US3244773A

US3244773A - Addition of trans-polybutadiene to prevent cold flow in cis-polybutadiene

Info

Publication number: US3244773A
Application number: US227031A
Authority: US
Inventors: Willie W Crouch
Original assignee: Phillips Petroleum Co
Current assignee: Phillips Petroleum Co
Priority date: 1962-09-28
Filing date: 1962-09-28
Publication date: 1966-04-05
Anticipated expiration: 1983-04-05

Description

United States Patent 3,244,773 I ADDITION OF TRANS-POLYBUTADIENE TO PRE- VENT COLD FLOW IN CIS-POLYBUTADIENE Willie W. Crouch, Bartlesville, Okla, assignor to Phillips Petroleum Company, a corporation of Delaware No Drawing. Filed Sept. 28, 1962, Ser. No. 227,031 2 Claims. (Cl. 260-894) This invention relates to a method for preventing or substantially reducing the tendency of cis-polybutadiene to cold flow. In one aspect, it relates to a novel composition containing cis-polybutad-iene and trans-polybutadiene, in which the tendency of cis-polybutadiene to cold flow is substantially reduced.

In recent years, a great deal of research work has been conducted in the field of olefin polymerization. Great advantages have been recently made in this field as the result of the discovery of new catalyst systems. These catalyst systems are often described as being stereospecific since they are capable of polymerizing monomers, particularly conjugated dienes', to a certain geometric configuration. One of the products which has attracted widespread attention because of its superior properties is a olybutadiene containing a high percentage, e.'g., at least 85 percent, of cis 1,4-addition. The physical properties of this high cis-polybutadiene are of such a nature that the polymer is particularly suitable for the fabrication of heavy duty tires and'other articles for which conventional synthetic rubbers have heretofore been comparatively unsatisfactory. However, in the processing of high cis-polybutadi'ene', particularly in packaging, shipping and storage, a certain amount of difficulty has been encountered because of the tendency of the polymer to cold flow when in the unvulcanized state. For example, if cracks or punctures develop in the package used in'storing the polymer, polymer will flow from the package with a resulting loss or contamination and sticking together of stacked packages. I

It is an object of this invention, therefore, to provide a method for eliminating or substantially reducing the tendency of cis-polybutadiene to cold flow when in the unvulcanized state. I

Another object of the invention is to provide a novel composition which contains cis polybutadiene and a minor amount of a trans-polybutadiene which prevents'or substantially reduces cold flow.

Other and further objects and advantages of the invention will become apparent to those skilled in the art upon consideration of the accompanying disclosure.

The present invention resides in the discovery that the tendency of cis-polybntadiene to cold flow can be reduced or substantially eliminated by blending the material with a trans-polybutad-iene. Broadly speaking, the composition of this invention comprises (1) a major amount of a cispolybutadiene containing at least 85 percent cis 1,4-addi tion, and (2) a minor amount of a trans-polybutadiene containing at least 70 percent trans 1,4-addition. Usually, the composition of this invention is prepared by blending with a cis-polybutadiene from 0.1 to 10.0 parts by weight of a tr'ans-polybutadiene per 100 parts by weight of the mixture of cis-polybutadiene and trans-polybutadiene. The blending operation is usually conducted at an elevated temperature, e.g., at a temperature in the range of 175 to 350 F. It is preferred to carry out the blending at a temperature in the range of 275 to 325 because the maximum reduction in cold flow is obtained when operating in this temperature range.

Any suitable method which will give a homogeneous blend can be used in blending the cis-polybutadiene with the trans-polybutadiene. A convenient method is to blend the materials on a roll mill, in a Banbury mixer, or similar kneading device. The mixing operation is conducted at an elevated temperature as specified herein-above. The mixing operation is continued for a period of time sufficient to obtain a homogeneous composition, e.-g., for a period in the range of about 30 seconds to 10 minutes or longer. In another method for blending the materials, solutions of the polymers in the hydrocarbon solvent are blended and the products are recovered by conventional means, such as by steam stripping, coagulation in an alcohol, such as isopropyl alcohol, or the like. After the blending operation is completed, the polymer composition can then be packaged and stored or transferred for utilization elsewhere. The compositioncan be blended, cornpounded, fabricated and cured according to procedures which are well known in the rubber art.

The trans-polybutadiene used in the present composition contains a high percentage, e.-g., at least percent, of trans 1,4-addition. A trans-polybntadiene suitable for use contains from about 70 to 95 percent and higher of trans l,4-addition, the remainder of the polymer being formed by l,2-addition and cis 1,4-addition. The amount of unsaturation other than trans-unsaturation present in the polymers appears to be immaterial. It is tobe understood that the present invention is, in general, applicable to any synthetic polybutadiene in which the above-mentioned percentage of the polymer is formed by trans 1,4- addition of the monomer. v v

The present invention is applicable to blends of cispolybutadiene and trans-polybutadiene regardless of the method employed in preparing the polymers. One method that can be advantageously utilized in preparing the trans-polybutadiene comprises the step of polymerizing 1,3-butadiene in the presence of a catalyst composition comprising (a) a complex aluminum hydride of an alkali metal, such as lithium aluminum hydride, and (b) titaniumtetraiodide. The amount of the hydride used in the catalyst composition is usually in the range of 0.5 to 6 moles per mole of titanium tetraiodide with a preferred mole ratio being from 1.3 to 3.0. The polymerization is generally carried out at a temperature in the range of 10 C. to C. in the presence of an inert hydrocarbon diluent. Diluents suitable for use include aromatics, such as benzene and toluene, and paraffins, such as normal pentane and isooctane. It is frequently preferred to charge the complex aluminum hydride to the reactor as a solution in a dialkyl ether, such as diethyl ether. This method of preparing transapolybutadiene is described in detail by R. P. Zelinski and D. R. Smith in US. Patent :No. 3,050,513.

The present invention is generally applicable to polybutadienes containing a high percentage of cis 1,4-addition. It is usually preferred that this cis-polybutadiene contain at least percent, cis 1,4-addition, e.g., 85 to 98 percent and higher. The cis-polybutadiene can be prepared by polymerizing 1,3-butadiene with any one of a large number of different stereo-specific catalyst systems. It is usuallypreferred to employ a catalyst which is selected from the group consisting of (1) a catalyst comprising an organornetal compound having the formula R M, wherein R is an alkyl, cycloalkyl, aryl, alkaryl, aralkyl, alkylcycloalkyl, cycloalkylalkyl, arylcycloalkyl or cycloalkylaryl radical, M is aluminum, mercury, zinc, beryllium, cadmium, magnesium, sodium or potassium, and m is equal to the valence of the metal M, and titanium tetraiodide, (2) a catalyst comprising an organometal compound having the formula R M', wherein R is an organo radical as defined above, M is aluminum, magnesium, lead, sodium or potassium, and n is equal to the valence of the metal M, titanium tetrachloride and titanium tetraiodide, (3) a catalyst comprising an organometal compound having the formula R M", wherein R is an organo radical as defined above, M" is aluminum or magnesium and a is equal to the valence of the metal M", a compound having the formula TiX wherein X is chlorine or bromine and b is an integer from 2 to 4, inelusive, and elemental iodine, (4) a catalyst comprising an organometal compound having the formula R M', wherein R is an organo radical as defined above, M"I is aluminum, gallium, indium or thallium, and x is equal to the valence of the metal M', a titanium halide having the formula TiX wherein X is chlorine or bromine, and an inorganic halide having the formula M I wherein M is beryllium, zinc, cadmium, aluminum, gallium, indum, thallium, silicon, germanium, tin, lead, phosphorus, antimony, arsenic and bismuth, and c is an integer from 2 to 5, inclusive, and (5) a catalyst comprising an organo compound having the formula R M, wherein R, M' and x are as defined above, titanium tetraiodide, and an inorganic halide having the formula M X wherein M" is aluminum, gallium, indium, thallium, germanium, tin, lead, phosphorus, antimony, arsenic or bismuth, X is chlorine or bromine, and d is an integer from 2 to 5, inclusive. The R radicals of the aforementioned formulas preferably contain up to and including carbon atoms.

The following are examples of preferred catalyst systems which can be used to polymerize 1,3-butadiene to a cis 1,4-polybutadiene: triisobutylaluminum and titanium tetraiodide; triethylaluminum and titanium tetraiodide; triisobutylaluminum, titanium tetrachloride and titanium tetraiodide; triethylaluminum, titanium tetrachloride and titanium tetraiodide; diethylzinc and titanium tetraiodide; dibutylmercury and titanium tetraiodide; triisobutylaluminum, titanium tetrachloride and iodine; triethylaluminum, titanium tetrabromide and iodine; n-amylsodium and titanium tetraiodide; phenylsodium and titanium tetraiodide; n-butylpotassium and titanium tetraiodide; phenylpotassium and titanium tetraiodide; n-amylsodium, titanium tetrachloride and titanium tetraiodide; triphenylaluminum and titanium tetraiodide; triphenylaluminum, titanium tetraiodide and titanium tetrachloride; triphenylaluminum, titanium tetrachloride and iodine; tri-alpha-naphthylaluminum, titanium tetrachloride and iodine; tribenzylaluminum, titanium tetrabromide and iodine; diphenylzinc and titanium tetraiodide; di-Z-tolylmercury and titanium tetraiodide; tricyclohexylaluminum, titanium tetrachloride and titanium tetraiodide; ethylcyclopentylzinc and titanium tetraiodide; tri(3-isobutylcyclohexyl)aluminum and titanium tetraiodide; tetraethyllead, titanium tetrachloride and titanium tetraiodide; trimethylphenyllead, titanium tetrachloride and titanium tetraiodide; diphenylmagnesium and titanium tetraiodide; di-n-propylmagnesium, titanium tetrachloride and titanium tetraiodide; dimethylmagnesium, titanium tetrachloride and iodine; diphenylmagnesium, titanium tetrabromide and iodine; methylethylmagnesium, and titanium tetraiodide; dibutylberyllium and titanium tetraiodide; diethylcadmium and titanium tetraiodide; diisopropylcadmium and titanium tetraiodide; triisobutylaluminum, titanium tetrachloride, and antimony triiodide; triisobutylaluminum, titanium tetrachloride and aluminum triiodide; triisobutylaluminum, titanium tetrabromide and aluminum triiodide; triethylaluminum, titanium tetrachloride and phosphorus triiodide; tri-n-dodecyaluminum, titanium tetrachloride and tin tetra- Cir iodide; triethylgallium, titanium tetrabromide and aluminum triiodide; tri-n-butylaluminum, titanium tetrachloride, and antimony triiodide; tricyclophenylaluminum, titanium tetrachloride, and silicon tetraiodide; triphenylaluminum, titanium tetrachloride, and gallium triiodide; triisobutylaluminum, titanium tetraiodide and tin tetrachloride; triisobutylaluminum, titanium tetraiodide and antimony trichloride; triisobutylaluminum, titanium tetraiodide and aluminum trichloride; triisobutylaluminum, titanium tetraiodide, and tin tetrabromide; triethylgallium, titanium tetraiodide, and aluminum tribromide; triethylaluminum, titanium tetraiodide, and arsenic trichloride; and tribenzylaluminum, titanium tetraiodide, and germanium tetrachloride.

The polymerization process for preparing cis-polybutadiene is carried out in the presence of a hydrocarbon diluent which is not deleterious to the catalyst system. Examples of suitable diluents include aromatic, paraffinic, and cycloparaffinic hydrocarbons, it being understood that mixtures of these materials can also be used. Specific examples of hydrocarbon diluents include benzene, toluene, n-butane, isobutane, n-pentane, isooctane, n-dodecane, cyclopentane, cyclohexane, methylcyclohexane, and the like. It is often preferred to employ aromatic hydrocarbons as the diluent.

The amount of the catalyst used in preparing the cispolybutadiene product can vary over a rather wide range. The amount of the organometal used in the catalyst composition is usually in the range of 0.75 to 20 mols per mol of the halogen-containing component, i.e., a metal halide with or without a second metal halide or elemental iodide. The mol ratio actually used in a polymerization will depend upon the particular components employed in the catalyst system. However, a preferred mol ratio is generally from 1:1 to 12:1 of the organometal compound to the halogen-containing component. When using a catalyst comprising an organometal compound and more than one metal halide, e.g., titanium tetrachloride and titanium tetraiodide, titanium tetrachloride or tetrabromide and aluminum iodide, the mol ratio of the tetrachloride or tetrabromide to the iodide is usually in the range of 0.05:1 to 5:1. With a catalyst system comprising an organometal compound, a titanium chloride or bromide and elemental iodine, the mol ratio of titanium halide to iodine is generally in the range of 10:1 to 0.25:1, preferably 3:1 to 0.25:1. The concentration of the total catalyst composition, i.e., organometal and halogen-containing component, is usually in the range of 0.01 to 10 weight percent, preferably in the range of 0.01 to 5 weight percent, based on the total amount of 1,3-butadiene charged to the reactor system.

The process for preparing cis-polybutadiene can be carried out at temperatures varying over a rather wide range, e.g., from-400 to 250 F. It is usually preferred to operate at a temperature in the range of -30 to F. The polymerization reaction can be carried out under auto'genous pressure or at any suitable pressure sutficient to maintain the reaction mixture substantially in the liquid phase. The pressure will thus depend upon the particular diluent employed and the temperature at which the polymerization is conducted. However, higher pressures can be employed if desired, these pressures being obtained by some such suitable method as the pressurization of the reactor with a gas which is inert with respect to the polymenization reaction.

Various materials are known to be detrimental to the catalyst employed in preparing the ci-s-polybutadiene. These materials include canbon dioxide, oxygen and water. It is usually desirable, therefore, that the butadiene and the diluent be freed of these materials as well as other materials which may tend to inactivate the catalyst. Furthermore, it is desirable to remove air and moisture from the reaction vessel in which the poly merization is to be conducted.

Upon completion of the polymerization reaction, the

. reactionmixture: is .then treatcdto inactivatethe catalyst aand recovcr the rubbery.- lymer. A: suitable method of accomplishing -.th-is result involves steam stripping the diluent *from thepolymer. .-In another suitable method,. a catalyst inactivating materiaLsu'ch as an alcohol, is added to --the=mi-xture so as to inactivate'thc catalyst and cause precipitation of the polymer. .Thepolymcr is'then se-paratcdi from' the alcohol and diluent. by any suitable means, h such as dccantation of filtration. .lthas been found to. be .-:aldvantageous toadd an antioxidant, such. as. 4,4-methylene-lbis-(2,6-di=tert-bu-tylphenl), to the polymer solution prior to recovery of the polymer. The polymer which has been recovered by. these methods is then treated in accordance with the present invention so as to reduce the tendency of 'the polymer 1 to cold flow.

. "A more comprehensive understandingof the invention may. be obtained byrc'ferringto the-following illustrated "6 EXAMPLE A seriesco-f'runswas carired'" out in-Which-varying amounts of a trans-po1ybutadienewereblended'with a cispolybutadiene. The .cis-polybutadicne; employcdpin the runs was prepared bypolymcrizing; 1,3.-butadiene;inthe presence of a catalyst obtained-by. mixingtriisobutylalu- -minu m, titanium tetrachloride. and: free. iodine. 'The cis-p olybutadienei product contained-about 95 t percent; ois

1,4-addition. The trans-polybutadiene=-used -.wasprepared by polymerizing l,3 butadiene-withza catalyst consisting of an. ether solution. of:lithiumialuminumhydride and titanium tetra-iodide. The" trans-poly butadiene :contained aboutx90 pcrcenttrans 1,4-addition.

' Blending. of the polymers was: carried out in B-an bury mixer. The -dump' temperature was; measurcdin each 1 run and the cold flow properties ofathe zblcnds. determined.

Portions of the blendedstookewere co-m'poundedima 12 52 23 gi -ii -gg however to undiuly I tread recipe and the physical properties were determined. The results obtained 'in- .these runs are shown below in the table.

TABLE Run No 1 2 3 4 5 6 7 8 9 10 11 Ois-polybutadine, Parts by Wt 95 95 95 96 97 98 99 99. 5 99. 75 100 100 Trans-polybutadiene, Parts by Wt- 5 5 5 4 3 2 1 0.5 0.25 Banbnry Dump Temp, F. 200 260 310 310 310 305 305 310 320 305 No mixing Mix Time, Min 0. 75 1. 75 3. 0 2. 5 2. 2. 1 2. 2 2. 1 2. 3 2. 0 Mooney, (ML-4 at 212"v F.) 2 42 36. 5 36 38 38 38 38 38 38 40 Cold-Flow 3 3. 4 2. 22 1. 8S 2. 58 3. 02 3. 51 3. 96 4. 04 3. 77 4. 39 5. 51

COMPOUNDING AND PHYSICAL PROPERTIES Carbon Black 50 50 50 50 50 50 50 50 50 50 Zinc Oxide 3 3 3 3 3 3 3 3 3 3 3 Stearic Acid. 2 2 2 2 2 2 2 2 2 2 2 Philrich 5 10 10 10 10 10 10 10 10 10 10 10 Flexamine 1 1 l 1 1 1 1 l 1 1 l Sulfur 1. 1. 75 1. 75 1. 75 1. 75 1. 75 1. 75 1. 75 1. 75 1. 75 1. 75 NOBS Special 6 1. 1 1. 1 1. 1 1. 1 1. 1 1. 1 1. 1 1. 1 1. l l. 1 1. 05

PROCESSING DATA Mooney (MS-1% at 212 F.) 2 43. 7 41. 0 41.0 .0 41.3 .7 41. 4 41.2 41. 0 40. 8 42. 2 Extrusion at 250 F; 1 I

In. min 43 38. 5 35 34.8 35. 8 35. 2 35. 0 35.0 33. 5 35.0 41, 5 g. min 108 98 93 91. 5 93. 5 92. 5 90. 5 92. 5 89. 5 92 103 Rating (Garvey Die) 7+ 7+ 7+ 8- 7+ 8- 8- 8 8- 8- 8- PHYSICAL PROPETIES (30 MIN. CURE AT 307 F.)

n X 10 4 moles/cc. 1.87 1. 1. 1.87 1. 87 1. 92 1. 93 1. 95 1. 90 1. 92 l. 90 300% Modulus, p.s.i. 1, 020 1, 1, 1, 080 1, 050 l, 080 1, 000 1, 000 960 1, 020 1, 030 Tensile, p.s.i. 2, 570 2, 310 2, 675 2, 555 2, 590 2, 370 2, 460 2, 495 2, 490 2, 450 2, 635 Elongation, Percent 54 48 545 530 550 480 52 510 510 510 520 Tear Strength, lb./incli 190 225 195 100 205 165 180 170 Heat Build-up, T., F." 48. 7 47. 6 47. 6 47. 3 46. 9 46. 9 46. 9 45. 6 45. 3 46. 3 46. 9 Resilience, Percent 74. 4 74. 6 75. 9 75. 3 75. 9 75. 3 75. 8 77. 2 76. 4 77.7 74. 4 Blowout, Min)- l5. 8 14. 1 11. 1 13. 4 9. 7 8. 9 10.8 14. 6 12. 6 12. 8 13. 8 Shore A Hardness 14 60.0 59.5 59.0 58. 5 58. 5 59.0 58. 5 59.0 58. 5 58. 5 59. 0

The temperature oi the blend upon completion oi the mixing operation.

2 ASTM D-297-55T.

3 Cold-Flow-Glass Plate Method. Method is based on the change in contact area oi tour right circular cylinders of rubber compressed between two glass plates. The cold flow rating is the ratio of the final contact area to the original contact area. Four pellets, approximately 0.450 inch in diameter and the same in height, are measured with a hand micrometer and recorded as thonsandths of an inch. The average diameter is obtained and squared. Glass plates 3 x 4 Weighing an average of 26-27 grams, which have been cleaned and polished with silicone lens tissues, are used for the test. Four rubber pellets are positioned at the corner of 1.5 x 2 rectangle within the glass plate. Another glass is positioned over the top of the pellets such that it is directly over the bottom plate and a 160 gram 3 x 4 lead plate is placed on top. The assembly is allowed to stand 18 hours at 80 F. after which the lead weight is removed and the contact area observed through the glass plate. Measurement is is first taken across the longest dimension of the contact area and a second measurement taken at right angles to the first one. The eight measurements (two for each pellet) are recorded and averaged to obtain a final average diameter. The value is squared and divided by the initial average diameter squared to obtain the cold flow.

4 Aromatic oil.

5 Physical mixture containing 65 percent of a complex diarylaminekctone reaction product and 35 percent of N,N-diphenyl-p-phenylenediamine.

6 N-oxydiethylene-Z-benzothiazyl sulienamide.

Extrusion is carried out at 250 F. by essentially the same procedure as described by Garbey et al., Inc. & Eng. Chem. 34, 1309 (1942). As regards the rating figure, l2 designates an extruded product considered to be periectlyformed whereas lower numerals indicate less perfect products.

3 Determined by the swelling method of Kraus as given in Rubber World, October, 1946. This value is the number of efiective network chains per unit volume of rubber. The higher the number, the more the rubber is crosslinked (vulcanized).

Z ASTM D4l2-51T. Scott Tensile Machine L-fi. Tests made at 10 ASTM D62454. Die A. 11 ASTM D6 2352T. Method A, Goodrich Flexometer, 143 lbs/sq. in. load, 0.175 inch stroke. Test specimen is a right circular cylinder 0.7 inch in diameter and 1 inch high.

ASTM D94555 (modified). Yerzley oscillograph. Test specimen is a right circular cylinder 0.7 inch in diameter and 1 inch high.

Goodrich Flexometer, 257 lbs/sq. in. load, 0.250 inch stroke, 200 F. oven temperature. Reported as running time to failure of test specimen.

14 ASTM D676-55T. Shore Durometer, Type A.

The data in the foregoing table show that a substantial reduction in the tendency of cispolybutadiene to cold flow is obtained by blending the polymer with a small amount of trans-polybutadiene. The physical properties of the vulcanizates were good at all levels, reaching a maximum in most instances at the point of greatest lowering in cold flow. Incorporation of the small amounts of trans-polybutadiene did not adversely effect the physical properties of the cis-polylbutadiene, and in many instances actually improved certain properties.

The composition of this invention is suitable for all uses for which the cis-polyvbutadiene per se can be employed. It is particularly useful in the manufacture of tire treads, tire carcass stocks, and other rubbery articles. It can be extruded, reinforced with conventional reinforcing agents, blended with other polymers, such asnatural and synthetic rubbers, extended with conventional extender oils, and vulcanized using recipes that are Well known in the rubber art.

As will be evident to those skilled in the art, many varitions and modifications of the invention can be practiced in view of the foregoing disclosure. Such variations and modifications are believed to come within the spirit and scope of the invention.

1. A rubbery, unvulcanized composition of matter comprising a blend of (1) a cis-poly butadiene containing at least 85 percent cis l,4-addition, and (2) from 0:1 to about 5 parts by weight of a trans-polybutadiene per 100 parts by weight of said cis-polybutadiene and said trans-polybutadiene said trans-polybutadiene containing at least percent trans 1,4-addition.

2. The composition of claim 1 in which said cis-polybutadiene contains from to 98 percent cis 1,4-addition and said trans-polybutadiene contains from 70 to percent trans 1,4-addition.

References Cited by the Examiner UNITED STATES PATENTS 3,050,513 8/1962 Zelinski et al. 26094.3 3,060,989 10/1962 R-ailsback et al. 260-455 3,166,609 1/1965 Wilder 260-894 SAMUEL H. BLECH, Primary Examiner.

WILLIAM H. SHORT, MURRAY TILLMAN,

Examiners.

Claims

1. A RUBBERY, UNVULCANIZED COMPOSITION OF MATTER COMPRISING A BLEND OF (1) A CIS-POLYBUTADIENE CONTAINING AT LEAST 85 PERCENT CIS 1,4-ADDITION, AND (2) FROM 0.1 TO ABOUT 5 PARTS BY WEIGHT OF A TRANS-POLYBUTADIENE PER 100 PARTS BY WEIGHT OF SAID CIS-POLYBUTADIENE AND SAID TRANS-POLYBUTADIENE SAID TRANS-POLYBUTADIENE CONTAINING AT LEAST 70 PERCENT TRANS 1,4-ADDITION.