Disclosure of Invention
Aiming at the defects of the prior art, the invention aims to provide an anti-aging high-viscosity modified asphalt additive and a preparation method thereof. The high-viscosity modified asphalt additive is developed to improve the viscosity of asphalt, is convenient to use and has better anti-aging performance. Another object of the present invention is to improve the compatibility and uniform dispersibility between the additive and the asphalt.
The invention provides an anti-aging high-viscosity modified asphalt additive which comprises the following raw material components in parts by weight:
SBS: 100 parts of (A);
petroleum resin: 20-40 parts of a solvent;
aromatic oil: 10-40 parts;
stabilizers and their coatings: 5-8 parts;
anti-aging agent: 1-4 parts;
the stabilizer and the coating thereof are granular, the diameter of the granules is 100-150 micrometers, and the thickness of the coating particle wall material is 3-6 micrometers. The weight ratio of the coating to the stabilizer is (2-7): 1, preferably (3-5): 1.
the coating is surface-modified silicon dioxide, and the surface-modified silicon dioxide is preferably organosilane-modified silicon dioxide. The organosilane is one or more of phenyltrimethoxysilane, phenyltriethoxysilane, phenyldichlorosilane and phenyltrichlorosilane.
The stabilizer is sulfur, preferably a mixture of sulfur and polysulfides. Wherein the proportion of sulfur and polysulfide is (1-3): 1. the polysulfide is one or more of diaryl disulfide, dimethyl disulfide and methyl ethyl disulfide.
The anti-aging agent may be a hindered phenol type antioxidant. The anti-aging agent is one or more of 2, 6-di-tert-butyl-p-cresol, p-tert-butyl catechol, 3, 5-di-tert-butyl-4-hydroxybenzyl diethyl phosphonate, n-octadecyl beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate, isooctyl beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate, 4' -thiobis (6-tert-butyl-3-methylphenol), pentaerythritol tetrakis [ beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) propionate ] and 1,3, 5-trimethyl-2, 4, 6-tris (3, 5-di-tert-butyl-4-hydroxybenzyl) benzene.
The SBS has a linear structure and the molecular weight of the SBS is 5-25 ten thousand.
The petroleum resin is carbon five petroleum resin, and the softening point of the petroleum resin is 90-120 ℃.
The aromatic oil is a component rich in aromatic hydrocarbon, and the weight content of the aromatic hydrocarbon is 40-80%. The extract oil can be derived from the extraction oil of the lubricant base oil in the solvent refining process, such as furfural refined extract oil, phenol refined extract oil and the like.
The invention also provides a preparation method of the anti-aging high-viscosity modified asphalt additive, which comprises the following steps:
(1) preparing a stabilizer suspension;
(2) adding dilute hydrochloric acid into the stabilizer suspension, and then dropwise adding ethyl orthosilicate to obtain a stabilizer and a coating thereof;
(3) adding a stabilizer and a coating thereof and organosilane into an organic solvent for surface modification reaction, and cooling to obtain the surface-modified stabilizer and the coating thereof;
(4) and uniformly mixing SBS, petroleum resin, aromatic oil, the surface modified stabilizer, the surface modified coating thereof and the anti-aging agent, blending, extruding and granulating by an extruder to obtain the anti-aging high-viscosity modified asphalt additive.
In the step (1), the stabilizer suspension is prepared by shearing and dispersing the stabilizer in an aqueous solution of sodium dodecyl sulfate and gelatin. The weight ratio of the stabilizer, sodium dodecyl sulfate, gelatin and water is (3-10): (0.01-3): (0.5-5): 50, preferably (5-8): (0.05-1): (1-3): 50. the shearing rotating speed is 3000-5000 rpm, and the time is 1-2 h.
The stabilizer is sulfur, preferably a mixture of sulfur and polysulfides. Wherein the proportion of sulfur to polysulfide is (1-3): 1.
in the step (2), the concentration of the dilute hydrochloric acid in the solution is 0.07-0.14 mol/L, preferably 0.09-0.10 mol/L.
And (3) dropwise adding tetraethoxysilane, stirring at a certain temperature for reaction, filtering, washing and drying to obtain the stabilizer and the coating thereof. The stirring temperature is 50-60 ℃, the stirring speed is 300-400 rpm, and the stirring time is 2-4 h. The weight ratio of the ethyl orthosilicate to the stabilizer is (2-7): 1, preferably (3-5): 1. the filtration, washing and drying can adopt the conventional method. The washing can be carried out by using solvents such as deionized water, ethanol and the like, and the drying is carried out to volatilize the solvents, wherein the drying temperature can be 50-80 ℃, and the drying time can be 3-5 h.
In the step (3), the surface modification reaction is performed under a heating reflux condition. The reaction temperature is 60-80 ℃, and the reaction time is 1-3 h.
In the step (3), after cooling, filtering, washing and drying are carried out to obtain the surface-modified stabilizer and the coating thereof. The filtration, washing and drying can be carried out by adopting a conventional method, the washing can be carried out by using solvents such as ethanol, the drying can be carried out to volatilize the solvents, the drying temperature can be 50-80 ℃, and the drying time can be 3-5 h.
In the step (3), the weight ratio of the stabilizer and the coating thereof, the organosilane and the organic solvent is 1: (0.01-0.15): (10-30), preferably 1: (0.08-0.12): (10-30), and the organic solvent is preferably one or more of xylene, toluene, cyclohexanone, chlorobenzene and pyridine.
In step (4), the extrusion is performed in an extruder. The extruder may be a conventionally used extruder. Because the extrudate contains the stabilizer and the coating particles thereof, the extrusion temperature is preferably 110-140 ℃ in order to avoid damaging the stabilizer and the coating particles thereof in the extrusion process. Preferably a screw extruder, and the rotating speed of the screw is 30-150 r/min. Further preferred is a twin-screw extruder, the two screws being parallel to each other in the barrel. The temperature in the barrel of the extruder is preferably controlled by multiple sections, for example, the barrel of the extruder can be divided into eight temperature sections, and the specific operating conditions are as follows: a first section is 110-120 ℃; the second section is 115-125 ℃; three sections are 120-130 ℃; the temperature of the fourth section is 120-130 ℃; five sections are 125-135 ℃; six sections are 130-140 ℃; seven sections are 125-135 ℃; eight sections are 120-130 ℃.
Compared with the prior art, the anti-aging high-viscosity modified asphalt additive and the preparation method thereof have the following advantages:
(1) the stabilizer is coated and then added into the high-viscosity modified asphalt additive, so that the method is convenient to use, avoids the step of adding the stabilizer additionally, separates the stabilizer from SBS, avoids the advanced crosslinking of SBS, and is beneficial to the uniform dispersion of the high-viscosity additive in the asphalt. Under the synergistic action of sulfur and polysulfide, the modified asphalt has better stability and dispersibility.
(2) The stabilizing agent and the capsule wall material of the coating thereof are silicon dioxide modified by organosilane, not only play a role in isolation, but also can increase the anti-aging performance, and can improve the problem of poor aging resistance of the drainage pavement prepared by using the high-viscosity asphalt additive under the synergistic action of the stabilizing agent and the anti-aging agent. The surface of the capsule wall material silicon dioxide is modified by macromolecular organosilane, and the modified capsule wall material silicon dioxide has good compatibility with asphalt.
(3) The anti-aging high-viscosity modified asphalt additive can obviously improve the viscosity of asphalt and enhance the cohesiveness of the asphalt, not only can be directly added into the asphalt to prepare the high-viscosity modified asphalt, but also can be added in the process of mixing the mixture, and has convenient construction and simple use.
Detailed Description
The technical solutions of the present invention are further described below by way of examples, which are not intended to limit the present invention.
Example 1
(1) 2.5 parts by weight of sulfur, 2.5 parts by weight of diaryl disulfide, 0.05 part by weight of sodium dodecylsulfate and 1 part by weight of gelatin were added to 50 parts by weight of the aqueous solution, and sheared at 3000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then dropwise adding 15 parts by weight of tetraethoxysilane, stirring and reacting for 2 hours at 50 ℃ and 300 rpm, cooling, filtering, washing with deionized water, and drying for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 0.8 part by weight of phenyl trimethoxy silane into 100 parts by weight of toluene, carrying out surface modification reaction for 1h at 60 ℃, cooling, filtering, washing with ethanol, and drying for 3h at 50 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%), 5 parts by weight of surface modified stabilizer and coating thereof (particle diameter is 137 micrometers, wall material thickness is 3.3 micrometers) and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, and then carrying out blending extrusion and granulation by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth section is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Example 2
(1) 3 parts by weight of sulfur, 2 parts by weight of dimethyl disulfide, 0.05 part by weight of sodium dodecyl sulfate and 3 parts by weight of gelatin were added to 50 parts by weight of the aqueous solution, and the mixture was sheared at 4000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then 24 parts by weight of ethyl orthosilicate is dropwise added, stirred and reacted for 3 hours at 55 ℃ and 350 rpm, filtered after cooling, washed by deionized water, and dried for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 1 part by weight of phenyl triethoxy silane into 200 parts by weight of toluene, carrying out surface modification reaction for 1h at 70 ℃, cooling, filtering, washing with ethanol, and drying for 4h at 50 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (molecular weight is 15 ten thousand), 30 parts by weight of carbon five petroleum resin (softening point is 100 ℃), 30 parts by weight of aromatic oil (aromatic hydrocarbon content is 60 wt%), 7 parts by weight of surface-modified stabilizer and coating thereof (particle diameter is 125 micrometers, wall material thickness is 5.6 micrometers), and 3 parts by weight of 4,4' -thiobis (6-tert-butyl-3-methylphenol), blending, extruding and granulating by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: a first stage is 115 ℃; the second section is 120 ℃; the third section is 125 ℃; the fourth stage is 125 ℃; the fifth section is 130 ℃; the six sections are 135 ℃; the seven sections are 130 ℃; the eight sections are 125 ℃, and the rotating speed of the screw is 80 r/min.
Example 3
(1) 6 parts by weight of sulfur, 2 parts by weight of ethyldisulfide, 0.08 part by weight of sodium dodecylsulfate and 1 part by weight of gelatin were added to 50 parts by weight of an aqueous solution, and sheared at 5000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.10 mol/L. And then, dropwise adding 32 parts by weight of ethyl orthosilicate, stirring and reacting for 3 hours at 60 ℃ and 350 rpm, cooling, filtering, washing with deionized water, and drying for 5 hours at 60 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 1 part by weight of phenyl dichlorosilane into 300 parts by weight of toluene, carrying out surface modification reaction for 2 hours at 75 ℃, cooling, filtering, washing with ethanol, and drying for 5 hours at 60 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (with the molecular weight of 20 ten thousand), 20 parts by weight of carbon five petroleum resin (with the softening point of 110 ℃), 40 parts by weight of aromatic oil (with the content of aromatic hydrocarbon of 80 wt%), 8 parts by weight of stabilizer after surface modification and coating thereof (with the particle diameter of 110 micrometers and the wall material thickness of 4.2 micrometers) and 4 parts by weight of beta- (3, 5-di-tert-butyl-4-hydroxyphenyl) isooctyl propionate, blending, extruding and granulating by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first stage is 120 ℃; the second section is 125 ℃; the third section is 130 ℃; the fourth stage is 130 ℃; the fifth section is 135 ℃; the six sections are 140 ℃; the seven sections are 135 ℃; the eight sections are at 130 ℃, and the rotating speed of the screw is 120 r/min.
Example 4
The only difference from example 1 is that sulfur alone is used as a stabilizer. The preparation process comprises the following steps:
(1) 5 parts by weight of sulfur, 0.05 part by weight of sodium dodecyl sulfate and 1 part by weight of gelatin are added into 50 parts by weight of aqueous solution, and the mixture is sheared for 1 hour at the rotating speed of 3000 rpm to prepare the stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then dropwise adding 15 parts by weight of ethyl orthosilicate, stirring and reacting for 2 hours at 50 ℃ and 300 rpm, cooling, filtering, washing with deionized water, and drying for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 0.8 part by weight of phenyl trimethoxy silane into 100 parts by weight of toluene, carrying out surface modification reaction for 1h at 60 ℃, cooling, filtering, washing with ethanol, and drying for 3h at 50 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%), 5 parts by weight of surface modified stabilizer and coating thereof (particle diameter is 139 micrometers, wall material thickness is 3.2 micrometers), and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, blending, extruding and granulating by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first stage is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth section is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Comparative example 1
The difference from example 1 is only the use of polysulfide alone as stabilizer. The preparation process comprises the following steps:
(1) 5 parts by weight of a diaryl disulfide, 0.05 part by weight of sodium dodecylsulfate and 1 part by weight of gelatin were added to 50 parts by weight of an aqueous solution, and sheared at 3000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then dropwise adding 15 parts by weight of ethyl orthosilicate, stirring and reacting for 2 hours at 50 ℃ and 300 rpm, cooling, filtering, washing with deionized water, and drying for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 0.8 part by weight of phenyl trimethoxy silane into 100 parts by weight of toluene, carrying out surface modification reaction for 1 hour at 60 ℃, cooling, filtering, washing with ethanol, and drying for 3 hours at 50 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%), 5 parts by weight of surface-modified stabilizer and coating thereof (particle diameter is 134 micrometers, wall material thickness is 3.4 micrometers), and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, blending, extruding and granulating by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth section is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Comparative example 2
The only difference is that the stabilizer and its coating are not surface-modified, as in example 1. The preparation process comprises the following steps:
(1) 2.5 parts by weight of sulfur, 2.5 parts by weight of diaryl disulfide, 0.05 part by weight of sodium dodecylsulfate and 1 part by weight of gelatin were added to 50 parts by weight of the aqueous solution, and sheared at 3000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then dropwise adding 15 parts by weight of ethyl orthosilicate, stirring and reacting for 2 hours at 50 ℃ and 300 rpm, cooling, filtering, washing with deionized water, and drying for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%), 5 parts by weight of sulfur-coated stabilizer and its coating (particle diameter is 137 micrometers, wall material thickness is 3.3 micrometers) and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, and then carrying out blending extrusion and granulation by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth section is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Comparative example 3
The only difference from example 1 is that the stabilizer is uncoated. The preparation process comprises the following steps:
uniformly mixing 100 parts by weight of SBS (with the molecular weight of 10 ten thousand), 40 parts by weight of carbon-five petroleum resin (with the softening point of 95 ℃), 20 parts by weight of aromatic oil (with the content of aromatic hydrocarbon of 40 wt%), 2.5 parts by weight of sulfur, 2.5 parts by weight of diaryl disulfide and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, and then carrying out blending extrusion and granulation by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth section is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Comparative example 4
The only difference from example 1 is that no stabilizer was added. The preparation process comprises the following steps:
uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%) and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, and then carrying out blending extrusion and granulation by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth stage is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Comparative example 5
The difference from example 1 is only the stabilizer and its coating particles and the wall material thickness. The preparation process comprises the following steps:
(1) 2.5 parts by weight of sulfur, 2.5 parts by weight of diaryl disulfide, 0.05 part by weight of sodium dodecylsulfate and 1 part by weight of gelatin were added to 50 parts by weight of the aqueous solution, and sheared at 12000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then dropwise adding 13 parts by weight of tetraethoxysilane, stirring and reacting for 2 hours at 50 ℃ and 300 rpm, cooling, filtering, washing with deionized water, and drying for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 0.8 part by weight of phenyl trimethoxy silane into 100 parts by weight of toluene, carrying out surface modification reaction for 1 hour at 60 ℃, cooling, filtering, washing with ethanol, and drying for 3 hours at 50 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%), 5 parts by weight of surface modified stabilizer and coating thereof (particle diameter is 43 micrometers, wall material thickness is 1.5 micrometers), and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, blending, extruding and granulating by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 110 ℃; the second section is 115 ℃; the third section is 120 ℃; the fourth section is 120 ℃; the fifth section is 125 ℃; the six sections are 130 ℃; the seven sections are 125 ℃; the eight sections are 120 ℃, and the rotating speed of the screw is 50 r/min.
Comparative example 6
The difference from example 1 is only in the extrusion temperature of the extruder. The preparation process comprises the following steps:
(1) 2.5 parts by weight of sulfur, 2.5 parts by weight of diaryl disulfide, 0.05 part by weight of sodium dodecyl sulfate and 1 part by weight of gelatin were added to 50 parts by weight of the aqueous solution, and the mixture was sheared at 3000 rpm for 1 hour to prepare a stabilizer suspension.
(2) Dilute hydrochloric acid was added to the stabilizer suspension to maintain the hydrochloric acid concentration at 0.09 mol/L. And then dropwise adding 15 parts by weight of ethyl orthosilicate, stirring and reacting for 2 hours at 50 ℃ and 300 rpm, cooling, filtering, washing with deionized water, and drying for 3 hours at 50 ℃ to obtain the stabilizer and the coating thereof.
(3) Adding 10 parts by weight of stabilizer and coating thereof and 0.8 part by weight of phenyl trimethoxy silane into 100 parts by weight of toluene, carrying out surface modification reaction for 1 hour at 60 ℃, cooling, filtering, washing with ethanol, and drying for 3 hours at 50 ℃ to obtain the surface-modified stabilizer and coating thereof.
(4) Uniformly mixing 100 parts by weight of SBS (molecular weight is 10 ten thousand), 40 parts by weight of carbon five petroleum resin (softening point is 95 ℃), 20 parts by weight of aromatic oil (aromatic hydrocarbon content is 40 wt%), 5 parts by weight of surface-modified stabilizer and coating thereof (particle diameter is 137 micrometers, wall material thickness is 3.3 micrometers), and 2 parts by weight of 2, 6-di-tert-butyl-p-cresol, blending, extruding and granulating by a double-screw extruder to obtain the anti-aging high-viscosity modified asphalt additive. The extruder operating conditions were: the first section is 150 ℃; the second section is 155 ℃; the third section is 160 ℃; the fourth stage is 160 ℃; the fifth section is 160 ℃; the six sections are 160 ℃; the seven sections are 160 ℃; the eight sections are 160 ℃, and the rotating speed of the screw is 50 r/min.
Test example
The anti-aging high-viscosity modified asphalt additive was added in an amount of 12 parts by weight to 100 parts by weight of molten base asphalt (vacuum residue, 25 ℃ penetration 711/10 mm), and the mixture was uniformly dispersed in the base asphalt by high-speed shearing at 175 ℃ for 1 hour and stirring at the same temperature for 0.5 hour, and the obtained high-viscosity modified asphalt was tested and the results are shown in Table 1. Wherein the thin film oven test is performed according to the standard GB/T5304-2001.
TABLE 1 Properties of base asphalts and modified asphalts obtained in examples and comparative examples
As can be seen from the above table results: the modified asphalt prepared by using the anti-aging high-viscosity modified asphalt additive in the examples 1 to 4 has high viscosity and good storage stability, which indicates that the modified asphalt has good dispersibility and uniformity. And under the synergistic action of sulfur and polysulfide, the modified asphalt in the example 1 has better stability and dispersibility than the modified asphalt in the example 4. Meanwhile, the modified asphalt provided by the invention has good ageing resistance.