WO1988000222A1 - Compositions d'asphalte modifiees - Google Patents

Compositions d'asphalte modifiees Download PDF

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Publication number
WO1988000222A1
WO1988000222A1 PCT/US1987/001474 US8701474W WO8800222A1 WO 1988000222 A1 WO1988000222 A1 WO 1988000222A1 US 8701474 W US8701474 W US 8701474W WO 8800222 A1 WO8800222 A1 WO 8800222A1
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WO
WIPO (PCT)
Prior art keywords
asphalt
weight
composition
polymer
modified
Prior art date
Application number
PCT/US1987/001474
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English (en)
Inventor
H. Richard Miller
Original Assignee
The Lubrizol Corporation
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by The Lubrizol Corporation filed Critical The Lubrizol Corporation
Publication of WO1988000222A1 publication Critical patent/WO1988000222A1/fr

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Classifications

    • CCHEMISTRY; METALLURGY
    • C08ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
    • C08LCOMPOSITIONS OF MACROMOLECULAR COMPOUNDS
    • C08L95/00Compositions of bituminous materials, e.g. asphalt, tar, pitch

Definitions

  • modified asphalt composi- tions and more particularly to modified asphalt composi ⁇ tions comprising asphalt and a minor amount, sufficient to reduce or retard degradation of the asphalt in service, of at least one polymer having a weight average molecular weight (Mw) of about 5,000 to about 1,000,000.
  • Mw weight average molecular weight
  • the modified asphalt compositions are useful in a variety of applications including roofing and paving.
  • the modified asphalts are useful particularly in preparing improved asphalt concrete compositions for paving compositions.
  • asphalt or "asphalt cement” as used in the description of the present application refers to any of a variety of solid or semi-solid materials at room tempera ⁇ ture which gradually liquify when heated, and in which the predominant constituents are naturally occurring bitumens of which are obtained as residue in petroleum refining.
  • Asphalt is further defined by Kirk-Oth er, Encyclopedia of Chemical Technology, Vol. 3, Third Ed. (1978) pp. 284-327, John Wiley & Sons, New York. An additional discussion appears in the publication entitled “A Brief Introduction to Asphalt and Some of its Uses", Manual Series No. 5 (MS-5) , The Asphalt Institute, 7th Ed., September, 1974. Both of these references are hereby incorporated by reference.
  • Asphalt cements have found particular utility when combined with aggregates. Such combinations, generally referred to as "asphalt concrete", are employed exten ⁇ sively as paving compositions for roads, roofs, driveways, parking lots, airport runways, etc.
  • the asphalt is converted to a fluid state when paving a road.
  • One fluid form is the suspension or emulsion of the asphalt in water.
  • water evaporates or separates, and the asphalt hardens into a continuous mass.
  • Another form of asphalt employed in road construction is a cutback,i.e., a liquid petroleum product produced by fluxing an asphaltic base with a suitable organic solvent or distillate.
  • a road is formed by paving the aggregate-containing cutback and evaporating the volatile distillate from the mass.
  • the asphalt and aggregate can be mixed and applied at elevated temper ⁇ atures at the fluid state of the asphalt to form the road.
  • This form of asphalt which is neither cut-back nor emulsified generally is referred to as asphalt cement.
  • the degree and rate of hardening of asphalt cement during application and while in service are factors affecting the durability of a surface such as a road pavement.
  • a certain amount of hardening of a freshly applied surface is often desirable in order to allow the newly placed surface to be placed into service quickly.
  • excessive hardening and loss of ductil ⁇ ity of an asphalt based surface can dramatically reduce its useful lifetime.
  • compositions contain ⁇ ing bitumen, olefin polymers, a basic substance and sulfur. These compositions are useful as sealing com ⁇ pounds and for the production of sheeting and film.
  • the softening point of asphalt can be increased by incorporat ⁇ ing into the asphalt a liquid polyolefin oil.
  • U.S. Patent 3,703,393 a method is described for increasing the softening point and increasing the penetration of an air-blown asphalt by mixing the asphalt with a liquid polyolefin oil having an average molecular weight of 500-2000.
  • U.S. Patent 4,166,049 describes a process of provid ⁇ ing a rubberized asphalt from reclaimed rubber produced from whole scrap tires suitable for use in road and highway construction.
  • Mw weight average molecular weight
  • the modified asphalt composition will contain from about 0.01 to about 10% by weight, based on the weight of the asphalt, of the polymer as defined.
  • the modified asphalt compositions of the present invention are useful in roofing and in preparing aggregate-containing asphalt concretes which can be employed as paving compositions.
  • the present invention relates to modified asphalt compositions, and more particularly, to modified asphalt compositions such as asphalt cements which, when combined with aggregates, will form asphalt concretes exhibiting significantly improved physical properties, and, in particular, desirable age-hardening characterisitcs.
  • modified asphalt compositions such as asphalt cements which, when combined with aggregates, will form asphalt concretes exhibiting significantly improved physical properties, and, in particular, desirable age-hardening characterisitcs.
  • the asphalts which can be modified in accordance with the invention include natural asphalts and petroleum tar (petroleum asphalt) which is generally known for roofing and paving applications.
  • the natural asphalt includes, for example, asphaltite such as gilsonite, grahamite and glance pitch; lake asphalt such as trinidad asphalt; and rock asphalt.
  • the petroleum asphalts include straight asphalt obtained by distillation of a crude oil (unblown and substantially unoxidized) , blown asphalt produced by blowing an oxygen-containing gas into a straight asphalt in the presence or absence of a catalyst, solvent- extracted asphalt obtained when asphaltic material is separated from the petroleum fraction containing it by the use of propane or other solvents, and cut-back asphalt which is a mixture of straight asphalt and a light petro- leum solvent.
  • the petroleum tars that may be modified include oil gas tar obtained as a by-product when gases are produced from petroleum fractions, such tar in refined form, cut-back tar obtained by mixing a light petroleum fraction with such tar, and tar pitch obtained as a residue by removing the volatile fraction from such tar.
  • asphalt cement refers to any of a variety of substantially unblown or unoxidized solid or semi-solid materials at room temperature which gradually liquify when heated. Its predominant constitu ⁇ ents are bitumens, which may be naturally occurring or obtained as the residue of refining processing.
  • the asphalt cements are generally characterized by a penetra ⁇ tion (PEN, measured in tenths of a millimeter, dmm) of less than 400 at 25°C, and a typical penetration is between 40 and 300 (ASTM Standard, Method D-5) .
  • PEN penetra ⁇ tion
  • ASTM Standard Standard
  • Asphalt cements are often defined in terms specified by the American Association of State Highway Transporta ⁇ tion Officials (AASHTO) AR viscosity system. Two sets of typical specifications are as follows. AASHTO M-226
  • Bitumens or asphalts are modified in accordance with the procedure of the invention by incorporating therein (B) a minor property improving amount, sufficient to reduce or retard degradation of the asphalt in service, of at least one polymer which is a homopolymer of a non- aromatic mono-olefin having at least 3 carbon atoms, or a copolymer of said non-aromatic mono-olefin with an aromat ⁇ ic mono-olefin, said polymer having a weight average molecular weight (Mw) of about 5,000 to about 1,000,000 as determined by gel permeation chromatography.
  • Mw weight average molecular weight
  • homopolymers can be prepared from non-aromatic mono-olefins having at least 3 carbon atoms and preferably no more than 20 carbon atoms by a number of polymerization techniques well known to those of skill in the art. It should be noted that "homopolymer” as used herein, describes polymers made from mono-olefins having the same number of carbon atoms. Thus, polymers made from a mixture of butene-1 and isobutylene are, in the terms of this specification and the appended claims, homopolymers of butylene.
  • polyisobutylene polymer might contain units, 80% of which are derived from isobutylene, 15% from 1-butene and 5% from 2-butene.
  • homopolymers made from C_ and C 2Q mono-olefins such as propene, 2-butene r isobutene, 1-hexe ⁇ e, 3-decene, 4-tetradecene, etc. More preferable are homopolymers derived from C. to C g alpha-olefins such as butene, isobutene, 1-pentene, 1-heptene, etc. The most preferred homopolymers are those of propene and the various butenes.
  • the polymer (B) of the polymeric composition of this invention also may be copolymers of said non-aromatic mono-olefins with one or more aromatic olefins.
  • Copolymers containing at least 50% by weight of said non-aromatic olefin and up to about 50% by weight of an aromatic olefin are useful.
  • the aromatic olefins are preferably vinyl aromatic monomers of up to 12 carbon atoms including styrene and substituted styrenes such as the methyl styrenes, alpha-halostyrenes, lower alkyl- substituted styrenes such as alpha-methylstyrene, alpha- ethylstyrene, para-tert-butylstyrene and para-lower alkoxystyrenes.
  • a particularly convenient technique for polymerizing such olefins for use in this invention is through the use of a Lewis acid catalyst such as aluminum chloride, boron trifluoride, titanium tetrafluoride and the like. These polymerizations are well known in the art and need not be described further at this point.
  • the polymer that is useful in the compositions of the present invention is a polyisobutene of Mw 53,500.
  • the homopolymers of the present invention i.e., component (B)
  • component (B) for reasons of oxidative stability, contain no more than 5% unsaturation on the basis of the total number of carbon-to-carbon covalent linkages present within an average molecule.
  • unsaturation can be measured by a number of means well known to those of skill in the art, such as infrared, NMR, etc. More preferably these polymers contain no discernable unsaturation.
  • a particularly preferred polymer meeting all of the above requirements is polyisobutene, although other polymers such as polypropylene may also prove equally useful and desirable.
  • Example 1 serve to illustrate the preparation of component (B) used in this invention and is not intended as limiting thereof.
  • Component (B) is produced in a continuous unit operation by reacting isobutylene in a butane-isobutylene environment using aluminum chloride catalyst at between -12 to -30°C. A portion of the reactor contents is withdrawn to determine the number average molecular weight and the reaction temperature is adjusted to obtain a number average molecular weight in the range of 75,000 to 130,000. Methylamyl alcohol is added to destroy the activity of the aluminum chloride which is then removed as the stream is passed through a filter. Mineral oil is added and the polymer content (10-20% of the total stream) is removed and the balance of the stream (mainly unreacted isobutylene and butane) is combined with fresh (99% plus) isobutylene. A polyisobutylene of weight average molecu ⁇ lar weight of about 119,000 is obtained that contains 69% oil.
  • Example 2 To 68,800 parts of the oil-containing material prepared in Example 1 is added one part of an azo dye in an aromatic solvent that is manufactured by Morton Chemi ⁇ cal Company, Patterson, New Jersey? 150 parts of 2,6-di- t-butyl-p-cresol and 31,050 parts mineral oil. The contents are blended until a homogeneous liquid is obtained.
  • Asphalts modified in this manner exhibit improved age hardening characteris- tics and reduced deterioration.
  • the polymers will be mixed with asphalt in the fluid or molten condition to dissolve or disperse the polymer in the asphalt.
  • the asphalt is heated to an elevated temperature to improve the fluidity of the asphalt. Temperatures of from about 100-225°C are suffi ⁇ cient although the precise temperature for any particular asphalt will depend on the source and nature of the asphalt material.
  • the amount of the polymers in the modified asphalt compositions of the present invention is an amount which is sufficient to reduce or retard degradation of the asphalt in service. In one embodiment, the amount will vary from as little as 0.01% up to about 20% or more of the polymer based on the weight of the asphalt. General ⁇ ly, however, the amount of polymer will be less than about 10% by weight of the weight of the asphalt. Most often, the amount of polymer incorporated in the asphalt will range from about 0.2 to about 3% or 5% by weight.
  • the asphalt When mixing the polymers of the present invention with the asphalt material, the asphalt should be at an elevated temperature and in a flowable fluid state.
  • a suitable temperature is one at which the bitumen or asphalt is thinner than molasses at ambient temperature, typically thicker than water, and is flowable or pourable without stirring.
  • a quantity of the asphalt should be sufficiently fluid to flow when placed on a solid surface. This is particularly advantageous if it is contemplated that the asphalt cement would be circulated under high speed agitation to provide a uniform dispersion or solution.
  • a suitable mixing temperature is on the order of a minimum of about 100°C for soft asphalt, and, preferably, on the order of 120°C or more. At temperatures below this level, mixing times for total dispersion, even if feasible, become excessive economically. On the other hand, the temperature of mixing should not be so high as to promote other reactions which could weaken the asphalt material. For this reason, it is preferred not to heat the asphalt cement above about 225°C, and thus, suitable mixing temperatures are from about 100°C to about 225°C with a preferred mixing temperature of from 120-180°C depending upon the type of asphalt and the mixing times and speeds.
  • the modified asphalt compositions of the present invention are particularly useful for preparing improved roofing asphalts, other asphalt coating compositions, and particularly for preparing improved aggregate-containing asphalts such as employed in the paving of roads, roofs, bridges, airport runways, sidewalks, etc.
  • the modified asphalt compositions of the present invention in fluid form are mixed generally with preheated, predried aggre- gates to form the homogeneous mixture of uniformly coated aggregates in a paving composition, typically as performed at an asphalt mixing plant.
  • the aggregate preferably is heated under conditions of time and temperature to drive off essentially all free moisture prior to mixing.
  • both the aggregate and the modified asphalt are typically at temperatures of about 100-160°C.
  • the composition is spread on a road bed, compacted and permitted to cure. After curing, the road comprises aggregate bound by a matrix of modified asphalt binder.
  • the modified asphalt compositions of the present invention may also be useful for preparing improved seal coats.
  • a seal coat is generally applied as a hot asphalt cement, cutback asphalt cement, or emulsified asphalt cement.
  • the seal coat is generally applied at a rate of about 0.05 to about 0.8 gallons per square yard of surface. The preferred application rate is about 0.35 gallons per square yard of surface.
  • the liquid material is generally sprayed from a truck.
  • the aggregate is placed on top of the asphalt cement. Rolling or compact- ing the aggregate into the asphalt cement finishes the application.
  • the function of the seal coat is to prevent damage to paving surfaces by providing a barrier to exclude the admittance of moisture to the underlying surfaces.
  • the useful function of the addition of polymer to this barrier is determined by the physical/chemical nature of the polymer modifying the consistency of the asphalt cement. This consistency can be defined as incorporating viscosi ⁇ ty, stickiness, ductibility and flexibility. Certain polymers are used in the United States today to improve the aggregate retention. Based upon the data provided in the tables, the composition of this invention also provides that protection.
  • the modified asphalt compositions of the present invention after formation, may be handled by conventional techniques to maintain them in fluid form under road- building conditions.
  • the modified asphalts may be formed into a cutback by fluxing the asphalt with a suitable volatile solvent or distillate.
  • the modified asphalt cutback may then be directly mixed with aggregate and applied as a paving composition in fluid form, possi ⁇ bly at ambient temperatures.
  • Another conventional tech ⁇ nique for fluidizing the modified asphalt cement prior to mixing with aggregate and forming into a paving composi- tion is to emulsify the modified asphalt by known tech ⁇ niques.
  • An advantage of this method of fluidizing is that after mixing with the aggregate, it may be applied as a paving composition at ambient temperature.
  • the modifier may be added to a previously prepared asphalt cutback or asphalt emulsion.
  • aggregate as used in the specification and claims is intended to include solid particles having a range of sizes including fine particles such as sand to relatively coarse particles such as crushed stone, gravel or slag.
  • the ratio of aggregate to modified bitumen or asphalt depends upon their properties and the desired end use.
  • the paving composi ⁇ tion will comprise a minimum of about 85% by weight of aggregate, and generally between about 90-96% by weight of the total paving composition will be aggregate.
  • Aggregate containing modified asphalt compositions can be prepared in accordance with the present invention by techniques known to the art. In one method, a modified asphalt cement is prepared in accordance with the method of the present invention, and the modified asphalt cement thereafter is mixed with an aggregate at an elevated temperature to form the desired paving composition.
  • modified asphalt compositions of the present invention and the aggregate containing asphalt composi ⁇ tions prepared utilizing the modified asphalt compositions of the present invention are characterized by an ability to retain their desirable characteristics in service.
  • the modified asphalts of the present invention retain their consistency and ductility for longer periods in service than do asphalt compositions which have not been modified in accordance with the present invention.
  • the following examples illustrate the modified asphalt compositions and aggregate-containing compositions of the present invention.
  • Example A A California Valley asphalt cement (CV) meeting the specification of AASHTO AR 4000 is modified with 3% by weight based on the weight of the asphalt of the polymer of Example 2 (containing 78% oil) by thoroughly mixing the polymer with the fluidized asphalt.
  • CV California Valley asphalt cement
  • the above aggregate has a composition of 49.2% crushed Canadian limestone #8 and 50.8% lake sand.
  • Liquid asphalt cements treated with the compositions of the invention show major benefits in retained ductility and/or flexibility when exposed to severe aging as demon ⁇ strated by the California Tilt-Oven Asphalt Durability Test and the Thin Film Oven Test. Measurements of low temperature elastic modulus, after accelerating laboratory aging, show significant improvement with the presence of the polymer composition of the present invention.
  • the modified asphalt cement of Example A is exposed to oxidative conditions and compared to the test minimum.
  • the test employed is the Thin Film Oven Test (ASTM D- 1754-78) , a standard test method to evaluate the effect of heat and air on a film of semi-solid asphaltic material.
  • a film of asphaltic material is heated in a specially equipped convection oven for 5 hours at 325°F (163°C) .
  • the amount of hardening is determined from changes in physical test values as measured before and after oven treatment.
  • ASTM Procedure D-1754-78 is herein incorporat ⁇ ed by reference.
  • the modified asphalt cement of Example A also is subjected to the California Tilt-Oven Asphalt Durability Test developed by California Department of Transportation personnel in an effort to establish an accelerated labora ⁇ tory procedure to simulate field aging in hot climates.
  • the method, as well as data correlating laboratory and field aging, is published in the AAPT 1981 Proceedings.
  • the presentation is entitled "A Comparison of Field and Laboratory Environments on Asphalt Durability".
  • the authors are Glenn R. Kemp and Nelson H. Predoehl.
  • the test procedure is correlated to 24 months in a hot desert climate.
  • the method utilizes the apparatus required for ASTM D-2872-84 (Rolling Thin Film Oven Test) with slight modifications to age asphalt at 235°F (113°C) for 168 hours. These conditions simulate the effect of field weathering for two years in a hot desert site. The effects of this age hardening are determined from measure ⁇ ments made on the residue.
  • asphalt additives also may be included in the modified asphalt compositions of the inventio «,
  • organic manganese compounds such as manganese naphthenate, manganese acetate, manganese octoate either alone or in combination with organic cobalt compounds are useful in improving the high temperature properties and increasing compressive, flexural and fatigue strength of cured road pavements.
  • Asphalts containing such additives are described in U.S. Patent 4,234,346, and the specifi ⁇ cation of this patent is incorporated herein by reference for its disclosure of manganese and manganese cobalt additives for asphalt.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Civil Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Medicinal Chemistry (AREA)
  • Polymers & Plastics (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Road Paving Structures (AREA)

Abstract

Les compositions d'asphalte modifiées décrites comprennent (A) de l'asphalte, et (B) une petite quantité suffisante pour réduire ou retarder la dégradation de l'asphalte en service, d'au moins un polymère qui est dérivé d'une oléfine non aromatique ayant un poids moléculaire moyen (Mw) compris entre 5000 environ et 1.000.000 environ. Généralement, la composition d'asphalte modifiée contient de 0,01 environ à 10 % environ en poids, calculée d'après le poids de l'asphalte, du polymère défini ci-dessus. Les compositions d'asphalte modifiées de la présente invention sont utiles dans des applications de couverture de toiture et dans la préparation de béton asphaltique contenant des aggrégats, lesquels bétons peuvent être utilisés comme compositions de pavage.
PCT/US1987/001474 1986-06-27 1987-06-19 Compositions d'asphalte modifiees WO1988000222A1 (fr)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
US87986686A 1986-06-27 1986-06-27
US879,866 1986-06-27

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WO1988000222A1 true WO1988000222A1 (fr) 1988-01-14

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EP (1) EP0271565A1 (fr)
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Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0368452A2 (fr) * 1988-09-26 1990-05-16 Exxon Chemical Patents Inc. Compositions de revêtement bitumineuses
AU615741B2 (en) * 1988-05-09 1991-10-10 Ube Industries, Ltd. Asphalt composition for waterproof sheets
WO1996005716A2 (fr) * 1994-08-18 1996-02-29 Anatoly Alexeevich Bespalov Procede d'elimination de petrole ou de produits de petrole brut d'une surface et procedes de regeneration et d'utilisation du produit utilise

Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3144423A (en) * 1960-08-29 1964-08-11 Sun Oil Co Asphalt composition containing atactic polypropylene
FR2089370A5 (fr) * 1970-04-18 1972-01-07 Huels Chemische Werke Ag
DE2044107A1 (en) * 1970-09-05 1972-03-09 Ilseder Schlackenverwertung Dr. Schmidt & Co KG, 3152 Groß Büken Road surfacing mixtures - contg polyisobutene additive to minimise winter damage
DE2146902A1 (de) * 1971-09-20 1973-03-29 Paul Haberl Verfahren zur herstellung einer polypropylen enthaltenden mischung auf bitumen- bzw. asphaltbasis und mit der mischung hergestellter strassenbelag
FR2217393A1 (fr) * 1973-02-13 1974-09-06 British Petroleum Co
US3853800A (en) * 1973-01-05 1974-12-10 P Haberl Process for preparing a mixture containing a binder material and polyolefin
FR2358444A1 (fr) * 1976-07-13 1978-02-10 Veba Chemie Ag Melanges stables de polyolefines atactiques et de bitume

Patent Citations (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3144423A (en) * 1960-08-29 1964-08-11 Sun Oil Co Asphalt composition containing atactic polypropylene
FR2089370A5 (fr) * 1970-04-18 1972-01-07 Huels Chemische Werke Ag
DE2044107A1 (en) * 1970-09-05 1972-03-09 Ilseder Schlackenverwertung Dr. Schmidt & Co KG, 3152 Groß Büken Road surfacing mixtures - contg polyisobutene additive to minimise winter damage
DE2146902A1 (de) * 1971-09-20 1973-03-29 Paul Haberl Verfahren zur herstellung einer polypropylen enthaltenden mischung auf bitumen- bzw. asphaltbasis und mit der mischung hergestellter strassenbelag
US3853800A (en) * 1973-01-05 1974-12-10 P Haberl Process for preparing a mixture containing a binder material and polyolefin
FR2217393A1 (fr) * 1973-02-13 1974-09-06 British Petroleum Co
FR2358444A1 (fr) * 1976-07-13 1978-02-10 Veba Chemie Ag Melanges stables de polyolefines atactiques et de bitume

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU615741B2 (en) * 1988-05-09 1991-10-10 Ube Industries, Ltd. Asphalt composition for waterproof sheets
EP0368452A2 (fr) * 1988-09-26 1990-05-16 Exxon Chemical Patents Inc. Compositions de revêtement bitumineuses
EP0368452A3 (fr) * 1988-09-26 1991-11-21 Exxon Chemical Patents Inc. Compositions de revêtement bitumineuses
WO1996005716A2 (fr) * 1994-08-18 1996-02-29 Anatoly Alexeevich Bespalov Procede d'elimination de petrole ou de produits de petrole brut d'une surface et procedes de regeneration et d'utilisation du produit utilise
WO1996005716A3 (fr) * 1994-08-18 2001-05-17 Anatoly Alexeevich Bespalov Procede d'elimination de petrole ou de produits de petrole brut d'une surface et procedes de regeneration et d'utilisation du produit utilise

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