CA2039486C - Using branched polymers to improve the storage stability of acid treated polymer modified asphalts - Google Patents
Using branched polymers to improve the storage stability of acid treated polymer modified asphalts Download PDFInfo
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- CA2039486C CA2039486C CA 2039486 CA2039486A CA2039486C CA 2039486 C CA2039486 C CA 2039486C CA 2039486 CA2039486 CA 2039486 CA 2039486 A CA2039486 A CA 2039486A CA 2039486 C CA2039486 C CA 2039486C
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- 229920000642 polymer Polymers 0.000 title claims abstract description 107
- 239000002253 acid Substances 0.000 title claims abstract description 69
- 239000010426 asphalt Substances 0.000 claims abstract description 99
- 239000000203 mixture Substances 0.000 claims abstract description 52
- 238000000034 method Methods 0.000 claims abstract description 29
- 150000007522 mineralic acids Chemical class 0.000 claims abstract description 13
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 claims description 25
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 claims description 20
- 229920001169 thermoplastic Polymers 0.000 claims description 15
- 229910000147 aluminium phosphate Inorganic materials 0.000 claims description 12
- -1 polyethylene, ethylene methacrylate Polymers 0.000 claims description 11
- 229920001187 thermosetting polymer Polymers 0.000 claims description 11
- 229920001971 elastomer Polymers 0.000 claims description 9
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 claims description 8
- 239000000806 elastomer Substances 0.000 claims description 8
- 239000004416 thermosoftening plastic Substances 0.000 claims description 8
- 239000004698 Polyethylene Substances 0.000 claims description 7
- DQXBYHZEEUGOBF-UHFFFAOYSA-N but-3-enoic acid;ethene Chemical compound C=C.OC(=O)CC=C DQXBYHZEEUGOBF-UHFFFAOYSA-N 0.000 claims description 7
- 239000005038 ethylene vinyl acetate Substances 0.000 claims description 7
- 229920001200 poly(ethylene-vinyl acetate) Polymers 0.000 claims description 7
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 claims description 7
- 229920000573 polyethylene Polymers 0.000 claims description 6
- 239000004814 polyurethane Substances 0.000 claims description 6
- 229920002635 polyurethane Polymers 0.000 claims description 5
- 239000004677 Nylon Substances 0.000 claims description 4
- 239000004642 Polyimide Substances 0.000 claims description 4
- 238000009835 boiling Methods 0.000 claims description 4
- 239000007789 gas Substances 0.000 claims description 4
- 229920001778 nylon Polymers 0.000 claims description 4
- 229920001721 polyimide Polymers 0.000 claims description 4
- 229920000181 Ethylene propylene rubber Polymers 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 3
- STVZJERGLQHEKB-UHFFFAOYSA-N ethylene glycol dimethacrylate Chemical group CC(=C)C(=O)OCCOC(=O)C(C)=C STVZJERGLQHEKB-UHFFFAOYSA-N 0.000 claims description 3
- 229910052760 oxygen Inorganic materials 0.000 claims description 3
- 239000001301 oxygen Substances 0.000 claims description 3
- 239000004636 vulcanized rubber Substances 0.000 claims 2
- 239000011230 binding agent Substances 0.000 abstract description 7
- 239000000463 material Substances 0.000 abstract description 4
- 238000000576 coating method Methods 0.000 abstract description 3
- 239000011248 coating agent Substances 0.000 abstract description 2
- 239000000047 product Substances 0.000 description 8
- 229920003023 plastic Polymers 0.000 description 5
- 239000004033 plastic Substances 0.000 description 5
- 239000012467 final product Substances 0.000 description 4
- 238000002156 mixing Methods 0.000 description 4
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 description 4
- WSFSSNUMVMOOMR-UHFFFAOYSA-N Formaldehyde Chemical compound O=C WSFSSNUMVMOOMR-UHFFFAOYSA-N 0.000 description 3
- 239000004702 low-density polyethylene Substances 0.000 description 3
- 229940099514 low-density polyethylene Drugs 0.000 description 3
- 239000003921 oil Substances 0.000 description 3
- 230000035515 penetration Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- 239000004709 Chlorinated polyethylene Substances 0.000 description 2
- 150000008064 anhydrides Chemical class 0.000 description 2
- 125000004432 carbon atom Chemical group C* 0.000 description 2
- 239000003085 diluting agent Substances 0.000 description 2
- YWEUIGNSBFLMFL-UHFFFAOYSA-N diphosphonate Chemical compound O=P(=O)OP(=O)=O YWEUIGNSBFLMFL-UHFFFAOYSA-N 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 229920001684 low density polyethylene Polymers 0.000 description 2
- 239000012188 paraffin wax Substances 0.000 description 2
- 238000005191 phase separation Methods 0.000 description 2
- 229920000728 polyester Polymers 0.000 description 2
- 239000005060 rubber Substances 0.000 description 2
- 238000005292 vacuum distillation Methods 0.000 description 2
- 229920002554 vinyl polymer Polymers 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-M Chloride anion Chemical compound [Cl-] VEXZGXHMUGYJMC-UHFFFAOYSA-M 0.000 description 1
- ZAMOUSCENKQFHK-UHFFFAOYSA-N Chlorine atom Chemical compound [Cl] ZAMOUSCENKQFHK-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 229920002943 EPDM rubber Polymers 0.000 description 1
- 244000043261 Hevea brasiliensis Species 0.000 description 1
- 229920000877 Melamine resin Polymers 0.000 description 1
- 239000004721 Polyphenylene oxide Substances 0.000 description 1
- 239000004734 Polyphenylene sulfide Substances 0.000 description 1
- XBDQKXXYIPTUBI-UHFFFAOYSA-M Propionate Chemical compound CCC([O-])=O XBDQKXXYIPTUBI-UHFFFAOYSA-M 0.000 description 1
- 229920006465 Styrenic thermoplastic elastomer Polymers 0.000 description 1
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 229920001807 Urea-formaldehyde Polymers 0.000 description 1
- 150000001241 acetals Chemical class 0.000 description 1
- UGZICOVULPINFH-UHFFFAOYSA-N acetic acid;butanoic acid Chemical compound CC(O)=O.CCCC(O)=O UGZICOVULPINFH-UHFFFAOYSA-N 0.000 description 1
- 229920006397 acrylic thermoplastic Polymers 0.000 description 1
- XECAHXYUAAWDEL-UHFFFAOYSA-N acrylonitrile butadiene styrene Chemical compound C=CC=C.C=CC#N.C=CC1=CC=CC=C1 XECAHXYUAAWDEL-UHFFFAOYSA-N 0.000 description 1
- 229920000122 acrylonitrile butadiene styrene Polymers 0.000 description 1
- 239000004676 acrylonitrile butadiene styrene Substances 0.000 description 1
- 239000000853 adhesive Substances 0.000 description 1
- 230000001070 adhesive effect Effects 0.000 description 1
- 229920003180 amino resin Polymers 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- FACXGONDLDSNOE-UHFFFAOYSA-N buta-1,3-diene;styrene Chemical compound C=CC=C.C=CC1=CC=CC=C1.C=CC1=CC=CC=C1 FACXGONDLDSNOE-UHFFFAOYSA-N 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 229920002301 cellulose acetate Polymers 0.000 description 1
- 229920006217 cellulose acetate butyrate Polymers 0.000 description 1
- 229920006218 cellulose propionate Polymers 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 150000001805 chlorine compounds Chemical class 0.000 description 1
- 239000011294 coal tar pitch Substances 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 229920001577 copolymer Polymers 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 239000010949 copper Substances 0.000 description 1
- 239000010779 crude oil Substances 0.000 description 1
- 230000001627 detrimental effect Effects 0.000 description 1
- 239000002270 dispersing agent Substances 0.000 description 1
- 239000006185 dispersion Substances 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 238000005187 foaming Methods 0.000 description 1
- IVJISJACKSSFGE-UHFFFAOYSA-N formaldehyde;1,3,5-triazine-2,4,6-triamine Chemical compound O=C.NC1=NC(N)=NC(N)=N1 IVJISJACKSSFGE-UHFFFAOYSA-N 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 238000007689 inspection Methods 0.000 description 1
- 229920000092 linear low density polyethylene Polymers 0.000 description 1
- 239000004707 linear low-density polyethylene Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000012528 membrane Substances 0.000 description 1
- 229920003052 natural elastomer Polymers 0.000 description 1
- 229920001194 natural rubber Polymers 0.000 description 1
- 239000003973 paint Substances 0.000 description 1
- 229920003229 poly(methyl methacrylate) Polymers 0.000 description 1
- 229920002492 poly(sulfone) Polymers 0.000 description 1
- 239000004417 polycarbonate Substances 0.000 description 1
- 229920000515 polycarbonate Polymers 0.000 description 1
- 229940068921 polyethylenes Drugs 0.000 description 1
- 229920002959 polymer blend Polymers 0.000 description 1
- ODGAOXROABLFNM-UHFFFAOYSA-N polynoxylin Chemical compound O=C.NC(N)=O ODGAOXROABLFNM-UHFFFAOYSA-N 0.000 description 1
- 229920000098 polyolefin Polymers 0.000 description 1
- 235000013824 polyphenols Nutrition 0.000 description 1
- 229920006380 polyphenylene oxide Polymers 0.000 description 1
- 229920001021 polysulfide Polymers 0.000 description 1
- 239000005077 polysulfide Substances 0.000 description 1
- 150000008117 polysulfides Polymers 0.000 description 1
- 229920002451 polyvinyl alcohol Polymers 0.000 description 1
- 235000019422 polyvinyl alcohol Nutrition 0.000 description 1
- 239000004800 polyvinyl chloride Substances 0.000 description 1
- 229920000915 polyvinyl chloride Polymers 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- SCUZVMOVTVSBLE-UHFFFAOYSA-N prop-2-enenitrile;styrene Chemical compound C=CC#N.C=CC1=CC=CC=C1 SCUZVMOVTVSBLE-UHFFFAOYSA-N 0.000 description 1
- 239000011435 rock Substances 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 239000000565 sealant Substances 0.000 description 1
- 229920002379 silicone rubber Polymers 0.000 description 1
- 230000000087 stabilizing effect Effects 0.000 description 1
- 229920000638 styrene acrylonitrile Polymers 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229920001897 terpolymer Polymers 0.000 description 1
- ISXSCDLOGDJUNJ-UHFFFAOYSA-N tert-butyl prop-2-enoate Chemical compound CC(C)(C)OC(=O)C=C ISXSCDLOGDJUNJ-UHFFFAOYSA-N 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 150000003673 urethanes Chemical class 0.000 description 1
- 238000004078 waterproofing Methods 0.000 description 1
Landscapes
- Addition Polymer Or Copolymer, Post-Treatments, Or Chemical Modifications (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Working-Up Tar And Pitch (AREA)
Abstract
This invention relates to a composition arid method for improving the storage stability of acid treated polymer modified asphalts. More specifically, the storage stability of an asphalt which contains greater than 1.0 wt.% polymer can be improved by adding a branched, rather than a non branched, polymer to an asphalt which has previously been reacted with an inorganic acid. The storage stable acid treated branched polymer modified asphalt thus produced is particularly well suited for use as a binder in paving materials and as a coating or saturant for roofing shingles.
Description
'- "
BACKGROUND OF THE INVENTTON
1. Field of the Invention This invention concerns a composition and method for improving the storage stability of said treated polymer modified asphalts using branched poly-mars.
BACKGROUND OF THE INVENTTON
1. Field of the Invention This invention concerns a composition and method for improving the storage stability of said treated polymer modified asphalts using branched poly-mars.
2. Discussion of Re3ated Art Asphalt is a bituminous material resulting from the distillation of crude oil° Typically, asphalt is derived from the bottoms of a vacuum distillation tower and has an atmospl2eric boiling paint of at least 38O°C. Because it is hydrophobic and has good adhe-si.veness and weatherability, asphalt has been used widely as a binder in paving materials and as a coating for roofing shingles, Frequently, polymeric materials have been added to asphalt to enhance its theological praperties, i.~., to improve its creep resistance above about 2A°C.
Polymer modified asphalts must also have goad phase aampatibility between the asphalt and polymer, and be storage stable at high temperatures for ease of hand-ling and application. Compatibility between the polymer and asphalt is very important to ensure that the properties of both are transferred to the finished product for good long term performance. Poor storage stability swill render the polymer mc~difisd asphalt unsuitable for use in paving binder applications, roofing applications, arid other industrial specialty products. Accordingly, various methods have been suggested for maintaining storage stability.
One method requires continuous mixing of the asphalt/polymer mixture to avoid phase separation (See, for example, U.S. Patents 4,240,946 and 4,314,921, which require high shear mixing to obtain physical dispersion of a polyolefin in bitumen. See also Transportation and Road Research Laboratory Report 1101 by J.H. Denning et al, Highways and Structures Department, Crowthorne, Berkshire, England (1983)). Another method discloses adding one or more dispersants to a polyethylene modified asphalt to avoid phase separation (See Jew et al, Journal of Applied Polymer Science, 31, pp.2685-2704 (1986)).
In yet another method, the composition of the asphalt is tailored to ensure compatibility with the polymer used or the polymer is selected to be compatible with the asphalt (See U.S. Patents 4,868,233 and 4,873,275).
In still another method, polymer modified asphalt is stabilized by the addition of an acid after the polymer has been added to the asphalt (See, for example, German Patent DE 22 55 173 C3 which discloses stabilizing mixtures of asphalt and styrenic thermoplastic elastomers (styrene-butadiene-styrene) by adding small amounts of 850 o-phosphoric acid or 36% hydrochloric acid to the asphalt/SBS mixture). More recently, it has been disclosed that the storage stability of acid treated polymer modified asphalts can be improved if the acid is added to the asphalt before the polymer.
However, none of these methods, alone or in combination, disclose that the storage stability of acid treated polymer modified asphalts can be further _~_ ~(~~~;:~~~°if improved if a branched, rather than a non-branched, polymer is added to the asphalt.
SUMMARY OF THE INVENTION
This invention relates t~ a composition and method for further improving the storage stability of acid treated polymer modified asphalts. More specifi-cally, the storage stability of an acid treated asphalt containing greater than 1.0 wt.% of a polymer can be further enhanced if branched, rather than non-branched, polymers are added to the asphalt.
DETAINED DESCRIPTION OF THE INVENTION
This invention requires asphalt, an inorganic acid, and a branched polymer.
The asphalt used in this invention may be obtained from a variety of sources including straight-run vacuum residue: mixtures of vacuum residue with diluents such as vacuum tower wash oil, paraffin distillate, aromatic and naphthenic oils, and mixtures thereofp oxidized vacuum residues or axidized mixtures of vacuum residues and diluent oils; and the like.
Other asphaltic z~laterials such as coal tar pitch, rock asphalt, and naturally occurring asphalt may also be used. Typically, the asphalt will have an atmospheric boiling point of at least 380~C, more typically of at least 440oG, and an asphaltene content of between about and about 30 wt.% as determined by ASTM D4124. Tn paving binder applications, the asphalt will typically comprise 85, preferably 90, wt.% or more of the acid treated polymer modified product (i._e., the final product). The asphalt will typically comprise 80, preferably 8~, wt.% or more of the final product when it is used in roofing applicationse An inorganic acid is than contacted with, or added to, the asphalt to form an acid treated asphalt.
In general, acid addition improves the temperature susceptibility of the asphalt and the stability of the acid treated polymer modified blend. Preferably, the inorganic acid is added slowly to the asphalt to avoid foaming which may occur if all the acid were added at one time. The inorganic acid content of the asphalt is not critical, but normally should range between about 0.2 and about 5.0 wt.%, preferably between about 0.25 and about 3.0 wt.~, of the asphalt. Although a wide variety of inorganic acids can be used, the inorganic acid will preferably be selected from the group con-sisting of hydrochloric acid, phosphoric acid, phos-phorus pentoxide, sulfuric acid, and mixtures thereof.
The term '°inorganic acid°' is meant to include compounds that are capable of forming an inorganic acid when contacted with tyre asphalt (~.g., chlorinated paraffin wax and polyvinyl chloride release hydrochloric acid when contacted with root asphalt). Hydrochloric acid, phosphoric acid, phosphorus pentoxide, and mixtures thereof are preferred inorganic acids, with phosphoric acid being particularly preferred. w Following acid addition, a branched polymer is then added to the acid treated asphalt to form an acid treated polymer modified asphalt that has enhanced storage stability relative ~o the storage stability obtained if ~ ndn-branched polymer (or a less branched polymer) were added to the acid treaded asphalt.
Howwer, the amount of polymer added to (br present in) the acid treated asphalt must be greater thaaz 1.0 wt.~
(preferably at least x.05 wt.~ and more preferably at least 2.0 wt.%) to obtain an enhancement in storage stability because at polymer concentrations of 1.0 wt.°s or less, polymer modified asphalts appear to be storage stable withaut acid addition. Conversely, polymer modified asphalts are believed to become increasingly less stable as the polymer concentration in the asphalt increases above 1.0 wt.o. However, the upper limit on the amount of polymer in the asphalt is not critical and can range up to 20 wt.o or more based on weight percent of the acid treated asphalt, although amounts below 20 wt.% are preferred.
Therefore, the amount of polymer in the asphalt will typically range from above 1.0 to about 20 wt.% based on weight of the acid treated asphalt. Preferably, the amount of polymer in the asphalt will range from about 1.5 to about 20 (preferably 15) wt.% and more preferably from about 2.0 to about 15 wt. o. when used as a paving binder, the acid treated polymer modified asphalt normally contains from about 3 (preferably 4) to about 8 wt.% polymer. When used for roofing applications, the acid treated polymer modified asphalt normally contains from about 8 to about 20 wt.o (preferably 15 wt.%) polymer.
A wide variety of branched polymers may be used in this invention. By "branched polymer" is meant a polymer in which a non ring carbon atom is directly bonded to 3 or 4 other carbon atoms that may be either rings or chains.
Suitable branched polymers include both thermoplastics and thermosets, as defined by ASTM D 883-69 Standard Definitions of Terms Relating to Plastics. ASTM D 883-69 defines a thermoplastic as a polymer that can be repeatedly softened when heated and hardened when cooled. A thermoset is defined as a polymer that can be changed into a substantially infusible or insoluble product when cured by heat or by chemical means.
Examples of suitable thermoplastics include acetals (e.g., polymers and copolymers of formaldehyde), acrylics, acrylonitrile-butadiene-styrene a.~~~~D
plastics, cellulosics (such as cellulose acetate, propionate and acetate-butyrate), chlorinated poly-ethylene, fluorocarbons, nylon, polycarbonates, poly-ethylenes, polyphenylene oxides, polyphenylene sul-fides, palypropylene, polystryene, polysulfone, poly-vinyl acetates, polyvinyl alcohols, polyvinyl chlo-rides, polyvinylidine chloride, styrene-acrylonitrile plastics, saturated polyesters, and thermoplastic elas-tomers of all classes including urethanes, polyesters, styrenics and olefinics. Preferred thermoplastics are polyethylene, ethylene methacrylate, ethylene-propylene elastomer, ethylene-vinyl acetate, nylon, uncured ethylene-propylene-dime terpolymers, and uncured thermoplastic styrenic elastomers (_e.a~., styrene-butadiene-styrene block copolymers), vaith ethylene methacrylate, ethylene-vinyl acetate, or their mixtures being most preferred.
Examples of suitable thermosets include amino resins (_e.g., melamine-formaldehyde, urea-formaldehyde, and mixtures thereof), phenolics, polyimides, polyure-thanes, polysulfides, silicone rubbers, unsaturated polyesters, and vulcanized (~..~., cured) rubbers (e_.~., natural rubbers and cured elastomers such as ethylene-propylene-diene terpolymers and styrene-butadiene-styrene block copolymers). Preferred thermosets are polyimides, polyurethanes, and vulcanized rubbers.
Most preferred are polyurethanes, cured elastomers, or their mixtures.
As used herein, "branched polymer" also includes derivatized analogues of these polymers such as polymers grafted with malefic anhydride (g. g.
ethylene vinyl acetate - malefic anhydride) or polymers grafted with sulfur or chlorine (~.g.. sulfonated polyethylene, chlorinated polyethylene, and the like).
The particular branched polymers used may be readily obtained in the marketplace from various chemical suppliers. Accordingly, their methods of preparation are well known to those skilled in the art (See Encyclopaedia of Polymer Science and Technology, Interscience Publishers, New York (1971); Kirk-Othmer Encyclopaedia of Chemical Technology, Wiley-Inter-Science, 3rd Ed., New York (1981);
G.L. Kinney, Engineering Properties and Applications of Plastics, John Wiley & Sons, New York (1957); and Plastics in Building, edited by Irving Skeist, Reinhold Publishing Corporation, New York (1966).
The conditions at which the acid and branched polymer are added to the asphalt are not critical and will vary with the particular asphalt and polymer used. However, the conditions will be within the ranges normally used for acid or polymer addition to asphalt. For example, acid is normally added slowly to the asphalt (typically, over a period of from about 1 to about 3 hours) at a temperature of from about 150°C to about 250°C, preferably from about 180°C
to about 210°C. Once a substantial amount (preferably all) of the acid has been added, the acid treated asphalt is mixed for an additional period of time (typically from about 0.5 to about 1 hour, although longer times could be used because no further reaction is likely to occur once all of the acid has been reacted or depleted). The branched polymer is then added to the acid treated asphalt at a temperature of from about 150° to about 300°C, preferably from about 175° to about 230°C. Typically, the polymer will be added over a period of from about 1.5 to about 3 hours to ensure adequate dispersal of the polymer. Although the polymer can be added over a longer period of time, it is important not to add the polymer over too short a period because the _ g _ polymer could then melt and coalesce when contacted by the hot acid treated asphalt. This would slow dis-persal of the polymer in the asphalt. Once polymer addition is complete, the acid treated polymer modified asphalt is mixed for an additional 0.5 to 1.5 hours or more.
The asphalt may be mixed or blended ~tvith the acid and polymer in any number of ways that can readily be selected by one skilled in the art. Suitable means include external mixers, roll mills, internal mixers, Banbury mixers, screw extruders, augers, and the like.
Normally, the mixing or blending during acid and polymer addition will be at ambient pressure.
An oxygen-containing gas (such as air) may be added to the asphalt before or during acid and polymer addition if desired. T3owever, in a preferred embodi-ment of this invention, the gas is not added before or during either step because it would tend to produce asphaltenes, which would have a detrimental effect on the storage stability of the :final product.
The acid treated branched polymer rnodi;~ied asphalt thus formed may be employed in essentially any application recquiring asphalt--based products with superior storage stability. Bxamples of such applica-tions include adhesives, coatings, fabricated products, road and roofing applications, sealants, sound and vibration dampening products, water proofing membranes and the like. I~owever, the final product is particu-larly well suited for use as a paving binder, particu-larly a binder in the load bearing course as well as the top or surface course of hot mix pavement struc-tures.
n~~~~~~
-The present invention will be further under-stood by reference to the following Example which is not intended to restrict the scope of the claims appended hereto. In the Example, the storage stability of the acid treated polymer modified asphalts tested was measured by placing a 200 gram sample in a copper tube (10 inches high and 1 inch in diameter) and heating it to 160oC for 5 days. Then the sample was removed from the tube and divided into top and bottom fractions. The viscosity of each fraction was measured at 135oC and then used to calculate the ratio of the top to the bottom viscosity. A ratio of 1.0 is consi-dered as optimum storage stability, with ratios above or below 1.0 representing mixtures that are increasing-ly less storage stable.
Example - Storage Stability of Acid Treated Linear and Branch Polyethylene Modified Asphalts ~fests were performed on two samples of a 300/400 penetration straight-run asphalt obtained from vacuum distillation. Phosphoric acid {85 wt.%) and linear low density polyethylene were added to one sample while the acid and branched low density poly-ethylene were added to the other sample. The tempera-~ture of the samples ranged between 190° and 200°C at all times daring the tests. The acid was added to the asphalt over approximately a trxenty minute period followed by reaction with the asphalt for about an additional thirty minutes. Polymer was then added over approximately a two to three minute period and mixed with the acid modified asphalt for from about two to about three hours. The asphalt was stirred during acid and polymer addition. The properties of the samples tested were determined and are shown in Table 1 below.
Q~.~~9 .Cable 1 Sample No. 1 2 Linear Branched Feedstock Inspections Polymer Low Density Polyethylene Wt. % - -.- - 5 - _______ felt IndeX - - --- 12 ---_--________ Density 0.923 0.91?
Asphalt, wt.% _- ____ g3,p _____ ____ Penetration at 25C, mm/10 ---- -- 31a ------_______ ~I3P04 (85%) , wt% - 2 , 0 .--:_r__-___ Product Insepections Su~tening Point, C 54 59 Penetration at 25'C, mm/10 96 95 Viscosity at 60C, Pa.S ?98 813 at x,35C, aSt 21?0 2009 Storage Stability at 160C 2.0 1,.3 The data, in Tabl e 1 show that the branched low density polyethylene gives tlae asphalt better -storage stability than do es the ~:ineardmsity l.ow polyethylene.
Polymer modified asphalts must also have goad phase aampatibility between the asphalt and polymer, and be storage stable at high temperatures for ease of hand-ling and application. Compatibility between the polymer and asphalt is very important to ensure that the properties of both are transferred to the finished product for good long term performance. Poor storage stability swill render the polymer mc~difisd asphalt unsuitable for use in paving binder applications, roofing applications, arid other industrial specialty products. Accordingly, various methods have been suggested for maintaining storage stability.
One method requires continuous mixing of the asphalt/polymer mixture to avoid phase separation (See, for example, U.S. Patents 4,240,946 and 4,314,921, which require high shear mixing to obtain physical dispersion of a polyolefin in bitumen. See also Transportation and Road Research Laboratory Report 1101 by J.H. Denning et al, Highways and Structures Department, Crowthorne, Berkshire, England (1983)). Another method discloses adding one or more dispersants to a polyethylene modified asphalt to avoid phase separation (See Jew et al, Journal of Applied Polymer Science, 31, pp.2685-2704 (1986)).
In yet another method, the composition of the asphalt is tailored to ensure compatibility with the polymer used or the polymer is selected to be compatible with the asphalt (See U.S. Patents 4,868,233 and 4,873,275).
In still another method, polymer modified asphalt is stabilized by the addition of an acid after the polymer has been added to the asphalt (See, for example, German Patent DE 22 55 173 C3 which discloses stabilizing mixtures of asphalt and styrenic thermoplastic elastomers (styrene-butadiene-styrene) by adding small amounts of 850 o-phosphoric acid or 36% hydrochloric acid to the asphalt/SBS mixture). More recently, it has been disclosed that the storage stability of acid treated polymer modified asphalts can be improved if the acid is added to the asphalt before the polymer.
However, none of these methods, alone or in combination, disclose that the storage stability of acid treated polymer modified asphalts can be further _~_ ~(~~~;:~~~°if improved if a branched, rather than a non-branched, polymer is added to the asphalt.
SUMMARY OF THE INVENTION
This invention relates t~ a composition and method for further improving the storage stability of acid treated polymer modified asphalts. More specifi-cally, the storage stability of an acid treated asphalt containing greater than 1.0 wt.% of a polymer can be further enhanced if branched, rather than non-branched, polymers are added to the asphalt.
DETAINED DESCRIPTION OF THE INVENTION
This invention requires asphalt, an inorganic acid, and a branched polymer.
The asphalt used in this invention may be obtained from a variety of sources including straight-run vacuum residue: mixtures of vacuum residue with diluents such as vacuum tower wash oil, paraffin distillate, aromatic and naphthenic oils, and mixtures thereofp oxidized vacuum residues or axidized mixtures of vacuum residues and diluent oils; and the like.
Other asphaltic z~laterials such as coal tar pitch, rock asphalt, and naturally occurring asphalt may also be used. Typically, the asphalt will have an atmospheric boiling point of at least 380~C, more typically of at least 440oG, and an asphaltene content of between about and about 30 wt.% as determined by ASTM D4124. Tn paving binder applications, the asphalt will typically comprise 85, preferably 90, wt.% or more of the acid treated polymer modified product (i._e., the final product). The asphalt will typically comprise 80, preferably 8~, wt.% or more of the final product when it is used in roofing applicationse An inorganic acid is than contacted with, or added to, the asphalt to form an acid treated asphalt.
In general, acid addition improves the temperature susceptibility of the asphalt and the stability of the acid treated polymer modified blend. Preferably, the inorganic acid is added slowly to the asphalt to avoid foaming which may occur if all the acid were added at one time. The inorganic acid content of the asphalt is not critical, but normally should range between about 0.2 and about 5.0 wt.%, preferably between about 0.25 and about 3.0 wt.~, of the asphalt. Although a wide variety of inorganic acids can be used, the inorganic acid will preferably be selected from the group con-sisting of hydrochloric acid, phosphoric acid, phos-phorus pentoxide, sulfuric acid, and mixtures thereof.
The term '°inorganic acid°' is meant to include compounds that are capable of forming an inorganic acid when contacted with tyre asphalt (~.g., chlorinated paraffin wax and polyvinyl chloride release hydrochloric acid when contacted with root asphalt). Hydrochloric acid, phosphoric acid, phosphorus pentoxide, and mixtures thereof are preferred inorganic acids, with phosphoric acid being particularly preferred. w Following acid addition, a branched polymer is then added to the acid treated asphalt to form an acid treated polymer modified asphalt that has enhanced storage stability relative ~o the storage stability obtained if ~ ndn-branched polymer (or a less branched polymer) were added to the acid treaded asphalt.
Howwer, the amount of polymer added to (br present in) the acid treated asphalt must be greater thaaz 1.0 wt.~
(preferably at least x.05 wt.~ and more preferably at least 2.0 wt.%) to obtain an enhancement in storage stability because at polymer concentrations of 1.0 wt.°s or less, polymer modified asphalts appear to be storage stable withaut acid addition. Conversely, polymer modified asphalts are believed to become increasingly less stable as the polymer concentration in the asphalt increases above 1.0 wt.o. However, the upper limit on the amount of polymer in the asphalt is not critical and can range up to 20 wt.o or more based on weight percent of the acid treated asphalt, although amounts below 20 wt.% are preferred.
Therefore, the amount of polymer in the asphalt will typically range from above 1.0 to about 20 wt.% based on weight of the acid treated asphalt. Preferably, the amount of polymer in the asphalt will range from about 1.5 to about 20 (preferably 15) wt.% and more preferably from about 2.0 to about 15 wt. o. when used as a paving binder, the acid treated polymer modified asphalt normally contains from about 3 (preferably 4) to about 8 wt.% polymer. When used for roofing applications, the acid treated polymer modified asphalt normally contains from about 8 to about 20 wt.o (preferably 15 wt.%) polymer.
A wide variety of branched polymers may be used in this invention. By "branched polymer" is meant a polymer in which a non ring carbon atom is directly bonded to 3 or 4 other carbon atoms that may be either rings or chains.
Suitable branched polymers include both thermoplastics and thermosets, as defined by ASTM D 883-69 Standard Definitions of Terms Relating to Plastics. ASTM D 883-69 defines a thermoplastic as a polymer that can be repeatedly softened when heated and hardened when cooled. A thermoset is defined as a polymer that can be changed into a substantially infusible or insoluble product when cured by heat or by chemical means.
Examples of suitable thermoplastics include acetals (e.g., polymers and copolymers of formaldehyde), acrylics, acrylonitrile-butadiene-styrene a.~~~~D
plastics, cellulosics (such as cellulose acetate, propionate and acetate-butyrate), chlorinated poly-ethylene, fluorocarbons, nylon, polycarbonates, poly-ethylenes, polyphenylene oxides, polyphenylene sul-fides, palypropylene, polystryene, polysulfone, poly-vinyl acetates, polyvinyl alcohols, polyvinyl chlo-rides, polyvinylidine chloride, styrene-acrylonitrile plastics, saturated polyesters, and thermoplastic elas-tomers of all classes including urethanes, polyesters, styrenics and olefinics. Preferred thermoplastics are polyethylene, ethylene methacrylate, ethylene-propylene elastomer, ethylene-vinyl acetate, nylon, uncured ethylene-propylene-dime terpolymers, and uncured thermoplastic styrenic elastomers (_e.a~., styrene-butadiene-styrene block copolymers), vaith ethylene methacrylate, ethylene-vinyl acetate, or their mixtures being most preferred.
Examples of suitable thermosets include amino resins (_e.g., melamine-formaldehyde, urea-formaldehyde, and mixtures thereof), phenolics, polyimides, polyure-thanes, polysulfides, silicone rubbers, unsaturated polyesters, and vulcanized (~..~., cured) rubbers (e_.~., natural rubbers and cured elastomers such as ethylene-propylene-diene terpolymers and styrene-butadiene-styrene block copolymers). Preferred thermosets are polyimides, polyurethanes, and vulcanized rubbers.
Most preferred are polyurethanes, cured elastomers, or their mixtures.
As used herein, "branched polymer" also includes derivatized analogues of these polymers such as polymers grafted with malefic anhydride (g. g.
ethylene vinyl acetate - malefic anhydride) or polymers grafted with sulfur or chlorine (~.g.. sulfonated polyethylene, chlorinated polyethylene, and the like).
The particular branched polymers used may be readily obtained in the marketplace from various chemical suppliers. Accordingly, their methods of preparation are well known to those skilled in the art (See Encyclopaedia of Polymer Science and Technology, Interscience Publishers, New York (1971); Kirk-Othmer Encyclopaedia of Chemical Technology, Wiley-Inter-Science, 3rd Ed., New York (1981);
G.L. Kinney, Engineering Properties and Applications of Plastics, John Wiley & Sons, New York (1957); and Plastics in Building, edited by Irving Skeist, Reinhold Publishing Corporation, New York (1966).
The conditions at which the acid and branched polymer are added to the asphalt are not critical and will vary with the particular asphalt and polymer used. However, the conditions will be within the ranges normally used for acid or polymer addition to asphalt. For example, acid is normally added slowly to the asphalt (typically, over a period of from about 1 to about 3 hours) at a temperature of from about 150°C to about 250°C, preferably from about 180°C
to about 210°C. Once a substantial amount (preferably all) of the acid has been added, the acid treated asphalt is mixed for an additional period of time (typically from about 0.5 to about 1 hour, although longer times could be used because no further reaction is likely to occur once all of the acid has been reacted or depleted). The branched polymer is then added to the acid treated asphalt at a temperature of from about 150° to about 300°C, preferably from about 175° to about 230°C. Typically, the polymer will be added over a period of from about 1.5 to about 3 hours to ensure adequate dispersal of the polymer. Although the polymer can be added over a longer period of time, it is important not to add the polymer over too short a period because the _ g _ polymer could then melt and coalesce when contacted by the hot acid treated asphalt. This would slow dis-persal of the polymer in the asphalt. Once polymer addition is complete, the acid treated polymer modified asphalt is mixed for an additional 0.5 to 1.5 hours or more.
The asphalt may be mixed or blended ~tvith the acid and polymer in any number of ways that can readily be selected by one skilled in the art. Suitable means include external mixers, roll mills, internal mixers, Banbury mixers, screw extruders, augers, and the like.
Normally, the mixing or blending during acid and polymer addition will be at ambient pressure.
An oxygen-containing gas (such as air) may be added to the asphalt before or during acid and polymer addition if desired. T3owever, in a preferred embodi-ment of this invention, the gas is not added before or during either step because it would tend to produce asphaltenes, which would have a detrimental effect on the storage stability of the :final product.
The acid treated branched polymer rnodi;~ied asphalt thus formed may be employed in essentially any application recquiring asphalt--based products with superior storage stability. Bxamples of such applica-tions include adhesives, coatings, fabricated products, road and roofing applications, sealants, sound and vibration dampening products, water proofing membranes and the like. I~owever, the final product is particu-larly well suited for use as a paving binder, particu-larly a binder in the load bearing course as well as the top or surface course of hot mix pavement struc-tures.
n~~~~~~
-The present invention will be further under-stood by reference to the following Example which is not intended to restrict the scope of the claims appended hereto. In the Example, the storage stability of the acid treated polymer modified asphalts tested was measured by placing a 200 gram sample in a copper tube (10 inches high and 1 inch in diameter) and heating it to 160oC for 5 days. Then the sample was removed from the tube and divided into top and bottom fractions. The viscosity of each fraction was measured at 135oC and then used to calculate the ratio of the top to the bottom viscosity. A ratio of 1.0 is consi-dered as optimum storage stability, with ratios above or below 1.0 representing mixtures that are increasing-ly less storage stable.
Example - Storage Stability of Acid Treated Linear and Branch Polyethylene Modified Asphalts ~fests were performed on two samples of a 300/400 penetration straight-run asphalt obtained from vacuum distillation. Phosphoric acid {85 wt.%) and linear low density polyethylene were added to one sample while the acid and branched low density poly-ethylene were added to the other sample. The tempera-~ture of the samples ranged between 190° and 200°C at all times daring the tests. The acid was added to the asphalt over approximately a trxenty minute period followed by reaction with the asphalt for about an additional thirty minutes. Polymer was then added over approximately a two to three minute period and mixed with the acid modified asphalt for from about two to about three hours. The asphalt was stirred during acid and polymer addition. The properties of the samples tested were determined and are shown in Table 1 below.
Q~.~~9 .Cable 1 Sample No. 1 2 Linear Branched Feedstock Inspections Polymer Low Density Polyethylene Wt. % - -.- - 5 - _______ felt IndeX - - --- 12 ---_--________ Density 0.923 0.91?
Asphalt, wt.% _- ____ g3,p _____ ____ Penetration at 25C, mm/10 ---- -- 31a ------_______ ~I3P04 (85%) , wt% - 2 , 0 .--:_r__-___ Product Insepections Su~tening Point, C 54 59 Penetration at 25'C, mm/10 96 95 Viscosity at 60C, Pa.S ?98 813 at x,35C, aSt 21?0 2009 Storage Stability at 160C 2.0 1,.3 The data, in Tabl e 1 show that the branched low density polyethylene gives tlae asphalt better -storage stability than do es the ~:ineardmsity l.ow polyethylene.
Claims (34)
1. In a method for improving the storage stability of an asphalt that contains greater than 1.0 to about 20 wt.% of a polymer which comprises:
(a) adding from about 0.2 to about 5 wt. of an inorganic acid to the asphalt to form an acid treated asphalt, and thereafter;
(b) adding the polymer to the acid treated asphalt to form an acid treated polymer modified asphalt;
the improvement which comprises adding a branched polymer to the acid treated asphalt to form a polymer modified asphalt that has improved storage stability relative to that obtained if a non-branched polymer had been added.
(a) adding from about 0.2 to about 5 wt. of an inorganic acid to the asphalt to form an acid treated asphalt, and thereafter;
(b) adding the polymer to the acid treated asphalt to form an acid treated polymer modified asphalt;
the improvement which comprises adding a branched polymer to the acid treated asphalt to form a polymer modified asphalt that has improved storage stability relative to that obtained if a non-branched polymer had been added.
2. The method of Claim 1, wherein the acid is selected from the group consisting of hydrochloric acid, phosphoric acid, phosphorus pentoxide, sulfuric acid, and mixtures thereof.
3. The method of Claim 2, wherein the acid is selected from the group consisting of hydrochloric acid, phosphoric acid, and mixtures thereof.
4. The method of Claim 1, 2 or 3, wherein from about 0.25 to about 3 wt.% of the acid is added to the asphalt.
5. The method of any one of Claims 1 to 4, wherein from 1.5 to about 15 wt.% of the branched polymer is present in the acid treated asphalt.
6. The method of Claim 5, wherein the branched polymer is a thermoplastic polymer, a thermoset polymer, or their mixtures.
7. The method of Claim 6, wherein the thermoplastic polymer is polyethylene, ethylene methacrylate, ethylene-propylene elastomer, ethylene-vinyl acetate, nylon, uncured thermoplastic styrenic elastomers, or mixtures thereof.
8. The method of Claim 6 or 7, wherein the thermoset polymer is polyimides, polyurethanes, vulcanized rubber, or mixtures thereof.
9. The method of any one of Claims 1 to 8, wherein (a) and (b) are preformed without the addition of an oxygen-containing gas.
10. The method of any one of Claims 1 to 9, where at least 2 wt.% of the branched polymer is present in the asphalt.
11. In a method for improving the storage stability of an asphalt having an atmospheric boiling point of at least 380°C and containing from above 1.0 to about 20 wt.% of a polymer which is a thermoplastic polymer, a thermoset polymer, or mixtures thereof, which comprises:
(a) adding from about 0.2 to about 5 wt.% of an inorganic acid selected from the group consisting of hydrochloric acid, phosphoric acid, phosphorous pentoxide, sulfuric acid, and mixtures thereof to the asphalt to form an acid treated asphalt, and thereafter;
(b) adding the polymer to the acid treated asphalt to form an acid treated polymer modified asphalt;
the improvement which comprises adding a branched polymer in (b) to form a polymer modified asphalt that has improved storage stability relative to that obtained if a non-branched polymer had been added.
(a) adding from about 0.2 to about 5 wt.% of an inorganic acid selected from the group consisting of hydrochloric acid, phosphoric acid, phosphorous pentoxide, sulfuric acid, and mixtures thereof to the asphalt to form an acid treated asphalt, and thereafter;
(b) adding the polymer to the acid treated asphalt to form an acid treated polymer modified asphalt;
the improvement which comprises adding a branched polymer in (b) to form a polymer modified asphalt that has improved storage stability relative to that obtained if a non-branched polymer had been added.
12. The method of Claim 11, wherein the acid is hydrochloric acid, phosphoric acid, or their mixtures.
13. The method of Claim 12, wherein the acid comprises phosphoric acid.
14. The method of Claim 11, 12 or 13, wherein the thermoplastic polymer is ethylene methacrylate, ethylene-vinyl acetate, or their mixtures.
15. The method of any one of Claims 11 to 14, wherein the thermoset polymer is polyurethanes, cured elastomers, or their mixtures.
16. The method of any one of Claims 11 to 15, wherein the acid treated polymer modified asphalt contains at least 80 wt.%
asphalt and from about 8 to about 20 wt.% polymer.
asphalt and from about 8 to about 20 wt.% polymer.
17. The method of Claim 16, wherein the acid treated polymer modified asphalt contains at least 85 wt.% asphalt and from about 3 to about 8 wt.% polymer.
18. The method of any one of Claims 11 to 17, wherein the polymer added in (b) comprises branched polyethylene.
19. In an asphaltic composition containing an inorganic acid and greater than 1.0 to about 20 wt.% of a polymer that is produced by the method comprising:
(a) adding from about 0.2 to about 5 wt.% of the acid to an asphalt to form an acid treated asphalt, and thereafter;
(b) adding the polymer to the acid treated asphalt to form an acid treated polymer modified asphaltic composition;
the improvement which comprises adding a branched polymer in (b) to form an asphaltic composition that has greater storage stability relative to that obtained if a non-branched polymer had been added.
(a) adding from about 0.2 to about 5 wt.% of the acid to an asphalt to form an acid treated asphalt, and thereafter;
(b) adding the polymer to the acid treated asphalt to form an acid treated polymer modified asphaltic composition;
the improvement which comprises adding a branched polymer in (b) to form an asphaltic composition that has greater storage stability relative to that obtained if a non-branched polymer had been added.
20. The composition of Claim 19, wherein the acid is selected from the group consisting of hydrochloric acid, phosphoric acid, phosphorus pentoxide, sulfuric acid, and mixtures thereof.
21. The composition of Claim 20, wherein the acid is selected from the group consisting of hydrochloric acid, phosphoric acid, and mixtures thereof.
22. The composition of Claim 19, 20 or 21, wherein from about 0.25 to about 3 wt.% of the acid is added to the asphalt.
23. The composition of any one of Claims 19 to 22, wherein from 1.5 to about 15 wt.% of the polymer is present in the acid treated asphalt.
24. The composition of Claim 23, wherein the polymer is a thermoplastic polymer, a thermoset polymer, or their mixtures.
25. The composition of Claim 24, wherein the thermoplastic polymer is polyethylene, ethylene methacrylate, ethylene-propylene elastomer, ethylene-vinyl acetate, nylon, uncured thermoplastic styrenic elastomers, or mixtures thereof.
26. The composition of Claim 24 or 25, wherein the thermoset polymer is polyimides, polyurethanes, vulcanized rubber, or mixtures thereof.
27. The composition of any one of claims 19 to 26, wherein (a) and (b) are preformed without the addition of an oxygen-containing gas.
28. The composition of any one of Claims 19 to 27, wherein the asphalt has an atmospheric boiling point of at least 380°C.
29. The composition of Claim 28, wherein the acid comprises phosphoric acid.
30. The composition of any one of Claims 24 to 29, wherein the thermoplastic polymer is ethylene methacrylate, ethylene-vinyl acetate, or their mixtures.
31. The composition of any one of Claims 24 to 30, wherein the thermoset polymer is polyurethanea, cured elastomers, or their mixtures.
32. The composition of any one of Claims 19 to 31, wherein the acid treated polymer modified asphalt contains at least 80 wt.%
asphalt and from about 8 to about 20 wt.% polymer.
asphalt and from about 8 to about 20 wt.% polymer.
33. The composition of Claim 32, wherein the acid treated polymer modified asphalt contains at least 85 wt.% asphalt and from about 3 to about 8 wt.% polymer.
34. The composition of any one of Claims 19 to 33, wherein the polymer added in (b) comprises branched polyethylene.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
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US07/517,776 US5095055A (en) | 1989-08-23 | 1990-05-02 | Using branched polymers to improve the storage stability of acid treated polymer modified asphalts (PNE-577) |
US517,776 | 1990-05-02 |
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CA2039486C true CA2039486C (en) | 2002-06-04 |
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