POLYMER MODIFIED ASPHALT FOR INDUSTRIAL APPLICATIONS

Abstract

This invention provides for a method for producing polymer modified asphalt (PMA) using base asphalt (bitumen) blended with partially air blown (“puffed”) asphalt which is further modified with polymers and additives to attain desired properties for industrial applications. The partially blown or blown asphalt is oxidized to a target softening point to suit the application. In another embodiment, the base asphalt is blended with hard PEN asphalt (“Zero PEN Asphalt”) which is further modified with polymers and additives to attain desired properties for industrial applications. By using the partially oxidized asphalt or blending the base asphalt with partially oxidized asphalt or hard PEN asphalt, the amount of polymers and additives needed to achieve desired properties and performance are significantly reduced. In fact, this technique can be used to attain polymer modified asphalt having a highly desirable combination of characteristics that could not otherwise be attained using the base asphalt.

Claims

1. An industrial asphalt composition which is comprised of a base asphalt, a partially blown asphalt, a polymer modifier, and at least one wax, wherein the base asphalt is not air blown, wherein the base asphalt is asphalt flux, wherein the partially blown asphalt is asphalt flux, and wherein the industrial asphalt composition has softening point which is within the range of 120° F. to 260° F., a penetration at 77° F. which is within the range of 12 dmm to 40 dmm, and a rotational viscosity which is within the range of 90 cP to 700 cP at 400° F.

2. The industrial asphalt composition of claim 1 wherein the partially blown asphalt has a softening point which is within the range of 120° F. to 230° F., wherein the partially blown asphalt has a penetration value which is within the range of 5 dmm to 30 dmm at 77° F., wherein the partially blown asphalt has a rotational viscosity which is within the range of 120 cP to 450 cP at 400° F.

3. The industrial asphalt composition of claim 1 wherein the industrial asphalt composition includes 5 weight percent to 95 weight percent of the partially blown asphalt and from 5 weight percent to 95 weight percent of the base asphalt.

4. The industrial asphalt composition of claim 1 wherein the base asphalt is selected from the group consisting of paving grade asphalts, flux grade asphalts, PEN grade asphalts, viscosity grade asphalts, and aged residue grade asphalts.

5. The industrial asphalt composition of claim 1 wherein the polymer modifier is present at a level which is within the range of 0.5 weight percent to 12 weight percent, and wherein the wax is present at a level which is within the range of 0.5 weight percent to 5 weight percent.

6. The industrial asphalt composition of claim 1 wherein the polymer modifier is selected from the group consisting of SBS, SEBS, copolymers of functionalized reactive elastomers (RET) or glycidyl acrylate copolymers of methyl, ethyl, butyl acrylates, and polyolefin homo-polymers and copolymers.

7. The industrial asphalt composition of claim 1 wherein the wax has a softening point which is within the range of 200° F. to 330° F., a penetration value at 77° F. which is within the range of 0.5 dmm to 15 dmm, and a rotational viscosity which is within the range of 2 cP to 100 cP at 400° F., and COC flash point of greater than 400° F.

8. An industrial asphalt composition which is comprised of a base asphalt, a hard PEN asphalt, a polymer modifier, and at least one wax, wherein the base asphalt is asphalt flux, wherein the hard PEN asphalt is asphalt flux, wherein the hard PEN asphalt has a penetration value which is within the range of 0.2 dmm to 15 dmm at 77°, wherein the industrial asphalt composition has softening point which is within the range of 120° F. to 260° F., a penetration at 77° F. which is within the range of 12 dmm to 40 dmm, and a rotational viscosity which is within the range of 90 cP to 700 cP at 400° F.

9. The industrial asphalt composition of claim 8 wherein the hard PEN asphalt has a softening point which is within the range of 140° F. to 240° F., wherein the hard PEN asphalt has a penetration value which is within the range of 0.2 dmm to 10 dmm at 77° F., and wherein the hard PEN asphalt has a rotational viscosity which is within the range of 25 cP to 450 cP at 400° F.

10. The industrial asphalt composition of claim 8 wherein the industrial asphalt composition includes 5 weight percent to 95 weight percent of the hard PEN asphalt and from 5 weight percent to 95 weight percent of the base asphalt.

11. The industrial asphalt composition of claim 8 wherein the base asphalt is selected from the group consisting of paving grade asphalts, flux grade asphalts, PEN grade asphalts, viscosity grade asphalts, and aged residue grade asphalts.

12. The industrial asphalt composition of claim 8 wherein the polymer modifier is present at a level which is within the range of 0.5 weight percent to 12 weight percent, and wherein the wax is present at a level which is within the range of 0.5 weight percent to 5 weight percent.

13. The industrial asphalt composition of claim 8 wherein the polymer modifier is selected from the group consisting of SBS, SEBS, copolymers of functionalized reactive elastomers (RET) or glycidyl acrylate copolymers of methyl, ethyl, butyl acrylates, and polyolefin homo-polymers and copolymers.

14. The industrial asphalt composition of claim 8 wherein the wax has a softening point which is within the range of 200° F. to 330° F., a penetration value at 77° F. which is within the range of 0.5 dmm to 15 dmm, and a rotational viscosity which is within the range of 2 cP to 100 cP at 400° F., and COC flash point of greater than 400° F.

15. The industrial asphalt composition of claim 8 wherein the industrial asphalt composition has softening point which is within the range of 130° F. to 260° F., a penetration at 77° F. which is within the range of 12 dmm to 40 dmm, and a rotational viscosity which is within the range of 90 cP to 700 cP at 400° F.

16. A method for producing an industrial asphalt composition which comprises blending a partially blown asphalt or a hard PEN asphalt into an asphalt base which is selected from the group consisting of paving grade asphalts, flux grade asphalts, PEN grade asphalts, viscosity grade asphalts, and aged residue grade asphalts, wherein the asphalt base is not air blown, wherein the base asphalt is asphalt flux, wherein the partially blown asphalt or hard PEN asphalt is asphalt flux, and wherein the industrial asphalt composition has softening point which is within the range of 120° F. to 260° F., a penetration at 77° F. which is within the range of 12 dmm to 40 dmm, and a rotational viscosity which is within the range of 90 cP to 700 cP at 400° F.

17. The method of claim 16 wherein partially blown asphalt is blended into the asphalt base, wherein the partially blown asphalt has a softening point which is within the range of 120° F. to 230° F., wherein the partially blown asphalt has a penetration value which is within the range of 5 dmm to 30 dmm at 77° F., and wherein the partially blown asphalt has a rotational viscosity which is within the range of 120 cP to 450 cP at 400° F.

18. The method of claim 16 wherein the hard PEN asphalt is blended into the asphalt base, wherein the hard PEN asphalt has a softening point which is within the range of 140° F. to 240° F., wherein the hard PEN asphalt has a penetration value which is within the range of 0.5 dmm to 15 dmm at 77° F., and wherein the hard PEN asphalt has a rotational viscosity which is within the range of 25 cP to 450 cP at 400° F.

19. The method of claim 16 wherein 20 weight percent to 80 weight percent of the hard PEN asphalt is blended into 20 weight percent to 80 weight percent of the base asphalt, wherein the hard PEN asphalt has a penetration value which is within the range of 0.2 dmm to 10 dmm at 77° F., wherein a polymer modifier is further blended into the asphalt base at a level which is within the range of 0.5 weight percent to 12 weight percent, and wherein a wax is further blended into the asphalt base at a level which is within the range of 0.5 weight percent to 5 weight percent.

20. A polymer modified asphalt composition which is comprised of the industrial asphalt composition of claim 1 and at least one aggregate or filler.

Description

DETAILED DESCRIPTION OF THE INVENTION

[0030] In accordance with this invention, partially oxidized or partially blown asphalt is further modified using polymers and/or additives. By using the partially oxidized asphalt or blending the base asphalt with partially oxidized asphalt or hard PEN asphalt, the amount of polymers and additives needed to achieve desired properties and performance are significantly reduced. Targeting various softening points for the partially oxidized asphalt which may or may not be blended with base asphalts (at various ratios) can be used to mitigate base asphalt quality variation. This technique of blending partially air blown asphalt and/or hard PEN asphalt with base asphalt broadens the types of asphalt available for use which would not otherwise be physically, mechanically or chemically suitable for use.

[0031] In the practice of this invention partially oxidized or partially blown asphalt and the base asphalt are blended and modified using polymers and/or additives. The partially blown asphalt has softening point which is within the range of 120° F. to 230° F., a penetration at 77° F. of 5 dmm to 30 dmm and a rotational viscosity of 120-450 cP at 400° F. More preferably the partially blown asphalt has softening point which is within the range of 140° F. to 190° F., a penetration at 77° F. which is within the range of 8 dmm to 16 dmm and a rotational viscosity which is within the range of 120 cP to 400 cP at 400° F.

[0032] Hard PEN grade asphalts (“Zero PEN asphalts”) from refineries blended with base asphalts and modified with polymers and/or additives can be utilized in the practice of this invention. The hard PEN asphalt utilized in the process of this invention will have a softening point which is within the range of 140° F. to 240° F., a penetration at 77° F. of 0.5 dmm to 15 dmm and rotational viscosity which is within the range of 25 cP to 450 cP at 400° F. The hard PEN asphalt will preferable have a softening point which is within the range of 150° F. to 210° F., a penetration value at 77° F. which is within the range of 0.2 dmm to 10 dmm, and a rotational viscosity which is within the range of 140 cP to 350 cP at 400° F.

[0033] Partially blown asphalt and/or hard PEN asphalt and base asphalt are blended together and can be further modified using asphalt modification polymers and/or additional additives. The partially oxidized asphalt constitutes 5 weight percent to 95 weight percent of the PMA and more preferably 20 weight percent to 90 weight percent of the PMA. Asphalt blends made with hard PEN asphalt will typically contain from 5 weight percent to 50 weight percent of the hard PEN asphalt and 50 weight percent to 95 weight percent of the base asphalt. The asphalt blend will preferably contain from 5 weight percent to 40 weight percent of the hard PEN asphalt.

[0034] The polymers that can be used for asphalt modification in accordance with this invention include block copolymers, such as SBS, SEBS, copolymers of functionalized reactive elastomers (RET) or glycidyl acrylate copolymers of methyl, ethyl, butyl acrylates, and polyolefin homo-polymers and copolymers such as polypropylene, polypropylene/ethylene copolymers and the likes. Partially blown asphalt can be blended with a block copolymer such as SEBS or SBS and a wax to yield a PMA suitable for manufacturing roofing products, paving and other industrial applications. The hard PEN asphalt can also be blended with base asphalt which is further modified with a block copolymer such as SEBS or SBS and wax to yield PMA suitable for paving, manufacturing roofing products and other industrial applications. The partially blown asphalt or hard PEN asphalt can also be blended with base asphalt which is further modified with polyolefins, crumb rubber, or ground tire rubber and a wax to yield PMA suitable for manufacturing roofing products, road paving and other industrial applications.

[0035] In some cases, cross linking agents and co-agents may be used to improve polymer network and dispersion in the PMA. The wax used in such applications can be natural or synthetic and have a softening point which is within the range of 200° F. to 330° F., a penetration value at 77° F. which is within the range of 0.5 dmm to 15 dmm and a rotational viscosity of which is within the range of 2 cP to 100 cP at 400° F. and COC flash point of greater than 400° F. The wax will more preferably have a softening point which is within the range of 200° F. to 350° F., a penetration at 77° F. which is within the range of 0.5 dmm to 10 dmm and rotational viscosity which is within the range of 2 cP to 150 cP at 400° F. and a COC flash point of greater than 475° F.

[0036] The ground tire rubber that can be employed in the practice of this invention will typically have a particle size which is within the range of 80 to 300 mesh and will more preferably have a mesh size which is within the range of 140 to 200. The plasticizers that can be utilized in the practice of this invention include aromatic oils, naphthenic oils, triglyceride oils, vegetable oils, and other forms of natural and synthetic oils.

[0037] Where the polymer modified asphalt (PMA) has softening point which is within the range of 130° F. to 260° F., a penetration at 77° F. which is within the range of 12 dmm to 40 dmm, and a rotational viscosity which is within the range of 90 cP to 700 cP at 400° F. More preferably the modified asphalt will have a softening point which is within the range of 200° F. to 250° F., a penetration at 77° F. of 15 dmm to 32 dmm, and rotational viscosity which is within the range of 100 cP to 500 cP at 400° F.

[0038] The industrial asphalt produced can be used in making roofing products and other industrial products using standard procedures. For instance, the industrial asphalt can be blended with fillers, stabilizers (like limestone, stonedust, sand, granule, etc.), polymers, recycled tire rubber, recycled engine oil residue, recycled plastics, softeners, antifungal agents, biocides (algae inhibiting agents), and other additives. For instance, aggregate and/or fillers can be added to the PMA for the manufacture of building materials, roofing materials (shingles, cap sheets, rolls base sheets and the like), paving and other industrial applications. By utilizing asphalts that are partially blown or not blown at all, blow loss and emissions are significantly reduced thus providing a more environmentally friendly method of producing asphaltic coating.

[0039] This invention is illustrated by the following examples that are merely for the purpose of illustration and are not to be regarded as limiting the scope of the invention or the manner in which it can be practiced. Unless specifically indicated otherwise, parts and percentages are given by weight.

EXAMPLES

[0040] A series of blends were made in accordance with this invention and blends were also made in accordance with the prior art for comparative purposes. These blends were made with various paving grade asphalts which could not be processed using conventional techniques into industrial asphalt which would be useful in roofing applications. A summary of these compositions and their properties is reported in the following tables.

TABLE-US-00001 TABLE 1 Base Asphalt Blown to Partially Roofing Soft- PEN Base Hard Blown coating Poly- SE- Plasti- ening Viscosity at Block Exam- Asphalt PEN Asphalt Softening RET GTR olefin SBS BS cizer Wax Point at 400° 77° F. # ple % % % Point Target % % % % % % % % (° F.) F. (cP) (dmm) 1 A Base 0.0 0.0 100.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 212.3 494 9.6 Asphalt A1 0.0 0.0 91.0 0.0 0.0 0.0 0.0 0.0 4.0 4.0 1.0 209 309 17.5 A1-1 91.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 4.0 4.0 1.0 140 97 53.0 A1-2 87.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 8.0 4.0 1.0 200 215 40.3 A2 0.0 0.0 91.0 0.0 0.0 0.0 0.0 0.0 4.0 4.0 1.0 207 318 17.3 A2-1 91.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 4.0 4.0 1.0 178 99 61.3 A2-2 87.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 8.0 4.0 1.0 224 221 52.0 2 B Base 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 209 395 11.0 Asphalt B1 74.0 20.0 0.0 100.0 0.0 0.0 0.0 0.0 4.5 0.0 1.5 214 206 17.3 B1-1 94.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 4.5 0.0 1.5 202 124 37.0 B1-2 90.5 0.0 0.0 0.0 0.0 0.0 0.0 0.0 8.0 0.0 1.5 227 367 28.3 B2 74.0 20.0 0.0 0.0 0.0 0.0 0.0 0.0 4.5 0.0 1.5 211 185 22.0 B2-1 94.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 4.5 0.0 1.5 202 124 37.0 B2-2 90.5 0.0 0.0 0.0 0.0 0.0 0.0 0.0 8.0 0.0 1.5 227 367 28.3 3 C Base 0.0 0.0 100.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 209 395 11.0 Asphalt C1 75.5 20.0 0.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 245 108 26.0 C1-1 95.5 0.0 0.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 215 54 49.3 C1-2 93.5 0.0 0.0 0.0 4.0 0.0 0.0 0.5 0.0 0.0 2.0 233 115 44.0 C2 75.5 20.0 0.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 232 120 31.0 C2-1 95.5 0.0 0.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 213 83 40.0 C2-2 92.0 0.0 0.0 0.0 2.0 0.0 0.0 4.0 0.0 0.0 2.0 239 160 34.0 D1 75.5 0.0 20.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 253 136 27.0 D1-1 95.5 0.0 0.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 213 83 40.0 D1-2 92.0 0.0 0.0 0.0 2.0 0.0 0.0 4.0 0.0 0.0 2.0 239 160 34.0 D2 75.5 0.0 20.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 223 118 37.0 D1-1 95.5 0.0 0.0 0.0 2.0 0.0 0.0 0.5 0.0 0.0 2.0 220 95 34.0 D1-2 92.0 0.0 0.0 0.0 2.0 0.0 0.0 4.0 0.0 0.0 2.0 249 123 38.2 4 E Base 0.0 0.0 100.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 208 391 5.0 Asphalt E1 73 20.0 0.0 0.0 2.0 0.0 0.0 3.0 0.0 0.0 2.0 238 222 24.7 E1-1 93 0.0 0.0 0.0 2.0 0.0 0.0 3.0 0.0 0.0 2.0 223 144 30.0 E1-2 91.5 0.0 0.0 0.0 2.0 0.0 0.0 3.0 0.0 0.0 2.0 231 217 27.0 E2 73 20.0 0.0 0.0 2.0 0.0 0.0 3.0 0.0 0.0 2.0 232 154 28.3 E2-1 93 0.0 0.0 0.0 2.0 0.0 0.0 3.0 0.0 0.0 2.0 219 125 38.0 E2-2 91.5 0.0 0.0 0.0 2.0 0.0 0.0 3.0 0.0 0.0 2.0 252 196 32.0 5 F Base 0.0 0.0 100.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 209 230 11.0 Asphalt F1 73 30.0 0.0 0.0 0.0 2.5 3.0 0.0 0.0 0.0 1.5 219 236 29.0 F1-1 93 0.0 0.0 0.0 0.0 2.5 3.0 0.0 0.0 0.0 1.5 192 104 47.3 F1-2 91.5 0.0 0.0 0.0 0.0 2.5 4.5 0.0 0.0 0.0 1.5 211 172 42.3 F2 73 30.0 0.0 0.0 0.0 2.5 3.0 0.0 0.0 0.0 1.5 201 202 22.7 F2-1 93 0.0 0.0 0.0 0.0 2.5 3.0 0.0 0.0 0.0 1.5 159 122 33.5 F2-2 91.5 0.0 0.0 0.0 0.0 2.5 4.5 0.0 0.0 0.0 1.5 207 238 33.0 6 G Base 0.0 100.0 0.0 0.0 0.0 0.0 0.0 0.0 0.0 212 494 9.6 Asphalt G1 43 0.0 50.0 0.0 0.0 2.5 3.0 0.0 0.0 0.0 1.5 238 279 18.3 G1-1 93 0.0 0.0 0.0 0.0 2.5 3.0 0.0 0.0 0.0 1.5 202 139 37.3 G1-2 91.5 0.0 0.0 0.0 0.0 2.5 4.5 0.0 0.0 0.0 1.5 248 598 32.0

TABLE-US-00002 TABLE 2 % Softening Viscosity Block Base Partially % Poly- % Point at 400° F. PEN at # Asphalt Blown SBS Butadiene Resin (° F.) (cP) 77° F. (dmm) 7 H1 No 0.00 0.00 0.00 132 31 33 H1-1 No 6.50 0.00 4.00 237 310 17 8 I1 Yes 0.00 0.00 0.00 210 209 12.3 I1-2 Yes 0.00 6.00 0.00 225 263 16 9 J1 Yes 0.00 0.00 178 144 13 J1-2 Yes 0.00 8.50 0.00 211 193 18 10 K1 Yes 0.00 0.00 0.00 184 143 13 K-2 Yes 0.00 8.50 0.00 221 190 16

[0041] While certain representative embodiments and details have been shown for the purpose of illustrating the subject invention, it will be apparent to those skilled in this art that various changes and modifications can be made therein without departing from the scope of the subject invention.