CN115353746B - A kind of ion exchange resin modified emulsified asphalt and its preparation method - Google Patents
A kind of ion exchange resin modified emulsified asphalt and its preparation method Download PDFInfo
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- 239000010426 asphalt Substances 0.000 title claims abstract description 126
- NWUYHJFMYQTDRP-UHFFFAOYSA-N 1,2-bis(ethenyl)benzene;1-ethenyl-2-ethylbenzene;styrene Chemical compound C=CC1=CC=CC=C1.CCC1=CC=CC=C1C=C.C=CC1=CC=CC=C1C=C NWUYHJFMYQTDRP-UHFFFAOYSA-N 0.000 title claims abstract description 37
- 239000003456 ion exchange resin Substances 0.000 title claims abstract description 37
- 229920003303 ion-exchange polymer Polymers 0.000 title claims abstract description 37
- 238000002360 preparation method Methods 0.000 title claims abstract description 11
- 125000002091 cationic group Chemical group 0.000 claims abstract description 12
- 239000003957 anion exchange resin Substances 0.000 claims abstract description 11
- 239000000654 additive Substances 0.000 claims abstract description 10
- 239000004372 Polyvinyl alcohol Substances 0.000 claims abstract description 8
- 229920002451 polyvinyl alcohol Polymers 0.000 claims abstract description 8
- 230000000996 additive effect Effects 0.000 claims abstract description 7
- 238000003756 stirring Methods 0.000 claims description 19
- 239000000203 mixture Substances 0.000 claims description 18
- 238000001704 evaporation Methods 0.000 claims description 15
- 230000008020 evaporation Effects 0.000 claims description 15
- 230000035515 penetration Effects 0.000 claims description 8
- 239000000839 emulsion Substances 0.000 claims description 6
- 229920001577 copolymer Polymers 0.000 claims description 2
- 238000005336 cracking Methods 0.000 claims description 2
- 238000004132 cross linking Methods 0.000 claims description 2
- 125000001453 quaternary ammonium group Chemical group 0.000 claims description 2
- 239000011347 resin Substances 0.000 abstract description 27
- 229920005989 resin Polymers 0.000 abstract description 27
- 238000003860 storage Methods 0.000 abstract description 7
- 238000005342 ion exchange Methods 0.000 abstract description 4
- 239000000463 material Substances 0.000 abstract description 3
- 230000007613 environmental effect Effects 0.000 abstract 1
- 239000002910 solid waste Substances 0.000 abstract 1
- 238000012360 testing method Methods 0.000 description 10
- 230000000052 comparative effect Effects 0.000 description 9
- 150000002500 ions Chemical class 0.000 description 7
- 230000007423 decrease Effects 0.000 description 6
- 239000007787 solid Substances 0.000 description 5
- 238000005516 engineering process Methods 0.000 description 4
- 239000000725 suspension Substances 0.000 description 4
- CSCPPACGZOOCGX-UHFFFAOYSA-N Acetone Chemical compound CC(C)=O CSCPPACGZOOCGX-UHFFFAOYSA-N 0.000 description 3
- UHOVQNZJYSORNB-UHFFFAOYSA-N Benzene Chemical compound C1=CC=CC=C1 UHOVQNZJYSORNB-UHFFFAOYSA-N 0.000 description 3
- XEKOWRVHYACXOJ-UHFFFAOYSA-N Ethyl acetate Chemical compound CCOC(C)=O XEKOWRVHYACXOJ-UHFFFAOYSA-N 0.000 description 3
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- YXFVVABEGXRONW-UHFFFAOYSA-N Toluene Chemical compound CC1=CC=CC=C1 YXFVVABEGXRONW-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 238000010276 construction Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 2
- IAZDPXIOMUYVGZ-UHFFFAOYSA-N Dimethylsulphoxide Chemical compound CS(C)=O IAZDPXIOMUYVGZ-UHFFFAOYSA-N 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 2
- 230000002776 aggregation Effects 0.000 description 2
- 230000003247 decreasing effect Effects 0.000 description 2
- 239000003995 emulsifying agent Substances 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 230000003993 interaction Effects 0.000 description 2
- VZGDMQKNWNREIO-UHFFFAOYSA-N tetrachloromethane Chemical compound ClC(Cl)(Cl)Cl VZGDMQKNWNREIO-UHFFFAOYSA-N 0.000 description 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 2
- SCYULBFZEHDVBN-UHFFFAOYSA-N 1,1-Dichloroethane Chemical compound CC(Cl)Cl SCYULBFZEHDVBN-UHFFFAOYSA-N 0.000 description 1
- 125000001989 1,3-phenylene group Chemical group [H]C1=C([H])C([*:1])=C([H])C([*:2])=C1[H] 0.000 description 1
- FFRBMBIXVSCUFS-UHFFFAOYSA-N 2,4-dinitro-1-naphthol Chemical compound C1=CC=C2C(O)=C([N+]([O-])=O)C=C([N+]([O-])=O)C2=C1 FFRBMBIXVSCUFS-UHFFFAOYSA-N 0.000 description 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-O Ammonium Chemical compound [NH4+] QGZKDVFQNNGYKY-UHFFFAOYSA-O 0.000 description 1
- 229920000034 Plastomer Polymers 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 238000006136 alcoholysis reaction Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- 150000003863 ammonium salts Chemical class 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 150000001450 anions Chemical class 0.000 description 1
- 239000010425 asbestos Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 229910002092 carbon dioxide Inorganic materials 0.000 description 1
- 239000001569 carbon dioxide Substances 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 239000003153 chemical reaction reagent Substances 0.000 description 1
- 238000004581 coalescence Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 229920001971 elastomer Polymers 0.000 description 1
- 239000000806 elastomer Substances 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 125000000524 functional group Chemical group 0.000 description 1
- 239000003502 gasoline Substances 0.000 description 1
- 230000002209 hydrophobic effect Effects 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 239000003350 kerosene Substances 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 238000002715 modification method Methods 0.000 description 1
- 239000003607 modifier Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000002861 polymer material Substances 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000000376 reactant Substances 0.000 description 1
- 238000000518 rheometry Methods 0.000 description 1
- 229910052895 riebeckite Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 230000035945 sensitivity Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 239000012798 spherical particle Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 229920006305 unsaturated polyester Polymers 0.000 description 1
- 235000015112 vegetable and seed oil Nutrition 0.000 description 1
- 239000008158 vegetable oil Substances 0.000 description 1
- 238000012795 verification Methods 0.000 description 1
- 239000012855 volatile organic compound Substances 0.000 description 1
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- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
- C08L95/005—Aqueous compositions, e.g. emulsions
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- Engineering & Computer Science (AREA)
- Civil Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Health & Medical Sciences (AREA)
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- Polymers & Plastics (AREA)
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Abstract
本发明的目的在于提供一种离子交换树脂改性乳化沥青及其制备方法,属于道路铺装材料技术领域,由离子交换树脂及乳化沥青制备而成,其中离子交换树脂改性乳化沥青由离子交换树脂、乳化沥青及添加剂组成,离子交换树脂为碱性阴离子交换树脂,乳化沥青为阳离子乳化沥青,添加剂选用聚乙烯醇。本发明制备的离子交换树脂改性乳化沥青具有制备工艺简单、储存稳定性强、抗高温稳定性强等优点,适用于夏季高温地区,同时本发明以环境友好的方式利用离子交换树脂固体废弃物,并获得性能优异的改性乳化沥青,对于环境保护具有重意义。The purpose of the present invention is to provide an ion exchange resin modified emulsified asphalt and its preparation method, belonging to the technical field of road paving materials, prepared from ion exchange resin and emulsified asphalt, wherein the ion exchange resin modified emulsified asphalt is obtained by ion exchange Composed of resin, emulsified asphalt and additives, the ion exchange resin is a basic anion exchange resin, the emulsified asphalt is a cationic emulsified asphalt, and the additive is polyvinyl alcohol. The ion-exchange resin-modified emulsified asphalt prepared by the invention has the advantages of simple preparation process, strong storage stability, and high-temperature resistance, and is suitable for high-temperature areas in summer. At the same time, the invention utilizes ion-exchange resin solid waste in an environmentally friendly manner , and obtain modified emulsified asphalt with excellent performance, which is of great significance to environmental protection.
Description
技术领域technical field
本发明属于道路铺装材料技术领域,具体涉及一种离子交换树脂改性乳化沥青及其制备方法,特别涉及一种特别适用于冷再生沥青路面的离子交换树脂改性乳化沥青及其制备方法。The invention belongs to the technical field of road paving materials, in particular to an ion exchange resin modified emulsified asphalt and a preparation method thereof, in particular to an ion exchange resin modified emulsified asphalt especially suitable for cold recycled asphalt pavement and a preparation method thereof.
背景技术Background technique
近年来,路面施工行业能源和资源消耗量问题、环境污染问题越来越引起人们的关注。与热拌沥青(HMA)技术相比,采用乳化沥青的冷拌沥青(CMA)技术具有显著优点。研究指出,相比于HMA 技术,CMA技术在整个路面施工过程中减少了沥青和骨料加热过程,可以节约50%以上的能源,在生产过程中只产生33%的二氧化碳和17%的挥发性有机化合物排放。然而,由于水及乳化剂的加入,乳化沥青及其混合料的力学性能有所下降,乳化沥青(EA)中的水分对乳化沥青蒸发残留物(EREA)的车辙系数、恢复率、复模量和疲劳寿命具有直接的影响。In recent years, the problems of energy and resource consumption and environmental pollution in the road construction industry have attracted more and more attention. Cold mix asphalt (CMA) technology using emulsified asphalt has significant advantages over hot mix asphalt (HMA) technology. The study pointed out that compared with HMA technology, CMA technology reduces the heating process of asphalt and aggregate during the entire pavement construction process, can save more than 50% of energy, and only produces 33% of carbon dioxide and 17% of volatile organic compound emissions. However, due to the addition of water and emulsifiers, the mechanical properties of emulsified asphalt and its mixture have declined. and fatigue life have a direct impact.
目前提高乳化沥青性能仍是道路建设领域广泛关注的一个问题。对乳化沥青的改性主要集中于采用弹性体、塑性体、聚合材料等物理改性方式,而从乳化沥青的离子和反应基团角度进行的改性研究相对较少。作为一种典型的双电层结构物质,乳化沥青由于其特殊的离子特性而与热拌沥青存在差异。研究表明只有当乳化沥青的离子与反应物离子相反才会发生化学反应,乳化剂离子类型对乳化沥青粘合剂的稳定性有明显的影响,添加盐或小固体颗粒可以加速沥青乳液的聚结。而乳化沥青的粘结性和稳定性还与沥青滴与矿物之间的固体润湿性和电相互作用有关,润湿性取决于疏水化固体团簇与沥青分子之间的相互作用。必须设置表面活性剂浓度,以便在沥青乳液特性和沥青与骨料之间的附着力之间建立平衡。同时乳化沥青pH对其稳定性也有很大影响,根据悬浮流变学理论得知合理的pH可以控制沥青液滴内的水量,使其粘结性和稳定性能更加良好。Improving the performance of emulsified asphalt is still a widely concerned issue in the field of road construction. The modification of emulsified asphalt mainly focuses on the use of physical modification methods such as elastomers, plastomers, and polymer materials, while relatively few studies have been conducted on the modification of emulsified asphalt from the perspective of ions and reactive groups. As a typical electric double layer structure substance, emulsified asphalt is different from hot mix asphalt due to its special ionic properties. Studies have shown that the chemical reaction will only occur when the ions of the emulsified asphalt are opposite to the reactant ions. The type of emulsifier ions has a significant impact on the stability of the emulsified asphalt binder. Adding salt or small solid particles can accelerate the coalescence of the asphalt emulsion . The cohesion and stability of emulsified asphalt are also related to the solid wettability and electrical interaction between asphalt droplets and minerals, and the wettability depends on the interaction between hydrophobic solid clusters and asphalt molecules. Surfactant concentration must be set to create a balance between bitumen emulsion properties and adhesion between bitumen and aggregate. At the same time, the pH of emulsified asphalt also has a great influence on its stability. According to the theory of suspension rheology, a reasonable pH can control the water amount in the asphalt droplet, making its cohesiveness and stability better.
离子交换树脂在溶液中会解离出亲油基团与亲水基团,其中亲油基团可与呈油性的沥青液滴相互吸附,亲水基团与乳化沥青本身的离子电性相反,具备发生化学反应的条件,可以表现出界面性质。因此,本发明采用碱性阴离子交换树脂对乳化沥青进行改性,为冷再生沥青路面提供一种性能优异的改性材料。The ion exchange resin will dissociate into lipophilic groups and hydrophilic groups in the solution, wherein the lipophilic groups can adsorb each other with the oily asphalt droplets, and the hydrophilic groups are opposite to the ionic properties of the emulsified asphalt itself. With the conditions for chemical reactions to occur, interface properties can be exhibited. Therefore, the present invention adopts the basic anion exchange resin to modify the emulsified asphalt, and provides a modified material with excellent performance for the cold recycled asphalt pavement.
发明内容Contents of the invention
本发明的目的在于提供一种离子交换树脂改性乳化沥青及其制备方法,采用乳化沥青、离子交换树脂、添加剂组成,最终在常温条件下形成一种性能优异的乳化沥青。本发明可提供一种制备简单、成本低廉、储存稳定性强、粘度高、抗高温稳定性强的改性乳化沥青。The purpose of the present invention is to provide an ion exchange resin modified emulsified asphalt and its preparation method, which is composed of emulsified asphalt, ion exchange resin and additives, and finally forms an emulsified asphalt with excellent performance under normal temperature conditions. The invention can provide a modified emulsified asphalt with simple preparation, low cost, strong storage stability, high viscosity and strong stability against high temperature.
本发明采用如下技术方案:The present invention adopts following technical scheme:
一种离子交换树脂改性乳化沥青,包括如下重量份数的组分:乳化沥青100份,离子交换树脂10-40份,添加剂0.2-1份。An ion exchange resin modified emulsified asphalt comprises the following components in parts by weight: 100 parts of emulsified asphalt, 10-40 parts of ion exchange resin, and 0.2-1 part of additives.
进一步地,所述乳化沥青为慢裂性阳离子乳化沥青,呈黑褐色乳液,其蒸发残留物技术指标不低于以下特征。Further, the emulsified asphalt is a slow-cracking cationic emulsified asphalt, which is a dark brown emulsion, and its evaporation residue technical index is not lower than the following characteristics.
进一步地,所述离子交换树脂为强碱性阴离子交换树脂,常温下是固态棕黄色至金黄色球状颗粒,带有季铵基[-N(CH3)3OH]、交联度不低于7%的苯乙烯-二乙烯苯共聚体,在溶液中会发生解离形成阴离子和亲油基团。Further, the ion exchange resin is a strongly basic anion exchange resin, solid brown to golden yellow spherical particles at room temperature, with a quaternary ammonium group [-N(CH 3 ) 3 OH], and a cross-linking degree of not less than 7%. The styrene-divinylbenzene copolymer will dissociate in solution to form anion and lipophilic groups.
进一步地,所述添加剂为间苯型不饱和聚酯长余辉骨料的添加剂,为聚乙烯醇,外观是白色片状、絮状或粉末状固体,微溶于二甲基亚砜,不溶于汽油、煤油、植物油、苯、甲苯、二氯乙烷、四氯化碳、丙酮、醋酸乙酯、甲醇、乙二醇等,黏度为3~70,pH值4.5~6.5,干燥失重≤5.0,酸值≤3.0%,醇解度85~89。Further, the additive is an additive for m-phenylene type unsaturated polyester long afterglow aggregate, which is polyvinyl alcohol, and its appearance is white flake, flocculent or powdery solid, slightly soluble in dimethyl sulfoxide, insoluble in Gasoline, kerosene, vegetable oil, benzene, toluene, dichloroethane, carbon tetrachloride, acetone, ethyl acetate, methanol, ethylene glycol, etc., viscosity 3-70, pH 4.5-6.5, loss on drying ≤ 5.0, Acid value ≤ 3.0%, alcoholysis degree 85-89.
一种离子交换树脂改性乳化沥青的制备方法,包括以下步骤:A preparation method of ion exchange resin modified emulsified asphalt, comprising the following steps:
步骤1:常温下,将添加剂按乳化沥青质量的0.2-1.0份掺量加入到乳化沥青后搅拌,搅拌速度为100-500转/min, 搅拌时间为1-3min,形成拌合液A。Step 1: At room temperature, add the additive to the emulsified asphalt in an amount of 0.2-1.0 parts of the emulsified asphalt mass, and stir at a stirring speed of 100-500 rpm for 1-3 minutes to form a mixture A.
步骤2:常温下,将强碱性阴离子交换树脂按乳化沥青质量的10-40份掺量加入到上述拌合液A中搅拌,搅拌速度为100-500转/min,搅拌时间为2-4min,离子交换树脂改性乳化沥青即制备完成。Step 2: At room temperature, add the strongly basic anion exchange resin to the above mixture A in an amount of 10-40 parts of the emulsified asphalt mass and stir at a stirring speed of 100-500 rpm for 2-4 minutes , the ion exchange resin modified emulsified asphalt is prepared.
本发明的有益效果如下:The beneficial effects of the present invention are as follows:
1. 离子交换树脂改性乳化沥青制备简单;1. The preparation of ion exchange resin modified emulsified asphalt is simple;
2. 离子交换树脂改性乳化沥青可以常温改性,制备的改性乳化沥青储存稳定性强;2. Ion exchange resin modified emulsified asphalt can be modified at room temperature, and the prepared modified emulsified asphalt has strong storage stability;
3. 制备的离子交换树脂改性乳化沥青粘度高;3. The prepared ion exchange resin modified emulsified asphalt has high viscosity;
4. 制备的离子交换树脂改性乳化沥青抗高温稳定性强。4. The prepared ion exchange resin modified emulsified asphalt has strong high temperature stability.
具体实施方式Detailed ways
本发明通过大量的试验研究和反复验证,发现一种离子交换树脂改性乳化沥青及其最佳制备方法。下面结合几个有代表性的实施例来具体说明本发明的实施情况,但下述实施例并不构成对本发明的限制。The present invention discovers an ion exchange resin modified emulsified asphalt and its optimal preparation method through a large number of experimental studies and repeated verifications. The implementation of the present invention will be specifically described below in conjunction with several representative examples, but the following examples do not constitute a limitation to the present invention.
实施例1Example 1
室温条件下,在100份阳离子乳化沥青中加入0.2份聚乙烯醇,在转速为500转/分钟的搅拌机条件下搅拌3min,所得拌合液A密封保存;At room temperature, add 0.2 parts of polyvinyl alcohol to 100 parts of cationic emulsified asphalt, stir for 3 minutes under the condition of a mixer with a rotation speed of 500 rpm, and store the obtained mixture A in a sealed manner;
室温条件下,在拌合液A中加入10份的强碱性阴离子交换树脂,在转速为500转/分钟的搅拌机条件下搅拌2min,获得离子交换树脂改性乳化沥青。At room temperature, add 10 parts of strong basic anion exchange resin to the mixture A, and stir for 2 minutes under the condition of a mixer with a rotation speed of 500 rpm to obtain ion exchange resin modified emulsified asphalt.
将离子交换树脂改性乳化沥青至于铝缸中,然后置于电炉或燃气炉(放有石棉垫)上缓缓加热,加热至试样中的水分已完全蒸发,然后在163℃±3.0℃温度下加热1min,获得离子交换树脂改性乳化沥青蒸发残留物。Put the ion exchange resin modified emulsified asphalt in the aluminum cylinder, then place it on the electric furnace or gas furnace (with asbestos pad) and heat it slowly until the moisture in the sample has completely evaporated, and then heat it at 163℃±3.0℃ Heating at low temperature for 1 min to obtain the evaporation residue of ion exchange resin modified emulsified asphalt.
实施例2Example 2
室温条件下,在100份阳离子乳化沥青中加入0.4份聚乙烯醇,在转速为500转/分钟的搅拌机条件下搅拌3min,所得拌合液A密封保存;At room temperature, add 0.4 parts of polyvinyl alcohol to 100 parts of cationic emulsified asphalt, stir for 3 minutes under the condition of a mixer with a rotating speed of 500 rpm, and seal the obtained mixture A for storage;
室温条件下,在拌合液A中加入20份的强碱性阴离子交换树脂,在转速为500转/分钟的搅拌机条件下搅拌2min,获得离子交换树脂改性乳化沥青。At room temperature, add 20 parts of strong basic anion exchange resin to the mixture A, and stir for 2 minutes under the condition of a mixer with a rotation speed of 500 rpm to obtain ion exchange resin modified emulsified asphalt.
离子交换树脂改性乳化沥青蒸发残留物与实施例1相同。The ion exchange resin modified emulsified asphalt evaporation residue is the same as in Example 1.
实施例3Example 3
室温条件下,在100份阳离子乳化沥青中加入0.6份聚乙烯醇,在转速为500转/分钟的搅拌机条件下搅拌3min,所得拌合液A密封保存;At room temperature, add 0.6 parts of polyvinyl alcohol to 100 parts of cationic emulsified asphalt, stir for 3 minutes under the condition of a mixer with a rotation speed of 500 rpm, and seal the obtained mixture A for storage;
室温条件下,在拌合液A中加入30份的强碱性阴离子交换树脂,在转速为500转/分钟的搅拌机条件下搅拌2min,获得离子交换树脂改性乳化沥青。At room temperature, add 30 parts of strongly basic anion exchange resin to the mixture A, and stir for 2 minutes under the condition of a mixer with a rotation speed of 500 rpm to obtain ion exchange resin modified emulsified asphalt.
离子交换树脂改性乳化沥青蒸发残留物与实施例1相同。The ion exchange resin modified emulsified asphalt evaporation residue is the same as in Example 1.
实施例4Example 4
室温条件下,在100份阳离子乳化沥青中加入0.8份聚乙烯醇,在转速为500转/分钟的搅拌机条件下搅拌3min,所得拌合液A密封保存;At room temperature, add 0.8 parts of polyvinyl alcohol to 100 parts of cationic emulsified asphalt, stir for 3 minutes under the condition of a mixer with a rotation speed of 500 rpm, and seal the obtained mixture A for storage;
室温条件下,在拌合液A中加入40份的强碱性阴离子交换树脂,在转速为500转/分钟的搅拌机条件下搅拌2min,获得离子交换树脂改性乳化沥青。At room temperature, add 40 parts of strong basic anion exchange resin to the mixture A, and stir for 2 minutes under the condition of a mixer with a rotation speed of 500 rpm to obtain ion exchange resin modified emulsified asphalt.
离子交换树脂改性乳化沥青蒸发残留物与实施例1相同。The ion exchange resin modified emulsified asphalt evaporation residue is the same as in Example 1.
实施例5Example 5
室温条件下,在100份阳离子乳化沥青中加入1.0份聚乙烯醇,在转速为500转/分钟的搅拌机条件下搅拌3min,所得拌合液A密封保存;At room temperature, add 1.0 parts of polyvinyl alcohol to 100 parts of cationic emulsified asphalt, stir for 3 minutes under the condition of a mixer with a rotation speed of 500 rpm, and store the obtained mixture A in a sealed manner;
室温条件下,在拌合液A中加入50份的强碱性阴离子交换树脂,在转速为500转/分钟的搅拌机条件下搅拌2min,获得离子交换树脂改性乳化沥青。At room temperature, add 50 parts of strong basic anion exchange resin to the mixture A, and stir for 2 minutes under the condition of a mixer with a rotation speed of 500 rpm to obtain ion exchange resin modified emulsified asphalt.
离子交换树脂改性乳化沥青蒸发残留物与实施例1相同。The ion exchange resin modified emulsified asphalt evaporation residue is the same as in Example 1.
对比例comparative example
室温条件下,取100份阳离子乳化沥青作为比较例。At room temperature, 100 parts of cationic emulsified asphalt was taken as a comparative example.
改性乳化沥青蒸发残留物与实施例1相同。The evaporation residue of modified emulsified asphalt is the same as in Example 1.
下面对实施例1~5以及对比例进行电导率、pH试验,分析改性乳化沥青内部离子强度和存储稳定性的影响;同时对改性乳化沥青蒸发残留物进行针入度、软化点、延度试验,以表征不同掺量树脂对乳化沥青蒸发残留物基本性能。各种试验情况以及测试结果如下:Carry out conductivity, pH test to embodiment 1~5 and comparative example below, analyze the impact of internal ionic strength and storage stability of modified emulsified asphalt; Simultaneously carry out penetration, softening point, Ductility test to characterize the basic performance of different content resins on the evaporation residue of emulsified asphalt. Various test conditions and test results are as follows:
1. 电导率及pH试验1. Conductivity and pH test
将制备好的离子交换树脂改性乳化沥青采用DDSJ-308A型电导率计和PHSJ-4A型pH计,测试实施例与比较例的电导率和pH,试验结果如下表1。The prepared ion exchange resin-modified emulsified asphalt was tested with a DDSJ-308A conductivity meter and a PHSJ-4A pH meter to test the conductivity and pH of the examples and comparative examples. The test results are shown in Table 1 below.
表1Table 1
根据表1 可知,相较于对比例,实施例1-5的电导率均获得增加,同时pH值均下降。随树脂掺量增加,实施例1-5乳化沥青电导率呈增大的趋势,从4.50ms/cm增加到19.38ms/cm。在掺量为40%后继续增加树脂,电导率上升速度减缓。离子交换树脂提高了改性悬浮液释放离子的能力,加入树脂后提高了改性乳化沥青的导电性能进一步提升,增加了释放离子的强度,进而改善了多相悬浮液稳定性;树脂掺量持续增加时,树脂在沥青乳液中的电离效果减弱,与乳化沥青离子交换程度降低,导致电导率上升速率减缓。乳化沥青pH随树脂掺量增加逐渐减小,酸性增强。已有研究表明,阳离子乳化沥青在酸性条件下可以促进铵分子反应生产阳离子分子(铵盐分子),更能发挥其稳定性与粘结性能。在较低的pH下,树脂的功能基团使用效率较高,对离子吸附量大。H+的增加,可以改变改性乳化沥青电离平衡,增加树脂—沥青结合结构双电层的厚度,增强其稳定性。但当树脂掺量超过30%时,阳离子乳化沥青H+浓度过大,反而会破坏双电层的结构,引起破乳,这就是电导率上升速度减缓。综上分析可以,采用适当掺量的再生树脂改性乳化沥青可以增强沥青乳液释放电子强度,增大扩散层厚度,增强多相悬浮体稳定性,延缓乳化沥青的破乳。According to Table 1, compared with the comparative examples, the conductivity of Examples 1-5 were all increased, while the pH values were all decreased. With the increase of resin content, the electrical conductivity of the emulsified asphalt in Example 1-5 showed an increasing trend, from 4.50ms/cm to 19.38ms/cm. After the dosage is 40%, continue to increase the resin, and the rate of increase in electrical conductivity slows down. The ion-exchange resin improves the ability of the modified suspension to release ions. After adding the resin, the conductivity of the modified emulsified asphalt is further improved, and the strength of the released ions is increased, thereby improving the stability of the multi-phase suspension; the resin dosage continues When increasing, the ionization effect of the resin in the asphalt emulsion weakens, and the degree of ion exchange with the emulsified asphalt decreases, resulting in a slowdown in the rate of increase in conductivity. The pH of emulsified asphalt decreases gradually with the increase of resin content, and the acidity increases. Previous studies have shown that cationic emulsified asphalt can promote the reaction of ammonium molecules to produce cationic molecules (ammonium salt molecules) under acidic conditions, and can better exert its stability and bonding performance. At a lower pH, the functional groups of the resin are used more efficiently and have a larger adsorption capacity for ions. The increase of H + can change the ionization balance of the modified emulsified asphalt, increase the thickness of the electric double layer of the resin-asphalt combined structure, and enhance its stability. However, when the resin content exceeds 30%, the H + concentration of cationic emulsified asphalt is too high, which will destroy the structure of the electric double layer and cause demulsification, which means that the increase rate of electrical conductivity will slow down. Based on the above analysis, the modified emulsified asphalt with an appropriate amount of recycled resin can enhance the electron intensity released from the asphalt emulsion, increase the thickness of the diffusion layer, enhance the stability of the multiphase suspension, and delay the demulsification of the emulsified asphalt.
2. 三大指标2. Three major indicators
依据规范《公路工程沥青及沥青混合料试验规程》(JTG E20-2011)对实施例1-5及对比例改性乳化沥青蒸发残留物进行针入度、软化点、延度试验,以表征不同掺量树脂对乳化沥青蒸发残留物基本性能的影响。测试结果见表2。Penetration, softening point, and ductility tests were performed on the evaporation residues of modified emulsified asphalt in Examples 1-5 and comparative proportions according to the "Test Regulations for Asphalt and Asphalt Mixtures in Highway Engineering" (JTG E20-2011) to characterize different Effect of resin content on basic properties of emulsified asphalt evaporation residue. The test results are shown in Table 2.
表2Table 2
从表2中可以看出,相较于对比例,实施例1-5改性乳化沥青的针入度和延度整体都呈下降趋势,而软化点逐渐升高。产生这种现象的原因是,再生树脂加入乳化沥青中,其会解离出亲油基团,与沥青分子结合后会形成大分子结构,增加了蒸发残留物的团聚能力;并且树脂力学强度高,二者的结合导致沥青整体变硬,针入度下降。在树脂掺量达到30%时针入度出现短暂的上升,由42.6mm上升至44.4mm,继续增加树脂针入度又下降。可能是因为30%树脂的亲油基团与沥青分子的结合达到了相互平衡的状态,而掺量继续增加时,将会打破这种平衡。改性沥青失稳,多余的树脂解离不充分,与沥青分子结合效果差,在沥青中出现相互结团成块的现象,导致针入度下降。总体上看,适当的树脂掺量会使其蒸发残留物变硬,增强乳化沥青的高温性能。It can be seen from Table 2 that, compared with the comparative example, the penetration and ductility of the modified emulsified asphalt of Examples 1-5 showed a downward trend overall, while the softening point gradually increased. The reason for this phenomenon is that when the recycled resin is added to the emulsified asphalt, it will dissociate the lipophilic group and form a macromolecular structure after combining with the asphalt molecule, which increases the agglomeration ability of the evaporation residue; and the resin has high mechanical strength , the combination of the two causes the asphalt to harden as a whole and the needle penetration decreases. When the resin content reaches 30%, the needle penetration increases temporarily, from 42.6mm to 44.4mm, and continues to increase the resin needle penetration and then decreases. It may be because the combination of lipophilic groups of 30% resin and asphalt molecules has reached a state of mutual equilibrium, and when the dosage continues to increase, this balance will be broken. The modified asphalt is destabilized, the excess resin dissociates insufficiently, and the binding effect with asphalt molecules is poor, and there is a phenomenon of mutual agglomeration in the asphalt, resulting in a decrease in penetration. In general, proper resin content will harden the evaporation residue and enhance the high temperature performance of emulsified asphalt.
从表2中可以看出,相较于对比例,实施例1-5改性乳化沥青残留物的延度从401.30mm下降至214.65mm,下降了46.5%。究其原因,在蒸发残留物中,沥青的塑性变形对延度起着决定性作。沥青之间的粘结性弱,而树脂在沥青之间形成的结合相塑性变形能力差,与改性沥青产生了变形薄弱区,所以导致乳化沥青的延度降低。It can be seen from Table 2 that compared with the comparative example, the ductility of the modified emulsified asphalt residue in Examples 1-5 decreased from 401.30 mm to 214.65 mm, a decrease of 46.5%. The reason is that in the evaporation residue, the plastic deformation of the asphalt plays a decisive role in the ductility. The cohesion between asphalt is weak, and the bonded phase formed by the resin between the asphalt has poor plastic deformation ability, which creates a weak deformation zone with the modified asphalt, so the ductility of the emulsified asphalt is reduced.
从表2中可以看出,相较于对比例,实施例1-5改性乳化沥青残留物软化点随再生树脂掺量增加呈上升趋势,树脂掺量在20%时,软化达到57.08℃,增长了6.1%;掺量大于20%时,软化点增长速率减缓。说明采用树脂作为乳化沥青改性剂会使沥青整体变硬,而随着树脂掺量的继续增加,改性乳化沥青受温度影响减弱,温度敏感性下降,改善了乳化沥青的高温性能。It can be seen from Table 2 that compared with the comparative example, the softening point of the modified emulsified asphalt residue in Examples 1-5 increases with the increase of the recycled resin content. When the resin content is 20%, the softening point reaches 57.08°C. Increased by 6.1%; when the content is greater than 20%, the growth rate of softening point slows down. It shows that the use of resin as emulsified asphalt modifier will make the asphalt hard as a whole, and with the continuous increase of resin content, the modified emulsified asphalt is less affected by temperature, and the temperature sensitivity is reduced, which improves the high temperature performance of emulsified asphalt.
综合再生树脂改性乳化沥青的三大指标发现,采用树脂改性乳化沥青会使乳化沥青蒸发残留物变稠变硬,增强乳化沥青高温性能,但抗裂性能下降。当树脂掺量为30%时树脂与沥青之间结合状态达到最佳,再生树脂可以充分发挥其性能,树脂改性乳化沥青会表现出相对较好的塑性变形能力和良好的高温性能。Based on the three major indicators of recycled resin-modified emulsified asphalt, it is found that the use of resin-modified emulsified asphalt will thicken and harden the evaporation residue of emulsified asphalt, enhance the high-temperature performance of emulsified asphalt, but reduce the crack resistance. When the resin content is 30%, the bonding state between resin and asphalt is the best, the recycled resin can give full play to its performance, and the resin-modified emulsified asphalt will show relatively good plastic deformation ability and good high temperature performance.
本发明中使用的试剂均为市售,本发明中使用的方法,若无特殊说明,均为常规方法。The reagents used in the present invention are all commercially available, and the methods used in the present invention are conventional methods unless otherwise specified.
最后应说明的是:以上所述实施例,仅为本发明的具体实施方式,用以说明本发明的技术方案,而非对其限制,本发明的保护范围并不局限于此,尽管参照前述实施例对本发明进行了详细的说明,本领域的普通技术人员应当理解:任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,其依然可以对前述实施例所记载的技术方案进行修改或可轻易想到变化,或者对其中部分技术特征进行等同替换;而这些修改、变化或者替换,并不使相应技术方案的本质脱离本发明实施例技术方案的精神和范围,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应所述以权利要求的保护范围为准。Finally, it should be noted that: the above-described embodiments are only specific implementations of the present invention, used to illustrate the technical solutions of the present invention, rather than limiting them, and the scope of protection of the present invention is not limited thereto, although referring to the foregoing The embodiment has described the present invention in detail, and those of ordinary skill in the art should understand that any person familiar with the technical field can still modify the technical solutions described in the foregoing embodiments within the technical scope disclosed in the present invention Changes can be easily thought of, or equivalent replacements are made to some of the technical features; and these modifications, changes or replacements do not make the essence of the corresponding technical solutions deviate from the spirit and scope of the technical solutions of the embodiments of the present invention, and should be included in the scope of the present invention within the scope of protection. Therefore, the protection scope of the present invention should be based on the protection scope of the claims.
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