CN119972723B - Multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium - Google Patents

Multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium

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Publication number
CN119972723B
CN119972723B CN202510478922.1A CN202510478922A CN119972723B CN 119972723 B CN119972723 B CN 119972723B CN 202510478922 A CN202510478922 A CN 202510478922A CN 119972723 B CN119972723 B CN 119972723B
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fly ash
asphalt
disposal
stirring
layer
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CN119972723A (en
Inventor
孙晓龙
黄国轩
覃潇
许新权
刘志胜
邹超
郭永昌
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Guangdong University of Technology
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Guangdong University of Technology
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    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/20—Agglomeration, binding or encapsulation of solid waste
    • B09B3/21—Agglomeration, binding or encapsulation of solid waste using organic binders or matrix
    • B09B3/23—Binders with asphalt
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/30—Destroying solid waste or transforming solid waste into something useful or harmless involving mechanical treatment
    • B09B3/38—Stirring or kneading
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B2101/00—Type of solid waste
    • B09B2101/30—Incineration ashes

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  • Engineering & Computer Science (AREA)
  • Environmental & Geological Engineering (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Civil Engineering (AREA)
  • Structural Engineering (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

本发明公开了一种基于沥青介质的垃圾飞灰多层立体化处置装置,属于垃圾飞灰处置技术领域,包括罐体;设置与所述罐体上方的下落处置单元;位于所述下落处置单元下方的旋转处置机构;位于所述旋转处置机构下方的搅拌处置机构、设置在所述搅拌处置机构下方的冷却处置机构,以及设置在所述罐体上的基础件。本发明从顶部的垃圾飞灰储存罐落下的飞灰通过下落处置单元、旋转处置机构、搅拌处置机构以冷却处置机构,从不同角度以及不同方向喷洒沥青裹覆飞灰并且通过多重拌合组件实现沥青与飞灰的交互混合,显著减小了飞灰的重金属浸出浓度,提高了重金属浸出抑制率以及飞灰在沥青中的分散性,最终材料存储罐收集处置完的垃圾飞灰‑沥青材料。

The present invention discloses a multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium, which belongs to the technical field of garbage fly ash disposal, and comprises a tank body; a falling disposal unit arranged above the tank body; a rotating disposal mechanism located below the falling disposal unit; a stirring disposal mechanism located below the rotating disposal mechanism, a cooling disposal mechanism arranged below the stirring disposal mechanism, and a base member arranged on the tank body. In the present invention, the fly ash falling from the top of the garbage fly ash storage tank is sprayed with asphalt from different angles and directions through the falling disposal unit, the rotating disposal mechanism, the stirring disposal mechanism, and the cooling disposal mechanism, and the fly ash is coated with asphalt from different angles and directions, and the interactive mixing of asphalt and fly ash is achieved through multiple mixing components, which significantly reduces the heavy metal leaching concentration of the fly ash, improves the heavy metal leaching inhibition rate and the dispersibility of the fly ash in the asphalt, and finally the material storage tank collects the disposed garbage fly ash-asphalt material.

Description

一种基于沥青介质的垃圾飞灰多层立体化处置装置A multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium

技术领域Technical Field

本发明涉及垃圾飞灰处置技术领域,具体涉及一种基于沥青介质的垃圾飞灰多层立体化处置装置。The present invention relates to the technical field of waste fly ash disposal, and in particular to a multi-layer three-dimensional waste fly ash disposal device based on asphalt medium.

背景技术Background Art

垃圾飞灰是城市生活垃圾焚烧过程中产生的细小颗粒物,主要由无机盐、重金属(如铅、镉、汞)和有机污染物(如二噁英)等组成。由于其颗粒细小、比表面积大,飞灰中的重金属和有机污染物具有较高的迁移性和生物毒性,对环境和人体健康构成严重威胁。Fly ash is a fine particle produced during the incineration of municipal solid waste. It is primarily composed of inorganic salts, heavy metals (such as lead, cadmium, and mercury), and organic pollutants (such as dioxins). Due to its small size and large surface area, the heavy metals and organic pollutants in fly ash are highly mobile and biotoxic, posing a serious threat to the environment and human health.

现有的垃圾飞灰无害化处置主要采用水泥或螯合剂等材料对飞灰实施固化进而实现无害化处理,固化过程主要采用混合固化的装置,即通过搅拌、混合等工艺将水泥或螯合剂与飞灰混合,形成固化体。然而,现有的垃圾飞灰搅拌混合固化装置存在以下缺点:Existing fly ash harmless disposal methods primarily use materials such as cement or chelating agents to solidify the fly ash and achieve harmless treatment. The solidification process primarily utilizes a mixing and solidification device, which mixes the cement or chelating agent with the fly ash through stirring and mixing processes to form a solidified body. However, existing fly ash mixing and solidification devices have the following disadvantages:

飞灰和固化介质交互混合后,飞灰在固化剂内部存在分散性不良问题,在外界影响下飞灰易出现重金属溶渗问题;现有的搅拌混合固化装置多采用简单的搅拌混合,固化介质对飞灰的包裹性基本为混合交互的单层包裹,在裹覆的薄弱区容易出现溶渗风险。After the fly ash and the solidifying medium are interactively mixed, the fly ash has a poor dispersion problem inside the solidifying agent, and under external influences, the fly ash is prone to heavy metal dissolution and infiltration problems; the existing stirring and mixing solidification devices mostly use simple stirring and mixing, and the solidifying medium's wrapping of the fly ash is basically a mixed and interactive single-layer wrapping, and the risk of dissolution and infiltration is prone to occur in the weak areas of the wrapping.

发明内容Summary of the Invention

鉴于上述存在的问题,提出了本发明。In view of the above-mentioned problems, the present invention is proposed.

因此,本发明解决的技术问题是:飞灰在固化剂内部存在分散性不良问题,并且固化介质对飞灰的包裹性基本为混合交互的单层包裹,在裹覆的薄弱区容易出现溶渗风险。Therefore, the technical problem solved by the present invention is that fly ash has a poor dispersion problem inside the curing agent, and the solidifying medium's wrapping of the fly ash is basically a mixed and interactive single-layer wrapping, and the risk of dissolution and infiltration is prone to occur in the weak areas of the wrapping.

为解决上述技术问题,本发明提供如下技术方案:一种基于沥青介质的垃圾飞灰多层立体化处置装置,其包括如下步骤,In order to solve the above technical problems, the present invention provides the following technical solutions: a multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium, which comprises the following steps:

罐体;Tank;

设置与所述罐体上方的下落处置单元,所述下落处置单元包括底板、布置于所述底板表面的疏油涂层、设置在所述罐体内壁的沥青喷洒器,以及设置于所述底板下端的挡板;下落处置单元为螺旋结构,实现了延长垃圾飞灰-沥青材料的下落时长,加长了处置时间和空间;A drop disposal unit is provided above the tank body, comprising a bottom plate, an oleophobic coating arranged on the surface of the bottom plate, an asphalt sprayer arranged on the inner wall of the tank body, and a baffle arranged at the lower end of the bottom plate; the drop disposal unit is a spiral structure, which extends the falling time of the fly ash-asphalt material and prolongs the disposal time and space;

位于所述下落处置单元下方的旋转处置机构,所述旋转处置机构包括位于罐体中部的旋转桶、位于所述旋转桶上方的自动喷头、设置于所述旋转桶侧面的鼓风机构,安装在所述旋转桶下方的底盘;A rotating disposal mechanism located below the falling disposal unit, comprising a rotating barrel located in the middle of the tank body, an automatic spray head located above the rotating barrel, an air blowing mechanism provided on the side of the rotating barrel, and a chassis installed below the rotating barrel;

位于所述旋转处置机构下方的搅拌处置机构、设置在所述搅拌处置机构下方的冷却处置机构,以及设置在所述罐体上的基础件。A stirring treatment mechanism is located below the rotating treatment mechanism, a cooling treatment mechanism is arranged below the stirring treatment mechanism, and a base member is arranged on the tank body.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述旋转桶的底部内壁设置有若干个凸块,开设在所述凸块之间的气门,以及设置在所述旋转桶底部的第一阀门。As a preferred solution of the multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium described in the present invention, the bottom inner wall of the rotating barrel is provided with a plurality of protrusions, valves are opened between the protrusions, and a first valve is provided at the bottom of the rotating barrel.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述鼓风机构包括开设在所述罐体内壁的进风口、与所述进风口连通的通风管,以及连接于所述通风管另一端的出风口;As a preferred embodiment of the asphalt medium-based multi-layer three-dimensional disposal device for fly ash of garbage described in the present invention, the air blowing mechanism includes an air inlet provided on the inner wall of the tank body, a ventilation pipe connected to the air inlet, and an air outlet connected to the other end of the ventilation pipe;

所述鼓风机构还包括设置在所述通风管中部的蜗壳;The air blowing mechanism further includes a volute disposed in the middle of the ventilation pipe;

所述蜗壳的内部设置有叶轮,以及与所述叶轮相连的轴承。An impeller and a bearing connected to the impeller are arranged inside the volute.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述底盘的内部开设多组导气管,以及预留于所述底盘表面的接入口;As a preferred solution of the multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium described in the present invention, wherein: multiple groups of air ducts are opened inside the chassis, and access ports are reserved on the surface of the chassis;

其中,所述导气管与出风口相连。Wherein, the air guide pipe is connected to the air outlet.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述搅拌处置机构包括搅拌桨、设置在所述搅拌桨侧面的连接管道、位于所述搅拌桨上方的红外线加热器,以及设置在所述搅拌桨之间下方的第二阀门;As a preferred embodiment of the asphalt-based multi-layer three-dimensional disposal device for fly ash of garbage of the present invention, the stirring and disposal mechanism includes a stirring paddle, a connecting pipe provided on the side of the stirring paddle, an infrared heater located above the stirring paddle, and a second valve provided below and between the stirring paddles;

所述搅拌桨的内端设置有圆盘,所述圆盘的内部固定连接搅拌轴。A disc is provided at the inner end of the stirring paddle, and the interior of the disc is fixedly connected to the stirring shaft.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述冷却处置机构包括设置在所述罐体下方的冷却罐、位于所述冷却罐上方的搅拌件、开设在所述搅拌件侧面的沥青喷洒管,以及位于所述冷却罐外部的液氮冷却室,所述冷却处置机构还包括开设在所述液氮冷却室侧面的输送口,以及位于冷却罐底部的第三阀门。As a preferred solution of the multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium described in the present invention, the cooling disposal mechanism includes a cooling tank arranged below the tank body, a stirring member located above the cooling tank, an asphalt spraying pipe opened on the side of the stirring member, and a liquid nitrogen cooling chamber located outside the cooling tank. The cooling disposal mechanism also includes a delivery port opened on the side of the liquid nitrogen cooling chamber, and a third valve located at the bottom of the cooling tank.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述搅拌件包括设置于所述冷却罐内部上侧靠近所述第二阀门的转动桨、用于连接所述转动桨的连接轴,以及设置于冷却罐表面的电动机。As a preferred solution of the asphalt medium-based multi-layer three-dimensional disposal device for garbage fly ash described in the present invention, the stirring element includes a rotating paddle arranged on the upper side of the interior of the cooling tank close to the second valve, a connecting shaft for connecting the rotating paddle, and an electric motor arranged on the surface of the cooling tank.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述基础件包括搅拌装置、位于所述罐体上端侧面的沥青存储室,以及罐体上端的垃圾飞灰储存罐;As a preferred embodiment of the asphalt medium-based multi-layer three-dimensional disposal device for garbage fly ash of the present invention, the base member includes a stirring device, an asphalt storage chamber located on the side of the upper end of the tank body, and a garbage fly ash storage tank at the upper end of the tank body;

所述基础件还包括连接在所述沥青存储室下方的沥青输送管,以及位于罐体下端的材料存储罐。The base member further includes an asphalt delivery pipe connected below the asphalt storage chamber, and a material storage tank located at the lower end of the tank body.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述垃圾飞灰储存罐的底部设置有第四阀门,所述垃圾飞灰储存罐的上方开设垃圾飞灰进料口;As a preferred embodiment of the asphalt medium-based multi-layer three-dimensional waste fly ash disposal device of the present invention, a fourth valve is provided at the bottom of the waste fly ash storage tank, and a waste fly ash feed port is provided above the waste fly ash storage tank;

其中,所述垃圾飞灰储存罐的底面为倾斜设置;Wherein, the bottom surface of the garbage fly ash storage tank is inclined;

所述沥青存储室的外侧预留沥青进料口,所述沥青存储室与沥青输送管之间设置第五阀门,所述沥青存储室与自动喷头之间设置第六阀门。An asphalt feed port is reserved on the outer side of the asphalt storage chamber, a fifth valve is provided between the asphalt storage chamber and the asphalt delivery pipe, and a sixth valve is provided between the asphalt storage chamber and the automatic sprinkler.

作为本发明所述的一种基于沥青介质的垃圾飞灰多层立体化处置装置的一种优选方案,其中:所述沥青输送管通过第六阀门与所述搅拌处置机构连接。As a preferred solution of the multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium described in the present invention, the asphalt delivery pipe is connected to the stirring disposal mechanism through a sixth valve.

本发明的有益效果:本装置通过将从顶部的垃圾飞灰储存罐落下的飞灰通过下落处置单元、旋转处置机构、搅拌处置机构以冷却处置机构,从不同角度以及不同方向喷洒沥青裹覆飞灰并且通过多重拌合组件实现沥青与飞灰的交互混合,显著减小了飞灰的重金属浸出浓度,提高了重金属浸出抑制率以及飞灰在沥青中的分散性,最终材料存储罐收集处置完的垃圾飞灰-沥青材料,处置完的垃圾飞灰-沥青材料还具有更高的资源化利用潜力,可用于道路修建、建筑填料等领域,实现废弃物的高效利用。The beneficial effects of the present invention are as follows: the device passes the fly ash falling from the top garbage fly ash storage tank through a falling disposal unit, a rotating disposal mechanism, a stirring disposal mechanism and a cooling disposal mechanism, sprays asphalt-coated fly ash from different angles and directions, and realizes interactive mixing of asphalt and fly ash through multiple mixing components, thereby significantly reducing the heavy metal leaching concentration of fly ash, improving the heavy metal leaching inhibition rate and the dispersion of fly ash in asphalt, and finally the material storage tank collects the disposed garbage fly ash-asphalt material. The disposed garbage fly ash-asphalt material also has higher resource utilization potential and can be used in road construction, building fillers and other fields to achieve efficient utilization of waste.

附图说明BRIEF DESCRIPTION OF THE DRAWINGS

为了更清楚地说明本发明实施例的技术方案,下面将对实施例描述中所需要使用的附图作简单的介绍,显而易见的,下面描述中的附图仅仅是本发明的一些实施例,对于本领域普通技术人员来讲,在不付出创造性劳动的前提下,还可以根据这些附图获得其他的附图。In order to more clearly illustrate the technical solutions of the embodiments of the present invention, the following briefly introduces the drawings required for use in the description of the embodiments. Obviously, the drawings described below are only some embodiments of the present invention. For ordinary technicians in this field, other drawings can be obtained based on these drawings without paying any creative work.

图1为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的剖面示意图。FIG1 is a cross-sectional schematic diagram of a multi-layer three-dimensional disposal device for fly ash based on an asphalt medium provided by an embodiment of the present invention.

图2为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的下落处置单元结构示意图。FIG2 is a schematic structural diagram of a falling disposal unit of a multi-layer three-dimensional disposal device for fly ash based on asphalt medium provided by an embodiment of the present invention.

图3为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的底盘结构示意图。FIG3 is a schematic diagram of the chassis structure of a multi-layer three-dimensional disposal device for fly ash based on asphalt medium provided by an embodiment of the present invention.

图4为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的旋转处置机构俯视图。FIG4 is a top view of a rotating disposal mechanism of a multi-layer three-dimensional disposal device for fly ash based on asphalt medium provided by one embodiment of the present invention.

图5为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的鼓风机构结构图。FIG5 is a structural diagram of the blowing mechanism of a multi-layer three-dimensional disposal device for fly ash based on asphalt medium provided by an embodiment of the present invention.

图6为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的搅拌处置机构俯视图。FIG6 is a top view of a stirring and disposal mechanism of a multi-layer three-dimensional disposal device for fly ash based on an asphalt medium provided by an embodiment of the present invention.

图7为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的冷却处置机构俯视图。FIG7 is a top view of a cooling treatment mechanism of a multi-layer three-dimensional treatment device for fly ash based on an asphalt medium provided by an embodiment of the present invention.

图8为本发明一个实施例提供的一种基于沥青介质的垃圾飞灰多层立体化处置装置的搅拌件结构图。FIG8 is a structural diagram of a stirring element of a multi-layer three-dimensional disposal device for fly ash based on asphalt medium provided by an embodiment of the present invention.

其中,1、罐体;2、下落处置单元;21、底板;22、疏油涂层;23、沥青喷洒器;24、挡板;3、旋转处置机构;31、旋转桶;311、凸块;312、气门;313、第一阀门;32、自动喷头;33、鼓风机构;331、进风口;332、出风口;333、通风管;334、蜗壳;3341、叶轮;3342、轴承;34、底盘;341、导气管;342、接入口;4、搅拌处置机构;41、搅拌桨;411、搅拌轴;412、圆盘;42、连接管道;43、红外线加热器;44、第二阀门;5、冷却处置机构;51、冷却罐;52、搅拌件;521、转动桨;522、连接轴;523、电动机;53、沥青喷洒管;54、液氮冷却室;55、输送口;56、第三阀门;6、基础件;61、搅拌装置;62、沥青存储室;621、沥青进料口;622、第五阀门;623、第六阀门;63、垃圾飞灰储存罐;631、第四阀门;632、垃圾飞灰进料口;64、沥青输送管;641、第六阀门;65、材料存储罐。Among them, 1. tank body; 2. drop disposal unit; 21. bottom plate; 22. oleophobic coating; 23. asphalt sprayer; 24. baffle; 3. rotating disposal mechanism; 31. rotating barrel; 311. bump; 312. valve; 313. first valve; 32. automatic nozzle; 33. blowing mechanism; 331. air inlet; 332. air outlet; 333. ventilation pipe; 334. volute; 3341. impeller; 3342. bearing; 34. chassis; 341. air guide pipe; 342. access port; 4. stirring disposal mechanism; 41. stirring paddle; 411. stirring shaft; 412. disc; 42. connecting pipe ; 43. Infrared heater; 44. Second valve; 5. Cooling disposal mechanism; 51. Cooling tank; 52. Stirring member; 521. Rotating paddle; 522. Connecting shaft; 523. Motor; 53. Asphalt spraying pipe; 54. Liquid nitrogen cooling chamber; 55. Delivery port; 56. Third valve; 6. Basic member; 61. Stirring device; 62. Asphalt storage chamber; 621. Asphalt feed port; 622. Fifth valve; 623. Sixth valve; 63. Garbage fly ash storage tank; 631. Fourth valve; 632. Garbage fly ash feed port; 64. Asphalt delivery pipe; 641. Sixth valve; 65. Material storage tank.

具体实施方式DETAILED DESCRIPTION

为使本发明的上述目的、特征和优点能够更加明显易懂,下面结合说明书附图对本发明的具体实施方式做详细的说明,显然所描述的实施例是本发明的一部分实施例,而不是全部实施例。基于本发明中的实施例,本领域普通人员在没有做出创造性劳动前提下所获得的所有其他实施例,都应当属于本发明的保护的范围。To make the above-mentioned objects, features, and advantages of the present invention more clearly understood, the following detailed description of the specific embodiments of the present invention is given in conjunction with the accompanying drawings. It is obvious that the described embodiments are only part of the embodiments of the present invention, not all of them. Based on the embodiments of the present invention, all other embodiments obtained by ordinary persons in this field without creative work should fall within the scope of protection of the present invention.

实施例1,参照图1~图8,为本发明的第一个实施例,该实施例提供了一种基于沥青介质的垃圾飞灰多层立体化处置装置,通过垃圾飞灰储存罐63的下方连接下落处置单元2,并且下落处置单元2为螺旋结构,下落处置单元2的下方安装了旋转处置机构3。Example 1, referring to Figures 1 to 8, is the first embodiment of the present invention. This embodiment provides a multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium, which is connected to the bottom of the garbage fly ash storage tank 63 through a falling disposal unit 2, and the falling disposal unit 2 is a spiral structure, and a rotating disposal mechanism 3 is installed below the falling disposal unit 2.

下落处置单元2初步处置垃圾飞灰,并通过重力作用使垃圾飞灰-沥青材料从下落处置单元2上部螺旋下落流入底部,垃圾飞灰-沥青材料会通过挡板24拦下并落在旋转处置机构3中,进一步混合交互垃圾飞灰与沥青,进而避免在下落处置单元2中沥青与垃圾飞灰的初步混合下,垃圾飞灰中的重金属未能充分得到处置封存。The falling disposal unit 2 preliminarily disposes of the fly ash, and causes the fly ash-asphalt material to spirally fall from the upper part of the falling disposal unit 2 to flow into the bottom through the action of gravity. The fly ash-asphalt material will be intercepted by the baffle 24 and fall into the rotating disposal mechanism 3, and further mix the fly ash and asphalt, thereby avoiding the heavy metals in the fly ash from being fully disposed of and sealed due to the preliminary mixing of asphalt and fly ash in the falling disposal unit 2.

下落处置单元2的侧面安装一组沥青喷洒器23,沥青喷洒器23以及底板21与罐体1之间为固定连接,使得底板21与罐体1直接连接在一起,底板21俯视为圆形,采用加热棒设置在底板21中,在加热时热量直接传递给底板21和沥青,促进沥青的流动。加热棒的材料选用陶瓷加热元件,其具有加热迅速、热效率高且使用寿命长等优点,能够适应频繁的加热和冷却过程。在底板21的面上覆盖有一层疏油涂层22,疏油涂层22采用聚四氟乙烯(PTFE)材料,PTFE具有优异的疏油性能和化学稳定性,能够有效防止沥青和油类物质的粘附,同时具有良好的耐高温和耐腐蚀性能。疏油涂层22的低摩擦系数还能够减少混合料在底板上的摩擦阻力,提高装置的运行效率,且保护了底板21免受化学腐蚀和机械磨损,延长装置的使用寿命,使得沥青与垃圾飞灰混合料顺利通过重力作用下到达旋转处置机构3。A set of asphalt sprayers 23 are installed on the side of the drop disposal unit 2. The asphalt sprayers 23 and the bottom plate 21 are fixedly connected to the tank body 1, so that the bottom plate 21 is directly connected to the tank body 1. The bottom plate 21 is circular when viewed from above. A heating rod is set in the bottom plate 21. During heating, heat is directly transferred to the bottom plate 21 and the asphalt, promoting the flow of the asphalt. The material of the heating rod is a ceramic heating element, which has the advantages of rapid heating, high thermal efficiency and long service life, and can adapt to frequent heating and cooling processes. The surface of the bottom plate 21 is covered with a layer of oleophobic coating 22. The oleophobic coating 22 is made of polytetrafluoroethylene (PTFE). PTFE has excellent oleophobic properties and chemical stability, can effectively prevent the adhesion of asphalt and oily substances, and has good high temperature resistance and corrosion resistance. The low friction coefficient of the oleophobic coating 22 can also reduce the frictional resistance of the mixture on the base plate, improve the operating efficiency of the device, and protect the base plate 21 from chemical corrosion and mechanical wear, extending the service life of the device, so that the asphalt and garbage fly ash mixture can smoothly reach the rotating disposal mechanism 3 under the action of gravity.

较佳的,下落处置单元2外沿焊接设置有一圈沥青存储室62,沥青喷洒器23通过沥青存储室62获得沥青并向下落处置单元2喷洒。将电加热板设置在沥青存储室62内壁来加热沥青,并且电加热板的材质为不锈钢,不锈钢材质不易被沥青腐蚀以及有较高的耐高温性能,选用多个较小的加热板组合安装在内壁的不同位置。下落处置单元2顶部连接着垃圾飞灰储存罐63,在垃圾飞灰储存罐63的罐底设有第四阀门631,通过第四阀门631将垃圾飞灰储存罐63中的垃圾飞灰通入下落处置单元2中,垃圾飞灰储存罐63的底面为倾斜设置,以及在其垃圾飞灰储存罐63表面设有一层疏油涂层,便于垃圾飞灰从垃圾飞灰储存罐63中落入下落处置单元2。Preferably, a circle of asphalt storage chamber 62 is welded on the outer edge of the drop disposal unit 2, and the asphalt sprayer 23 obtains asphalt through the asphalt storage chamber 62 and sprays it onto the drop disposal unit 2. An electric heating plate is set on the inner wall of the asphalt storage chamber 62 to heat the asphalt, and the material of the electric heating plate is stainless steel, which is not easily corroded by asphalt and has high high temperature resistance. A plurality of smaller heating plates are selected and installed in combination at different positions on the inner wall. The top of the drop disposal unit 2 is connected to the garbage fly ash storage tank 63, and a fourth valve 631 is provided at the bottom of the garbage fly ash storage tank 63. The garbage fly ash in the garbage fly ash storage tank 63 is passed into the drop disposal unit 2 through the fourth valve 631. The bottom surface of the garbage fly ash storage tank 63 is inclined, and a layer of oleophobic coating is provided on the surface of the garbage fly ash storage tank 63 to facilitate the garbage fly ash from the garbage fly ash storage tank 63 to fall into the drop disposal unit 2.

较佳的,如图1、图3、图4以及图5所示,旋转处置机构3四周设置着与沥青存储室62相连的沥青输送管64,沥青输送管64将沥青存储室62中的沥青输送往搅拌处置机构4进一步处置垃圾飞灰中的重金属。旋转处置机构3的两侧与罐体1相连的部位焊接了通风管333,通过鼓风机构33将气体通入旋转处置机构3中的导气管341中,鼓风机构33采用高强度工程塑料制造的叶轮3341和不锈钢材料制造的蜗壳334,鼓风机构33设置于旋转处置机构3侧面,通过进风口331和出风口332提供稳定的气流,确保垃圾飞灰-沥青材料在旋转桶31内的均匀分布。工程塑料具有良好的耐腐蚀性和机械强度,不锈钢则具有良好的耐高温和耐腐蚀性能。导气管341将气体通过旋转桶31底部的气门312向旋转桶31通气,从而将旋转桶31底部的垃圾飞灰喷向上层,与自动喷头32相配合进一步地交互混合处置垃圾飞灰中的重金属。旋转桶31底部还设有8个凸块311,凸块311与气门312交错布置,凸块311中设有与上述底板21中相同的加热棒来加热旋转桶31内的垃圾飞灰-沥青材料,凸块311的存在有一定的搅拌作用并且可增加沥青与垃圾飞灰混合料的表面积,更好的让自动喷头32处置封存垃圾飞灰中的重金属,自动喷头32采用不锈钢材料制造。不锈钢具有良好的耐腐蚀性和机械强度,能够承受高温沥青的喷洒和长期使用。将加热电缆设置在旋转桶31的内壁中,且呈螺旋状布置的方式,在旋转桶31旋转的同时,加热电缆能够均匀地为旋转桶31和内部的垃圾飞灰-沥青材料提供热量。Preferably, as shown in Figures 1, 3, 4, and 5, the rotating disposal mechanism 3 is surrounded by asphalt delivery pipes 64 connected to the asphalt storage chamber 62. The asphalt delivery pipes 64 deliver the asphalt in the asphalt storage chamber 62 to the mixing disposal mechanism 4 for further treatment of heavy metals in the garbage fly ash. Ventilation pipes 333 are welded to the parts of the rotating disposal mechanism 3 connected to the tank body 1 on both sides. Gas is passed into the air guide pipe 341 in the rotating disposal mechanism 3 through the blowing mechanism 33. The blowing mechanism 33 uses an impeller 3341 made of high-strength engineering plastic and a volute 334 made of stainless steel. The blowing mechanism 33 is set on the side of the rotating disposal mechanism 3 and provides a stable airflow through the air inlet 331 and the air outlet 332 to ensure the uniform distribution of the garbage fly ash-asphalt material in the rotating barrel 31. Engineering plastics have good corrosion resistance and mechanical strength, while stainless steel has good high temperature resistance and corrosion resistance. The air duct 341 ventilates the rotating drum 31 through the valve 312 at the bottom of the rotating drum 31, thereby spraying the fly ash at the bottom of the rotating drum 31 toward the upper layer. This, in conjunction with the automatic nozzle 32, further interacts and mixes the heavy metals in the fly ash. The rotating drum 31 also has eight bumps 311 at the bottom. These bumps 311 are staggered with the valves 312. The bumps 311 are equipped with heating rods, similar to those in the base plate 21, to heat the fly ash-asphalt material within the rotating drum 31. The presence of the bumps 311 provides a certain stirring effect and increases the surface area of the asphalt-fly ash mixture, allowing the automatic nozzle 32 to better dispose of the heavy metals trapped in the fly ash. The automatic nozzle 32 is made of stainless steel. Stainless steel has excellent corrosion resistance and mechanical strength, capable of withstanding high-temperature asphalt spraying and long-term use. The heating cables are set in the inner wall of the rotating barrel 31 and arranged in a spiral shape. When the rotating barrel 31 rotates, the heating cables can evenly provide heat to the rotating barrel 31 and the garbage fly ash-asphalt material inside.

较佳的,旋转桶31下方设置有底盘34,底盘34与罐体1四周固定连接,相连处设置有4个接入口342将旋转桶31中的垃圾飞灰-沥青材料送入搅拌处置机构4,在接入口342附近与罐体1相连的底盘34在靠近所述接入口342时,高度由高到低向接入口342处倾斜以便于垃圾飞灰-沥青材料更好地流向搅拌处置机构4。Preferably, a chassis 34 is provided under the rotating barrel 31, and the chassis 34 is fixedly connected to the tank body 1 on all sides. Four inlets 342 are provided at the connection to deliver the garbage fly ash-asphalt material in the rotating barrel 31 into the mixing and disposal mechanism 4. The chassis 34 connected to the tank body 1 near the inlet 342 is tilted from high to low toward the inlet 342 when approaching the inlet 342 so that the garbage fly ash-asphalt material can better flow to the mixing and disposal mechanism 4.

使用时,本装置在搅拌装置61的驱动下,使得搅拌轴411旋转,进而使旋转处置机构3中的旋转桶31旋转,并配合自动喷头32完成垃圾飞灰中重金属的处置封存。在旋转桶31旋转的过程中,自动喷头32会持续喷洒,并在鼓风机构33的作用下,底部的气门312打开,将底部的垃圾飞灰-沥青材料喷向上层接受自动喷头32的喷洒处置,以确保螺旋式的下落处置单元2中未能充分处置的垃圾飞灰得到进一步处置封存。此外,在旋转处置结束后,设置于旋转桶31内的第一阀门313将会打开,使得垃圾飞灰-沥青材料流向旋转桶31下方的底盘34,从而顺着底盘34通过接入口342流向下方的搅拌处置机构4。When in use, this device is driven by the stirring device 61 to rotate the stirring shaft 411, thereby rotating the rotating barrel 31 in the rotating disposal mechanism 3, and cooperating with the automatic sprinkler 32 to complete the disposal and sealing of heavy metals in the garbage fly ash. During the rotation of the rotating barrel 31, the automatic sprinkler 32 will continue to spray, and under the action of the blowing mechanism 33, the valve 312 at the bottom will open, spraying the garbage fly ash-asphalt material at the bottom to the upper layer to be sprayed and disposed by the automatic sprinkler 32, so as to ensure that the garbage fly ash that has not been fully disposed of in the spiral falling disposal unit 2 is further disposed of and sealed. In addition, after the rotational disposal is completed, the first valve 313 set in the rotating barrel 31 will open, allowing the garbage fly ash-asphalt material to flow to the chassis 34 below the rotating barrel 31, and then flow along the chassis 34 through the inlet 342 to the stirring disposal mechanism 4 below.

实施例2,如图6所示,在搅拌轴411的底部与圆盘412相连,圆盘412外侧设置有四片搅拌桨41,搅拌桨41外围设置有4组连接管道42,便于让旋转处置机构3中的垃圾飞灰-沥青材料流入搅拌处置机构4中进行进一步的处置,4组连接管道42可与沥青输送管64相配合,在垃圾飞灰-沥青材料通入连接管道42时,进一步冲入搅拌处置机构4中进行进一步处置封存。采用加热电缆在搅拌处置机构4底部呈螺旋状布置的方式,使搅拌处置机构4在搅拌的同时加热沥青防止沥青冷却固化。搅拌桨41上方的红外线加热器43的加热元件选用石英管发热体,其具有较高的发热效率和稳定的红外线发射率,在搅拌过程中加热沥青使沥青保持良好的流动性,在搅拌处置机构4底部设置有第二阀门44,可将搅拌处置后的垃圾飞灰-沥青材料送入冷却处置机构5中。在冷却处置机构5顶部设置有两个搅拌件52将搅拌处置机构4中流下的垃圾飞灰-沥青材料甩入四周的冷却罐51上。In Example 2, as shown in Figure 6 , the bottom of the stirring shaft 411 is connected to a disk 412. Four stirring paddles 41 are positioned outside the disk 412. Four sets of connecting pipes 42 are located around the paddles 41, facilitating the flow of fly ash-asphalt material from the rotating disposal mechanism 3 into the mixing and disposal mechanism 4 for further disposal. These four connecting pipes 42 cooperate with the asphalt delivery pipe 64. Once the fly ash-asphalt material enters the connecting pipes 42, it is further flushed into the mixing and disposal mechanism 4 for further disposal and storage. Heating cables are arranged in a spiral pattern at the bottom of the mixing and disposal mechanism 4, allowing the mixing and disposal mechanism 4 to heat the asphalt while stirring, preventing it from cooling and solidifying. The infrared heater 43 above the stirring paddles 41 uses a quartz tube heating element as its heating element, which has high heating efficiency and stable infrared emissivity. This heating element heats the asphalt during the stirring process, maintaining good fluidity. A second valve 44 is located at the bottom of the mixing and disposal mechanism 4, allowing the fly ash-asphalt material to be transported to the cooling and disposal mechanism 5 after stirring. Two stirring members 52 are provided on the top of the cooling and disposal mechanism 5 to throw the garbage fly ash-asphalt material flowing out of the stirring and disposal mechanism 4 into the cooling tanks 51 around it.

如图7所示,冷却罐51的外壁上连接着液氮冷却室54,液氮冷却室54采用高强度铝合金材料制造。液氮冷却室54设置于冷却罐51外侧,通过液氮的快速冷却作用,能够迅速降低垃圾飞灰-沥青材料的温度,确保其快速固化。如图8所示,在电动机523的驱动下,连接轴522旋转带动转动桨521旋转,从而将搅拌处置机构4落下的垃圾飞灰-沥青材料做最后的搅拌处置,搅拌件52两侧设置有两个沥青喷洒管53,冷却罐51的底部设置有第三阀门56,最终垃圾飞灰-沥青材料通过第三阀门56到达材料存储罐65。As shown in Figure 7 , the outer wall of the cooling tank 51 is connected to a liquid nitrogen cooling chamber 54, which is made of a high-strength aluminum alloy. Liquid nitrogen cooling chamber 54 is located outside the cooling tank 51. Through the rapid cooling effect of liquid nitrogen, the temperature of the fly ash-asphalt material can be quickly reduced, ensuring its rapid solidification. As shown in Figure 8 , driven by the motor 523, the connecting shaft 522 rotates, driving the rotating paddle 521 to rotate, thereby performing the final mixing and disposal of the fly ash-asphalt material dropped from the mixing and disposal mechanism 4. Two asphalt spray pipes 53 are provided on both sides of the stirring element 52. A third valve 56 is provided at the bottom of the cooling tank 51. Finally, the fly ash-asphalt material passes through the third valve 56 and reaches the material storage tank 65.

使用时,通过下落处置单元2以及旋转处置机构3与垃圾飞灰的交互混合后,垃圾飞灰-沥青材料从连接管道42中流下,同时沥青输送管64中的第六阀门641打开,沥青从沥青输送管64底部冲出,将垃圾飞灰-沥青材料冲进搅拌处置机构4进行搅拌处置,搅拌完成后搅拌处置机构4底部的第二阀门44打开,垃圾飞灰-沥青材料流向冷却处置机构5中。在搅拌件52的两侧设置有两个沥青喷洒管53,通过沥青喷洒管53喷出沥青。搅拌件52将垃圾飞灰-沥青材料甩向冷却罐51的同时,沥青喷洒管53喷洒沥青进行最后的喷洒处置,最后在液氮冷却室54的作用下,冷却罐51中的垃圾飞灰-沥青材料冷却凝结成块。冷却处置完成后冷却处置机构5底部的第三阀门56打开,垃圾飞灰-沥青材料掉入材料存储罐65中,待材料存储罐65装满后打开外部的拉门,将材料存储罐65取出。During use, after interactive mixing with the fly ash through the falling disposal unit 2 and the rotating disposal mechanism 3, the fly ash-asphalt material flows down from the connecting pipe 42. At the same time, the sixth valve 641 in the asphalt delivery pipe 64 opens, and asphalt is flushed out from the bottom of the asphalt delivery pipe 64, flushing the fly ash-asphalt material into the mixing disposal mechanism 4 for mixing and disposal. After the mixing is completed, the second valve 44 at the bottom of the mixing disposal mechanism 4 opens, and the fly ash-asphalt material flows into the cooling disposal mechanism 5. Two asphalt spraying pipes 53 are provided on both sides of the stirring member 52, through which asphalt is sprayed. While the stirring member 52 throws the fly ash-asphalt material toward the cooling tank 51, the asphalt spraying pipes 53 spray asphalt for the final spraying treatment. Finally, under the action of the liquid nitrogen cooling chamber 54, the fly ash-asphalt material in the cooling tank 51 is cooled and condensed into blocks. After the cooling treatment is completed, the third valve 56 at the bottom of the cooling treatment mechanism 5 is opened, and the garbage fly ash-asphalt material falls into the material storage tank 65. After the material storage tank 65 is full, the external sliding door is opened and the material storage tank 65 is taken out.

实施例3,为本发明的第四个实施例,取一定量的某垃圾焚烧电厂的布袋飞灰,测定其基本成分和重金属含量。将飞灰通过本发明的基于沥青介质的垃圾飞灰多层立体化处置装置进行处理后,从垃圾飞灰-沥青材料储存罐取出经过多重立体处置后的垃圾飞灰-沥青材料,制成40mm×40mm×50mm的试块,进行重金属浸出浓度测定,通过本装置处置前后的垃圾飞灰重金属浸出浓度计算出本装置对于垃圾飞灰重金属浸出的抑制率。Example 3, the fourth example of the present invention, measured a certain amount of bagged fly ash from a waste incineration power plant to determine its basic composition and heavy metal content. After treating the fly ash using the present invention's multi-layered, three-dimensional fly ash treatment device based on an asphalt medium, the fly ash-asphalt material, after undergoing the multi-layered, three-dimensional treatment, was removed from the fly ash-asphalt material storage tank and fabricated into 40 mm x 40 mm x 50 mm test blocks. The heavy metal leaching concentrations were then measured. The inhibition rate of heavy metal leaching from the fly ash by the device was calculated based on the heavy metal leaching concentrations before and after treatment.

对比例1Comparative Example 1

采用水泥固化垃圾飞灰,并通过水泥固化前后的垃圾飞灰重金属浸出浓度计算出水泥对于垃圾飞灰重金属浸出的抑制率。垃圾飞灰来源于我国某垃圾焚烧电厂的布袋飞灰,并测定其基本成分和重金属含量。水泥类型为42.5#普通硅酸盐水泥,在1000g垃圾飞灰中加入200g水泥在搅拌锅中充分搅拌均匀后,将水泥固化处理飞灰后注入尺寸为40mm×40mm×50mm模具中制成试块,在振动台上振动成型后于室内标准养护条件下养护28d(养护环境的相对湿度保持在95%以上,温度保持在20℃±2℃)。Cement was used to solidify fly ash, and the inhibition rate of heavy metal leaching from fly ash was calculated based on the heavy metal leaching concentrations before and after cement solidification. The fly ash was sourced from bagged fly ash from a waste incineration power plant in my country, and its basic composition and heavy metal content were determined. 42.5# ordinary Portland cement was used. 200g of cement was added to 1000g of fly ash and thoroughly mixed in a mixing pot. The cement-solidified fly ash was then poured into a 40mm x 40mm x 50mm mold to produce a test block. After being vibrated on a vibration table and formed, the blocks were cured indoors under standard curing conditions for 28 days (relative humidity maintained above 95% and temperature maintained at 20°C ± 2°C).

对比例2Comparative Example 2

采用沥青固化垃圾飞灰,并通过沥青固化前后的垃圾飞灰重金属浸出浓度计算出沥青对于垃圾飞灰重金属浸出的抑制率。垃圾飞灰来源于我国某垃圾焚烧电厂的布袋飞灰,并测定其基本成分和重金属含量。沥青类型为AH-70重交通道路沥青,在1000g垃圾飞灰中加入沥青600g,采用沥青拌合锅,拌合温度为160℃,将沥青和飞灰充分搅拌混合,搅拌时间为3分钟,最后将垃圾飞灰-沥青胶浆倒入40mm×40mm×50mm模具中制成试块。Asphalt was used to solidify fly ash, and the inhibition rate of heavy metal leaching from fly ash was calculated based on the heavy metal leaching concentrations before and after asphalt solidification. The fly ash was sourced from bagged fly ash from a waste incineration power plant in my country, and its basic composition and heavy metal content were determined. AH-70 heavy-duty road asphalt was used. 600g of asphalt was added to 1000g of fly ash. The asphalt and fly ash were thoroughly mixed in an asphalt mixing kettle at 160°C for 3 minutes. The fly ash-asphalt mortar was then poured into a 40mm x 40mm x 50mm mold to form a test block.

对比例3Comparative Example 3

采用螯合剂固化垃圾飞灰,并通过螯合剂固化前后的垃圾飞灰重金属浸出浓度计算出螯合剂对于垃圾飞灰重金属浸出的抑制率。垃圾飞灰来源于广东某垃圾焚烧电厂的布袋飞灰,并测定其基本成分和重金属含量。螯合剂的主要成分为二甲基二硫代氨基甲酸盐,在1000g的垃圾飞灰中加入40g螯合剂,垃圾飞灰与螯合剂在混炼机内充分混炼10min(温度控制在20-30℃)后,制成40mm×40mm×50mm的试块。A chelating agent was used to solidify fly ash. The inhibition rate of heavy metal leaching from the fly ash was calculated based on the heavy metal leaching concentrations before and after chelating. The fly ash was sourced from bagged fly ash from a waste incineration power plant in Guangdong Province, and its basic composition and heavy metal content were determined. The chelating agent, primarily dimethyldithiocarbamate, was added to 1000g of fly ash. The fly ash and chelating agent were thoroughly mixed in a mixer for 10 minutes (temperature controlled at 20-30°C) before being formed into 40mm×40mm×50mm test blocks.

根据《固体废物浸出毒性浸出方法醋酸缓冲溶液法》(HJ/T300-2007)测定实施例1、对比例1、对比例2以及对比例3原飞灰中的Pb、Cr、Cd、Ni、Cu和Zn的重金属浸出浓度。采用《固体废物浸出毒性浸出方法硫酸硝酸法》(HJ/T 299-2007)对实施例1、对比例1、对比例2以及对比例3中的固化试块进行试样制备和重金属浸出浓度的测试,并获取不同试样的重金属浸出浓度。采用浸出浓度计算相应的重金属浸出抑制率,其中重金属浸出抑制率=()×100%,C前是固化前垃圾飞灰重金属浸出浓度,C后是固化后垃圾飞灰重金属浸出浓度,测试结果如下表一、表二所示:The heavy metal leaching concentrations of Pb, Cr, Cd, Ni, Cu and Zn in the raw fly ash of Example 1, Comparative Example 1, Comparative Example 2 and Comparative Example 3 were determined according to the "Solid Waste Leaching Toxicity Leaching Method - Acetate Buffer Solution Method" (HJ/T300-2007). The solidified test blocks in Example 1, Comparative Example 1, Comparative Example 2 and Comparative Example 3 were prepared and tested for heavy metal leaching concentrations using the "Solid Waste Leaching Toxicity Leaching Method - Sulfuric Acid and Nitric Acid Method" (HJ/T 299-2007), and the heavy metal leaching concentrations of different samples were obtained. The corresponding heavy metal leaching inhibition rate was calculated using the leaching concentration, where the heavy metal leaching inhibition rate = ( )×100%, Cbefore is the heavy metal leaching concentration of garbage fly ash before solidification, and Cafter is the heavy metal leaching concentration of garbage fly ash after solidification. The test results are shown in Table 1 and Table 2 below:

表一 :实施例及对比例的垃圾飞灰重金属浸出浓度Table 1: Heavy metal leaching concentrations of fly ash from examples and comparative examples

表二:实施例及对比例的垃圾飞灰重金属浸出抑制率Table 2: Heavy metal leaching inhibition rate of fly ash of examples and comparative examples

根据表二可以看出,通过本装置处置后制成的试块的垃圾飞灰各重金属元素浸出的抑制率相对于对比例1(采用水泥固化)、对比例2(采用沥青固化)以及对比例3(采用螯合剂固化)的重金属浸出的抑制率均有显著提高,平均提高幅度分别为23.45%、21.75%和22.48%,由此可知本发明的基于沥青介质的垃圾飞灰多层立体化处置装置能够大幅降低垃圾飞灰中重金属的浸出。According to Table 2, it can be seen that the inhibition rate of leaching of various heavy metal elements in the garbage fly ash of the test blocks prepared after treatment by this device is significantly improved compared with the inhibition rate of heavy metal leaching in Comparative Example 1 (solidified by cement), Comparative Example 2 (solidified by asphalt) and Comparative Example 3 (solidified by chelating agent), with the average increase being 23.45%, 21.75% and 22.48% respectively. It can be seen that the multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium of the present invention can greatly reduce the leaching of heavy metals in garbage fly ash.

应说明的是,以上实施例仅用于说明本发明的技术方案而非限制,尽管参照较佳实施例对本发明进行了详细说明,本领域的普通技术人员应当理解,可以对本发明的技术方案进行修改或者等同替换,而不脱离本发明技术方案的精神和范围,其均应涵盖在本发明的权利要求范围当中。It should be noted that the above embodiments are only used to illustrate the technical solutions of the present invention and are not intended to limit the present invention. Although the present invention has been described in detail with reference to preferred embodiments, those skilled in the art should understand that the technical solutions of the present invention may be modified or replaced by equivalents without departing from the spirit and scope of the technical solutions of the present invention, which should all be included in the scope of the claims of the present invention.

Claims (10)

1. A multi-layer three-dimensional disposal device for garbage fly ash based on asphalt medium is characterized by comprising,
A tank body (1);
A falling treatment unit (2) arranged above the tank body (1), wherein the falling treatment unit (2) comprises a bottom plate (21), an oleophobic coating (22) arranged on the surface of the bottom plate (21), an asphalt sprayer (23) arranged on the inner wall of the tank body (1), and a baffle plate (24) arranged at the lower end of the bottom plate (21);
A rotary disposal mechanism (3) positioned below the falling disposal unit (2), wherein the rotary disposal mechanism (3) comprises a rotary barrel (31) positioned in the middle of the tank body (1), an automatic spray head (32) positioned above the rotary barrel (31), a blast mechanism (33) arranged on the side surface of the rotary barrel (31), and a chassis (34) arranged below the rotary barrel (31);
a stirring treatment mechanism (4) positioned below the rotary treatment mechanism (3), a cooling treatment mechanism (5) arranged below the stirring treatment mechanism (4), and a base piece (6) arranged on the tank body (1).
2. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 1, wherein a plurality of protruding blocks (311) are arranged on the inner wall of the bottom of the rotary barrel (31), air valves (312) are arranged between the protruding blocks (311), and a first valve (313) is arranged at the bottom of the rotary barrel (31).
3. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 2, wherein the air blowing mechanism (33) comprises an air inlet (331) formed on the inner wall of the tank body (1), a ventilation pipe (333) communicated with the air inlet (331), and an air outlet (332) connected with the other end of the ventilation pipe (333);
The air blowing mechanism (33) further comprises a volute (334) arranged in the middle of the ventilation pipe (333);
An impeller (3341) and a bearing (3342) connected with the impeller (3341) are arranged in the volute (334).
4. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 3, wherein a plurality of groups of air ducts (341) are arranged inside the chassis (34), and an access opening (342) is reserved on the surface of the chassis (34);
Wherein, air duct (341) links to each other with air outlet (332).
5. A multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 4, wherein the stirring disposal mechanism (4) comprises a stirring paddle (41), a connecting pipeline (42) arranged on the side surface of the stirring paddle (41), an infrared heater (43) positioned above the stirring paddle (41), and a second valve (44) arranged between the stirring paddle (41) and below;
the inner end of the stirring paddle (41) is provided with a disc (412), and the inside of the disc (412) is fixedly connected with a stirring shaft (411).
6. A multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 5, wherein the cooling disposal mechanism (5) comprises a cooling tank (51) arranged below the tank body (1), a stirring piece (52) arranged above the cooling tank (51), an asphalt spraying pipe (53) arranged on the side surface of the stirring piece (52), and a liquid nitrogen cooling chamber (54) arranged outside the cooling tank (51), and the cooling disposal mechanism (5) further comprises a conveying port (55) arranged on the side surface of the liquid nitrogen cooling chamber (54), and a third valve (56) arranged at the bottom of the cooling tank (51).
7. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 6, wherein the stirring piece (52) comprises a rotating paddle (521) arranged on the upper side inside the cooling tank (51) and close to the second valve (44), a connecting shaft (522) for connecting the rotating paddle (521), and a motor (523) arranged on the surface of the cooling tank (51).
8. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 7, wherein the base member (6) comprises a stirring device (61), an asphalt storage chamber (62) positioned on the side surface of the upper end of the tank body (1), and a waste fly ash storage tank (63) positioned on the upper end of the tank body (1);
the base member (6) further comprises an asphalt delivery pipe (64) connected below the asphalt storage chamber (62), and a material storage tank (65) located at the lower end of the tank body (1).
9. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 8, wherein a fourth valve (631) is arranged at the bottom of the waste fly ash storage tank (63), and a waste fly ash feed inlet (632) is arranged above the waste fly ash storage tank (63);
wherein the bottom surface of the garbage fly ash storage tank (63) is obliquely arranged;
An asphalt feeding port (621) is reserved at the outer side of the asphalt storage chamber (62), a fifth valve (622) is arranged between the asphalt storage chamber (62) and the asphalt conveying pipe (64), and a sixth valve (623) is arranged between the asphalt storage chamber (62) and the automatic spray head (32).
10. The multi-layer three-dimensional disposal device for waste fly ash based on asphalt medium according to claim 9, wherein the asphalt delivery pipe (64) is connected with the stirring disposal mechanism (4) through a sixth valve (641).
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Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0949207A (en) * 1995-08-07 1997-02-18 Hokuriku Asukon Kk Aggregate recovery method and equipment for asphalt waste
JPH09225431A (en) * 1996-02-23 1997-09-02 Hitachi Zosen Corp Fly ash treatment method and equipment in refuse incineration facility

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* Cited by examiner, † Cited by third party
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CN105693123B (en) * 2016-03-10 2018-04-10 重庆三峰环境产业集团有限公司 The method and its clean applications in bituminous paving that domestic garbage incineration flyash is granulated altogether with cement, silicon ash, flyash
CN106167689B (en) * 2016-07-20 2017-12-19 陈刚才 A kind of incineration firing flying dust bituminous concrete binding material and bituminous concrete
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Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0949207A (en) * 1995-08-07 1997-02-18 Hokuriku Asukon Kk Aggregate recovery method and equipment for asphalt waste
JPH09225431A (en) * 1996-02-23 1997-09-02 Hitachi Zosen Corp Fly ash treatment method and equipment in refuse incineration facility

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