoline and epoxides, and ionic compounds, and combinations thereof.

[0057] Specific examples of the groups that can modify the polymer include, but are not limited to, unsaturated cyclic anhydrides and their aliphatic diesters, and the diacid derivatives. For example, maleic anhydride and compounds selected from C.sub.1-C.sub.10 linear and branched dialkyl maleates, C.sub.1-C.sub.10 linear and branched dialkyl fumarates, itaconic anhydride, C.sub.1-C.sub.10 linear and branched itaconic acid dialkyl esters, maleic acid, fumaric acid, itaconic acid, and combinations thereof.

[0058] Commercially available examples of polymeric coupling agents useful in the present invention may include, but are not limited to, polymers available under the trade name LICOCENE, or LICOLUBE, from Clariant Corporation, such as LICOCENE 6452 (e.g., LICOCENE PP MA 6452) and LICOCENE 4351(e.g., LICOCENE PE MA 4351); polymers under the trade name A-C Performance Additives from Honeywell Corporation, such as AC-575 which is an ethylene maleic anhydride copolymer, and AC-392 and AC-395 which are high density oxidized polyethylene; products under the trade name CERAMER from Baker-Hughes Company EXXELOR from ExxonMobil Chemical Company; and Epolene from Westlake Chemical Company; and mixtures thereof.

[0059] The coating composition may further optionally include a polymeric performance improving agent. The polymeric performance improving agent can help to simultaneously provide particular performance characteristics, such as particular appearance properties and particular mechanical and chemical resistance properties for a coated article, which are desirable for some coating applications. The coating composition may include for example from 0 wt % to about 35 wt % of the polymeric performance improving agent, based on the total weight of the solid content, as defined herein, of the coating composition. All individual values and sub-ranges from 0 wt % to about 35 wt % of the polymeric performance improving agent are included herein and disclosed herein; for example, the wt % can be from a lower limit of 0 wt %, about 5 wt % or about 10 wt % to an upper limit of about 15 wt %, about 20 wt %, or about 35 wt %. For example, the coating composition may comprise from 0 wt % to about 15 wt %, or from 0 wt % to about 20 wt %, or from 0 wt % to about 35 wt %, or from about 5 wt % to about 15 wt %, or from about 5 wt % to about 20 wt %, or from about 5 wt % to about 35 wt %, or from about 10 wt % to about 15 w %, or from about 10 wt % to about 20 wt % or from about 10 wt % to about 35 wt % of the polymeric performance improving agent, based on the total weight of the solid content of the coating composition.

[0060] The polymeric performance improving agent can have an acid number of for example less than about 60 in one embodiment, less than about 50 in another embodiment, or less than about 42 in still another embodiment. Acid number can be determined by ASTM D-1386, for example. Acid number can refer to an amount of KOH in mgKOH/g polymer required to neutralize acid functionality when measured by titration. Alternatively the percent functionality can be determined by Fourier Transform Infrared Spectroscopy (FTIR).

[0061] The polymeric performance improving agent can have a melt index value of for example less than about 100 in one embodiment, less than about 70 in another embodiment, or less than about 30 in still another embodiment. Melt index values can be determined by ASTM D-1238, for example. As used herein, melt index values can be defined as the amount of polymer melt passing in dg/min (or g/10 min) through a heated syringe with a plunger load, e.g., at 190 C. and 2.16 kg load for polyethylene based polymer and at 230 C. and 2.16 kg for polypropylene based polymer.

[0062] Embodiments of the present disclosure provide that the polymeric performance improving agent can be selected from the group consisting of functionalized polyethylene, functionalized polypropylene, non-functionalized copolymer of ethylene and propylene and any combination thereof. Examples of the functionalized polyethylene include, but are not limited to, maleic anhydride functionalized polyethylene, such as high density polyethylene. Maleic anhydride functionalized polyethylene copolymers, terpolymers and blends may also be used. Maleic anhydride functionality can be incorporated into the polymer by grafting or other reaction methods. When grafting, the level of maleic anhydride incorporation is typically below about 3 percent by weight based on the weight of the polymer.

[0063] Examples of commercially available maleic anhydride functionalized polyethylene include those available under the tradename AMPLIFY available from The Dow Chemical Company, such as AMPLIFY GR-204, among others. Amplify GR-204 is 2,5-Furandione modified ethylene/hexene-1 polymer. Other examples of maleic anhydride functionalized polyethylene are available under the tradename FUSABOND available from E.I. du Pont de Nemours and Company such as FUSABOND E-100, FUSABOND E-158, FUSABOND E265, FUSABOND E528, FUSABOND E-589, FUSABOND M-603, among others; Other maleic anhydride grafted polyethylene polymers, copolymers, and terpolymers may include POLYBOND available from Chemtura, such as POLYBOND 3009 and POLYBOND 3029, among others; OREVAC available from ARKEMA, such as OREVAC 18510P, among others; PLEXAR from Lyondell Chemical Company, such as PLEXAR PX-2049; also grades available under the tradename YPAREX from B.V. DSM Engineering Plastics, such as YPAREX 8305; and polymers available under the tradename EXXELOR, such as Exxelor PE 1040. Other examples include LOTADER 4210 a random terpolymer of ethylene, acrylic ester and maleic anhydride available from ARKEMA. Additional polyethylene functionalized with glycidyl methacrylate may be used. Other examples of the polymeric performance improving agent include non-functionalized polymers available under the trade name VERSIFY, such as VERSIFY 4200, VERSIFY 4000, VERSIFY 3200, VERSIFY 3000, and VERSIFY 3300, all available from The Dow Chemical Company. Any two or more of the above compounds in combination can be used if desired.

[0064] In another embodiment, the acid groups of the polymeric stabilizing agent may be partially or fully neutralized with a neutralizing agent. When neutralization desired, in certain embodiments, neutralization of the stabilizing agent may be from 25 to 200 percent on a molar basis; or in the alternative, from 50 to 165 percent on a molar basis; or in the alternative, from 50 to 150 percent on a molar basis; or in the alternative, from 50 to 120 percent on a molar basis.

[0065] Examples of suitable neutralizing agents include a volatile base. As used herein a volatile base is a base that can be evaporated (conversion of a liquid to a gas or vapor) at a temperature in a range from about 100 C. to about 200 C. at a pressure in a range of about 1 atmosphere. Examples of such a volatile base include, but are not limited to, N,N-dimethylethanolamine (DMEA), ammonia, hydrazine, methylamine, ethylamine, diethylamine, triethylamine, isobutylamine, N,N-diisopropylethylamine, morpholine, piperazine, ethylenediamine, and 1,4-diazabicyclo[2.2.2]octane), and mixtures thereof. The volatile base reverts to the acid form upon the formation of the coating layer where the acid form can help to promote adhesion of the coating layer to the surface of the substrate.

[0066] Other neutralizing agents can include, for example, an amine such as monoethanolamine, or 2-amino-2-methyl-1-propanol (AMP), or mixtures thereof. Amines useful in embodiments disclosed herein may include diethanolamine, triethanolamine, and TRIS AMINO (each available from Angus), NEUTROL TE (available from BASF), as well as triisopropanolamine and diisopropanolamine; and mixtures thereof. Other useful amines may include dimethylamine, trimethylamine, mono-n-propylamine, butylamine, dibutylamine, tributylamine, dimethyl benzyl amine, dimethyl n-propylamine, N-methanol amine, N-aminoethylethanolamine, N-methyldiethanolamine, monoisopropanolamine, N,N-dimethyl propanolamine, 2-amino-2-methyl-1-propanol, 1,2-diaminopropane, tris(hydroxymethyl)-aminomethane, ethylenediamine, N,N,NN-tetrakis(2-hydroxylpropyl)ethylenediamine, 3-methoxypropyl amine, imino bis-propyl amine, and the like; and mixtures thereof. In some embodiments, mixtures of amines or mixtures of amines and surfactants may be used. In one embodiment, the neutralizing agent may be a polymeric amine (e.g., diethylene triamine) Those of ordinary skill in the art will appreciate that the selection of an appropriate neutralizing agent depends on the specific composition formulated, and that such a choice is within the knowledge of those of ordinary skill in the art. In one embodiment, amines with boiling points below 250 C. may be used as the neutralizing agents.

[0067] The coating composition further includes a fluid medium. The fluid medium may be, for example, water; or in the alternative, the fluid medium may be a mixture of water and one or more organic solvents. For example, the organic solvent useful in the present invention may include one or more water miscible solvents or one or more water immiscible solvents, or combinations thereof. The coating composition of the present disclosure includes from about 15 percent by volume to about 99 percent by volume of fluid medium, based on the total volume of the coating composition. In particular embodiments, the fluid medium content may be in the range of from about 30 percent by volume to about 80 percent by volume, or in the alternative from about 35 percent by volume to about 75 percent by volume, or in the alternative from about 40 percent by volume to about 70 percent by volume, based on the total volume of the coating composition.

[0068] Fluid medium content of the coating composition may preferably be controlled so that the solids content (base polymer(s), polymeric stabilizing agent(s), polymeric coupling agent and optionally polymeric performance improving agent(s)) is from about 15 percent to about 99 percent by weight of the coating composition. In particular embodiments, the solids range may be from about 15 percent to about 85 percent by weight of the coating composition. In other particular embodiments, the solids range may be from about 30 percent to about 80 percent by weight of the coating composition. In other particular embodiments, the solids range is from about 35 percent to about 75 percent by weight of the coating composition. In certain other embodiments, the solids range is from about 40 percent to about 70 percent by weight of the coating composition.

[0069] The coating composition of the present disclosure may optionally be blended with one or more cross-linkers such as those described in PCT Publication No. WO/2011/011707. These cross-linkers may be organic, or inorganic (i.e., zinc nanoparticles) in nature, or mixtures thereof. The coating composition of the present disclosure may also be optionally be blended with one or more binder compositions such as acrylic latex, vinyl acrylic latex, styrene acrylic latex, vinyl acetate ethylene latex, and combinations thereof; optionally one or more fillers; optionally one or more additives such as catalysts, wetting agents, defoamers, flow agents, release agents, slip agents, anti-blocking agents, additives to mask sulfur staining, pigment wetting/dispersion agents, anti-settling agents, UV stabilizers, adhesion promoters; optionally one or more lubricants such as fatty acid ester wax, silicon-based wax, fluorine-based wax, polyethylene or any other similar polyolefin wax, carnauba wax, lanolin wax or the like; optionally one or more corrosion inhibitors such as aluminum, and zinc: optionally one or more pigments, e.g., titanium dioxide, barium sulfate, mica, calcium carbonate, silica, zinc oxide, milled glass, aluminum trihydrate, talc, antimony trioxide, fly ash, and clay or the like; optionally one or more co-solvents, e.g., glycols, glycol ether, 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate, alcohols, mineral spirits, aromatic solvents and benzoate esters or the like; optionally one or more dispersants, e g , aminoalcohols, and polycarboxylates; optionally one or more surfactants; optionally one or more preservatives, e.g., biocides, mildewcides, fungicides, algaecides, and combinations thereof; optionally one or more thickeners, e.g., cellulosic based thickeners such as hydroxyethyl cellulose, hydrophobically modified alkali soluble emulsions (HASE thickeners such as UCAR POLYPHOBE TR-116) and hydrophobic ally modified ethoxylated urethane thickeners (HEUR); or optionally one or more additional neutralizing agents, e.g., hydroxides, amines, ammonia, and carbonates; optionally one or more solvents or coalescing agents.

[0070] In addition, the coating composition may be blended with one or more dispersions, emulsions, suspensions, colloidal suspensions, and the like.

[0071] The coating composition can be formed by any number of methods recognized by those of ordinary skill in the art. Dispersion equipment can be operated in batch, semi-batch, or continuous mode. Examples of mixers used in the dispersion include rotor-stator, microfluidizer, high pressure homogenizer, ultrasonic, impinging jet, Cowles blade, planetary mixers, and melt kneading devices such as extruders.

[0072] In one embodiment, the base polymer and the polymeric stabilizing agent are melt-kneaded in an extruder along with the fluid medium (e.g., water) and optionally the neutralizing agent to form a dispersion. In another embodiment, the base polymer and the polymeric stabilizing agent are compounded, and then melt-kneaded in an extruder in the presence of the fluid medium (e.g., water), and optionally the neutralizing agent, thereby forming a dispersion. In some embodiments, the dispersion may first be diluted to contain from about 1% to about 20%, from about 1% to about 5%, or from about 1% to about 3%, by weight of the fluid medium; and then subsequently, the dispersion may further be diluted to comprise greater than about 25% by weight of the fluid medium. In one embodiment, further dilution may be accomplished via water and/or a solvent as provided herein.

[0073] Melt-kneading means known in the art may be used. In some embodiments, a kneader, a BANBURY mixer, single-screw extruder, or a multi-screw extruder, e.g., a twin screw extruder, is used. One example of a suitable extruder system is provided in PCT publication WO 2011/068525 entitled Extruder Screw, which is incorporated herein by reference.

[0074] A process for producing the coating composition in accordance with the present disclosure is not particularly limited. For example, an extruder, in certain embodiments, for example, a twin screw extruder, is coupled to a back pressure regulator, melt pump, or gear pump. Exemplary embodiments also provide a neutralizing agent reservoir and an initial fluid medium reservoir, each of which includes a pump. Desired amounts of neutralizing agent and initial fluid medium are provided from the neutralizing agent reservoir and the initial fluid medium reservoir, respectively. Any suitable pump may be used, but in some embodiments, for example, a pump that provides a flow of about 150 cubic centimeters per minute (cc/min) at a pressure of about 240 bar is used to provide the neutralizing agent and the initial fluid medium to the extruder. In other embodiments, a liquid injection pump provides a flow of about 300 cc/min at about 200 bar or about 600 cc/min at about 133 bar. In some embodiments, the neutralizing agent and initial fluid medium are preheated in a pre-heater.

[0075] The base polymer, in the form of pellets, powder, or flakes, is fed from the feeder to an inlet of the extruder where the base polymer is melted or compounded. The polymeric stabilizing agent, polymeric coupling agent, and the polymeric performance improving agent can also be fed simultaneously with the base polymer into the extruder via the feeder; or in the alternative, the polymeric stabilizing agent can be compounded into the base polymer, and then fed into the extruder via the feeder. In the alternative, the polymeric stabilizing agent can be metered via an inlet prior to the emulsification zone into the molten compound including the base polymer. In some embodiments, the polymeric stabilizing agent is added with the base polymer and in other embodiments, the polymeric stabilizing agent is provided separately to the twin screw extruder. The polymer melt is then delivered from the mix and convey zone to an emulsification zone of the extruder where the initial amount of fluid medium and neutralizing agent from the fluid medium and neutralizing agent reservoirs are added through an inlet. In some embodiments, the polymeric coupling agent and the polymeric performance improving agent can be added additionally or exclusively to the fluid medium stream.

[0076] In some embodiments, further fluid medium may be added via fluid medium inlet from fluid medium reservoir in a dilution and cooling zone of the extruder. Typically, the dispersion is diluted to at least about 30 weight percent fluid medium in the cooling zone. In addition, the diluted mixture may be diluted any number of times until the desired dilution level is achieved. In some embodiments, the dispersion is further cooled after exiting the extruder by the use of a suitable heat exchanger. In other embodiments, fluid medium is not added into the twin screw extruder but rather to a stream containing the melt after the melt has exited from the extruder. In this manner, vapor pressure (e.g., steam pressure) build-up in the extruder is eliminated and the dispersion may be formed in a secondary mixing device such as a rotor stator mixer.

[0077] In another embodiment, the coating composition can be formed in a continuous high shear mixer without the use of a melt kneading extruder. In this embodiment, the first stream including one or more liquid or molten base polymers is supplied to a continuous high shear mixer from a suitable liquid pump for example, a syringe pump, gear pump, or progressive cavity pump. The first stream is flowed through a first conduit and merged continuously with a second stream containing fluid medium that is flowed through a second conduit. The first and second streams are merged into a disperser in the presence polymeric stabilizing agent, polymeric coupling agent and the polymeric performance improving agent with the neutralizing agent. The agents can be added to either the first or second stream, or as a separate stream. A third stream including the fluid medium (e.g., water) can be added downstream from the disperser. The flow rates of the streams are adjusted to achieve a dispersion having the desired amount of polymer phase and percent solids.

[0078] The disperser can be any one of a number of continuous inline mixers, for example, an IKA high-shear mixer, Oakes rotor stator mixer, Ross mixer, Silverson mixer, or centrifugal pump. The rotations-per-minute (rpm) setting of the disperser can be used to help control the particle size of the dispersed hydrophobic phase in the dispersion. The system can be heated to provide the polymer and neutralizer components at a suitable viscosity for pumping. Steam formation is reduced by controlling the pressure through the use of a backpressure regulator, gear pump, metering pump, or other suitable device near the exit of the process. In some embodiments, the dispersion is further cooled after exiting the disperser by the use of a suitable heat exchanger.

[0079] In another embodiment, the coating composition can be formed in a batch or semi-batch process using a high shear mixer where the mixer may, for example, be disposed within a pressurized tank to, for example, reduce steam formation. All or at least a portion of the dispersion is removed from the tank during processing, and optionally cooled by the use of a suitable heat exchanger.

[0080] During the preparation of the coating composition, optionally one or more additives can be added to the coating composition if desired. The additives useful in the coating composition of the present invention include for example fillers; catalysts; cross-linkers; wetting agents; defoamers; flow agents; release agents; slip agents; anti-blocking agents; additives to mask sulfur staining; pigment wetting/dispersion agents; anti-settling agents; UV stabilizers; adhesion promoters; lubricants such as fatty acid ester wax, silicon-based wax, fluorine-based wax, polyethylene or any other similar polyolefin wax, carnauba wax, lanolin wax or the like, or mixtures thereof; corrosion inhibitors such as aluminum, zinc, or mixtures thereof; pigments such as titanium dioxide, mica, calcium carbonate, barium sulfate, silica, zinc oxide, milled glass, aluminum trihydrate, talc, antimony trioxide, fly ash, and clay or the like, or mixtures thereof; dyes; co-solvents such as glycols, glycol ether, 2,2,4-trimethyl-1,3-pentanediol monoisobutyrate, alcohols, mineral spirits, and benzoate esters or the like, or mixtures thereof; dispersants such as aminoalcohols, polycarboxylates, or mixtures thereof; surfactants; defoamers; preservatives such as biocides, mildewcides, fungicides, algaecides, and combinations thereof; thickeners such as cellulosic based thickeners including hydroxyethyl cellulose, hydrophobically modified alkali soluble emulsions (HASE thickeners such as UCAR POLYPHOBE TR-116) and hydrophobically modified ethoxylated urethane thickeners (HEUR), or mixtures thereof; or additional neutralizing agents such as hydroxides, amines, ammonia, and carbonates. Any of the above compounds may be added to the coating composition formulation; or in the alternative, may be added to the dispersion post dispersion formulation process.

[0081] During the preparation of the coating composition, the polymeric stabilizing agent may also be added to the dispersion post dispersion formulation process.

[0082] Optionally, during the dispersion of the base polymer another polymer dispersion or emulsion may be used as a portion of the aqueous phase of the dispersion. Examples include, but are not limited to, dispersions, emulsions, suspensions, or colloidal suspensions containing acrylic, epoxy, polyester, polyurethane, polyolefin, polyamide and the like.

[0083] Exemplary solvents and thinners include, but are not limited to, glycol ethers, alcohols, aromatics such as aromatic hydrocarbons, white spirit, branched ketones, and esters; and mixtures thereof. Exemplary additives include, but are not limited to, catalysts, lubricants, wetting agents, defoamers, flow agents, release agents, slip agents, anti-blocking agents, additives to mask sulfur staining, pigment wetting/dispersion agents, anti-settling agents, UV stabilizers, adhesion promoters, and mixtures thereof. Pigments include, but are not limited to titanium dioxide, zinc oxide, aluminum oxide, zinc, aluminum, and mixtures thereof.

[0084] One embodiment of the present invention includes adding an epoxy resin to the waterborne dispersion composition to obtain the spray-dried protective powder coating layer useful as component (b). For example, the epoxide compound can be any conventional epoxide (or epoxy) compound.

[0085] One embodiment of the epoxy compound added to the waterborne dispersion of the present invention, may be for example a single epoxy compound used alone; or a combination of two or more epoxy compounds known in the art such as any of the epoxy compounds described in Lee, H. and Neville, K., Handbook of Epoxy Resins, McGraw-Hill Book Company, New York, 1967, Chapter 2, pages 2-1 to 2-27, incorporated herein by reference. In a preferred embodiment, the epoxy compound may include for example epoxy resins based on reaction products of polyfunctional alcohols, phenols, cycloaliphatic carboxylic acids, aromatic amines, or aminophenols with epichlorohydrin. A few non-limiting embodiments include, for example, bisphenol A diglycidyl ether, bisphenol F diglycidyl ether, resorcinol diglycidyl ether, and triglycidyl ethers of para-aminophenols. Other suitable epoxy resins known in the art include for example reaction products of epichlorohydrin with o-cresol novolacs, hydrocarbon novolacs, and, phenol novolacs. The epoxy compound may also be selected from commercially available epoxy resin products such as for example, D.E.R. 331, D.E.R.332, D.E.R. 354, D.E.R. 580, D.E.N. 425, D.E.N. 431, D.E.N. 438, D.E.R. 736, or D.E.R. 732, DER 667, DER 669, OUDRASperse WB 3001, 4001 or 6001epoxy resins available from The Dow Chemical Company.

[0086] In one preferred embodiment, a waterborne dispersion of solid epoxy (e.g., >type 1 solid epoxy) can be used in the present invention.

[0087] Generally, the amount of the epoxide used to produce the epoxy-terminated prepolymer is used in an excess amount; and can be from about 10 wt % to about 45 wt % in one embodiment, from about 15 wt % to about 45 wt % in another embodiment; and from about 10 wt % to about 25 wt % in still another embodiment; based on the weight of the components to make the epoxy-terminated prepolymer composition.

[0088] Other optional compounds that may be added to the waterborne dispersion of the present invention may include, for example, pigment dispersions, other polyolefin dispersions, epoxy curing agents, POD crosslinkers and catalysts, and the like, and mixtures thereof.

[0089] Alternative surfactants can also be used in the present invention including for example Unicid 350 available from Baker Hughes, Inc. In another embodiment, when an additional surfactant is used in the present composition, the required amount of Primacor 5980i used in the composition can be minimized to allow the powders to be dried above a temperature of about 60 C. For example, the concentration of Primacor 5980i in the composition can be reduced to a level of less than about 15 wt % in one embodiment and less than about 10 wt % in another embodiment.

[0090] In general, the process for preparing the waterborne dispersion composition of the present invention includes melt blending the required and optional components in an extruder to melt the combination of components to form a liquid melt material. For example, in one embodiment, a combination of the following components can be processed through an extruder: (i) a base polymer such as HDPE DMDA-8940 NT available from The Dow Chemical Company, (ii) a polymeric performance improving agent such as AMPLIFY GR-204 available from The Dow Chemical Company; (iii) a polymeric stabilizing agent such as PRIMACOR 5980i available from The Dow Chemical Company; (iv) a polymeric coupling agent such as LICOCENE PE MA 4351available from Clariant Corporation; and optionally any other desirable additives to form the melt blend; and then adding (v) a fluid medium such as water; and (vi) a neutralizing agent such as DMEA to the melt blend.

[0091] All the compounds of the waterborne dispersion are typically mixed and dispersed at a temperature enabling the preparation of an effective waterborne dispersion composition having the desired balance of properties for use in powder coating applications. For example, the temperature during the mixing of all components may be generally from about 100 C. to about 200 C. in one embodiment, and from about 140 C. to about 170 C. in another embodiment.

[0092] The preparation of the waterborne dispersion of the present invention, and/or any of the steps thereof, may be a batch or a continuous process. The mixing equipment used in the process may be any vessel and ancillary equipment well known to those skilled in the art.

[0093] The process for preparing the polyolefin powder of the present invention includes spray drying the waterborne dispersion, and optionally spray drying a blend of polyolefin dispersion with epoxy dispersion. While spray drying is one preferred embodiment of a method to produce the dry powder, other possible methods may include for example, a two-step process including the steps of (i) pan drying the dispersion and (ii) then grinding the pan dried material into a fine powder; and filtration of the waterborne dispersion follow but by a water wash and drying.

[0094] A substrate, such as a metal pipe, is first covered with a FBE. Then the spray-dried powder coating is applied onto at least a portion of the FBE.

[0095] The spray-dried powder is then cured.

[0096] The curing of the powder coating composition may be carried out at a predetermined temperature and for a predetermined period of time sufficient to cure the composition to produce the protective coating layer. For example, the temperature of curing the formulation may be generally from about 180 C. to about 250 C. in one embodiment; from about 200 C. to about 240 C. in another embodiment; and from about 220 C. to about 230 C. in still another embodiment.

[0097] Generally, the curing time for the powder coating composition may be chosen between about 0.5 minutes to about 10 minutes in one embodiment, between about 1.0 minutes to about 5 minutes in another embodiment, and between about 2.0 minutes to about 3 minutes in still another embodiment. Below a period of time of about 1.0 minute, the time may be too short to ensure sufficient curing conditions; and above about 10 minutes, the time may be too long to be practical or economical.

[0098] For example, the coating of the present invention exhibits an impact resistance generally of between about 1.0 and about 10.0 Joules per millimeter of coating (J/mm) in one embodiment, between about 2.0 and about 5.0 J/mm in another embodiment, and between about 3.0 and about 4.0 J/mm in still another embodiment. The impact resistance of the coating can be measured by the method described in Clause 12.12 of CSA Z245.20.

[0099] The present invention is primarily used to produce the protective coating for various enduse applications. For example, the coating can be used to protect steel pipe used in pipeline construction from corrosion, concrete reinforcing bars (rebar) and on a wide variety of piping connections such as valves, fittings, and the like using powder coating or fluidizing bed techniques.

[0100] The properties of the coatings of the present invention advantageously allow the coatings to be used in various other fields and applications. For example, the coatings can be used as protective coatings in the paints and other coatings industries.

[0101] The coating of the present invention is used, for example, to provide a protective coating for a metal pipe. Once the various layers of the present invention are prepared, conventional methods and known techniques in the art can be used to apply the coating layers onto the metal pipe. For example, U.S. Patent Application Publication No. US20040191515 Al incorporated herein by reference, describes methods for performing the coating process for a metal pipe; and generally such process can be used to prepare the coating for a metal pipe in the present invention.

[0102] Generally, the method for coating a pipe includes the following steps of: (1) cleaning the pipe to a white metal finish; (2) heating the pipe to a targeted temperature; (3) applying a FBE coating to the surface of the pipe; (4) applying one or more protective layer(s) to the surface of the FBE coating; and (5) quenching the coated pipe.

EXAMPLES

[0103] The following examples and comparative examples further illustrate the present invention in detail but are not to be construed to limit the scope thereof.

[0104] Various terms and designations used in the following examples are explained herein below:

[0105] DMEA stands for N,N-dimethylethanolamine

[0106] PP stands for polypropylene.

[0107] HDPE stands for high density polyethylene.

[0108] POD stands for polyolefin dispersion.

[0109] 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N is a powder coating and commercially available from 3M Company.

[0110] POLYARMOR G 17 is a thermoplastic powder coating commercially available from PROTECH Company, and is used in the Examples as a commercial control.

[0111] HDPE DMDA-8940 NT is a high density polyethylene and commercially available from The Dow Chemical Company.

[0112] AMPLIFY GR-204 is 2,5-furandione modified ethylene/hexene-1 polymer and commercially available from The Dow Chemical Company.

[0113] AFFINITY GA1900 is ethylene-1-octene copolymer and commercially available from The Dow Chemical Company.

[0114] PRIMACOR 5980i is ethylene/acrylic acid copolymer and commercially available from The Dow Chemical Company.

[0115] LICOCENE PE MA 4351 is ethylene/maleic anhydride copolymer and commercially available from Clariant Corporation.

[0116] 6D43 Polypropylene is 1-propene, polymer with ethene and commercially available from Braskem Corp.

[0117] BHX-10083 is maleated propene homopolymer and commercially available from Baker Hughes.

[0118] BHX-10016 is maleated propene homopolymer and commercially available from Baker Hughes.

[0119] Unicid 350 is a mono-carboxylic acid functional alkane and commercially available from Baker Hughes, Inc.

[0120] DER 669E is an epoxy resin having an EEW of 2500 to 4000 grams/equivalent and commercially available from The Dow Chemical Company.

[0121] DER 667E is an epoxy resin having an EEW of 1600 to 1950 grams/equivalent and commercially available from The Dow Chemical Company.

[0122] DER 331 is an epoxy resin having an EEW of from 182 to 192 grams/equivalent and commercially available from The Dow Chemical Company.

[0123] E-Sperse 100 is an anionic surfactant and commercially available from Ethox Chemical.

[0124] PLURONIC F108 is non-ionic surfactant and commercially available from BASF Corporation.

[0125] DOWFAX 2A1 is an anionic surfactant and commercially available from The Dow Chemical Company.

[0126] 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N is a fusion bonded epoxy and is commercially available from the 3M Corporation.

[0127] The aqueous dispersions or dry powders were tested according the following testing procedures to measure various properties:

[0128] Particle Size Measurement

[0129] Particle size was measured using a COULTER LS-230 or COULTER LS-13-320 particle size analyzer (Beckman Coulter Corporation).

[0130] To measure the mean particle size of the spray dried powder, powder was dispersed into deionized (DI) water at 1 percent (%) solids by weight and vortexed for 30 seconds (s) twice. Particle size of the powder was measured with a Beckman Coulter LS 13 320 Laser Light Diffraction Particle Size analyzer, using an optical model predetermined by the instrument software. The volume average particle size of the powder was determined.

[0131] Measurement Percent Solids

[0132] Percent solids was measured using a microwave solids analyzer or an infrared solids analyzer. One analyzer used was the OHAUS MB45 infrared moisture analyzer (available from Ohaus Corporation).

[0133] The coated panels were tested according the following testing procedures to measure the various properties of the coatings:

[0134] Thickness Measurement

[0135] The thickness of the coating layer was measured according to ASTM-D 1186-93 which is a non-destructive measurement of dry film thickness of non-magnetic coatings applied to a ferrous base, using a POSITECTOR 6000 coating thickness gauge. A standard panel without any coating was used for calibration. The thickness of the coating layer on the coated panels was the average of a minimum of 4 separate measurements. The measured thickness is reported in mils (25 micrometers/mil).

[0136] Adhesion

[0137] The cross-hatch adhesion of the coating layer was measured according to ASTM-D 3359-08. This method includes making a square lattice pattern with 10 cuts in each direction with 1 millimeter (mm) distance between neighboring cuts on the coating layer. A pressure sensitive tape over the cut area is applied and then the tape is pulled parallel to the substrate surface. Adhesion is evaluated by visual observation and designating the results using a scale from 0B to 5B as described in the table below, with 5B indicating perfect adhesion to the substrate and 0B indicating complete removal of the coating from the substrate.

TABLE-US-00001 Rating Description 5B The edges of the cuts are completely smooth; none of the squares of the lattice is detached. 4B Small flakes of the coating are detached at intersections; less than 5% of the area is affected. 3B Small flakes of the coating are detached along the edges and at intersections of cuts. The area affected is 5-15% of the lattice. 2B The coating has flaked along the edges and on parts of the squares. The area affected is 15-35% of the lattice. 1B The coating has flaked along the edges of cuts in large ribbons and whole squares have detached. The area affected is 35-65% of the lattice. 0B Flaking and detachment is worse than 1B.

[0138] Acid/Base Resistance

[0139] The acid resistance of the coating layer was tested using 98% (mass fraction) sulfuric acid, 37% (kg HCl/kg) hydrochloric acid, and acetic acid (12 Normality); and the base resistance of the coating layer was tested using 50% (kg NaOH/kg) sodium hydroxide. This method includes placing drops of each of the acids, or base, on the coating surface and then placing a plastic cap over the acid/base/methanol to inhibit evaporation. Acid or base, can be added as needed, to maintain exposure of the coating. The samples are kept at room temperature (about 23 C.) for 7 days and then subsequently completely rinsed with water. After the samples dry, the adhesion of the coating layer is tested and its performance is rated on a scale of from 1 to 5, with 5 indicating an intact coating and 1 indicating a completely etched coating based on adhesion of the coating after exposure.

[0140] Solvent Resistance (MEK Double Rub)

[0141] The solvent resistance of the coating layer was tested according to ASTM D4752 using methyl ethyl ketone (MEK). In this method, samples are tested using a piece of cotton cheesecloth attached with copper wire to a 0.68 kg hammer The cheesecloth is saturated with MEK and then placed on the coating. The hammer is pushed forward and then back at a rate of approximately 1 second per cycle. The coating layer is visually inspected after every 20 double rub cycle for any signs of damage or delaminating. This procedure is repeated until a bare panel is showing (at this observation point, record the number of double rubs as the MEK double rub (DR) result for the sample) or until a total of 200 double rubs is reached. Alternatively, an automated tester, available from DJH Designs may be used to measure the number of double rubs. The automated tester works in a semi-automatic fashion by moving a cotton pad, attached to a weighted block, that applies about 0.15 kg/cm.sup.2 pressure, in a back and forth motion across the coated panel. Each back and forth is referred to as one double rub.

[0142] Impact Resistance

[0143] The impact resistance of the coating layer was measured using a GARDNER falling weight impact tester according to ASTM D-2794. In this method, indentation in both direct and indirect modes is measured; and the units of measure are inch-lbs (2.54-.

[0144] Mandrel Wedge Bend

[0145] The mandrel wedge bend flexibility of the coating layer was tested using a conical mandrel following ASTM D522-93a. Measurements are in millimeters from the small end of the mandrel to where cracking has ceased.

[0146] Hot-Wet Adhesion

[0147] The hot-wet adhesion of the coating layer was measured after 2 days, 4 days, 7 days, and 14 days at 753 C. Using this method, test specimens are immersed in a temperature controlled tap water bath at 75 C. At set intervals the specimens are removed from the bath, and within 1 hour (hr) of removal, an approximately 30 mm x 15 mm rectangle is scribed with a utility knife all the way through the coating layer to the substrate. The adhesion performance of the coating is ranked on a scale of from 1 through 5 (with 1 being the best and 5 being the worst) depending upon the resistance demonstrated by the coating to the levering action of the utility knife (as described in the cathodic disbondment testing method below).

[0148] Cathodic Disbondment

[0149] To measure cathodic disbondment of a coating layer, a 6.4 mm diameter holiday is drilled through the coating layer to expose the steel substrate. A hollow plastic cylinder is centered over the holiday, filled with a 3% saline solution and covered with a lid. A reference electrode is inserted in to the solution and connected to a positive terminal from a DC power supply while a bare spot prepared on the specimen is attached to a negative terminal. The assembly is placed in an oven at 65 C. for 48 hr while 3.5 volts (V) (negative relative to the calomel reference electrode) is applied. Upon testing completion the cell is dismantled and the test specimen is air cooled on the bench top. Within 1 hr, the disbondment of the coating is evaluated using a utility knife by inserting a tip of the blade under the primer at the holiday and levering off the primer until a definite resistance is experienced. The resulting disbonded radius is recorded from the edge of the original holiday.

[0150] Low Temperature Impact Resistance

[0151] The low temperature impact resistance of coated panels can be tested as follows: coated panels are first placed in a Thermo Scientific Revco Ultra-low Temperature Chest Freezer and cooled to 32 C. for at least 4 hr prior to testing. Upon removal of the coatings from the freezer, the cooled specimens are horizontally mounted on a magnetized stage in an impact tester. Impact energy is applied to the coated panel by dropping a 1.82 kg mass from preset heights with 1.5 Joule (J) increments. All tests are complete within 30 s. The tested coated panel samples are allowed to warm to room temperature. After the coating surface is patted dry using a paper towel, a DC holiday tester is used to detect any coating failures.

Examples 1-9

Dispersion Preparation

[0152] In Examples (Ex.) 1-9, various aqueous dispersions, using the components and conditions as described in Table I, were prepared using the following general procedure:

[0153] Components 1-4 listed in Table I were fed into a 25 mm diameter twin screw extruder using a controlled rate feeder; using the feed rate in grams/minute (g/min) as indicated in Table I. Components 1-4 were forwarded through the extruder and melted to form a liquid melt material.

[0154] The extruder temperature profile was ramped up to approximately 160 C. Water and neutralizing agent were mixed together and fed to the extruder at a rate indicated in Table I for neutralization at an initial water introduction site. Then dilution water was fed into the extruder via two separate pumps into a dilution zone of the extruder at two locations (1.sup.st and 2.sup.nd locations) of the dilution zone at a rate indicated in Table I. The extruder temperature profile was cooled back down to a temperature below 100 C. near the end of the extruder. The extruder speed was approximately 1,200 revolutions per minute (rpm). At the extruder outlet, a backpressure regulator was used to adjust the pressure inside the extruder barrel to a pressure adapted to reduce steam formation (generally, the pressure was from about 2 MPa to about 4 MPa).

[0155] An aqueous dispersion product exited from the extruder. The aqueous dispersion was filtered through a 200 micrometer (m) filter. The resultant filtered aqueous dispersion had a solids content measured in weight percent (wt %); and the solids particles of the dispersion had a mean particle size measured in microns (or micrometers). The solids content of the aqueous dispersion was measured using an infrared solids analyzer; and the particle size of the solids particles of the aqueous dispersion was measured using a COULTER LS-230 particle size analyzer (available from Beckman Coulter Corporation). The solids content and the mean particle size (PS) of the solids particles of the dispersion are described in Table I.

TABLE-US-00002 TABLE I Composition and Process Conditions for Examples 1-9 Extruder Tem- perature Com- Com- Com- Com- Initial Dilution in ponent ponent ponent ponent Water Base/ Water Polymer Ex- Ex- 1 2 3 4 (feed Surfactant 1.sup.st/2.sup.nd Melt truder ample (feed rate (feed rate (feed rate (feed rate rate in (feed rate (feed rate Zone Speed % No. in g/min) in g/min) in g/min) in g/min) g/min) in g/min) in g/min) ( C.) (rpm) Solids P.S. pH 1 HDPE AM- PRIMA- LICOCENE (67) DMEA 240/16 160 1200 47.9 0.77 10.1 DMDA PLIFY COR PE MA (30) 8940 GR- 5980i 4351 NT 204 (72) (21) (189) (42) 2 HDPE AM- PRIMA- LICOCENE (60.5) DMEA 240/14 160 1200 46.6 0.68 10.3 DMDA PLIFY COR PE MA 4351 (32) 8940 GR-204 5980i (27.5) NT (40.3) (42.4) (192) 3 HDPE AMP- PRIMA- LICOCENE (66.6) DMEA 240/24 160 1200 47.0 0.68 10.1 DMDA LIFY COR PE MA (32.6) 8940 GR-204 5980i 4351 NT (32.5) (71.6) (21.2) (198.5) 4 PP 6D43 BHX- UNICID (5.8) DMEA 75/0 170 470 n.d. 2.13 9.0 (64) 10083 350 (2) (5.8) (5.8) 5 PP 6D43 BHX- UNICID (6.7) DMEA 54/0 170 470 54.6 2.09 9.0 (64) 10016 350 (2) (5.8) (5.8) 6 DER 667E (6.6) E-SPERSE 74/0 150 450 55.4 0.61 7.0 (96) 100 (4) 7 DER 669E DER 331 (6.6) E-SPERSE 68/0 150 450 58.2 1.00 6.6 (90) (10) 100 (4) 8 AFFINITY (5.56) EMPICOL 102/0 80 450 46.9 0.50 3.5 GA1900 ESB-70 (90.4) 3.0 9 AFFINITY TiO.sub.2 (8.7) PLURONIC (163/0) 130 450 56.1 0.42 8.0 GA1900 (148.5) F108/ (60) DOWFAX 2A1 (6.2/5.4)

Examples 10-12

Epoxy/Polyolefin Blend Dispersion Preparation

[0156] The polyolefin dispersion of Example 4 above was blended with the epoxy dispersion of Example 6 to make a 10% epoxy/90% polyolefin blend (Example 10).

[0157] The polyolefin dispersion of Example 5 above was blended with the epoxy dispersion of Example 6 to make a 10% epoxy/90% polyolefin blend (Example 11).

[0158] The polyolefin dispersion of Example 2 was blended with the epoxy dispersion of Example 7 to make a 10% epoxy/90% polyolefin blend (Example 12).

[0159] In the above blends, the epoxy dispersions were mixed with the polyolefin dispersions within 1 hr before spray drying the blends.

[0160] A few characteristics of some of the above blends of polyolefin and epoxy dispersions prepared in Examples 10-12 are shown in Table II.

Examples 13 and 14

Polyolefin/Polyolefin Blend Dispersion Preparation

[0161] A polyolefin dispersion blend was prepared by blending the dispersion of Example 1 with the polyolefin dispersion of Example 8 to form the polyolefin dispersion blend (Example 13). In preparing the above polyolefin dispersion blend, the dispersions were blended at a ratio of 10% Example 8 dispersion to 90% Example ldispersion.

[0162] Another polyolefin dispersion blend was prepared by blending the dispersion of Example 1 with the polyolefin dispersion of Example 9 to form the polyolefin dispersion blend (Example 14). In preparing the above polyolefin dispersion blend, the dispersions were blended at a ratio of 10% Example 9 dispersion to 90% Example 1 dispersion.

[0163] Characteristics of the above blends of dispersions prepared in Examples 13-14 are shown in Table II.

TABLE-US-00003 TABLE II First Second Dispersion and Dispersion and Ex. Polyolefin Blend Dispersion amount amount No. Type (%) (%) 10 Epoxy + Polyolefin Ex. 6 Ex. 4 (10) (90) 11 Epoxy + Polyolefin Ex. 6 Ex. 5 (10) (90) 12 Epoxy + Polyolefin Ex. 7 Ex. 2 (10) (90) 13 Polyolefin-Polyolefin Ex. 8 Ex. 1 (10) (90) 14 Polyolefin/TiO2-Polyolefin Ex. 9 Ex. 1 (10) (90)

Examples 15-23

Spray-Dried Powder Preparation

[0164] The aqueous polymer compositions of the present invention, including the polyolefin dispersions and the polyolefin/epoxy dispersion blends prepared in Examples 1-14 were spray dried to prepare Examples 15-23 according to the following general procedure:

[0165] A two-fluid nozzle atomizer was equipped on a MOBILE MINOR 2000 Model H spray dryer (available from GEA Process Engineering Inc.). The nitrogen pressure to the nozzle was fixed at 1 bar (100 kPa) with 50% flow which is equivalent to about 6.0 kg/hr of air flow. A glass jar was placed under the cyclone of the dryer with a valve on the bottom of the cyclone open. Each of the aqueous dispersions (the olefin or olefin-epoxy dispersions), individually or as a blend, (about 40-50 wt % solid content) was pumped into a heated chamber of the dryer by an emulsion feed pump. The spray drying process was conducted in a nitrogen (N.sub.2) environment with an inlet temperature of the dryer fixed at 120 C. The outlet temperature of the dryer was controlled at about 45 C. by tuning the feed rate of the dispersion (generally at a feed rate of about 20-30 milliliters per minute [mL/min]). In some examples, hydrophobic surface modified CaCO3 (WINNOFIL S, from Solvay Chemicals) was fed into the heated chamber of the spray dryer to act as an anti-caking agent. The amount of modified CaCO3 added was about 1 wt % based on the total formulation. Most of the resultant dry powder was recovered in the glass jar attached to the cyclone. The mean particle size of the dry powder was measured to be in the range of from about 10 m to about 80 m.

[0166] Table III shows a few characteristics of the various polyolefin powders and polyolefin-epoxy hybrid powders prepared by the above spray drying procedure.

TABLE-US-00004 TABLE III Spray Dried Powder Formulation and Properties Aqueous Dispersion or Dispersion Blend used to Powder Ex. prepare powder (Example V.sub.mean Moisture No. Number) Polymer Type (m) (%) 15 5 Polyolefin 16 11 Epoxy + Polyolefin 16.1 0.97 17 4 Polyolefin 18 10 Epoxy + Polyolefin.sup.a 19 2 Polyolefin 19.0 2.23 20 12 Epoxy + Polyolefin.sup.b 21.3 2.54 21 13 Polyolefin + Polyolefin.sup.c 68.9 3.8 22 1 Polyolefin.sup.c 30.3 4.63 23 14 Polyolefin + Polyolefin-TiO.sub.2.sup.c 69.1 4.76 Notes for Table III .sup.aDER 667E/E-Sperse100 (96/4) Vmean = 0.615 m, epoxy dispersion was mixed into POD within 1 hr before spray drying .sup.bDER 669E/331/E-Sperse 100 (90/10/4) Vmean = 0.998 m, epoxy dispersion was mixed into POD within 1 hr before spray drying .sup.cOne (1) % CaCO3 was used as anticaking agent during spray drying. Large mean particle size after drying is likely caused by high solid content (high viscosity)

Examples 24-30

POD Powder Coating on Steel Substrates

[0167] Phosphate treated steel panels (Q-panels), generally 800 microns thick, were coated with between 37 and 150 microns of the polyolefin, or polyolefin/epoxy powders using a NORDSON Sure Coat manual cup spraying gun. The spraying gun parameters were 95 kV, with 68.9 kPa fluidizing, atomizing, and auxiliary air flows. The panels were heated to 200 C. after which the powder was applied to the panels. Following application of the powder, the panels were cured at 140-200 C. for 5 minutes (min). In contrast, the comparative material, POLYARMOR G-17, was cured for 20 min at 200 C.

Examples 31-34

1-BE/POD Coating Preparation

[0168] Part AGeneral Powder Coating Procedures for a Two-Layer FBE/POD Coating

[0169] Preparation of a 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N (Control #1) is carried out as follows: 4 steel panels (76 mm203 mm3 mm) are preheated at 240 C. for 30 min. Each panel is coated with the 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N using a fluidized bed method well known to those skilled in the art. Each coated panel is post cured at 240 C. for 3 min in a post cure oven. The cured coated panels are removed from the oven and the panels are placed into a water container to quench for about 2-3 min. The coating thickness of the panels is measured and can be from about 380 m to about 410 m thick.

[0170] Alternatively, preparation of a 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N (Control #2) is carried out as follows: 4 steel panels (76 mm203 mm3 mm) at 240 C. for 30 min Each panel is coated with the 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N using a fluidized bed method well known to those skilled in the art. Each coated panel is post cured at 240 C. for 3 min in a post cure oven. The cured coated panels are removed from the oven and placed into a water container to quench for about 2-3 min. The coating thickness of the panels is measured and can be about 200 m to about 250 m thick.

[0171] Coating the fusion bonded epoxy substrates with each of the above POD coatings is carried out as follows: each panel is coated with 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N using a fluidized bed method well known to those skilled in the art. The coating thickness of each panel is measured and can be from about 200 microns to about 250 microns thick. Each coated panel is post cured at 240 C. for 1.5 min in a post cure oven. The cured coated panels are removed from the oven and placed on a copper bar in a spray booth. When the coated panel temperature cools to 200 C., each panel is spray coated with each of the POD powders using a NORDSON Sure Coat manual cup gun. The spraying gun parameters are 95 kV, with 68.9 kPa fluidizing, atomizing, and auxiliary air flows. The panels are heated to 200 C. after which the powder is applied to the panels. The above process is repeated three more times. A total of four panels are prepared according to the above process. Each of the four panels is placed into a post cure oven (heated at 200 C.) for 3 min. The panels are removed from the oven and placed into a water container to quench for about 2 min to about 3 min. The coating thickness of the panels is measured and can be from about 200 m to about 250 m thick. Table IV shows the coating thickness of the coatings prepared by the above process.

TABLE-US-00005 TABLE IV Coatings and Properties Prepared from Coating Example powder of Thickness No. Example Coating Polymer Type (mils) 24 POLYARMOR G 17 3.8 25 15 Polyolefin ~5 26 16 Epoxy + Polyolefin ~4 27 17 Polyolefin 2.8 28 18 Epoxy + Polyolefin 3.8 29 19 Polyolefin 2.4 30 20 Epoxy + Polyolefin 2.4 31 21 Polyolefin + Polyolefin 8.0 32 22 Polyolefin 8.4 33 23 Polyolefin + Polyolefin-TiO.sub.2 8.0 34 3M SCOTCHKOTE 8-15 Fusion-Bonded Epoxy Coating 226N

[0172] Part B: Performance Results

[0173] The coated panels from Part A were tested to measure the various properties of the coatings. Tables V, VI and VII summarize the performance testing on POD films wherein the POD films were powder coated directly to metal panels.

[0174] Table VIII summarizes the performance for POD films coated onto fusion bonded epoxy. Table VIII also includes performance data for two epoxy controls.

TABLE-US-00006 TABLE V Performance of Polypropylene Powder Coatings on Metal Panels Coating from Example Powder of Coating Hard- Impact Impact Mandrel No. Ex. No. Type ness MEK Direct Reversed Adhesion (mm) 24 POLY- 34 200 120 120 5 0 ARMOR G 17 (Commercial Control) 25 15 PP 93 200 0 0 0 22 26 16 PP + 10% 93 200 0 0 0 60 Epoxy 27 17 PP 79 200 0 0 1 0 28 18 PP + 10% 93 200 0 0 4 16 Epoxy

TABLE-US-00007 TABLE VI Chemical Resistance (7 day exposure) Acid/Base (concentrated) of Polypropylene Powder Coatings on Metal Panels Example Polypropylene 50 wt % No. Coating Type HC.sub.2H.sub.3O.sub.2 HCl H.sub.2SO.sub.4 NaOH 24 POLYARMOR 5 5 5 5 G 17 (Commercial Control) 25 PP 4 0 0 0 26 PP + 10% Epoxy 4 0 4 4 27 PP 4 0 0 0 28 PP + 10% Epoxy 4 4 3 4

[0175] Tables V and VI above list the performance results for steel panels coated with the polypropylene dispersions 10% epoxy dispersion. POLYARMOR G-17 is a commercial control.

Examples 29-30

POD Powder Coating Preparation

[0176] In these Examples 29-30, two powder coatings were made using a high density polyethylene dispersion. One coating sample was prepared with the HDPE dispersion alone; and one coating sample was prepared using a 10% epoxy dispersion blended in with the HDPE dispersion. The coating samples were prepared and tested as described in Examples 24-30 above for powder coated on steel substrates.

[0177] Table VII lists the performance results for the two powder coatings. As shown in Table VII, the two powders show significant improvement in both mechanical properties (e.g., direct and indirect impact, and mandrel wedge bend), as well as chemical resistance (e.g., MEK double rubs and acid/base resistance) compared to PP (Examples 25-28) powders. As indicated in Table VI, the HDPE powder has an acid/base resistance equivalent to POLYARMOR G-17, but the HDPE powder has better direct impact and double the hardness than POLYARMOR G-17. Also, the adhesion and mandrel wedge bend performance properties of the HDPE powder are equivalent to that of the POLYARMOR G-17 control.

TABLE-US-00008 TABLE VII Performance of High Density Polyethylene Powder Coatings on Metal Panels Coating from Example Powder Hard- Ad- MEK Direct Reversed Wedge Acetic 37% 98% 50% No. of Ex. ness hesion DR Impact Impact Bend Acid HCl H.sub.2SO.sub.4 NaOH 29 19 67 5B 200 160 100 4 mm 5B 5B 5B 5B 30 20 64 5B 200 160 100 3 mm 5B 3B 4B 5B

Examples 31-34

FBE/POD Coating Preparation

[0178] In these Examples 31-34, powder coatings were made using a high density polyethylene dispersion; and the performance of the powder coatings was compared to a fusion bonded epoxy Control (Ex. 34: 3M SCOTCHKOTE Fusion-Bonded Epoxy Coating 226N).

[0179] One coating sample was prepared using a blend of (i) the HDPE dispersion and (ii) TiO.sub.2 encapsulated with AFFINITY GA1900 (Example 31). One coating sample was prepared with the HDPE dispersion alone (Example 32); one coating sample was prepared using a 10% AFFINITY GA1900 blended in with the HDPE dispersion (Example 33); and the other sample was a fusion bonded epoxy control described in Example 34. The coating samples were prepared and tested as described above.

[0180] Table VIII lists the performance results for the fusion bonded epoxy Control (Example 34) and the three powder coatings (Examples 31-33) made from a HDPE dispersion and applied over a FBE. Cathodic disbondment was measured after 48 hr, and as shown in Table VIII. All of the powder coated samples (Examples 31-33) had the same, or better, cathodic disbondment as the fusion bonded epoxy Control (Example 34). In addition, the hot/wet adhesion results, up to the 14th day measurement, for the powder coatings (Examples 31-33) were equivalent to the FBE Control (Example 34). The impact resistance of the HDPE coated FBE (Examples 31-33) was significantly improved over the FBE layer itself (Example 34).

TABLE-US-00009 TABLE VIII Performance of HDPE and HDPE/Hybrid Powders on FBE Impact Impact Cathodic (1.5 J) (3.0 J) Coating Hot-wet Hot-wet Hot-wet Hot-wet Dis- 32 C./ 32 C./ Ex. of Adhesion Adhesion Adhesion Adhesion bondment 1 hr 1 hr No. Example (2 Days) (4 Days) (7 Days) (14 Days) (mm) (# holidays) (# holidays) 31 27 1 1 1 5 4.0 0 0 32 28 1 1 1 5 4.0 0 0 33 29 1 1 1 5 4.0 0 0 34 3M 1 1 1 1 4.0 3 3 SCOTCH KOTE Fusion- Bonded Epoxy Coating 226N