CN107830527A - Waste treatment device and waste treatment method - Google Patents
Waste treatment device and waste treatment method Download PDFInfo
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- CN107830527A CN107830527A CN201711265173.6A CN201711265173A CN107830527A CN 107830527 A CN107830527 A CN 107830527A CN 201711265173 A CN201711265173 A CN 201711265173A CN 107830527 A CN107830527 A CN 107830527A
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/006—General arrangement of incineration plant, e.g. flow sheets
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/80—Shredding
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/20—Waste heat recuperation using the heat in association with another installation
- F23G2206/203—Waste heat recuperation using the heat in association with another installation with a power/heat generating installation
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J2215/00—Preventing emissions
- F23J2215/10—Nitrogen; Compounds thereof
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- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E20/00—Combustion technologies with mitigation potential
- Y02E20/12—Heat utilisation in combustion or incineration of waste
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
Description
技术领域technical field
本发明涉及废物处理技术领域,尤其是涉及一种废物处理装置及废物处理方法。The invention relates to the technical field of waste treatment, in particular to a waste treatment device and a waste treatment method.
背景技术Background technique
传统的废物处置是通过焚烧方式进行处理,焚烧技术是一种高温热处理技术,即以一定量的过剩空气与被处理的有机废物在焚烧炉内进行氧化燃烧反应,废物中的有害有毒物质在高温下氧化、热解而被破坏,是一种可同时实现废物无害化、减量化、资源化的处理技术。但焚烧过程中会产生焚烧残余物,包括焚烧废物产生的飞灰、残渣、氮氧化合物及酸性气体,飞灰中包含着有毒物质二噁英颗粒,残渣中包含重金属等物质,如若将上述焚烧的产物直接排到空气中,将会造成空气的污染。Traditional waste disposal is processed by incineration. Incineration technology is a high-temperature heat treatment technology, that is, a certain amount of excess air is oxidized and burned in an incinerator with the organic waste to be processed. Harmful and toxic substances in the waste It is a treatment technology that can simultaneously realize waste harmlessness, reduction, and resource utilization. However, the incineration process will produce incineration residues, including fly ash, residue, nitrogen oxides and acid gases produced by incineration of waste. The fly ash contains toxic dioxin particles, and the residue contains heavy metals and other substances. If the above incineration If the product is discharged directly into the air, it will cause air pollution.
本申请人发现现有技术至少存在以下技术问题:The applicant finds that the prior art has at least the following technical problems:
现有的废物处理装置在排放焚烧产物时存在环境污染的问题。The existing waste treatment device has the problem of environmental pollution when discharging incineration products.
发明内容Contents of the invention
本发明的目的在于提供一种废物处理装置及废物处理方法,以解决现有技术中存在的废物处理装置排放焚烧产物时造成环境污染的技术问题。本发明提供的诸多技术方案中的优选技术方案所能产生的诸多技术效果详见下文阐述。The object of the present invention is to provide a waste treatment device and a waste treatment method to solve the technical problem of environmental pollution caused by waste treatment devices discharging incineration products in the prior art. The many technical effects that can be produced by the preferred technical solutions among the many technical solutions provided by the present invention are described in detail below.
为实现上述目的,本发明提供了以下技术方案:To achieve the above object, the present invention provides the following technical solutions:
本发明提供的一种废物处理装置,包括废物预处理装置、废物熔融炉、飞灰收集装置和气体净化装置,其中,A waste treatment device provided by the present invention includes a waste pretreatment device, a waste melting furnace, a fly ash collection device and a gas purification device, wherein,
所述废物预处理装置与所述废物熔融炉相连通,废物经过所述废物预处理装置后能进入所述废物熔融炉并在所述废物熔融炉内焚烧,所述废物熔融炉均与所述飞灰收集装置以及所述气体净化装置相连通;The waste pretreatment device is connected with the waste melting furnace, and waste can enter the waste melting furnace after passing through the waste pretreatment device and be incinerated in the waste melting furnace, and the waste melting furnace is connected with the waste melting furnace The fly ash collection device and the gas purification device are connected;
所述废物熔融炉包括熔融排渣口和废气排出口,废物在所述废物熔融炉内焚烧产生的废渣在所述废物熔融炉的底部受热成熔融态后能从所述熔融排渣口排出形成无害固态物质,废物在所述废物熔融炉内焚烧后产生的二噁英在所述废物熔融炉内燃烧后能转成无毒性物质,所述飞灰收集装置能收集从所述废气排出口排出的部分或全部飞灰并将飞灰输送至所述废物熔融炉内使飞灰在所述废物熔融炉内受热成熔融态,所述气体净化装置能净化从所述废气排出口排出的气体且净化后的气体排入大气。The waste melting furnace includes a melting slag outlet and a waste gas outlet, and the waste slag generated by incineration of waste in the waste melting furnace can be discharged from the melting slag outlet after being heated to a molten state at the bottom of the waste melting furnace to form Harmless solid matter, the dioxin produced after the waste is incinerated in the waste melting furnace can be converted into non-toxic substances after being burned in the waste melting furnace, and the fly ash collecting device can be collected from the waste gas outlet Part or all of the fly ash is discharged and transported to the waste melting furnace so that the fly ash is heated into a molten state in the waste melting furnace, and the gas purification device can purify the gas discharged from the waste gas outlet And the purified gas is discharged into the atmosphere.
优选地,所述废物处理装置还包括余热回收装置,所述余热回收装置与所述废气排出口相连通;所述余热回收装置为余热锅炉。Preferably, the waste treatment device further includes a waste heat recovery device, and the waste heat recovery device is in communication with the exhaust gas outlet; the waste heat recovery device is a waste heat boiler.
优选地,所述废物熔融炉包括焚烧熔融部、燃烧部和连接所述焚烧熔融部和所述燃烧部的锥形连接部,所述焚烧熔融部、所述锥形连接部和所述燃烧部从下到上依次设置,靠近所述焚烧熔融部的底端设置有所述熔融排渣口,所述燃烧部的顶端设置有所述废气排出口;Preferably, the waste melting furnace includes an incineration melting part, a combustion part and a conical connecting part connecting the incineration melting part and the burning part, the incineration melting part, the conical connecting part and the burning part Arranged sequentially from bottom to top, the melting and slag discharge port is provided near the bottom end of the incineration and melting part, and the waste gas discharge port is provided at the top of the combustion part;
所述焚烧熔融部还包括废物焚烧部和废渣熔融部,所述废物焚烧部设置在所述废渣熔融部的上方且所述废物焚烧部与所述废渣熔融部连接,废物在所述废物焚烧部燃烧、废渣在所述废渣熔融部受热。The incineration and melting part also includes a waste incineration part and a waste slag melting part, the waste incineration part is arranged above the waste slag melting part and the waste incineration part is connected to the waste slag melting part, and waste is collected in the waste incineration part Combustion and waste slag are heated in the waste slag melting part.
优选地,所述焚烧熔融部和所述燃烧部均为圆柱形,所述燃烧部与所述焚烧熔融部直径比的范围为1.5~3;靠近所述焚烧熔融部底端的侧面上均匀设置有主加热源,所述主加热源为燃烧器或等离子体发生器的一种或几种;所述燃烧部的侧壁上均匀的设置有副加热源,所述副加热源为燃烧器或等离子体发生器的一种或几种。Preferably, both the incineration melting part and the burning part are cylindrical, and the diameter ratio of the burning part to the burning melting part ranges from 1.5 to 3; A main heating source, the main heating source is one or more of a burner or a plasma generator; a secondary heating source is uniformly arranged on the side wall of the combustion part, and the secondary heating source is a burner or a plasma generator One or several body generators.
优选地,所述废物焚烧部和所述燃烧部内均通有辅助燃烧的气化剂,废物在缺氧的环境下燃烧、二噁英在富氧的环境下燃烧。Preferably, both the waste incineration part and the combustion part are passed through a gasification agent for auxiliary combustion, waste is burned in an oxygen-deficient environment, and dioxins are burned in an oxygen-enriched environment.
优选地,所述废物熔融炉采用耐热钢材质制成;所述废物熔融炉的内侧壁上沿从内向外的方向依次设置有绝热层、耐热层和耐高温腐蚀层。Preferably, the waste melting furnace is made of heat-resistant steel; the inner wall of the waste melting furnace is sequentially provided with a heat-insulating layer, a heat-resistant layer and a high-temperature corrosion-resistant layer along the direction from the inside to the outside.
优选地,所述废物预处理装置包括废物贮仓和破碎机,待破碎的废物经过所述破碎机处理后输送至所述废物贮仓,所述废物贮仓内的废物经过螺旋给料机进入所述废物熔融炉内;破碎后的废物长度小于100mm。Preferably, the waste pretreatment device includes a waste storage bin and a crusher, the waste to be crushed is transported to the waste storage bin after being processed by the crusher, and the waste in the waste storage bin enters through a screw feeder In the waste melting furnace; the length of the crushed waste is less than 100mm.
优选地,所述气体净化装置包括除酸塔和脱硝装置,所述余热回收装置、所述除酸塔、所述飞灰收集装置和所述脱硝装置依次设置;Preferably, the gas purification device includes an acid removal tower and a denitration device, and the waste heat recovery device, the acid removal tower, the fly ash collection device and the denitration device are arranged in sequence;
所述废物处理装置还包括引风机,所述引风机驱动所述脱硝装置内的气体从烟囱排出。The waste treatment device also includes an induced fan, which drives the gas in the denitrification device to be discharged from the chimney.
一种利用所述的废物处理装置处理废物的废物处理方法,包括以下步骤:A waste treatment method utilizing the waste treatment device to treat waste, comprising the following steps:
S1、预处理废物;S1. Pretreatment of waste;
S2、废物通过所述螺旋给料机输送至所述废物熔融炉内;S2. The waste is transported into the waste melting furnace through the screw feeder;
S3、废物在所述废物熔融炉内燃烧;S3, waste is burned in the waste melting furnace;
S4、产生的熔融态废渣从所述熔融排渣口排出,从所述废气排出口排出的飞灰被所述飞灰收集装置收集后输送至所述焚烧熔融部,从所述废气排出口排出的气体经过所述气体净化装置后排入大气。S4. The generated molten waste slag is discharged from the melting slag discharge port, and the fly ash discharged from the waste gas discharge port is collected by the fly ash collection device and then transported to the incineration and melting part, and discharged from the waste gas discharge port The gas is discharged into the atmosphere after passing through the gas purification device.
优选地,步骤S4还包括以下步骤:Preferably, step S4 also includes the following steps:
S41、从所述熔融排渣口排出废渣经过废渣池水冷后形成玻璃体,从所述废气排出口排出的飞灰依次经过所述余热回收装置、所述除酸塔后进入所述飞灰收集装置内;从所述废气排出口排出的气体依次经过所述余热回收装置、所述除酸塔、所述飞灰收集装置以及所述脱硝装置并在所述引风机的驱动下从烟囱中排出。S41. The waste slag discharged from the melting slag discharge port is water-cooled in the waste slag pool to form a glass body, and the fly ash discharged from the waste gas discharge port passes through the waste heat recovery device, the acid removal tower, and then enters the fly ash collection device Inside; the gas discharged from the exhaust gas outlet passes through the waste heat recovery device, the acid removal tower, the fly ash collection device and the denitrification device in sequence, and is discharged from the chimney driven by the induced draft fan.
本发明提供一种废物处理装置及废物处理方法,以解决现有技术中存在的废物处理装置排放焚烧产物时造成环境污染的技术问题,本发明的废物处理装置能将废渣加热成熔融态且熔融态的废渣急冷成玻璃体,避免重金属从废渣中溢出、能将二噁英分解成无毒性物质、能将飞灰收集并输送至废物熔融炉内、能将废气净化后排入大气,降低焚烧废物时对空气造成的污染;余热回收装置可用以回收热量,减小能量的浪费;废物熔融炉的结构以热源分布能够在废渣被熔融、二噁英被分解的情况下节省能源;废物在氧气不足下的条件下燃烧能降低二噁英的生成,从燃烧的方式上降低二噁英的产生,降低分解二噁英需要的热量;二噁英在富氧的条件下能充分分解,从燃烧方式上避免二噁英排入大气;除酸塔和脱硝装置分别用来去除气体中的酸性气体和氮氧化合物。The invention provides a waste treatment device and a waste treatment method to solve the technical problem of environmental pollution caused by the waste treatment device discharging incineration products in the prior art. The waste treatment device of the invention can heat the waste residue into a molten state and melt it The waste slag in the state is quenched into a glass body to prevent heavy metals from overflowing from the waste slag, decompose dioxins into non-toxic substances, collect fly ash and transport them to the waste melting furnace, purify the waste gas and discharge it into the atmosphere, and reduce incineration waste The waste heat recovery device can be used to recover heat and reduce energy waste; the structure of the waste melting furnace and the distribution of heat sources can save energy when the waste slag is melted and dioxins are decomposed; waste in the absence of oxygen Combustion under low conditions can reduce the formation of dioxins, reduce the production of dioxins from the combustion method, and reduce the heat required for decomposition of dioxins; dioxins can be fully decomposed under oxygen-enriched conditions, and from the combustion method In order to prevent dioxins from being discharged into the atmosphere; the acid removal tower and the denitration device are used to remove acid gases and nitrogen oxides in the gas respectively.
附图说明Description of drawings
为了更清楚地说明本发明实施例或现有技术中的技术方案,下面将对实施例或现有技术描述中所需要使用的附图作简单地介绍,显而易见地,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 in the embodiments of the present invention or the prior art, the following will briefly introduce the drawings that need to be used in the description of the embodiments or the prior art. Obviously, the accompanying drawings in the following description are only These are some embodiments of the present invention. Those skilled in the art can also obtain other drawings based on these drawings without creative work.
图1是废物处理装置的结构示意图;Fig. 1 is the structural representation of waste disposal device;
图2是废物熔融炉的结构示意图。Fig. 2 is a schematic structural diagram of a waste melting furnace.
图中1-废物预处理装置;110-废物贮仓;120-破碎机;2-废物熔融炉;21-熔融排渣口;22-废气排出口;23-焚烧熔融部;231-废物焚烧部;232-废渣熔融部;24-燃烧部;25-锥形连接部;26-绝热层;27-耐热层;28-耐高温腐蚀层;3-飞灰收集装置;4-余热回收装置;5-主加热源;6-副加热源;7-螺旋给料机;8-除酸塔;9-脱硝装置;10-引风机;11-废渣池;12-烟囱。In the figure 1-waste pretreatment device; 110-waste storage bin; 120-crusher; 2-waste melting furnace; 21-melting slag outlet; 22-exhaust gas outlet; ;232-waste slag melting part; 24-combustion part; 25-conical connection part; 26-heat insulation layer; 27-heat-resistant layer; 28-high temperature corrosion resistance layer; 3-fly ash collection device; 5-main heating source; 6-subsidiary heating source; 7-screw feeder; 8-acid removal tower; 9-denitration device; 10-induced fan; 11-waste residue pool; 12-chimney.
具体实施方式Detailed ways
为使本发明的目的、技术方案和优点更加清楚,下面将对本发明的技术方案进行详细的描述。显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动的前提下所得到的所有其它实施方式,都属于本发明所保护的范围。In order to make the purpose, technical solution and advantages of the present invention clearer, the technical solution of the present invention will be described in detail below. Apparently, the described embodiments are only some of the embodiments of the present invention, but not all of them. Based on the embodiments of the present invention, all other implementations obtained by persons of ordinary skill in the art without making creative efforts fall within the protection scope of the present invention.
本发明提供了一种废物处理装置,包括废物预处理装置1、废物熔融炉2、飞灰收集装置3和气体净化装置,其中,废物预处理装置1与废物熔融炉2相连通,废物经过废物预处理装置1后能进入废物熔融炉2并在废物熔融炉2内焚烧,废物熔融炉2均与飞灰收集装置3以及气体净化装置相连通;The invention provides a waste treatment device, comprising a waste pretreatment device 1, a waste melting furnace 2, a fly ash collection device 3 and a gas purification device, wherein the waste pretreatment device 1 is connected with the waste melting furnace 2, and the waste passes through the waste After the pretreatment device 1, it can enter the waste melting furnace 2 and burn in the waste melting furnace 2, and the waste melting furnace 2 is connected with the fly ash collecting device 3 and the gas purification device;
废物熔融炉2包括熔融排渣口21和废气排出口22,废物在废物熔融炉2内焚烧产生的废渣在废物熔融炉2的底部受热成熔融态后能从熔融排渣口21排出形成无害固态物质,废物在废物熔融炉2内焚烧后产生的二噁英在废物熔融炉2内燃烧后能转成无毒性物质,飞灰收集装置3能收集从废气排出口22排出的部分或全部飞灰并将飞灰输送至废物熔融炉2内使飞灰在废物熔融炉2内受热成熔融态,气体净化装置能净化从废气排出口22排出的气体且净化后的气体排入大气。废渣中残留有重金属等有毒物质,从熔融排渣口21排出的废渣经过冷却处理形成固态物质,固态物质可以是玻璃体,将重金属等有毒物质固化在玻璃体内,毒物浸出极低,降低重金属对环境的污染,同时,可以将玻璃体作为普通废物处理或作为路基材料,大大减小了废物的填埋量;二噁英在废物熔融炉2内燃烧后能转成无毒性物质,避免二噁英排放到空气中对人类的生存环境造成危害;飞灰收集装置3能收集从废气排出口22排出的部分或全部飞灰并将飞灰输送至废物熔融炉2内使飞灰在废物熔融炉2内受热成熔融态,最终也固化在玻璃体内,飞灰属于危险废物,直接排放大气会造成环境污染,本发明装置降低飞灰的排出量,降低焚烧废物时飞灰对环境的污染;气体净化装置能净化从废气排出口22排出的气体且净化后的气体排入大气,降低酸性气体或氮氧化合物等对环境污染,解决现有技术中存在的废物处理装置排放焚烧产物时造成环境污染的技术问题,本发明装置降低焚烧废物时对环境造成的污染。The waste melting furnace 2 includes a melting slagging port 21 and a waste gas discharge port 22. The waste slag produced by incineration of waste in the waste melting furnace 2 can be discharged from the melting slagging port 21 after being heated into a molten state at the bottom of the waste melting furnace 2 to form a harmless gas. Solid matter, the dioxin produced after the waste is burned in the waste melting furnace 2 can be converted into non-toxic substances after being burned in the waste melting furnace 2, and the fly ash collection device 3 can collect part or all of the fly ash discharged from the exhaust gas outlet 22. ash and transport the fly ash to the waste melting furnace 2 so that the fly ash is heated into a molten state in the waste melting furnace 2, the gas purification device can purify the gas discharged from the waste gas outlet 22 and the purified gas is discharged into the atmosphere. Toxic substances such as heavy metals remain in the waste slag, and the waste slag discharged from the molten slag outlet 21 is cooled to form a solid substance. The solid substance can be a vitreous body, and the toxic substances such as heavy metals are solidified in the vitreous body, and the leaching of toxic substances is extremely low, reducing the impact of heavy metals on the environment. At the same time, the glass body can be treated as ordinary waste or used as a roadbed material, which greatly reduces the amount of landfill waste; dioxins can be converted into non-toxic substances after burning in the waste melting furnace 2, so as to avoid the discharge of dioxins In the air, it will cause harm to the living environment of human beings; the fly ash collection device 3 can collect part or all of the fly ash discharged from the exhaust gas outlet 22 and transport the fly ash to the waste melting furnace 2 to make the fly ash in the waste melting furnace 2 It is heated into a molten state and finally solidified in the glass body. Fly ash is a hazardous waste, and direct discharge into the atmosphere will cause environmental pollution. The device of the present invention reduces the discharge of fly ash and reduces the pollution of fly ash to the environment during waste incineration; the gas purification device The technology that can purify the gas discharged from the exhaust gas outlet 22 and discharge the purified gas into the atmosphere, reduce the environmental pollution caused by acid gas or nitrogen oxides, and solve the environmental pollution caused by the waste treatment device in the prior art when the incineration products are discharged Problem, the device of the present invention reduces the pollution caused to the environment when burning waste.
作为可选的实施方式,废物处理装置还包括余热回收装置4,余热回收装置4与废气排出口22相连通;余热回收装置4用以回收热量,余热回收装置4为余热锅炉,烟气温度从1100℃降低到约为550℃,余热锅炉可生成蒸汽和热水对外供热。As an optional embodiment, the waste treatment device also includes a waste heat recovery device 4, which communicates with the exhaust gas outlet 22; the waste heat recovery device 4 is used to recover heat, and the waste heat recovery device 4 is a waste heat boiler, and the temperature of the flue gas is from 1100°C is reduced to about 550°C, and the waste heat boiler can generate steam and hot water for external heating.
作为可选的实施方式,废物熔融炉2包括焚烧熔融部23、燃烧部24和连接焚烧熔融部23和燃烧部24的锥形连接部25,焚烧熔融部23、锥形连接部25和燃烧部24从下到上依次设置,靠近焚烧熔融部23的底端设置有熔融排渣口21,燃烧部24的顶端设置有废气排出口22,废物在焚烧熔融部23内燃烧,部分废物也可以锥形连接部25内燃烧,二噁英在燃烧部24内燃烧;焚烧熔融部23还包括废物焚烧部231和废渣熔融部232,废物焚烧部231设置在废渣熔融部232的上方且废物焚烧部231与废渣熔融部232连接,废物在废物焚烧部231燃烧、废渣在废渣熔融部232受热;焚烧熔融部23和燃烧部24均为圆柱形,燃烧部24与焚烧熔融部23直径比的范围为1.5~3;靠近焚烧熔融部23底端的侧面上均匀设置有主加热源5,主加热源5为燃烧器或等离子体发生器的一种或几种;燃烧部24的侧壁上均匀的设置有副加热源6,副加热源6为燃烧器或等离子体发生器的一种或几种。As an optional embodiment, the waste melting furnace 2 includes an incineration and melting part 23, a combustion part 24 and a conical connection part 25 connecting the incineration and melting part 23 and the combustion part 24, and the incineration and melting part 23, the conical connection part 25 and the combustion part 24 are arranged in sequence from bottom to top, a melting slag outlet 21 is provided near the bottom end of the incineration and melting part 23, and a waste gas discharge port 22 is provided at the top of the combustion part 24, and the waste is burned in the incineration and melting part 23, and part of the waste can also be tapped The dioxin is burned in the burning part 24; the burning and melting part 23 also includes a waste burning part 231 and a waste residue melting part 232, and the waste burning part 231 is arranged above the waste residue melting part 232 and the waste burning part 231 Connected with the waste slag melting part 232, the waste is burned in the waste incineration part 231, and the waste slag is heated in the waste slag melting part 232; the incineration melting part 23 and the burning part 24 are both cylindrical, and the range of the diameter ratio of the burning part 24 to the burning and melting part 23 is 1.5 ~3; The main heating source 5 is evenly arranged on the side near the bottom end of the incineration melting part 23, and the main heating source 5 is one or more of burners or plasma generators; the side wall of the burning part 24 is evenly arranged with The secondary heating source 6 is one or more of a burner or a plasma generator.
废渣成熔融状态需要的温度不小于1400℃,二噁英分解需要的温度不小于1100℃,因为废渣成熔融状态需要的温度高,所以焚烧熔融部23的直径小于燃烧部24直径时,即焚烧熔融部23的内部区域小时,可以减小焚烧熔融部23内的热量散失,保证废渣熔融所需的温度;废物的焚烧的温度在700℃-900℃,进入废物熔融炉2的废物位于焚烧熔融部23的上部,即在废物焚烧部231内燃烧,废渣集中在焚烧熔融部23的底部,即在废渣熔融部232被加热,且废渣熔融的温度大于废物燃烧的温度,为了充分利用热量,所以主加热源5应位于靠近焚烧熔融部23底端的侧面上,可以位于废渣熔融部232的侧面上;二噁英分解的热量可以来源于废物燃烧产生的热量,同时副加热源6也可以为二噁英燃烧提供热量。The temperature required for waste slag to become molten is not less than 1400°C, and the temperature required for dioxin decomposition is not less than 1100°C. Because the temperature required for waste slag to become molten is high, so when the diameter of the incineration melting part 23 is smaller than the diameter of the combustion part 24, it is incinerated The inner area of the melting part 23 is small, which can reduce the heat loss in the incineration melting part 23 and ensure the temperature required for waste slag melting; the temperature of waste incineration is 700°C-900°C, and the waste entering the waste melting furnace 2 is located at the incineration melting point. The top of part 23, that is, burns in the waste incineration part 231, and the waste slag concentrates on the bottom of the incineration melting part 23, that is, is heated in the waste slag melting part 232, and the temperature of waste slag melting is greater than the temperature of waste combustion. In order to make full use of heat, so The main heating source 5 should be located on the side near the bottom of the incineration melting part 23, and can be located on the side of the waste residue melting part 232; the heat of dioxin decomposition can come from the heat generated by waste combustion, and the secondary heating source 6 can also be two The burning of oxins provides heat.
作为可选的实施方式,废物焚烧部231和燃烧部24内均通有辅助燃烧的气化剂,废物在缺氧的环境下燃烧、二噁英在富氧的环境下燃烧,废物焚烧部231通入的气化剂是不充足的,因为当废物在氧气不足的情况下燃烧时,能有效控制废物燃烧时二噁英的生产,此时,焚烧温度控制在700℃-900℃,从燃烧方式上降低二噁英的生成,减小分解二噁英时所需要的热量;燃烧部24通入足量的气化剂,因为二噁英在富氧的环境下燃烧能充分的分解,能避免二噁英排入大气。As an optional embodiment, both the waste incineration part 231 and the combustion part 24 are provided with a gasification agent for auxiliary combustion, waste is burned in an oxygen-deficient environment, dioxins are burned in an oxygen-enriched environment, and the waste incineration part 231 The gasification agent introduced is insufficient, because when the waste is burned under the condition of insufficient oxygen, it can effectively control the production of dioxin when the waste is burned. At this time, the incineration temperature is controlled at 700°C-900°C. In this way, the formation of dioxins can be reduced, and the heat required for decomposing dioxins can be reduced; the combustion part 24 can be fed with a sufficient amount of gasification agent, because dioxins can be fully decomposed when burned in an oxygen-enriched environment, and can Avoid release of dioxins into the atmosphere.
作为可选的实施方式,废物熔融炉2采用耐热钢材质制成;废物熔融炉2的内侧壁上沿从内向外的方向依次设置有绝热层26、耐热层27和耐高温腐蚀层28。As an optional embodiment, the waste melting furnace 2 is made of heat-resistant steel; the inner wall of the waste melting furnace 2 is sequentially provided with a heat-insulating layer 26, a heat-resistant layer 27 and a high-temperature corrosion-resistant layer 28 along the direction from the inside to the outside. .
作为可选的实施方式,废物预处理装置1包括废物贮仓110和破碎机120,待破碎的废物经过破碎机120处理后输送至废物贮仓110,废物贮仓110可以与给料阀连接,废物贮仓110内的废物通过料阀进入螺旋给料机7且经过螺旋给料机7进入废物熔融炉2内;预处理废物,首先先将废物分类,需要破碎的废物放入破碎机120进行破碎处理,破碎处理的目的是为了便于垃圾的焚烧,破碎后的废物长度小于100mm,破碎后的废物输送至废物贮仓110,分类后不需要进行破碎处理的废物放入废物贮仓110。As an optional embodiment, the waste pretreatment device 1 includes a waste storage bin 110 and a crusher 120, and the waste to be crushed is transported to the waste storage bin 110 after being processed by the shredder 120, and the waste storage bin 110 can be connected with a feeding valve, The waste in the waste storage bin 110 enters the screw feeder 7 through the material valve and enters the waste melting furnace 2 through the screw feeder 7; to pretreat the waste, firstly, the waste is classified, and the waste to be crushed is put into the crusher 120 for further processing. Crushing treatment, the purpose of the crushing treatment is to facilitate the incineration of garbage. The length of the broken waste is less than 100mm, and the broken waste is transported to the waste storage bin 110.
作为可选的实施方式,气体净化装置包括除酸塔8和脱硝装置9,余热回收装置4、除酸塔8、飞灰收集装置3和脱硝装置9依次设置;除酸塔8是为了除去废气中的酸性气体,并将废气温度降低到250℃以下,脱销装置9是为了去除氮氧化物;废物处理装置还包括引风机10,引风机10驱动脱硝装置9内的气体从烟囱12排出。As an optional embodiment, the gas purification device includes an acid removal tower 8 and a denitrification device 9, and the waste heat recovery device 4, the acid removal tower 8, the fly ash collection device 3 and the denitrification device 9 are arranged in sequence; the acid removal tower 8 is for removing waste gas The acid gas in the waste gas and reduce the temperature of the exhaust gas to below 250°C. The denitrification device 9 is to remove nitrogen oxides; the waste treatment device also includes an induced draft fan 10, which drives the gas in the denitrification device 9 to be discharged from the chimney 12.
一种利用废物处理装置处理废物的废物处理方法,包括以下步骤:A waste treatment method for treating waste with a waste treatment device, comprising the following steps:
S1、预处理废物;S1. Pretreatment of waste;
S2、废物通过螺旋给料机7输送至废物熔融炉2内;S2, the waste is transported to the waste melting furnace 2 through the screw feeder 7;
S3、废物在废物熔融炉2内燃烧;S3, the waste is burned in the waste melting furnace 2;
S4、产生的熔融态废渣从熔融排渣口21排出,从废气排出口22排出的飞灰被飞灰收集装置3收集后输送至焚烧熔融部23,从废气排出口22排出的气体经过气体净化装置后排入大气;S4. The generated molten waste slag is discharged from the melting slag discharge port 21, and the fly ash discharged from the waste gas discharge port 22 is collected by the fly ash collection device 3 and then transported to the incineration melting part 23, and the gas discharged from the waste gas discharge port 22 is subjected to gas purification After the device is discharged into the atmosphere;
步骤S4还包括以下步骤:Step S4 also includes the following steps:
S41、从熔融排渣口21排出废渣经过废渣池11水冷后形成玻璃体,从废气排出口22排出的飞灰依次经过余热回收装置4、除酸塔8后进入飞灰收集装置3内;从废气排出口22排出的气体依次经过余热回收装置4、除酸塔8、飞灰收集装置3以及脱硝装置9并在引风机10的驱动下从烟囱12中排出。S41, the waste slag discharged from the molten slag discharge port 21 is water-cooled in the waste slag pool 11 to form a glass body, and the fly ash discharged from the waste gas discharge port 22 enters the fly ash collection device 3 after passing through the waste heat recovery device 4 and the acid removal tower 8 in turn; from the waste gas The gas discharged from the outlet 22 passes through the waste heat recovery device 4 , the acid removal tower 8 , the fly ash collection device 3 and the denitrification device 9 in sequence, and is discharged from the chimney 12 driven by the induced draft fan 10 .
步骤S1中,预处理废物,首先将废物分类,需要破碎的废物放入破碎机120进行破碎处理,然后将破碎后的废物输送至废物贮仓110,分类后不需要进行破碎处理的废物放入废物贮仓110;步骤S41中,熔融状态下的废渣进入废渣池11内急冷至常温后成为玻璃体;在步骤S3中,废物在熔融炉2内燃烧,包括了废物的燃烧过程、废渣的加热至熔融的过程以及二噁英燃烧分解的过程。In step S1, the waste is pretreated. First, the waste is classified, and the waste that needs to be crushed is put into the crusher 120 for crushing treatment, and then the crushed waste is transported to the waste storage bin 110, and the waste that does not need to be crushed is put into the Waste storage bin 110; in step S41, the waste slag in the molten state enters the waste slag pool 11 and is rapidly cooled to normal temperature to become a glass body; in step S3, the waste is burned in the melting furnace 2, including the combustion process of waste, the heating of waste slag to The process of melting and the process of burning and decomposing dioxins.
本发明提供的一种废物处理装置及废物处理方法,降低排放焚烧产物时造成环境污染。The waste treatment device and the waste treatment method provided by the invention can reduce environmental pollution caused by discharging incineration products.
以上所述,仅为本发明的具体实施方式,但本发明的保护范围并不局限于此,任何熟悉本技术领域的技术人员在本发明揭露的技术范围内,可轻易想到变化或替换,都应涵盖在本发明的保护范围之内。因此,本发明的保护范围应以所述权利要求的保护范围为准。The above is only a specific embodiment of the present invention, but the scope of protection of the present invention is not limited thereto. Anyone skilled in the art can easily think of changes or substitutions within the technical scope disclosed in the present invention. Should be covered within the protection scope of the present invention. Therefore, the protection scope of the present invention should be determined by the protection scope of the claims.
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