Asphalt compositions comprising hydrogenated and aminated vegetable oil, asphalt products made from such asphalt compositions, and the methods of making and using such compositions and products
a technology of hydrogenated and aminated vegetable oil and asphalt composition, which is applied in the field of asphalt compositions, to asphalt products made from such asphalt compositions, and the methods of making and using such compositions, and can solve the problems of high cost of novachip bonded friction course system, high cost of spray paver machines, and inability to justify the expense of many paving contractors and state and county transportation agencies. to achieve the effect of reducing the bond strength
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example 1
[0205]Bond Strength Evaluation of DOT™ C10 and DOT™ C12 Tack Coat
[0206]Bond strength testing was conducted for each tack coat sample at two different application rates and substrate conditions. The substrate conditions represented both milled and unmilled surfaces. Three replicates were prepared for each combination, for a total of 24 samples tested.
[0207]General Procedure. A single, 9.5 mm nominal maximum aggregate size (NMAS) Superpave mix developed by Basic Construction Company, LLC, located in Newport News, Va., was used as the surface mix for all samples tested. The mix design contained 35 percent recycled asphalt pavement (RAP), and had an optimum asphalt content of 5.55 percent. For the substrate samples, both milled and unmilled samples were used. The unmilled samples were prepared using a 12.5 mm NMAS Superpave mix designed to meet Alabama Department of Transportation's (ALDOT) 424 Specifications. The optimum asphalt content for the mixture was 4.6 percent. For the DOT™ C10...
example 2
[0225]This example shows the effect of additive on softening point and Pen value of PG 67-22 asphalt binder. Results are shown in Table 4 of FIG. 7.
[0226]As shown by the data, with the additive of the present invention, there is a steep increase in Softening Point without need for blowing. As an improvement of the additive over blowing, there is no oxidative aging of binder as in blowing. Also, use of the additive of the present invention results in less than 10% of batch cycle time compared to blowing. Further, use of the additive of the present invention results in more than 10 times production volume compared to blowing. As an advantage, use of the additive of the present invention may be with standard production equipment. Finally, use of the additive of the present invention results in moderate decrease in Pen value unlike blowing or hard wax additives such as Fischer-Tropsch Waxes.
example 3
[0227]This example shows use of the additive of the present invention in the production of BUR Roofing Grades from standard refinery asphalt streams and demonstrates that blowing is not necessary. The results are shown in Table 5 of FIG. 8.
[0228]As shown, use of the additives of the preset invention makes it possible to use a wider range of refinery asphalt binder streams thus resulting in a more varied supply flexibility. Use of the additives of the present invention, eliminates blowing associated pollution / emissions, energy consumption, long batch cycle times, higher viscosity of binder and formation of carcinogenic components resultant from blowing. Also, use of the additives of the present invention substantially enhance operational safety as the binder may be handled at lower temperatures.
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Abstract
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