Effect of Polymerization Conditions on Thermal and Mechanical Properties of Ethylene/1-Butene Copolymer Made with Ziegler-Natta Catalysts

Abstract

The effect of polymerization conditions on thermal and mechanical properties of ethylene/1-butene copolymers synthesized through titanium-magnesium-supported Ziegler-Natta catalysts was studied. The increase in hydrogen pressure leads to a decrease in molecular weight (MW), storage modulus, and melting temperature. However, it yields an increase in molecular weight distribution (MWD), tan...δ , % crystallinity, tensile modulus, yield stress, and strain at break. The effects of ethylene pressure and polymerization temperature on the copolymer MW, MWD and thermal and mechanical properties have been investigated. However, the impacts of ethylene pressure and polymerization temperature on copolymer modulus, tensile strength, % crystallinity, crystallization peak temperature, yield stress, strain at break, and yield strain are marginal. The hydrogen pressure plays a major role in controlling the copolymer properties because it acts as an efficient chain transfer agent during polymerization reaction. The MW is the key parameter that influences flow activation energy. However, the other mechanical, dynamic mechanical, and thermal properties not only depend on MW but are also influenced by other parameters.

(ProQuest: ... denotes non-US-ASCII text omitted.)

Mostafizur Rahaman 1 and M. Anwar Parvez 1 and J. B. P. Soares 2 and I. A. Hussein 1

Academic Editor:Giridhar Madras

1, Department of Chemical Engineering, King Fahd University of Petroleum and Minerals, Dhahran 31261, Saudi Arabia
2, Department of Chemical and Materials Engineering, University of Alberta, Edmonton, AB, T6G 2V4, Canada

Received 20 February 2014; Accepted 22 May 2014; 11 June 2014

This is an open access article distributed under the Creative Commons Attribution License, which permits unrestricted use, distribution, and reproduction in any medium, provided the original work is properly cited.

1. Introduction

The synthesis of ethylene-butene copolymers has been an attractive subject to many authors because of their interesting properties like low density, high degree of branching, and low cost price per unit volume compared to ethylene-propylene copolymer [1-3]. One of the great advantages of these copolymers is that they can also be reused without decreasing their processing and physical properties. Quan et al. have synthesized ethylene-butene copolymer through gas phase polymerization technique, where highly active catalysts like TiCl₄ , SiO₂ or ZnCl₂ /alcohol/AlR₃ , and Ti(OBu)₄ /MgCl₂ are used [4]. They have reported that the synthetic products have the properties of both oligomer and copolymer, and the melting temperature, crystallinity, and crystallite size decrease with the increase in butene content in the copolymer. The effect of polymerization conditions, like hydrogen and comonomer concentration, and polymerization time on the properties of ethylene-butene copolymer synthesized in two-step process has been reported elsewhere [1]. The influence of reaction time on ethylene/1-butene copolymer synthesized over supported titanium-magnesium catalyst has also been studied [5, 6]. It has been shown that the increase in reaction time from 5 to 40 min results in small increase in molecular weight (MW), narrowing of molecular weight distribution (MWD), and decrease in 1-butene content in the copolymer.

Earlier, the synthesis of homo- and copolymer of ethylene using Zeigler-Natta and other different catalysts has been carried out where discussions have been made on various aspects of polymerization processes like the effect of catalyst type on copolymer properties, relationship of catalyst composition with molecular structure of homo- and copolymers, and so forth [7-10]. The advantages of using Zeigler-Natta catalysts are that they produce polymer products with high melting point, high MW, and controllable morphology. However, there are some disadvantages associated with Ziegler-Natta catalysts. These catalysts have less control over the growing polymer chain branching because there is the presence of multiple metal sites on transition metal, and also the removal of catalyst from the final product is very difficult [11]. Recently, we have systematically discussed the effect of different polymerization conditions on dynamic mechanical, thermal, and mechanical properties of polyethylene homopolymers made with Ziegler-Natta catalysts [12]. Moreover, some correlations of homopolymers MW with different solid state properties were also made in the same literature [12].

In the present section, we have extended our previous work, where ethylene/1-butene copolymers have been synthesized over the same titanium-magnesium catalyst in laboratory-scale reactor and investigated the effect of different polymerization conditions on copolymers MW, MWD, thermal, and mechanical properties. Similarly, some correlations of copolymers MW with their solid state properties like dynamic mechanical, thermal, and tensile properties have been established and the fittings have been logically discussed.

2. Materials, Methods, and Experimental Techniques

2.1. Materials

Ultrahigh purity nitrogen (99.999%) and polymer grade ethylene (99.9%) were supplied by Praxair, Canada. All the operations were performed under nitrogen using standard Schlenk techniques or inside the glove box. Ethylene and nitrogen were purified by passing through columns. These columns are packed with R3-11 copper catalyst, activated alumina, and 3A/4A mixed molecular sieves. The materials such as titanium (IV) chloride (TiCl₄ , 99%) and magnesium chloride (MgCl₂ , power-325 mesh) were procured from Aldrich (Canada) and 2-ethyl-1-hexanol (99%) was purchased from Alfa Aesar, Germany. These materials were used for catalyst synthesis without further purification. Triethyl aluminum (TEA, 1 M in hexane) was used as an activator and purchased from Aldrich, Canada. The reaction diluent, hexane (HPLC grade, 95% n-hexane), was purchased from J. T. Baker, USA. This was used for the synthesis of catalyst and copolymer. It was purified by passing through columns packed with activated alumina and molecular sieves (Zeolum Type F-9, Tosoh Co., Japan). The purified solvent was stored in Schlenk flasks (Sigma-Aldrich, Canada) with 3A/4A mixed molecular sieves.

2.2. Synthesis of Magnesium-Supported Ziegler-Natta Catalyst

The solvent, hexane (200 mL), was taken to a 500 mL round bottled flask. Magnesium chloride (7.62 g, 0.08 mol) and 2-ethyl-1-hexanol (37.5 mL, 0.24 mol) were added to it. A clear solution of the mixture was obtained after stirring and refluxing for 24 hours. Titanium (IV) chloride (0.5 mol) was slowly added dropwise to it at a stirring rate of 700 rpm and at a temperature of 30°C. The mixture was kept for 2 hours to complete the reaction. The obtained precipitate was filtered and washed three times with hexane followed by drying under nitrogen flow. Finally, at the end of reaction, a dried white powder was isolated. Scheme 1 represents the synthetic route for the synthesis of the catalyst.

Scheme 1: Synthesis of the magnesium-supported Ziegler-Natta catalyst.

[figure omitted; refer to PDF]

2.3. Synthesis of Ethylene/1-Butene Copolymers

The synthesis of ethylene/1-butene copolymers is conducted under various reaction conditions using magnesium-supported Ziegler-Natta catalyst. A semibatch autoclave reactor (300 mL) was used for the polymerization reactions. This reactor was composed of a mass flow meter and a temperature control unit. The temperature was controlled with a cooling coil and an electric heater. The tolerance of polymerization temperature was ± ^0.2° C of the set point. The reactor was purged five times with nitrogen before each reaction followed by heating up to 140°C under vacuum. The reactor was purged again to the set point temperature under nitrogen flow. Solvent (200 mL) and triethyl aluminum activator (2.0 mmol) were taken in to the reactor followed by stirring for 5 minutes. Catalyst slurry (3.0 mg) mixed with hexane was injected into the reactor and was stirred for 10 minutes. In this typical polymerization process, as, for example, the first run for sample 1, ethylene was continuously flowed to meet the ethylene pressure of 5 bar inside the reactor under a stirring rate of 500 rpm. Prior to ethylene, 1-butene (71.3 mmol) was fed into the reactor. Hydrogen gas was passed to the reactor until the pressure reached 1 bar. The polymerization/reaction temperature was adjusted to 60°C and the polymerization was carried out for 30 mins. Ethylene flow to the reactor was stopped at the end of the polymerization time and the reactor was rapidly vented for reducing pressure and removing reactant. The set temperature was reduced to room temperature. The copolymer so obtained was precipitated in 200 mL ethanol followed by filtering and finally drying under vacuum. The detailed reaction condition and composition for all the copolymer samples are given in Table 1.

Table 1: Ethylene/1-butene copolymerization data (polymerization time: 30 min).

s/number	P C 2 H 4 (bar)	1-Butene fraction (mmol)	Poly. temp. (°C)	P H 2 (bar)	MW (g/mol)	Mn (g/mol)	PDI (MWD)
1	5	71.3	60	1	162534	55472	2.93
2	5	71.3	60	2	149653	45765	3.27
3	5	71.3	60	3	123342	31871	3.87
4	5	71.3	80	1	132669	42117	3.15
5	5	71.3	80	2	119172	34442	3.46
6	5	71.3	80	3	107637	26775	4.02
7	5	142.6	60	1	144653	42978	3.53
8	5	142.6	60	2	130350	33337	3.91
9	5	142.6	60	3	121622	26967	4.51
10	5	142.6	80	1	129823	34163	3.80
11	5	142.6	80	2	101153	23800	4.25
12	5	142.6	80	3	91842	19335	4.75
13	10	71.3	60	1	176583	61254	2.88
14	10	71.3	60	2	159136	51734	3.08
15	10	71.3	60	3	131776	36043	3.66
16	10	71.3	80	1	141970	46828	3.03
17	10	71.3	80	2	123435	37772	3.27
18	10	71.3	80	3	112062	29464	3.80
19	10	142.6	60	1	156754	45182	3.47
20	10	142.6	60	2	142238	36729	3.87
21	10	142.6	60	3	126835	29251	4.34
22	10	142.6	80	1	135454	37635	3.60
23	10	142.6	80	2	116068	28714	4.04
24	10	142.6	80	3	96752	21543	4.49

2.4. Gel Permeation Chromatography (GPC)

Gel permeation chromatography (GPC-IR, Polymer Char, Spain) was used to measure molecular weight and molecular weight distribution of copolymers. The samples were dissolved in 1,2,4-trichlorobenzene at 160°C followed by passing through three linear Polymer Laboratories columns. These columns were calibrated with polystyrene standards and operated at a flow rate of 1 mL/min. The detailed procedure of GPC characterizations has been mentioned elsewhere [13].

2.5. Differential Scanning Calorimetry (DSC)

Differential scanning calorimetry (DSC, TA Instruments DSC Q1000 series, USA) was used to determine the melting temperature of the polymers. DSC test was carried out in nitrogen environment at a heating rate of 10°C/min, where two scans were performed. The thermal properties of polymer depend on the previous history. Therefore, it is a common practice in thermal analysis to heat the samples to remove the previous history and then perform the characterization under the same controlled history. The second scan was used to characterize the polymer samples.

2.6. Dynamic Mechanical Analysis (DMA)

DMA (TA instrument, Q800 series, USA) tests of the polymeric samples were performed in single cantilever (8 mm length fixture) mode. The sample specimens with a dimension of 8 mm in length and 10.1 mm in width and thickness between 0.65 and 0.75 mm were prepared using the fixed size mold in a carver press. The temperature step sweep was varied from 40 to 80°C with a step of 10°C per each frequency sweep. For frequency sweep, the range of frequency was 0.1-100 Hz at the strain 15 micron. Temperature and frequency sweep test was run in strain controlled mode. Time-temperature-superposition (TTS) mode was used to analyze the experimental data for getting flow activation energy.

2.7. Mechanical Testing

The mechanical testing of polymeric samples was carried out at room temperature using Instron (model 5567, USA) tensile testing machine at a crosshead speed of 50 mm/min, where gauge length was kept at 25 mm. The samples were prepared according to ASTM D638 (Type V) using a dog-bone mold in carver press.

3. Results and Discussion

3.1. Effect of Polymerization Conditions on MW and MWD of Ethylene/1-Butene Copolymers

The variation of different polymerization conditions on MW and MWD of ethylene/1-butene copolymers has been shown in Table 1. The effect of hydrogen pressure on MW and MWD has been investigated at 1, 2, and 3 bar pressure. It is seen from the table that, with the increase in hydrogen pressure, there is a decrease in copolymer MW and broadening of MWD. This decrease in copolymer MW and broadening of MWD can be explained by considering the role of hydrogen pressure on the polymerization reaction. Actually, the hydrogen present in the polymerization reaction acts as a chain transfer agent for the reaction [1, 14]. Thus the increase in hydrogen pressure results in the termination of polymerization reaction. This leads to the lowering of copolymer MW and broadening of MWD. Moballegh and Hakim have reported that an increase in hydrogen concentration by 0.26 mol raised the MWD from 8 to about 22.8 with considerable decrease in copolymer MW [1]. This observation is consistent with our results mentioned herein. This decrease in MW and broadening of MWD with respect to hydrogen pressure are observed at both ethylene pressure values (5 and 10 bar) and both polymerization temperatures (60 and 80°C).

The variation of MW and MWD with respect to ethylene pressure (5 and 10 bar) has been shown in Table 1. The increase in ethylene pressure increases the copolymer MW and narrows the MWD. MW is found to increase from 119172 g/mol to 123435 g/mol (sample sets numbers 5 and 17) when ethylene pressure was increased from 5 to 10 bar while other polymerization conditions were kept the same. This change represents an increase of 3.45% in MW and reduction in MWD from 3.46 to 3.27 (5.8% reduction in MWD). This decrement/increment level of percentage for MW and MWD varies with the sample sets. The ethylene present in the polymerization reaction acts as an activator for the catalyst in the reaction [14]. At high ethylene pressure, the role of ethylene as an activator is increased which results in copolymer with high MW and narrow MWD.

Table 1 shows that MW and MWD of copolymer are also affected by polymerization temperature. An increase in polymerization temperature from 60 to 80°C results in the lowering of MW and broadening of MWD, which can be attributed to the strong chain transfer reaction during copolymerization. The effect of comonomer concentration (1-butene) on MW and MWD has been reported at two different concentrations in the table. It is seen that the increase in comonomer concentration from 71.3 to 142.6 mmol/L results in a decrease in MW and broadening of MWD due to the chain transfer reaction mechanism [1]. In fact, the increase in comonomer concentration leads to a decrease in the catalyst activity as reported in the literature [15-17].

3.2. Dynamic Mechanical Analysis (DMA)

The effects of frequency and temperature on dynamic mechanical properties like storage modulus, G [variant prime], and tan...δ (damping factor) have been presented for the copolymer sample 2 (polymerized at ethylene pressure = 5 bar; hydrogen pressure = 2 bar; polymerization temperature = 60°C; and polymerization time = 30 min). The frequency has been varied from 0.1 to 100 Hz where the temperatures are 50°C, 60°C, 70°C, and 80°C. The variation of G [variant prime] versus frequency measured at different temperatures is presented in Figure 1. There is almost a linear increase in G [variant prime] with the increase in frequency. On the contrary, G [variant prime] is found to decrease with the increase in temperature steps. This is due to softening of copolymer at high temperature, which leads to lowering of storage energy and thus G [variant prime]. Figure 2 shows the effect of frequency on tan...δ at different temperatures. It is observed that tan...δ value decreases with the increase in frequency but increases with the increase in temperature. This increment in tan...δ with the increase in temperature is due to loss in storage energy at higher temperature.

Figure 1: Dynamic temperature step/frequency sweep for copolymer sample 2 synthesized at _PC2H4 =5 bar, _PH2 =2 bar, _{Tpolymerization} temperature = 60°C, and _{tpolymerization} time = 30 min.

[figure omitted; refer to PDF]

Figure 2: Dynamic temperature step/frequency sweep (tan...δ ) for copolymer sample 2 synthesized at _PC2H4 =5 bar, _PH2 =2 bar, _{Tpolymerization} temperature = 60°C, and _{tpolymerization} time = 30 min.

[figure omitted; refer to PDF]

The effect of frequency on G [variant prime] at different hydrogen pressure, namely, 1, 2, and 3 bar, for the samples 1, 2, and 3 has been presented in Figure 3. The copolymerization conditions for these samples are the same (ethylene pressure = 5 bar; polymerization temperature = 60°C; and polymerization time = 30 min). The increase in hydrogen pressure results in reduction of G [variant prime] as is observed from the figure. Actually, the hydrogen present in the reaction system acts as an efficient chain transfer agent for the reaction as has been mentioned earlier. This leads to copolymer with short chain length having lower MW. In fact, the degree of chain entanglements in polymer decreases with the decrease in MW and consequently results in lower value of G [variant prime]. Figure 4 shows tan...δ against frequency plots at different hydrogen pressure for the same set of samples. It is observed from this figure that the increase in hydrogen pressure leads to increase in tan...δ value at any particular frequency. In fact, the polymer with lower MW (short chain length) will have higher molecular movement compared to high MW polymer of the same category. This is because the polymer with low MW will have low surface area per unit chain length, which results in low physical attraction between the molecules [18]. Thus the increase in molecular movement in copolymer results in higher value of tan...δ , as tan...δ is a measure of structural transformation (molecular movement) in polymer. The higher the value of tan...δ is, the higher the structural transformation in polymer will be. This is the reason for low molecular weight polymer (short chain length polymer) having higher value of tan...δ compared to long chain length polymer. The effects of ethylene pressure and polymerization temperature on both G[variant prime] and tan...δ of the polymer are almost similar (not shown in picture). The differences exist only in their magnitude. The variations of G [variant prime] and tan...δ with respect to frequency/temperature sweep, ethylene and hydrogen pressure, and polymerization temperature have been investigated for all samples but are not reported in this paper because the trend in variations is similar for all the samples. The correlation of G [variant prime] and tan...δ with MW of polymers has been established and the linear fit of the plots is shown in Figures 5(a) and 5(b). The increase in MW leads to increase in G [variant prime] which results in a reduction in tan...δ values. The coefficients of correlation (R² ) of the linear fit for G [variant prime] and tan...δ are 0.964 and 0.955, respectively. Both R² are almost close to unity, indicating good linear correlation of G [variant prime] and tan...δ with MW.

Figure 3: Storage modulus of copolymers synthesized at _PC2H4 =5 bar, _{Tpolymerization} = 60°C, and _{tpolymerization} = 30 min (samples 1, 2, and 3).

[figure omitted; refer to PDF]

Figure 4: tan ... δ of copolymers synthesized at _PC2H4 =5 bar, _{Tpolymerization} = 60°C, and _{tpolymerization} = 30 min (samples 1, 2, and 3).

[figure omitted; refer to PDF]

Figure 5: Correlation plots of MW with G [variant prime] (a), tan...δ (b), and ΔE (c).

[figure omitted; refer to PDF]

The time temperature superposition (TTS) technique has been applied to get the activation energy (ΔE ) for all the samples in solid state extracted from the DMA data. The results of activation energy have been presented in Table 2. The activation energy for all samples falls in the range of 183.9-265.8 kJ/mol. It is seen that the sample with higher MW exhibits higher ΔE . The data of ΔE are plotted against MW and are shown in Figure 5(c), which reveals a linear relationship of ΔE with MW. The value of R² (0.992) is very close to unity, indicating that MW is the single parameter which influences ΔE .

Table 2: Activation energy for copolymer samples (polymerization time: 30 min).

s/number	P C 2 H 4 (bar)	1-Butene fraction (mmol)	Poly. temp. (°C)	P H 2 (bar)	Activation energy (kJ/mol)	MW (g/mol)
1	5	71.3	60	1	253.9	162534
2	5	71.3	60	2	243.7	149653
3	5	71.3	60	3	214.4	123342
4	5	71.3	80	1	225.1	132669
5	5	71.3	80	2	213.9	119172
6	5	71.3	80	3	198.4	107637
7	5	142.6	60	1	235.4	144653
8	5	142.6	60	2	223.4	130350
9	5	142.6	60	3	214.1	121622
10	5	142.6	80	1	220.5	129823
11	5	142.6	80	2	194.1	101153
12	5	142.6	80	3	183.9	91842
13	10	71.3	60	1	265.8	176583
14	10	71.3	60	2	248.6	159136
15	10	71.3	60	3	218.3	131776
16	10	71.3	80	1	232.6	141970
17	10	71.3	80	2	214.8	123435
18	10	71.3	80	3	204.7	112062
19	10	142.6	60	1	243.6	156754
20	10	142.6	60	2	233.4	142238
21	10	142.6	60	3	217.4	126835
22	10	142.6	80	1	227.8	135454
23	10	142.6	80	2	206.1	116068
24	10	142.6	80	3	188.6	96752

3.3. Differential Scanning Calorimeter (DSC)

The thermal properties of copolymer, that is, the crystallization temperature (Tc), melting temperature (Tm), and % crystallinity (%Xc), have been extracted from DSC and are shown in Table 3. The results show that Tc of copolymer remains in the range of 114.69-117.89°C. This implies that the effects of polymerization parameters, covered in this study, on Tc are marginal.

Table 3: DSC analysis for copolymer samples (polymerization time 30 min).

s/number	P C 2 H 4 (bar)	1-Butene fraction (mmol)	Poly. temp. (°C)	P H 2 (bar)	T c (°C)	T m (°C)	% cryst. (cooling)
1	5	71.3	60	1	117.89	130.12	46.32
2	5	71.3	60	2	116.86	128.76	49.54
3	5	71.3	60	3	115.52	125.92	53.86
4	5	71.3	80	1	116.91	128.36	48.13
5	5	71.3	80	2	115.42	127.37	52.03
6	5	71.3	80	3	114.37	124.73	56.57
7	5	142.6	60	1	116.83	129.54	48.60
8	5	142.6	60	2	115.52	127.31	52.44
9	5	142.6	60	3	114.63	124.82	55.58
10	5	142.6	80	1	115.34	127.43	50.83
11	5	142.6	80	2	114.45	125.86	53.61
12	5	142.6	80	3	113.92	123.99	56.63
13	10	71.3	60	1	119.55	133.14	51.75
14	10	71.3	60	2	118.56	131.81	54.86
15	10	71.3	60	3	117.94	129.77	57.08
16	10	71.3	80	1	118.34	131.99	53.19
17	10	71.3	80	2	116.57	129.68	56.83
18	10	71.3	80	3	115.29	128.40	59.12
19	10	142.6	60	1	118.67	130.83	53.21
20	10	142.6	60	2	116.79	128.90	56.50
21	10	142.6	60	3	115.80	126.09	61.63
22	10	142.6	80	1	116.77	128.93	55.66
23	10	142.6	80	2	115.12	127.09	59.10
24	10	142.6	80	3	114.69	125.91	63.62

The effect of hydrogen pressure can be correlated with copolymer melting point as can be seen from the table. It is observed that Tm decreases with the increase in hydrogen pressure. However, this decrement in melting point is less significant. This decrement in melting point with the increase in hydrogen pressure can be explained by considering the role of hydrogen as chain transfer agent during reaction which already has been mentioned earlier. This role of hydrogen leads to lower MW copolymer that means lower surface area of copolymer. Thus, there will be less physical attraction between low MW polymers chains for which less energy is required to overcome this force of attraction [18]. This is why, with the increase in hydrogen pressure, the melting point of the copolymer decreases. The ethylene pressure has less impact on melting point of copolymer. It is seen from the table that Tm at 5 bar of ethylene pressure is in the range of 123.99-130.12°C, whereas at 10 bar of ethylene pressure is in the range of 125.91-133.14°C. Thus a little bit positive shift of temperature is observed when ethylene pressure is increased. This positive shift may be due to narrow MWD of polymers synthesized at high ethylene pressure. Similarly, the effect of polymerization temperature on copolymer melting point is less significant as is observed from the table.

The effect of polymerization parameters on copolymer crystallinity has been reported in the same table as is observed in the last column. It is revealed from this table that the copolymer crystallinity increases with the increase in hydrogen pressure. As the coordination polymerization method is processed through successive polymerization and crystallization [19], the increase in hydrogen pressure blocks the active sites of polymerization resulting in decrease in polymerization rate; as a consequence, the crystallization rate is increased. This is why the increase in hydrogen pressure leads to increase in crystallinity [20]. An almost similar observation has been made for ethylene pressure; that is, the increment in copolymer crystallinity is less significant with the increase in ethylene pressure from 5 to 10 bar as is observed from the table. However, the increment in crystallinity varies according to the condition of polymerization. Shin et al. have also reported similar results that the increase in ethylene pressure leads to marginal increase in crystallinity [21]. The variation of copolymer crystallinity with the increase in polymerization temperature is also marginal as is observed from the table.

The influence of MW on polymer Tm, Tc, and %Xc has been investigated and the related plots are presented in Figures 6(a)-6(c). It is observed from the figure that, for all the three cases, though the data points are scattered randomly, there are the overall improvement in Tm (Figure 6(a)) and Tc (Figure 6(b)) and reduction in %Xc (Figure 6(c)) with the increase in MW. The R² of the linear fits for Tm, Tc, and %Xc are 0.39, 0.49, and 0.65, respectively, far away from the unity. Thus it can be said that the polymers Tm, Tc, and %Xc are not only influenced by MW but also dependent on other parameters.

Figure 6: Correlation plots of MW with Tm (a), Tc (b), and %Xc (c).

[figure omitted; refer to PDF]

3.4. Mechanical Properties

The results of mechanical properties of copolymers like tensile modulus (TM), tensile strength (TS), and % strain at break (SB) are affected by the polymerization parameters. Table 4 shows the mechanical testing results of copolymer for all the samples. It is seen that the increase in hydrogen pressure results in the increase in tensile modulus. This type of result is obtained when polymerization is carried out at both 5 and 10 bar ethylene pressure. When polymerization is performed at 5 bar ethylene pressure, the modulus is in the range of 419 ± 18-499 ± 20 MPa at 1 bar hydrogen pressure, 514 ± 21-565 ± 27 MPa at 2 bar hydrogen pressure, and 591 ± 28-648 ± 33 MPa at 3 bar hydrogen pressure. Almost similar results are obtained when polymerization condition is maintained at 10 bar ethylene pressure, where the tensile modulus is in the range of 458 ± 16-512 ± 29 MPa at 1 bar hydrogen pressure, 535 ± 23-589 ± 36 MPa at 2 bar hydrogen pressure, and 634 ± 29-712 ± 39 MPa at 3 bar hydrogen pressure. Thus a careful look at the results reveals that the tensile modulus value at 10 bar ethylene pressure is higher compared to tensile modulus value at 5 bar ethylene pressure. Actually, the tensile modulus is related to copolymer crystallinity as shown in Table 3. It is seen that the copolymer with higher crystallinity is having higher modulus.

Table 4: Mechanical properties of ethylene/1-butene copolymer (polymerization time: 30 min).

s/number	P C 2 H 4 (bar)	1-Butene fraction (mmol/L)	Poly. temp. (°C)	P H 2 (bar)	Modulus (MPa)	Yield stress (MPa)	Yield strain (%)	Strain at break (%)	TS (MPa)
1	5	71.3	60	1	419 ± 18	13.63 ± 1.13	3	669 ± 23	48.65 ± 4.48
2	5	71.3	60	2	514 ± 21	15.12 ± 1.25	3	756 ± 27	45.55 ± 3.56
3	5	71.3	60	3	591 ± 28	17.08 ± 1.32	3	817 ± 35	41.42 ± 3.24
4	5	71.3	80	1	445 ± 15	14.12 ± 1.21	4	686 ± 32	47.91 ± 4.25
5	5	71.3	80	2	544 ± 20	15.22 ± 1.27	3	790 ± 28	43.89 ± 3.96
6	5	71.3	80	3	615 ± 31	17.29 ± 1.31	3	845 ± 39	39.89 ± 3.47
7	5	142.6	60	1	437 ± 17	14.05 ± 1.12	4	678 ± 25	47.32 ± 4.14
8	5	142.6	60	2	536 ± 22	15.58 ± 1.18	4	771 ± 29	43.45 ± 3.82
9	5	142.6	60	3	620 ± 29	17.21 ± 1.24	4	823 ± 33	40.24 ± 3.32
10	5	142.6	80	1	499 ± 20	14.18 ± 1.14	4	698 ± 34	46.55 ± 4.06
11	5	142.6	80	2	565 ± 27	15.75 ± 1.19	4	785 ± 37	42.61 ± 3.75
12	5	142.6	80	3	648 ± 33	17.51 ± 1.25	3	842 ± 42	38.64 ± 3.26
13	10	71.3	60	1	458 ± 16	13.81 ± 1.11	3	687 ± 26	51.94 ± 4.57
14	10	71.3	60	2	535 ± 23	15.34 ± 1.22	3	784 ± 35	46.65 ± 4.12
15	10	71.3	60	3	634 ± 29	17.23 ± 1.29	3	843 ± 39	42.67 ± 3.35
16	10	71.3	80	1	472 ± 19	14.62 ± 1.13	3	702 ± 33	49.43 ± 4.36
17	10	71.3	80	2	575 ± 25	15.58 ± 1.20	3	798 ± 37	44.68 ± 3.94
18	10	71.3	80	3	682 ± 34	17.47 ± 1.26	3	856 ± 41	41.53 ± 3.28
19	10	142.6	60	1	481 ± 23	14.27 ± 1.15	3	698 ± 29	49.84 ± 4.19
20	10	142.6	60	2	554 ± 27	15.74 ± 1.23	4	812 ± 36	44.66 ± 3.86
21	10	142.6	60	3	665 ± 34	17.67 ± 1.31	3	876 ± 43	41.83 ± 3.42
22	10	142.6	80	1	512 ± 29	14.63 ± 1.17	3	718 ± 25	47.45 ± 4.14
23	10	142.6	80	2	589 ± 36	16.42 ± 1.28	3	828 ± 37	43.36 ± 3.68
24	10	142.6	80	3	712 ± 39	18.19 ± 1.33	3	896 ± 42	40.35 ± 3.16

The results of % strain at break reported in the table show an increment in % strain at break with the increase in hydrogen pressure. The % strain at break at 1 bar hydrogen pressure is in the range of 669 ± 23- 698 ± 34, at 2 bar hydrogen pressure is in the range 756 ± 27- 785 ± 37, and at 3 bar hydrogen pressure is in the range of 817 ± 35- 842 ± 42, when polymerization is conditioned at 5 bar ethylene pressure. Similarly, when polymerization is conditioned at 10 bar ethylene pressure, the range of % strain at break at 1 bar hydrogen pressure is 687 ± 26- 718 ± 25, at 2 bar hydrogen pressure is 784 ± 35- 828 ± 37, and at 3 bar hydrogen pressure is 843 ± 39- 896 ± 42. Thus the % strain at break is somewhat high for the copolymer synthesis at higher ethylene pressure. It is observed from the table that the yield strain remains in between 3 and 4%. A careful look at Tables 4 and 3 reveals that the copolymer with low MW is having higher % strain at break.

Some variation of yield stress (YS) with the increase in hydrogen pressure is observed from the results shown in the same table. When polymerization is conditioned at 5 bar ethylene pressure, the yield stress ranges at 1 bar, 2 bar, and 3 bar hydrogen pressure are 13.63 ± 1.13-14.18 ± 1.14 MPa, 15.12 ± 1.25- 15.75 ± 1.19 MPa, and 17.08 ± 1.32- 17.51 ± 1.25 MPa, respectively. This shows an increment in yield stress with the increase in hydrogen pressure. A similar type of increment is observed when polymerization is conditioned at 10 bar ethylene pressure; that is, the yield stress ranges are 13.81 ± 1.11- 14.63 ± 1.17 MPa, 15.34 ± 1.22- 16.42 ± 1.28 MPa, and 17.23 ± 1.29- 18.19 ± 1.33 MPa at 1 bar, 2 bar, and 3 bar hydrogen pressure, respectively. So, from these results it comes true that the effect of ethylene pressure on yield stress is less significant compared to the effect of hydrogen pressure. It is also evident from the table that the polymerization temperature has low impact on yield stress. The tensile strength of copolymer improves with the increase in ethylene pressure but decreases with the increase in hydrogen pressure and polymerization temperature as is observed from the table.

The data of tensile modulus (TM), tensile strength (TS), % strain at break (SB), and yield stress (YS) are plotted against MW and are shown in Figures 7(a)-7(d), respectively. An effort to make linear fits of randomly scattered data points has been made for all four cases. There is overall decrement in TM, SB, and YS with the increase in MW. The improvement happened only for TS. The R² of linear fits for TM (Figure 7(a)), TS (Figure 7(b)), SB (Figure 7(c)), and YS (Figure 7(d)) are 0.68, 0.72, 0.61, and 0.60, respectively. These R² values are not close to unity, indicating that these mechanical properties not only depend on MW but are also influenced by other parameters. Actually, rather than MW, these mechanical properties also depend on several parameters like polymer crystallinity, backbone chain length, branch (side) chain length, chain entanglement, branch chain content, and so forth [4, 12, 22-25]. Thus the establishment of perfect correlation of MW with these mechanical properties is really difficult.

Figure 7: Correlation plots of MW with TM (a), TS (b), SB (c), and YS (d).

[figure omitted; refer to PDF]

4. Conclusions

The increase in both hydrogen pressure and polymerization temperature leads to decrease in copolymer MW and broadening of MWD. But the ethylene pressure plays the opposite role. DMA results show an increase in storage modulus but decrease in tan...δ value with the increase in frequency. On the contrary, the storage modulus value decreases but tan...δ value increases with the increase in temperature. An increase in hydrogen pressure results in reduction of copolymer storage modulus and melting point but increase in crystallinity, tensile modulus, % strain at break, and yield stress. It is seen that the copolymer with higher MW exhibits higher activation energy. It is revealed that the copolymer with higher crystallinity is having higher tensile modulus. However, the impacts of other polymerization parameters like ethylene pressure and polymerization temperature on copolymer modulus, tensile strength, crystallinity, Tc, yield stress, % strain at break, and yield strain are marginal. The major role of hydrogen in controlling the copolymer properties is due to its acting as an efficient chain transfer agent during polymerization reaction. The correlation of MW with the thermal and mechanical properties of the polymer is given in this paper. The MW is the key parameter that influences ΔE , whereas the other dynamic mechanical (G [variant prime] and tan...δ ), thermal (Tm, Tc, and %Xc), and mechanical (TM, TS, SB, and YS) properties not only depend on MW but are also influenced by different parameters as mentioned earlier. However, almost good linear correlation of MW with G [variant prime] and tan...δ is observed.

Acknowledgments

The authors acknowledge the financial support provided by King Abdul Aziz City for Science and Technology for this research project under research Grant no. AT-27-67. The authors also acknowledge the facilities and support provided by KFUPM.

Conflict of Interests

The authors declare that there is no conflict of interests regarding the publication of this paper.

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