Patent Application
20110288193
The present invention relates to a novel process for the production of polybutadiene-containing mouldings.
Polybutadiene-containing mouldings are mainly used in the tyre industry as former strip for sidewalls or treads. A decisive factor here is that the surface of these is smooth and that the number of indentations at their edges has been minimized.
Polybutadienes with high cis content and with minimum polydispersity are known to provide excellent properties in tyre mixtures, e.g. low rolling resistance or low tyre abrasion. Polydispersity is generally determined by gel-permeation chromatography, being the quotient obtained by dividing weight-average molar mass Mw by number-average molar mass Mn, thus representing the breadth of distribution of the molar masses.
As described inter alia in S. L. Agrawal et al., Rubber World—Akron, 2005, Vol. 232/3, pages 17 to 19 and 56, broad polydispersity advantageously affects processing performance, whereas narrow polydispersity advantageously affects the service properties of the rubber. According to Jochen Schnetger, Lexikon der Kautschuktechnologie [Rubber technology encyclopaedia], Hüthig Verlag Heidelberg, 3rd Edition, 2003, page 319, a broad distribution of the molar masses leads to good processing performance of the rubbers and rubber mixtures, apparent inter alia in relatively low mixture viscosity, relatively low mixing time and relatively low extrusion temperatures. For this reason, a polybutadiene with broad molar mass distribution is often used, giving an improvement in processability but having a disadvantageous effect on the property profile of the tyre.
Accordingly, the processing of the abovementioned polybutadienes with narrow polydispersity in the mixture is difficult. If these mixtures are processed at the conventional high temperatures which are mostly above 90° C., extrusion speed has to be reduced drastically in order to obtain an acceptable extrudate quality, and this reduces the cost-effectiveness of the process.
It was therefore an object to provide a novel cost-effective process for the production of polybutadiene-containing mouldings which does not have the disadvantages of the prior art.
It has now been found that low extrusion temperatures have a favourable effect on the surface characteristic of the mixtures, and this is all the more surprising because it is generally only higher temperatures that improve properties, for example in the case of cobalt-catalysed polybutadiene.
The present invention therefore provides a process for the production of polybutadiene-containing mouldings, characterized in that at least one polybutadiene with cis content greater than 95%, preferably greater than 96%, and polydispersity smaller than 2.5 is mixed with at least one filler and with at least one processing aid and then extruded at temperatures of from 40 to 75° C. preferably from 40 to 55° C.
The polybutadienes used with cis content (1,4-cis content) greater than 95%, preferably greater than 96%, and with polydispersity smaller than 2.5, particularly preferably in the range from 1.7 to 2.2, are preferably those which have 1,2-vinyl content smaller than 1%, preferably smaller than 0.8%, and Mooney viscosity ML 1+4 at 100° C. of from 35 to 80 Mooney units, preferably in the range from 40 to 75 Mooney units. Those used are preferably neodymium-catalysed polybutadienes (catalysed by neodymium-containing systems). These involve commercially obtainable products. By way of example, these can be produced according to EP-A 11 184 and EP-A 7027, using neodymium-containing catalysts.
The term neodymium-containing catalysts includes Ziegler-Natta catalysts based on neodymium compounds, these being soluble in hydrocarbons. It is particularly preferable to use neodymium carboxylates, in particular neodymium neodecanoate, neodymium octanoate, neodymium naphthenate, neodymium 2,2-diethylhexanoate and/or neodymium 2,2-diethylheptanoate. When these catalysts are used in the polymerization of, for example, butadiene, they give, in very high yields and with high selectivity, a polybutadiene which particularly features a high proportion of 1,4-cis units.
In one embodiment of the process according to the invention, the filler used comprises carbon black and/or silica.
Fillers that can be used are any of the known fillers used in the rubber industry. These encompass both active and inert fillers.
Examples that may be mentioned are:
Fillers preferably used are fine-particle silicas, carbon blacks and/or zinc salts of acrylic or methacrylic acid.
The fillers mentioned can be used alone or in a mixture. In one particularly preferred embodiment, the filler used comprises a mixture composed of pale-coloured fillers, such as fine-particle silicas, and of carbon blacks, the mixing ratio of pale-coloured fillers to carbon blacks being from 0.05 to 20, preferably from 0.1 to 15.
The amounts used here of the fillers are preferably in the range from 10 to 500 parts by weight of filler, based on 100 parts by weight of rubber. It is particularly preferable to use from 20 to 200 parts by weight.
In addition to the polybutadienes, mentioned, other rubbers can also be used, examples being natural rubber, or else other synthetic rubbers. The amount of these is usually in the range from 0.5 to 85% by weight, preferably from 10 to 70% by weight, based on the entire amount of rubber in the rubber mixture. The amount of additionally added rubbers depends again on the respective intended use.
Synthetic rubbers known from the literature are listed here by way of example. They encompass inter alia
For the purposes of the invention, processing aids include by way of example substances which serve for the crosslinking of the rubber mixtures (crosslinking agents), or which improve the physical properties of the resultant vulcanizates for their specific intended purpose.
Crosslinking agents used in particular comprise sulphur or sulphur-donor compounds. Examples of suitable crosslinking chemicals are organic peroxides, e.g. dicumyl peroxide, tert-butyl cumyl peroxide, bis(tert-butylperoxyisopropyl)benzene, di-tert-butyl peroxide, dibenzoyl peroxide, bis(2,4-dichlorobenzoyl) peroxide, tert-butyl perbenzoate, and also organic azo compounds, such as azobisisobutyronitrile and azobiscyclohexanonitrile, and also di- and polymercapto compounds, such as dimercaptoethane, 1,6-dimercaptohexane, 1,3,5-trimercaptotriazine, and mercapto-terminated polysulphide rubbers, e.g. mercapto-terminated reaction products of bischloroethyl formal with sodium polysulphide. It is moreover possible as mentioned to use further processing aids, such as the known reaction accelerators, antioxidants, heat stabilizers, light stabilizers, antiozonants, processing aids, plasticizers, tackifiers, blowing agents, dyes, pigments, waxes, extenders, e.g. DAE (distillate aromatic extract) oil, TDAE (treated distillate aromatic extract) oil, MES (mild extraction solvates) oil, RAE (residual aromatic extract) oil, TRAE (treated residual aromatic extract) oil, naphthenic and heavy naphthenic oils, organic acids, retardants, metal oxides, and also activators.
Preferred processing aids used are reaction accelerators, antioxidants, antiozonants, extenders, e.g. the conventional naphthenic, aromatic or aliphatic extender oils, organic acids, e.g. stearic acid, retarders, metal oxides, such as zinc oxide, and also activators, e.g. silanes.
The amount of processing aid is preferably in the range from 0.1 to 20%, based on the rubber used, and depends on the desired property profile of the mixtures.
The mixtures can by way of example be produced via blending of the rubbers with filler and with the further mixing constituents in or on suitable mixing apparatuses, e.g. kneaders, rolls or extruders.
For use of the mixtures by way of example in the tyre industry, or in the production of technical rubber products or in the golf-ball industry, the mixtures are used to produce mouldings, mostly in the form of extrudates, profiles or former strips. The mouldings can by way of example be produced in suitable apparatuses such as extruders or calenders.
The temperature during the said processing depends on the rubbers used. When 100 phr of polybutadiene according to the invention are used, the preferred temperature is from 40 to 55° C. In the mixture with, for example, styrene-butadiene rubber, the temperature is preferably from 50 to 75° C., depending on the proportion of the styrene-butadiene rubber. The meaning of 1 phr here is 1 g of substance, based on 100 g of polymer.
The necessary temperature is mostly achieved by using mechanical energy, where the mixture is, by way of example, kneaded along a relatively long path within the interior of a screw-based extruder, and is thus heated. The shaping process mostly uses a die, through which the heated mixture is forced. The preferred intention is that the mouldings are dimensionally stable, have a smooth surface, and have no indentations at the sides or corners.
The quality of the resultant mouldings here is preferably assessed using the Garvey die to DIN 2230-96 in an extrusion test.
The processing of the polybutadienes according to the invention with polydispersity smaller than 2.5 is found to be very easy and to give smooth surfaces on the mouldings, when the processing temperature is lowered, as a function of the proportion of the polybutadiene, to from 40 to 75° C., or in the case of mixtures without further rubber components, to values below 55° C. This process permits utilization of the favourable properties of these narrowly distributed polybutadienes, e.g. markedly reduced rolling resistance, markedly improved rebound resilience or markedly lower abrasion when comparison is made with other polybutadienes, good processing, for example in various mixtures for tyre technology, in the golf-ball industry or for the production of technical rubber products.
The examples below serve to illustrate the invention, but with no resultant limiting effect.
Rubber mixtures were produced comprising BUNA™ CB 22 and BUNA™ CB 25 as Nd-catalysed polybutadienes, and also, for comparison, TAKTENE® 220 and TAKTENE® 221 as co-polybutadiene. The analytical results for the polybutadienes are stated in Table 1. Table 2 lists the constituents of the mixtures. The mixtures were initially produced without sulphur and accelerator in a 1.5 l kneader. The mixture constituents sulphur and accelerator were then admixed on a roll at 40° C.
The following substances were used for the studies on the mixtures:
To assess surface, an extrudate was produced through the Garvey die from the unvulcanized mixtures of Inventive Examples 1 and 2, and CE1 and CE2, and studied. The extrusion test was carried out using a Brabender miniature extruder with a Garvey die of dimensions 16 mm/10 d. The quality of the surface was evaluated to DIN 2230-96, Rating System B. Profile quality from A8 to A10 is evaluated as good, and quality from C3 to E1 is evaluated as poor. However, the evaluation can also be carried out on the basis of the figures, without any rating system.
For 90° C., the temperature of the barrel was controlled to 90° C. and that of the die was controlled to 105° C. For 55° C., the temperature of the barrel and die was controlled at 55° C.
It can be seen that for 90° C. the surface quality of the extruded mouldings (I and III) in the Comparative Examples CE1 and CE2 is substantially smoother, with rating A9, than for 55° C. (II and IV), with rating from C3 to D2. In Inventive Examples 1 and 2, the polybutadienes exhibit a smoother surface of the mouldings for 55° C. (VI and VIII), with rating from A8 to A9, than for 90° C. (V and VII), with rating from C3 to D2.
The figures clearly show the good effect of the low temperature on the surface profile of the mixtures according to Inventive Examples 1 and 2. Use of cis-polybutadienes with polydispersity smaller than 2.5 can combine vulcanizate properties which are very good in comparison with other polybutadienes, e.g. markedly reduced rolling resistance, improved rebound resilience or reduced abrasion, with simple production of mouldings with a smooth surface, if the processing temperature is lowered, as a function of the proportion of the said polybutadienes, to from 40 to 75° C., or in the case of mixtures without further rubber components, to values below 55° C.
The lower temperature permits by way of example extrusion of mixtures using Nd-catalysed polybutadienes at the same high speed usually used at the higher temperatures for other mixtures, and this underlines the quality of the process according to the invention.
| Number | Date | Country | Kind |
|---|---|---|---|
| 10 2008 053 888.4 | Oct 2008 | DE | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2009/063954 | 10/23/2009 | WO | 00 | 8/10/2011 |
