Study of the thermo-oxidative degradation behavior of isotactic polypropylene with the varying ethylene content

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Indian Journal of Chemistry Vol. 46B, July 2007, pp. 1198-1202 Note Study of the thermo-oxidative degradation behavior of isotactic polypropylene with the varying ethylene content M S Alam*, S M Abdur Razzaque, G M Arifuzzaman Khan A K Chakraborty & M Moniruzzaman Department of Applied Chemistry & Chemical Technology Islamic University, Kushtia 7003, Bangladesh E-mail: gm_arifuzzaman@yahoo.com Received 21 December 2004; accepted (revised) 8 September 2006 The thermo-oxidative degradation behavior of isotactic polypropylene is studied as a function of varying ethylene and oxygen concentration effects by means of gel permeation chromatography (GPC) measurement. The thermal stability of three types of isotactic polypropylene viz.,, which contains 0, 0.5, 2.7 wt% of ethylene, respectively having similar average molecular weights and molecular weight distribution ( M w/ M n) is studied in solution at 453 K. Under this condition, the changes of molecular weight and M w/ M n in isotactic polypropylene samples are decreased with the increase of ethylene. The rate of degradation has also been increased with the increase of oxygen concentration for each sample. The variation of time effect on changing of GPC curve is also studied. GPC curves are changed preferably by the scission of longer chain in, and with the increasing degradation time. The results reveal that the thermo-oxidative stability of isotactic polypropylene significantly depends upon the varying ethylene content incorporation. Keywords: Isotactic polypropylene, ethylene unit incorporation, thermo-oxidative degradation, stability, gel permeation chromatography Polypropylene (PP) in terms of stereoregular is divided into isotactic PP, syndiotactic PP and atactic PP. Among them, isotactic PP has been widely used in the world as medical goods, fibres, raping films etc 1-2. However, isotactic, which has methine protons is very vulnerable to oxidative degradation. The oxidative degradation of isotactic PP is recognized to proceed by radical formation reaction that leads to the scission of the polymer chain, which level is corresponding to the different primary structure of isotactic PP. As a function of isotacticity, the difference in the oxidizability between isotactic PP, syndiotactic PP and atactic PP has been studied to some extent 3-9 and it was concluded that isotactic PP is more susceptible to oxidation. The addition of stabilizers is widely used to improve the oxidative stability of isotactic PP. However, the stabilizers have the disadvantage of limited retain-ability because of volatility 10. Besides stabilizers, there are also other factors that influence the stability of isotactic PP, such as the ethylene incorporation. Terano et al. studied the improvement oxidative stability of isotactic PP by the incorporation of ethylene 11-13. In this study, the thermo-oxidative degradation of isotactic PP was investigated in terms of varying ethylene and oxygen concentration effects at 453 K in solution. Thus, this method is suitable to discuss the effect of single polymer chain on degradation. The purpose of this work is to get the information about the influence of varying ethylene concentration effects in degradation of isotactic PP. Experimental Section Materials Isotactic polypropylene containing varying ethylene content 0, 0.5, 2.7 wt%, respectively are named as, and produced by MgCl 2 - supported Ziegler catalyst were supplied from Chisso Co., Ltd. In order to remove any unfavorable catalyst residues and stabilizers, these samples were stirred overnight in distilled water containing a small amount of ethanol at room temp. Then, they were reprecipitated from a boiling xylene solution into ethanol. Methods The purified samples were dried in vacuo at 333 K for 5 hr. The degradation was carried out in a glassreactor where 20 mg polymer was dissolved in 20 ml 1, 2, 4-trichlorobenzene at 453 K under the various oxygen concentrations (N 2 : 0%, air: 20%, O 2 : 100%) for 30 min. In the case of the degradation under N 2, the reactor was evacuated and filled up with N 2 for 45 min. This procedure was done to remove the O 2 absorbed on the polymer. In the case of the degradation under air and/or under pure O 2, the degradation was performed when the systems were purged by air and/or O 2 using the same apparatus (Figure 1). After the thermo-oxidative degradation, the treated samples in solution were precipitated by ethanol, filtered and dried in vacuo at 333 K for 1 hr. No

NOTES 1199 Gas Tank O 2, Air, N 2 3 4 5 Gas Trap Oil Bath 453 K Figure 1 An apparatus for thermal degradation of polypropylenes additional stabilizer and additive were used during degradation. The degree of degradation was evaluated by the changes of molecular weight and molecular weight distribution ( M w/ M n) of various isotactic PP samples. 463 K at a scanning rate of 10 K/min. Indium was used as the standard for calibrating the temperature axis and the melting temp. at the maximum of the endothermic peak was taken. All the molecular orbital calculations were performed by the PM3 optimization with UHF calculation, as realized in the MOPAC version 7 program. The key word precise was used to increase by a factor of 100 the criteria for terminating all optimization, both electronic and geometric semiempirical methods now based on better approximation and implemented on small computers can be very easily used for the investigation of various reaction mechanisms. Results and Discussion Isotactic polypropylene is a typical plastic whose properties are profoundly affected by the primary structure as a function of varying ethylene Measurement incorporation which the relative stability and Molecular weights and M w/ M n of isotactic PP degradation behavior of isotactic PP are dependent determined by GPC (Senshu, SSC-7100) with on. To get the clear image about the effect of varying polystyrene gel columns (Tosoh, TSK gel G3000HHR primary structure on the degradation of isotactic PP; and G5000HHR) at 413 K using o-di-cholorobenzene, and were used in this study after containing 2,6-di-tert-butyl-p-cresol (antioxidant) as a washing. The degradation reaction was performed at solvent. The calibration curve of the isotactic PP was 453 K for each sample. Degrading polymer molecules made with standard polystyrene samples. undergo a series of chemical reactions whose effects The stereoregularity (pentad fraction) of the can be structural modifications such as side-group polymer was determined by 13 C NMR measurement reaction or elimination or cross-linking. In most cases, using a Varian Gemini-300 spectrometer at 393 K on bond scissions take place on the polymer main chains 20% (w/v) solution in 1,2,4-trichlorobenzene. 10% to yield radical species that may initiate chain (v/v) Benzene-d 6 was added as an internal lock, and processes, while average molecular weights and hexamethyldisiloxane was used as internal chemical shift reference. The melting temp. of PP sample was determined by differential scanning calorimetry (DSC, METTLER DSC 820). Calorimetry was made in nitrogen flux to avoid thermal degradation. The 10 mg of samples molecular weight distribution ( M w/ M n) change continuously 14. Therefore, average molecular weights and M w/ M n changes can reveal fundamental characteristics of the degradation process. Table I lists the calculated values of number average molecular weight ( M n), weight average sealed in aluminium pans and heated from 293 K to molecular weight ( M w), M w/ M n, tacticity Table I - Sample characteristics of isotactic polypropylenes Sample E a wt% M n b M w b M w/ M n b Tacticity c (mmmm%) 0.0 70000 400000 5.7 99 438 0.5 71000 390000 5.5 96 433 2.7 72500 415000 5.7 92 420 a Ethylene content (E wt%) in polypropylene per 100 segments. b M n, M w and M w/ M n were estimated by GPC. c Tacticity was determined by 13 C NMR spectroscopy. d Melting temperature (Tm) determined by DSC. T m d

1200 INDIAN J. CHEM., SEC B, JULY 2007 Table II Effect of ethylene concentration on degradation of isotactic PP under air at 453K for 30 min Sample M n M w M w/ M n 54000 190000 3.5 57000 230000 4.0 62000 293000 4.7 (mmmm%) and melting temperature (Tm) for virgin, and samples by using GPC, NMR and DSC measurements. From this table it is observed that they have almost same average molecular weights and M w/ M n values. The effect of ethylene concentration on thermooxidative degradation of isotactic polypropylenes (, and ) is shown in Table II. The degradation is carried out in solution under air at 453 K for 30 min. The degree of degradation was evaluated by the changes of M n, M w and M w/ M n comparing with the virgin samples. Under this condition, the values of M n, M w and M w/ M n were decreased at lower rate with increasing ethylene concentration. This means that the rate of degradation in and is reduced due to varying ethylene concentration effects compared to. To perform the ethylene concentration effect, the thermo-oxidative degradation behavior of, and by the treatment in various oxygen atmospheres in solution was investigated at the same time and temperature (Table III). It can be seen that decrease in M n, M w and M w/ M n of all samples occurs with the increasing oxygen concentration. Under nitrogen, the M n values for all degraded samples kept constant with the M n values of virgin samples. However, the decreasing rate in is higher than those of and. This reveals that the termination reaction rapidly occurs in compared to and. In general, if the degradation occurs by the chain reaction the GPC curve shifts toward the lower molecular weight side. The GPC curves of, and are shown in Figure 2 as a function of degradation time. The curves of degraded samples were analyzed in respect of virgin isotactic polypropylenes. With the increase of degradation time, the curves shifted towards the lower molecular weight side and it is clearly observed that the shape of the curve changes with reduction in width together Table III - Effect of oxygen concentration on degradation of isotactic PP at 453K for 30 min Sample Oxygen concentration (%) 0 20 100 M n M w M w/ M n 70000 71000 72500 54000 57000 62000 51000 55500 59000 2hr 0h 0h 400000 390000 415000 190000 230000 293000 158000 198000 260000 2 7 8 9 Log M 2h 0h 2h 2 3 4 5 6 7 8 9 Log M 2 3 4 5 6 7 8 9 LogM 5.7 5.5 5.7 3.5 4.0 4.7 3.0 3.6 4.4 Figure 2 Effect of time on GPC curves of ip, epp and under O 2 at 453 K in solution

NOTES 1201 and or CH C C. 180 0 C 3 ~H O 2 C C 1800 C H 2 Fast O O H. C C. CH CH2 180 C C. 0 C 3CH2 180 0 CH C 3 CH ~ 2 C C ~ O 2 O O. Slow C C CH. ~ and or 180 0 CH C 3 C C ~ H2 C C. OH H O. H 180 0 CH C 3 ~H2 C C O +. H C C ~ 180 0 C. OH C C ~ O. 180 0 C ~H2 C C ~ O +. Scheme I Hydroperoxide formation and decomposition reactions in and or with the drastic decrease of the high molecular weight region. However, the shifting and narrowing of the GPC curves of and are lower than that of. With the continuation of degradation the amount of short chains could be developed. On the basis of the results the feasible reason for the difference in the stabilities between, and is considered to be as follows: The oxidative degradation of PP has been reported to proceed by a free radical chain reactive mechanism to form a carbonyl group (C=O) via a reaction involving hydroperoxide group (R) formation 15. In the presence of ethylene unit in and, a significant variation in degradation behavior was observed between, and. There are two possible mechanisms for the slower decrease of molecular weight of or compared with that of. First, it has been frequently shown that polyethylene (PE) leads to cross-linking during degradation, and therefore an equilibrium may be established between the thermal degradation of the PP blocks and the cross-linking of the PE blocks. This equilibrium may give a reduced rate of molecular weight change. The second mechanism, shown in Scheme I, is for the formation reaction of R in and or. The formation of alkyl radical by the dissociation of tertiary C-H bond occurs first. The reaction of this alkyl radical with oxygen leads to the production of the peroxy radical which propagates the chain reaction by intramolecular tertiary C-H abstraction from as well as secondary C-H abstraction from or. The abstraction reactions produce the hydroperoxides, which are responsible for the autocatalytic nature of the oxidation. The existence of the secondary C-H in or (sec C-H bond energy: 397KJ/mol>tert C-H bond energy: 368KJ/mol) may depress the rate of the chain reaction involving hydroperoxide, leading to a drop in the degradation rate. However, the content of the ethylene unit in or is too low to completely suppress the formation reaction of hydroperoxide. As another consideration, this difference of the degradation between the and or seems to be due to the differences in the decomposition reaction of R. As shown in Scheme I, the chain scission is known to proceed by two alternative pathways, the main chain scission or dissociation of methyl group 16 as side chain scission. Main chain scission gives an end-chain ketone and alkyl radicals in the polymer chain, which leads to the reformation

1202 INDIAN J. CHEM., SEC B, JULY 2007 of R. In chain ketones and methyl radicals are formed as side chain scission from the dissociation of methyl groups. The higher mobility of methyl radicals may cause more frequent association with hydroperoxide or alkoxy radicals. This more frequent association leads to a higher rate of termination than would be expected between the less mobile alkoxy and hydroperoxide groups. In order to examine the difference in the R decomposition reaction between and or, the bond energy of the main chain was estimated by the MOPAC calculation (Cambridge Soft Corp., Chem 3D Pro Ver. 3.51). The bond energy of or was found to be slightly higher than that of (: 185 kj/mol, or : 190 kj/mol), suggesting that the dissociation of methyl group in and may be feasible, and main chain scission occurs in due to the lower bond energy. Since the degradation mechanism of and partially involves the dissociation of the methyl group, the rate of propagation of the radical chain reaction is thought to be gradually suppressed and finally terminated. Conclusion Thermo-oxidative degradation behavior of dissolved isotactic PP was examined as a function of varying ethylene and oxygen concentration effects. The observation exhibited the different degradation behavior of isotactic PP. The relative stability of polypropylenes decreases in the following order: >>. The results demonstrated that the stability of can be improved by the incorporation of varying ethylene content through changing the reaction pathway of degradation. Acknowledgement The authors are grateful to Prof. M. Terano, Department of Chemical Materials Science, Japan Advanced Institute of Science and Technology, Japan for his cooperation to measure GPC, NMR and DSC of the samples, which are used in this investigation. References 1 Vasile C & Seymour R B, Handbook of polyolefins (Marcel Dekker, New York), 1993, P479. 2 Karger-Kocsis J, Polypropylene Copolymers and Blends, (Chapman and Hall Publisher, Tokyo), 1995, Vol 2. 3 Nakatani H, Hatanaka T, Nitta K & Terano M, Res Adv In Macromolecules, 1, 2000,17. 4 Hatanaka T, Mori H & Terano M, Polym Degrad Stab, 65, 1999, 271. 5 Hatanaka T, Mori H & Terano M, Polym Degrad Stab, 64, 1999, 271. 6 Mori H, Hatanaka T & Terano M, Macromol Rapid Commun, 18, 1997, 157. 7 Kato M, Tsuruta A, Kuroda S & Osawa Z, Polym Degrad Stab, 67, 2000, 1. 8 Kato M & Osawa Z, Polym Degrad Stab, 65, 1999,457. 9 Osawa Z, Kato M & Terano M, Macromol Rapid Commun, 18, 1997, 667. 10 Vink P, In: G. Scott Ed., Developments in Polymer Stabilization-6, (Applied Science Publishers Ltd, London) 1980, P117. 11 Alam M S, Ichiki T, Liu B, Nakatani H & Terano M, Recent Research Developments in Polym Sci, 6, 2002, 19. 12 Alam M S, Ichiki T, Liu B, Nakatani H & Terano M, Future Technologies for Polyolefin and Olefin Polymerization Catalysis (Kodansha Publisher, Tokyo), 2002, P21. 13 Alam M S, Ph.D Thesis, Submitted in Japan Advanced Institute of Science and Technology, Japan, March 2002. 14 Chiantore O & Guaita M, J Appl Polym Sci: Appl Polym Symp, 52, 1993, 1. 15 Alam M S, Nakatani H, Ichiki T, Goss G S, Liu B & Terano M, J Appl Polym Sci, 86, 2002, 1863. 16 Carlsson D J & Wiles D M, Macromolecules, 2(6), 1969, 597.