DE102020105848A1 - Thermoplastic extrusion and / or 2-component polymer additive as well as manufacturing process for this and additive use therefor - Google Patents

Abstract

The invention relates to thermoplastic extrusion and / or 2-component polymer additive comprising binder-free tetrapodal zinc oxide, at least 90 percent by weight of the additive consisting of tetrapodal zinc oxide, the additive being in briquette form and a density between 1.0 and 1.5 Grams per cubic centimeter. The invention further relates to a thermoplastic extrusion and / or 2-component polymer additive manufacturing process and an additive use.

Description

The invention relates to a thermoplastic extrusion and / or 2-component polymer additive comprising binder-free tetrapodal zinc oxide as well as a production method for this and an additive use therefor.

Thermoplastics are obtained through polymerization. During this process, monomers combine to form a macromolecule, the polymer. The polymerization is started by activating the monomer, for example by supplying heat or high-energy radiation, by increasing the pressure or by using catalysts.

Polymerization-induced phase separation due to different polarity between monomer and polymer systems is known. This effect is partly desirable for a controlled morphology. If this is not the case, antiseparation additives can be used. However, these often also take part in the reaction or influence the micro- and nanostructure of the polymers.

Subsequent addition of these antiseparation additives to fully reacted polymers such as thermoplastics such as polyethylene terephthalate or polylactic acid can also lead to an improvement in the mechanical properties of the polymers such as tensile strength or even tack.

From the prior art, tetrapodal zinc oxide is known as such as an additive for polymer improvement. Tetrapodal zinc oxide is usually added as an additive in the production of plastic and rubber and, thanks to its “crow's foot” shape, causes mechanical anchoring and more even force distribution in the composites.

Chinese universities and companies in particular have used tetrapodal zinc oxide in various composites in recent years.

In the pamphlet CN 104419198B A flame-retardant, antistatic, continuously long glass fiber-reinforced, high-temperature-resistant nylon composite material and a manufacturing process for it are described.

The pamphlet CN104592536A discloses a method of making a tetrapod-shaped zinc oxide whisker / natural latex composite latex film.

The pamphlet CN104725761A discloses a manufacturing method for a new ABS resin based material.

In the pamphlet CN104788780A a polyethylene tear film and a manufacturing method therefor are described.

The pamphlet CN105623248A discloses a polyamide composite and a manufacturing method therefor.

From the pamphlet CN107501700A a processing method for a motor vehicle soundproofing material is known.

The pamphlet CN109181085A discloses a reinforced plastic masterbatch for a low shrinkage thick walled polypropylene product and method of manufacture.

The pamphlet CN1927933A relates to a modified atactic polypropylene resin.

In all of the publications listed above, tetrapodal zinc oxide particles in the form of zinc oxide whiskers are used without further processing.

The pamphlet EP 0 325 797 A1 discloses, for example, zinc oxide whiskers, the crystal structure of which has a central body and four needle crystal projections extending radially from this central body.

The pamphlet EP 2 550 241 B1 however, describes cross-linked tetrapodal zinc oxide. Three-dimensional networks based on the interpenetration of crystalline tetrapod legs are formed.

The problems in the prior art are essentially that the classic plastic reinforcement is carried out purely mechanically in polymerization. A high degree of filling of complex geometries such as fibers is required. In addition, no additives can be added for the subsequent reaction of unused monomers.

So far, no inorganic emulsifiers are known for the chemical reaction during the polymerization of two or more liquids in food technology.

The present invention is based on the object of providing an additive with which the mechanical properties of thermoplastics can be improved by adding it to the extrusion process. Specifically, a higher mechanical strength of the end product and reproducible properties can be achieved through the reaction of unreacted components, such as lower unwanted stickiness of the freshly extruded plastic.

In addition, in the chemical reaction during the polymerization of two or more liquids, the additive used as an emulsifier should improve mixing, which in turn optimizes the reaction of two immiscible liquids of different polarity. In this way, the reactions should run much more reliably down to the micro level. The better mixing should also improve the material properties such as reduced stickiness, more consistent glass transition and higher tensile strength. The degree of additive filling should be kept as low as possible and the additive should not take part in the reaction.

By adding the additive, it should also be possible to mix water and oil mixtures. According to the current state of the art, necessary but harmful emulsifiers are added to foodstuffs and cosmetics. Lecithins are currently the best-known class of emulsifiers in food technology. They stabilize water-oil mixtures through the formation of micelles. In medical technology, polysorbate is used as an emulsifier for water-oil mixtures. However, long-term exposure to polysorbate can have harmful effects on living things. So far, no inorganic emulsifiers are known in food technology.

Another task of the additive is to distribute insoluble substances in a polar medium. This is important for the distribution of drugs such as ciclosporin in water.

This object is achieved with an additive according to the main claim, a production method for producing the additive and an additive use according to the independent claims.

The thermoplastic extrusion and / or 2-component polymer additive comprises binder-free tetrapodal zinc oxide, at least 90 percent by weight of the additive consisting of tetrapodal zinc oxide and the additive in briquetted form with a density between 1.0 and 1.5 grams per cubic centimeter is present. Tetrapodal zinc oxide is, by definition, made up of unbroken tetrapods.

Because the briquetted form can have predetermined breaking points for portioning, simple portioning of the additive is possible depending on the required amount and intended use.

If the individual tetrapodal zinc oxide particles have a diameter from the interval 100 nanometers to 100 micrometers, the zinc oxide structure has a morphology that allows the structure to be broken across the reactive plane. The tetrapodal zinc oxide particles should not be less than 100 nanometers in size, since otherwise enough shear forces can no longer be applied to break off zinc oxide structures from the tetrapodal zinc oxide particles. The zinc oxide particle size should be less than 100 micrometers so that it can be used in small and / or thin components such as foils. Since larger particles can more easily lead to crack nuclei in the polymer, smaller particles in the range of 100 nanometers should preferably be used. The aspect ratio of the tetrapodal zinc oxide particles should be greater than 3. At least individual particles, but preferably a network of particles, should be used in order to obtain, among other things, good processability and low dust generation.

1. a. Vermischen von in Pulverform und / oder in vernetzter Form vorliegendem tetrapodalem Zinkoxid mit einem Binderpolymer und Zinkmetall-Pulver, wobei die Gewichtsanteile von Binderpolymer und tetrapodalem Zinkoxid in einem vorbestimmten Verhältnis zwischen 1 : 2 und 1 : 7 eingerichtet werden und dem Gemisch aus tetrapodalem Zinkoxid und Binderpolymer bis zu 10 Gewichtsprozent Zinkmetall-Pulver beigemischt werden und für eine Änderung der Dichte der Anteil Binderpolymer zu tetrapodalem Zinkoxid in den zuvor genannten Verhältnissen variiert werden kann;
2. b. Einfügen / Einfüllen / Geben des homogenisierten Gemisches in eine Brikettier-Pressform;
3. c. Wärmebehandeln des Gemisches in der Pressform für wenigstens eine Stunde bei einer Temperatur wenigstens 10 °C oberhalb der Bindetemperatur des Schmelzpolymers;
4. d. Abkühlen bzw. Abkühlen lassen auf eine Temperatur wenigstens 20 °C unterhalb der Schmelztemperatur des Binderpolymers;
5. e. Entnehmen des Inhalts der Pressform als formbeständiger Grünling;
6. f. Sintern des Grünlings bei Temperaturen zwischen 900 °C und 1100 °C für 3 bis 5 Stunden unter Verbrennen des Binderpolymers;
7. g. Abkühlen bzw. Abkühlen lassen des Zinkoxid-Briketts.

The thermoplastic extrusion and / or 2-component polymer additive manufacturing process is carried out with the following steps:

1. a. Mixing of tetrapodal zinc oxide present in powder form and / or in crosslinked form with a binder polymer and zinc metal powder, the weight proportions of binder polymer and tetrapodal zinc oxide being set up in a predetermined ratio between 1: 2 and 1: 7 and the mixture of tetrapodal zinc oxide and Binder polymer up to 10 percent by weight of zinc metal powder can be admixed and the proportion of binder polymer to tetrapodal zinc oxide can be varied in the aforementioned proportions to change the density;
2. b. Inserting / filling / giving the homogenized mixture in a briquetting press mold;
3. c. Heat treating the mixture in the mold for at least one hour at a temperature at least 10 ° C. above the bonding temperature of the melt polymer;
4. d. Cooling or allowing to cool to a temperature at least 20 ° C. below the melting temperature of the binder polymer;
5. e. Removing the contents of the mold as a shape-retaining green compact;
6. f. sintering the green compact at temperatures between 900 ° C. and 1100 ° C. for 3 to 5 hours while burning the binder polymer;
7. G. Cooling down or allowing the zinc oxide briquette to cool down.

Both polyvinyl butyrals, polycaprolactams, polyethylene glycols or waxes can be used as binder polymer in the process. The binder polymer can preferably be selected from the polymers mentioned.

The binder polymer can preferably have a melting point below 100.degree. If plastic molds are used to press the zinc oxide briquettes, this is necessary. When using molds made of metal, other polymers with higher melting points can also be used.

The grain size of the zinc metal powder should not be larger than the diameter of the individual tetrapodal zinc oxide particles. Standard spherical microparticles and nanoparticles can be used. The reason for adding zinc metal powder is to increase the strength of the zinc oxide briquette through the formation of crystal penetrations.

Since the tetrapodal zinc oxide can be mixed with the binder polymer with a mechanical stirrer at 100 revolutions per minute, the process is carried out as gently as possible, since the tetrapodal zinc oxide is not broken during the mixing process.

• - Mechanische Verstärkung im Vergleich zum ungefüllten Kunststoff;
• - Homogenere Eigenschaften des Kunststoffkomposits in Bezug auf beispielsweise Zugfestigkeit, Streckgrenze, Glasübergangstemperatur;
• - Reduktion der Klebrigkeit und Gleitreibung im Vergleich zum ungefüllten Kunststoff;
• - Spannungsrelaxation von mechanischen Verarbeitungsspannungen im Vergleich zum ungefüllten Kunststoff.

As an additive use of the zinc oxide briquette according to the invention, for example, the portioned addition of the additive to a masterbatch or a prepolymer component before a polymer extrusion and the grinding of the additive by an extruder can be seen. The additive according to the invention can also be used in the production of 2-component polymers. It is added in portions to a component as an emulsifier and homogenized with the help of a mechanical mixing unit. In both cases, the use of the additive improves the product. The zinc oxide briquette is activated by grinding, i.e. by breaking the tetrapods in the polymer. When the tetrapods break, highly reactive, polar planes are released in the c-axis of the wurtzite structure, which react with the polymer components. It is important that the additive according to the invention is broken down in the polymer in order to bring reactive planes into connection with polymer components. If the additive and thus also the tetrapods are broken outside the polymer, the reactive surfaces react with the air atmosphere and the additive can no longer work. The highly reactive levels are significantly more energetic than the intact side surfaces grown in the synthesis process for microcrystals. A more homogeneous reaction of the plastics is made possible. The resulting plastic composite is characterized by at least one of the following properties:

• - Mechanical reinforcement compared to unfilled plastic;
• - More homogeneous properties of the plastic composite with regard to, for example, tensile strength, yield point, glass transition temperature;
• - Reduction of stickiness and sliding friction compared to unfilled plastic;
• - Stress relaxation of mechanical processing stresses compared to unfilled plastic.

Since the zinc oxide briquette can be used in a mass ratio between 0.5% and 0.01% of additive to polymer, only low degrees of filling, i.e. degrees of filling less than 1 percent by weight, are necessary to achieve good results. Even with a filling level of 1 - 1000, a clear change in the mechanical properties can be seen. The degrees of filling customary in, for example, fiber-reinforced plastics are significantly higher.

Because composites can be produced with at least one polar component before, during or after the polymerization by polycondensation or polyaddition, it is possible to obtain the properties described above. In particular, the additive should preferably be introduced into the hydroxyl group or a component equipped with this type of group and ground there, since the positive effect of the additive can then be fully exploited.

If the homogenization of the components in the production of 2-component polymers either with a standard ultrasonic rod with, for example, 100 watts effective power at 50 percent amplitude and a duration of 20 seconds or with a dissolver disc for dispersing micro and nanoparticles with at least 6000 Revolutions per minute takes place for at least 5 minutes, good, reproducible values with regard to the breaking of the tetrapods are achieved. This leads to the plastic composites being required to have a low degree of filling.

The dosage form of the tetrapodal zinc oxide in the form of a zinc oxide briquette has various advantages. The zinc oxide briquette can be transported without the tetrapodal zinc oxide breaking and dusting of the tetrapodal zinc oxide during transport can also be avoided. The additive in the form of a zinc oxide briquette is easy to use and can be added reliably. Breaking points for separation and portioning further simplify handling.

The additive can be used as an additive to thermoplastic plastics and an improvement of up to 30 percent in the mechanical properties is achieved even if the amount is added below 1 percent by weight. Since the principle of action is based on the small grinding or breaking of the microstructures, the additive can be introduced in any conventional extrusion process in order to develop its effect and to strengthen the end product. In this way, material can be saved in many applications such as film production. The films can be made thinner because less material reinforced by the extrusion additive has the same strength as thicker material without additive. Due to the small quantities and the classification of zinc oxide as a biomaterial, its use is not limited by the particular application of the plastic.

Due to the improvement in the mechanical properties and the more homogeneous reaction, it should be possible that some layer systems, such as films for the food industry, can be avoided. These layer systems are used for preservation by means of an oxygen barrier on meat products, for example, and are not recyclable due to the layering of different polymers.

In addition to using the additive in thermoplastics, it can also be used in thermosets and elastomers. Here the additive causes a more homogeneous reaction.

Apart from this additive, no fillers are known which have a homogenizing effect with such a small addition.

• Herstellungsbeispiel Additiv:
  • Für ein Zinkoxid-Brikett mit einer Dichte von 1,3 Gramm pro Kubikzentimeter wird eine Pressform eines Volumens von 10 Kubikzentimeter verwendet. Es wird eine Mischung von 2 Gramm Polyvinylbutyral als Mikropulver (Partikelgröße >10 Mikrometer) und 13 Gramm unzerkleinertes tetrapodales Zinkoxid mit einer Größe zwischen 100 Nanometer und 100 Mikrometer verwendet. Die Pulver werden vorsichtig händisch gemischt, bis eine homogene Mischung entsteht. Die gesamten 15 Gramm des entstandenen Pulvers werden in die Pressform gegeben und das Volumen auf 10 Kubikzentimeter gepresst. Die Pressform wird mitsamt dem Inhalt bei 80 °C für eine Stunde gelagert, so dass das Polyvinylbutyral schmilzt und das verbleibende Pulver verklebt. Dadurch kann die gepresste Masse entformt werden und anschließend in einem Hochtemperaturofen bei 900 - 1100 °C für 3-5 Stunden gebacken werden. Nach dem Abkühlen kann das Zinkoxid-Brikett vakuumverpackt werden.
• Anwendungsbeispiel 1 - Additiv in Thermoplast:
  • Bei der Verarbeitung von polaren, thermoplastischen Kunststoffen (Polyamid, Polyethylenterephtalat, Polymilchsäure, etc.) kann je nach Fassungsvolumen des Extruders, der für die Kunststoffverarbeitung genutzt wird, ein Massenanteil zwischen 0,5 % und 0,01 % Zinkoxid-Brikett zugegeben werden. Das Brikett mit dem entsprechenden Gewicht wird in die Zugabevorrichtung des Kunststoffes gegeben. Durch normalen Betrieb des Schneckenextruders wird das Brikett in die funktionalen Einzelbestandteile zerrieben. Dazu ist es erforderlich, den Extruder für eine gewisse Zeit Mischen zu lassen. Die genaue Zeit für eine homogene Vermischung hängt vom jeweiligen Polymer und der Verarbeitungstemperatur ab und entspricht der Zeit, die benötigt wird, um andere Stoffe (Farbstoffe und Füllstoffe) beizumischen. Anschließend können aus dem additiverten Polymer wiederum Pellets oder Granulat hergestellt werden, die anschließend weiterverarbeitet werden können. Die additivierten Kunststoffe weisen bei korrekter Verarbeitung eine oder mehrere der folgenden Eigenschaften auf: höhere Zugfestigkeit, verringerte Klebrigkeit, gleichmäßigere Glastemperatur beim Vergleich mehrerer Batches.
• Anwendungsbeispiel 2 - Additiv in 2-Komponenten-Polymer:
  • Bei der Verarbeitung von 2-Komponenten-Polymeren mit mindestens einer polaren Komponente (Epoxidharze, Polyurethane, etc.) wird das Zinkoxid-Brikett in die polare Komponente zu dosiert. Die Zugabe erfolgt zwischen 0,5 % und 0,01 % Zinkoxid-Brikett gewichtsanteilig gerechnet auf das Gewicht des fertigen Polymers. Mithilfe einer mechanischen Mischeinheit (Dispergator, Ultraschallstab) wird diese Mischung homogenisiert, bis alle Arme / Stacheln kaputtgebrochen sind. Bei Verwendung eines handelsüblichen Ultraschallstabs entspricht das etwa 20 Sekunden bei 50 % Amplitude. Nach der Homogenisierung werden die beiden Komponenten des 2-Komponenten-Polymers in einem Zeitraum von bis zu 2 Wochen nach der Einmischung des Zinkoxid-Briketts im korrekten Mischungsverhältnis gemischt und laut Herstellervorgaben zur Polymerisation gebracht. Das fertige Polymer weist im Gegensatz zum nicht-additivierten Kunststoff eine oder mehrere der folgenden Eigenschaften auf: höhere Zugfestigkeit, verringerte Klebrigkeit, homogenere Glasübergangstemperatur.

A production example and two application examples of the invention are given below, these being intended to explain the invention and not to be regarded as restrictive:

• Production example additive:
  • For a zinc oxide briquette with a density of 1.3 grams per cubic centimeter, a mold with a volume of 10 cubic centimeters is used. A mixture of 2 grams of polyvinyl butyral as micropowder (particle size> 10 micrometers) and 13 grams of uncomminuted tetrapodal zinc oxide with a size between 100 nanometers and 100 micrometers is used. The powders are carefully mixed by hand until a homogeneous mixture is obtained. The entire 15 grams of the resulting powder are placed in the mold and the volume is pressed to 10 cubic centimeters. The mold and its contents are stored at 80 ° C. for one hour so that the polyvinyl butyral melts and the remaining powder sticks together. This allows the pressed mass to be removed from the mold and then baked in a high-temperature oven at 900 - 1100 ° C for 3-5 hours. After cooling, the zinc oxide briquette can be vacuum packed.
• Application example 1 - additive in thermoplastic:
  • When processing polar, thermoplastic plastics (polyamide, polyethylene terephthalate, polylactic acid, etc.), a mass fraction of between 0.5% and 0.01% zinc oxide briquette can be added, depending on the capacity of the extruder that is used for plastics processing. The briquette with the appropriate weight is placed in the plastic dispenser. Normal operation of the screw extruder grinds the briquette into its individual functional components. To do this, it is necessary to let the extruder mix for a certain period of time. The exact time for a homogeneous mixing depends on the respective polymer and the processing temperature and corresponds to the time required to mix in other substances (dyes and fillers). Subsequently, pellets or granules can be produced from the polymer with the addition of additives, which can then be further processed. When processed correctly, the plastics with additives have one or more of the following properties: higher tensile strength, reduced stickiness, more uniform glass temperature when comparing several batches.
• Application example 2 - additive in 2-component polymer:
  • When processing 2-component polymers with at least one polar component (epoxy resins, polyurethanes, etc.), the zinc oxide briquette is added to the polar component. The addition takes place between 0.5% and 0.01% zinc oxide briquette based on the weight of the finished polymer. With the help of a mechanical mixing unit (disperser, ultrasonic rod), this mixture is homogenized until all arms / spines have broken. When using a commercially available ultrasonic rod, this corresponds to about 20 seconds at 50% amplitude. After homogenization, the two components of the 2-component polymer are mixed in the correct mixing ratio within a period of up to 2 weeks after the zinc oxide briquette has been mixed in, and polymerized according to the manufacturer's instructions. In contrast to the non- plastic with additives has one or more of the following properties: higher tensile strength, reduced stickiness, more homogeneous glass transition temperature.

QUOTES INCLUDED IN THE DESCRIPTION

This list of the documents listed by the applicant was generated automatically and is included solely for the better information of the reader. The list is not part of the German patent or utility model application. The DPMA assumes no liability for any errors or omissions.

Patent literature cited

• CN 104419198 B [0007]
• CN 104592536 A [0008]
• CN 104725761 A [0009]
• CN 104788780 A [0010]
• CN 105623248 A [0011]
• CN 107501700 A [0012]
• CN 109181085 A [0013]
• CN 1927933 A [0014]
• EP 0325797 A1 [0016]
• EP 2550241 B1 [0017]

Claims (11)

Thermoplastic extrusion and / or 2-component polymer additive comprising binder-free tetrapodal zinc oxide, wherein - at least 90 percent by weight of the additive consists of tetrapodal zinc oxide; - the additive is in briquette form and - Has a density between 1.0 and 1.5 grams per cubic centimeter. Additive after Claim 1 , characterized in that the individual tetrapodal zinc oxide particles have a diameter from the interval 100 nanometers to 100 micrometers. Thermoplastic extrusion and / or 2-component polymer additive manufacturing process with the following steps: a. Mixing of tetrapodal zinc oxide present in powder form and / or in crosslinked form with a binder polymer and zinc metal powder, wherein the weight proportions of binder polymer and tetrapodal zinc oxide are established in a predetermined ratio between 1: 2 and 1: 7 and - Up to 10 percent by weight of zinc metal powder are added to the mixture of tetrapodal zinc oxide and binder polymer; b. Inserting / filling / giving the homogenized mixture in a briquetting press mold; c. Heat treating the mixture in the mold for at least one hour at a temperature at least 10 ° C. above the bonding temperature of the melt polymer; d. Cooling to a temperature at least 20 ° C. below the melting temperature of the binder polymer; e. Removing the contents of the mold as a shape-retaining green compact; f. sintering the green compact at temperatures between 900 ° C. and 1100 ° C. for 3 to 5 hours with burning of the binder polymer; G. Cooling the zinc oxide briquette. Manufacturing process according to Claim 3 , characterized in that the binder polymer is selected from or comprises at least one polymer from the following substances: - polyvinyl butyral, - polycaprolactam, - polyethylene glycol, - wax. Manufacturing process according to one of the Claims 3 or 4th , characterized in that the binder polymer has a melting point below 100 ° C. Manufacturing method according to one of the preceding claims, characterized in that the grain size of the zinc metal powder is not larger than the diameter of the individual tetrapodal zinc oxide particles. Manufacturing method according to one of the preceding claims, characterized in that the mixing is carried out with a mechanical stirrer at 100 revolutions per minute. Additive use according to one of the Claims 1 or 2 , characterized in that the portioned additive - is added to a masterbatch or a prepolymer component before polymer extrusion and ground by an extruder or - is added to a component as an emulsifier when producing 2-component polymers and is homogenized using a mechanical mixing unit. Additive usage according to Claim 8 , characterized in that the additive is used in a proportion between 0.5% and 0.01% by weight of additive to polymer. Additive use according to one of the Claims 1 or 2 for the production of composites, characterized in that composites are formed with at least one polar component before, during or after the polymerization by polycondensation or polyaddition. Additive usage according to Claim 8 , characterized in that the homogenization of the components in the production of 2-component polymers - with a standard ultrasonic rod at 50% amplitude and a duration of at least 20 seconds or - with a dissolver disc for dispersing micro and nanoparticles at at least 6000 Revolutions per minute takes place for at least 5 minutes.