WO2021248925A1 - High-reference hot mix plant recycling device - Google Patents

High-reference hot mix plant recycling device Download PDF

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WO2021248925A1
WO2021248925A1 PCT/CN2021/075415 CN2021075415W WO2021248925A1 WO 2021248925 A1 WO2021248925 A1 WO 2021248925A1 CN 2021075415 W CN2021075415 W CN 2021075415W WO 2021248925 A1 WO2021248925 A1 WO 2021248925A1
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drying drum
regeneration
aggregate
fine
hot
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PCT/CN2021/075415
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French (fr)
Chinese (zh)
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高国强
潘泽源
王俊峰
马昆斌
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福建省铁拓机械股份有限公司
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    • EFIXED CONSTRUCTIONS
    • E01CONSTRUCTION OF ROADS, RAILWAYS, OR BRIDGES
    • E01CCONSTRUCTION OF, OR SURFACES FOR, ROADS, SPORTS GROUNDS, OR THE LIKE; MACHINES OR AUXILIARY TOOLS FOR CONSTRUCTION OR REPAIR
    • E01C19/00Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving
    • E01C19/02Machines, tools or auxiliary devices for preparing or distributing paving materials, for working the placed materials, or for forming, consolidating, or finishing the paving for preparing the materials
    • E01C19/10Apparatus or plants for premixing or precoating aggregate or fillers with non-hydraulic binders, e.g. with bitumen, with resins, i.e. producing mixtures or coating aggregates otherwise than by penetrating or surface dressing; Apparatus for premixing non-hydraulic mixtures prior to placing or for reconditioning salvaged non-hydraulic compositions
    • E01C19/1004Reconditioning or reprocessing bituminous mixtures, e.g. salvaged paving, fresh patching mixtures grown unserviceable; Recycling salvaged bituminous mixtures; Apparatus for the in-plant recycling thereof
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/02Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity

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  • the invention relates to the technical field of asphalt mixture thermal regeneration equipment, in particular to a high-reference plant-mix thermal regeneration equipment.
  • Asphalt mixture thermal regeneration technology is a technology for recycling waste asphalt mixtures.
  • various grades of cold waste asphalt mixtures are simultaneously sent to the drying and heating system for drying. After dry heating treatment, it is mixed with a certain proportion of new aggregate, asphalt, mineral powder, etc. to finally produce a qualified asphalt mixture finished material.
  • this method of plant-mix thermal regeneration currently has the following problems:
  • the coarse and fine materials in the waste asphalt mixture enter the drying drum for heating at the same time. It is difficult to ensure the uniformity of the heating of the coarse and fine materials. Under the same environment, the fine aggregate is more likely to be heated than the coarse aggregate, so it is very easy to cause the fine material to be heated.
  • the extremely high temperature during the heating process causes serious aging of the asphalt on the surface of the fine material; because the asphalt content in the fine material accounts for a large proportion of the waste asphalt mixture, once the asphalt of the fine material has aging problems, it will greatly reduce the waste asphalt mixture. The quality of the material ultimately affects the quality of the finished material.
  • the fine materials in the waste asphalt mixture are directly put into the mixing tank.
  • This method has the following shortcomings.
  • the fine materials are directly put into the mixing tank without being dried and heated and mixed with high-temperature virgin materials or recycled materials. , It will produce a lot of water vapor instantly, causing the negative pressure pipeline of the original equipment to be very easy to block, and it is very easy to cause the positive pressure in the mixing tank to be instantaneously, causing the soft connection part of the original equipment to fall off, and finally resulting in a large amount of dust and asphalt smoke. Pollution of the environment, threatening the safety of operators; and the amount of fine materials added is very limited. If a large amount of fine materials that have not been dried and heated are added to the mixing tank, the quality of the finished materials will be affected;
  • the present invention provides a high-reference plant mixing heat regeneration equipment, which has simple operation, good effect, practicality, compact structure, energy saving and environmental protection, and convenient installation and maintenance.
  • the main technical solutions adopted by the present invention include:
  • a high-reference plant mixing heat regeneration equipment comprising a first regeneration drying drum, a second regeneration drying drum and a hot air furnace arranged at intervals, the first regeneration drying drum and the second regeneration drying drum are The first discharging box and the second discharging box are respectively communicated with the first air outlet pipe and the second air outlet pipe of the hot blast furnace;
  • the feed ends of the first regenerative drying drum and the second regenerative drying drum are connected with a first-stage sedimentation chamber, and the first-stage sedimentation chamber is connected with a tail gas treatment pipeline, and the tail gas treatment pipeline is connected to the hot blast furnace through a return air pipe
  • a return air blower is connected between the tail gas processing pipeline and the return air pipe;
  • a secondary settling chamber is connected to the tail gas processing pipeline;
  • the heat required to dry the coarse aggregate and the fine aggregate is generated by the burner and transferred through the hot blast furnace.
  • a part of the hot gas directly enters the first regeneration drying drum through the first air outlet pipe to exchange heat with the coarse aggregate.
  • Another part of the hot air can enter the second regeneration drying drum through the second air outlet pipe to exchange heat with the fine aggregate;
  • the exhaust gas treatment pipeline and the secondary sedimentation chamber After the exhaust gas generated by the first regeneration drying drum and the second regeneration drying drum is processed by the primary sedimentation chamber, the exhaust gas treatment pipeline and the secondary sedimentation chamber, a part of the exhaust gas is sent to the original drying drum through the exhaust fan. After the secondary combustion process, the other part enters the hot blast furnace through the return air pipe and mixes with the flame of the burner to generate hot air to provide heat to the first regeneration drying drum and the second regeneration drying drum;
  • the recycled coarse aggregate and fine aggregate are separately dried and heated by the first regeneration drying drum and the second regeneration drying drum.
  • the heated coarse aggregate is stored in the first hot material temporary storage bin through the first discharge box.
  • the heated fine aggregate is stored in the second hot material temporary storage bin through the second discharge box.
  • the coarse aggregate and the fine aggregate can be weighed in the regeneration weighing scale.
  • the feeding end of the first regeneration drying drum is connected to the discharge end of the recycled coarse aggregate hoist; the feeding end of the recycled coarse aggregate hoist is connected to the belt conveyor of the recycled coarse aggregate.
  • the discharge end is connected; the feeding end of the recycled coarse aggregate belt conveyor is matched with the recycled coarse aggregate silo.
  • the feed end of the second regeneration drying drum is communicated with the discharge end of the regeneration fine aggregate hoist; the feed end of the regeneration fine aggregate hoist is connected to the belt conveyor of the regeneration fine aggregate.
  • the discharge end is connected; the feeding end of the recycled fine aggregate belt conveyor is matched with the recycled fine aggregate silo.
  • first air outlet pipe and/or the second air outlet pipe are provided with a regulating air door.
  • the secondary settling chamber is communicated with the feed end of the recycled fine aggregate hoist through a recycled powder pipeline.
  • the beneficial effects of the present invention are as follows: 1.
  • the coarse and fine materials can be separately heated, and the coarse and fine materials are dried and heated by independent regeneration drying drums. It is easier to control the temperature of the coarse and fine materials, especially the control of the fine materials, and the regeneration is controlled by frequency conversion.
  • the rotation speed of the drying drum can be selected to control the amount of fine aggregate addition, and the size of the air door can be adjusted in coordination to effectively ensure the discharge temperature of the fine aggregate.
  • the coarse and fine materials can be controlled by double drums. Separate heating can effectively control the discharge temperature of the recycled coarse material and the recycled fine material, thereby effectively increasing the output of the recycled material and realizing the high reference of the recycled material. 2.
  • the fine materials filtered and settled in the primary sedimentation chamber and secondary sedimentation chamber can be recycled and reused to reduce the external discharge of solid particles, thereby reducing environmental pollution; 3.
  • By measuring the coarse and fine materials separately it can greatly Improve the grading accuracy of coarse and fine materials, especially to meet the gradation control requirements of fine aggregates, thereby ensuring the grading requirements of finished materials; 4.
  • the added function is integrated into the existing plant mixing heat regeneration equipment, with compact structure, installation and maintenance convenient.
  • Figure 1 is a schematic diagram of the structure of the present invention.
  • a high-reference plant mixing heat regeneration equipment as shown in Figure 1, includes a first regeneration drying drum 1 and a second regeneration drying drum 2 arranged at intervals, and the feed of the first regeneration drying drum 1
  • the end is connected with the discharge end of the recycled coarse aggregate elevator 3; the feed end of the recycled coarse aggregate elevator 3 is connected with the discharge end of the recycled coarse aggregate belt conveyor 4;
  • the feed end of the belt conveyor 4 is matched with the recycled coarse aggregate silo 5;
  • the feed end of the second regeneration drying drum 2 is connected to the discharge end of the recycled fine aggregate elevator 6;
  • the feed end of the recycled fine aggregate hoist 6 is communicated with the discharge end of the recycled fine aggregate belt conveyor 7; the feed end of the recycled fine aggregate belt conveyor 7 is opposite to the recycled fine aggregate silo 8 Cooperate.
  • first discharge box 9 and the second discharge box 10 on the first regeneration drying drum 1 and the second regeneration drying drum 2 are respectively connected to the first outlet pipe 11 and the second outlet pipe 11 of the hot blast furnace 13
  • the air outlet pipe 12 is connected; the hot blast furnace 13 is connected to the burner 15; in order to facilitate the control of the air volume of the hot air, the first air outlet pipe 11 and/or the second air outlet pipe 12 are provided with a regulating air door 14.
  • the first discharge box 9 and the second discharge box 10 are provided with a regenerative weighing scale 16 underneath the regenerative weighing scale 16 is provided with a stirring cylinder 17; in order to facilitate the heat dissipation of the heating material,
  • the first discharging box 9 and the second discharging box 10 are respectively connected with a first hot material temporary storage bin 18 and a second hot material temporary storage bin 19, the first hot material temporary storage bin 18 and the second hot material temporary storage bin 18
  • the discharge end of the material temporary storage bin 19 is connected with the regeneration weighing scale 16.
  • the feed ends of the first regeneration drying drum 1 and the second regeneration drying drum 2 are connected with a primary sedimentation chamber 20, and the primary sedimentation chamber 20 is connected with a tail gas treatment pipeline 21 and a tail gas treatment pipeline 21.
  • the upper part is communicated with the hot blast furnace 13 through a return air pipe 22; a return air blower 23 is connected between the exhaust gas treatment pipeline 21 and the return air pipe 22.
  • the tail gas treatment pipeline 21 contains particulate matter
  • the tail gas treatment pipeline 21 is connected with a secondary settling chamber 24, and the secondary settling chamber 24 is connected to the recycled fine aggregate through the powder recovery pipeline 25 The feeding end of the hoist 6 is connected.
  • a smoke exhaust fan 26 is connected to the exhaust gas treatment pipeline 21, and the exhaust end of the smoke exhaust fan 26 is in communication with the original drying drum.
  • the recycled coarse aggregate and the fine aggregate are separately dried and heated by the first regeneration drying drum 1 and the second regeneration drying drum 2 respectively, and the heated coarse aggregate is stored in the first thermal material temporary storage bin In 18, the heated fine aggregate is stored in the second hot material temporary storage bin 19.
  • the coarse aggregate and the fine aggregate can be weighed in the regenerating weighing scale 16, and finally put in at the same time.
  • the mixing tank 17 is mixed with the raw aggregates and the like, and finally a qualified finished material is formed.
  • the heat required to dry the coarse aggregate and the fine aggregate is generated by the burner 15 and transferred through the hot blast furnace 13, and part of the hot gas directly enters the first regeneration drying drum 1 through the first air outlet pipe 11
  • the internal heat exchange with the coarse aggregate, the other part of the hot air can enter the second regenerative drying drum 2 through the second air outlet pipe 12 to exchange heat with the fine aggregate.
  • the second air outlet pipe 12 is equipped with a regulating air door 14, which can be Control the heat flow entering the second regeneration drying drum 2.
  • the second regeneration drying drum 2 can control the drum speed by frequency conversion, select the appropriate drum speed according to the amount of fine material, and cooperate with the adjusting damper 14 to control the fine material discharge temperature.
  • the exhaust gas treatment pipeline 21 and the secondary sedimentation chamber 24 a part of the exhaust gas passes through the exhaust fan 26.
  • the tail gas is sent into the primary drying drum for secondary combustion treatment, and the other part enters the hot blast furnace 13 through the return air pipe 22 and mixes with the flame of the burner 15 to generate hot air for the first regeneration drying drum 1 and the second regeneration.
  • the drying drum 2 provides heat.
  • the coarse and fine materials can be heated separately, and the coarse and fine materials are dried and heated by independent regeneration drying drums. It is easier to control the temperature of the coarse and fine materials, especially the control of the fine materials.
  • the rotation speed of the regeneration drying drum is controlled by frequency conversion. Therefore, it is possible to select the size of the finer aggregate addition to control the different speeds, and adjust the size of the damper, so as to effectively ensure the discharge temperature of the fine aggregate, and the coarse and fine materials are separately heated by the double rollers, which can be effective Control the discharge temperature of the recycled coarse material and the recycled fine material, thereby effectively increasing the output of the recycled material and realizing the high reference of the recycled material.
  • This embodiment can recycle and reuse the fine materials filtered and settled in the primary sedimentation chamber and secondary sedimentation chamber, reducing the external discharge of solid particles, thereby reducing environmental pollution; by separately measuring the coarse and fine materials, it can greatly improve The grading accuracy of coarse and fine materials, especially to meet the gradation control requirements of fine aggregates, so as to ensure the grading requirements of finished materials; the added function is integrated in the existing plant mixing heat regeneration equipment, with compact structure and convenient installation and maintenance.

Abstract

A high-reference hot mix plant recycling device, comprising a first recycling drying roller (1), a second recycling drying roller (2) and a hot air furnace (13) provided at intervals, the material feeding ends of the first recycling drying roller (1) and the second recycling drying roller (2) being sequentially connected to a primary settling chamber (20) and an exhaust gas treatment pipe (21), and the exhaust gas treatment pipe (21) communicating with the hot air furnace (13) by means of an air return pipe (22); a secondary settling chamber (24) is connected onto the exhaust gas treatment pipe (21); a first material discharging box (9) and a second material discharging box (10) on the first recycling drying roller (1) and the second recycling drying roller (2) communicate with a first air outlet pipe (11) and a second air outlet pipe (12) of the hot air furnace (13), respectively; heat generated by a burner (15) is transferred through the hot air furnace (13), and recycled coarse aggregate and fine aggregate are independently dried and heated by means of the first recycling drying roller (1) and the second recycling drying roller (2), respectively; the heated coarse aggregate is stored in a first hot material temporary storage bin (18) by means of the first material discharging box (9), and the heated fine aggregate is stored in a second hot material temporary storage bin (19) by means of the second material discharging box (10); and after being weighed by means of a recycling metering scale (16) according to grading requirements, the heated coarse and fine aggregates are simultaneously placed into a stirring cylinder (17) for stirring with virgin aggregate, so as to finally form a finished material that is up to standard. The device can control the heating temperature and can prevent aggregate aging.

Description

一种高参比厂拌热再生设备High-reference plant mixing hot regeneration equipment 技术领域Technical field
本发明涉及沥青混合料热再生设备技术领域,尤其涉及一种高参比厂拌热再生设备。The invention relates to the technical field of asphalt mixture thermal regeneration equipment, in particular to a high-reference plant-mix thermal regeneration equipment.
背景技术Background technique
沥青混合料热再生技术是将废旧沥青混合料进行回收利用的一种技术,在现有厂拌热再生技术中,将各种级配的冷废旧沥青混合料同时送入烘干加热系统进行烘干加热处理后,再与一定比例的新骨料、沥青、矿粉等进行拌合,最终生产出合格的沥青混合料成品料。但是这种厂拌热再生方式目前存在以下问题:Asphalt mixture thermal regeneration technology is a technology for recycling waste asphalt mixtures. In the existing plant-mix thermal regeneration technology, various grades of cold waste asphalt mixtures are simultaneously sent to the drying and heating system for drying. After dry heating treatment, it is mixed with a certain proportion of new aggregate, asphalt, mineral powder, etc. to finally produce a qualified asphalt mixture finished material. However, this method of plant-mix thermal regeneration currently has the following problems:
1、废旧沥青混合料中的粗细料同时进入烘干滚筒加热,很难保证粗细料的受热均匀性,在相同的环境下细集料比粗集料更容易受热,所以非常容易导致细料在加热过程中温度超高,导致细料表面的沥青老化严重;由于细料中的沥青含量占废旧沥青混合料的比例较大,一旦细料这部分沥青产生老化问题,则将大大降低废旧沥青混合料的质量,最终影响成品料的质量。1. The coarse and fine materials in the waste asphalt mixture enter the drying drum for heating at the same time. It is difficult to ensure the uniformity of the heating of the coarse and fine materials. Under the same environment, the fine aggregate is more likely to be heated than the coarse aggregate, so it is very easy to cause the fine material to be heated. The extremely high temperature during the heating process causes serious aging of the asphalt on the surface of the fine material; because the asphalt content in the fine material accounts for a large proportion of the waste asphalt mixture, once the asphalt of the fine material has aging problems, it will greatly reduce the waste asphalt mixture. The quality of the material ultimately affects the quality of the finished material.
2、有废旧沥青混合料中的细料有通过直接投入搅拌缸的方式,这种方式存在以下缺点,细料未经过烘干加热直接投入到搅拌缸中与高温原生料或再生料进行混合搅拌,会瞬间产生大量水蒸气,导致原生设备负压管路非常容易堵,极易导致搅拌缸内瞬间产生正压,致使原生设备软连接部分脱落,最终导致大量粉尘,沥青烟气冒出,严重污染环境,危机操作人员安全;且细料添加量非常有限,如果将大量未经烘干加热的细料加入搅拌缸,将会影响成品料质量;2. The fine materials in the waste asphalt mixture are directly put into the mixing tank. This method has the following shortcomings. The fine materials are directly put into the mixing tank without being dried and heated and mixed with high-temperature virgin materials or recycled materials. , It will produce a lot of water vapor instantly, causing the negative pressure pipeline of the original equipment to be very easy to block, and it is very easy to cause the positive pressure in the mixing tank to be instantaneously, causing the soft connection part of the original equipment to fall off, and finally resulting in a large amount of dust and asphalt smoke. Pollution of the environment, threatening the safety of operators; and the amount of fine materials added is very limited. If a large amount of fine materials that have not been dried and heated are added to the mixing tank, the quality of the finished materials will be affected;
3、有通过一段可实现预热功能的输送装置(如螺旋输送等)将细料投入搅拌缸的方式,这种方式虽可有效的缓解冷料直接投入搅拌缸所产生的问题,但由于螺旋输送装置空间小,细料在内部不易形成热交换, 所以这种方式无法实现较高产量的细料添加,从而无法实现再生料高参比功能。3. There is a way to put fine materials into the mixing tank through a conveying device (such as screw conveying, etc.) that can realize the preheating function. Although this method can effectively alleviate the problems caused by the direct input of cold materials into the mixing tank, because of the screw The space of the conveying device is small, and the fine material is not easy to form heat exchange inside, so this method cannot realize the fine material addition with a higher output, and thus cannot realize the high reference function of the recycled material.
发明内容Summary of the invention
(一)要解决的技术问题(1) Technical problems to be solved
为了解决现有技术的上述问题,本发明提供一种一种高参比厂拌热再生设备,其操作简单,效果好,实用,结构紧凑,节能环保,安装维护方便。In order to solve the above-mentioned problems of the prior art, the present invention provides a high-reference plant mixing heat regeneration equipment, which has simple operation, good effect, practicality, compact structure, energy saving and environmental protection, and convenient installation and maintenance.
(二)技术方案(2) Technical solution
为了达到上述目的,本发明采用的主要技术方案包括:In order to achieve the above objectives, the main technical solutions adopted by the present invention include:
一种高参比厂拌热再生设备,包括按间隔设置的第一再生烘干滚筒、第二再生烘干滚筒和热风炉膛,所述第一再生烘干滚筒和第二再生烘干滚筒上的第一出料箱和第二出料箱分别与热风炉膛的第一出风管和第二出风管相连通;A high-reference plant mixing heat regeneration equipment, comprising a first regeneration drying drum, a second regeneration drying drum and a hot air furnace arranged at intervals, the first regeneration drying drum and the second regeneration drying drum are The first discharging box and the second discharging box are respectively communicated with the first air outlet pipe and the second air outlet pipe of the hot blast furnace;
所述第一再生烘干滚筒和第二再生烘干滚筒的进料端连接有一级沉降室,一级沉降室上连接有尾气处理管路,尾气处理管路上通过回风管与热风炉膛相连通;所述尾气处理管路与回风管之间连接有回风风机;所述尾气处理管路上连接有二级沉降室;The feed ends of the first regenerative drying drum and the second regenerative drying drum are connected with a first-stage sedimentation chamber, and the first-stage sedimentation chamber is connected with a tail gas treatment pipeline, and the tail gas treatment pipeline is connected to the hot blast furnace through a return air pipe A return air blower is connected between the tail gas processing pipeline and the return air pipe; a secondary settling chamber is connected to the tail gas processing pipeline;
烘干粗集料与细集料所需的热量由燃烧器产生,并通过热风炉膛传递,其中一部分热气通过第一出风管直接进入第一再生烘干滚筒内与粗集料进行热交换,另一部分热气可通过第二出风管进入第二再生烘干滚筒内与细集料进行热交换;The heat required to dry the coarse aggregate and the fine aggregate is generated by the burner and transferred through the hot blast furnace. A part of the hot gas directly enters the first regeneration drying drum through the first air outlet pipe to exchange heat with the coarse aggregate. Another part of the hot air can enter the second regeneration drying drum through the second air outlet pipe to exchange heat with the fine aggregate;
第一再生烘干滚筒和第二再生烘干滚筒产生的尾气经过一级沉降室、尾气处理管路和二级沉降室处理后,一部分尾气经过排烟风机将尾气送入原生烘干滚筒内进行二次燃烧处理,另一部分通过回风管进入热风炉膛与燃烧器的火焰进行混合,产生热气给第一再生烘干滚筒和第二再生烘干滚筒提供热量;After the exhaust gas generated by the first regeneration drying drum and the second regeneration drying drum is processed by the primary sedimentation chamber, the exhaust gas treatment pipeline and the secondary sedimentation chamber, a part of the exhaust gas is sent to the original drying drum through the exhaust fan. After the secondary combustion process, the other part enters the hot blast furnace through the return air pipe and mixes with the flame of the burner to generate hot air to provide heat to the first regeneration drying drum and the second regeneration drying drum;
再生粗集料与细集料分别通过第一再生烘干滚筒和第二再生烘干滚 筒独立烘干加热,加热好的粗集料通过第一出料箱存放在第一热料暂存仓中,加热好的细集料通过第二出料箱存放在第二热料暂存仓中,可以根据级配需求,分别对粗集料和细集料在再生计量秤中进行计量称重,最后同时投放至搅拌缸内与原生骨料一起搅拌,最终形成合格的成品料。The recycled coarse aggregate and fine aggregate are separately dried and heated by the first regeneration drying drum and the second regeneration drying drum. The heated coarse aggregate is stored in the first hot material temporary storage bin through the first discharge box. , The heated fine aggregate is stored in the second hot material temporary storage bin through the second discharge box. According to the grading requirements, the coarse aggregate and the fine aggregate can be weighed in the regeneration weighing scale. Finally, At the same time, put it into the mixing tank and mix with the original aggregate to form a qualified finished material.
进一步地,所述第一再生烘干滚筒的进料端与再生粗集料提升机的出料端相连通;所述再生粗集料提升机的进料端与再生粗集料皮带输送机的出料端相连通;所述再生粗集料皮带输送机的进料端与再生粗集料料仓相配合。Further, the feeding end of the first regeneration drying drum is connected to the discharge end of the recycled coarse aggregate hoist; the feeding end of the recycled coarse aggregate hoist is connected to the belt conveyor of the recycled coarse aggregate. The discharge end is connected; the feeding end of the recycled coarse aggregate belt conveyor is matched with the recycled coarse aggregate silo.
进一步地,所述第二再生烘干滚筒的进料端与再生细集料提升机的出料端相连通;所述再生细集料提升机的进料端与再生细集料皮带输送机的出料端相连通;所述再生细集料皮带输送机的进料端与再生细集料料仓相配合。Further, the feed end of the second regeneration drying drum is communicated with the discharge end of the regeneration fine aggregate hoist; the feed end of the regeneration fine aggregate hoist is connected to the belt conveyor of the regeneration fine aggregate. The discharge end is connected; the feeding end of the recycled fine aggregate belt conveyor is matched with the recycled fine aggregate silo.
进一步地,所述第一出风管和/或第二出风管上设有调节风门。Further, the first air outlet pipe and/or the second air outlet pipe are provided with a regulating air door.
进一步地,所述二级沉降室通过回收粉管道与再生细集料提升机的进料端相连通。Further, the secondary settling chamber is communicated with the feed end of the recycled fine aggregate hoist through a recycled powder pipeline.
(三)有益效果(3) Beneficial effects
本发明的有益效果是:1、可实现粗细料分开加热,粗细料分别通过独立的再生烘干滚筒进行烘干加热,更易于控制粗细料的温度,特别是细料的控制,通过变频控制再生烘干滚筒的转速,从而可以更加细集料添加量的大小进行选择不同转速的控制,以及配合调整调节风门的大小,从而可以有效的保证细集料的出料温度,通过双滚筒对粗细料分开加热,可以有效的控制再生粗料和再生细料的出料温度,从而有效的提高再生料的产量,实现再生料的高参比。2、可将一级沉降室、二级沉降室中过滤沉降下来的细料回收再利用,减少固体颗粒对外排放,从而减少了对环境造成的污染;3、通过对粗细料分别计量,可以大大提高粗细料的级配精度,特别是满足对细集料的级配控制要求,从而保证成品料的级配要求;4、添加功能集成于现有厂拌热再生设备内部,结构紧凑,安装维 护方便。The beneficial effects of the present invention are as follows: 1. The coarse and fine materials can be separately heated, and the coarse and fine materials are dried and heated by independent regeneration drying drums. It is easier to control the temperature of the coarse and fine materials, especially the control of the fine materials, and the regeneration is controlled by frequency conversion. The rotation speed of the drying drum can be selected to control the amount of fine aggregate addition, and the size of the air door can be adjusted in coordination to effectively ensure the discharge temperature of the fine aggregate. The coarse and fine materials can be controlled by double drums. Separate heating can effectively control the discharge temperature of the recycled coarse material and the recycled fine material, thereby effectively increasing the output of the recycled material and realizing the high reference of the recycled material. 2. The fine materials filtered and settled in the primary sedimentation chamber and secondary sedimentation chamber can be recycled and reused to reduce the external discharge of solid particles, thereby reducing environmental pollution; 3. By measuring the coarse and fine materials separately, it can greatly Improve the grading accuracy of coarse and fine materials, especially to meet the gradation control requirements of fine aggregates, thereby ensuring the grading requirements of finished materials; 4. The added function is integrated into the existing plant mixing heat regeneration equipment, with compact structure, installation and maintenance convenient.
附图说明Description of the drawings
图1为本发明结构示意图。Figure 1 is a schematic diagram of the structure of the present invention.
具体实施方式detailed description
为了更好的解释本发明,以便于理解,下面结合附图,通过具体实施方式,对本发明作详细描述。In order to better explain the present invention and facilitate understanding, the following describes the present invention in detail through specific embodiments in conjunction with the accompanying drawings.
一种高参比厂拌热再生设备,如图1所示,包括按间隔设置的第一再生烘干滚筒1和第二再生烘干滚筒2,所述第一再生烘干滚筒1的进料端与再生粗集料提升机3的出料端相连通;所述再生粗集料提升机3的进料端与再生粗集料皮带输送机4的出料端相连通;所述再生粗集料皮带输送机4的进料端与再生粗集料料仓5相配合;所述第二再生烘干滚筒2的进料端与再生细集料提升机6的出料端相连通;所述再生细集料提升机6的进料端与再生细集料皮带输送机7的出料端相连通;所述再生细集料皮带输送机7的进料端与再生细集料料仓8相配合。A high-reference plant mixing heat regeneration equipment, as shown in Figure 1, includes a first regeneration drying drum 1 and a second regeneration drying drum 2 arranged at intervals, and the feed of the first regeneration drying drum 1 The end is connected with the discharge end of the recycled coarse aggregate elevator 3; the feed end of the recycled coarse aggregate elevator 3 is connected with the discharge end of the recycled coarse aggregate belt conveyor 4; The feed end of the belt conveyor 4 is matched with the recycled coarse aggregate silo 5; the feed end of the second regeneration drying drum 2 is connected to the discharge end of the recycled fine aggregate elevator 6; The feed end of the recycled fine aggregate hoist 6 is communicated with the discharge end of the recycled fine aggregate belt conveyor 7; the feed end of the recycled fine aggregate belt conveyor 7 is opposite to the recycled fine aggregate silo 8 Cooperate.
具体地,所述第一再生烘干滚筒1和第二再生烘干滚筒2上的第一出料箱9和第二出料箱10分别与热风炉膛13的第一出风管11和第二出风管12相连通;所述热风炉膛13与燃烧器15相连接;为了方便控制热风的风量,所述第一出风管11和/或第二出风管12上设有调节风门14。Specifically, the first discharge box 9 and the second discharge box 10 on the first regeneration drying drum 1 and the second regeneration drying drum 2 are respectively connected to the first outlet pipe 11 and the second outlet pipe 11 of the hot blast furnace 13 The air outlet pipe 12 is connected; the hot blast furnace 13 is connected to the burner 15; in order to facilitate the control of the air volume of the hot air, the first air outlet pipe 11 and/or the second air outlet pipe 12 are provided with a regulating air door 14.
具体地,所述第一出料箱9和第二出料箱10的下方设有再生计量秤16,所述再生计量秤16的下方设有搅拌缸17;为了方便加热物料的热量散发,所述第一出料箱9和第二出料箱10上分别连接有第一热料暂存仓18和第二热料暂存仓19,所述第一热料暂存仓18和第二热料暂存仓19的出料端与再生计量秤16相连接。Specifically, the first discharge box 9 and the second discharge box 10 are provided with a regenerative weighing scale 16 underneath the regenerative weighing scale 16 is provided with a stirring cylinder 17; in order to facilitate the heat dissipation of the heating material, The first discharging box 9 and the second discharging box 10 are respectively connected with a first hot material temporary storage bin 18 and a second hot material temporary storage bin 19, the first hot material temporary storage bin 18 and the second hot material temporary storage bin 18 The discharge end of the material temporary storage bin 19 is connected with the regeneration weighing scale 16.
具体地,所述第一再生烘干滚筒1和第二再生烘干滚筒2的进料端连接有一级沉降室20,一级沉降室20上连接有尾气处理管路21,尾气处理管路21上通过回风管22与热风炉膛13相连通;所述尾气处理管路 21与回风管22之间连接有回风风机23。Specifically, the feed ends of the first regeneration drying drum 1 and the second regeneration drying drum 2 are connected with a primary sedimentation chamber 20, and the primary sedimentation chamber 20 is connected with a tail gas treatment pipeline 21 and a tail gas treatment pipeline 21. The upper part is communicated with the hot blast furnace 13 through a return air pipe 22; a return air blower 23 is connected between the exhaust gas treatment pipeline 21 and the return air pipe 22.
进一步地,因尾气处理管路21内的尾气中含有颗粒物,故所述尾气处理管路21上连接有二级沉降室24,所述二级沉降室24通过回收粉管道25与再生细集料提升机6的进料端相连通。Further, because the tail gas in the tail gas treatment pipeline 21 contains particulate matter, the tail gas treatment pipeline 21 is connected with a secondary settling chamber 24, and the secondary settling chamber 24 is connected to the recycled fine aggregate through the powder recovery pipeline 25 The feeding end of the hoist 6 is connected.
进一步地,为了将产生的尾气进行二次利用,所述尾气处理管路21上连接有排烟风机26,所述排烟风机26的出气端与原生烘干滚筒相连通。Further, in order to reuse the generated exhaust gas, a smoke exhaust fan 26 is connected to the exhaust gas treatment pipeline 21, and the exhaust end of the smoke exhaust fan 26 is in communication with the original drying drum.
本实施例中,再生粗集料与细集料分别通过第一再生烘干滚筒1和第二再生烘干滚筒2独立烘干加热,加热好的粗集料存放在第一热料暂存仓18中,加热好的细集料存放在第二热料暂存仓19中,可以根据级配需求,分别对粗集料和细集料在再生计量秤16中进行计量称重,最后同时投放至搅拌缸17内与原生骨料等一起搅拌,最终形成合格的成品料。In this embodiment, the recycled coarse aggregate and the fine aggregate are separately dried and heated by the first regeneration drying drum 1 and the second regeneration drying drum 2 respectively, and the heated coarse aggregate is stored in the first thermal material temporary storage bin In 18, the heated fine aggregate is stored in the second hot material temporary storage bin 19. According to the grading requirements, the coarse aggregate and the fine aggregate can be weighed in the regenerating weighing scale 16, and finally put in at the same time. The mixing tank 17 is mixed with the raw aggregates and the like, and finally a qualified finished material is formed.
本实施例中,烘干粗集料与细集料所需的热量由燃烧器15产生,并通过热风炉膛13传递,其中一部分热气通过第一出风管11直接进入第一再生烘干滚筒1内与粗集料进行热交换,另一部分热气可通过第二出风管12进入第二再生烘干滚筒2内与细集料进行热交换,第二出风管12上装有调节风门14,可控制进入第二再生烘干滚筒2内部热量流量,第二再生烘干滚筒2可变频控制滚筒转速,根据细料量的多少选择适当的滚筒转速,配合调节风门14控制细料出料温度。In this embodiment, the heat required to dry the coarse aggregate and the fine aggregate is generated by the burner 15 and transferred through the hot blast furnace 13, and part of the hot gas directly enters the first regeneration drying drum 1 through the first air outlet pipe 11 The internal heat exchange with the coarse aggregate, the other part of the hot air can enter the second regenerative drying drum 2 through the second air outlet pipe 12 to exchange heat with the fine aggregate. The second air outlet pipe 12 is equipped with a regulating air door 14, which can be Control the heat flow entering the second regeneration drying drum 2. The second regeneration drying drum 2 can control the drum speed by frequency conversion, select the appropriate drum speed according to the amount of fine material, and cooperate with the adjusting damper 14 to control the fine material discharge temperature.
本实施例中,第一再生烘干滚筒1和第二再生烘干滚筒2产生的尾气经过一级沉降室20、尾气处理管路21和二级沉降室24处理后,一部分尾气经过排烟风机26将尾气送入原生烘干滚筒内进行二次燃烧处理,另一部分通过回风管22进入热风炉膛13与燃烧器15的火焰进行混合,产生热气给第一再生烘干滚筒1和第二再生烘干滚筒2提供热量。In this embodiment, after the exhaust gas generated by the first regeneration drying drum 1 and the second regeneration drying drum 2 is processed by the primary sedimentation chamber 20, the exhaust gas treatment pipeline 21 and the secondary sedimentation chamber 24, a part of the exhaust gas passes through the exhaust fan 26. The tail gas is sent into the primary drying drum for secondary combustion treatment, and the other part enters the hot blast furnace 13 through the return air pipe 22 and mixes with the flame of the burner 15 to generate hot air for the first regeneration drying drum 1 and the second regeneration. The drying drum 2 provides heat.
本实施例可实现粗细料分开加热,粗细料分别通过独立的再生烘干滚筒进行烘干加热,更易于控制粗细料的温度,特别是细料的控制,通过变频控制再生烘干滚筒的转速,从而可以更加细集料添加量的大小进行选择不同转速的控制,以及配合调整调节风门的大小,从而可以有效 的保证细集料的出料温度,通过双滚筒对粗细料分开加热,可以有效的控制再生粗料和再生细料的出料温度,从而有效的提高再生料的产量,实现再生料的高参比。In this embodiment, the coarse and fine materials can be heated separately, and the coarse and fine materials are dried and heated by independent regeneration drying drums. It is easier to control the temperature of the coarse and fine materials, especially the control of the fine materials. The rotation speed of the regeneration drying drum is controlled by frequency conversion. Therefore, it is possible to select the size of the finer aggregate addition to control the different speeds, and adjust the size of the damper, so as to effectively ensure the discharge temperature of the fine aggregate, and the coarse and fine materials are separately heated by the double rollers, which can be effective Control the discharge temperature of the recycled coarse material and the recycled fine material, thereby effectively increasing the output of the recycled material and realizing the high reference of the recycled material.
本实施例可将一级沉降室、二级沉降室中过滤沉降下来的细料回收再利用,减少固体颗粒对外排放,从而减少了对环境造成的污染;通过对粗细料分别计量,可以大大提高粗细料的级配精度,特别是满足对细集料的级配控制要求,从而保证成品料的级配要求;添加功能集成于现有厂拌热再生设备内部,结构紧凑,安装维护方便。This embodiment can recycle and reuse the fine materials filtered and settled in the primary sedimentation chamber and secondary sedimentation chamber, reducing the external discharge of solid particles, thereby reducing environmental pollution; by separately measuring the coarse and fine materials, it can greatly improve The grading accuracy of coarse and fine materials, especially to meet the gradation control requirements of fine aggregates, so as to ensure the grading requirements of finished materials; the added function is integrated in the existing plant mixing heat regeneration equipment, with compact structure and convenient installation and maintenance.
以上所述仅为本发明的较佳实施例,凡依本发明申请专利范围所做的均等变化与修饰,皆应属本发明的涵盖范围。The foregoing descriptions are only preferred embodiments of the present invention, and all equivalent changes and modifications made in accordance with the scope of the patent application of the present invention should fall within the scope of the present invention.

Claims (5)

  1. 一种高参比厂拌热再生设备,其特征在于,包括按间隔设置的第一再生烘干滚筒(1)、第二再生烘干滚筒(2)和热风炉膛(13),所述第一再生烘干滚筒(1)和第二再生烘干滚筒(2)上的第一出料箱(9)和第二出料箱(10)分别与热风炉膛(13)的第一出风管(11)和第二出风管(12)相连通;A high-reference plant mixing heat regeneration equipment, which is characterized in that it comprises a first regeneration drying drum (1), a second regeneration drying drum (2) and a hot blast furnace (13) arranged at intervals. The first discharge box (9) and the second discharge box (10) on the regeneration drying drum (1) and the second regeneration drying drum (2) are respectively connected to the first outlet pipe ( 11) Connect with the second air outlet pipe (12);
    所述第一再生烘干滚筒(1)和第二再生烘干滚筒(2)的进料端连接有一级沉降室(20),一级沉降室(20)上连接有尾气处理管路(21),尾气处理管路(21)上通过回风管(22)与热风炉膛(13)相连通;所述尾气处理管路(21)与回风管(22)之间连接有回风风机(23);所述尾气处理管路(21)上连接有二级沉降室(24);The feed ends of the first regeneration drying drum (1) and the second regeneration drying drum (2) are connected with a primary sedimentation chamber (20), and the primary sedimentation chamber (20) is connected with an exhaust gas treatment pipeline (21) ), the tail gas treatment pipeline (21) is connected to the hot blast furnace (13) through a return air pipe (22); a return air fan ( 23); The tail gas treatment pipeline (21) is connected with a secondary settling chamber (24);
    烘干粗集料与细集料所需的热量由燃烧器(15)产生,并通过热风炉膛(13)传递,其中一部分热气通过第一出风管(11)直接进入第一再生烘干滚筒(1)内与粗集料进行热交换,另一部分热气可通过第二出风管(12)进入第二再生烘干滚筒(2)内与细集料进行热交换;The heat required for drying coarse and fine aggregates is generated by the burner (15) and is transferred through the hot blast furnace (13), and part of the hot air directly enters the first regeneration drying drum through the first air outlet pipe (11) (1) The internal heat exchange with the coarse aggregate, and the other part of the hot air can enter the second regeneration drying drum (2) through the second air outlet pipe (12) to exchange heat with the fine aggregate;
    第一再生烘干滚筒(1)和第二再生烘干滚筒(2)产生的尾气经过一级沉降室(20)、尾气处理管路(21)和二级沉降室(24)处理后,一部分尾气经过排烟风机(26)将尾气送入原生烘干滚筒内进行二次燃烧处理,另一部分通过回风管(22)进入热风炉膛(13)与燃烧器(15)的火焰进行混合,产生热气给第一再生烘干滚筒(1)和第二再生烘干滚筒(2)提供热量;After the exhaust gas generated by the first regeneration drying drum (1) and the second regeneration drying drum (2) is processed by the primary sedimentation chamber (20), the exhaust gas treatment pipeline (21) and the secondary sedimentation chamber (24), part of The exhaust gas passes through the exhaust fan (26) to send the exhaust gas into the original drying drum for secondary combustion treatment, and the other part enters the hot blast furnace (13) through the return air pipe (22) to mix with the flame of the burner (15) to produce The hot air provides heat to the first regeneration drying drum (1) and the second regeneration drying drum (2);
    再生粗集料与细集料分别通过第一再生烘干滚筒(1)和第二再生烘干滚筒(2)独立烘干加热,加热好的粗集料通过第一出料箱(9)存放在第一热料暂存仓(18)中,加热好的细集料通过第二出料箱(10)存放在第二热料暂存仓(19)中,可以根据级配需求,分别对粗集料和细集料在再生计量秤(16)中进行计量称重,最后同时投放至搅拌缸(17)内与原生骨料一起搅拌,最终形成合格的成品料。The recycled coarse aggregate and fine aggregate are separately dried and heated by the first regeneration drying drum (1) and the second regeneration drying drum (2), and the heated coarse aggregate is stored in the first discharge box (9) In the first hot material temporary storage bin (18), the heated fine aggregates are stored in the second hot material temporary storage bin (19) through the second discharge box (10), and can be adjusted separately according to the grading requirements. Coarse aggregates and fine aggregates are weighed in a regenerated weighing scale (16), and finally put into the mixing tank (17) at the same time and mixed with the original aggregates to form a qualified finished product.
  2. 如权利要求1所述的一种高参比厂拌热再生设备,其特征在于,所述 第一再生烘干滚筒(1)的进料端与再生粗集料提升机(3)的出料端相连通;所述再生粗集料提升机(3)的进料端与再生粗集料皮带输送机(4)的出料端相连通;所述再生粗集料皮带输送机(4)的进料端与再生粗集料料仓(5)相配合。The high-reference plant-mix thermal regeneration equipment according to claim 1, wherein the feed end of the first regeneration drying drum (1) and the output of the recycled coarse aggregate hoist (3) The feed end of the recycled coarse aggregate hoist (3) is connected with the discharge end of the recycled coarse aggregate belt conveyor (4); the recycled coarse aggregate belt conveyor (4) The feed end is matched with the recycled coarse aggregate silo (5).
  3. 如权利要求1所述的一种高参比厂拌热再生设备,其特征在于,所述第二再生烘干滚筒(2)的进料端与再生细集料提升机(6)的出料端相连通;所述再生细集料提升机(6)的进料端与再生细集料皮带输送机(7)的出料端相连通;所述再生细集料皮带输送机(7)的进料端与再生细集料料仓(8)相配合。The high-reference plant-mix thermal regeneration equipment according to claim 1, wherein the feed end of the second regeneration drying drum (2) and the output of the regeneration fine aggregate hoist (6) The feed end of the regenerated fine aggregate hoist (6) is connected to the discharge end of the regenerated fine aggregate belt conveyor (7); the regenerated fine aggregate belt conveyor (7) The feed end is matched with the regenerated fine aggregate silo (8).
  4. 如权利要求1所述的一种高参比厂拌热再生设备,其特征在于,所述第一出风管(11)和/或第二出风管(12)上设有调节风门(14)。The high-reference plant mixing heat regeneration equipment according to claim 1, characterized in that, the first air outlet pipe (11) and/or the second air outlet pipe (12) are provided with a regulating damper (14) ).
  5. 如权利要求3所述的一种高参比厂拌热再生设备,其特征在于,所述二级沉降室(24)通过回收粉管道(25)与再生细集料提升机(6)的进料端相连通。The high-reference plant mixing heat regeneration equipment according to claim 3, characterized in that, the secondary settling chamber (24) is fed by the recycled powder pipeline (25) and the recycled fine aggregate elevator (6). The material ends are connected.
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