A production process, equipment and system for plant-mixed warm and hot recycled asphalt mixture

Abstract

The present invention discloses a production process, equipment and system for factory-mixed (warm) hot recycled asphalt mixture, which specifically includes the following mixing methods: fine recycled coarse aggregate enters the hot recycled material drying drum through the cold material bin of the original mixing station together with the new aggregate for heating, screening, and weighing into the main mixing pot; fine recycled coarse aggregate is heated, temporarily stored, and weighed into the main mixing pot through the hot regeneration system; oil-rich fine aggregate is heated to a certain temperature through the cold addition system to the recycled material mixing cylinder, and asphalt regeneration agent is added for mixing, stirring, temporary storage, and weighing into the main mixing pot. By controlling the mixing amount at 15% to 35%, and combining multiple mixing methods, it is ensured that the discharge temperature and performance of the asphalt mixture meet the technical requirements. The preheating and regeneration strategy of oil-rich fine aggregate is used to improve the application efficiency of recycled materials, which can save the amount of sand and gravel materials, save asphalt resources, and reduce carbon emissions and harmful gas emissions during mixing, paving, and rolling.

Description

Technical Field

[0001] The present invention relates to the technical field of recycled materials, and in particular to a production process, equipment and system for factory-mixed warm and hot recycled asphalt mixture. Background Art

[0002] Asphalt pavement is a high-grade pavement widely used in road construction. Asphalt pavement is a variety of pavement formed by paving and rolling asphalt concrete. Asphalt concrete is a mixture formed by fully mixing asphalt materials with a certain viscosity and appropriate amount and mineral aggregates with a certain grade. Asphalt concrete, as an asphalt pavement material, must withstand the repeated effects of vehicle loads and the long-term effects of environmental factors during use. Therefore, asphalt concrete must have a certain bearing capacity and good durability against natural factors. In other words, it must be able to show sufficient stability in high temperature environments, crack resistance in low temperature conditions, good water stability, long-lasting anti-aging and anti-skid properties that are conducive to safety, so as to ensure the good service function of asphalt pavement.

[0003] Asphalt binder improves the ability of paving aggregate to resist damage to the road surface caused by traffic and natural factors, making the road surface smooth, dust-free, impermeable and durable. Asphalt pavement has a high recycling value after being damaged. After the old asphalt pavement is recycled, crushed and screened, it is remixed with regeneration agent, new asphalt material, new aggregate and the like in a certain proportion to form an asphalt mixture. However, the higher the amount of recycled material in the existing technology, the greater the amount of regeneration agent, the longer the required heating time, and the increase in the emission of harmful gases and dust, which not only harms the health of construction operators, but also pollutes the atmosphere, and the performance of the mixture is unstable. For various reasons, the amount of recycled material in the existing thermal regeneration technology is low and the mixing temperature is high, which limits the promotion and application of this technology. In addition, in the heating process of recycled materials, there is a lack of effective control of energy, which also makes the heating process unable to reach the optimal state, which may affect the final performance and quality of the recycled materials.

[0004] In view of this, the present invention provides a plant-mixed warm and hot recycled asphalt mixture production process, equipment and system to solve the technical problems existing in the above-mentioned prior art. Summary of the invention

[0005] Based on the technical problems existing in the background technology, the present invention proposes a production process for plant-mixed warm and hot recycled asphalt mixture, comprising the following steps:

[0006] Step 1: 10% to 50% of the recycled coarse aggregate is passed through the cold material bin and simultaneously enters the hot recycled material drying drum with the new aggregate to be heated to 200℃ for screening;

[0007] Step 2: 20% to 35% of fine recycled coarse aggregate is heated, temporarily stored, and weighed into the main mixer through a hot recycled material drying drum;

[0008] Step 3: 20% to 35% of oil-rich fine aggregate is placed in the cold admixture batching machine, conveyed to the cold recycled material elevator through a belt, lifted to the cold recycled material cold admixture temporary storage bucket, weighed through the cold recycled material cold admixture metering bucket, and then entered into the regeneration mixing pot and mixed with the asphalt regeneration agent, and then conveyed to the main mixing pot through the cold recycled material chute;

[0009] Step 4: Dry mix all the materials in steps 1, 2 and 3 for a certain period of time, then add asphalt binder and stir to make the finished product of recycled asphalt mixture.

[0010] Preferably, the present invention comprises the following steps:

[0011] Step 1: Heat 30% to 50% of recycled coarse aggregate to above 120°C in a hot recycled material drying drum, preheat 20% to 35% of recycled fine aggregate to 80°C and mix with new aggregate;

[0012] Step 2: 30% to 50% of the recycled coarse aggregate is sent to the countercurrent heated hot recycled material drying drum through the hot recycled material batching machine and the belt conveyor, heated to above 120°C in the hot recycled material drying drum, lifted to the hot recycled material scraper conveyor by the hot recycled material elevator, and then transported to the hot recycled material temporary storage hopper through the hot recycled material scraper conveyor. After being weighed by the weighing system according to the mix ratio, it enters the main agitator mixing tank through the chute;

[0013] Step 3: 20% to 35% of oil-rich fine aggregate is placed in the cold admixture batching machine, conveyed to the cold admixture heater by a belt to be preheated to 80°C, lifted to the cold admixture temporary storage bucket by the cold admixture elevator, weighed by the cold admixture metering bucket, and conveyed to the main agitator mixing tank;

[0014] Step 4: Heat 20% to 50% of new aggregate to 200°C through a hot recycled material drying drum, sieve through a vibrating screen, weigh according to the mix ratio and then enter the main agitator mixing tank;

[0015] Step 5: After the hot recycled coarse aggregate, warm recycled oil-rich fine aggregate and new aggregate are stirred in the mixing tank of the main mixer for a certain period of time, they are stirred with the asphalt binder to generate the finished recycled asphalt mixture.

[0016] Preferably, the present invention comprises the following steps:

[0017] Step 1: 30% to 50% of the recycled coarse aggregate is sent to the countercurrent heated hot recycled material drying drum through the hot recycled material batching machine via the belt conveyor, and heated to above 120°C in the hot recycled material drying drum. The new aggregate is heated to 200°C through the hot recycled material drying drum, sieved through a vibrating screen, and weighed according to the mix ratio before entering the main agitator mixing tank;

[0018] Step 2: The recycled coarse aggregate heated at 120°C and the new aggregate heated at 200°C are simultaneously put into the mixing tank of the main mixer and some asphalt is added for pre-coating;

[0019] Step 3: Place 20% to 35% of oil-rich fine aggregate in the cold admixture batching machine, convey it to the cold admixture heater through a belt to preheat it to 80°C, and then lift it to the cold admixture temporary storage bucket through the cold admixture elevator. After being weighed by the cold admixture metering bucket, it enters the recycled material mixer for premixing with the regeneration agent.

[0020] Step 4: After that, all aggregates are weighed in proportion and enter the mixing tank of the main mixer through the chute to mix with the remaining asphalt to complete the mixing process and generate the finished product of recycled asphalt mixture;

[0021] In the present invention, preferably, the factory temperature of the finished recycled asphalt mixture is between 120°C and 180°C.

[0022] In the present invention, preferably, in the first step, when the amount of recycled material added is 50% to 60%, a hot mix method is used, and when it is greater than 60%, a warm mix method is used.

[0023] In the present invention, preferably, the regenerated material is recycled from old asphalt mixture pavement material by milling or mechanical excavation, and finely separated by dust removal, flexible breaking up, primary screening, primary crushing, secondary crushing, deasphalting film, and fine screening process;

[0024] Primary screening produces one kind of fine aggregate, and fine screening produces 3 to 5 kinds of coarse aggregate and one kind of oil-rich fine aggregate.

[0025] A plant-mixed warm and hot recycled asphalt mixture production equipment, the production equipment is used to implement the above-mentioned production process, the production equipment includes a main agitator installed in the equipment building area, a hot recycled material chute, a cold admixture chute, a hot recycled material metering hopper, a hot recycled material temporary storage hopper, a recycled material agitator, a cold admixture metering hopper, a cold admixture temporary storage hopper, a cold admixture elevator, a hot recycled material scraper conveyor, a regeneration agent platform, a hot recycled material elevator 1, a flue gas treatment device, a hot recycled material elevator 2, a cold admixture heater, a combustion hot air system, a hot recycled material drying drum; and a cold admixture batching machine and a hot recycled material batching machine set on the ground;

[0026] The hot recycled material chute and the cold mixed material chute are respectively installed above the main agitator, and the hot recycled material metering hopper and the hot recycled material temporary storage hopper are sequentially installed above the hot recycled material chute, and the recycled material agitator, the cold mixed material metering hopper and the cold mixed material temporary storage hopper are sequentially installed above the cold mixed material chute;

[0027] The cold admixture batching machine conveys the material to the cold admixture heater through a conveyor belt, and the cold admixture heater conveys the material to the cold admixture temporary storage bucket through a cold admixture elevator, and the regeneration agent in the regeneration agent platform is added to the regeneration material agitator through an adding system;

[0028] The hot recycled material drying drum is arranged between the hot recycled material elevator 2 and the hot recycled material elevator 1. The hot recycled material drying drum relies on the combustion hot air system for temperature control, and the outlet of the hot recycled material elevator 1 is arranged at the inlet of the hot recycled material scraper conveyor. The material of the hot recycled material batching machine is transported to the hot recycled material elevator 2 through the conveyor belt.

[0029] A plant-mixed warm and hot recycled asphalt mixture production system, the system comprising a sensor module, a logic control module, and an actuator module;

[0030] Sensor module, used to monitor the temperature data of cold admixture heater and hot recycled material drying drum in real time;

[0031] A logic control module is used to receive temperature data and pressure data, perform real-time analysis and processing, and obtain a heating signaling group and a corresponding number of heating units; wherein the heating signaling group includes a low-power heating signaling, a conventional heating signaling, and a high-power heating signaling;

[0032] An actuator module, used for dynamically controlling and adjusting the heating units on the cold admixture heater according to the generated heating signal and the corresponding number of heating units, so as to achieve the desired heating effect;

[0033] In the present invention, preferably, the temperature data and pressure data are received and analyzed and processed in real time, specifically:

[0034] The cold-mixed material heater includes several heating units; the heating temperature of the heating unit is obtained, and the heating temperature of all the heating units is averaged to obtain the heating mean value; the temperature monitoring time zone is set, and the heating mean value at any collection time in the temperature monitoring time zone is preprocessed; the preprocessing includes the calculation of the mean, variance, and range; the preprocessed value is normalized to obtain the heating value;

[0035] Obtain the temperature at a set position in the hot recycled material drying drum, and pre-process the temperature at any collection time in the temperature monitoring time zone; perform normalization calculation on the pre-processed value to obtain the drum temperature value JW2;

[0036] Perform weighted calculation on the heating value and the barrel temperature value to obtain the temperature adjustment value; obtain the set preheating temperature threshold group of the material; compare the temperature adjustment value with any threshold in the preheating temperature threshold group to obtain the heating signaling group;

[0037] Calculate the heat energy required to heat the material from its current temperature to the desired temperature, obtain the material's mass flow rate, specific heat capacity, and temperature change, using the formula: ; Where Q represents the required heat energy, m represents the mass flow rate of the material, and c represents the specific heat capacity. Indicates the difference between the current temperature and the required temperature; adjust the required heat load according to the actual efficiency, the formula is expressed as: , and the required total power P is obtained; where η is the thermal efficiency of the heater;

[0038] Get the rated power p of any heating unit in the cold admixture heater; calculate based on the rated power and total power, using the formula , the number of heating units that need to be turned on is determined as ni; wherein k represents the weight coefficient of the corresponding heating signal in the heating signaling group, and i represents the number of the low-power heating signaling, the conventional heating signaling, and the high-power heating signaling, which is represented by i=1, 2 or 3.

[0039] Preferably in the present invention, the system further comprises a communication module, a user access module, and a data storage module;

[0040] A data storage module, used to store temperature data and heating signaling of a cold admixture heater and a hot recycled material drying drum and the corresponding number of heating units;

[0041] A user access module, used to access the information stored in the data storage module;

[0042] The communication module is used to realize data synchronization among the sensor module, the logic control module and the actuator module.

[0043] Compared with the prior art, the present invention provides a production process, equipment and system for plant-mixed warm and hot recycled asphalt mixture, which has the following beneficial effects:

[0044] The present invention ensures that the discharge temperature and performance of the asphalt mixture meet the technical requirements by controlling the admixture amount at 15% to 35% and combining a variety of admixture methods. The preheating and regeneration strategy of oil-rich fine aggregate is used to improve the application efficiency of the recycled material, which can save the amount of sand and gravel materials, save asphalt resources, and reduce carbon emissions and harmful gas emissions during mixing, paving, and rolling, thereby reducing carbon emissions and harmful gas emissions during the construction process and promoting environmental protection and resource conservation.

[0045] The present invention uses a production system to carefully analyze and process the temperatures of the cold-additive heater and the hot-recycled material drying drum, dynamically adjusts the operating status and quantity of the heating units according to real-time data, improves energy utilization efficiency, avoids energy waste, and achieves precise control of the heating process, ensuring that the temperature is always within an appropriate range, which helps to improve product quality. BRIEF DESCRIPTION OF THE DRAWINGS

[0046] Figure 1 This is a structural schematic diagram of a plant-mixed warm and hot recycled asphalt mixture production equipment proposed by the present invention.

[0047] Figure 2 This is a side structural schematic diagram of a plant-mixed warm and hot recycled asphalt mixture production equipment proposed by the present invention.

[0048] Figure 3 This is a principle block diagram of a plant-mixed warm and hot recycled asphalt mixture production system proposed by the present invention.

[0049] In the figure: 1. Equipment building frame; 2. Main agitator; 3. Hot recycled material chute; 4. Cold mixed material chute; 5. Hot recycled material metering hopper; 6. Hot recycled material temporary storage hopper; 7. Recycled material agitator; 8. Cold mixed material metering hopper; 9. Cold mixed material temporary storage hopper; 10. Cold mixed material elevator; 11. Hot recycled material scraper conveyor; 12. Regeneration agent platform; 13. Hot recycled material elevator 1; 14. Flue gas treatment equipment; 15. Hot recycled material elevator 2; 16. Cold mixed material batching machine; 17. Cold mixed material heater; 18. Combustion hot air system; 19. Hot recycled material batching machine; 20. Hot recycled material drying drum. DETAILED DESCRIPTION

[0050] Embodiments of the present invention are described in detail below, examples of which are shown in the accompanying drawings, wherein the same or similar reference numerals throughout represent the same or similar elements or elements having the same or similar functions. The embodiments described below with reference to the accompanying drawings are exemplary and are only used to explain the present invention, and cannot be understood as limiting the present invention.

[0051] Embodiment 1: A process for producing warm and hot recycled asphalt mixture in a factory, comprising: feeding 10% to 50% recycled coarse aggregate into a hot recycled material drying drum 20 simultaneously with new aggregate through a cold material bin, heating the mixture to 200°C, screening the mixture through a vibrating screen, weighing the mixture according to the mix ratio, and then feeding the mixture into the mixing cylinder of the main agitator 2; feeding 20% ​​to 35% recycled fine aggregate into the mixing cylinder of the recycled material agitator 7 through an existing hot regeneration system by cold addition, mixing the mixture with a regeneration agent, and then feeding the mixture into the mixing cylinder of the main agitator 2; mixing the mixture dry-mixing for a certain period of time, and then mixing the mixture with an asphalt binder to form a finished product.

[0052] Furthermore, 20% to 35% of the oil-rich fine aggregate is placed in the cold admixture batching machine 16, conveyed to the cold admixture elevator 10 through a belt, lifted to the cold admixture temporary storage bucket 9, weighed by the cold admixture metering bucket 8, and conveyed to the mixer 2 mixing cylinder through the cold admixture chute 4; 10% to 50% of the recycled coarse aggregate passes through the hot recycled cold material bin into the hot recycled material drying drum 20 and is heated to 200°C, and then weighed and enters the main mixer 2 mixing cylinder; after dry mixing for a certain period of time, it is mixed with the asphalt binder to form a finished product.

[0053] The recycled asphalt concrete mixing process adopts the mixing method of existing factory-mixed hot recycling equipment, with the total mixing ratio of recycled materials being 25% to 40%, and the factory temperature of the finished recycled asphalt mixture being between 140°C and 180°C. It is suitable for various mixture types and layers.

[0054] Technical indicators of AC-16 asphalt mixture corresponding to Example 1

[0055]

[0056] Embodiment 2: A process for producing factory-mixed warm and hot recycled asphalt mixture, comprising heating 30% to 50% recycled coarse aggregate to above 120°C in a hot recycled material drying drum 20, preheating 20% ​​to 30% recycled fine aggregate to 80°C and mixing with new aggregate, and adopting a hot mix method when the amount of recycled material added is 50% to 60%, and a warm mix method when it is greater than 60%.

[0057] 30% to 50% of the recycled coarse aggregate is sent to the hot recycled material drying drum 20 with countercurrent heating through the hot recycled material batching machine 19 via a belt conveyor, heated to above 120°C in the hot recycled material drying drum 20, lifted to the hot recycled material scraper conveyor 11 via a hot recycled material elevator 13, and transported to the hot recycled material temporary storage bucket 6 via the hot recycled material scraper conveyor 11, and then enters the mixing cylinder of the main agitator 2 through a chute after being weighed by a weighing system according to the mix ratio.

[0058] 20% to 30% of oil-rich fine aggregate is placed in a cold admixture batching machine 16, conveyed by a belt to a cold admixture heater 17 to be preheated to 80°C, and then lifted to a cold recycled material temporary storage bucket 9 by a cold recycled material elevator 10, weighed by a cold recycled material metering bucket 8, and then conveyed to a mixing cylinder of a mixer 2.

[0059] 20% to 50% of new aggregate is heated to 200°C by hot recycled material drying drum 20, sieved by a vibrating screen, weighed according to the mix ratio and then enters the mixing tank of the main mixer 2.

[0060] The hot recycled coarse aggregate, warm recycled oil-rich fine aggregate and new aggregate are mixed with the asphalt binder in the mixing cylinder of the agitator 2 for a certain period of time. The factory temperature of the finished recycled asphalt mixture is between 140℃ and 180℃.

[0061] On the basis of Example 1, the hot recycled material drying drum 20 is used to heat the recycled coarse aggregate separately and then add it. The total blending ratio of the recycled material reaches 50% to 80%. The recycled fine aggregate is preheated and added through a special adding system, and the performance of the asphalt mixture is further improved.

[0062] Technical indicators of AC-16 asphalt mixture corresponding to Example 2

[0063]

[0064] Embodiment 3: A process for producing warm and hot recycled asphalt mixture in a factory, comprising feeding 30% to 50% recycled coarse aggregate through a hot recycled material batching machine 19 via a belt conveyor into a countercurrent heated hot recycled material drying drum 20, heating the hot recycled material drying drum 20 to above 120°C, heating new aggregate through a hot recycled material drying drum 2 to 200°C, screening through a vibrating screen, and entering the mixing cylinder of the main agitator 2 after being weighed according to the mix ratio.

[0065] The recycled coarse aggregate heated at 120°C and the new aggregate heated at 200°C are synchronously fed into the mixing cylinder of the main mixer 2 and part of asphalt is added for pre-coating. At the same time, 20% to 30% of the oil-rich fine aggregate is placed in the cold admixture batching machine 16, conveyed by a belt to the cold admixture heater 17 for preheating to 80°C, and then lifted to the cold admixture temporary storage bucket 9 by the cold admixture elevator 10. After being weighed by the cold admixture metering bucket 8, they enter the recycled material mixer 7 for pre-mixing with the regeneration agent. The regeneration agent is added to the cold recycled material mixer 7 through the adding system.

[0066] After that, all aggregates are weighed in proportion and enter the mixing cylinder of the main mixer 2 through the chute to mix with the remaining asphalt to complete the mixing process. The factory temperature of the finished recycled asphalt mixture is between 120℃ and 180℃.

[0067] On the basis of the recycled asphalt concrete mixing process of Example 2, the pre-coating of coarse aggregate and the pre-mixing process of recycled fine aggregate and regeneration agent are added to further improve the performance of the asphalt mixture, and the total blending ratio of recycled materials reaches 50% to 100%.

[0068] refer to Figure 1-2, a kind of plant-mixed warm and hot recycled asphalt mixture production equipment, including a mixer 2, a hot recycled material chute 3, a cold admixture chute 4, a hot recycled material metering hopper 5, a hot recycled material temporary storage hopper 6, a recycled material mixer 7, a cold admixture metering hopper 8, a cold admixture temporary storage hopper 9, a cold admixture elevator 10, a hot recycled material scraper conveyor 11, a regeneration agent platform 12, a hot recycled material elevator 13, a flue gas treatment device 14, a hot recycled material elevator 2 15, a cold admixture heater 17, a combustion hot air system 18, and a hot recycled material drying drum 20 installed in the equipment building frame 1 area; and a cold admixture batching machine 16 and a hot recycled material batching machine 19 arranged on the ground;

[0069] The hot recycled material chute 3 and the cold mixed material chute 4 are respectively installed above the agitator 2, and the hot recycled material metering hopper 5 and the hot recycled material temporary storage hopper 4 are sequentially installed above the hot recycled material chute 3, and the recycled material agitator 7, the cold mixed material metering hopper 8, and the cold mixed material temporary storage hopper 9 are sequentially installed above the cold recycled material chute 4;

[0070] The material of the cold admixture batching machine 16 is transported to the cold production false material heater 17 through the conveyor belt, and the cold production false material heater 17 transports the material to the cold admixture temporary storage bucket 9 through the cold admixture elevator 10, and the regeneration agent in the regeneration agent platform 12 is added to the regeneration material mixer 7 through the adding system;

[0071] The hot recycled material drying drum 20 is arranged between the hot recycled material elevator 2 15 and the hot recycled material elevator 1 13. The hot recycled material drying drum 20 relies on the combustion hot air system 18 for temperature control, and the outlet of the hot recycled material elevator 13 is arranged at the inlet of the hot recycled material scraper conveyor 11. The hot recycled material batching machine 19 transports the materials to the hot recycled material elevator 2 15 through the conveyor belt.

[0072] Example 3 Corresponding AC-16 asphalt mixture technical indicators

[0073]

[0074] Example 4: Reference Figure 3 , a plant-mixed warm and hot recycled asphalt mixture production system, including a sensor module, a logic control module, and an actuator module;

[0075] The sensor module is used to monitor the temperature data of the cold admixture heater 17 and the hot recycled material drying drum 20 in real time;

[0076] The logic control module is used to receive temperature data and pressure data and perform real-time analysis and processing, specifically:

[0077] The cold additive heater 17 includes several heating units; the heating temperature of the heating unit is obtained, and the heating temperature of all the heating units is averaged to obtain the heating mean; the temperature monitoring time zone is set, and the heating mean at any collection time in the temperature monitoring time zone is preprocessed; the preprocessing includes the calculation of the mean, variance, and range; the preprocessed value is normalized to obtain the heating value JW1;

[0078] Obtain the temperature at a set position in the hot recycled material drying drum 20, and pre-process the temperature at any collection time in the temperature monitoring time zone; perform normalization calculation on the pre-processed value to obtain the drum temperature value JW2;

[0079] The heating value and the barrel temperature value are weighted and calculated, and the temperature adjustment value JW is obtained using the formula JW=JW1×w1+JW2×w2; wherein w1 and w2 represent the weights of the heating value and the barrel temperature value respectively; the set preheating temperature threshold group of the material is obtained, including thresholds Ja, Jb, and Jc; the temperature adjustment value is compared with any threshold in the preheating temperature threshold group, specifically:

[0080] If 0≤JW<Ja, a low-power heating signal is generated;

[0081] If Ja≤JW<Jb, generate conventional heating signaling;

[0082] If Jb≤JW<Jc, a high-power heating signal is generated;

[0083] Marking low-power heating signaling, conventional heating signaling, and high-power heating signaling as a heating signaling group;

[0084] Calculate the heat energy required to heat the material from its current temperature to the desired temperature, obtain the material's mass flow rate, specific heat capacity, and temperature change, using the formula: ; Where Q represents the required heat energy, m represents the mass flow rate of the material, and c represents the specific heat capacity. Indicates the difference between the current temperature and the required temperature; adjust the required heat load according to the actual efficiency, the formula is expressed as: , and the required total power P is obtained; where η is the thermal efficiency of the heater;

[0085] Obtain the rated power p of any heating unit in the cold admixture heater 17; calculate based on the rated power and total power, using the formula , the number of heating units that need to be turned on is determined to be ni; wherein k represents the weight coefficient of the corresponding heating signal in the heating signal group, and i represents the number of the low-power heating signal, the conventional heating signal, and the high-power heating signal, which is represented by i=1, 2 or 3;

[0086] The actuator module is used to dynamically control and adjust the heating units on the cold admixture heater 17 according to the generated heating signal and the corresponding number of heating units to achieve the desired heating effect.

[0087] The present invention also includes a communication module, a user access module, and a data storage module;

[0088] A data storage module, used to store temperature data and heating signaling of the cold admixture heater 17 and the hot regenerated material drying drum 20 and the corresponding number of heating units;

[0089] A user access module, used to access the information stored in the data storage module;

[0090] The communication module is used to realize data synchronization among the sensor module, the logic control module and the actuator module.

[0091] Table 1 and Table 2 of RAP aggregate refinement (primitive) technical indicators provided in Examples 1-4

[0092] Table 1 RAP recycled aggregate specifications (after extraction)

[0093]

[0094] Table 2 Technical indicators of RAP aggregate regeneration

[0095]

[0096] The above are only preferred specific implementation modes of the present invention, but the protection scope of the present invention is not limited thereto. Any technician familiar with the technical field can make equivalent replacements or changes according to the technical solutions and inventive concepts of the present invention within the technical scope disclosed by the present invention, which should be covered by the protection scope of the present invention.

Claims

1. A plant-mixed warm and hot recycled asphalt mixture production system, characterized in that: The system is used for plant-mixed warm and hot recycled asphalt mixture production equipment, the production equipment comprising a main agitator (2) installed in the equipment building frame (1) area, a hot recycled material chute (3), a cold recycled material chute (4), a hot recycled material metering hopper (5), a hot recycled material temporary storage hopper (6), a cold recycled material agitator (7), a cold admixture metering hopper (8), a cold admixture temporary storage hopper (9), a cold recycled material elevator (10), a hot recycled material scraper conveyor (11), a regeneration agent platform (12), a hot recycled material elevator 1 (13), a flue gas treatment device (14), a hot recycled material elevator 2 (15), a cold admixture heater (17), a combustion hot air system (18), a hot recycled material drying drum (20); and a cold admixture batching machine (16) and a hot recycled material batching machine (19) arranged on the ground; The hot recycled material chute (3) and the cold recycled material chute (4) are respectively installed above the main agitator (2), and the hot recycled material metering hopper (5) and the hot recycled material temporary storage hopper (6) are installed in sequence above the hot recycled material chute (3), and the cold recycled material agitator (7), the cold admixture metering hopper (8), and the cold admixture temporary storage hopper (9) are installed in sequence above the cold recycled material chute (4); The material of the cold admixture batching machine (16) is transported to the cold admixture heater (17) via a conveyor belt, and the cold admixture heater (17) transports the material to the cold admixture temporary storage bucket (9) via a cold recycled material elevator (10), and the regeneration agent in the regeneration agent platform (12) is added to the cold recycled material agitator (7) via an adding system; The hot regenerated material drying drum (20) is arranged between the hot regenerated material elevator 2 (15) and the hot regenerated material elevator 1 (13), the hot regenerated material drying drum (20) relies on the combustion hot air system (18) for temperature control, and the outlet of the hot regenerated material elevator 1 (13) is arranged at the inlet of the hot regenerated material scraper conveyor (11), the hot regenerated material batching machine (19) conveys the material to the hot regenerated material elevator 2 (15) through a conveyor belt, and the cold admixture heater (17) includes a plurality of heating units; The system includes a sensor module, a logic control module, and an actuator module; The sensor module is used to monitor the temperature data of the cold admixture heater (17) and the hot recycled material drying drum (20) in real time; The logic control module is used to receive temperature data and pressure data, perform real-time analysis and processing, and obtain a heating signaling group and a corresponding number of heating units; wherein the heating signaling group includes a low-power heating signaling, a conventional heating signaling, and a high-power heating signaling; The actuator module is used to dynamically control and adjust the heating units on the cold admixture heater (17) according to the generated heating signal and the corresponding number of heating units to achieve the desired heating effect; The logic control module receives temperature data and pressure data and performs real-time analysis and processing, specifically: Obtain the heating temperature of the heating unit, calculate the average of the heating temperatures of all heating units to obtain the heating mean; set the temperature monitoring time zone, and preprocess the heating mean at any collection time in the temperature monitoring time zone; the preprocessing includes the calculation of the mean, variance, and range; The pre-processed value is normalized and calculated to obtain the heating value JW1; Acquiring the temperature at a set position in the hot recycled material drying drum (20), and pre-processing the temperature at any sampling time in the temperature monitoring time zone; The pre-processed value is normalized and calculated to obtain the barrel temperature value JW2; The heating value and the barrel temperature value are weighted and calculated, and the temperature adjustment value JW is obtained using the formula JW=JW1×w1+JW2×w2; wherein w1 and w2 represent the weights of the heating value and the barrel temperature value respectively; the set preheating temperature threshold group of the material is obtained, including thresholds Ja, Jb, and Jc; the temperature adjustment value is compared with any threshold in the preheating temperature threshold group, specifically: If 0≤JW<Ja, a low-power heating signal is generated; If Ja≤JW<Jb, generate conventional heating signaling; If Jb≤JW<Jc, a high-power heating signal is generated; Marking low-power heating signaling, conventional heating signaling, and high-power heating signaling as a heating signaling group; Using the formula: ; Calculate the heat energy required to heat the material from the current temperature to the required temperature, obtain the mass flow rate, specific heat capacity and temperature change of the material, where Q represents the required heat energy, m represents the mass flow rate of the material, and c represents the specific heat capacity. Indicates the difference between the current temperature and the required temperature; adjust the required heat load according to the actual efficiency, the formula is expressed as: , and the required total power P is obtained; where η is the thermal efficiency of the heater; Obtain the rated power p of any heating unit in the cold admixture heater (17); calculate based on the rated power and the total power, using the formula , the number of heating units that need to be turned on is determined as ni; wherein k represents the weight coefficient of the corresponding heating signal in the heating signaling group, and i represents the number of the low-power heating signaling, the conventional heating signaling, and the high-power heating signaling, which is represented by i=1, 2 or 3.

2. A plant-mixed warm and hot recycled asphalt mixture production system according to claim 1, characterized in that: The system also includes a communication module, a user access module, and a data storage module; The data storage module is used to store temperature data and heating signaling of the cold admixture heater (17) and the hot regenerated material drying drum (20) and the corresponding number of heating units; The user access module is used to access the information stored in the data storage module; The communication module is used to achieve data synchronization among the sensor module, the logic control module and the actuator module.

3. A process for producing warm and hot recycled asphalt mixture in a factory, characterized in that: The production process is implemented using the plant-mixed warm and hot recycled asphalt mixture production system according to claim 2, and the process includes the following steps: 30% to 50% of the recycled coarse aggregate is heated to above 120°C in a hot recycled material drying drum (20), and 20% to 30% of the recycled oil-rich fine aggregate is preheated to 80°C and mixed with the new aggregate; 30% to 50% of the recycled coarse aggregate is sent to a hot recycled material drying drum (20) heated by countercurrent heating through a hot recycled material batching machine (19) and a belt conveyor, and is heated to above 120° C. in the hot recycled material drying drum (20), and is lifted to a hot recycled material scraper conveyor (11) through a hot recycled material elevator (13), and is conveyed to a hot recycled material temporary storage hopper (6) through the hot recycled material scraper conveyor (11), and is weighed according to the mixing ratio through a weighing system and then enters the mixing tank of the main agitator (2) through a chute; 20% to 30% of the recycled oil-rich fine aggregate is placed in a cold admixture batching machine (16), conveyed by a belt to a cold admixture heater (17) to be preheated to 80° C., and then lifted to a cold recycled material cold admixture temporary storage hopper (9) via a cold recycled material elevator (10), weighed by a cold admixture metering hopper (8), and then conveyed to a recycled material agitator (7) and into a mixing tank of a main agitator (2); 20% to 50% of new aggregate is heated to 200° C. by a hot recycled material drying drum (20), sieved by a vibrating screen, weighed according to the mix ratio, and then enters the mixing tank of the main mixer (2); The hot recycled coarse aggregate, the warm recycled oil-rich fine aggregate and the new aggregate are stirred in the mixing tank of the main mixer (2) for a certain period of time and then stirred with the asphalt binder to produce a recycled asphalt mixture product; When the amount of recycled material added is between 50% and 60%, the hot mix method is used; when it is greater than 60%, the warm mix method is used.

4. A process for producing warm and hot recycled asphalt mixture in a factory, characterized in that: The production process is implemented using the plant-mixed warm and hot recycled asphalt mixture production system described in claim 2, and the process includes the following steps: 30% to 50% of the recycled coarse aggregate is sent to a hot recycled material drying drum (20) with countercurrent heating via a hot recycled material batching machine (19) and a belt conveyor, and is heated to above 120° C. in the hot recycled material drying drum (20). The new aggregate is heated to 200° C. via the hot recycled material drying drum (20), sieved through a vibrating screen, and weighed according to the mixing ratio before entering the mixing tank of the main agitator (2); The recycled coarse aggregate heated at 120°C and the new aggregate heated at 200°C are simultaneously fed into the mixing tank of the main mixer (2) and part of the asphalt is added for pre-coating; 20% to 30% of the recycled oil-rich fine aggregate is placed in a cold admixture batching machine (16), conveyed to a cold admixture heater (17) by a belt to be preheated to 80° C., lifted to a cold admixture temporary storage hopper (9) by an elevator (10), weighed by a cold admixture metering hopper (8), and then entered into a recycled material mixer (7) for premixing with a regeneration agent; Then, all aggregates are weighed in proportion and enter the main mixer (2) through the chute to be mixed with the remaining asphalt binder to complete the mixing process and generate the finished product of recycled asphalt mixture; When the amount of recycled material added is between 50% and 60%, the hot mix method is used; when it is greater than 60%, the warm mix method is used.

5. A process for producing warm and hot recycled asphalt mixture in a factory according to claim 3 or 4, characterized in that: The recycled material is the old asphalt mixture pavement material that is recycled by milling or mechanical excavation, and finely separated by dust removal, flexible breaking up, primary screening, primary crushing, secondary crushing, deasphalting, and fine screening processes; Primary screening produces one kind of fine aggregate, and fine screening produces 3 to 5 kinds of coarse aggregate and one kind of oil-rich fine aggregate.

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