AU599210B2 - Flow resistant asphalt paving binder - Google Patents

Flow resistant asphalt paving binder Download PDF

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AU599210B2
AU599210B2 AU12568/88A AU1256888A AU599210B2 AU 599210 B2 AU599210 B2 AU 599210B2 AU 12568/88 A AU12568/88 A AU 12568/88A AU 1256888 A AU1256888 A AU 1256888A AU 599210 B2 AU599210 B2 AU 599210B2
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copolymer
asphalt
binder
ethylene
alkyl
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Lawrence George Kaufman
Lyle Edwin Moran
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ExxonMobil Technology and Engineering Co
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Exxon Research and Engineering Co
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Signature of Applicant (s) or Seal of Company and Signatures of its Officers as prescribed by Its Articles of Association.
LODGED AT SUBl 2 MAR 19 Melbour EXXON RESEARCH AND ENGI EERING COMPANY OFFICE] by 88 ae, Ian A. Scott Registered Patent Attorney i .I M MI -ii ;i COMMONWEALTH OF AUC FRALIA 2 PATENTS ACT 1952-69 COMPLETE SPECiFICATION
(ORIGINAL)
Class Int. Class Application Number: Lodged: Complete Specification Lodged: Accepted: Published: Priority r i' rna-Y-.
Related Art: Name of Applicant: Address of Applicant: Actial Inventor: Address for Service: EXXON RESEARCH AND ENGINEERING COMPANY P.O. Box 390, Florham Park, New Jersey 07932, United States of America LYLE EDWIN MORAN and LAWRENCE GEORGE KAUFMAN EDWD. WATERS SONS, 50 QUEEN STREET, MELBOURNE, AUSTRALIA, 3000.
Complete Specification for the invention entitled: FLOW RESISTANT ASPHALT PAVING BINDER The following statement is a full description of this invention, including the best method of performing it known to us 1.
lr j i L~ 1- BACKGROUND OF THE INVENTION 1. Field of the Invention This invention relates to asphalt paving binders having enhanced resistance to creep and their method of preparation.
2. Discussion of Related Art Asphalt is a bituminous material resulting from the distillation of crude oil. Typically, oo o asphalt is derived from the bottoms of a vacuum a distillation tower and has an atmospheric boiling °oo point of at least 380*C. Because it is hydrophobic 0 00 o, and has good adhesiveness and weatherability, oi asphalt has been used widely as a binder in paving ooo materials and as a coating for roofing shingles.
When used in roofing applications a 0 0 0 shingle coating or a saturant), asphalt is usually 0 00 0 polymerized by undergoing oxidative dehydrogenation 0 o0 in which the asphalt is contacted with an oxygen- 0 C containing gas (usually air) at temperatures ranging between about 200" and about 300"C for between about 6 and about 24 hours. This procedure is described 0 in detail by L.W. Corbett in "Bituminous Materials: o o0 Asphalts, Tars and Pitches", Interscience "Publishers, New York (1965) and by E.J. Barth in "Asphalt Science and Technology", Gordon and Breach Science Publishers, New York (1968), the disclosures of each being incorporated herein by reference.
r 2 Oxidative dehydrogenation improves the creep (i.e.
flw) resistance and weatherability of the asphalt, and reduces its sensitivity to temperature changes.
When used as a conventional paving binder, the asphalt does not usually undergo oxidative dehydrogenation, but rather, is manufactured to meet certain control specifications such as flash point (ASTM D-92), penetration at 25"C (ASTM apparent viscosity at 60*C (ASTM D-2171) and kinematic viscosity at 135*C (ASTM D-2170). In addition to the control specifications, a paving asphalt should also meet certain performance specifications such as ductility (ASTM D-113), solubility in trichloro- 9900 ethylene (ASTM D-2042), and thin film oven aging S0 (ASTM D-1754).
0 0 S* In the past, asphalts which met the oo o: above-mentioned control and performance specifications were generally considered more than adequate as paving binders. However, more recently, asphalt users have been demanding higher performance pro- 0 00 o ducts. For example, today's increased heavy truck traffic volume is stressing and destroying roads.
One of the major problems resulting from this 0' increased traffic loading is pavement rutting due to the natural tendency of asphalt to creep over a period of time, particularly during the increased temperatures of summer. Therefore, road construction contractors are now in serious need of paving asphalt binders which have an increased resistance to creep.
3 In general, there are two basic methods which are typically employed to change or adjust the rheological and chemical properties of an asphalt: blend resins and oils into said asphalt, or (2) incorporate certain additives such as chemical compounds and polymers into the asphalt. Several examples of the latter method are mentioned below.
U.S. Patent 3,249,567 discloses the use of ethylene copolymers to lower the penetration value of bitumens.
U.S. Patent 3,985,694 discloses an asphalt composition that contains synthetic terpene resins 0 o as well as interpolymers of ethylene and vinyl o acetate and an organic acid.
a CO .000 0 0 S. European Patent 162,561 discloses an o. ethylene vinyl acetate containing asphalt formulation for surface dressing of roads. Similarly, German Patent DE 3027279A1 discloses a surface dressing composition which includes coal tar, o°o bitumen and ethylene-vinyl acetate.
Japanese Patent 83,047424 discloses the 0"o o use of ethylene copolymers in asphalt paving materials to improve resistance to temperature changes.
o. o U.S. Patent 4,560,414 discloses a method of preparing a paving asphalt composition with improved flow resistance by incorporating granulated Trinidad Epure therein as well as pulverulent solids to prevent recaking of the Trinidad Epure.
4 Among the pulverulent solids listed are polymeric resins.
U.S. Patent 3,980,598 discloses a mixture comprising from 97 to 3 wt. asphalt and from 3 to 97 wt. ethylene copolymer in which the asphalt is a deasphalted asphalt having a penetration of less than 10 at 25"C. No mention is made of the asphaltene content except for an 'example which shows an asphalt having 8.5 wt. asphaltenes in mixture with 50 wt. polymer.
Finally, U.S. Patents 4,451,598 and 4,650,820 disclose bitumen-terpolymer compositions.
The wt. bitumen and terpolymer ranged from 35 to and 5 to 65, respectively, in the '598 patent, and from 95 to 99 and 1 to 5, respectively, in the '820 patent. No mention is made of the asphaltene content of the bitumen.
Thus, the prior art does not teach or suggest that the asphalt used in an ethylene copolymer modified paving binder must have an asphalto ene content below a critical level if the binder is to be both storage stable and have enhanced creep .resistance.
SUMMARY OF THE INVENTION Now according to the present invention, it has been discovered that paving asphalts (especially of the hot mix, hot laid type) may be modified so as to have improved stability and rheological properties by the addition of certain copolymers of 5 i ethylene with vinyl acetate or lower alkyl esters of acrylic acid and methacrylic acid to an asphalt, provided said asphalt has an asphaltene content below a critical level. More specifically, an asphalt cement or binder having both enhanced storage stability and creep resistance relative to conventional binders straight-run asphalts obtained from residua from vacuum distillation of crude oil) is formed when the asphalt used in said binder has an asphaltene content of about 7 wt. or less, based on wt. of the asphalt. The ethylenevinyl acetate, ethylene-alkyl acrylate or ethylenealkyl methacrylate copolymer added to the asphalt in accordance with the practice of the present inven- S, 0 tion should have a melt index of from about 0.3 to 0
Q
about 20g/10 min. and a vinyl acetate, acrylate or methacrylate content of from 3 to about 30 wt. o The amount of copolymer used with said asphalt 00; should range from about 3.5 to about 10%, based on 0 0 the total weight of polymer and asphalt.
The composition of the present invention is particularly suitable for use as a binder in the ,00 load bearing course as well as the top or surface course of pavement structures, particularly hot mix 0o"0 pavement structures. Thus, in one embodiment of the present invention there is provided an improvement in pavement structures wherein the binder in said 4'l structures comprises an asphalt containing about 7 Swt. or less asphaltenes and from about 3.5 to about 10% by weight of a copolymer of ethylene with from 3 to about 30 wt. vinyl acetate, alkyl acrylate or alkyl methacrylate.
VTi 6 In yet another embodiment, the present invention relates to a method of improving both the storage stability and creep resistance of asphalt paving binders by incorporating into the asphalt used in said binders from about 3.5 to about 10 wt.
of a copolymer of ethylene which contains from 3 to about 30 wt. vinyl acetate, alkyl acrylate or alkyl methacrylate.
BRIEF DESCRIPTION OF THE DRAWINGS Figures 1 to 5 are graphs showing the creep resistance of various asphalt paving binders i versus time.
DETAILED DESCRIPTION OF THE INVENTION ,According to the present invention, asphalt paving binders which exhibit an increased resistance to creep or deformation may be formed by adding or incorporating into the asphalt used in said binder from about 3.5 to about 10% by weight of a copolymer of ethylene and from 3 to 30 wt. vinyl Sacetate, alkyl acrylate or alkyl methacrylate.
Preferably, the alkyl group of the alkyl acrylate and alkyl methacrylate will be methyl, ethyl, or butyl. Importantly, only copolymers which have a melt index in the range of from about 0.3 to about 20g/10 min. and ethylene contents of from about to 97 wt. are suitable. Optionally, but prefer- Sably, the copolymer may have from about 0.3 to about 0.8% by weight of maleic anhydride grafted onto the ethylene-vinyl acetate or alkyl acrylate or alkyl methacrylate copolymer.
7 1 The amount of copolymer added to the asphalt should range from about 3.5 (preferably from about 4) to about 10 wt. An amount below about wt. will result in a paving binder having unacceptable creep resistance while amounts greater than about 10 wt. result in a product with a viscosity that renders the product impractical and unsuitable for use as a paving binder, particularly a hot mix paving binder. Typically, the viscosity of the paving binder of the present invention should not exceed about 1200 cSt at 135"C.
The asphalt used must be low in asphaltenes to ensure both satisfactory creep resistance and storage stability of the binder. To o obtain these benefits, it is critical that the asphalt (or blend of asphalts) to which the icopolymer is added contain about 7 wt. or less 4: asphaltenes (for example, from 0% to about 7 wt. based on wt. of the asphalt. Preferably the asphaltene content will be about 6.5 wt. or less, most preferably about 6.0 wt. or less.
The asphalt 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 thereof; oxidized vacuum residues or oxidized mixtures of vacuum residues and diluent oils and the like. Other asphaltic materials 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 8 typically at least 440*C, and will comprise at least about 85, preferably at least about 90, more preferably at least about 95, wt. of the binder.
In a particularly preferred embodiment of the present invention, the asphalt paving binder will contain from about 4 to about 6 weight percent of an ethylene vinyl acetate copolymer having a melt index of about 1 to about 5g/10 min. and a vinyl acetate content of from about 3 to about 12 wt. When the asphalt is modified with an ethylene methacrylate copolymer, it is particularly preferred that the asphalt binder contain from about a O, 4 to about 5 wt. of maleic anhydride-grafted Sethylene methacrylate copolymer having a melt index of from about 3 to about 5g/10 min., a methyl- 0 acrylate content of about 20 wt. and a maleic o anhydride content of from about 0.3 to about 0.8 wt.
The asphalt may be mixed or blended with the copolymer in any number of ways which can 0' readily be selected by one skilled in the art.
Suitable means include external mixers,iroll mills, Sinternal mixers, Banbury mixers, screw extruders, augers and the like. Blending times can range broadly; i.e. from about 1 hour to about 8 hours or Smore. Typically, blending times of about 1 to about 4 hours will be employed.
Similarly, the particular conditions at which the asphalt is blended with the copolymer are not critical. Typically, the blending will be 9 performed at ambient pressure and at a temperature between about 1500 and about 300*C, preferably between about 150" and about 230*C.
The present invention will be further understood by reference to the following Examples which are not intended to restrict the scope of the claims appended hereto. In the Examples, the storage stability and creep resistance of the paving binders tested were measured as follows: Storage Stability A 200 gram sample is placed in a copper tube (10 inches high and 1 inch in diameter) and Sof heated at 160'C for 5 days. Then the sample is S'removed from the tube and divided into top and bottom fractions. The viscosity of each fraction is measured at 135"C. The ratio of the top over the bottom viscosity at 135"C is then calculated. A ratio of 0.90 to 1.1 is preferred; 0.8-0.9 and 1.1-1.2 is borderline; and less than 0.8 or more than 1.2 is a failure.
Creep Resistance 0a 0 The sliding plate rheometer is used to measure the creep resistance and shear of the I asphalts tested over a continuous range of loading times following the procedure set forth by Fenijn and Krooshof in "Proceedings of CTAA", Winnipeg, Canada, November 1970, the disclosure of which is incorporated herein by reference. In the Examples, data were obtained at 20* and/or 40*C since asphalt pavement will be prone to rutting under heavy loads at--these temperatures. From these data, creep resistance log creep compliance in square meters per newton) was plotted against time to show the creep behavior of the composition. If the composition creeps or flows with time, the curve will slope upwards. If the composition has good flow resistance, the curve will tend to become horizontal and flatten or plateau.
Example 1 EVA Polymer Modified Asphalt Preferred to Unmodified Asphalt In this example, 38.4 grams of ethylene vinyl acetate (EVA) having a 3.3 to 4.0 melt index and 9 1 wt. vinyl acetate content VA) were blended into 729.2 grams of vacuum residue having a 204 penetration at 25'C and containing less than 5 wt. asphaltenes. The final concentration o of polymer in the blend was 5.0 wt. The blending operation was conducted at 190'C for two hours in a baffled autoclave equipped with a stirrer rotating at 1750 rpm. The properties of the EVA modified paving binder were determined as were the o corresponding properties of an unmodified vacuum residue having a 194 penetration at 25°C. The results are summarized in Table 1 and shown in 4 1 Figure 1.
00 4 '0 ~~i~ii 11 Table 1 Unmodified Asphalt EVA-Modified Asphalt Feed Inspections Asphalt: Wt. Asphaltenes, wt. Penetration at 25"C Polymer: Wt. Melt Index, g/10 min Product Inspections Softening Point, *C Penetration at 25°C 4oC Penetration Index Viscosity: 60*C, Pa.S 135*C, cSt Storage Stability Creep Resistance at 20" and 40"C (See Figure 1) Test performed only to measure at 100 5 194 204 3.3-4.0 4 0.
0d O 0# 0 O 0404804 4 0 4 04 0~ o 0] 00 0 00 00 0 0 00r 4* 00 00 9 41.0 194.0 26.0 14.0 -2.19 29.6 163.0 1.00 Poor at 20°C (1) 78.8 98.0 21.3 11.7 -0.64 543.9 492.3 1.05 Excellent at 20*C because sample too soft t The data in Table 1 show that the unmodified asphalt has acceptable storage stability but unacceptable creep resistance at 20° and 40"C. In contrast, the EVA-modified asphalt has excellent storage stability and creep resistance at 20* and 12 Example 2 Maleated EVA Polymer Modified Asphalt Preferred to Unmaleated EVA Polymer Modified and Unmodified Asphalts Using the procedure of Example 1, 43.9 grams of 4.0 M.I. EVA (27% VA) were blended into 834 grams of a vacuum residue having a 204 penetration at 25"C and containing less than 5 wt. asphaltenes to form a blend having a polymer content of 5 wt. Using the same procedure, 0.5 to 0.6 wt. maleic anhydride was grafted onto the same EVA copolymer. Then 27 grams of the maleated EVA were Sblended into 513.1 grams of vacuum residue having a 201 penetration at 25"C and containing less than wt. asphaltenes to give a final polymer concentration of 5 wt. The properties of the un-maleated and maleated products were evaluated as were the corresponding properties of an unmodified vacuum t residue having a 194 penetration at 25"C. The results are summarized in Table 2 and shown in Figure 2.
L--C
-13- Table 2 Maleated Unmodified EVA-Modified EVA-Modified Asphalt Asphalt Asphalt Feed Inspections Asphalt: Wt. 100 95 Asphaltenes,wt% <5 <5 Penetration at 25"C 194 204 201 Polymer: Wt. 0 5 Melt Index, mins 4 4 Product Inspections Softening Point, °C 41.0 54.3 58.0 Penetration at 25"C 194.0 133.5 111.0 0 C 26.0 29.3 25.7 4°C 14.0 11.0 13.0 Penetration Index -2.19 -1.01 -0.49 Viscosity: Pa.S 29.6 73.5 92.7 135"C, cSt 163.0 529.2 590.8 Storage Stability 1.00 0.97 0.99 Creep Resistance at 20* and 40°C Poor at Fair Excellent (See Figure 2) 20°C (1) Test performed only at 20"C because sample too soft to measure at The data in Table 2 show that grafting of maleic anhydride onto ethylene vinyl acetate produces a copolymer modified asphalt which has improved rheological performance over that of the un-maleated polymer modified asphalt.
L
14 Example 3 Maleated EMA Polymer Modified Asphalt Preferred to Unmaleated EMA Polymer Modified and Unmodified Asphalts Using the procedure of Example 1, 32.8 grams of 4.4 M.I. 20% methyl acrylate (MA) were blended into 624 grams of a vacuum residue having a 201 penetration at 25°C and containing less than wt. asphaltenes to give a 5 wt. polymer content blend.
Using the same procedure, 0.3 to 0.8 wt. maleic anhydride was grafted onto the same EMA copolymer. Then 39.4 grams of the maleated EVA were 3o E blended into 748.9 grams of 204 penetration at So vacuum residue having less than 5 wt. asphaltenes S° to give a final polymer concentration of 5 wt. 0 o The properties of the un-maleated and maleated O0 0 products were evaluated as were the corresponding properties of an unmodified vacuum residue having a 194 penetration at 25"C. The results are summarized o *o in Table 3 and shown in Figure 3.
0Qa 0 000 7\ ~~1 15 Table 3 Unmodified Asphalt EMA-Modified Asphalt Maleated EMA-Modified Asphalt 0 00 0 0 0a00 0 4. 0 0 00 a o 0 00 0 0 000 0 0 00 0 00 0 00 o ac Feed Inspections Asphalt: Wt. Asphaltenes,wt% Penetration at 25°C Polymer: Wt. Melt Index, mins.
Product Inspections Softening Point, °C Penetration at 25°C 4 0
C
Penetration Index Viscosity: 0 C, Pa.S 135°C, cSt Storage Stability Creep Resistance at 20° and 40°C (See Figure 3) 204 4.4 41.0 194.0 26.0 14.0 -2.19 29.6 163.0 1.00 Poor at 20°C (1) 62.1 115.0 24.0 12.8 -0.82 68.4 531.0 0.95 Fair 68.0 112.0 27.5 13.7 -0.27 103.0 624.4 1.04 Excellent 00 0 0o a 4 r Test performed only at 20°C because sample too soft to measure at 40 0
C.
The data in Table 3 show that grafting of maleic anhydride onto ethylene methyl acrylate produces a copolymer modified asphalt which has excellent rheological performance compared with the un-maleated polymer modified asphalt.
1 _I& ~1 i, t -i -~I 16 Example 4 Minimum Polymer Concentration in Paving Binder In this example, paving binders having 2, 3, and 4 wt. EVA were prepared. For the 2 wt. case, 14.7 grams of ethylene vinyl acetate (EVA) having a 3.3 to 4.0 melt index and containing 9 1 wt. VA were blended into 620.6 grams of vacuum residue having a 204 penetration at 25"C and containing less than 5 wt. asphaltenes. For the 3 wt. EVA case, 21.4 grams of the same EVA copolymer were blended into 691.2 grams of the same residue.
For the 4 wt. case, 25.3 grams of the same EVA grade were blended into 607 grams of a vacuum residue having a 193 penetration at 25"C. The properties of the resulting paving binders were determined and compared with the corresponding S. properties of the 5 wt. EVA binder from Example 1.
The results are summarized in Table 4 and shown in Figure 4.
S 4 4 (4^ 1sf 41 I
I-
17 Table 4 Feed Inspections Polymer: Wt.% 2 3 4 Melt Index,g/10 mins.
Asphalt: Wt. 98 97 96 Asphaltenes,wt% Penetration at Product Inspections 204 204 193 204 0 1r II 4 Softening Point,
°C
Penetration at 4'C Penetration Index Viscosity: Pa.S 135"C, cSt Creep Resistance at 40°C (See Figure 4) 48.4 168.5 25.0 12.3 72.0 129.7 22.7 10.0 76.0 105.0 19.0 12.0 78.8 98.0 21.3 11.7 -1.98 -1.60 -1.15 -0.64 58.8 257.4 Poor 86.4 309.0 543.9 285.4 405.0 492.3 Poor Good Excellent that acceptable The data in Table 4 show creep resistance is obtained only when the asphalt paving binder has a polymer content of about 3.5 wt.
or greater.
Example 5 Effect of Asphaltene Concentration on Storage Stability and Creep Resistance Following the procedure of Example 1, blends of 5 wt. ethylene vinyl acetate (EVA) with a melt index ranging from 3.3-4 and 9 1 wt. VA were made with the following asphalt blends:
L--
-18a straight-run vacuum residue having a penetration of greater than 400 at 25"C and no asphaltenes; (ii) a blend of a straight-run vacuum residue having a 276 penetration at 25*C and 3.9 wt.% asphaltenes, and 9 wt.% of a paraffin lube distillate having no asphaltenes; (iii) a blend of a straight-run o0 asphalt having a 85/95 penetration S o at 25*C and 17.13 wt.% asphaltenes o and a straight-run asphalt 0 o having a 70 penetration at 25'C and o 00 S5.14 wt.% asphaltenes; o0q000 (iv) same as (iii); o o same as (iii); oo (vi) a straight-run asphalt having a 190 penetration at 25"C and 15 wt.% asphaltenes.
The asphaltene content of each blend was measured by ASTM D 4124. The properties of the resulting paving binders were determined and are summarized in Table 5 and shown in Figure o 0 a 0 0 00 a 0 0 o e 0 0 4 0 0 0 0 a 00 00 0 Tabl e Sampole Identification Feed Inspections Polymer: wt Melt Index, g/10 mins.
Asphalt: Wt. Asphaltenes, wt.% Product Inspiections Softening Point, *C Penetration at 25*C bO*c 4*C Penetration Index Viscosity: 600C, Pa.S 1350C, cSt Storage Stability Creep Resistance at 40*C (See Figure Too high to measure.
ii)- iiil (iv) (vi 3.3-4.0 0 3.5 5.7 6.5 8.4 87.0 177.30 34.2 17.0 0.95 551.7 367.5 0.93 77.8 185.0 39.0 21.0 -0.78 238.0 350.0 0.94 91 38 8 3 -1.2 (1) 1074 1.0 90 38 4 -0.03 6374 1111 1.2 88 43 10 5 -0.49 (1) 1162 1.4 47.0 99.3 30.3 16.7 0.85 (1) 997 4.9 Excellent Poor(2) Test performed only at 24*C because sample too soft to measure at aa 20 The data in Table 5 show that a paving binaer having both acceptable storage stability and creep resistance is obtained only if the asphaltene content of the asphalt used in said binder is about 7 wt. or less Example 6 Effect of Vinyl Acetate Content on Paving Binder In this example, 40.9 grams of EVA with a M.I. and containing 40 wt. VA were blended into 776.9 grams of vacuum residue having a 201 penetration at 25°C and containing less than 5 wt. asphaltenes to give a 5 wt. EVA concentration.
tol.. The properties of the resulting paving binders were tit determined and compared with the corresponding ,properties of the 5 wt. EVA binder from Example 1.
The results are summarized in Table 6.
ii 4 a 21 Table 6 EVA (40% VA) EVA VA) Feed Inspections Polymer: Wt. Melt Index, mins. Asphalt: Wt. Asphaltenes,wt% Penetration at 25°C 201 204 0 00 o 4 0 00 0 00 00 0000 0 04 00 S 00 4 A, *4 0 0 4 0 04o 0 0 o 04 0 0 0 0 S0 o< Product Inspections Softening Point, °C Penetration at 25°C 10°C 4"C Penetration Index Viscosity: Pa.S 135"C, cSt Creep Resistance at +40°C 39.2 78.8 118.3 32.3 13.8 -0.02 42.5 255.0 98.0 21.3 11.7 -0.64 543.9 492.3 Excellent _j Not possible to measure because of gross separation The data in Table 6 show that high vinyl acetate content EVA does not produce a modified paving binder with acceptable creep resistance.
Example 7 Effect of Varying Polymer Melt Index and Vinyl Acetate Content Several blends were made according to the procedure used in Example 1: 54.8 grams of EVA with 2500 M.I. and 14% VA were blended with 1041 grams of -1 -1 1- _W r 22 201 penetration at 25°C vacuum residue having less than 5% asphaltenes.
(ii) 39.2 grams of EVA with 2500 M.I. and 28% VA were blended with 744.4 grams of 201 penetration at 25*C vacuum residue having less than 5% asphaltenes.
(iii) 36.1 grams of EVA with 45 M.I. and 33% VA were blended with 685.0 grams of 201 penetration at 25"C vacuum residue having less than 5% asphaltenes.
o (iv) 37.4 grams of EVA with 150 M.I. and 19% o° VA were blended with 771.0 grams of 201 s penetration at 25*C vacuum residue hav- Sf ing less than 5% asphaltenes.
The properties of the resulting products were determined and are summarized in Table 7.
t I 1 L 4i *fle 0 0 a a C a a o 000 00 0 SO 0 0 0 0 00 00 0 0 0 0 0 0 0.00004 00 0 0 0 Table 7 Sample Identification Jjj Feed Inspections Iiii (iii) (iv)
(V)
Polymer: EVA(14%VA) EVA(28%VA) EVA(33%VA) EVA(19%) EVA(9% VA) Wt. Melt Index, mins. 2,500 2,500 45 150 3,3-4.0 Asphalt: Wt. Penetration at 204 Product Inspections Softening Point, *C 45.5 Penetration at 25'C 166.80 101C 26.70 4*C 11.50 Penetration Index -1.88 viscosity: Pa.S 32.70 135 0 C, cSt 225.0 Creep Resistance at +40*C (1) Flows, too soft to measure 38.0 104 .2 41.3 15 .3 1.63 29.3 234.0 (1) 39.1 163.3 36.5 14 .3 -0.90 118 .2 384.0 (1) 58.5 108 .8 26.3 11.2 -0.97 46.3 339.0 (1) 78.8 98.0 21.3 11.7 -0.64 543.9 492.3 Excel lent 24 The data in Table 7 show that a range of EVA- polymers with melt indices and vinyl acetates outside of the claimed ranges do not form paving binders with acceptable creep resistance.
Example 8 Effect of High Copolymer Concentration on Paving Binder Viscosity In this example, two blends were prepared having different polymer levels.
Using the procedure of Example 1, 32.1 grams of EVA having a 3.3 to 4.0 g/10 mins. MI and 9 4 1 wt. VA were blended into 729.9 grams of o asphalt which contained a vacuum residue with a penetration at 25°C and 10 wt. of a paraffin lube 0oo distillate. The asphalt had a viscosity of 1176 cSt at 100°C. The final concentration of copolymer in o. the blend was 5 wt. A second blend was prepared by mixing 0o 0 481.04 grams of the same EVA copolymer into 459.2 04 ograms of the same asphalt used to make the first blend. The final concentration of copolymer in this 0 ablend was 15 wt. The second blend was made using the procedure of Example 1 except that the copolymer was added in 3 increments of about 27 grams per increment. About 15 to 30 minutes separated the addition of each increment to minimize potential damage to the mixer from the high viscosity of the blend.
The properties of the resulting products were determined and are summarized in Table 8.
25 Table 8 Feed Inspections Polymer: Wt. Melt Index, mins.
Asphalt: Wt. Asphaltenes,wt% Viscosity at 100"C, cSt Product Inspections Softening Point, °C Penetration at 25°C 10'C 4oC Penetration Index Viscosity: Pa.S 135"C, cSt Storage Stability EVA(9% 95 1176 1348 0 '00 0 C0 o 0 0 CIO C? 0 0 0 0 000 0 0 o 0004 o oa S00 00 0 0 00 0 00 00 0.
4,4 0 0Q 0 00 70 16 7 -0.71 (1) 599 1.0 12 6 0.62 (1) 6924 0.63 Too high to measure.
The data in Table 8 show that the presence of 15 wt. copolymer in the paving binder results in a viscosity at 135"C that renders the product impractical and unsuitable for use as a paving binder.
A larger amount of polymer would result in a product having even greater (and therefore less acceptable) viscosities. In addition, the high copolymer content binder had unacceptable storage stability.
r i

Claims (19)

1. A storage stable and creep resistant asphalt paving binder which comprises an asphalt having a-bou 7 wt. or less asphaltenes, and from about 3.5 to'abut-10 wt. of a copolymer of ethylene with at least one compound se- lected from the group of vinyl acetate, alkyl acry- late or alkyl methacrylate, wherein said copolymer So has a melt index of from abhoLt0.3 to abet- 20g/10 Q 0 mins. and contains from abot 70 to -abeu-e- 97 wt. ethylene. 004 9 0
2. The binder of claim 1 wherein alkyl is methyl, ethyl or butyl. 0
3, The binder of claim 2 wherein said co- o'P polymer has from abut 0.3 to abett 0.8 wt. maleic anhydride grafted thereon.
4. The binder of claim 1 wherein said co- polymer is ethylene with from abeut 3 to about 12 wt. vinyl acetate and has a melt index of from about 1 to -about 5g/10 mins.
The binder of claim 4 wherein from Sabout 4 to abe-t 6 wt. of said copolymer is present therein.
6. The binder of claim 1 wherein said co- polymer is ethylene with about 20 wt. alkyl
7- I a 27 methacrylate and has a melt index of from abut--3 to ab out 5g/10 mins. 7. The binder of claim 6 wherein from about 0.3 to about- 0.8 wt. maleic anhydride is grafted onto said copolymer.
8. The binder of claim 7 wherein from abte 4 to a4eut 5 wt. of said copolymer is present therein.
9. A method for improving the storage stability and creep resistance of an asphalt paving 0 0 binder which comprises: 'a o o, providing an asphalt having an asphaltene content of abheet 7 wt. or less, and incorporating into said asphalt from abutr 3.5 to about 10 wt. of a'-opolymer of ethyl- Sene with at least one compound selected from the group of vinyl acetate, alkyl acrylate or alkyl methacrylate, wherein said copolymer has a melt index of from about- 0.3 to -ab.ou 20g/10 mins. and contains from about-70 to abeat 97 wt. ethylene.
The method of claim 9 wherein alkyl is methyl, ethyl or butyl.
11. The method of claim 10 wherein said copolymer has from -abot- 0. 3 to abottt- 0.8 wt. maleic anhydride grafted thereon. ,DI T, |:3QV/ b-L -I 28
12. The method of claim 9 wherein said copolymer is ethylene with from -a-bo 3 to abeit 12 wt. vinyl acetate and has a melt index of from -a~eut 1 to abeut- 5g/10 mins.
13. The method of claim 12 wherein from abot. 4 to abeot- 6 wt. of said copolymer is present therein.
14. The method of claim 9 wherein said said copolymer is ethylene with -abeA-t 20 wt. alkyl methacrylate and has a melt index of from abot 3 to Sor -about 5g/10 mins.
The method of claim 14 wherein from Smabout- 0.3 to abesat- 0.8 wt. maleic anhydride is grafted onto said copolymer.
16. The method of claim 15 wherein from abow- 4 to -abeit 5 wt. of said copolymer is present therein. 4
17. A pavement structure containing an asphalt paving binder which comprises an asphalt containing from 0 to about 7 wt. asphaltenes and from about -3.5 to -~oat 10 wt. of an ethylene copolymer of vinyl acetate, alkyl acrylate or alkyl methacrylate, said copolymer having a melt index of from abe~u 0.3 to-about 20g/10 mins. and an ethylene content between abeut-70 and -abeu 97 wt.
18. The pavement structure of claim 17 wherein alkyl is-methyl, ethyl or butyl. i/ AQ 29
19. The pavement structure of claim 17 wherein said copolymer has from about- 0.3 to about 0.8 wt. maleic anhydride grafted thereon. DATED this 1st day of March 1988. EXXON RESEARCH AND ENGINEERING COMPANY c CtP a I6 EDWD. WATERS SONS PATENT ATTORNEYS QUEEN STREET MELBOURNE. VIC. 3000.
AU12568/88A 1987-03-03 1988-03-02 Flow resistant asphalt paving binder Ceased AU599210B2 (en)

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US021189 1987-03-03

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CN102617968B (en) * 2012-03-23 2014-05-07 重庆鹏方路面工程技术研究院有限公司 Cooling reclaiming agent for road and preparation method thereof
CN114381132B (en) * 2022-01-14 2022-12-06 苏州科技大学 Copolymer modified asphalt

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3980598A (en) * 1974-08-28 1976-09-14 Basf Aktiengesellschaft Mixtures based on ethylene copolymers and asphalt
EP0162561A1 (en) * 1984-04-13 1985-11-27 Exxon Research And Engineering Company Surface dressing of roads

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3980598A (en) * 1974-08-28 1976-09-14 Basf Aktiengesellschaft Mixtures based on ethylene copolymers and asphalt
EP0162561A1 (en) * 1984-04-13 1985-11-27 Exxon Research And Engineering Company Surface dressing of roads

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CA1315438C (en) 1993-03-30
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