POLYAMIC ACID RESIN IN REACH-APPROVED SOLVENT SYSTEM FOR WIRE COATING APPLICATIONS

Abstract

The present invention discloses a polyamic acid resin composition in a REACH-approved solvent system for use in wire coating applications. The polyamic acid resin composition comprises a molecular weight greater than 8,000 grams per mole, more preferably greater than 20,000 grams per mole. The REACH-approved solvent system comprising a primary REACHapproved solvent with one or more optional secondary REACH-approved co-solvents. The secondary REACH-approved co-solvent can be reactive or non-reactive with dianhydride. The present invention also discloses the elimination of solvents in polyamic acid resin to produce a REACH-approved polyamic acid resin powder.

Claims

1. A method for preparing polyamic acid, comprising: reacting a dianhydride and a diamine at a molar ratio of 0.95 to 0.99:1.

2. Polyamic acid, obtained by reacting a dianhydride and a diamine at a molar ratio of 0.95 to 0.99:1.

3. A polyamic acid resin composition, comprising: polyamic acid obtained by reacting a dianhydride and a diamine at a molar ratio of 0.95 to 0.99:1; and at least one solvent approved under the Registration, Evaluation, Authorization, Restriction of Chemicals (REACH) regulation (REACH-approved solvent).

4. The polyamic acid resin composition of claim 3, wherein the at least one REACH-approved solvent comprises 80 to 100 wt % of a primary solvent and 0 to 20 wt % of a secondary co-solvent.

5. A method for coating a wire, comprising: applying the polyamic acid resin composition of claim 3 onto a surface of a wire.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0018] According to the first embodiment of the present invention, the molar ratio is reduced below an equimolar ratio of dianhydride to diamine to reach a molecular weight of the polyamic acid resin above 8,000 grams per mole, more preferably above 20,000 grams per mole. The molar ratio of dianhydride to diamine can vary, depending on the molecular weight of dianhydride and diamine used. Reducing the molar ratio of dianhydride to diamine will allow for viscosity adjustments in REACH-approved solvents, such as dimethyl sulfoxide, that produce high viscosity polyamic acid resins with equimolar compositions of dianhydride and diamine. Viscosity of the polyamic acid resin is reduced to between 5 and 500 poise. Reducing the viscosity allows for the system described in the present invention to be compatible with existing wire coating processes and equipment.

[0019] Examples of dianhydride compatible with the first embodiment of the present invention include, but are not limited to pyromellitic dianhydride, 2,3,6,7-naphthalenetetracarboxylic dianhydride, 3,3′,4,4′-biphenyltetracarboxylic dianhydride, 1,2,5,6-naphthalenetetracarboxylic dianhydride, 2,2′, 3,3′-biphenyltetracarboxylic dianhydride, 3,3′4,4′-benzophenonetetracarboxylic dianhydride, 2,2-bis(3,4-dicarboxyphenyl)propane dianhydride, 3,4,9,10-perylenetetracarboxylic dianhydride, bis(3,4-dicarboxyphenyl)propane dianhydride, 1,1-bis(2,3-dicarboxyphenyl)ethane dianhydride, 1,1-bis(3,4-dicarboxyphenyl)ethane dianhydride, bis(2,3-dicarboxyphenyl)methane dianhydride, bis(3,4-dicarboxyphenyl)ethane dianhydride, oxydiphthalic dianhydride, bis(3,4-dicarboxyphenyl)sulfone dianhydride, p-phenylenebis (trimellitic acid monoester acid anhydride), ethylenebis(trimellitic acid monoester acid anhydride), (bisphenol A)bis(trimellitic acid monoester acid anhydride), and analogs thereof. The dianhydrides listed may be used alone or in combination of two or more.

[0020] Examples of diamine include, but are not limited to 4,4′-diaminodiphenylpropane, 4,4′-diaminodiphenylmethane, 3,3′-dimethylbenzidine, 3,3′-dimethoxybenzidine, 3,3′-dichlorobenzidine, 4,41-diaminodiphenyl sulfide, 3,3′-diaminodiphenylsulfone, 4,4′-diaminodiphenylsulfone, 4,4′-diaminodiphenyl ether, 1,5-diaminonaphthalene, 4,4′-diaminodiphenyldiethylsilane, 4,4′-diaminodiphenylsilane, 4,4′-diaminodiphenylethylphosphine oxide, 4,4′-diaminodiphenyl-N-methylamine, 4,4′-diaminodiphenyl-N-phenylamine, 1,4-diaminobenzene (p-phenylenediamine), 1,3-diaminobenzene, 1,2-diaminobenzene, and analogs thereof. The diamines listed may be used alone or in combination of two or more.

[0021] The solvent system according to the first embodiment of the present invention comprises of a primary REACH-approved solvent and an optional secondary REACH-approved co-solvent. Equal to or more than 80 weight percent, including 100 weight percent, of the solvent system must consist of the primary REACH-approved solvent. Equal to or less than 20 weight percent, including 0 weight percent, of the solvent system consists of one or more of the secondary REACH-approved co-solvents.

[0022] Examples of primary REACH-approved solvents include, but are not limited to dimethyl sulfoxide, hexamethylphospharamide, and γ-butyrolactone.

[0023] The optional secondary REACH-approved co-solvent can be either a non-reactive or reactive with dianhydride. Examples of non-reactive secondary REACH-approved co-solvents include, but are not limited to xylene, aromatic naphtha, acetone, and 1,3-dioxolane.

[0024] Reactive secondary REACH-approved co-solvents react with the dianhydride to form an ester in cis or trans conformation according to the following reaction. The co-solvent will have a nucleophile component such as an OH— group on an alcohol. The nucleophile will react with the carbonyl groups on the dianhydride to open the rings and complex. Due to symmetry on the dianhydride, the formation of esters can either be cis or trans symmetry.

[0025] The ester formation lowers the viscosity and molecular weight of the resin at temperatures below 100° C. This reduction is due to shortened polyamic acid chains, caused by a portion of the available dianhydride reacting with the reactive secondary REACH-approved co-solvent. At curing temperatures above 100° C., the dianhydride is released from the ester and the molecular weight and viscosity increase as the polyamic acid chains increase in length with the released dianhydride.

[0026] Examples of reactive optional secondary REACH-approved co-solvents include, but are not limited to protic solvents such as hexanol, 2-ethyl-1-butanol, 2-ethyl-1-hexanol, propanol, isopropanol, ethanol, and methanol.

[0027] Additionally, the composition of the solvent system can also optionally contain an additive that is commonly known to a person having ordinary skill in the art to be suitable for the production of polyamic acid resin. For example, additives including, but not limited to hydrophobic non-ionic ethoxylates and alcohols and siloxanes can be added to adjust surface tensions and improve wettability in coating applications.

[0028] In addition to the polyamic acid resin composition taught in the present invention, the solvent system is compatible with commercially available polyamic acid materials including, but not limited to IST RC-5019, IST RC-5057, IST RC-5069, and IST RK-5097.

[0029] The polyamic acid resin disclosed in the present invention may be prepared by any method that is known to a person of ordinary skill in the art. For example, the polyamic acid resin may be prepared by adding the desired solvent system to a reactor and setting the reactor temperature to 20° C. Adding diamine to reactor and agitating the solution at 500 rpm until dissolved. Progressively adding dianhydride, in an amount that yields a molar ratio of dianhydride to diamine added that is between 0.95:1 and 0.99:1, preferably between 0.96:1 and 0.99:1, to the reactor during a period of 45 minutes with agitation speeds between 500 rpm and 800 rpm. Further agitating the solution for three hours at 300 rpm.

[0030] The second embodiment of the present invention provides a resin powder with only trace amounts of solvent remaining. The polyamic acid resin powder can be optionally made according to the first embodiment, using non-equimolar amounts of dianhydride and diamine to control the viscosity of the solution. The polyamic acid resin powder can be dissolved in a solvent system of choice. This includes non-REACH-approved solvents including, but not limited to N-methylpyrrolidone, N—N-dimethylacetamide, or dimethylformamide. The resin formed by dissolving polyamic acid resin powder in solvent can be utilized in wire coating applications. The polyamic acid resin powder is compatible with existing wire coating processes. The polyamic acid resin powder, regardless of the solvent the resin polyamic acid was originally formed in, is REACH-approved due to only trace amounts of the solvent remaining.

[0031] The polyamic acid resin powder according to the second embodiment of the present invention can be prepared by any method that is known to a person of ordinary skill in the art for the removal of solvent from polyamic acid resin. For example, a resin polyamic acid can be precipitated in water by adding the resin to a mixer filled with water at high agitation speeds. The precipitated polyamic acid can be collected, washed multiple times in water to remove additional solvent, and then dried in a vacuum oven at temperatures below 60° C. The dried polyamic acid can then be collected and is capable of being dissolved in a REACH-approved solvent.

EXAMPLES

[0032] The following examples illustrate the method for preparing the polyamic acid resin in a REACH-approved solvent system according to the first embodiment of the of the present invention. Furthermore, the following examples illustrate the retention of material properties of the resin with decreasing molecular weight, relatively low viscosity of the resin, and successful adhesion to wire of the resin in the first embodiment of the present invention.

Example 1

[0033] Example 1 is prepared by adding dimethyl sulfoxide to a reactor and setting the reactor temperature to 20° C. Adding 4,4′-diaminodiphenyl ether to reactor and agitating the solution at 100 rpm until dissolved. Progressively adding pyromellitic dianhydride, in an amount that yields a molar ratio of pyromellitic dianhydride to 4,4′-diaminodiphenyl ether added that is 0.97:1, to the reactor during a period of 45 minutes with agitation speeds between 10 to 100 rpm. Further agitating the solution for three hours at 10 rpm.

[0034] The method described in Example 1 is a preferred method for making solvent based systems.

Example 2

[0035] Example 2 is prepared using a method similar to Example 1, except pyromellitic dianhydride is added to yield a molar ratio of pyromellitic dianhydride to 4,4′-diaminodiphenyl ether added that is 0.98:1.

Example 3

[0036] Example 3 is prepared using a method similar to Example 1, except pyromellitic dianhydride is added to yield a molar ratio of pyromellitic dianhydride to 4,4′-diaminodiphenyl ether added that is 0.995:1.

Example 4

[0037] Example 4 is prepared using a method similar to Example 1, except pyromellitic dianhydride is added to yield a molar ratio of pyromellitic dianhydride to 4,4′-diaminodiphenyl ether added that is 0.96:1.

Example 5

[0038] Example 5 is prepared using a method similar to Example 1, except the solvent system 4,4′-diaminodiphenyl ether is dissolved in includes hexanol in addition to dimethyl sulfoxide.

Example 6

[0039] Example 6 is prepared using a method similar to Example 1, except the solvent system 4,4′-diaminodiphenyl ether is dissolved in includes aromatic naphtha in addition to dimethyl sulfoxide.

Comparative Example 1

[0040] Comparative Example 1 is prepared using a method similar to Example 1, except pyromellitic dianhydride is added to yield a molar ratio of pyromellitic dianhydride to 4,4′-diaminodiphenyl ether added that is 1:1.

Comparative Example 2

[0041] Comparative Example 2 is prepared using a method similar to Example 1, except the solvent system consists of dimethylformamide instead of dimethyl sulfoxide and pyromellitic dianhydride is added to yield a molar ratio of pyromellitic dianhydride 4,4′-diaminodiphenyl ether that is 1:1.

[0042] The data collected in Table 1 was performed by casting and chemically curing thin films of approximately 25 micron thickness in the laboratory using standard industry methods. The films were then cut into 0.5 inch strips and tested on an Instron 4464 model tensile tester for the physical properties of tensile strength, percent elongation, and modulus. Testing was performed following standard ASTM D-882 procedures.

TABLE-US-00001 TABLE 1 Material Properties Molar Ratio of Tensile Elonga- Young's Dianhydride Strength tion Modulus Modulus Example and Diamine (psi) (%) (ksi) (ksi) Example 1 0.97:1 23525 71.2 425 428 Example 2 0.98:1 21882 72.3 401 400 Example 3 0.995:1  24591 80.1 355 366 Comparative   1:1 24689 73.1 415 420 Example 1 Comparative   1:1 25700 71.2 399 439 Example 2

[0043] Table 1 shows that decreasing the molar ratio of dianhydride to diamine thereby decreasing the molecular weight of the polyamic acid does not significantly affect the material properties of the polyamic acid resin in REACH-approved solvent systems. Example 1, 2, and 3 are polyamic acid resins according to the first embodiment of the present invention with material properties that are acceptable for use in wire coating applications.

[0044] The data collected in Table 2 was measured by placing ˜200 g of varnish at ˜20° C. into a beaker and testing the viscosity using a Brookfield HADV-I+ viscometer. The spindle type and rotational speed values were adjusted to maintain a viscometer reading range within 25% to 75% for improved consistency.

TABLE-US-00002 TABLE 2 Viscosity of Examples Example Viscosity Example 1 11.64 poise Example 2 32.24 poise Example 3 192 poise Example 4 6.64 poise Example 5 14.40 poise Example 6 15.40 poise Comparative Example 1 382 poise Comparative Example 2 19.5 poise

[0045] Target viscosities for wire coating applications typically run between 5 to 500 poise and more preferably between 5 to 100 poise. As shown in Table 2 the Examples 1, 2, 4, 5, 6, and Comparative Example 2 all have a viscosity in the preferred viscosity range. Example 3 is slightly higher than preferred viscosity, due to the 0.995:1 molar ratio of dianhydride to diamine of this sample. Comparative Example 1 with equimolar ratios of diamine to dianhydride has viscosities significantly higher than preferred and cannot be used by traditional existing wire coating equipment.

[0046] A copper adhesion test was designed to ensure reasonable adhesion to copper with the new formulations. The adhesion test was performed by applying a thin layer approximately 0.002 inches in thickness of resin to an untreated copper surface and then running the coating through a specific heat cycle in an oven. The level of adhesion was graded from 0 correlating to no adhesion to 10 correlating to the highest adhesion level possible. The results of the experiment are shown in Table 3.

TABLE-US-00003 TABLE 3 Wire Coating Quality and Appearance Comparative Example 6 Example 2 Example 5 (0.97:1, with (1:1, non- Example 4 Example 2 Example 3 (0.97:1, with Aromatic REACH Oven Conditions (0.96:1) (0.97:1) (0.98:1) Hexanol) Naphtha) solvent) 240 sec at 140° C., 1 1 1 3 4 — 20 sec at 350° C., 120 sec at 450° C. 240 sec at 150° C., 6 7 8 3 4 — 20 sec at 350° C., 120 sec at 450° C. 240 sec at 160° C., 8 10 9 3 7 — 20 sec at 350° C., 120 sec at 450° C. 240 sec at 170° C., 10 10 9 3 8 — 20 sec at 350° C., 120 sec at 450° C. 240 sec at 180° C., 9 9 8 3 6 — 20 sec at 350° C., 120 sec at 450° C. 240 sec at 190° C. 8 7 7 4 — — 20 sec at 350° C. 120 sec at 450° C. 240 sec at 200° C. 4 (Blisters) 3 (Blisters) 3 (Blisters) 8 — 9 20 sec at 350° C. 120 sec at 450° C. 240 sec at 210° C. 6 (Blisters) 6 (Blisters) 4 (Blisters) 4 — — 20 sec at 350° C. 120 sec at 450° C.

[0047] Values above 7 in Table 3 represent good adhesion to copper and values below 3 represent poor levels of adhesion. REACH-approved resins in Table 3 typically showed the best adhesion levels when the initial oven temperatures were between 160 and 200° C. Blisters in the REACH-approved resin was typical in initial temperatures 200° C. and above in testing. Example 5, which contained a reactive co-solvent, hexanol, did not blister as badly as other examples with a single solvent system at high oven temperatures. Example 6 with a non-reactive co-solvent, aromatic naphtha, showed best adhesion at lower temperatures than single solvent systems. Non-REACH-approved resins are typically used with initial temperatures above 200° C. in industry. The non-REACH-approved resin, Comparative Example 2, showed good adhesion when tested with initial temperatures at 200° C. The heat adjustments needed for REACH-approved resins tested in this experiment are within the acceptable ranges for standard wire coating processing equipment.