WO2011134366A1 - Directly-mixed rubber asphalt mixture and production method thereof - Google Patents

Directly-mixed rubber asphalt mixture and production method thereof Download PDF

Info

Publication number
WO2011134366A1
WO2011134366A1 PCT/CN2011/073110 CN2011073110W WO2011134366A1 WO 2011134366 A1 WO2011134366 A1 WO 2011134366A1 CN 2011073110 W CN2011073110 W CN 2011073110W WO 2011134366 A1 WO2011134366 A1 WO 2011134366A1
Authority
WO
WIPO (PCT)
Prior art keywords
rubber
asphalt
rubber powder
mixture
modifier
Prior art date
Application number
PCT/CN2011/073110
Other languages
French (fr)
Chinese (zh)
Inventor
周其强
Original Assignee
Zhou Qiqiang
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Zhou Qiqiang filed Critical Zhou Qiqiang
Publication of WO2011134366A1 publication Critical patent/WO2011134366A1/en

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B26/00Compositions of mortars, concrete or artificial stone, containing only organic binders, e.g. polymer or resin concrete
    • C04B26/02Macromolecular compounds
    • C04B26/26Bituminous materials, e.g. tar, pitch
    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B2111/00Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
    • C04B2111/00474Uses not provided for elsewhere in C04B2111/00
    • C04B2111/0075Uses not provided for elsewhere in C04B2111/00 for road construction
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Definitions

  • the present invention relates to a method of producing a rubber asphalt mixture and a rubber asphalt mixture produced therefrom.
  • Rubber asphalt is a product obtained by mixing rubber powder and asphalt in a certain ratio, and is a binder used in various types of flexible pavement construction.
  • the mixture of rubber asphalt and mineral material is called rubber asphalt mixture.
  • rubber asphalt concrete When it is paved and rolled, it is also called rubber asphalt concrete.
  • the rubber asphalt pavement technology has formed a relatively complete wet process and dry process.
  • the dry process is a method in which rubber powder is added to a mineral material and placed in a mixing plant, and a hot asphalt mixture is added to produce a rubber asphalt mixture.
  • the wet process is a production method in which rubber powder and asphalt are first mixed to form rubber asphalt and then mixed with mineral materials to produce rubber asphalt mixture. Rubber asphalt mixtures are also classified into dry and wet rubber asphalt mixtures, depending on the production process.
  • the wet process first adds the rubber powder to the matrix asphalt and stirs under high temperature conditions, the rubber powder is fully swelled in the matrix asphalt and a relatively complicated material exchange and chemical reaction with the asphalt occurs.
  • the rubber powder is here. Desulfurization and degradation occur during the process, which improves the adhesion of rubber particles.
  • some rubber components enter the asphalt, and the asphalt is modified to improve the adhesion of the asphalt and to strengthen the asphalt.
  • the wet rubber asphalt mixture exhibits excellent properties of high viscosity and high elasticity.
  • the dry process involves adding rubber particles directly to the aggregate and then spraying it into hot asphalt to form a rubber asphalt mixture. Due to the addition of highly elastic waste rubber particles, the elasticity and damping properties of the road surface can be increased, and the tire/road surface pumping noise and the tire vibration noise can be reduced.
  • the processing method of the rubber particles used in the dry process is simple, the process of mixing the mixture is simple, time-consuming, and does not require expensive rubber asphalt production equipment and energy costs, and is economical and efficient compared with the wet process.
  • the rubber particles in the dry rubber asphalt mixture can not complete the process of desulfurization and degradation, and can not modify the asphalt with material exchange with asphalt. , can only be used as aggregates,
  • the effect on the performance improvement of asphalt pavement is not obvious. Therefore, the performance of the existing dry rubber asphalt mixture is inferior to that of the wet asphalt, especially the water stability is poor, and it is often necessary to add additives such as cement and lime to improve the water stability in the production process. Due to the poor adhesion of the rubber particles and the poor miscibility with the mineral materials, the premixing of the mineral materials and the rubber particles is required, which affects the heat storage of the mixture and limits the paving and rolling time, so that the paving is formed.
  • Rubber asphalt concrete is only suitable for the middle and lower layers of highways due to its low quality.
  • the rubber asphalt will absorb the equal volume of asphalt, so that the ratio of the mixture to the oil and stone (the mass ratio of the asphalt to the mineral) increases, limiting the amount and quality of the rubber powder modifier, and increasing The cost of the rubber asphalt mixture.
  • the object of the present invention is to overcome the above-mentioned shortcomings of the prior art dry rubber asphalt mixture and its production process, and to provide a high-volume dry rubber asphalt mixture and a production method thereof.
  • the rubber asphalt mixing method of the invention has the advantages of simple production method and easy operation, and the rubber powder modifier dosage ratio can be improved by the method, the rubber particle asphaltene can be changed, the “glue oil” can be realized, the amount of the petroleum matrix asphalt can be reduced, and the rubber can be improved. The amount and quality of the powder modifier.
  • the rubber asphalt mixture production method of the invention does not need the premixing process of the traditional dry process, and does not need to add mineral powder, cement, lime lime or blending oil, extended oil and other auxiliary agents, and the rubber asphalt mixture prepared by the technology.
  • the indicators are in line with industry standards and are very economical.
  • the rubber powder is obtained by pulverizing a skewed nylon or a meridian steel waste tire.
  • a method for producing a straight rubber asphalt mixture comprising the following steps:
  • Preparation of rubber asphalt mixture The mineral material is heated to 210 ⁇ 220 °C, and the petroleum matrix asphalt is heated to 160 ⁇ 170 °C.
  • C8H1802 which is white powder or flake, has the function of promoting the low-temperature synthesis of asphaltenes from petroleum asphalt and rubber hydrocarbon molecules, and can increase the permeability of rubber powder modifier.
  • the rubber asphalt mixture of the present invention is prepared by heating the matrix asphalt to
  • the rubber powder modifier prepared according to the method of the invention has strong permeability, and the rubber particles become rubber oil at high temperature, and some components of the rubber powder enter the asphalt, and asphaltene changes occur, thereby realizing "glue oil” and rubber powder reform.
  • the compatibility of the agent with the ore material is strong, and the rubber powder modifier can penetrate into the stone lattice, thereby increasing the amount of the rubber powder modifier in the rubber asphalt and reducing the amount of the asphalt.
  • the oil to stone ratio of the mix can be reduced from 8-10 to 6-8.
  • the straight rubber asphalt mixture of the invention is evaluated by the Marshall test method and the road performance index, and a plurality of technical indicators are obviously higher than the industry standard, and can be used for waterproofing and leakproof use of road construction and roof tunnels.
  • the rubber pitch in the examples of the present invention was prepared as follows:
  • the straight rubber asphalt mixture of the present embodiment is prepared as follows:
  • the material is prepared according to the density of the Marshall test piece at the optimum oil-stone ratio of 0.98 times.
  • the method "forms ⁇ 10 X 10cm cylindrical test piece to ensure the same degree of compaction as the site.
  • test results of the high-volume straight-mixed rubber asphalt mixture prepared by the above three examples are as follows: Table 1, Marshall test results

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Ceramic Engineering (AREA)
  • Materials Engineering (AREA)
  • Structural Engineering (AREA)
  • Organic Chemistry (AREA)
  • Compositions Of Macromolecular Compounds (AREA)
  • Road Paving Structures (AREA)

Abstract

A rubber asphalt mixture and a preparation method thereof are disclosed. The mixture is prepared with gradation stone, petroleum matrix asphalt and rubber powder modifier in a weight ratio of 89-94:4-6:2-5, wherein the rubber powder modifier consists of rubber power and hexanediol in a weight ratio of 100:3-7. The method comprises the following steps: mixing the hexanediol and the waste tyre powder according to the ratio to obtain the rubber powder modifier by mixing and wetting; heating the mineral aggregates to the temperature of 210 to 220°C, and then adding the rubber powder modifier and the petroleum matrix asphalt into the mineral aggregates at the same time to obtain the mixture after mixing for 40 to 60 seconds. The method is simple and free of pre-mixing the rubber powder and the stone. The transformation from rubber to oil can be implemented, and the petroleum-stone ratio of the mixture can be reduced to 6-8. All technical parameters of the directly-mixed rubber asphalt mixture are higher than those of the industrial standard, and the directly-mixed rubber asphalt mixture can be used for the road construction and water prevention and leakage prevention of roof and tunnels.

Description

一种直拌橡胶沥青混合料及其生产方法  Straight mixed rubber asphalt mixture and production method thereof
技术领域 Technical field
本发明涉及一种生产橡胶沥青混合料的方法及其生产的橡胶沥青混合料。  The present invention relates to a method of producing a rubber asphalt mixture and a rubber asphalt mixture produced therefrom.
背景技术 Background technique
橡胶沥青是橡胶粉与沥青按一定比例拌合而得到的产物, 是一种用于多种类型柔性路面 施工中的粘结剂。 橡胶沥青与矿料拌合而得到的混合物称为橡胶沥青混合料, 当其摊铺碾压 成型后, 又称为橡胶沥青混凝土。 目前橡胶沥青路面技术已经形成比较完善的湿法工艺和干 法工艺。 干法工艺是将橡胶粉加入矿料后, 投放到拌和楼里, 同时加入热沥青拌和生产橡胶 沥青混合料的生产方法。 湿法工艺是首先将橡胶粉和沥青拌和, 形成橡胶沥青后再与矿料拌 和生产橡胶沥青混合料的生产方法。 根据生产工艺的不同, 橡胶沥青混合料也相应地分为干 法和湿法橡胶沥青混合料两种。  Rubber asphalt is a product obtained by mixing rubber powder and asphalt in a certain ratio, and is a binder used in various types of flexible pavement construction. The mixture of rubber asphalt and mineral material is called rubber asphalt mixture. When it is paved and rolled, it is also called rubber asphalt concrete. At present, the rubber asphalt pavement technology has formed a relatively complete wet process and dry process. The dry process is a method in which rubber powder is added to a mineral material and placed in a mixing plant, and a hot asphalt mixture is added to produce a rubber asphalt mixture. The wet process is a production method in which rubber powder and asphalt are first mixed to form rubber asphalt and then mixed with mineral materials to produce rubber asphalt mixture. Rubber asphalt mixtures are also classified into dry and wet rubber asphalt mixtures, depending on the production process.
由于湿法工艺首先将橡胶粉加入到基质沥青中, 在高温条件下搅拌, 使橡胶粉在基质沥 青中得到充分溶胀并与沥青发生较为复杂的物质交换与化学反应, 一方面, 橡胶粉在此过程 中发生脱硫、 降解, 提高了橡胶颗粒的粘着性能; 另一方面, 部分橡胶成分进入沥青中, 对 沥青进行改性以提高沥青的粘接性等性能并对沥青起到加劲作用。 因而, 湿法橡胶沥青混合 料表现出高粘度、 高弹性的优良性能。 但是, 湿法工艺需要专门的橡胶沥青生产设备, 设备 投入大, 并且湿法工艺复杂, 流程长, 需要在高温下反应 l-4h, 能耗较大。 干法工艺是将橡胶颗粒直接加入集料中, 然后喷入热沥青拌制成橡胶沥青混合料。 由于 高弹性废旧橡胶颗粒的加入, 可增加路面的弹性和阻尼性能, 可降低轮胎 /路面泵气噪声和减 小轮胎振动噪声。 干法工艺所用的橡胶颗粒加工工艺简单, 拌制混合料的工艺简单、 费时较 短, 不需要昂贵的橡胶沥青生产设备及能源费用, 较湿法工艺经济、 效率高。 但是, 由于干 法橡胶沥青混合料的制备时间短, 只有 1分钟左右, 干法橡胶沥青混合料中的橡胶颗粒不能 完成脱硫、 降解的过程, 也不能与沥青进行物质交换而对沥青进行改性, 仅能充当集料使用, 对沥青路面性能改善效果不明显。 因而, 现有的干法橡胶沥青混合料的性能较湿法沥青的性 能差, 特别是水稳定性差, 生产过程中往往需要添加水泥、 硝石灰等添加剂来改善水稳性。 由于橡胶颗粒的粘接性较差, 与矿料的混溶性差, 需进行矿料与橡胶颗粒的预拌, 影响了混 合料的热储并限制了摊铺碾压时间, 使得摊铺成型的橡胶沥青混凝土由于质量较低而仅适宜 作公路的中下层。 并且干法橡胶沥青混合料在拌制时, 橡胶沥青会吸收等体积沥青, 使混合 料油石比 (沥青与矿料的质量比) 增加, 限制了橡胶粉改性剂掺量及质量, 加大了橡胶沥青 混合料的成本。 目前国内外橡胶粉改性剂的掺量质量比例为沥青:橡胶粉改性剂 =1 : 0.2〜0.3, 高于此比例则摊铺碾压不能成型, 橡胶沥青用量为混合料总重量的 8〜10%。 Since the wet process first adds the rubber powder to the matrix asphalt and stirs under high temperature conditions, the rubber powder is fully swelled in the matrix asphalt and a relatively complicated material exchange and chemical reaction with the asphalt occurs. On the one hand, the rubber powder is here. Desulfurization and degradation occur during the process, which improves the adhesion of rubber particles. On the other hand, some rubber components enter the asphalt, and the asphalt is modified to improve the adhesion of the asphalt and to strengthen the asphalt. Thus, the wet rubber asphalt mixture exhibits excellent properties of high viscosity and high elasticity. However, the wet process requires special rubber asphalt production equipment, the equipment investment is large, and the wet process is complicated, the process is long, and it needs to react at high temperature for l-4h, and the energy consumption is large. The dry process involves adding rubber particles directly to the aggregate and then spraying it into hot asphalt to form a rubber asphalt mixture. Due to the addition of highly elastic waste rubber particles, the elasticity and damping properties of the road surface can be increased, and the tire/road surface pumping noise and the tire vibration noise can be reduced. The processing method of the rubber particles used in the dry process is simple, the process of mixing the mixture is simple, time-consuming, and does not require expensive rubber asphalt production equipment and energy costs, and is economical and efficient compared with the wet process. However, due to the short preparation time of the dry rubber asphalt mixture, only about 1 minute, the rubber particles in the dry rubber asphalt mixture can not complete the process of desulfurization and degradation, and can not modify the asphalt with material exchange with asphalt. , can only be used as aggregates, The effect on the performance improvement of asphalt pavement is not obvious. Therefore, the performance of the existing dry rubber asphalt mixture is inferior to that of the wet asphalt, especially the water stability is poor, and it is often necessary to add additives such as cement and lime to improve the water stability in the production process. Due to the poor adhesion of the rubber particles and the poor miscibility with the mineral materials, the premixing of the mineral materials and the rubber particles is required, which affects the heat storage of the mixture and limits the paving and rolling time, so that the paving is formed. Rubber asphalt concrete is only suitable for the middle and lower layers of highways due to its low quality. When the dry rubber asphalt mixture is mixed, the rubber asphalt will absorb the equal volume of asphalt, so that the ratio of the mixture to the oil and stone (the mass ratio of the asphalt to the mineral) increases, limiting the amount and quality of the rubber powder modifier, and increasing The cost of the rubber asphalt mixture. At present, the proportion of rubber powder modifier at home and abroad is asphalt: rubber powder modifier = 1: 0.2~0.3, higher than this ratio, paving and rolling can not be formed, the amount of rubber asphalt is 8 of the total weight of the mixture. ~10%.
发明内容 Summary of the invention
本发明的目的在于克服现有干法橡胶沥青混合料及其生产工艺中所存在的上述不足, 提 供一种的高掺量干法橡胶沥青混合料及其生产方法。本发明的橡胶沥青混合的生产方法简单、 操作容易, 通过该方法提高橡胶粉改性剂掺量比, 能使橡胶颗粒沥青质变, 实现 "胶变油", 降低石油基质沥青的用量, 提高橡胶粉改性剂的掺量和质量。 本发明的橡胶沥青混合料生产 方法无需传统干法工艺的预拌工艺, 也不需要添加矿粉、 水泥、 硝石灰或调和油、 延展油等 其它助剂, 制备的橡胶沥青混合料各项技术指标符合行业标准, 并且十分经济。  SUMMARY OF THE INVENTION The object of the present invention is to overcome the above-mentioned shortcomings of the prior art dry rubber asphalt mixture and its production process, and to provide a high-volume dry rubber asphalt mixture and a production method thereof. The rubber asphalt mixing method of the invention has the advantages of simple production method and easy operation, and the rubber powder modifier dosage ratio can be improved by the method, the rubber particle asphaltene can be changed, the “glue oil” can be realized, the amount of the petroleum matrix asphalt can be reduced, and the rubber can be improved. The amount and quality of the powder modifier. The rubber asphalt mixture production method of the invention does not need the premixing process of the traditional dry process, and does not need to add mineral powder, cement, lime lime or blending oil, extended oil and other auxiliary agents, and the rubber asphalt mixture prepared by the technology. The indicators are in line with industry standards and are very economical.
本发明实现上述发明目的的技术方案为:  The technical solution of the present invention to achieve the above object of the invention is:
一种直拌橡胶沥青混合料, 它是按以下重量比的组份进行配置: 级配石料: 石油基质沥 青: 橡胶粉改性剂 =89〜94: 4〜6: 2〜5, 所述橡胶粉改性剂由如下重量比的组份组成: 橡胶 粉: 己二醇 =100: 3〜7。 所述橡胶粉是由斜交尼龙或子午钢丝废旧轮胎经粉碎加工而成。 A straight mix rubber asphalt mixture, which is configured according to the following weight ratio components: grading stone: petroleum matrix asphalt: rubber powder modifier = 89~94 : 4~6: 2~5, the rubber The powder modifier consists of the following weight ratio components: Rubber powder: hexanediol = 100: 3 to 7. The rubber powder is obtained by pulverizing a skewed nylon or a meridian steel waste tire.
一种直拌橡胶沥青混合料的生产方法, 包括以下步骤:  A method for producing a straight rubber asphalt mixture, comprising the following steps:
( 1 )、 制备橡胶粉改性剂: 将己二醇按橡胶粉: 己二醇 =100 : 3〜7的重量比例掺入橡胶 粉中, 拌和润湿得橡胶粉改性剂, 将橡胶粉改性剂装入拌和楼粉仓备用; (2)、 制备橡胶沥青混合料: 将矿料加热至 210〜220°C, 石油基质沥青加热至 160〜170 °C, 按照极配石料: 沥青: 橡胶粉改性剂 =89〜94: 4〜6: 2〜5 的重量比例, 向矿料中同时 加入橡胶粉改性剂和石油基质沥青, 拌合 40〜60s, 控制混合料出料温度为 180〜200°C, 得 到橡胶沥青混合料。 (1) Preparation of rubber powder modifier: hexanediol is blended into rubber powder according to the weight ratio of rubber powder: hexanediol = 100: 3~7, mixed and wetted to obtain rubber powder modifier, rubber powder The modifier is put into the mixing room of the mixing room for use; (2) Preparation of rubber asphalt mixture: The mineral material is heated to 210~220 °C, and the petroleum matrix asphalt is heated to 160~170 °C. According to the polar stone: Asphalt: Rubber powder modifier=89~94 : 4 ~6: 2~5 weight ratio, adding rubber powder modifier and petroleum matrix asphalt to the mineral material, mixing 40~60s, controlling the mixture discharge temperature to 180~200°C, and obtaining rubber asphalt mixture .
本发明的橡胶沥青混合料按以下重量比的组份进行配置: 级配石料: 石油基质沥青: 橡 胶粉改性剂 =89〜94: 4〜6: 2〜5, 橡胶粉改性剂由废轮胎粉和己二醇组成, 己二醇是一种橡 胶交联剂, 化学组份为 2,5-二甲基 -2,5-己二醇, 英文名: 2,5-dimethyl-2,5-hexanediol, 分子式The rubber asphalt mixture of the present invention is configured in the following weight ratio components: Graded stone: Petroleum matrix asphalt: Rubber powder modifier = 89~94 : 4~6: 2~5, rubber powder modifier from waste Tire powder and hexanediol, hexanediol is a rubber cross-linking agent, the chemical component is 2,5-dimethyl-2,5-hexanediol, English name: 2,5-dimethyl-2,5 -hexanediol, molecular formula
C8H1802, 为白色粉状或片状, 具有促进石油沥青和橡胶碳氢分子低温合成沥青质的功能, 能增加橡胶粉改性剂的渗透性。 本发明的橡胶沥青混合料的制备方法是将基质沥青加热至C8H1802, which is white powder or flake, has the function of promoting the low-temperature synthesis of asphaltenes from petroleum asphalt and rubber hydrocarbon molecules, and can increase the permeability of rubber powder modifier. The rubber asphalt mixture of the present invention is prepared by heating the matrix asphalt to
160〜170°C后, 与橡胶粉改性剂同时加入到加热的级配石料中, 拌和 40-60s, 即可得到橡胶 沥青。 该方法无需将橡胶粉与石料进行预拌, 方法简单。 按照本发明方法制备的橡胶粉改性 剂的渗透性较强, 橡胶颗粒在高温下变成橡胶油, 胶粉的某些成分进入沥青, 发生沥青质变, 实现"胶变油",橡胶粉改性剂与矿石料的混溶性较强,橡胶粉改性剂可以渗透入石料晶格中, 从而可以提高橡胶沥青中橡胶粉改性剂的用量而降低沥青的用量。 混合料的油石比可由 8-10 降低为 6-8。本发明的直拌橡胶沥青混合料用马歇尔试验方法及路用性能指标进行评价, 多项 技术指标均明显高于行业标准, 可用于公路施工和屋面隧道防水防漏使用。 After 160~170 °C, it is added to the heated grading stone at the same time as the rubber powder modifier, and mixed for 40-60 s to obtain rubber asphalt. The method does not need to premix the rubber powder and the stone, and the method is simple. The rubber powder modifier prepared according to the method of the invention has strong permeability, and the rubber particles become rubber oil at high temperature, and some components of the rubber powder enter the asphalt, and asphaltene changes occur, thereby realizing "glue oil" and rubber powder reform. The compatibility of the agent with the ore material is strong, and the rubber powder modifier can penetrate into the stone lattice, thereby increasing the amount of the rubber powder modifier in the rubber asphalt and reducing the amount of the asphalt. The oil to stone ratio of the mix can be reduced from 8-10 to 6-8. The straight rubber asphalt mixture of the invention is evaluated by the Marshall test method and the road performance index, and a plurality of technical indicators are obviously higher than the industry standard, and can be used for waterproofing and leakproof use of road construction and roof tunnels.
具体实施方式 detailed description
下面结合具体实施方式对本发明作进一步的详细描述。 但不应将此理解为本发明上述主 题的范围仅限于以下的实施例, 凡基于本发明内容所实现的技术均属于本发明的范围。  The present invention will be further described in detail below in conjunction with the specific embodiments. However, the scope of the above-mentioned subject matter of the present invention should not be construed as being limited to the following embodiments, and the technology implemented based on the present invention is within the scope of the present invention.
本发明列举的实施例中的橡胶沥青按照以下方法制备:  The rubber pitch in the examples of the present invention was prepared as follows:
实施例 1  Example 1
本实施例列举的直拌橡胶沥青混合料, 为 AC10级配城市白加黑混合料, 按以下重量比 的组份进行配置: 石料: 石油基质沥青: 橡胶粉改性剂 =89: 6: 5, 所述橡胶粉改性剂由如下 重量比的组份组成: 废轮胎胶粉: 己二醇 =100: 3。 The straight mix rubber asphalt mixture listed in this embodiment is AC10 grade urban white plus black mixture, and is configured according to the following weight ratio components: Stone material: petroleum matrix asphalt: rubber powder modifier=89: 6: 5 , the rubber powder modifier is as follows Component composition of weight ratio: Waste tire rubber powder: hexanediol = 100: 3.
本实施例的直拌橡胶沥青混合料按以下方法制备:  The straight rubber asphalt mixture of the present embodiment is prepared as follows:
( 1 )、制备橡胶粉改性剂:将己二醇按橡胶粉: 己二醇 =100: 3的重量比例掺入橡胶粉中, 拌和润湿得橡胶粉改性剂, 将橡胶粉改性剂装入拌和楼粉仓备用;  (1) Preparation of rubber powder modifier: hexanediol is blended into rubber powder according to the weight ratio of rubber powder: hexanediol=100:3, and the rubber powder modifier is mixed and wetted to modify the rubber powder. The agent is charged into the mixing room of the mixing room;
(2)、 制备橡胶沥青混合料: 在拌和仓将级配石料加热至 210〜220°C, 将石油基质沥青 加热至 160〜170°C, 按照极配石料: 沥青: 橡胶粉改性剂 =89: 6: 5的重量比例, 通过电 脑计量控制,将橡胶粉改性剂和石油基质沥青同时喷洒入拌和仓内与石料拌合 40〜60s, 即完 成胶变油的沥青改性过程, 控制混合料出料温度为 180〜200°C, 得到橡胶沥青混合料。  (2) Preparation of rubber asphalt mixture: The grading stone is heated to 210~220 °C in the mixing chamber, and the petroleum matrix asphalt is heated to 160~170 °C. According to the matching stone: Asphalt: Rubber powder modifier= 89: 6: 5 weight ratio, through the computer metering control, the rubber powder modifier and the petroleum matrix asphalt are simultaneously sprayed into the mixing chamber and the stone is mixed for 40~60s, that is, the asphalt modification process of the rubber-to-oil is completed, and the control is completed. The mixture discharge temperature was 180 to 200 ° C to obtain a rubber asphalt mixture.
实施例 2  Example 2
本实施例列举的直拌橡胶沥青混合料, 为 AC13—级路面层混合料, 按以下重量比的组 份进行配置: 石料: 石油基质沥青: 橡胶粉改性剂 =92: 5: 3, 所述橡胶粉改性剂由如下重量 比的组份组成: 废轮胎胶粉: 己二醇 =100: 5。  The straight mix rubber asphalt mixture enumerated in this embodiment is an AC13-grade pavement layer mixture, and is configured according to the following weight ratio components: Stone material: petroleum base asphalt: rubber powder modifier=92: 5:3, The rubber powder modifier consists of the following weight ratio components: Waste tire rubber powder: hexanediol = 100: 5.
本实施例的直拌橡胶沥青混合料按以下方法制备:  The straight rubber asphalt mixture of the present embodiment is prepared as follows:
( 1 )、制备橡胶粉改性剂:将己二醇按橡胶粉: 己二醇 =100: 5的重量比例掺入橡胶粉中, 拌和润湿得橡胶粉改性剂, 将橡胶粉改性剂装入拌和楼粉仓备用;  (1) Preparation of rubber powder modifier: hexanediol is blended into rubber powder according to the weight ratio of rubber powder: hexanediol=100:5, mixed and wetted to obtain rubber powder modifier, and rubber powder modified The agent is charged into the mixing room of the mixing room;
(2)、 制备橡胶沥青混合料: 在拌和仓将级配石料加热至 210〜220°C, 将石油基质沥青 加热至 160〜170°C, 按照极配石料: 沥青: 橡胶粉改性剂 =92: 5: 3的重量比例, 通过电脑 计量控制,将橡胶粉改性剂和石油基质沥青同时喷洒入拌和仓内与石料拌合 40〜60s, 即完成 胶变油的沥青改性过程, 控制混合料出料温度为 180〜200°C, 得到橡胶沥青混合料。  (2) Preparation of rubber asphalt mixture: The grading stone is heated to 210~220 °C in the mixing chamber, and the petroleum matrix asphalt is heated to 160~170 °C. According to the matching stone: Asphalt: Rubber powder modifier= 92: 5: 3 weight ratio, through the computer metering control, the rubber powder modifier and the petroleum matrix asphalt are simultaneously sprayed into the mixing chamber and the stone is mixed for 40~60s, that is, the asphalt modification process of the rubber-to-oil is completed, and the control is completed. The mixture discharge temperature was 180 to 200 ° C to obtain a rubber asphalt mixture.
实施例 3  Example 3
本实施例列举的直拌橡胶沥青混合料, 为 AC16中间层混合料, 按以下重量比的组份进 行配置: 石料: 石油基质沥青: 橡胶粉改性剂 =94: 4: 2, 所述橡胶粉改性剂由如下重量比的 组份组成: 废轮胎胶粉: 己二醇 =100: 7。 本实施例的直拌橡胶沥青混合料按以下方法制备: The straight rubber asphalt mixture enumerated in this embodiment is an AC16 intermediate layer mixture, and is configured according to the following weight ratio components: Stone: petroleum matrix asphalt: rubber powder modifier = 94: 4: 2, the rubber The powder modifier consists of the following weight ratio components: Waste tire rubber powder: hexanediol = 100: 7. The straight rubber asphalt mixture of the present embodiment is prepared as follows:
( 1 )、制备橡胶粉改性剂:将己二醇按橡胶粉: 己二醇 =100: 7的重量比例掺入橡胶粉中, 拌和润湿得橡胶粉改性剂, 将橡胶粉改性剂装入拌和楼粉仓备用;  (1) Preparation of rubber powder modifier: hexanediol is blended into rubber powder according to the weight ratio of rubber powder: hexanediol=100:7, and the rubber powder modifier is mixed and wetted to modify the rubber powder. The agent is charged into the mixing room of the mixing room;
(2)、 制备橡胶沥青混合料: 在拌和仓将级配石料加热至 210〜220°C, 将石油基质沥青 加热至 160〜170°C, 按照极配石料: 沥青: 橡胶粉改性剂 =94: 4: 2的重量比例, 通过电脑 计量控制,将橡胶粉改性剂和石油基质沥青同时喷洒入拌和仓内与石料拌合 40〜60s, 即完成 胶变油的沥青改性过程, 控制混合料出料温度为 180〜200°C, 得到橡胶沥青混合料。  (2) Preparation of rubber asphalt mixture: The grading stone is heated to 210~220 °C in the mixing chamber, and the petroleum matrix asphalt is heated to 160~170 °C. According to the matching stone: Asphalt: Rubber powder modifier= 94: 4: 2 weight ratio, through the computer metering control, the rubber powder modifier and the petroleum matrix asphalt are simultaneously sprayed into the mixing chamber and mixed with the stone for 40~60s, that is, the asphalt modification process of the rubber-to-oil is completed, and the control is completed. The mixture discharge temperature was 180 to 200 ° C to obtain a rubber asphalt mixture.
用马歇尔试验方法及路用性能指标对各实施例的直拌橡胶混合料的质量进行评价: 马歇尔试验: (表干法 T0705-2000)  The quality of the straight mix rubber mixture of each example was evaluated by the Marshall test method and the road performance index: Marshall test: (surface dry method T0705-2000)
高温车辙试验  High temperature rutting test
根据 《公路工程沥青及沥青混合料试验规程》 (JTJ052-2000 ) 中沥青混合料车辙试验方 法进行高温车辙试验, 按现行 《公路沥青路面施工技术规范》 (JTGF40-2004) 中的相关技术 要求评价。  According to the Test Procedure for Asphalt Mixture of Highway Engineering Asphalt and Asphalt Mixture (JTJ052-2000), the high temperature rutting test is carried out according to the relevant technical requirements in the current Technical Specifications for Highway Asphalt Pavement Construction (JTGF40-2004). .
低温小梁弯曲试验  Low temperature trabecular bending test
根据 《公路工程沥青及沥青混合料试验规程》 (JTJ052-2000 ) 中沥青混合料弯曲试验标 准 (T0715-1993 ) 进行低温小梁弯曲试验, 按现行 《公路沥青路面施工技术规范》 (JTGF40-2004) 中的相关技术要求评价。  According to the Bending Test Standard for Asphalt Mixtures in the Test Procedure for Asphalt and Asphalt Mixtures of Highway Engineering (JTJ052-2000) (T0715-1993), the low-temperature trabecular bending test is carried out according to the current Technical Specifications for Construction of Highway Asphalt Pavement (JTGF40-2004). Relevant technical requirements in the evaluation.
水稳定性试验  Water stability test
根据 《公路工程沥青及沥青混合料试验规程》 (JTJ052-2000 ) 中沥青混合料冻融劈裂试 验条件进行试验, 按照最佳油石比下的马歇尔试件密度的 0.98倍备料, 采用 "静压法"成型 Φ 10 X 10cm圆柱体试件, 保证与现场相同的压实度。  According to the test conditions for the freeze-thaw splitting of asphalt mixture in the Test Procedure for Asphalt and Asphalt Mixtures of Highway Engineering (JTJ052-2000), the material is prepared according to the density of the Marshall test piece at the optimum oil-stone ratio of 0.98 times. The method "forms Φ 10 X 10cm cylindrical test piece to ensure the same degree of compaction as the site.
[0020] 上述三个实施例所制备的高掺量直拌橡胶沥青混合料的试验结果如下: 表 1、 马歇尔试验结果
Figure imgf000008_0001
[0020] The test results of the high-volume straight-mixed rubber asphalt mixture prepared by the above three examples are as follows: Table 1, Marshall test results
Figure imgf000008_0001
表 2、 车辙试验动稳定度指标检验结果
Figure imgf000008_0002
Table 2, rutting test dynamic stability index test results
Figure imgf000008_0002
表 3、 弯曲破坏应变指标检验结果
Figure imgf000008_0003
Table 3. Test results of bending failure strain index
Figure imgf000008_0003
表 4、 冻融劈裂试验结果
Figure imgf000008_0004
替换页(细则第 26条)
Table 4, freeze-thaw split test results
Figure imgf000008_0004
Replacement page (Article 26)

Claims

1. 一种直拌橡胶沥青混合料, 其特征在于它是按以下重量比的组份进行配置: 级配石料: 石 油基质沥青: 橡胶粉改性剂 =89〜94: 4〜6: 2〜5, 所述橡胶粉改性剂由如下重量比的组份组 成: 橡胶粉: 己二醇 =100 : 3〜7。 1. A straight mix rubber asphalt mixture characterized in that it is configured in the following weight ratio components: Graded stone: Petroleum matrix asphalt: Rubber powder modifier = 89~94 : 4~6: 2~ 5. The rubber powder modifier is composed of the following components by weight: rubber powder: hexanediol = 100: 3 to 7.
2. —种权利要求 1所述直拌橡胶沥青混合料的生产方法, 其特征在于包括以下步骤: 2. A method of producing a straight rubber asphalt mixture according to claim 1, comprising the steps of:
( 1 )、制备橡胶粉改性剂: 将己二醇按橡胶粉: 己二醇 =100 : 3〜7的重量比例掺入橡胶粉中, 拌和润湿得橡胶粉改性剂, 将橡胶粉改性剂装入拌和楼粉仓备用; (1) Preparation of rubber powder modifier: hexanediol is blended into rubber powder according to the weight ratio of rubber powder: hexanediol = 100: 3~7, mixed and wetted to obtain rubber powder modifier, rubber powder The modifier is put into the mixing room of the mixing room for use;
(2)、 制备橡胶沥青混合料: 将矿料加热至 210〜220°C, 石油基质沥青加热至 160〜170°C, 按照极配石料: 沥青: 橡胶粉改性剂 =89〜94: 4〜6: 2〜5 的重量比例, 向矿料中同时加入 橡胶粉改性剂和石油基质沥青, 拌合 40〜60s, 控制混合料出料温度为 180〜200°C, 得到橡 胶沥青混合料。 (2) Preparation of rubber asphalt mixture: The mineral material is heated to 210~220 °C, and the petroleum base asphalt is heated to 160~170 °C. According to the polar stone: Asphalt: Rubber powder modifier=89~94 : 4 ~6: 2~5 weight ratio, adding rubber powder modifier and petroleum matrix asphalt to the mineral material, mixing 40~60s, controlling the mixture discharge temperature to 180~200°C, and obtaining rubber asphalt mixture .
PCT/CN2011/073110 2010-04-28 2011-04-21 Directly-mixed rubber asphalt mixture and production method thereof WO2011134366A1 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
CN201010158249.7 2010-04-28
CN2010101582497A CN101798203B (en) 2010-04-28 2010-04-28 Directly-mixed rubber asphalt mixture and production method thereof

Publications (1)

Publication Number Publication Date
WO2011134366A1 true WO2011134366A1 (en) 2011-11-03

Family

ID=42594068

Family Applications (1)

Application Number Title Priority Date Filing Date
PCT/CN2011/073110 WO2011134366A1 (en) 2010-04-28 2011-04-21 Directly-mixed rubber asphalt mixture and production method thereof

Country Status (2)

Country Link
CN (1) CN101798203B (en)
WO (1) WO2011134366A1 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103669153A (en) * 2013-12-31 2014-03-26 山东卓洋机电科技有限公司 Low-temperature micro-surfacing construction technology

Families Citing this family (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101798203B (en) * 2010-04-28 2012-05-16 周其强 Directly-mixed rubber asphalt mixture and production method thereof
CN102040354B (en) * 2010-11-16 2012-11-21 中交第一公路勘察设计研究院有限公司 Environment-friendly high-elastic asphalt mixture used as stress absorbing layer
CN102952293A (en) * 2011-08-30 2013-03-06 中国石油化工股份有限公司 Compound rubber powder modifying agent as well as preparation method and application method thereof
CN102503245B (en) * 2011-10-25 2013-05-15 华南理工大学 Cold recycled asphalt mixture and its normal temperature emulsification regeneration method
CN102382480B (en) * 2011-12-15 2013-03-20 周其强 Application of organosilicon residues in preparation of synthetic rubber asphalt
CN103570279B (en) * 2013-10-25 2015-05-20 广东易山重工股份有限公司 Material for quickly and effectively repairing pits of asphalt pavement and preparation method thereof
CN104140223B (en) * 2014-07-29 2016-05-11 重庆路面科技有限公司 One is delivered directly activation rubber-asphalt mixture and preparation method thereof
CN109665753B (en) * 2018-12-20 2020-03-27 中交云南高速公路发展有限公司 Directly throwing rubber powder, asphalt mixture, pavement using the mixture and processing method thereof
CN110028800A (en) * 2019-03-21 2019-07-19 华南理工大学 A kind of miscible method of rubber asphalt of the drag reducer of viscosity reduction containing liquid

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1528823A (en) * 2003-09-26 2004-09-15 沈阳三鑫公路工程有限公司 Preparation method of waste rubber powder modified asphalt
CN1609165A (en) * 2003-10-24 2005-04-27 中国石油化工股份有限公司 Waste rubber powder modified asphalt and its prepn process
CN1970638A (en) * 2005-11-22 2007-05-30 四川维城磁能有限公司 Modified asphalt and method for making same
CN1970608A (en) * 2005-11-22 2007-05-30 四川维城磁能有限公司 Activating rubber powder and its preparation method
CN101275026A (en) * 2007-03-30 2008-10-01 上海群康沥青科技有限公司 Production method for modified rubber asphalt
CN101798203A (en) * 2010-04-28 2010-08-11 周其强 Directly-mixed rubber asphalt mixture and production method thereof

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
AU3657099A (en) * 1998-04-20 1999-11-08 Ashland Inc. Asphalt release agent
JP2003171557A (en) * 2001-12-05 2003-06-20 Fiber Resin Kk Non-heating type modified asphalt, water-permeable pavement structure therefrom and construction method therefor
CN201245808Y (en) * 2008-08-07 2009-05-27 廊坊通用机械制造有限公司 Rubber modified asphalt apparatus

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1528823A (en) * 2003-09-26 2004-09-15 沈阳三鑫公路工程有限公司 Preparation method of waste rubber powder modified asphalt
CN1609165A (en) * 2003-10-24 2005-04-27 中国石油化工股份有限公司 Waste rubber powder modified asphalt and its prepn process
CN1970638A (en) * 2005-11-22 2007-05-30 四川维城磁能有限公司 Modified asphalt and method for making same
CN1970608A (en) * 2005-11-22 2007-05-30 四川维城磁能有限公司 Activating rubber powder and its preparation method
CN101275026A (en) * 2007-03-30 2008-10-01 上海群康沥青科技有限公司 Production method for modified rubber asphalt
CN101798203A (en) * 2010-04-28 2010-08-11 周其强 Directly-mixed rubber asphalt mixture and production method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103669153A (en) * 2013-12-31 2014-03-26 山东卓洋机电科技有限公司 Low-temperature micro-surfacing construction technology
CN103669153B (en) * 2013-12-31 2016-08-17 山东卓洋机电科技有限公司 Low temperature micro-surfacing construction technique

Also Published As

Publication number Publication date
CN101798203B (en) 2012-05-16
CN101798203A (en) 2010-08-11

Similar Documents

Publication Publication Date Title
WO2011134366A1 (en) Directly-mixed rubber asphalt mixture and production method thereof
CN104312175B (en) A kind of asphalt modifier, modified emulsifying asphalt and modified asphalt mixture and each preparation method
CN101899218A (en) Asphalt warm-mix agent and asphalt mixture mixed by same as well as preparation methods thereof
CN101134655A (en) Gneiss asphalt concrete and preparation method thereof
CN103396043B (en) Warmly-mixed TOR (trans-polyoctenamer rubber reactive modifier) rubber asphalt mixture and preparation method thereof
CN106145776A (en) A kind of polyurethane-polyurea modified asphalt mixture and preparation thereof and application
CN103864352B (en) Durable high-modulus thermal regeneration mixture, preparation method and application
CN103204644B (en) Warmly bitumen-mixed modifier and preparation method thereof
CN102816448B (en) Warm-mixing heavy traffic asphalt and preparation method thereof
CN108975760A (en) A kind of reinforcing agent and application modified for acidity aggregate asphalt
Dulaimi et al. The development of a novel, microwave assisted, half-warm mixed asphalt
CN112062504A (en) Cold-mix concrete and preparation method thereof
CN114920497A (en) Harmless utilization method of oil shale slag and dry distillation drilling oil scrap slag
CN110643185A (en) Reaction type high-viscosity liquid asphalt and preparation method and application thereof
CN117551357A (en) A two-component polyurethane warm-mix composite modified asphalt, asphalt mixture and preparation method thereof
CN104556820B (en) Interfacial modifier capable of improving pitch-aggregate performance and preparation method thereof
CN107500611B (en) Waste grease premixed reinforced asphalt mixture and preparation method thereof
CN106630769A (en) Modified emulsified asphalt cold-mixed and cold-laid mixture for heavy traffic paving middle course and preparation method of modified emulsified asphalt cold-mixed and cold-laid mixture
CN105884264A (en) High-modulus asphalt mixture and preparation method thereof
CN103360773B (en) A kind of composite asphalt modifier and preparation method thereof and application
CN111689717A (en) Antiskid and wear-resistant colored asphalt concrete
CN102690082B (en) Method for preparing modified asphalt macadam mixture by pretreated rock asphalt
CN113735483B (en) A nanocomposite natural rock modified asphalt mixture additive
CN101830669A (en) Method for manufacturing synthetic asphalt for extra heavy traffic
CN112250347A (en) Asphalt concrete suitable for low-heat valley areas and preparation method thereof

Legal Events

Date Code Title Description
121 Ep: the epo has been informed by wipo that ep was designated in this application

Ref document number: 11774357

Country of ref document: EP

Kind code of ref document: A1

NENP Non-entry into the national phase

Ref country code: DE

122 Ep: pct application non-entry in european phase

Ref document number: 11774357

Country of ref document: EP

Kind code of ref document: A1