CN116041732A - Wheel-non-sticking emulsified asphalt and preparation method thereof - Google Patents
Wheel-non-sticking emulsified asphalt and preparation method thereof Download PDFInfo
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- CN116041732A CN116041732A CN202211635906.1A CN202211635906A CN116041732A CN 116041732 A CN116041732 A CN 116041732A CN 202211635906 A CN202211635906 A CN 202211635906A CN 116041732 A CN116041732 A CN 116041732A
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- asphalt
- emulsifier
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- hot water
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- 239000010426 asphalt Substances 0.000 title claims abstract description 142
- 238000002360 preparation method Methods 0.000 title claims abstract description 27
- 239000003995 emulsifying agent Substances 0.000 claims abstract description 87
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 83
- 239000003607 modifier Substances 0.000 claims abstract description 56
- 229920000468 styrene butadiene styrene block copolymer Polymers 0.000 claims abstract description 18
- 239000011159 matrix material Substances 0.000 claims abstract description 17
- 239000002994 raw material Substances 0.000 claims abstract description 10
- 239000000084 colloidal system Substances 0.000 claims description 77
- 239000008149 soap solution Substances 0.000 claims description 48
- 239000007788 liquid Substances 0.000 claims description 26
- 239000000344 soap Substances 0.000 claims description 26
- 238000004132 cross linking Methods 0.000 claims description 18
- 238000007599 discharging Methods 0.000 claims description 14
- 150000001768 cations Chemical class 0.000 claims description 13
- 238000010438 heat treatment Methods 0.000 claims description 13
- 238000000034 method Methods 0.000 claims description 11
- 239000000243 solution Substances 0.000 claims description 7
- 125000002091 cationic group Chemical group 0.000 claims description 6
- LZZYPRNAOMGNLH-UHFFFAOYSA-M Cetrimonium bromide Chemical compound [Br-].CCCCCCCCCCCCCCCC[N+](C)(C)C LZZYPRNAOMGNLH-UHFFFAOYSA-M 0.000 claims description 3
- TWFQJFPTTMIETC-UHFFFAOYSA-N dodecan-1-amine;hydron;chloride Chemical compound [Cl-].CCCCCCCCCCCC[NH3+] TWFQJFPTTMIETC-UHFFFAOYSA-N 0.000 claims description 3
- 239000008236 heating water Substances 0.000 claims description 3
- 238000003801 milling Methods 0.000 claims description 3
- 238000004519 manufacturing process Methods 0.000 claims 1
- 238000010276 construction Methods 0.000 abstract description 9
- 239000000463 material Substances 0.000 abstract description 6
- 239000012790 adhesive layer Substances 0.000 abstract description 5
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 abstract 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 24
- 239000000203 mixture Substances 0.000 description 24
- 238000003860 storage Methods 0.000 description 22
- 230000004927 fusion Effects 0.000 description 11
- 239000010410 layer Substances 0.000 description 6
- 238000013112 stability test Methods 0.000 description 5
- 230000001070 adhesive effect Effects 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- 239000000853 adhesive Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 230000000052 comparative effect Effects 0.000 description 2
- 238000004945 emulsification Methods 0.000 description 2
- 239000000839 emulsion Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 238000003892 spreading Methods 0.000 description 2
- -1 acrylic ester Chemical class 0.000 description 1
- 230000006978 adaptation Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000011229 interlayer Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000005096 rolling process Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
Classifications
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J3/00—Processes of treating or compounding macromolecular substances
- C08J3/02—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques
- C08J3/03—Making solutions, dispersions, lattices or gels by other methods than by solution, emulsion or suspension polymerisation techniques in aqueous media
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2395/00—Bituminous materials, e.g. asphalt, tar or pitch
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08J—WORKING-UP; GENERAL PROCESSES OF COMPOUNDING; AFTER-TREATMENT NOT COVERED BY SUBCLASSES C08B, C08C, C08F, C08G or C08H
- C08J2453/00—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers
- C08J2453/02—Characterised by the use of block copolymers containing at least one sequence of a polymer obtained by reactions only involving carbon-to-carbon unsaturated bonds; Derivatives of such polymers of vinyl aromatic monomers and conjugated dienes
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A30/00—Adapting or protecting infrastructure or their operation
- Y02A30/30—Adapting or protecting infrastructure or their operation in transportation, e.g. on roads, waterways or railways
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Health & Medical Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Medicinal Chemistry (AREA)
- Polymers & Plastics (AREA)
- Organic Chemistry (AREA)
- Compositions Of Macromolecular Compounds (AREA)
- Processes Of Treating Macromolecular Substances (AREA)
Abstract
The invention provides non-stick wheel emulsified asphalt, and relates to the technical field of pavement asphalt materials. The non-stick wheel emulsified asphalt provided by the invention comprises the following preparation raw materials in parts by weight: 500-600 parts of matrix asphalt, 150-170 parts of emulsifier, 40-100 parts of modifier and 3500-4000 parts of water; the modifier is styrene-butadiene-styrene block copolymer (SBS) or sulfur powder. The emulsified asphalt provided by the invention can not adhere to tires in summer high-temperature seasons, so that the construction vehicle is prevented from damaging the adhesive layer material, the bonding efficiency and the bonding strength are improved, and the durability of the pavement is also improved.
Description
Technical Field
The invention relates to the technical field of pavement asphalt materials, in particular to non-stick emulsified asphalt and a preparation method thereof.
Background
In the road engineering construction process, the process of spreading adhesive layer materials is adopted between adjacent structural layers, and the process has the effects of completely bonding an upper asphalt layer, a lower asphalt layer or an asphalt layer and a structural object into a whole, and promoting the formation of an integral stress structure between the layers, so that dislocation and lateral movement of the interlayer structure caused by traffic load are reduced, the occurrence of road surface diseases is reduced, and the durability of the road surface is improved.
At present, emulsified asphalt is commonly used as adhesive layer oil in pavement construction. The properties of emulsified asphalt are determined by the properties of raw asphalt, the softening point is usually below 50 ℃, and the phenomenon of tire adhesion easily occurs after spreading adhesive layer oil in summer seasons at high temperature.
Disclosure of Invention
The invention aims to provide non-wheel-sticking emulsified asphalt and a preparation method thereof, which can avoid the phenomenon of sticking tires in high-temperature seasons in summer.
In order to achieve the above object, the present invention provides the following technical solutions:
the invention provides non-stick emulsified asphalt, which comprises the following preparation raw materials in parts by weight: 500-600 parts of matrix asphalt, 150-170 parts of emulsifier, 40-100 parts of modifier and 3500-4000 parts of water; the modifier is a styrene-butadiene-styrene block copolymer.
Preferably, the emulsifier is a cationic emulsifier.
Preferably, the cationic emulsifier comprises dodecylammonium chloride, cetyltrimethylammonium bromide or a cation Q 12-2 。
The invention provides a preparation method of non-stick wheel emulsified asphalt, which comprises the following steps:
heating water to obtain hot water;
dissolving an emulsifier into the hot water to obtain an emulsifier solution;
mixing the modifier with the emulsifier solution to perform a crosslinking reaction to obtain soap solution;
colloid milling the heated matrix asphalt and the soap solution to obtain non-sticky emulsified asphalt; the rotating speed of the colloid mill is 5000-6000 r/min.
Preferably, the temperature of the hot water is 70-80 ℃.
Preferably, the temperature of the soap solution is 50-80 ℃.
Preferably, the heating temperature of the matrix asphalt is 120-130 ℃.
Preferably, the time of the colloid mill is 3-5 min.
Preferably, the colloid mill includes: and opening the colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the temperature of the whole machine, discharging the hot water, adding soap liquid into the hot water, starting the colloid mill machine again to rotate, rotating the colloid mill at 3000-5000 r/min, and adding heated asphalt into the colloid mill after the rotation of the colloid mill is stable.
The invention provides non-stick emulsified asphalt, which comprises the following preparation raw materials in parts by weight: 500-600 parts of matrix asphalt, 150-170 parts of emulsifier, 40-100 parts of modifier and 3500-4000 parts of water; the modifier is a styrene-butadiene-styrene block copolymer (SBS). The emulsified asphalt provided by the invention has the advantages that the modifier is used in the formula, and the modifier can be added to perform a crosslinking reaction with asphalt to improve the softening point of the asphalt, so that the emulsified asphalt provided by the invention can not adhere to tires in high-temperature seasons in summer and on construction sites, the damage of construction vehicles to adhesive materials is avoided, in addition, the adhesive efficiency and adhesive strength are improved by using the modifier, and the durability of a pavement is improved.
In addition, the emulsion breaking speed of the conventional emulsified asphalt adhesive layer oil is low, and the upper layer mixture can be paved after water is evaporated to form a film for a long time, so that the construction efficiency is influenced.
The invention provides the preparation method of the non-stick wheel emulsified asphalt, which adopts the colloid mill and controls the rotating speed of the colloid mill, so that the demulsification speed of the emulsified asphalt can be increased, and the construction efficiency can be improved.
Detailed Description
The invention provides non-stick emulsified asphalt, which comprises the following preparation raw materials in parts by weight: 500-600 parts of matrix asphalt, 150-170 parts of emulsifier, 40-100 parts of modifier and 3500-4000 parts of water; the modifier is a styrene-butadiene-styrene block copolymer.
In the present invention, the raw materials used are commercially available products well known in the art, unless specifically described otherwise.
The preparation raw materials of the non-stick wheel emulsified asphalt provided by the invention comprise 500-600 parts by weight of matrix asphalt, preferably 520-590 parts by weight, and more preferably 540-580 parts by weight. The present invention is not particularly limited to the specific type of matrix asphalt, and asphalt for road construction well known in the art may be used.
Based on the weight parts of the matrix asphalt, the preparation raw materials of the non-stick wheel emulsified asphalt provided by the invention comprise 150-170 parts of emulsifying agent, preferably 155-165 parts, and more preferably 160 parts. In the present invention, the emulsifier is preferably a cationic emulsifier, preferably comprising dodecylammonium chloride, cetyltrimethylammonium bromide or a cation Q 12-2 。
Based on the weight parts of the matrix asphalt, the preparation raw materials of the non-stick emulsified asphalt provided by the invention comprise 40-100 parts of modifier, preferably 50-90 parts. In the present invention, the modifier is a styrene-butadiene-styrene block copolymer.
The preparation raw materials of the non-stick wheel emulsified asphalt provided by the invention comprise 3500-4000 parts of water, preferably 3600-3900 parts, and more preferably 3700-3800 parts by weight of matrix asphalt.
The emulsified asphalt provided by the invention uses the modifier, and the addition of the modifier can generate certain crosslinking reaction with asphalt to improve the softening point of the asphalt, so that the emulsified asphalt provided by the invention does not adhere to tires in high-temperature seasons in summer.
In addition, the modifier is used in the formula of the invention, so that the viscosity of the asphalt can be reduced, the emulsification temperature is reduced, the asphalt is easy to emulsify, and meanwhile, the asphalt can be subjected to crosslinking reaction with the emulsifier, thereby being beneficial to improving the high-temperature and low-temperature performances of the asphalt.
The invention provides a preparation method of non-stick wheel emulsified asphalt, which comprises the following steps:
heating water to obtain hot water;
dissolving an emulsifier into the hot water to obtain an emulsifier solution;
mixing the modifier with the emulsifier solution to perform a crosslinking reaction to obtain soap solution;
colloid milling the heated matrix asphalt and the soap solution to obtain non-sticky emulsified asphalt; the rotating speed of the colloid mill is 6000r/min.
In the present invention, the temperature of the hot water is preferably 80 ℃.
The invention preferably places the weighed emulsifier in a container for standby, heats water to 80 ℃, adds the emulsifier into the container filled with the emulsifier, stirs the emulsifier until the emulsifier is completely dissolved in the hot water, then adds the weighed modifier until the modifier and the emulsifier are uniformly mixed, and carries out crosslinking reaction to obtain the soap solution.
In the present invention, the temperature of the soap solution is preferably 50 to 80 ℃. The pH value of the soap solution is preferably 0.5-3; the present invention preferably achieves the above-described requirements by adjusting the pH of the soap solution with hydrochloric acid.
After the soap solution is obtained, the heated matrix asphalt and the soap solution are subjected to colloid mill to obtain the non-stick emulsified asphalt.
In the present invention, the heating temperature of the matrix asphalt is preferably 120 to 130 ℃.
In the present invention, the colloid mill preferably includes:
and opening the colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the temperature of the whole machine, discharging the hot water, adding soap liquid into the hot water, starting the colloid mill machine again to rotate, rotating the colloid mill at 3000-5000 r/min, and adding heated asphalt into the colloid mill after the rotation of the colloid mill is stable.
In the invention, the rotating speed of the colloid mill is preferably 6000r/min, and the time is preferably 3-5 min. The invention fuses the matrix asphalt with the soap solution through a colloid mill.
The invention firstly washes and preheats the colloid mill machine by hot water, thus preventing the soap liquid temperature from falling too fast. The invention prevents asphalt from caking in a machine due to the control of the rotating speed of the colloid mill at a higher level, and improves the emulsification effect.
The non-stick emulsified asphalt and the preparation method thereof provided by the invention are described in detail below with reference to examples, but they should not be construed as limiting the scope of the invention.
The storage stability test method of each example is: pouring into a stability test tube for stability test. The percent of the difference in solids content of the upper and lower sections of the test tube was used as data for storage stability.
Example 1
The selected asphalt is No. 70; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3840g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 43g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 1.5 by hydrochloric acid, and the soap solution is kept for standby.
563g of asphalt is heated to 130 ℃, and the temperature is kept to be not lower than 120 ℃ for waiting to use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
And pouring the obtained non-stick wheel emulsified asphalt into a stability test tube for stability test.
Stability is characterized by the percentage of the difference in solids content of the upper and lower sections of the test tube, the smaller the difference the more stable.
Storage stability: 0.22% (one day);
storage stability: 0.23% (five days).
Example 2
The selected asphalt is No. 70; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3594g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 43g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 1.5 by hydrochloric acid, and the soap solution is kept for standby.
Heating 527g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.14% (one day);
storage stability: 0.07% (five days).
Example 3
The selected asphalt is No. 70; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 57g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is measured to be 1.3, the pH value is adjusted to be 1.3 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.19% (one day);
storage stability: 0.18% (five days).
Example 4
The selected asphalt is No. 70; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 71g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 1.1 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.2% (one day);
storage stability: 0.19% (five days).
Example 5
The selected asphalt is No. 70; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 85.8g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 1 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.08% (one day)
Storage stability: 0.12% (five days)
Example 6
The selected asphalt is No. 30; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 100g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 0.8 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.06% (one day);
storage stability: 0.42% (five days).
Example 7
The selected asphalt is No. 30; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 43g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 1.5 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.4% (one day)
Storage stability: 0.69% (five days)
Example 8
The selected asphalt is No. 30; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 57g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH value is adjusted to 1.3 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.93% (one day)
Storage stability: 0.9% (five days)
Example 9
The selected asphalt is No. 30; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 71g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, a soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the measured pH value is=1.1, the pH value is adjusted to 1.1 by hydrochloric acid, and the soap solution is kept for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.35% (one day);
storage stability: 0.55% (five days).
Example 10
The selected asphalt is No. 30; the emulsifying agent is cation Q 12-2 (Shandong Paenii New Material Co., ltd.); the modifier is SBS.
The preparation method comprises the following steps:
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 85.8g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the pH=1 is measured, the pH is adjusted to 1 by hydrochloric acid, and the soap solution is ready for standby.
Heating 572g of asphalt to 130 ℃, keeping the temperature not lower than 120 ℃ and waiting for use;
turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Storage stability: 0.25% (one day);
storage stability: 0.33% (five days).
Index detection
Heating emulsified asphalt by an electromagnetic oven at a temperature not exceeding 160 ℃ to finally reach constant weight, and testing various indexes.
Table 1 properties of emulsified asphalt prepared in examples 1 to 5
TABLE 2 Performance data for emulsified asphalt prepared in examples 6 to 10
Comparative example
Selecting materials: asphalt No. 70 is selected, an acrylic ester emulsion LFE01 (Shanghai Saifu chemical development Co., ltd.) is selected as a modifier, and a cationic emulsifier EM-310 (Shanghai Soifu materials Co., ltd.) is selected as an asphalt emulsifier.
160g of emulsifier is placed in a container, 3901g of water is heated to 80 ℃, the obtained hot water is added into the container filled with the emulsifier, the mixture is stirred until the emulsifier is completely dissolved in the water, 43g of modifier is added until the mixture is uniformly mixed, the modifier and the emulsifier undergo a crosslinking reaction, so that soap solution is obtained, the temperature of the soap solution is kept at 55-60 ℃, the measured pH value is=2.0, the pH value is adjusted to 2.0 by hydrochloric acid, and the soap solution is kept for standby.
572g of asphalt is heated to 130 ℃, and the temperature is kept at not lower than 120 ℃ and the asphalt is waited for use.
Turning on a colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the whole temperature of the machine, discharging the hot water, adding prepared soap liquid into the machine, turning on the colloid mill machine again to rotate, adding the prepared asphalt into the machine after the colloid mill rotates stably at 5000r/min, adjusting the rotating speed to 6000r/min, and carrying out high-speed rotation fusion on the mixed asphalt and the soap liquid together by the colloid mill for 3-5 min to obtain the non-sticky wheel emulsified asphalt.
Experimental results: 50.20 percent of penetration; the softening point is: 45.3 ℃; the ductility is: 60cm.
The performances of the emulsified asphalt are lower than those of the non-stick emulsified asphalt prepared by the method.
From the results of the above examples and comparative examples, it can be seen that:
the softening point of the emulsified asphalt prepared by the method is higher than 40 ℃ of that of the conventional asphalt, so that the softening point of the asphalt can be improved on the premise of not changing other performances by the technical scheme provided by the invention. In addition, the technical scheme provided by the invention is feasible and highly applicable by adopting the emulsifying agent and the modifying agent with different proportions in the above embodiment.
The results in tables 1 and 2 show that the emulsified asphalt prepared by the invention has better softening point ductility than that of common asphalt. And the anti-skid value (experimental value is higher, 60-80) of the road surface test is better, so that the non-stick emulsified asphalt prepared by the invention has better adhesive property.
The practical application effect shows that the non-stick emulsified asphalt has excellent non-stick characteristic, and asphalt is not taken away under the condition of transportation and rolling of the mixture in the construction site.
The foregoing is merely a preferred embodiment of the present invention and it should be noted that modifications and adaptations to those skilled in the art may be made without departing from the principles of the present invention, which are intended to be comprehended within the scope of the present invention.
Claims (9)
1. The non-stick emulsified asphalt is characterized by comprising the following preparation raw materials in parts by weight: 500-600 parts of matrix asphalt, 150-170 parts of emulsifier, 40-100 parts of modifier and 3500-4000 parts of water; the modifier is a styrene-butadiene-styrene block copolymer.
2. The non-stick emulsified asphalt of claim 1, wherein the emulsifier is a cationic emulsifier.
3. The non-stick emulsified asphalt of claim 2, wherein the cationic emulsifier comprises dodecylammonium chloride, cetyltrimethylammonium bromide, or a cation Q 12-2 。
4. A method for preparing non-stick emulsified asphalt as set forth in any one of claims 1 to 3, comprising the steps of:
heating water to obtain hot water;
dissolving an emulsifier into the hot water to obtain an emulsifier solution;
mixing the modifier with the emulsifier solution to perform a crosslinking reaction to obtain soap solution;
colloid milling the heated matrix asphalt and the soap solution to obtain non-sticky emulsified asphalt; the rotating speed of the colloid mill is 5000-6000 r/min.
5. The method according to claim 4, wherein the hot water has a temperature of 70 to 80 ℃.
6. The method of claim 4, wherein the soap solution has a temperature of 50 to 80 ℃.
7. The method according to claim 4, wherein the heating temperature of the base asphalt is 120 to 130 ℃.
8. The method according to claim 4, wherein the time of the colloid mill is 3 to 5 minutes.
9. The method of manufacturing according to claim 4, wherein the colloid mill comprises: and opening the colloid mill machine, pouring hot water at 100 ℃ to rotate, raising the temperature of the whole machine, discharging the hot water, adding soap liquid into the hot water, starting the colloid mill machine again to rotate, rotating the colloid mill at 3000-5000 r/min, and adding heated asphalt into the colloid mill after the rotation of the colloid mill is stable.
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KR20010068964A (en) * | 2000-01-11 | 2001-07-23 | 박찬구 | Method of rubberized asphalt emulsion by using styrene-butadiene block copolymer |
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CN112266622A (en) * | 2020-10-27 | 2021-01-26 | 河北省交通规划设计院 | Wheel-sticking-free emulsified asphalt and preparation method thereof |
CN113789060A (en) * | 2021-09-10 | 2021-12-14 | 湖北国创高新材料股份有限公司 | High-viscosity wheel-sticking-free emulsified asphalt and preparation method thereof |
CN115449231A (en) * | 2022-09-30 | 2022-12-09 | 中路交科科技股份有限公司 | High-toughness wheel-sticking-free emulsified asphalt and preparation method thereof |
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KR20010068964A (en) * | 2000-01-11 | 2001-07-23 | 박찬구 | Method of rubberized asphalt emulsion by using styrene-butadiene block copolymer |
CN104479375A (en) * | 2014-12-04 | 2015-04-01 | 天津海泰环保科技发展有限公司 | SBS (styrene-butadiene-styrene triblock copolymer) and liquid rubber composite modified emulsified asphalt and preparation method thereof |
CN112266622A (en) * | 2020-10-27 | 2021-01-26 | 河北省交通规划设计院 | Wheel-sticking-free emulsified asphalt and preparation method thereof |
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