SBS (Styrene-Butadiene-Styrene) modified asphalt and production method thereof
A technology of modified asphalt and production method, which is applied to building components, building insulation materials, buildings, etc., can solve the problem of high processing cost, and achieve the effect of shortening modification time, excellent modification effect, and shortening modification time.
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Embodiment 1
[0018] (1) Heat 5kg of No. 70 matrix asphalt to make its actual temperature reach the processing permit temperature of 175-185°C, and add it to No. 1 mixing tank;
[0019] (2) When adding asphalt to cover the bottom of the tank, add 200g of linear SBS modifier at the same time, and stir, and the stirring temperature is maintained at 175-185°C;
[0020] (3) After the mixing is complete, send the homogeneously mixed asphalt obtained in step (2) into the colloid mill through the glue through the pipeline, and at the same time continuously pump into the colloid mill to pump Kunlun brand KA80 type petroleum (aromatic rubber oil) 100g and 8g of sulfur powder, after grinding, pump them continuously into the No. 2 mixing tank; after the asphalt in the No. 1 mixing tank completely enters the No. 2 mixing tank, the modified asphalt in the No. In the storage tank, the SBS modified asphalt is obtained; during the grinding process, the No. 2 mixing tank continues to stir until the asphalt ...
Embodiment 2
[0022] (1) Heat 20kg of No. 70 matrix asphalt in the No. 1 mixing tank, so that its actual temperature reaches the processing license temperature of 175-185 ° C, and add it to the No. 1 mixing tank;
[0023] (2) When the amount of asphalt added is half of the total amount, add 720g of linear SBS modifier at the same time, and stir, and the stirring temperature is maintained at 175-185°C;
[0024] (3) After the stirring is complete, the uniformly mixed asphalt obtained in step (2) is sent into the colloid mill through the pipeline, and at the same time, the Kunlun brand KN4006 type petroleum (naphthenic rubber oil) 600g and sulfur are continuously pumped into the colloid mill 36g of powder, after grinding, pump it continuously into the No. 2 mixing tank; after the asphalt in the No. 1 mixing tank completely enters the No. 2 mixing tank, the modified asphalt in the No. 2 mixing tank is ground again by a colloid mill and then pumped into the storage tank , to obtain SBS modified ...
Embodiment 3
[0026] The SBS modified asphalt that embodiment 2 produces is detected, and each index is as follows:
[0027] Penetration (25°C, 100g, 5s): 75~61 (0.1mm); Penetration Index PI: -0.39; Ductility (5°C, 5cm / min): 38cm; Softening point: 84~61.5°C; Dynamic viscosity (60°C): >13000Pa·s; kinematic viscosity (135°C): 2.050Pa·s; flash point: 351°C; solubility: 99.74%; elastic recovery (25°C): 94%; storage stability segregation, 48h softening point difference: 0.2°C;
[0028] Residue after RTFOT: mass change 0.06%; ductility (5°C) 21 cm.
[0029] It can be seen from the various quality indicators obtained by testing that the modified asphalt prepared by the production method of SBS modified asphalt of the present invention can fully meet the requirements of I-C grades.
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