STABILISING POLYMERS

Abstract: A process for improving the stability of a polymer comprises mixing the polymer with a sulphurcontaining compound under conditions which cause oxidation of the compound, and adding an ultra-violet stabiliser to the polymer. Oxidation may be achieved by conducting the mixing in closed apparatus, in the presence of a peroxide, or in apparatus open to the atmosphere. The uv stabiliser may be added before mixing, e. g. chemically incorporated in the sulphur-containing compound.

Description: STABILISING POLYMERS This invention relates to a process for stabilising polymers such as polyolefines. It is known that sulphur-containing compounds can be used to stabilise polyolefines. British Patent Specification No. 794,878 discloses the stabilisation of low pressure polyolefines with up to 2% w/w of a tetraalkylthiuram, e.g. tetramethylthiuram, disulphide. US Patent Specification No. 2,582,510 has a similar disclosure, but in which sulphur is used as an additional stabiliser. Burn et al., J. Inst. Petr.(1971) 57 (558) 319-330,discuss the kinetics of cumene hydroperoxide decomposition in the presence of a disulphide, "using the same reaction conditions as with zinc dithiophosphate. The results show that, at the lowest concentration employed (2.5 x 10 5 M), the disulphide is inactive, unlike the zinc dithiophosphate. The kinetics also show a completely different concentration effect from that obtained with the zinc dithiophosphate. Disulphide can therefore be dismissed as a key intermediate in the zinc dithiophosphate-catalysed decomposition of cumene hydroperoxide". Howard et al., Can. J. Chem. (1973) 51, 1543-1553, discuss a study of the reaction of zinc dialkyl dithiophosphates and related compounds with peroxy radicals. They state that "it would appear that zinc dithiophosphates react with hydroperoxides to produce a more active antioxidant", but also that "there is no experimental evidence to indicate that peroxy radicals react with organosulphur compounds at the sulphur atom" and that compounds such as the disulphide t(i-PrO)2PS2J2 "do not inhibit autoxidation or react with t-butylperoxy radicals 11 at low temperatures Howard et al., Can. J. Chem. (1976) 54, 390-401, report a study of the reaction of nickel dialkyldithiocarbamates and dialkyldithiophosphates with hydroperoxides. They report that their work "has produced results which are at variance with those reported in the literature and indicates that these nickel complexes cannot be expected to function as preventive antioxidants at ambient temperature Al-Malaika and Scott, Eur. Poly. J. (1980) 16, 503-509, describe the reaction of nickel dialkyldithiophosphates, and also the corresponding dithiocarbamates and xanthates, with a hydroperoxide in a solvent, in the absence of polymer. In each case, the salts first removed peroxide by one mechanism, as they are converted to disulphides; after an induction period, in which the disulphides are further oxidised, they become antioxidants acting by a different mechanism. Al-Malaika and Scott, Eur. Polym. J. (1980) 16, 709-714, disclose the use of nickel dithiophosphates and xanthates, and the corresponding disulphides, for the stabilisation of polyethylene, using an open or closed mixer. It is suggested that improved uv stabilisation is achieved as a result of oxidation of a disulphide. In each experiment, the amount of the sulphur-containing additive was 0.25 mmole (0.135 g nickel 0,0-dibutyl dithiophosphate) per 100 g polymer0 Although disulphides of the type described above can act as good heat stabilisers when processed as described, they provide little or no effective lightstabilising properties. It has now been found that polymers such as those of the type described can be stabilised, using known stabilisers, under commercially more attractive conditions, to give products having high stability, in particular good uv stability. According to the present invention, a process for improving the stability of a polymer comprises mixing the polymer with a sulphur-containing compound under conditions which cause oxidation of the compound, and adding an ultra-violet stabiliser to the polymer. The ultra-violet stabiliser may be added before, during or after the mixing. The invention involves oxidative processing of a polymer, contrary to normal practice in industry, where every effort is made to exclude air. In the method according to the present invention, deliberate oxidation allows compounds generally thought to be poor stabilisers to be converted into very effective antioxidants. Surprisingly, it has been found that the use of a conventional uv stabiliser can act synergically with the sulphurcontaining compound, even if added before mixing, whereas uv stabilisers are normally rendered ineffective by oxidation. The sulphur-containing compound, as added to the mix, may be considered to be a precursor of the active stabilising entity, and will be referred to herein as a "precursor". One or more precursors may be used. In general, the sulphur-containing precursor is of the type X-(S) n I wherein n is a positive integer and X and Y are either separate groups which may be the same or different or are one linking, divalent group, and where preferably at least one of X and Y contains one or more atoms of sulphur0 When X and Y are separate and the same, they are preferably one of EMI4.1 wherein each Z is R2N- or RO- and R is alkyl, aryl, aralkyl, heteroaryl, heteroalkyl or alkenyl, any of which may bear substituents. The group or groups R may also form part of a polymer or oligomer chain or, in cases where two groups R are present in the same group X or Y, the R groups may be linked to each other by a chain of 2 to 4 carbon atoms to form a heterocyclic ring. When X and Y are separate and different, X may be, for example, one of the groups defined above, preferably II, III or IV, while Y is of the same form but containing an R group which may be a stabilising group per Seo such as 4-benzoyl-3-hydroxyphenylO Alternatively, Y may be be a uv stabilising group which yields a uv stabiliser in situ in the process of the invention0 When X and Y are linked, R groups in each of formulae II-V may be one, divalent, group, eOg. C18 alkylene. X and Y may also be linked so that the precursor is S8 e n is generally 1 to 8, e.g. 1 to 4, and is preferably at least 2. The precursor is thus preferably a disulphide or other polysulphide. Examples (the second of which has an incorporated uv stabilising group) are: EMI5.1 EMI6.1 Precursor compounds such as those exemplified here may all be prepared by general methods described in the literature. For example, the dithiophosphates (containing Group II) are prepared by the series of reactions: EMI6.2 <tb> P2S5 <SEP> + <SEP> 4ROH <SEP> > <SEP> 2 <SEP> (RO)2P(S)SH <SEP> + <SEP> H2S <tb> <SEP> NH <SEP> oxidation <tb> <SEP> NH3 <SEP> 2(RO)2P(S)SNH4 <SEP> oxidation <SEP> (S) <SEP> -S-S- <SEP> (S) <SEP> P <SEP> (OR) <SEP> 2 <tb> and these reactions are described by Wystrack et al. r J. Org. Chem. (1956) 21, 705 and Makens et al., Anal. Chem. (1955) 27, 1062. Dithiocarbamates and xanthates may be made by reacting CS2 with either amines or alcohols to give the corresponding dithioacids which are converted to the sodium salt and oxidised. For example, the disulphides derived from the xanthates may be prepared according to the method of Whitby et al., Trans. RoyO Soc. Can. (1929) 23, 21. Some of the dithiocarbamates are already articles of commerce used for other purposes. Disulphides, tetrasulphides and zinc or nickel salts may be obtained commercially. An alternative procedure is to make the compound of formula I from the salt, e.g. a nickel or zinc salt, of a dithioacid by oxidation during polymer processing prior to the oxidation of the compound of formula I which produces the effective stabiliser. Suitable polymers for use in the invention are thermoplastic polymers such as polyolefines,acrylonitrilebutadiene-styrene, ethylene-propylene-diene terpolymer, polyvinyl chloride, polystyrene and unsaturated rubbers treated before vulcanisation. Preferred polymers include polyolefines. Particularly suitable polyolefines are polyethylene and polypropylene. The process of the invention may be conducted in various ways, in order to ensure the necessary oxidising conditions. These may be summarised as follows: Procedure A: the precursor is mixed with the polymer and processed in a mixer open to the atmosphere, e.g. in a torque rheometer. Procedure B: the polymer/precursor mixture is processed in a mixer which is closed for most of the mixing period but which is opened to the atmosphere for a short time during that period. This procedure is similar to A but can sometimes provide a more satisfactory degree of oxidation. Procedure C: the polymer and precursor are mixed without contact with the atmosphere, e.g. in a closed mixer, and oxidation is achieved by including a suitable compound in the reaction mixture Such a compound may be a radical generator such as a peroxide, e.g. a hydroperoxide. Mixing may be conducted for, for example, 1 to 60 minutes. Up to 30 minutes is usually satisfactory in procedure A, while up to 20, and often no more than 10, minutes are satisfactory in procedures B and CO In procedure B, a torque rheometer may be open for only one minute of a 10 minute mixing period, the apparatus being closed during the first 5 and last 4 minutes of this period. The temperature during mixing will usually be at least 75, preferably at least 100, and more preferably at least 150 C. In general, times and temperatures will be dependent on the nature of the polymer; typical examples are, particularly in procedure A, 30 minutes at 1500C for polyethylene and 15 minutes at 1800C for polypropylene. The same temperatures are appropriate for the same polymers in the other procedures. The amount of precursor which is used may be chosen so that the product of the oxidative mixing procedure has the desired concentration of stabiliser0 For example, the amount may be 0.01 to 5, preferably 0.03 to 3, and more preferably 0.05 to 0.5% by weight of precursor, based on the weight of polymer. Such concentrations can be used particularly satisfactorily in procedure C. In general, it is preferred that a higher concentration of precursor should be used, and that the product of the oxidative mixing is diluted with further polymer; the diluted product may contain an amount of antioxidant within the ranges given immediately above. Before dilution, the product may be termed a "masterbatch". A masterbatch preferably contains at least 0.5% by weight of the precursor, with respect to the weight of the polymer; the concentration of the precursor in the polymer, for masterbatching, is usually no more than 50, preferably no more than 30, more preferably from 1 to 20, and most preferably from 2 to 10% by weight. If procedure C is used, suitable peroxides have a half-life of 0.1 to 400 min. at the operating temperature. Examples include cumene, tert-butyl and diisopropylbenzene hydroperoxides, and di-tert-butyl and dicumyl peroxides. The peroxide is preferably chosen so that fram 0.5 to 3 g atan 0 are taken up during the mixing, per g atom S in the precursor. This range is also preferred for procedures A and B, making the latter more appropriate if controlled aeration is necessary. In either case, suitable oxidation conditions can be achieved using masterbatching under the given mixing conditions of time and temperature. If a masterbatching technique is used, the masterbatch may be diluted with the same or different polymer as that in the masterbatch, or used to stabilise other organic materials, against oxidation. Dilution with a polymer may be conducted in a closed mixer for, for example, 5 minutes. As has been indicated above, uv stabiliser may be added before (separately from and/or chemically incorporated in the precursor), during or after the mixing. If masterbatching is used, after mixing and before dilution can be a convenient point to add uv stabiliser. Addition during the mixing is less often convenient, particularly in procedure C although the opening of closed apparatus in procedure B allows a suitable opportunity. Nevertheless, if desired, the specified oxidative mixing period may be foliowed by a further processing period, e.g. of 5 minutes, following the addition of uv stabiliser. It is often preferred that part at least of the uv stabiliser should be added before the oxidative mixing period. Any other desired additives to the polymer may be included at the same time as uv stabiliser. Any material known to have a uv stabilising effect on the polymer in question may be used in the invention. Uv stabilisers are generally well known, and examples are given in "The World Index of Polyolefin Stabilizers ed. T.J. Henman, pub. Kogan Page, London (1982). Such compounds include 2-hydroxybenzophenones, 2-hydroxyphenylbenz- triazoles, hindered phenols, hindered piperidines and nickel and zinc salts of the type described above for use as starting materials for the precursor compounds. More than one uv stabiliser may be used. For example, one stabiliser may be added before, and another after, the oxidative mixing. Compounds which do not contain sulphur, and which cannot be oxidised to give the active antioxidants which the process of the invention gives, can be added at any stage. Compounds such as the nickel and zinc salts described above may be added after the oxidative mixing, in order to provide uv stability. The amount of uv stabiliser used in the invention may be such that the product, after dilution if a masterbatch technique has been used, contains from 0.01 to 3, more preferably 0.1 to 1, % by weight of the uv stabiliser with respect to the weight of polymer in the product. It is a feature of the effective antioxidants used in the invention that, unlike presently commercially available stabilisers, they are virtually non-volatile and often cannot be extracted by, for example, boiling water for 30 hours. It appears that the oxidation not only forms new antioxidants but also results in very strong association between the antioxidant and the polymer. This makes the products of the invention, not only very effective as will be apparent from the data presented below, but also more durable than currentlyavailable stabilised polymers. The polymer products of the invention can also be colourless. Polyethylene treated by the process of the invention can be used, for example, in greenhouse films and boat covers. Polypropylene can be treated by the process of the invention to give fibres having desirable properties. Products of the invention can also be used for garden hose, insulation for electrical (e.g. telephone) wiring, solar collectors, bottle crates, suitcases, automobile fenders, garden furniture and film for the protection of building sites. The following Examples illustrate the invention, or are given for the purposes of comparison. Of the abbreviations used in the Examples, "DBDS" and "DODS" are sulphur-containing precursors exemplified above. TBH" is tert-butyl hydroperoxide. The structures of the stabilisers which are used are as follows ("Irganox", ACyasorb" and "Tinuvin" are registered Trade Marks): Irganox 1010 EMI12.1 EMI12.2 <tb> <SEP> OH <tb> <SEP> (CH3) <SEP> C <SEP> (CH3) <SEP> 3 <tb> Irganox <SEP> 1076 <tb> <SEP> CH2CH2COOCl <SEP> 8H37 <tb> Cyasorb UV 531 HOBP EMI12.3 EMI12.4 <tb> <SEP> tert-CH17 <SEP> 0 <tb> Cyasorb <SEP> UV <SEP> 1084 <SEP> 2 <SEP> - <SEP> - <SEP> - <SEP> knit <SEP> no <SEP> C <SEP> --NH2C4H9 <tb> <SEP> tert-C8H17 <SEP> 0 <tb> Tinuvin 326 EMI12.5 Tinuvin 770 EMI13.1 NiDSBP NiDOP ZnDSBP EMI13.2 In the Examples, the main test procedures used are as follows: : Carbonyl Index and Embrittlernent time This procedure is described by Willard et al., 'Instrumental Methods of Analysis" 5th edition (1974) published by van Nostrand (New York). A film is irradiated in a uv cabinet and the formation of carbonyl is measured in the infra-red at 1710 cm-1. The embrittlement time is measured by flexing samples through 180 and recording the time of irradiation (at 300C) before they break. Thermal Stability The embrittlement time is measured for film held at 140 C in a circulating oven. Melt Flow Index The melt stability is measured in a Davenport melt indexer at 2300C under a load of 2.16 kg. The weight extruded in 10 minutes is measured. Examples 1 and 2 Low density polyethylene was processed in an open mixer for 30 minutes at 150 C with, per 100 g thereof, 2.5 g diisopropyl dithiophosphoryl disulphide (Example 1) or isopropyl dithiocarbonyl disulphide (Example 2), and 2.5 g HOBP. When the product of each run was diluted to 0.1 g/100 g in low density polyethylene, the respective photo-embrittlement times were 5500 and 4800 hours. When Example 1 was repeated, except that the processing was conducted in a closed mixer, the embrittlement time was 2550. A conventional combination of uv stabilisers (CZasorbs W 531, i.e. HOBP, and UV 1084), each used in an amount of 0.2 g per 100 g of polymer, when processed normally in a closed mixer, gave an embrittlement time of 3300 hours. A control film, without any additives, gave an embrittlement time of 1050 hours. Example 3 Polypropylene was processed in an open mixer for 10 minutes at 180 0C with 2.5 g DODS per 100 g and then diluted to 0.2 g/100 g by the addition of 0.1 g/100 g NiDOP and 0.2 g/100 g HOBP. The embrittlement time was 4200 hours. Example 4 Polypropylene was processed in an open mixer for 15 minutes at 180 0C with 2.5 g DODS and 2.5 g HOBP per 100 g, and then diluted to 0.2% (total additive concen tration), with the addition of 0.2 g/100 g NiDOP. The embrittlement time was more than 4250 hours. By contrast, the conventional combination of uv stabilisers specified in the comparison to Examples 1 and 2, each used in an amount of 0.2 g/100 g of polymer, when processed normally in a closed mixer, gave uv embrittlement time of 1530 hours. A control film, without any additives, gave an embrittlement time of 90 hours. Procedures generally similar to those of the preceding Examples were used in those reported below. If the masterbatch technique was used, the amount of additive before oxidative mixing is given in the "masterbatch" column, and other additions are made before dilution with the same polymer and processing for 5 min. in a closed mixer (torque rheoneter).Procedures A, B and C are as generally described above; in procedure A, polyethylene is oxidatively processed for 30 minutes and polypropylene for 15 minutes; in procedure B, the mixer is closed for 5 minutes, open for 1 minute and closed for 4 minutes, before dilution; procedure C is conducted for 10 minutes. Procedure N avoids deliberate oxidation, although a minor degree of oxidation can occur in batch processing. Temperatures were 1500C and 180 0C for polyethylene and polypropylene, respectively. Polypropylene was used in Examples 5 to 79 and 85 to 90, polyethylene in 80 to 84. The results of these Examples are given in the following Tables. Table 1 shows the advantages of oxidising the precursor. Table 2 shows that procedure C can be preferable to procedure A. Table 3 illustrates the superiority of the invention (3-II) aver commercial stabilisation systems (3-I),and the synergism between an oxidised sulphurcontaining compound and a conventional uv stabiliser. Table 4 illustrates the use of metal complexes which are apparently converted to disulphide precursors in situ. Table 5 illustrates the use of another precursor and, like the two previous Tables, demonstrates the advantage of incorporating at least one of the uv stabilisers in the oxidative mixing stage. Tables 6 and 7 illustrate the advantages of the invention, in terms of stabilisation measured by melt flow index and thermal stability tests. Table 8, like Table 5, illustrates the use of a complex to form the precursor, and illustrates the fact that a uv stabiliser (HOBP) alone loses activity on oxidation but becomes more effective when used in the oxidative mixing process of the present invention. Table 9 illustrates results achieved after extracting diluted masterbatch films with boiling water for 20 hours. TABLE 1 EMI17.1 Carbonyl <tb> Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> Index <SEP> at <tb> No. <SEP> Procedure <tb> DBDS <SEP> S8 <SEP> HOBP <SEP> NiDSBP <SEP> 1000hrs. <tb> 5 <SEP> 2.5% <SEP> S8 <SEP> A <SEP> - <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.11 <tb> 6 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> - <SEP> 0.2 <SEP> 0.1 <SEP> 0.11 <tb> 7 <SEP> 2.5%S8 <SEP> + <SEP> 2.5%DBDS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.11 <tb> 8 <SEP> 2.5%S8 <SEP> + <SEP> 2.5%HOBP <SEP> A <SEP> - <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.10 <tb> 9 <SEP> 2.5%DBDS <SEP> + <SEP> 2.5% <SEP> A <SEP> 0.2 <SEP> - <SEP> 0.2 <SEP> 0.1 <SEP> 0.10 <tb> HOBP <tb> Controls <tb> 10 <SEP> 2.5% <SEP> S8 <SEP> N <SEP> - <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.42 <tb> 11 <SEP> 2.5% <SEP> DBDS <SEP> N <SEP> 0.2 <SEP> - <SEP> 0.2 <SEP> 0.1 <SEP> 0.20 <tb> 12 <SEP> 2.5%S8 <SEP> + <SEP> 2.5% <SEP> HOBP <SEP> N <SEP> - <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.30 <tb> TABLE 2 EMI18.1 Carbonyl <SEP> Time(hrs) <SEP> Embrittle Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> Index <SEP> at <SEP> to <SEP> carbonyl <SEP> ment <SEP> time <tb> No. <SEP> Procedure <tb> DBDS <SEP> TBH <SEP> HOBP <SEP> NiDSBP <SEP> 1000hrs. <SEP> index <SEP> 0.5 <SEP> (hours) <tb> 13 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> 350 <SEP> 420 <tb> 14 <SEP> - <SEP> C <SEP> 0.2 <SEP> 0.1 <SEP> 200 <SEP> 550 <tb> 15 <SEP> - <SEP> C <SEP> 0.2 <SEP> 0.2 <SEP> 650 <SEP> 700 <tb> 16 <SEP> - <SEP> C <SEP> 0.2 <SEP> 0.2 <SEP> 500 <SEP> 650 <tb> 17 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> - <SEP> 0.2 <SEP> 0.2 <SEP> 0.045 <tb> 18 <SEP> - <SEP> C <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.075 <tb> 19 <SEP> 2.5%DBDS <SEP> + <SEP> A <SEP> 0.1 <SEP> - <SEP> 0.1 <SEP> 0.1 <SEP> 680 <SEP> 950 <tb> 2.5% <SEP> HDBP <tb> 20 <SEP> - <SEP> C <SEP> 0.1 <SEP> 0.05 <SEP> 0.1 <SEP> 0.1 <SEP> 0.08 <tb> 21 <SEP> - <SEP> C <SEP> 0.1 <SEP> 0.1 <SEP> 0.1 <SEP> 0.1 <SEP> 0.07 <tb> 22 <SEP> - <SEP> C <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> 0.1 <SEP> 0.18 <tb> 23 <SEP> 2.5%DBDS <SEP> + <SEP> 2.5% <SEP> C <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> - <SEP> 0.08 <tb> TBH <tb> 24 <SEP> 2.5%DBDS <SEP> + <SEP> 2.5% <SEP> C <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.09 <tb> TBH <tb> 25 <SEP> 2.5%DBDS <SEP> + <SEP> 2.5% <SEP> C <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.09 <tb> TBH <tb> TABLE 3-I EMI19.1 Embrittle Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Stabiliser <SEP> ment <SEP> time <tb> No. <SEP> Procedure <tb> DBDS <SEP> HOBP <SEP> NiDSBP <SEP> Other <SEP> (hours) <tb> 26 <SEP> HOBP <SEP> N <SEP> 0.2 <SEP> 400 <tb> 27 <SEP> HOBP <SEP> N <SEP> 0.3 <SEP> 650 <tb> 28 <SEP> Cyasorb <SEP> UV <SEP> 1084 <SEP> N <SEP> 0.2 <SEP> 445 <tb> 29 <SEP> Cyasorb <SEP> UV <SEP> 1084 <SEP> N <SEP> 0.4 <SEP> 890 <tb> 30 <SEP> Tinuvin <SEP> 770 <SEP> N <SEP> 0.2 <SEP> 540 <tb> 31 <SEP> Tinuvin <SEP> 770 <SEP> N <SEP> 0.4 <SEP> 900 <tb> 32 <SEP> HOBP <SEP> + <SEP> Cyasorb <tb> UV1084 <SEP> N <SEP> 0.2 <SEP> 0.2 <SEP> 1520 <tb> 33 <SEP> DBDS <SEP> N <SEP> 0.1 <SEP> 220 <tb> 34 <SEP> DBDS <SEP> N <SEP> 0.15 <SEP> 240 <tb> 35 <SEP> DBDS <SEP> N <SEP> 0.2 <SEP> 280 <tb> 36 <SEP> Ni <SEP> DSBP <SEP> N <SEP> 0.1 <SEP> 1050 <tb> 37 <SEP> Ni <SEP> DSBP <SEP> N <SEP> 0.15 <SEP> 1500 <tb> 38 <SEP> Ni <SEP> DOP <SEP> N <SEP> 0.2 <SEP> 750 <tb> TABLE 3-II EMI20.1 Embrittle Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> ment <SEP> time <tb> No. <SEP> Procedure <tb> DBDS <SEP> HOBP <SEP> NiDSBP <SEP> (hours) <tb> 39 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <SEP> B <SEP> 0.15 <SEP> 0.3 <SEP> 0.15 <SEP> > 5000 <tb> HOBP <SEP> + <SEP> 2.5%NiDSBP <tb> 40 <SEP> 2.5% <SEP> DBDS <SEP> N <SEP> 0.15 <SEP> 0.3 <SEP> 0.15 <SEP> 2900 <tb> 41 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 2.5% <SEP> A <SEP> 0.1 <SEP> 0.2 <SEP> 0.2 <SEP> 2800 <tb> 42 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <SEP> A <SEP> 0.1 <SEP> 0.2 <SEP> 0.2 <SEP> 3150 <tb> HOBP <tb> 43 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <SEP> N <SEP> 0.1 <SEP> 0.2 <SEP> 0.2 <SEP> 2000 <tb> HOBP <tb> 44 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <SEP> N <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> 2100 <tb> HOBP <tb> 45 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <tb> HOBP <SEP> + <SEP> 2.5%NiDSBP <SEP> B <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> > 4500 <tb> 46 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 2800 <tb> 47 <SEP> 2.5% <SEP> DBDS <SEP> N <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> 1500 <tb> TABLE 4 EMI21.1 Carbonyl <tb> Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> Index <SEP> at <tb> No. <SEP> Procedure <tb> ZnDSBP <SEP> HOBP <SEP> NiDSBP <SEP> 1000hrs. <tb> 48 <SEP> 2.5% <SEP> ZnDSBP <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.12 <tb> 49 <SEP> 2.5% <SEP> ZnDSBP <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.15 <tb> 50 <SEP> 2.5% <SEP> ZnDSBP <SEP> + <tb> 2.5% <SEP> HOBP <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.06 <tb> 51 <SEP> 2.5% <SEP> ZnDSBP <SEP> + <tb> 2.5% <SEP> HOBP <SEP> N <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.08 <tb> TABLE 5 EMI21.2 Carbonyl <tb> Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> Index <SEP> at <tb> No. <SEP> Procedure <tb> DODS <SEP> HOBP <SEP> NiDOP <SEP> 1000hrs. <tb> 52 <SEP> 2.5% <SEP> DODS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.060 <tb> 53 <SEP> 5% <SEP> DODS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.075 <tb> 54 <SEP> 10% <SEP> DODS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.085 <tb> 55 <SEP> 2.5% <SEP> DODS <SEP> + <SEP> 2.5% <tb> HOBP <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 0.045 <tb> TABLE 6 EMI22.1 Embrittle- <SEP> Melt <tb> Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> ment <SEP> time <SEP> flow <tb> No. <SEP> Procedure <tb> DBDS <SEP> HOBP <SEP> NiDSBP <SEP> Others <SEP> (hours) <SEP> index <tb> 56 <SEP> No <SEP> additive <SEP> N <SEP> 90 <SEP> 0.81 <tb> 57 <SEP> Irganox <SEP> 1076 <SEP> N <SEP> 0.2 <SEP> 325 <SEP> 0.39 <tb> 58 <SEP> Irganox <SEP> 1076 <SEP> N <SEP> 0.4 <SEP> 350 <SEP> 0.35 <tb> 59 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <SEP> B <SEP> 0.15 <SEP> 0.3 <SEP> 0.15 <SEP> > 5000 <SEP> 0.29 <tb> HOBP <SEP> + <SEP> 2.5% <tb> NiDSBP <tb> 60 <SEP> 2.5%DBDS <SEP> + <SEP> 5% <SEP> HOBP <tb> + <SEP> 2.5% <SEP> NiDSBP <SEP> B <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> > 3500 <SEP> 0.27 <tb> 61 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <tb> HOBP <SEP> A <SEP> 0.1 <SEP> 0.2 <SEP> 0.2 <SEP> > 3000 <SEP> 0.21 <tb> 62 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 2800 <SEP> 0.31 <tb> 63 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> 420 <SEP> 0.34 <tb> 64 <SEP> 20% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> 330 <SEP> 0.37 <tb> 65 <SEP> 2.5% <SEP> S8 <SEP> A <SEP> 0.2 <SEP> 480 <SEP> 0.34 <tb> TABLE 7 EMI23.1 Embrittle Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> ment <SEP> time <tb> No. <SEP> Procedure <tb> DODS <SEP> HOBP <SEP> NiDOP <SEP> (hours) <tb> 66 <SEP> 2.5% <SEP> DODS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 40 <tb> 67 <SEP> 2.5% <SEP> DODS <SEP> + <SEP> 5% <SEP> A <SEP> 0.13 <SEP> 0.27 <SEP> 0.2 <SEP> 65 <tb> HOBP <tb> 68 <SEP> 5% <SEP> DODS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 65 <tb> 69 <SEP> 2.5% <SEP> DODS <SEP> + <SEP> 2.5% <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.2 <SEP> 65 <tb> HOBP <tb> Controls <SEP> Irg. <SEP> Cy. <SEP> Other <tb> 70 <SEP> No <SEP> addition <SEP> N <SEP> 1 <tb> 71 <SEP> Irganox <SEP> 1076 <SEP> N <SEP> 0.2 <SEP> 60 <tb> 72 <SEP> Irganox <SEP> 1076 <SEP> N <SEP> 0.4 <SEP> 92 <tb> 73 <SEP> Irganox <SEP> 1010 <SEP> N <SEP> 0.2 <SEP> 48 <tb> 74 <SEP> Irganox <SEP> 1010 <SEP> N <SEP> 0.4 <SEP> 54 <tb> 75 <SEP> Cyasorb <SEP> UV <SEP> 1084 <SEP> N <SEP> 0.2 <SEP> 12 <tb> 76 <SEP> Cyasorb <SEP> UV <SEP> 1084 <SEP> N <SEP> 0.4 <SEP> 28 <tb> 77 <SEP> Irganox <SEP> 1076 <SEP> + <tb> HOBP <SEP> N <SEP> 0.2 <SEP> 0.2 <SEP> 60 <tb> 78 <SEP> Irgenox <SEP> 1076 <SEP> + <tb> Tinuvin <SEP> 770 <SEP> N <SEP> 0.2 <SEP> 0.2 <SEP> 12 <tb> 79 <SEP> Cyasorb <SEP> UV <SEP> 1084 <SEP> + <tb> HOBP <SEP> N <SEP> 0.2 <SEP> 0.2 <SEP> 16 <tb> TABLE 8 Additives each 2.5 x 10-4 moles per 100g. EMI24.1 <tb> Ex. <SEP> Additi@@ <SEP> <SEP> Oxidation <SEP> Time <SEP> (hours) <SEP> to <tb> No. <SEP> Additive <SEP> procedure <SEP> carbonyl <SEP> Index <SEP> 8.0 <tb> 80 <SEP> | <SEP> None <SEP> A <SEP> 180 <tb> 81 <SEP> HOBP <SEP> A <SEP> 290 <tb> 82 <SEP> HOBP <SEP> N <SEP> 820 <tb> 83 <SEP> NiDSBP <SEP> A <SEP> 1550 <tb> 84 <SEP> | <SEP> NiDSBP <SEP> and <SEP> HOBP <SEP> A <SEP> 2520 <tb> TABLE 9 EMI25.1 Carbonyl <SEP> Embrittle Ex. <SEP> Oxidation <SEP> % <SEP> w/w <SEP> on <SEP> Dilution <tb> Masterbatch <SEP> Index <SEP> at <SEP> ment <SEP> time <tb> No. <SEP> Procedure <tb> DBDS <SEP> HOBP <SEP> NiDSBP <SEP> Tin. <SEP> 750 <SEP> hrs. <SEP> (hours) <tb> 85 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.2 <SEP> 0.2 <SEP> 0.1 <SEP> 0.10 <tb> 86 <SEP> 2.5% <SEP> DBDS <SEP> A <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> 0.10 <tb> 87 <SEP> 2.5% <SEP> DBDS <SEP> + <SEP> 5% <tb> HOBP <SEP> A <SEP> 0.1 <SEP> 0.2 <SEP> 0.2 <SEP> 0.09 <tb> 88 <SEP> 2.5% <SEP> DBDS <SEP> + <tb> 5% <SEP> HOBP <SEP> + <SEP> B <SEP> 0.1 <SEP> 0.2 <SEP> 0.1 <SEP> 0.07 <tb> 2.5% <SEP> NiDSBP <tb> 89 <SEP> 2.5% <SEP> DBDS <SEP> + <tb> 5% <SEP> HOBP <SEP> + <SEP> B <SEP> 0.15 <SEP> 0.3 <SEP> 0.15 <SEP> 0.06 <tb> 2.5% <SEP> NiDSBP <tb> Control <tb> 90 <SEP> Tinuvin <SEP> 770 <SEP> N <SEP> 0.2 <SEP> 0.55 <SEP> (at <SEP> 350 <tb> 350 <SEP> hr.) <tb>

Claims: CLAIMS 1. A process for improving the stability of a polymer, which comprises mixing the polymer with a sulphurcontaining compound under conditions which cause oxidation of the compound, characterised in that an ultra-violet stabiliser is added to the polymer. 2. A process according to claim 1, in which the mixing is conducted in closed apparatus in the presence of a peroxide. 3. A process according to claim 1, in which the mixing is conducted in apparatus open to the atmosphere. 4. A process according to any preceding claim, in which the mixture comprises at least 0.5% by weight of the sulphur-containing compound, based on the weight of the polymer, and the product of the oxidative mixing is diluted with polymer which has not been so treated. 5. A process according to any preceding claim, in which the polymer product contains the equivalent of from 0.05 to 1% w/w of the sulphur-containing compound. 6 A process according to any preceding claim, in which the sulphur-containing compound has the formula X-(S) nY wherein n is from 2 to 8, and X and Y are either separate groups which are the same or different, at least one of which contains one or more sulphur atoms, or are one linking, divalent group. 7. A process according to any preceding claim, in which part at least of the ultra-violet stabiliser is added before the mixing. 8. A process according to claim 7, in which the ultraviolet stabiliser is chemically incorporated in the sulphur-containing compound. 9. A process according to any preceding claim, in which the polymer product contains the equivalent of from 0.1 to 1% w/w of the ultra-violet stabiliser. 10. A process according to any preceding claim, in which the polymer is polyethylene or polypropylene.

Inventors: AL-MALAIKA, SAHAR NADUM, SCOTT, GERALD
Applicants: SHELL INTERNATIONALE RESEARCH MAATSCHAPPIJ B.V.
Application year: 1983
Main classification: C08K5
IPC codes: C08L101, C08L23, C08K5