EP1274773A1

EP1274773A1 - Improvement of the dispersion of pigments in polypropylene

Info

Publication number: EP1274773A1
Application number: EP01925331A
Authority: EP
Inventors: Gerd Hohner; Rainer Bott; Reiner Hess
Original assignee: Clariant GmbH
Current assignee: Clariant Produkte Deutschland GmbH
Priority date: 2000-03-01
Filing date: 2001-02-15
Publication date: 2003-01-15
Also published as: US20030050381A1; JP2003525329A; HK1052520A1; CN1406264A; WO2001064776A1

Abstract

The invention relates to the use of polyolefin waxes, which are produced by means of metallocene catalysis, for improving the dispersion of pigments in polypropylene.

Description

Improve the dispersion of pigments in polypropylene

The present invention relates to a process for the improved production of a colorant, consisting of at least one colorant which is distributed very finely in a meltable base material (matrix) which is solid at room temperature, and to the use of polyolefin waxes which coexist with Metallocene catalysts have been produced to improve the dispersion of the colorant in the polypropylene matrix, in particular for the production of polypropylene fibers.

Pigment preparations that can be used for coloring polyolefins are known:

DE-B-1 239 093 describes a carrier material for producing a pigment preparation which consists of a mixture of an amorphous ethylene-propylene block copolymer which has a viscosity of 5000 to 300,000 cps at 150 ° C. and a low molecular weight, crystalline polypropylene consists.

DE-A-26 52 628 describes the use of a low molecular weight polypropylene wax with a viscosity of 500 to 5000 cP at 170 ° C. as a dispersing aid.

DE-C-42 36 337 describes the use of polyacrylate esters as dispersants for pigments in plastic matrices.

US Pat. No. 5,880,193 describes the use of an amorphous poly-σ-olefin (0-90%) which is used in a mixture with a polyolefin wax (0-90%) and a special polyacrylate (0-50%).

All of the substances or mixtures listed above have the disadvantage that wetting, in particular difficult to disperse organic pigments, such as the quinacridone group or phthalocyanines, is insufficient, and these are therefore only insufficiently finely distributed in the polypropylene matrix, which leads to strand breaks due to coarse pigment particles, especially in the subsequent production of polypropylene fibers.

The object was therefore to provide a dispersing aid for pigments in polypropylene which effects a sufficient dispersion of the polymer particles, so that there are fewer strand breaks during fiber production.

Surprisingly, it was found that polyolefin waxes produced by metallocene catalysis ensure very good dispersion of pigments in polypropylene.

The invention relates to the use of means

Metallocene catalysts produced polyolefin waxes as dispersants for pigments in polypropylene.

Another object of the invention is a process for the production of a masterbatch by mixing a polymer with a colorant, characterized by admixing at least one polyolefin wax obtained by metallocene catalysis.

The pigments are preferably organic pigments.

Suitable polyolefin waxes are homopolymers of ethylene or propylene or copolymers of both olefins or copolymers of ethylene or propylene with one or more further olefins. Linear or branched olefins having 4-18 C atoms are preferred as further olefins

4-6 carbon atoms. Examples include 1-butene, 1-hexene, 1-octene or 1-octadecene and styrene. The copolymers consist of 70-99.9, preferably 80-99% by weight of ethylene or propylene. Homopolymers of are preferred Ethylene or propylene and copolymers of ethylene and propylene.

Polyolefin waxes with a dropping point between 90 and 165 ° C., preferably between 100 and 160 ° C., a melt viscosity at 170 ° C. between 5 and 10,000 mPa-s, preferably between 10 and 5000 mPa-s and a density at 20 are particularly suitable ° C between 0.86 and 0.98 g / cm ³ , preferably between 0.87 and 0.96 g / cm ³ .

The waxes can be used both as such and in a polar modified form. Modifications known per se are, for example, oxidation with air or graft polymerization with polar monomers, for example maleic anhydride.

In preferred embodiments of the invention, the metallocene waxes used according to the invention are used in admixture with auxiliaries and additives which improve the dispersing action of the metallocene waxes. Such auxiliaries and additives include, for example

a) polyethylene glycol b) PE waxes, c) PTFE waxes, d) PP waxes, e) amide waxes, f) FT paraffins, g) montan waxes, h) natural waxes, i) macro and microcrystalline paraffins, j) polar polyolefin waxes, or k) sorbitan esters

I) polyamides, m) polyolefins, n) PTFE, o) wetting agents, p) silicates.

Additive a) is polyethylene glycol, molecular weight range preferably 10 to 50,000 daltons, in particular 20 to 35,000 daltons. The polyethylene glycol can be mixed in amounts of preferably up to 5% by weight of the composition containing metallocene wax.

In preferred embodiments, additive b) is polyethylene homo- and copolymer waxes which were not produced by means of metallocene catalysis and which have a number average molecular weight of 700 to 10,000 g / mol at a dropping point between 80 and 140 ° C.

In preferred embodiments, additive c) is polytetrafluoroethylene with a molecular weight between 30,000 and 2,000,000 g / mol, in particular between 100,000 and 1,000,000 g / mol.

In preferred embodiments, additive d) is polypropylene homo- and copolymer waxes, which were not produced by means of metallocene catalysis and which have a number average molecular weight of 700 to 10,000 g / mol at a dropping point between 80 and 160 ° C.

In preferred embodiments, additive e) is amide waxes which can be prepared by reacting ammonia or ethylenediamine with saturated and / or unsaturated fatty acids. The fatty acids are, for example, stearic acid, tallow fatty acid, palmitic acid or erucic acid.

In preferred embodiments, additive f) is FT paraffins with a number average molecular weight of 400 to 800 g / mol at a dropping point of 80 to 125 ° C.

Additive g) is preferably montan waxes including acid and ester waxes with a carbon chain length of the carboxylic acid from C ₂₂ to C ₃₆ . The ester waxes are preferably reaction products of the montanic acids with mono- or polyhydric alcohols having 2 to 6 carbon atoms, such as, for example, ethanediol, 1-butane, 3-diol or 1-propane, 2,3-triol.

In a preferred embodiment, additive h) is carnauba wax or candelilla wax.

Additive i) is paraffins and microcrystalline waxes which are obtained from petroleum refining. The dropping points of such paraffins are preferably between 45 and 65 ° C, those of such microcrystalline waxes preferably between 73 and 100 ° C.

In preferred embodiments, additive j) is polar polyolefin waxes, which can be prepared by oxidation of ethylene or propylene homopolymer and copolymer waxes or by grafting them with them

Maleic anhydride. Polyolefin waxes with a dropping point 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) between 10 and 10,000 mPas, in particular between, are particularly preferred for this purpose 50 and 5000 mPas and a density at 20 ° C between 0.85 and 0.96 g / cm ³ .

In preferred embodiments, additive k) is reaction products of sorbitol (sorbitol) with saturated and / or unsaturated fatty acids and / or montanic acids. The fatty acids are, for example, stearic acid, tallow fatty acid, palmitic acid or erucic acid.

Additive I) is preferably ground polyamides, for example polyamide-6, polyamide-6,6 or polyamide-12. The particle size of the polyamides is preferably in the range of 5-200 μm, in particular 10-100 μm. Additive m) is a polyolefin, for example polypropylene, polyethylene or copolymers of propylene and ethylene of high or low density with molecular weights of preferably 10,000 to 1,000,000 D, in particular 15,000 to 500,000 D as number average for the molecular weight, the particle size of which Grinding is in the range of preferably 5-200 μm, in particular 10-100 μm.

Additive n) is thermoplastic PTFE with a molecular weight of preferably 500,000-10,000,000 D, in particular 500,000-2,000,000 D as the number average, the particle size of which is preferably 5-200 μm, in particular 10-100 μm, by grinding lies.

Additive o) is an amphiphilic compound that generally lowers the surface tension of liquids. The wetting agents are, for example, alkyl ethoxylates, fatty alcohol ethoxolates, alkyl benzene sulfonates or betaines.

Additive p) is a silicate which is not used as a filler for the pigment in the formulation. Preference is given to using silicic acids or talc.

The mixing ratio of component a) to components b) to p) can be varied in the range from 1 to 99% by weight a) to 1 to 99% by weight b) to p). If a mixture of several of the components b) to p) is used, the quantity given applies to the sum of the quantities of these components.

In a preferred embodiment, the waxes are used in micronized form for the purpose according to the invention. The use of polyolefin wax and optionally admixed auxiliaries and additives as ultra-fine powder with a particle size distribution dgo <40 μm is particularly preferred.

The use according to the invention is particularly preferred Polyolefin waxes for the production of color concentrates for polyethylene (LD) films.

Metallocene catalysts for the preparation of the polyolefin waxes are chiral or nonchiral transition metal compounds of the formula M ¹ L _X. The

Transition metal compound M ¹ L _X contains at least one metal central atom M ¹ to which at least one π ligand, for example a cyclopentadienyl ligand, is bonded. In addition, substituents such as halogen, alkyl, alkoxy or aryl groups can be bound to the metal central atom M ¹ . M ¹ is preferably an element of III., IV., V. or VI. Main group of the periodic table of the elements, such as Ti, Zr or Hf. Cyclopentadienyl ligand is understood to mean unsubstituted cyclopentadienyl radicals and substituted cyclopentadienyl radicals such as methylcyclopentadienyl, indenyl, 2-methylindenyl, 2-methyl-4-phenylindenyl, tetrahydrolindenrofluoryl or octa-tetra-hydrofluoryl or octa-tetra-hydrofluoryl or octa. The π ligands can be bridged or unbridged, whereby single and multiple bridging - also via ring systems - are possible. The term metallocene also includes compounds with more than one metallocene fragment, so-called multinuclear metallocenes. These can have any substitution pattern and bridging variant. The individual metallocene fragments of such multinuclear metallocenes can be of the same type or different from one another. Examples of such multinuclear metallocenes are described, for example, in EP-A-632 063.

Examples of general structural formulas of metallocenes and their activation with a cocatalyst include given in EP-A-571 882.

The invention is illustrated by the following examples.

Examples

The melt viscosities of the waxes used below were determined using a rotary viscometer in accordance with DGF-M-Ill 8 (57), the dropping points in accordance with DGF-M-Ill 3 (75) (standards of the German Society for Fat science), the densities determined according to DIN 53479.

To define the quality of the dispersion of a pigment in the polyolefin matrix, the filter value is used below, which is defined as follows:

DF = (P max- P 0) mpigment

The filter value according to this definition thus reflects the extent of the pressure increase due to filtration of a certain dispersed amount of pigment, hence the degree of "blocking" of the filter by undispersed or poorly dispersed pigment, based on the amount of pigment used.

In the production of the pigment masterbatches according to the example, a Henschel mixer FM 10 is used, which typically provides a statistical distribution of the feed components for 4 to 10 minutes (at room temperature) at 600 to 1500 revolutions / min. The actual dispersion (typically one in an iPP matrix) takes place in a co-rotating twin-screw extruder with a partial process length of 30 to 48 D, which works with a temperature profile of 30 to 230 ° C (feed -> nozzle). The number of revolutions is between 100 and 550 revolutions / minute, and a throughput of 4 to 30 kg / h is used. The following table shows the examples according to the procedure according to the invention or corresponding comparative examples according to the prior art:

Claims

gPatentansprüche

1. Use of polyolefin waxes produced using metallocene catalysts as a dispersing aid for pigments in polypropylene.

2. Use according to claim 1, wherein the polyolefin wax is derived from olefins having 3 to 6 carbon atoms or from styrene.

3. Use according to claim 1 and / or 2, wherein the polyolefin wax has a dropping point of 90 to 130 ° C, a melt viscosity at 140 ° C from 10 to

10000 mPa-s and a density of 0.89 to 0.98 g / cm ³ .

4. Use according to one or more of claims 1 to 3, wherein the polyolefin waxes are polar modified.

5. Use according to one or more of claims 1 to 4, wherein the polyolefin waxes in admixture with one or more auxiliaries and additives selected from the group consisting of a) polyethylene glycol b) PE waxes, c) PTFE waxes, d) PP waxes, e) amide waxes, f) FT paraffins, g) montan waxes, h) natural waxes, i) macro and microcrystalline paraffins, j) polar polyolefin waxes, or k) sorbitan esters I) polyamides, finely ground m) polyolefins, finely ground n) PTFE, finely ground in a weight ratio of polyolefin wax: auxiliary and additive 1:99 to 99: 1.

6. Use according to one or more of claims 1 to 5, wherein polyolefin wax and optionally the admixed auxiliaries and additives are present as ultra-fine powder with a particle size distribution dgo <40 μm.

7. Use according to one or more of claims 1 to 6, wherein the polypropylene is polypropylene fibers.

8. A process for the preparation of a masterbatch by mixing a polymer with a colorant, characterized by admixing at least one polyolefin wax obtained by metallocene catalysis.