Use of wax mixtures for coatings

Abstract
The invention provides for the use of mixtures of waxes which comprise
Description


[0001] The present invention relates to the use of metallocene waxes, their oxidates and blends thereof with further waxes, and also the corresponding micronisates, for coating materials.


[0002] In the preparation of coating materials, waxes are generally added in a concentration of 0.01-10%. The waxes in question are PE waxes, PTFE waxes, PP waxes, amide waxes, FT paraffins, montan waxes, natural waxes, macrocrystalline and microcrystalline paraffins, polyethylene copolymers, sorbitan esters and metallocene waxes, and also blends thereof, as disclosed in EP-A-0 890 619. The blends may be present in different combinations, both as powder mixtures and as melt mixtures.


[0003] These waxes are added in the form of flakes, granules, powders, dispersions, emulsions or micronisates, the preferred use form being regardable as a finely micronized powder with particle sizes up to 4 μm in DV50 value. (DV50 value: 50% of the wax particles are smaller than or equal to 4 μm). These waxes are used in order to achieve the following effects in the coating materials:


[0004] better scratch resistance


[0005] better abrasion resistance


[0006] better dispersing of pigments


[0007] better pigment stability


[0008] improvement in sedimentation tendency


[0009] improvement in redispersion of pigments


[0010] active orienting substance for effect pigments


[0011] effective flatting


[0012] satisfactory feel


[0013] improvement in lubricity


[0014] improvement in metal marking


[0015] achieving effective incorporation of effect pigments


[0016] influencing of rheological properties


[0017] better blocking resistance


[0018] better sandability


[0019] degassing additive in powder coatings


[0020] additive for increasing throughput in powder coatings.


[0021] These wax additives can be used in all coating systems (e.g., low solids, medium solids, high solids, solvent-based coating materials, aqueous or water-dilutable coating materials, powder coating materials, physically drying coating systems, chemically curing coating materials, and radiation-curing coating materials, such as UV coating materials, for example).


[0022] Since pure polyethylene waxes and metallocene waxes cannot be used in all coating systems, especially not in aqueous systems, use is also made of wax oxidates.


[0023] Since the individual types of wax display different effects in the coating materials, it is preferred to use wax mixtures of PE waxes, PTFE waxes, PP waxes, amide waxes, FT paraffins, montan waxes, natural waxes, macrocrystalline and microcrystalline paraffins, polyethylene copolymers, sorbitan esters and metallocene waxes in order to combine the abovementioned effects with one another and to obtain corresponding improvements in coating materials.


[0024] It was an object of the invention to find wax mixtures, for use in coating materials, which exhibit a particularly large number of the effects set out above. Surprisingly, the mixtures with metallocene waxes showed the most marked improvements. With these mixtures, a particular improvement is obtained in the grindability for the production of wax micronisates; in other words, the yields are increased.


[0025] A further advantage of using waxes produced by the metallocene process is their ready grindability, for which reason fewer auxiliaries are consumed in this case than in the case of wax mixtures comprising waxes produced, for example, with the Ziegler-Natta process.


[0026] The invention provides for the use of mixtures of waxes which comprise


[0027] a) a homopolymer or copolymer of C2-C18 α-olefins, prepared by means of metallocene catalysis, and also degradation waxes produced from relatively high-chain-length polyolefins produced by means of metallocene catalysis, and, as auxiliaries, one or more other waxes selected from the group consisting of


[0028] b) PE waxes,


[0029] c) PTFE waxes,


[0030] d) PP waxes,


[0031] e) amide waxes,


[0032] f) FT paraffins,


[0033] g) montan waxes,


[0034] h) natural waxes,


[0035] i) macrocrystalline and microcrystalline paraffins,


[0036] j) polar polyolefin waxes, or


[0037] k) sorbitan esters,


[0038] l) polyamides,


[0039] m) polyolefins,


[0040] n) PTFE,


[0041] o) wetting agents,


[0042] p) silicates


[0043] for improving the properties of coating materials.


[0044] The invention further provides coating materials comprising the wax mixtures described.


[0045] The homopolymer or copolymer of C2-C18 α-olefins prepared by means of metallocene catalysis (a) preferably have the following properties:
1Dropping point (Dp):80-165°C.Acid number (AN):0-50mg KOH/gDensity:0.87-1.03g/cm3Melt viscosity at 170° C.:10-100 000mPas.


[0046] Suitable polyolefin waxes include homopolymers of ethylene or propylene or copolymers of ethylene or propylene with one another or with one or more 1-olefins. 1-Olefins used include linear or branched olefins having 4-18 carbon atoms, preferably 4-6 carbon atoms. These olefins may have an aromatic substitution which is in conjugation with the olefinic double bond. Examples of such compounds are 1-butene, 1-hexene, 1-octene or 1-octadecene, and also styrene. Preference is given to copolymers of ethylene with propene or 1-butene. Ethylene copolymers of this kind have ethylene contents of 70-99.9% by weight, preferably 80-99% by weight.


[0047] Especially suitable polyolefin waxes are those having a dropping point of between 90 and 160° C., preferably between 100 and 155° C., a melt viscosity at 140° C. of between 10 and 10 000 mPas, preferably between 50 and 5 000 mPas, and a density at 20° C. of between 0.89 and 0.96 g/cm3, preferably between 0.91 and 0.94 g/cm3.


[0048] Also suitable are metallocene waxes modified by oxidation, such as may be obtained, for example, by treating the wax melt with air in accordance with EP-A-0 896 591. The disclosure content of this document in respect of the oxidative treatment of wax melts is hereby incorporated into the present specification by reference.


[0049] Metallocene catalysts for preparing the polyolefin waxes are chiral or nonchiral transition metal compounds of the formula M1Lx. The transition metal compound M1Lx contains at least one central metal atom M1 to which at least one π ligand, e.g., a cyclopentadienyl ligand, is attached. Furthermore, substituents, such as halogen, alkyl, alkoxy or aryl groups, for example, may be attached to the central metal atom M1. M1 is preferably an element from main group III, IV, V or VI of the periodic table of the elements, such as Ti, Zr or Hf. Cyclopentadienyl ligand comprehends unsubstituted cyclopentadienyl radicals and substituted cyclopentadienyl radicals such as methylcyclopentadienyl, indenyl, 2-methylindenyl, 2-methyl-4-phenylindenyl, tetrahydroindenyl or octahydrofluorenyl radicals. The π ligands may be bridged or non-bridged, with both single and multiple bridges—including bridges via ring systems—being possible. The metallocene designation also embraces compounds having more than one metallocene fragment, known as polynuclear metallocenes. These may have arbitrary substitution patterns and bridging variants. The individual metallocene fragments of such polynuclear metallocenes may be both identical to one another and different from one another. Examples of such polynuclear metallocenes are described, for example, in EP-A-0 632 063. Examples of general structural formulae of metallocenes and also of their activation with a cocatalyst are given, inter alia, in EP-A-0 571 882. The disclosure contents of these subjects in the two documents is hereby incorporated by reference.


[0050] Additive b) comprises, in preferred embodiments, polyethylene homopolymer and copolymer waxes which have not been prepared by means of metallocene catalysis and which have a number-average molecular weight of from 700 to 10 000 g/mol with a dropping point of between 80 and 140° C.


[0051] Additive c) comprises in preferred embodiments polytetrafluoroethylene having a molecular weight of between 30 000 and 2 000 000 g/mol, in particular between 100 000 and 1 000 000 g/mol.


[0052] Additive d) comprises, in preferred embodiments, polypropylene homopolymer and copolymer waxes which have not been prepared by means of metallocene catalysis and which have a number-average molecular weight of from 700 to 10 000 g/mol with a dropping point of between 80 and 160° C.


[0053] Additive e) comprises, in preferred embodiments, amide waxes preparable by reacting ammonia or ethylenediamine with saturated and/or unsaturated fatty acids. The fatty acids comprise, for example, stearic acid, tallow fatty acid, palmitic acid or erucic acid.


[0054] Additive f) comprises, in preferred embodiments, FT paraffins having a number-average molecular weight of from 400 to 800 g/mol with a dropping point from 80 to 125° C.


[0055] Additive g) preferably comprises montan waxes, including acid waxes and ester waxes having a carboxylic acid carbon chain length of from C22 to C36.


[0056] The ester waxes preferably comprise reaction products of the montanic acids with monohydric or polyhydric alcohols having 2 to 6 carbon atoms, such as ethanediol, butane-1,3-diol or propane-1,2,3-triol, for example.


[0057] Additive h) in one preferred embodiment comprises carnauba wax or candelilla wax.


[0058] Additive i) comprises paraffins and microcrystalline waxes which are obtained in the course of petroleum refining. The dropping points of such paraffins are preferably between 45 and 65° C., those of microcrystalline waxes of this kind preferably between 73 and 100° C.


[0059] Additive j) comprises, in preferred embodiments, polar polyolefin waxes preparable by oxidizing ethylene or propylene homopolymer and copolymer waxes or grafting them with maleic anhydride. Particularly preferred starting material for this purpose comprises polyolefin waxes having a dropping point of between 90 and 165° C., in particular between 100 and 160° C., a melt viscosity at 140° C. (polyethylene waxes) or at 170° C. (polypropylene waxes) of between 10 and 10000 mPas, in particular between 50 and 5000 mPas, and a density at 20° C. of between 0.85 and 0.96 g/cm3.


[0060] Additive k) comprises, in preferred embodiments, reaction products of sorbitol with saturated and/or unsaturated fatty acids and/or montanic acids. The fatty acids comprise, for example, stearic acid, tallow fatty acid, palmitic acid or erucic acid.


[0061] Additive l) preferably comprises ground polyamides, examples being polyamide-6, polyamide-6,6 or polyamide-12. The particle size of the polyamides is preferably in a range of 5-200 μm, in particular 10-100 μm.


[0062] Additive m) comprises polyolefins, i.e., for example, polypropylene, polyethylene or copolymers of propylene and ethylene of high or low density with molar weights of preferably from 10 000 to 1 000 000 D, in particular from 15 000 to 500 000 D, as numerical averages of the molecular weight, whose particle size as a result of grinding is in the range of preferably 5-200 μm, in particular 10-100 μm.


[0063] Additive n) comprises thermoplastic PTFE having a molar weight of preferably 500 000-10 000 000 D, in particular 500 000-2 000 000 D, as numerical average, whose particle size as a result of grinding is in the range of preferably 5-200 μm, in particular 10-100 μm.


[0064] Additive o) comprises amphiphilic compounds which generally lower the surface tension of liquids. The wetting agents comprise, for example, alkyl ethoxylates, fatty alcohol ethoxylates, alkylbenzenesulfonates or betaines.


[0065] Additive p) comprises silicates which are not used as filler or pigment in the formulas. It is preferred to use silicas or talc.


[0066] The proportion of ingredient a) to ingredients b) to p) may be varied in the range from 1 to 99% by weight a) to 1 to 99% by weight b) to p). Where a mixture of two or more of ingredients b) to p) is used, the indicated amount applies to the sum of the amounts of these ingredients.


[0067] In one preferred embodiment, the waxes are used in micronized form for the purpose according to the invention. Particular preference is given to the use of polyolefin wax and optionally admixed auxiliaries and additives as an ultrafine powder with a particle size distribution d90<40 μm.


[0068] Parameters improved include the flatting of the coating materials, the dispersibility and stability (sedimentation tendency or bodying tendency) in coating materials and dispersions, an improvement in the slip, hardness and abrasion resistance, an increase in the throughput and improvement in pigment dispersion in powder coating materials, and better antiblocking and handling sensation (soft feel). The wax mixtures generally comprise powder mixtures and/or melt mixtures.






EXAMPLES

[0069]

2





TABLE 1










Characterization of the ingredients of the wax mixtures used












Dropping



Wax type
Acid number
point
Viscosity















Metallocene PE
0
mg KOH/g
124° C.
250
mPas (140° C.)


wax


Metallocene PP
0
mg KOH/g
135° C.
40
mPas (170° C.)


wax


Oxidized
20
mg KOH/g
114° C.
200
mPas (120° C.)


metallocene


PE wax


PE wax
0
mg KOH/g
125° C.
300
mPas (140° C.)


PP wax
0
mg KOH/g
 160° C.*
1500
mPas (170° C.)


Oxidized PE wax
20
mg KOH/g
114° C.
200
mPas (120° C.)


Amide wax
6
mg KOH/g
140° C.
10
mPas (150° C.)


Montan wax 1
17
mg KOH/g
 82° C.
30
mPas (100° C.)


Montan wax 2
14
mg KOH/g
100° C.
300
mPas (120° C.)


Carnauba wax
9
mg KOH/g
 82° C.
30
mPas (90° C.)


FT paraffin
0
mg KOH/g
110° C.
20
mPas (120° C.)






*Softening point








[0070]

3





TABLE 2










Wax mixtures (all mixtures micronized to DV50 = 8 μm)











Code
Ingredient 1
Ingredient 2
Ingredient 3
Proportion





M1
Oxidized
Carnauba wax

1:1



metallocene PE wax


M2
Metallocene PE wax
Oxidized

7:3




metallocene PE




wax


M3
Metallocene PE wax
Amide wax

1:1


M4
Metallocene PE wax
PTFE wax

9:1


M5
Metallocene PE wax
Oxidized
PTFE wax
12:7:1 




metallocene PE




wax


M6
Metallocene PP wax
Amide wax

1:1


M7
Metallocene PP wax
Amide wax

5:1


M8
Metallocene PP wax
Metallocene PE

1:1




wax


M9
Metallocene PP wax
Oxidized

1:1




metallocene PE




wax


 M10
Oxidized
Montan wax
Montan wax
2:1:1



metallocene PE wax
1
2


 M11
Metallocene PE wax
Oxidized
Sorbitan
1:1:1




metallocene PE
tristearate




wax


 M12
Metallocene PE wax
FT paraffin

5:1


V1
Oxidized PE wax
Carnauba wax

1:1


V2
PE wax
Oxidized PE wax

7:3


V3
PE wax
Amide wax

1:1


V4
PE wax
PTFE wax

9:1


V5
PE wax
Oxidized PE wax
PTFE wax
12:7:1 


V6
PP wax
Amide wax

1:1


V7
PP wax
Amide wax

5:1


V8
PP wax
PE wax

1:1


V9
PP wax
Oxidized PE wax

1:1


 V10
Oxidized PE wax
Montan wax
Montan wax
2:1:1




1
2


 V11
PE wax
Oxidized PE wax
Sorbitan
1:1:1





tristearate


 V12
PE wax
FT paraffin

5:1










[0071] Preparation of an Aqueous Wax Dispersion from a Micropowder:


[0072] 1% by weight of Tylose® is stirred into 60% by weight of water and allowed to swell briefly, after which 39% by weight of micronized oxidized wax is incorporated into the Tylose solution by dispersion.
4TABLE 3Dispersing/stability of wax mixturesWaxDispersing/stabilityExample 1M1good/very goodExample 2M2good/very goodExample 3M9good/very goodExample 4 M10very good/very goodExample 5V1good/very goodExample 6V2good/very goodExample 7V9moderate/moderateExample 8 V10good/very good


[0073] Incorporation of an Aqueous Wax Dispersion into an Aqueous Acrylic Varnish:


[0074] 4% by weight of the wax dispersion specified in example 2 is stirred into 96% by weight of aqueous acrylic varnish (based on Mowilith® LDM 7460) and then drawn down onto a glass plate using a frame coater (60 μm wet film thickness). After drying, the gloss is measured.
5TABLE 4Gloss of the wax mixturesDispersion fromBase waxGloss (60° angle)Acrylic varnishno wax120Example 9Example 1M122Example 10Example 2M225Example 11Example 3M925Example 12Example 4 M1020Example 13Example 5V130Example 14Example 6V230Example 15Example 7V928Example 16Example 8 V1025


[0075] Incorporation of Micronized Waxes into a Nitrocellulose Standard Varnish for Purposes of Matting and Slip:


[0076] 2% by weight of micronized wax are incorporated by dispersion into 98% by weight of NC varnish by means of a dissolver and then drawn down onto a glass plate using a frame coater (60 μm wet film thickness). After drying, the gloss is measured.
6TABLE 5Gloss and slip of the wax mixturesWaxGloss (60° angle)SlipNitrocellulose varnishNo wax1380.42Example 17M30.17Example 18M4450.12Example 19M50.09Example 20M6250.10Example 21M725Example 22M8300.25Example 23M9410.25Example 24 M10300.15Example 25V3270.22Example 26V4500.15Example 27V5450.15Example 28V6300.17Example 29V7300.30Example 30V8400.30Example 31V9500.28Example 32 V10350.22


[0077] Incorporation into a White Hybrid Powder Coating Material for the Purpose of Improving the Pencil Hardness and Abrasion Resistance:


[0078] The waxes are mixed with the individual raw materials in a high-speed mixer, and then the raw materials are extruded at 110° C. in a twin-screw laboratory extruder (PC19-25 from APV), ground to <125 μm and applied to aluminum or steel sheet. After baking (at 180° C. for 15 minutes) the coated sheets are stored in a controlled-climate chamber for 24 hours, after which the pencil hardness (according to Wolff-Wilborn) is measured and the Taber Abraser abrasion test carried out.
7TABLE 6Pencil hardness and abrasion testWax, in each casePencil hardness1% based on totalaccording toAbrasion testformulaWolff-Wilbornafter 250 turnsHybrid powderNo wax2B52 mgcoating materialExample 33M2HB48 mgExample 34M3F35 mgExample 35M4F25 mgExample 36M6F20 mgExample 37M7H15 mgExample 38 M10HB25 mgExample 39V2B50 mgExample 40V3HB41 mgExample 41V4HB42 mgExample 42V6B46 mgExample 43V7B38 mgExample 44 V10HB40 mg


[0079] Incorporation into a Blue Hybrid Powder Coating Material for the Purpose of Improving the Dispersion and Throughput:


[0080] The waxes are mixed with one another with the individual raw materials in a high-speed mixer, and then the raw materials are extruded at 110° C. in a twin-screw laboratory extruder (PC19-25 from APV), for which it is necessary to set the metering level to a power consumption of 70% on the extruder; during this procedure, the throughput is detected; the extrudate is then ground to <125 μm and applied to aluminum or steel sheet. After baking (at 180° C. for 15 minutes) the coated sheets are stored in a controlled-climate chamber for 24 hours, after which the depth of color is measured.
8TABLE 7Depth of colorWax, in each case1% based on total% improvementformulain throughputDepth of colorHybrid powderNo wax100%coating materialExample 45M118%110%Example 46M220%105%Example 47M315%107%Example 48M630%105%Example 49M825%107%Example 50 M1050%120%Example 51V113%107%Example 52V215%100%Example 53V310%102%Example 54V610%100%Example 55V815%105%Example 56 V1045%112%


[0081] Incorporation into an Alkyd Resin Varnish for the Purpose of Assessing the Blocking Properties and the Feel:


[0082] 2% by weight of micronized wax are incorporated into the alkyd resin varnish with the aid of a dissolver, after which the varnish is applied to glass (at least 2 plates in each case) with the aid of a frame coater (60 μm wet film thickness). After storage in a controlled-climate chamber for 24 hours, the feel is assessed (subjectively), after which the plates are stored in an oven at 50° C. for 24 hours. In this case the plates are placed with the coating on top of one another and are loaded with a 500 g weight. Thereafter, the blocking behavior is assessed.
9TABLE 8Assessment of the blocking behaviorAssessment schemeBlocking resistanceNoneNo blockingTraceVery slight blocking evidentLittleWhen the upper board is raised, the underneathboard comes with it but parts by itself after a fewsecondsSomeWhen the upper board is raised, the underneathboard comes with it, but has to be separated by handwithout perceptible application of forceMarkedWhen the upper board is raised, the underneathboard comes with it but has to be separated withsome application of force.SubstantialThe plates have to be separated with considerableapplication of force.


[0083]

10





TABLE 9










Feel characteristics of the wax mixtures













Blocking



Wax
Feel (subjective)
characteristics














Alkyl resin varnish
No wax
Plasticky, slightly tacky
Substantial


Example 57
M3
Good feel, no sticking
Trace


Example 58
M4
Good feel, very smooth
None


Example 59
M6
Good feel, smooth
Trace


Example 60
 M10
Soft, pleasant, somewhat
Little




smooth


Example 61
V3
Good feel, very slight
Little




sticking


Example 62
V4
Good feel, smooth
Little


Example 63
V6
Slightly tacky
Some


Example 64
 V10
Pleasant
Little










[0084] Incorporation into a 2K PU Varnish, Applied to Wooden Boards, and Assessment of sandability:


[0085] 2 or 4% by weight of micronized wax are incorporated by dispersion into one component of a 2K polyurethane varnish system, after which the 2nd component is added and the composition is applied by brush to a wooden board in a cross pass. The board is then left to dry in a controlled-climate chamber for 24 hours. The sanding test is then carried out, in which a sheet of abrasive paper (240 grit) is stretched over a wooden block, passed over the wooden board 20× without pressure, and then the abrasion is assessed. The lower the level of coating on the abrasive paper, the better the sandability.
11TABLE 10Sandability of additived varnishWaxSandability2K PU varnishNo waxVery poor, abrasive paper clogged after just 10strokesExample 65M1Moderate, abrasive paper almost cloggedExample 66M3Very good, no clogging observable after 20strokesExample 67M6Very good, no clogging observable after 20strokesExample 68M7Good, slight clogging of the abrasive paperExample 69 M10Good, slight clogging of the abrasive paperExample 70V1Poor, abrasive paper clogged after 20 strokesExample 71V3Good, slight clogging of the abrasive paperExample 72V6Good, slight clogging of the abrasive paperExample 73V7Poor, abrasive paper clogged after 20 strokesExample 74 V10Poor, abrasive paper clogged after 20 strokes


Claims
  • 1. The use of mixtures of waxes which comprise a) a homopolymer or copolymer of C2-C18 α-olefins, prepared by means of metallocene catalysis, and also degradation waxes produced from relatively high-chain-length polyolefins produced by means of metallocene catalysis, and, as auxiliaries, one or more other waxes selected from the group consisting of b) PE waxes, c) PTFE waxes, d) PP waxes, e) amide waxes, f) FT paraffins, g) montan waxes, h) natural waxes, i) macrocrystalline and microcrystalline paraffins, j) polar polyolefin waxes, or k) sorbitan esters, l) polyamides, m) polyolefins, n) PTFE, o) wetting agents, p) silicates for improving the properties of coating materials.
  • 2. The use as claimed in claim 1, wherein ingredient a) is an oxidate of a metallocene wax.
  • 3. The use as claimed in claim 1 and/or 2, wherein ingredient a) comprises a homopolymer or copolymer of ethylene or of propylene.
  • 4. The use as claimed in one or more of claims 1 to 3, wherein the wax specified as ingredient a) has a melt viscosity at 140° C. of from 10 to 10 000 mPas.
  • 5. The use as claimed in one or more of claims 1 to 4, wherein the wax specified as ingredient a) has a density of from 0.87 to 1.03 g/cm3.
  • 6. The use as claimed in one or more of claims 1 to 5, wherein the wax specified as ingredient b) is a polyethylene wax not prepared by means of metallocene catalysis, having a number-average molecular weight of from 700 to 10 000 g/mol.
  • 7. The use as claimed in one or more of claims 1 to 6, wherein the wax specified as ingredient d) is a polypropylene wax not prepared by means of metallocene catalysis, having a number-average molecular weight of from 700 to 10 000 g/mol.
  • 8. The use as claimed in one or more of claims 1 to 7, wherein the wax specified as ingredient j) is a polyethylene or polypropylene wax modified by oxidation or grafting with maleic anhydride.
  • 9. The use of micronized waxes as defined in one or more of claims 1 to 8.
  • 10. Coating materials comprising wax mixtures as claimed in one or more of claims 1 to 9.
Priority Claims (2)
Number Date Country Kind
100234410 May 2000 DE
100634222 Dec 2000 DE
PCT Information
Filing Document Filing Date Country Kind
PCT/EP01/04778 4/27/2001 WO