This invention relates to bitumen compositions and methods for their preparation. More specifically, it relates to compositions of bitumen and polyolβfinβ, e.g. polyethylene or polypropylene, useful in adhesives, caulkings, sealants and the like, and as binders for mixing with inorganic aggregates such as stone, sand etc _* to form paving and other road construction materials.

It is nown in the prior art that polymeric materials may be dispersed in bitumen to form useful mixtures. Numerous examples may be found in the literature pertaining to the modification of bitumen with elastomers, block copoly ecs, polyolefins, vinyl polymers and the like. More recently it has been found that mixtures of polyethylene and bitumen possess qualities which are particularly suitable Cor use in paving mixtures. The polyethylene is reported to counteract the tendency of the bitumen to soften at elevated temperatures and to become brittle at low temperatures. Such compositions are described in U.S. patent 4,314,921 βiegensein and Canadian patent 1,066,831 Hemeran, for example. A disadvantage of such polyethylene - bitumen mixtures, however, is their tendency towards instability at elevated temperatures. Such mixtures are of the nature of emulsions, with the bitu βnt forming the continuous phase and the polyethylene forming the dispersed phase. The polyethylene (oc other similar polyolefin) is substantially insoluble in the

_b itumen, so that a two phase system can form. The low density polyethylene phase tends to rise to the surface of the liquified _b itumen at elevated temperatures and form a viscous layer which is difficult to redisperse. Such instability is of concern to potential users, since the separation could cause serious difficulties in handling and processing the mixtures during normal paving practice.

Moreover, on preparing such compositions, there is a large increase in viscosity of the mixture after addition of minor quantities of polyethylene, AS a result, the mixing times required for mixing the aggregate into the mixture in the hot mix paving process (usually in a pug mill) are lengthened, thus tending to increase the mixing power requirements and costs, and reduce the economic benefits _* It is an object of the present invention to provide novel bitumen•-- ^• poly lefin compositions which overcome or at least reduce one or more of these disadvantages.

In one aspect, the present invention provides bitu en-polyolefin compositions containing an emulsifying system or the polyolefin therein, which has the effect of stabilising the dispersion of polyolefin in the mixture and counteracting the tendency to phase separation. The emulsifying system comprises a polyolefin wax with a polymeric chain structure compatible with the polyolefin dispersed in the mixture, and having polar functional groups at one chain end. In one embodiment of the invention, the polyolefin wax terminal functional groups react or otherwise chemically associate with

subsequently added inorganic aggregate materials, to form a stabilized mixture therewith. In another, and preferred, embodiment, the emulsifier system additional includes an inorganic metal compound which will chemically associate with the polar functional groups of the polyolefin wax. The components of the emulsifying system associate together and with the polyolefin in the itumen-polyolefin mixture to create a stable dispersion containing discrete polyolefin particles therein. Not only does tne emulsifying system stabilise the dispersion, but also the polyolefin wax addition serves to reduce the viscosity of the mixture, hence reducing the mixing power requirements and rendering high mixing temperatures unnecessary. The resulting compositions are particularly suitable for use as bindrs, to be mixed with aggregates to form road construction materials.

Whilst it is not Intended that the invention should be limited to any particular theory or mode of action of the emulsifying system, it is believed that the polyolefin wax polymer chains associate with the polymer chains of the polyolefin of the mixture, with the hydrocaroon-incompatible polar headgroups thereof protruding outwardly from the polymer particles. In the absence of inorganic metal compounds, the polar groups form a protecting sheath around the polyolefin dispersed phase and subsequently react with added aggregates to stabilize the mixture. When a metal oxide is included as a part of the emulsifier system, the metal oxide reacts with oc otherwise chemically associates with the polar headgroups, so as

effec _t ively to encase the emulsified polyolefin particles in a sheath of inorganic material. As a result, reagglomeration of the polyethylene dispersion is effectively prevented or at least substantially hindered, and the density of the dispersed polyethylene particles in the bitumen is increased, so that they remain in suspension and do not rise to the surface.

Thus according to the present invention, in one aspect, there is provided a bitu βn-polyole in composition suitable for mixing with aggregates to provide paving compiβitions, said bitumen-polyolefin composition comprising a continuous bitumen phase and a dispersed polyolefin phase, the polyolefin phase being present therein as discrete regions stabilized with an emulsi ier system comprising a terminally functionaiized polyolefin wax having main polymeric chains compatible with the polyolefin of the dispersed phase. ^' Preferably, the emulsifier system also includes at least one inorganic metal compound in chemical association with the functional end groups of the polyolefin wax.

According to a second aspect of the present invention, there is provided a bitumen composition comprising bituminous binder and inorganic aggregates, the bituminous binder comprising a bitumen continuous phase, and a polyolefin dispersed phase, said bituminous binder also including an emulsifier system comprising a terminally functionaiized polyolefin wax, said polyolefin wax having main polymeric chains compatible with polyolefin dispersed phase.

According to a third aspect, there is provided a

process of preparing bitumen-polyole in compositions having a continuous bitumen phase and a dispersed polyolefin phase, which comprises mixing the bitumen and polyolefin in the presence of an emulsifier system for the polyolefin, said emulsifier system comprising a polyolefin wax having main polymeric chains compatible with the polyolefin of the dispersed phase and having functional end groups.

Preferably, the emulsifier system in all the various aspects of the invention, also includes at least one inorganic metal compound in chemical association with the functional end groups of the polyolefin wax, or capable of chemical reaction therewith.

The preferred polyolefin waxes for use in the emulsifier systems of the present invention have acidic functional end groups, to react with basic metal oxides, preferably used aβ the inorganic metal compound, when polyethylene is used as the polyolefin of the dispersed phase, as is preferred, the emulsifier has a polyethylene-compatible backbone chain. The polyolefin wax component of the emulsifier system preferably has a molecular weight of from about 200 to about 10,000. Its essential characteristics are a ain. olymeric backbone chain exhibiting a high degree of compatibility with the dispersed phase polyolefin, and functional end groups on one end of the polymeric chains. Preferably these functional end groups are acid groups such as cacboxyltc acid groups, so that ehy will react with basic inorganic metal oxides preferably chosen as the inorganic metal compounds of the emulsifier system

In one embodiment of the invention the polyolefin wax of the emulsifier system comprises a long chain fatty acid such as dodecanoic acid, tetradecanoic acid, hexadeσanoic acid, octadecanoic acid (stearic acid) for example, or an unsaturated fatty acid such as cis-9-hexadecenoic acid, cis-9-octadecenoic acid, cis-9,cis-l2-octadecadienoic acid, 9,11-octadecadienoic acid isomers, and cis-9, trans-ll, trans- 13-oσtadecatrienoic acid. Alternatively, the fatty acid may contain certain functional groups such as hydroxyl groups substituted on its Onon-ter inal carbon atoms, for example, l2-hydroxy-cis-9-octadecenoic acid, as long as the functional groups do not signi icantly detract from the compatibility with the polyolefin.

According to another and more preferred embodiment, however, the polyole in wax of the- emulsi ier system is a polyolefin wax of molecular weight 1,000 - 10,000, and having carboxyliσ acid terminal groups at one chain end. Preferred examples, when the dispersed phase of the binder is polyethylene, are maleated polyethylenes, or ethylene copolymers ₍ having the required degree of compatibility with the polyethylene of the binder. Materials of such molecular weights show a higher and more desirable degree of compatibility with the dispersed phase polyolefins of the binder. Maleated polyethylene waxes of such molecular weights are known and are commercially available, eg. under the trade mark EPOLfiNE (from Eastman Chemical Products Inc.), and under the trade mark S-17 from Nippon Petrochemicals Company.

Suitable copolymers include maleated copolymers of ethylene with vinyl acetate, propylene, l-butene or other alpha olefins, for example, or unsaturatβd copolymers of ethylene, e.g. EPDM elastomers. Alternatively, the polyolefin wax of the emulsifier system may comprise a low molecular weight polar wax derived from oxidized polyethylene.

It will thus be understood that the polyolefin wax of the emulsifier system should be partially soluble in the polyolefin, preferably polyethylene phase of the binder, such that the end polar substituent confers sufficient surface activity to cause the emulsifier system to accumulate preferentially at the interface between the emulsified particles and the suspending bitumen phase. Under such favourable conditions, the polar acid groups are accessible for reaction with basic metal oxides. While σarboκyl groups are favoured functional groups for this purpose, it will be readily recognised that most polar organic groups will preferentially adsorb or be attracted to inorganic particles by virtue of their inherent charge separation (polarity) . It is not essential that the inorganic particles react to form carboxylates or salts. The surface active emulsifying wax promotes the formation of an inorganic sheath surrounding each polyethylene particle, thereby preventing coalescence.

The metal component may be selected from the group including oxides, hydroxides, carbonates or silicates of magnesium, calcium, barium, iron, zinc, aluminum, silica, tin, lead, antimony, titanium or zirconium. Certain metal oxides.

hydroxides, carbonates or silicates that catalyse oxidation of the bitumen should be excluded. In addition to the above metal salts, one may use fly ash and mixed oxides or mixed silicates as may be obtained oy fine grinding of naturally occurring minerals. It will be apparent that the fine ground mineral component should be considerably smaller than the emulsified particles in order to form an adhering sheath at the interface. Thus the metal compound is preferably added at colloidal size ranges, e.g. 25 microns. Reactive metal oxides will evolve spontaneously from metal salts at the pσlyolβ in-bitumen interface. In an alternative procedure, the metal carboxylate derivatives of the polyolefin wax emulsifying agent may be employed directly, instead of creating the salt in-situ.

A preferred group of inorganic compounds are the basic metal oxides. Particularly preferred is ferric oxide. It has been found that ferric oxide confers on the system a high degree of moisture resistance, probably as a result of its ability to promote a high degree of adhesion between the bitumen of the binder and the subsequently added aggregate _* In any event, ferric oxide appears to be unique in its ability to prevent moisture from destroying the bond between the bitumen and the aggregate.

The relative proportions of bitumen, polyethylene modifier, emulsifying agent and metal compound (including oxides, hydroxides, silicates and carboxylates) may be varied through ratios according to the desired level of performance. For most purposes, the weight percentage of polyethylene should

be between about S and 20%, the polyolefin wax of the emulsifier system 0.5 to 5%, and the metal compound in the range of I to

10%, based on the total weight of binder. The exact concentration of each reagent depends upon several factors in addition to the stability such as the viscosity, low temperature performance and Marshall test values. The final concentration of polyethylene is preferably 5-10*.

As used herein, the term bitumen refers to viscous aromatic residues from petroleum sources (pitches) , and naturally occurring bitumens such as asphaltites, e.g. Gilsonite. To prepare the compositions of the present invention, techniques normally employed for preparing bitu en-polyolefin compositions may be employed.

The ingredients may be mixed in any particular sequence using a high speed stirrer with shearing ring, sig a blade mixer or mixing extruder. In the preferred method the bitumen and other ingredients are mixed together in a Brabender mixing head with counter rotating sigma blades. The concentration of the polyethylene is suitably initially near 50% by weight so that a concentrated dispersion of polyethylene in bitumen is produced after several minutes of mixing near l20 ^β C. The hot viscous mixture may be cooled and pelletized until ready for use. This peiletized concentrate may be further diluted in heated bitumen with an ordinary stirrer to form a smooth, 3tabie emulsion of desired concentration. The pellets are readily stored in bags or containers since they are quite stable and do not adhere to each other, maintaining a free flowing nature as in the case of

pelletized plastics materials. If preferred, the pellet concentrate may be added directly to the pug mill without intermediate dilution. In the pug mill, the concentrate is mixed with reinforcing aggregates and additional quantities of bitumen, ready for application to a surface.

Alternatively, the polyethylene may be dispersed in bitumen using a high speed shearing impeller of the silverson type. Under these conditions, the maximum concentration that can be easily controlled is approximately 10% by weight - polyethylene.

The polyolefin wax of the emulsifier system used in the compositions of this invention reduces the the viscosity of the mixture dramatically, so that larger concentrations of the polyethylene may be incorporated into the bitumen without adversely affecting the speed of mixing with aggregate in the pug mill. The process is applicable to all grades of bitumen, the grade of bitumen being selected according to end use e.g. paving requirements. The polyolefin is preferably polyethylene, but ethylene-propylene copolymers, especially those containing »t least 50% by weight of ethylene, and polypropylene, can also be used. The polyolefin may be waste or scrap polyethylenes or copolymers thereof.

While this invention discloses an improved method of dispersing polyethylenes in bitumen for paving applications, it will also be apparent that these mixtures will have utility in adhesive mixtures, caulks and sealants, potting resins, crack fillers, pot-hole fillers, mortars, coatings, weatherproofing

f a _b rics and paper s, roof ing shing les and mo lded goods. The invention is fu rthe r il lustrated in the following non-limiting specific examples.

Example.I Linear low density polyethylene (22.5 Exxon Escorene,

Melt Index 50 g/10 min. ) was mixed with bitumen (22.5 g Gulf Clarkson 85/100 Pen.) , maleated polyethylene wax (3 g Nippon Petrochemical sample) and ferric oxide (2 g Fisher Scientific reagent grade) in a Brabender Mixing Head (50 ml capacity) at 120 ^β C and 40 rp for 5 minutes. The hot mixture was poured onto an aluminum plate and allowed to cool to room temperature. The resulting sheet of bitumen containing dispersed polyethylene could be cut into small non-tacky pieces with scissors and stored for future use _* Portions o the concentrate were further diluted in heated bitumen (at 140*C) to concentrations of 6, 8, 10 and 12 percent polyethylene (by weight) using a standard laboratory stirrer. The suspensions were then placed in an air oven at 145 - 5 ^» C for at least six hours without agitation. After this period of time the liquid mixtures were removed from the oven and checked for signs of separation. In these examples the dispersions remained stable with no evident sign of separation. The dispersions remained smooth and glossy without the formation of a surface layer of polyethylene. Similar mixtures without added stabilizers tended to separate rapidly at temperatures above 140°C into a surface layer of polyethylene which was extremely viscous and impossible to redisperse.

Example 2

Linear low density polyethylene (22 g Exxon Escorene, Melt Index 50 g/10 min.) was mixed with bitumen (22 g Gulf Clarkson 80/100 Pen.), 3.5 g stearic acid (Fisher Scientific reagent grade) and 2.5 g ferric oxide (Fisher Scientific reagent grade) in a Brabender Mixing Head equipped with roller blades. The mixture was subjected to mixing at l60 ^β C and 100 rpm for 5 minutes before pouring the hot mixture onto an aluminum plate where it cooled into a tough film. After cooling to room temperature the film was cut into small pieces and further diluted with heated bitumen (at l40 ^a C) to 8% polyethylene (by weight) using a simple laboratory stirrer (a high speed stirrer is unnecessary) . The resulting dispersion was of smooth consistency with no observable particles therein _* A portion of the mixture was placed in a heated air oven at 145 ⁺ 5 ^β C for 6 hours without agitation to detect evidence of separation of the polyethylene. After six hours, reddish-orange oily droplets appeared on the surface of the mixture which were assumed to be excess stearic acid. However, these droplets were easily redispersed with a stirring rod to form a smooth, uniform mixture without any observable particles in suspension. As in Example I, the viscosity of the mixture was noticeably reduced in the presence of the dispersing agent, an important property which helps to promote rapid mixing with aggregates for paving applications.

Example 3

Linear low density polyethylene (22 g Exxon Escorene, Melt Flow Index 50 g/min.) was mixed with 22 g bitumen (Gulf Clarkson 80/100 Pen.) , 3.5 g maleated polyethylene wax (Nippon Petrochemical Co. sample, molecular weight 3800 g/mol) and 2.5 g calcium hydroxide (Fisher Scientific reagent grade) at l60 ^β C in a Brabender Mixing Head equipped with roller blades. After 5 minutes mixing at 100 rpm the liquid contents were poured onto an aluminum plate and the cooled sheet cut ^' into small pieces for further use. Portions of the concentrate were then diluted in additional bitumen at 140*C using a simple low speed laboratory stirrer to 8 percent polyethylene (by weight) . The diluted mixture was then placed in an air oven and allowed to stand for 6 hours at 145- 5*C in order to test the stability of the mixture with respect to separation of the polyethylene. Some slight segregation was observed after 6 hours but the particles were easily rβdispersed by gentle agitation to form a smooth, uniform mixture again. The viscosity of the mixture appeared to be greater than that of the ferric oxide system but considerbiy less than that of the unstabilized mixture.