JPH0154368B2 - - Google Patents

Description

[Detailed description of the invention]

The present invention relates to polypropylene compositions. Both crystalline and amorphous polypropylene are well known. Crystalline polypropylene is generally considered to consist of at least primarily an isotactic or syndiotactic structure;
Amorphous polypropylene is then generally considered to consist of at least primarily an atactic structure. U.S. Pat. Nos. 3,112,300 and 3,112,301 to Natsuta et al. describe isotactic polypropylene and primarily isotactic polypropylene, respectively. Structural formulas for isotactic and syndiotactic polypropylenes are listed in Listner U.S. Pat. No. 3,511,824.
given to the number. "Atactic" polypropylene is defined as polypropylene in which substituted methyl groups are arranged randomly above and below the backbone of the atoms, where the backbones of the atoms all lie in the same plane. Most commercial grades of polypropylene are highly crystalline and are commonly used in the production of plastic products. Amorphous polypropylene is also commercially available and is generally a gummy material of low strength. Amorphous polypropylene is usually present as a small fraction in primarily isotactic polypropylene,
and can be easily extracted. They are commonly used for adhesive applications. Rubbery polypropylenes are also known. Such products have been said to be produced directly by conventional polymerization using specific catalysts, repeated extraction of conventional polypropylene, chemical treatment of crystalline polypropylene, and a series of polymerization steps. A typical rubber-like polypropylene is Schrage
No. 3,329,741 to Natsuta et al., U.S. Pat. However, such polypropylene has not found significant use in products requiring elastomeric polymers. There is therefore a need for polypropylene with practical elastic properties that can be produced as a direct reaction product by a practical process. The present invention has a main melting point between 135 and 155 °C, and 1.5
Has an intrinsic viscosity of ~9, exhibits no yield point, 150%
and an intrinsic viscosity of greater than 1.50 and an isotactic crystalline content of from about 0.5 to about 5% by weight.
a diethyl ether soluble fraction containing about 10-80% by weight, and a film formed from the fraction at about 25°C when viewed under a crossed Nicol prism in a polarizing microscope or crossed polarizing at 25°C. A polypropylene plastic consisting essentially of a blend of about 5 to 95 parts by weight of a separable elastic polypropylene characterized by exhibiting birefringence when stretched between sheets) and about 95 to 5 parts by weight of a highly isotactic polypropylene. provide something. The present invention provides that the "whole polymer", ie the direct reaction product without separation of any polypropylene component, is itself elastic and exhibits properties similar to vulcanized rubber. Contains elastic separable products. The production of the above-mentioned total polymer (elastic polypropylene) involves changing the reaction conditions or the proportion of monomers,
This is achieved without sequential polymerization, which is altered during the polymerization period to produce alternating "blocks" in the polymer structure. "Fractionable" means that the product is heterogeneous and therefore consists essentially of two or more fractions that are easily separable by extraction with solvents such as diethyl ether and hexane. means. Therefore, the total polymer is essentially about 10 to 80
% by weight (preferably 40-75%) of the diethyl ether soluble fraction and various proportions of other fractions, typically about 10-35% by weight soluble in boiling hexane but insoluble in boiling diethyl ether. % fraction and about 10-55% fraction insoluble in boiling hexane. The "diethyl ether soluble fraction" or "ether soluble fraction" as used herein with respect to polypropylene is determined in boiling diethyl ether by the method described below under Analytical Methods. The elasticity measure used to describe the elastic polypropylene component of the present invention is that compression molded specimens are
It is defined as the elongation remaining in a compression molded specimen after being stretched to 300% elongation at 75°C (22-24°C) and then immediately allowed to recover at the same rate until the specimen becomes zero stress. It is the "tensileset" expressed as a percentage of the original length or distance between gauge lines. has a residual elongation not exceeding 100%. Some samples have a residual elongation of 75% or less. The elastomeric polypropylene that is a component of the present invention does not exhibit a yield point. As used herein, yield The point is
There is a strain (or elongation) value such that the stress (force) required to further increase elongation is reduced when tested to failure by ASTM method D412 at 20 inches (51 cm)/min and 25°C. It means that. The tensile and stress-strain measurements mentioned herein, including the Examples and Reference Examples, are based on the ASTM method.
0.25 inch (0.6 cm) width and 0.018 thickness by D412
-0.080 inch (0.045-0.20 cm) straight specimens and dumbbell specimens, except where an average value is indicated, two samples of the product are tested. The accompanying drawings illustrate the stress-strain (hysteresis) of a typical polymer (polymer of Reference Example 1) that is a component of the present invention in a highly isotopic manner according to the prior art sold by Hercules Inc. tactical polypropylene,
“Pro-Fax” 6523 (Isotactic content 94
%). The polymer of Reference Example 1 has a residual elongation of 93% at a tensile rate of 20 inches/min (51 cm/min) and the same relaxation rate. It does not indicate a yield point. Isotactic polypropylene is
has a residual elongation of 300% (i.e. shows no recovery);
and approximately 15% at a tension rate of 0.2 in/min (0.5 cm/min) and a relaxation rate of 20 in/min (51 cm/min).
The yield point is indicated by elongation. The elastic polymer which is a component of the present invention has a content of 1.5 to 9,
Preferably it has an intrinsic viscosity of 3 to 8, and the diethyl ether soluble fraction has an intrinsic viscosity of greater than 1.5, preferably greater than 2.5. Intrinsic viscosity, as used herein, is measured in decahydronaphthalene at 135°C by the method described below under "Analytical Methods." It is expressed in deciliters per gram (dl/g). The elastic polypropylene that is a component of the present invention gradually becomes more elastic as the content of the ether-soluble fraction and the intrinsic viscosity increase. Birefringence is clearly visible when a film formed by compressing a sample of the ether soluble fraction between microscope slides is viewed under a crossed Nicol prism at about 25° C. in a hot stage polarized light microscope. As the temperature increases, birefringence disappears in the range of the melting point of the film.
Birefringence is also clearly visible when films formed from the ether soluble fraction are compressed or stretched between crossed polarizers at temperatures of about 25°C. The total polymer has an isotactic content of 55% or less, preferably about 25-45%. "Isotactic content" means the proportion of polymerized propylene units that result in an ax segment in which five consecutive polymerized propylene units have the same configuration. Thus, a polypropylene in which 45% of the polymerized propylene units are contained in segments of 5 or more sequentially polymerized propylene units, and each such unit has the same configuration, has a 45% isotactic content. have a rate. The isotactic content described herein can be measured directly by ¹³ C nuclear magnetic resonance (nmr) according to methods known in the art, a preferred example of which is described in the "Analytical Methods" section below. It is explained there. For a given isotactic content, the elastomeric polymers of which the present invention is a component are highly elastic, as demonstrated by their residual elongation and absence of yield point. All polymers also have syndiotactic content. By syndiotactic content is meant that portion of polymerized propylene in which methyl groups are present alternately above and below the plane of the main chain. Syndiotactic content can also be measured directly by ¹³ Cnmr. The total polymer was determined by ASTM method D412 to be approximately
It has a tensile strength ranging from 400psi to 2500psi (28Kg/ ^cm2 to 175Kg/ ^cm2 ), with an ether soluble fraction of approx.
It has a tensile strength of 100 psi (17.5 Kg/cm ² ) to 600 psi (42 Kg/cm ² ). Each total polymer has a major melting point between about 135 and 155°C as determined by the method described below under "Analytical Methods." The diethyl ether soluble fractions of the new elastomeric polypropylenes have properties that distinguish them from the solvent extracted fractions of polypropylenes of the art. For example, they have relatively high values of w/n, where w is the weight average molecular weight;
n is the number average molecular weight, as shown by
It has a relatively wide molecular weight distribution. Billmeyer,
“Textbook of Polymer Science”, pp6-7
(Interscience/Wiley.1962). Ratio w/
n is referred to herein as dispersity. It is determined by gel permeation chromatography (GPC). The diethyl ether soluble fraction also has a relatively high intrinsic viscosity compared to that of the corresponding total polymer. The ratio of the intrinsic viscosity of the ether-soluble fraction to the total polymer is usually in the range 0.5 to 0.9. Furthermore, the diethyl ether soluble fraction is approximately 0.5
It has an isotactic crystalline content of ~5% by weight. Crystallinity content is strongly suggested by birefringence, evidenced and determined by heat of fusion (Δhf) and ¹³ Cnmr. ¹³ Cnmr data indicate that the crystallinity of these fractions is isotactic.
The technique for determining the above characteristics is the “analytical method” described later.
Let's discuss. The above discussion of the nature of the ether soluble fraction applies particularly to the ether soluble fraction of the total polymer isolated from the polymerization mixture by methods that do not involve hot melting or extrusion. Generally, the total polymer as isolated from the reaction system exhibits a higher percentage of ether extractable components, ie, about 30-80%, than after hot-melting extrusion or other fabrication. This decrease is believed to be due to the interaction of the more highly crystalline components in the product with the ether soluble fraction. High molecular weight and diethyl ether soluble components are important factors contributing to the elastic properties of the elastomeric polymers that are a component of the present invention. In this regard,
This elastomeric polymer differs from prior art polymers whose elastic properties are limited to the fraction soluble in hexane. The ether soluble fraction of the elastomeric polymers that are a component of this invention are highly elastomeric, but generally have low tensile strength. It can be combined with more crystalline polypropylene (ie, higher isotactic content polypropylene) to provide an elastic material with further improved tensile strength. It is believed that the isotactic units in the more crystalline polypropylene cocrystallize with the isotactic units in the ether soluble component to provide a cross-linked elastic network. The elastic polypropylene that is a component of the present invention is
propylene in the presence of a catalyst which is the reaction product of an organometallic compound with a partially hydrated surface of a metal oxide such as Al ₂ O ₃ , TiO ₂ , SiO ₂ and MgO or physical mixtures thereof. It can be produced by polymerization. The organometallic compound has the formula (RCH ₂ ) ₄ M, where M is Ti, Zr or Hf;
R is aryl, aralkyl, tertiary alkyl (e.g. trialkylmethyl) or trialkylsilyl, and the RCH ₂ group has no hydrogen bonded to the carbon in the β-position relative to M;
It is a compound of The alkyl groups mentioned above can contain 1 to 12 carbon atoms. Typically, the two catalyst components are reacted in a ratio of 0.01 to 1.0 mmole of organometallic compound per gram of metal oxide. Preferred catalysts are organozirconium compounds ( _RCH2 ) _4Zr , especially tetraneophylzirconium (TNZ) and hydroxylated alumina ( _Al2O3 ), about 0.1 to 1.0 organozirconium compounds per gram of alumina _.
The catalyst resulting from the reaction in millimolar proportions. Such catalysts and their preparation are described in US Pat. No. 3,932,307 to Setterguist. Preferably, the hydroxylated alumina is produced by equilibrating fumed alumina with atmospheric moisture and thereby absorbing atmospheric moisture, followed by heating in a nitrogen stream at about 120-500° C. for 1 minute to 10 hours. Ru. Suitable catalysts also include reaction products of the metal oxides described above with other organometallic compounds described above, which catalysts are prepared in the same manner as the preferred neophyll zirconium aluminates on alumina catalysts described above. Representative organometallic compounds include tetraneopentylzirconium, tetrabenzyltitanium, tetrabenzylzirconium, tetraneopentylhafnium, tetrabenzylhafnium, tetrakis(trimethylsilylmethyl)zirconium,
Includes tetraneofyl titanium and tetraneopentyl titanium. Included among the suitable catalysts are catalysts prepared by hydrogenating the above-described reaction products of organometallic compounds and metal oxides according to Setargist, US Pat. No. 3,950,269. In the polymerization process, the catalyst, usually in the form of a suspension in a hydrocarbon such as cyclohexane (approximately 2.5 to 50 milliliters of hydrocarbon per gram of metal oxide), is contacted with propylene in liquid form, or propylene is mixed with hexane or cyclohexane. It can be dissolved in a suitable solvent such as. Using any of these document media, the catalyst can also be prepared by combining the components in the presence of the monomer(s). Preferably, the reaction medium is liquid propylene and the reaction involves the production of a slurry of polypropylene in liquid monomer. Usually the catalyst is present in an amount of 1 gram atom of zirconium, haunium or titanium in the catalyst for every 200,000 to 2,000,000 grams of propylene. The reaction can be carried out at atmospheric pressure or at elevated pressures up to 5000 psi (350 Kg/cm ² ). Both batch and continuous polymerization methods can be used. Typical batch reaction times are about 10 minutes to 1 hour. The reaction temperature ranges from about 0°C to 175°C, preferably from 25°C to 100°C. The presence of hydrogen in the reaction medium not only reduces the solid viscosity of the polymers of the invention, but also increases the proportion of the dielether soluble fraction. Therefore, the polypropylene of the present invention is usually produced in the presence of hydrogen gas. Thus, when using neophyl zirconium aluminate on alumina catalyst at 50°C, the partial pressure of hydrogen at about 20 psi (1.4 Kg/cm ² ) is at least 35 with an intrinsic viscosity of at least 1.50, usually 2 or greater. yielding a product containing % ether soluble fraction. As the amount of hydrogen increases, the proportion of ether soluble fraction generally increases without significantly reducing the intrinsic viscosity of such fraction. The ratio of zirconium to metal oxide in the catalyst influences the proportion of ether soluble fraction obtained both in the presence and absence of hydrogen. Therefore, for the rate at which neophyll zirconium aluminate on alumina catalyst is used, a zirconium to alumina ratio of about 0.6 mmol of tetraneofyl zirconium per gram of alumina is typically used for polymers containing about 30% by weight of the ether-soluble fraction. give rise to
As the zirconium-alumina ratio decreases,
The proportion of ether soluble fraction increases. The intrinsic viscosity of the total polymer and the proportion of the ether-soluble fraction can also be controlled by the reaction temperature.
As the reaction temperature increases, the intrinsic viscosity decreases, and the proportion of the ether-soluble fraction decreases, especially around
Increases at temperatures above 50°C. The residual elongation of the total polymer generally decreases as the content of the ether-soluble fraction and the intrinsic viscosity increase. The polymer has a particularly low elongation set when the intrinsic viscosity of the ether soluble fraction is 2.5 or higher. Reference examples illustrate methods of making such polymers. The order in which propylene, hydrogen and catalyst are fed to the reaction zone usually does not have significant consequences, but M
It has been found that when Hf, the proportion of ether soluble polymer increases if the catalyst is contacted with hydrogen for at least about 5 minutes before the propylene is introduced. After venting the excess propylene, the polypropylene can be isolated by conventional methods. If the reaction medium is liquid propylene, hot milling, extraction-extrusion, or steam-stripping is used to remove any residual unreacted propylene and any volatile solvent that made up the catalyst slurry. be able to. Alternatively, the product mixture can be swollen into a gel by the addition of a liquid hydrocarbon such as cyclohexane, and the polypropylene can be precipitated and converted to a filterable solid by the addition of a liquid such as acetone, followed by The polypropylene is then isolated by filtration. When the reaction medium is a liquid such as cyclohexane, the polypropylene can be isolated by precipitation with acetone followed by filtration as described above. As mentioned above, the isolation method used can affect the amount of diethyl ether soluble fraction found in the recovered polymer. The elastic polypropylene that is a component of the present invention can be produced in good yields, especially when neophyl zirconium aluminate on alumina catalyst is used. Yields range from about 30,000 to 1,000,000 grams of polymer per gram atom of zirconium, and usually at least about 2,000,000 grams of polymer per gram atom of zirconium. The ether soluble fraction of the invention is separated by extraction with boiling diethyl ether. Polypropylene, a component of the present invention, includes copolymers containing small amounts of units derived from α-olefins other than propylene, eg, up to about 10 mole percent of the total polymer. Such α-olefin is
They can be incorporated into polymers by copolymerization without changing the essential properties described herein. Representative such α-olefins are ethylene, 1-butene, 1-pentene and 1-hexene. The present invention uses a wide proportion of the total polymer, e.g.
It can be blended with highly isotactic polypropylene up to 95% by weight to provide a blend with useful properties. Blends of the present invention containing about 60-95% by weight polypropylene and 40-5% by weight highly isotactic polypropylene generally have elastic properties. The highly isotactic polypropylene used has an isotactic content of at least about 85%. There are various commercial polypropylenes of this type, an example of which is "Pro-fax" 6523, mentioned above. The elastomeric polypropylene component of the present invention can be processed in the same manner as conventional elastomers.
If desired, the product can be formulated with additives such as carbon black, mineral fillers, oils and pigments. Polypropylene is used as a film with elastic properties (heat-shrinkable film), filament, for use in fiber and heat and textile coating applications, wire and cable coatings, hot melt adhesives and injection molded articles, compression molded articles, or tires and It is an excellent general purpose thermoplastic elastomer with properties that make it suitable for extrusion molded products such as tubes. Oriented objects such as uniaxially oriented straps and uniaxially or biaxially oriented films can also be formed from all polymers and from the elastic blends (polypropylene compositions) described above. Uniaxially oriented films exhibit superior elastic recovery after elongation. Biaxially oriented films are particularly valuable in packaging applications. This is because they combine the characteristics of high extensibility desirable in stretch wrapping with low shrinkage tension desirable in heat shrinkable wrapping. Biaxially oriented films can be made, for example, by simultaneously stretching the film in two directions (usually
400-700%) using known techniques by subsequent gradual relaxation of the tension. The film can be heated to about 125° C. during the stretching period, where it is still cooled under tension. The polymers that are a component of the present invention do not require the addition of extractable plasticizers for high flexibility and are therefore suitable for use in milk, blood and parenteral fluids (parenteral fluids).
It is also particularly useful for extruded flexible tubing used in contact with liquids such as liquids. Such tubing can be used in extruder and tubing die and pin mechanisms, including screws for polyethylene.
It can be made by known methods such as melt extrusion at temperatures between 390° and 480° C. (200° C. and 250° C.). The tube is extruded into a vacuum box filled with water to quench the product and maintain its dimensions.
Typically, all-polymer or highly isotactic polypropylene and all-polymer elastomeric blends are used for this application. Products of the type described above can be made directly from the whole polymer and often from the diethyl ether soluble fraction and from blends of these polymers with highly isotactic polypropylene. In some applications, polymers can be subjected to thermal and mechanical treatments such as shearing for use in products requiring lower molecular weights and narrower molecular weight distributions. A particularly important advantage of the present invention is that the elastic polypropylene can be used as it is, which is produced directly and therefore does not need to be separated into its components to be used in the production of such products. Solubility in any of the solvents mentioned herein is determined as follows: Heat the solvent to boiling in a round bottom glass flask. The steam rises through the outer region of the vertical cylindrical chamber and is cooled in a reflux condenser. The condensate is allowed to drip into a fiore or glass cylinder with a glass filter disk at its bottom, the cylinder being suspended in the center of a vertical cylinder. Cylindrical paper is
Contains a sample (1-2 g) of polypropylene with an average particle size not greater than about 1/8 inch (3 mm).
The outer wall of the paper cylinder is surrounded by hot solvent vapor and heated, so that the actual extraction takes place at or near the boiling temperature of the solvent. Extraction is 0.01 for an overnight (at least 15 hours) extraction period.
This continues until losses of less than g occur. All operations are carried out in an atmosphere of nitrogen and solvent vapor. The percentage of sample extracted is the soluble portion. The intrinsic viscosity referred to herein is determined as follows: At 25°C, 0.075 g of polypropylene sample is
0.1g of BHT (2,6-di-t-butyl-
4-methylphenol) in 50 ml of decahydronaphthalene to obtain a weight-volume concentration of 0.05% at 135°C, at which temperature the sample was heated under nitrogen for 2 hours.
Dissolve as time passes by stirring with a magnetic stirrer. The solution was passed through a filter stick and passed through a Cannon-Ubbelohde viscometer.
viscometer) and its run-off time is measured at 135°C compared to the run-off time of the solvent alone. Viscosity (ηinh) = 1nT/To/C T = Outflow time of solution To = Outflow time of solvent C = Concentration ( ^0.05 g/deciliter) The 13 Cnmr spectrum is determined as follows: ^{The 13} Cnmr spectrum is determined by the Bruker WH operating at 22.63MHz in the Fourier transform method.
90nmr spectro maker (Bruker WH-
Obtained at 137°C using a 90nmr spectrometer.
For a typical operation, 10000 scans are employed. The radio frequency pulses are adjusted to provide a 60° tilt angle. Sample as stabilizer
It is tested as a solution of 0.2 g of polymer in a mixture of 1 ml of o-dichlorobenzene and 1 ml of dideuterotetrachloroethane containing 0.05 wt-vol% BHT, and tetramethylsilane as a standard. ^{The 13} Cnmr isotactic content is the area of the mmmm pentad peak at approximately 21.7 ppm divided by the total area of the ¹³ C methyl resonance;
Zambelli et al; Macromolecules, 6 , 925
(1973). Syndiotactic content is approx.
It is determined in the same way from the peak at 20.2 ppm. Crystallinity by ¹³ Cnmr As described above for polypropylene samples, ¹³ Cnmr
If there is some sufficiently long isotactic array crystallization, there may be a decrease in the height and area of the mmmm pendad peak when the solution is cooled to ambient temperature.
This difference is a measure of the ¹³ C "rigidity" of the polymer and corresponds to an isotactic pentad that has become immobile. The observed percentage pentad isotactic content of hot and cold polymer solutions can be specified as F and C, respectively. Then the % ^13C stiffness is
Formula % ¹³ C stiffness = H - C (100 - H) / 100 - C The term (100 - H) / (100 - C) brings the absolute values of the non-isotactic pentads of H and C to the same level. used as such. ) % ^13C isotactic stiffness is correlated with crystallinity measured by differential scanning calorimetry (see below). % ^13C isotactic crystallinity is
Formula, % ^13C isotactic crystallinity = 0.625×
(% ¹³ C isotactic stiffness). The factor 0.625 is the slope of the line obtained by plotting 2Δhf (see below) versus % ¹³ C isotactic stiffness for a number of polypropylenes including Pro-fox 6523. The melting points referred to herein are principal melting points determined by differential scanning calorimetry (dsc). 10−20mg
Heating the sample from -40℃ to 200℃ at 20℃/min,
Cool from 200°C to -40°C at 5°C/min, and
Reheat from -40°C to 200°C at 10°C/min. The principal melting point is the heat transfer obtained in the reheating operation.
flow)/temperature curve and is the temperature at the main endothermic peak on that curve. The melting point of the ether soluble fraction is determined by initial heating. All of the ether soluble fractions in the following examples had comparable thermal histories (70° C./4 hours to remove volatiles, followed by room temperature storage). To further discuss the operation, Ke,
“Newer Methods of Polymer
Characterization” p.350 (Interscience, 1964)
reference. Crystallinity by heat of fusion The heat of fusion, Δhf, is calculated from the area enclosed by the dsc melting peak. The start and stop temperatures, ie the lower and upper limits that determine the portion of the curve to be used to calculate the area, are selected visually as the deviation of the curve from the baseline. The formula used is Δhf = area/Km, where K is a calibration constant assumed to be independent of temperature and determined by the use of indium with known heat transfer, and m is the mass of the sample. Values are reported as calories/gram. See Ke (supra), pp357-359. The weight fraction of the crystalline polymer, Xc, is expressed by the formula Δhf=
XcΔho, where Δhf is the heat of fusion per gram of polymer and Δho is the heat of fusion per gram of pure crystal. Mark and Tobolsky, “Polymer
Science and Materials”, p180 (Interscience/
See Wiley, 1971). A value of Δho of 50 calories per gram has been proposed for polypropylene. Xc expressed as a percentage is Δhf/50×
100, or equal to 2Δhf. Birefringence or double refraction
is a well-known optical phenomenon resulting from differences in the refractive index of light that is polarized due to differences in polarizability in various directions in an anisotropic material. It is possible to observe minute details under a polarizing microscope, and even more simply by stretching the film between two orthogonal polarizers and viewing it through these polarizers as a multicolored spectral pattern. can be observed. Both methods are used in the Examples and Reference Examples below. For example, Battista,
“Fundamentals of High Polymers”. pp97-98
(Reinhold, 1958): Seymour, “Inyroduction
of Polymer Chemistry”, pp284-285 (McGram
―Hill1971): and Tonford, “Physical
Chemistry of Macromolecules”, pp116―118
See (Wiley, 1961). The present invention will be further explained by the following examples and reference examples. Parts and percentages are by weight unless otherwise specified. Care is taken in the Examples and References to exclude oxygen and water from the polymerization and all steps preceding it. All materials used are of high purity. The catalyst slurry is made up under nitrogen and all transfers are performed under nitrogen. Except as noted, in the Examples and Reference Examples, the alumina support was prepared by equilibrating the fumed alumina with atmospheric moisture, subsequently heating the resulting product at 400° C. for 4 hours in a nitrogen stream, It is then produced by cooling under nitrogen. Reference Example 1 Heat a stainless steel autoclave equipped with a stirrer at 150° C. for 2 hours while evacuating. The vacuum source is shut off, the autoclave is filled with nitrogen to a pressure of 300 psi (21 Kg/cm ² ), and the system is allowed to cool to room temperature. A slurry of the catalyst is prepared by stirring 1 g of alumina (Al ₂ O ₃ ) in 40 ml of cyclohexane for 14 hours, adding a solution of 0.36 mmol of tetraneophylzirconium in 2.0 ml of toluene, and stirring for 1 hour or more. . The slurry is transferred by syringe to a 75 ml stainless steel cylinder designed so that its contents can be injected by nitrogen pressure into the autoclave used for the polymerization. Cyclohexane (450 ml) was passed through a bed of Woelm acid alumina into a glass container and then passed under nitrogen into an autoclave previously evacuated to atmospheric pressure,
Then purge with nitrogen. The autoclave is evacuated to a pressure of about 50 mm for 1 minute and charged with 126 g of propylene while stirring at 500 rpm {90 psi (6.3 Kg/cm ² ) pressure at 22° C.}. Hydrogen at a total pressure of 115psi (8.0Kg/cm ² )
(Inject to give a hydrogen partial pressure of 25 psi (1.8 Kg/cm ² ). Heat the solution to 50°C, inject the catalyst slurry, and then increase the temperature to 70°C for about 5 minutes. The system was then heated to 50°C (total pressure 97~
200psi) (6.8~14Kg/ ^cm2 )
Keep at 50-52 °C for an hour, then evacuate, cool and open the autoclave. The viscous mixture recovered is divided into three approximately equal parts and each is stirred in a blender with about 700 ml of acetone. The resulting solids were separated by filtration, combined, and treated with Irggnox 1010 (Irggnox 1010).
1010) Antioxidant (tetrakis-[methylene 3-
Stir in a blender with about 700 ml of acetone containing 0.3 g of (3',5'-di-t-butyl-4'-hydroxyphenyl)propionate]methane.
Filter, air dry and in a vacuum oven for 70-80 min.
After drying for 4 hours at °C, 102.4 g of polypropylene
is obtained as a crumb-like solid. Test films pressed at 225°C are non-tacky, reasonably strong, extensible, and elastic. The intrinsic viscosity of the polymer is 5.5 and the isotactic content by ¹³ Cnmr is 37%. Its melting point is 151°C. The product contains 46.5% diethyl ether soluble fraction with an intrinsic viscosity of 3.1. Birefringence is clearly visible when a film formed from this fraction is stretched between crossed polarizers at room temperature. The ratio of the intrinsic viscosity of the ether soluble fraction to the total polymer is 0.56. No reduction in syndiotactic pentads is observed from ¹³ Cnmr. 2%
The isotactic crystallinity of is determined by ¹³ Cnmr and a melting point of 58°C and a Δhf of 1.6 cal/g are observed. The degree of distribution is equal to 7.6. Approximately 25 pieces of film
It can also be clearly seen when viewed under a crossed Nicol prism using a hot stage polarizing microscope at ℃. Temperature 1
When ramping at 10°C per minute, birefringence disappears at about 78°C. All-polymer 30 mil (0.76 mm) films are made by hot compression molding samples of the product at 180°C. When samples of this film are stretched at 20 inches (51 cm) per minute and immediately allowed to recover to zero stress at the same rate, they exhibit an average residual elongation of 93%. Other samples of this film were tested at 620% elongation to break in stress-strain tests.
It shows a tensile strength at break of 966psi (68Kg/cm ² ). No yield point is observed in these determinations. Reference Example 2 1 Heat a stainless steel autoclave equipped with a stirrer at 150° C. for 2 hours while evacuating. Shut off the vacuum source and add propylene to 50psi (3.5Kg/cm ² )
The autoclave was charged to a pressure of , and the system was allowed to cool to room temperature. A slurry of benzyl hafnium aluminate catalyst on alumina is prepared by stirring a solution of 1 g of alumina, 0.29 mmol of tetrabenzyl hafnium in 3.0 ml of toluene and 40 ml of cyclohexane for 17 hours. The autoclave is evacuated to remove excess propylene, evacuated at approximately 50 mm for 1 minute, and cooled in ice/methanol. Start stirring at 200 rpm and charge 168 g of propylene to the autoclave. System at 25℃ (pressure 155psi) (10.8Kg/cm ² )
and hydrogen at a hydrogen pressure of 25psi (1.8Kg/cm ² ).
(total pressure 180psi) (12.6Kg/cm ² ). The catalyst slurry is then injected as in Reference Example 1. The system is heated to 75° C. for 35 minutes, then heated at 72-77° C. at autogenous pressure (400-435 psi) (28.0-30.5 Kg/cm ² ), after which the autoclave is evacuated and cooled. . Add 300 ml of cyclohexane to the product in a blender.
and convert it into a gel. Then 1 part of acetone is added, the mixture is stirred for about 1 hour and the product is separated by filtration. Irganox 1010 (Irganox 1010) Antioxidant 0.3
Stir in a blender with 1 g of fresh acetone, separate by filtration, air dry,
It is then dried in a vacuum oven at 70-80°C for 4 hours to obtain 40.9 g of solid polypropylene. The product has an intrinsic viscosity of 8.2 and an isotactic content according to ¹³ Cnmr of 45%. Melting point is 145°C. When extracted with diethyl ether, the product is found to contain an ether-soluble fraction which constitutes 39.1% of the total polymer and has an intrinsic viscosity of 4.7. The ratio of the intrinsic viscosity of the ether soluble fraction to the total polymer is 0.57. This is clearly visible when a film formed from this fraction is stretched between crossed polarizers at room temperature. An isotactic crystallinity of 1% is determined by ¹³ Cnmr and a melting point of 57°C and a Δhf of 1.5 cal/g are observed. No reduction in syndioctotic pentads is observed in ¹³ Cnmr. The degree of distribution is equal to 5.1.
Birefringence is also clearly visible when the film is viewed in a hot stage polarizing microscope under a crossed Nicol prism at approximately 25°C. When the temperature is increased by 10°C per minute, birefringence disappears at about 98°C. All-polymer 18 mil (0.45 mm) films are made by hot compression molding samples of the product at 180°C. 20 samples of this film per minute
When stretched at 51 cm and immediately recovered to zero stress at the same rate, they
Shows an average residual elongation of 106%. Stress until breakage
Other samples of this film in strain tests were 510
Average tensile strength at break of 2280 psi (160 Kg/cm ² ) at % elongation. No yield point is observed in these decisions. Reference Example 3 Heat a stainless steel autoclave equipped with a stirrer at 150° C. for 2 hours while evacuating. Shut off the vacuum source and add propylene to 50psi (3.5Kg/cm ² )
The autoclave was charged to a pressure of 100 mL and the system was allowed to cool to room temperature. A slurry of the catalyst is prepared by stirring a solution of 1.0 g of alumina, 0.3 mmol of tetranepentylzirconium in 4.0 ml of toluene and 40 ml of cyclohexane for 16 hours. The autoclave is evacuated to remove excess propylene, evacuated at approximately 50 mm for 1 minute and cooled in ice. Start stirring at 200 rpm and charge 168 g of propylene to the autoclave. The stirring speed was increased to 500 rpm and the system was heated to 27°C (pressure 165psi;
11.5Kg/cm ² ), and the hydrogen partial pressure is
It is introduced into the autoclave at a pressure of 25 psi (1.8 Kg/cm ² ) (total pressure 190 psi; 13.3 Kg/cm ² ). The catalyst slurry is then injected as in Reference Example 1. system
Heated to 50°C for 16 minutes, then heated to 50°C at autogenous pressure (270-300psi; 18.9-21.0Kg/ ^cm2 ).
Heat at 54° C. for 1 hour, then evacuate the autoclave and cool. Add 400ml of cyclohexane to the product in a blender.
and stir to convert it into a gel. Then add 1 part of acetone and stir the mixture for about 1 minute,
The product is then separated by filtration. that
Stir in a blender with 1 part of fresh acetone containing 0.3 g of Irganox 1010 antioxidant, separate by filtration and 4 parts at 70-80 °C in a vacuum oven.
Air dry for an hour to obtain 81.7 g of solid polypropylene. The intrinsic viscosity of the product is 5.4, the isotactic content by ¹³ Cnmr is 40%, and the melting point is
The temperature is 150℃. When extracted with diethyl ether, the product is found to contain an ether soluble fraction that constitutes 50.8% of the total polymer and has an intrinsic viscosity of 4.8. The ratio of the intrinsic viscosity of the ether soluble fraction to the total polymer is 0.89. Birefringence is clearly visible when a film formed from this fraction is stretched between crossed polarizers at room temperature. A melting point of 73°C and a Δhf of 1.3 cal/g are observed. Distribution degree is 4.6
be equivalent to. A 29 mil (0.73 mm) film of all polymer is prepared by hot compression molding a sample of the above product at 180°C. sample of this film per minute.
When stretched at 20 inches (51 cm) and immediately allowed to recover to zero stress at the same rate, they exhibit an average residual elongation of 54%. Other samples of this film have a stress-to-strain test of 30% to failure.
It shows an average tensile strength at break of 1500 psi (105 Kg/cm ² ) at an elongation of . No yield point is observed in these determinations. Reference example 4 Polymer preparation 19 g activated alumina in 487 ml cyclohexane
The slurry is placed in a dry glass bottle under a nitrogen atmosphere. A solution of 4.8 mmol of tetraneophyl zircomium in 24 ml of toluene is added with stirring. Seal the bottle and stir the catalyst slurry overnight using a magnetic stirrer. The dry 5-gallon (19) reactor was purged with propylene to remove nitrogen and then flushed with propylene.
Prepare 3300g. After warming to 25° C., hydrogen is added to increase the reactor pressure by 90 psi (6.3 Kg/cm ² ) and the catalyst slurry is injected by the method of Reference Example 1 with stirring at 500 rpm. The reaction temperature increases to 35°C with the addition of catalyst. Heat is applied to raise the reactor temperature to 40°C. Over the 1 hour reaction period, the reactor temperature was 40-64°C and the pressure was
235-325psi (16.4-22.7Kg/ ^cm2 ). During the course of the reaction, the temperature is controlled within a certain range by venting gas from the reactor, and additional amounts of hydrogen are injected to replace the hydrogen lost through venting. Polypropylene products at temperatures up to 120°C
The solvent is removed by grinding using a roll rubber mill. At this point, the stabilizer [3-methyl-6-tert-
3 moles of butylphenol and 1 mole of crotonaldehyde
0.2% of the condensation product with molar (“Topanol” CA) and 0.5% of dilaurylthiodiopionate (“Cyanox” LTDP)] are also added. 1948g
A stabilized polypropylene having a weight of . The product was transferred onto a two-roll rubber mill at 180°C for 5 minutes.
Leave for a minute to remove traces of solvent. Its intrinsic viscosity is 3.3 and isotactic content is 36%
The melting point is 146°C. A 200 g sample is extracted with boiling diethyl ether and the product is found to contain 66% total polymer and have an ether soluble fraction with an intrinsic viscosity of 1.9. The ratio of the intrinsic viscosity of the ether soluble fraction to the total polymer is 0.58. Birefringence is clearly visible when a film formed from this fraction is stretched between crossed polarizers at room temperature. An isotactic crystallinity of 3% was determined by ¹³ Cnmr, and a melting point of 57°C and 1.6 cal/g.
Δhf is obtained. No reduction in syndioctotic pentads is observed in ¹³ Cnmr. The degree of distribution is equal to 10.6. Birefringence is also clearly visible when films made from the ether-soluble fraction are viewed under a crossed Nicol prism in a hot-stage polarizing microscope at about 25°C. Temperature 10℃ per minute
The birefringence disappears at 59°C. The all-polymer 31 mil (0.78 mm) film exhibits an average residual elongation of 85%. Its average tensile strength at break is 920 psi (65 Kg/cm ² ) at 725% expansion. No yield point is observed. 79 mil (2.0 mm) film of the same polymer
20 inches/min (51 cm/min) at 23°C under ASTM conditions
The film was uniaxially stretched to 700% at the same speed, and then relaxed at the same speed until the stress disappeared. The resulting sample is 330% of the original length, which is due to the stretching ratio
2.3 is shown. The stretched sample was 2206 psi (154 psi) at 180% elongation at 20 in/min (51 cm/min).
Kg/cm ² ) indicates the tensile strength at break. It immediately recovers completely from this strain and exhibits very high elasticity. No yield point is observed. B Film Preparation and Testing Films of various thicknesses were made from the product described in part A by compression molding at 225°C;
Then, it is rapidly cooled in water at 5-10℃. The elastic behavior is
Stretching 2.2-4.2 mil (0.056-0.011mm) films to 100%, 200% and 300% of their original length;
Measured by a stretch-recovery test consisting of stress removal and relaxation for 1 hour. Measure the extent to which they recover. The results are shown in the table below.
Percentage recovery is defined as 100 x (maximum stretch elongation - length of relaxation)/(maximum stretch length - original length). Elongation recovery 100% 92% 200% 91% 300% 88.5% A heat-shrinkable film is produced by biaxial orientation. A 30 mil (0.76 mm) film was heated at 125°C for 2 minutes, simultaneously stretched 4 times in the vertical direction at 125°C and a strain rate of 10000%/min, and stretched 5 times at 125°C stretching temperature.
Anneal for a minute, cool and remove from the stretcher, after which it relaxes to (3.75X) ² . The film shrinkage is then measured at various temperatures with the results shown in the table below:

[Table] Reference Example 5 Prepare a 0.00125M solution of tetraneophylzirconium in cyclohexane. 0.00125M of tetraneophylzirconium at a rate of ^294cm3 /hr
The solution and a suspension of 0.0374 g of alumina per ml of mineral oil were fed at a rate of 1.4 g Al ₂ O ₃ /hr into a 961 cm ³ capacity stirred autoclave made of stainless steel, where it was heated to 51 °C. A suspension of active supported catalyst comprising neophyl zirconium aluminate on alumina is prepared by dilution with 161 cm ³ of retained hexane. Dry in a nitrogen stream at 1000°C and at 73°C.
Alumina is produced by rehydration by contact with a 50% relative humidity atmosphere for 16 hours and then redrying by heating at 400° C. for 4 hours in a stream of N ₂ . Continuously feeding the catalyst suspension at the same rate into a 253 cm ³ stainless steel autoclave after a protection time of about 117 minutes to allow the reaction between the tetraneophylzirconium and the activated alumina to produce neophyllzirconium aluminate; and cyclohexane
Dilute at 158 cm ³ /hr. After a holding time of 25 minutes in the autoclave, the diluted catalyst suspension was heated to 1850 psi.
(130Kg/cm ² ) and maintained at 85℃ and stirred.
Continuously feed a 253 cm ³ stainless steel polymerization vessel where it is brought into contact with propylene. 386 by introducing propylene into a stream of cyclohexane being fed at a rate of 592 cm ³ /hr.
Feed propylene at a rate of g/hr. An additional flow of 250 cm ³ /hr of cyclohexane is fed as a flash to the stirrer and the product stream is
All feed is withdrawn at the same rate so that the apparent residence time in the reactor is approximately 7.6 minutes. The product mixture is passed through a chamber where a 0.00836M solution of isopropanol in cyclohexane is added at 523 cm ³ /hr.
The catalyst is deactivated by adding at a rate of . The polypropylene solution is continuously discharged through a controlled pressure reducing valve to a product receiver maintained at 50°C. The polymer product is isolated by treatment with acetone. The precipitated polymer is chopped in a Waring blender in the presence of acetone. The polymer pieces are air dried in a feed and then dried in a heated roll machine. Produces 12g product per hour. The product has a specific year of 3.0, an isotactic content of 44% and a melting point of 150°C. A 30 mil (0.76 mm) film of all polymer is prepared by hot compression molding a sample of the product at 180°C. When samples of this film are stretched at 20 inches (51 cm) per minute and immediately recovered to zero stress at the same strain, they exhibit an average residual elongation of 89%. Other samples of this film in the stress-strain-to-break test exhibit a tensile strength at break of 1506 psi (106 Kg/cm ² ) at 780% elongation. No yield point is observed in these determinations. The total polymer is extracted with boiling diethyl ether and then the ether soluble fraction is extracted with boiling hexane. You will get the following data:

[Table] Birefringence is clearly visible when a film formed from the ether soluble fraction is stretched between crossed polarizers at room temperature. 1% isotactic crystallinity
¹³ C _onr and a Δhf of 2.7 cal/g is observed. No reduction in syndiotactic pentads is observed in ^13C _onr . The degree of distribution is equal to 7.6. Birefringence is also clearly visible when the film is viewed under an orthogonal Nicol prism in a hot stage polarizing microscope at about 25°C. When the temperature is increased at 10°C per minute, birefringence disappears at about 60°C. The ratio of the intrinsic viscosity of the ether soluble fraction to the total polymer is 0.80. Example 1 A Polymer Preparation A 1 gallon (3.8) stainless steel autoclave equipped with an agitator is heated at 150° C. for 2 hours while evacuating. Shut off the vacuum source and remove the propylene.
Charge the autoclave to a pressure of 50 psi (3.5 Kg/cm ² ) and allow the system to cool to room temperature. 5.7 g of alumina and 183 ml of cyclohexane were stirred for 18 hours, a solution of 1.43 ml of tetraneophylzirconium in 7.2 ml of toluene was added, and
Prepare catalyst slurry by stirring for 1.5 hours. The autoclave was evacuated, evacuated for 1 minute at approximately 50 mm to remove excess propylene, and heated to 0°C.
Cool lower. Start stirring at 500 rpm,
Then, charge 795 g of propylene into the autoclave. The system was heated to 25°C (pressure 130 psi, 9.1 Kg/cm ² ), and hydrogen was heated to a hydrogen partial pressure of 30 psi (2.1 Kg/cm ² ).
Introduce into autoclave until . Internal pressure continues to rise to 185 psi (12.9 Kg/cm ² ). The catalyst slurry is injected as in Reference Example 1. The system was heated to 35°C for 14 minutes and then heated at autogenous pressure (245-280psi, 17.1-19.6Kg/ ^cm2 ) for 35 minutes.
Heat at ˜51° C. for 1 hour, then evacuate the autoclave and cool. The product is added to cyclohexane 1 and the mixture is allowed to stand overnight. Then 1 part of acetone is added, the mixture is stirred in a blender and the product is separated by filtration. Repeat this treatment with acetone. The final product is 1.5
Place in a blender with 1 g of fresh acetone containing 1 g of Irganox 1010 antioxidant. Leave the mixture overnight and stir. The solids are separated by filtration, air dried and dried in a vacuum oven at 70-80°C for 4 hours to yield 247.3 g of solid polypropylene. The product has an intrinsic viscosity of 5.4, an isotactic content of 36% and a melting point of 144°C. When extracted with boiling diethyl ether, the product consists of 74.5% of the total polymer and
It is found to contain an ether soluble fraction with an intrinsic viscosity of 4.6. The portion of the polymer that is insoluble in diethyl ether is extracted with boiling hexane to obtain a hexane-soluble fraction that constitutes 11.4% of the total polymer and has an intrinsic viscosity of 4.6. The hexane-insoluble fraction constitutes 14.1% of the total polymer and
It has an intrinsic viscosity of 6.1. When the film formed from the ether soluble fraction is stretched between crossed polarizers at room temperature, birefringence is clearly visible. An isotactic crystallinity of 1% was determined from ¹³ C _onr , and a melting point of 60°C and
A Δhf of 1.5 cal/g is observed. No reduction in syndiotactic pentads is observed with ^13C _onr . The degree of distribution is equal to 6.2. The ratio of the intrinsic viscosity of the ether soluble fraction to that of the total polymer is 0.85
It is. Birefringence can also be clearly seen when the film is viewed under a crossed Nicol prism using a hot stage polarizing microscope at approximately 25°C. Temperature 10℃ per minute
Birefringence disappears at about 88°C. A 31 mil (0.78 mm) film of all polymer is produced by hot compression molding a sample of the product at 180°C. When samples of this film are stretched at 30 inches (51 cm) per minute to 300% elongation and immediately allowed to recover at the same rate to zero stress, they exhibit an average residual elongation of 41%. Other samples of this film exhibit an average tensile strength at break of 884 psi (62 Kg/cm ² ) at 725% in stress-strain to break tests. No yield point is observed in these tests. B Blend Production and Characteristics 1 Ether Soluble Fraction + Isotactic Polypropylene The ether soluble fraction described in Part A
0.5% Cyanox LTDP Thiodipropionate and
Stabilize by milling with 0.25% Topanol CA stabilizer. Samples of stabilized ether-soluble polymers are processed on a rubber roll machine.
Blend with various amounts of isotactic polypropylene (pro-fax 6523, 94% isotactic content, melting point 166°C) for 5 minutes at 180°C.
Tensile elongation was determined by compression molding approximately 30 mils (0.76 mm) thick film at 180°C, elongating 300%, and relaxing as in Reference Example 1, and then at 20 in/min (51 cm/min). ) until it breaks. You will get the following data:

【table】

[Table])
2 Total Polymer + Isotactic Polypropylene The entire polymer described in Part A stabilized with 0.5% Cyanox LTDP and 0.25% Topanol CA as in Part B1 was milled at 180°C to Pro-
Mix with Fax 6523 isotactic polypropylene. 29 mil (0.74mm) compression molded at 180°C
Two samples of the film have an average residual elongation of 68%, and the other sample has a stress/strain tensile strength at break of 2000 psi (741 Kg/cm ² ) at 780%. Pro-Fax
Two samples of films of the same polymer blend containing 33% have an average tensile set elongation of 128%. The two other samples were 2272 psi (160 psi) at 680% elongation.
It has an average tensile strength at break of Kg/cm ² ). No yield point is observed for either blend. 3 Ether soluble fraction + hexane insoluble fraction Ether soluble fraction and hexane insoluble fraction 33%
A blend of the hexane-insoluble fractions of all the polymers described in Part A containing was prepared by milling the polymers together at 150°C by the method of Parts B1 and B2, and a 31 mil (0.79 mm) film was prepared by milling the polymers together at 150°C. of
Compression mold at 180℃. The two samples have an average residual elongation of 52% and no yield point. Two other samples have an average tensile strength at break of 1263 psi (89.1 Kg/cm ² ) at 760% elongation. Reference Example 6 This reference example illustrates the decrease in the percentage of the ether soluble fraction and the decrease in the intrinsic viscosity of that fraction when milling the elastic polypropylene that is a component of the present invention. 1 A stainless steel autoclave equipped with a stirrer is heated at 150°C with 500 ml of cyclohexane, the cyclohexane is removed under vacuum at 90°C, and the autoclave is purged with nitrogen at 150°C for 4 hours. As the purge continues, a slurry of 1.0 g of alumina in 40 ml of cyclohexane is introduced.
Hydrogen (5 ml at 500 psi; 350 Kg/cm ² ) was introduced,
The autoclave is cooled to 8° C. and 200 g of propylene are added from the cylinder. The autoclave was warmed to 20°C and a solution of 0.5 mmol of tetraneophylzirconium in 5 ml of toluene was added to the system.
It is introduced under nitrogen pressure as in Reference Example 1 while stirring at 500 rpm. The temperature is immediately raised to 24°C, increased to 28°C in about 15 minutes, and then lowered to 23°C in 1 hour while exhausting excess propylene. The resulting gel is cut into chunk pieces and heated under vacuum at 70 °C to remove all volatiles. 55.5 g of elastic polypropylene are obtained. At this point the product has an intrinsic viscosity of 8.2, an isotactic content of 25% and a melting point of 144°C.
It contains 57% diethyl ether soluble fraction, which has an intrinsic viscosity of 6.4, a degree of distribution of 13.9,
It has a melting point of 51°C and a Δhf of 1.6 cal/g. The film made from the ether soluble fraction was heated to about 25°C.
Birefringence is clearly visible when viewed under a crossed Nicol prism in a hot-stage polarizing microscope. When the temperature is increased by 10°C per minute,
Birefringence disappears at about 85°C. Then 53g of product was added to 0.265g of Cyanox.
Mill with LTDP and 0.132 g Topanol CA antioxidant for 10 minutes at 180°C. The milled product has an intrinsic viscosity of 7.5 and 22%
Contains an ether soluble fraction, which has an intrinsic viscosity of 9.1, a degree of distribution of 3.6, a melting point of 49°C and a
It has Δhf of g. 75~80mil (0.19~0.20cm)
A sheet of the milled product is compression molded at 180°C. When samples of this sheet are stretched at 20 inches (51 cm) per minute to 300% elongation and immediately recovered to zero stress at the same rate, they exhibit an average tensile residual elongation of 39%. Other samples of this sheet were tested in stress-strain tests to failure.
Shows an average tensile strength at break of 1500 psi (105 Kg/cm ² ) at 910% elongation. No yield point is observed in these tests. Reference Example 7 Reference Example 6 pre-adjusted as described in Reference Example 6
A slurry of 2 g of alumina in 80 ml of cyclohexane is introduced into the autoclave. The autoclave is sealed and pressurized with ethylene to 65 psi total pressure. The total pressure is then brought to 90 psi with hydrogen, the vessel is cooled, and 168 g of propylene is introduced. As the system was stirred at 500 rpm, the temperature rose to 50 °C and the tetraneophylzirconium
4 ml of a solution of toluene containing 0.4 mmol are forced in together with nitrogen. There is an immediate temperature swing to 95°C and the polymerization is allowed to proceed for 1 hour with the temperature gradually decreasing to 54°C. Excess propylene is vented at the polymerization temperature and the product is freed of volatiles by nitrogen purge and evacuation at 70° C./0.2 mm. 146 g of an elastic polypropylene/ethylene copolymer containing 6 mol % (4% by weight) of units derived from ethylene are obtained. When isolated, it has an intrinsic viscosity of 5.9, an ether solubility of 64%, a melting point of 142°C, and a glass transition temperature (Tg) of ~21°C. The intrinsic viscosity of the ether soluble fraction is 3.35. 143g
The product is 0.72g Cyanox LTDP and 0.36g
Milled for 10 min at 150 °C with Topanol CA antioxidant. An 80 mil (0.20 cm) thick sheet of the milled product is compression molded at 150°C.
A sample of this sheet was run at 20 inches (51
They exhibit an average residual elongation of 87% when stretched to 300% elongation at cm) and immediately recovered to zero stress at the same rate. Other samples of this sheet exhibit an average tensile strength of 700 psi (49 Kg/cm ² ) at 900% elongation in the stress-strain-to-break test.
No yield point is observed in these determinations. The combined ethylene content is
¹³ Decided by C _onr ; Tanaka and Hatada,
J. Polym. Sci., Polym. Chem. Ed., 11 2057 (1973).
reference. Tg is determined from the dsc curve: Ke (above),
See p350.

[Brief explanation of drawings]

The accompanying drawings show the elastic polymer, a component of the present invention, produced according to Reference Example 1 and the commercially available highly isotactic polypropylene (Pro-
Fax6523) shows the stress-strain curve.

Claims (1)

[Claims] 1. has a main melting point between 135 and 155°C, has an intrinsic viscosity of 1.5 and 9, exhibits no yield point, has a residual elongation not exceeding 150%, and has a residual elongation of not more than 1.50. 10 to 80% by weight of a diethyl ether soluble fraction having an intrinsic viscosity of greater than The formed film is composed of about 5 to 95 parts by weight of a separable elastic polypropylene that exhibits birefringence when viewed under a crossed Nicol prism under a polarizing microscope at about 25°C and about 95 to 5 parts by weight of a highly isotactic polypropylene. A polypropylene composition consisting essentially of a blend. 2. The polypropylene composition of claim 1 consisting essentially of a blend of about 60 to 95 parts by weight of said elastic polypropylene and about 40 to 5 parts by weight of said highly isotactic polypropylene.