CN115322812A - Fixed type sludge gasification, decoking and ash removal coupling waste incineration power generation device and method - Google Patents
Fixed type sludge gasification, decoking and ash removal coupling waste incineration power generation device and method Download PDFInfo
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- 238000005235 decoking Methods 0.000 title claims abstract description 13
- 238000010248 power generation Methods 0.000 title claims abstract description 13
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- 238000010168 coupling process Methods 0.000 title claims abstract description 8
- 238000005859 coupling reaction Methods 0.000 title claims abstract description 8
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- 239000002956 ash Substances 0.000 claims abstract description 25
- 238000007254 oxidation reaction Methods 0.000 claims abstract description 24
- 230000003647 oxidation Effects 0.000 claims abstract description 23
- 239000010813 municipal solid waste Substances 0.000 claims abstract description 19
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/02—Fixed-bed gasification of lump fuel
- C10J3/20—Apparatus; Plants
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/58—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels combined with pre-distillation of the fuel
- C10J3/60—Processes
- C10J3/64—Processes with decomposition of the distillation products
- C10J3/66—Processes with decomposition of the distillation products by introducing them into the gasification zone
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/723—Controlling or regulating the gasification process
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J3/00—Production of combustible gases containing carbon monoxide from solid carbonaceous fuels
- C10J3/72—Other features
- C10J3/82—Gas withdrawal means
- C10J3/84—Gas withdrawal means with means for removing dust or tar from the gas
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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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/12—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating using gaseous or liquid fuel
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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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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
- C10J—PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES; CARBURETTING AIR OR OTHER GASES
- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0913—Carbonaceous raw material
- C10J2300/0916—Biomass
- C10J2300/0923—Sludge, e.g. from water treatment plant
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- C10J2300/00—Details of gasification processes
- C10J2300/09—Details of the feed, e.g. feeding of spent catalyst, inert gas or halogens
- C10J2300/0953—Gasifying agents
- C10J2300/0973—Water
- C10J2300/0976—Water as steam
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- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/164—Integration of gasification processes with another plant or parts within the plant with conversion of synthesis gas
- C10J2300/1643—Conversion of synthesis gas to energy
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- C—CHEMISTRY; METALLURGY
- C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
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- C10J2300/00—Details of gasification processes
- C10J2300/16—Integration of gasification processes with another plant or parts within the plant
- C10J2300/1671—Integration of gasification processes with another plant or parts within the plant with the production of electricity
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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
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- Gasification And Melting Of Waste (AREA)
Abstract
Description
技术领域technical field
本发明涉及一种固定式污泥气化除焦除灰耦合垃圾焚烧发电装置及方法,主要应用领域包括市政污泥的处置、工业污水厂排放污泥的处置等。该发明针对所有市政污泥和具有一定热值(干基污泥热值大于12600kJ/kg)的工业污泥的处置。The invention relates to a fixed sludge gasification decoking and ash removal coupled waste incineration power generation device and method. The main application fields include the disposal of municipal sludge, the disposal of sludge discharged from industrial sewage plants, and the like. The invention is aimed at the disposal of all municipal sludge and industrial sludge with a certain calorific value (dry sludge calorific value greater than 12600kJ/kg).
背景技术Background technique
污泥处理是对污泥进行减量化、稳定化和无害化处理的过程。污水处理程度越高,就会产生越多的污泥残余物需要加以处理。对现代化的污水处理厂而言,污泥的处理与处置已成为污水处理系统运行中最复杂、且花费最高的一部分。Sludge treatment is the process of sludge reduction, stabilization and harmless treatment. The higher the degree of wastewater treatment, the more sludge residues are generated that need to be disposed of. For modern sewage treatment plants, the treatment and disposal of sludge has become the most complex and expensive part of the operation of the sewage treatment system.
城市污泥是城市污水处理不可避免的产物,如何使污泥的处置与环境保护之间达到一个良好的平衡是当前面临的重大课题。城市污泥是一种常见的固态污染物,但是如果将其进行合理的加工,则会成为一种有用的资源。目前对于城市污泥处理处置方法及深化利用是一项重要的研究课题,它对保护环境具有积极的意义。污泥科学合理的利用可以避免资源的极度浪费,具有非常重要的现实意义和经济社会价值。此外,我国对现有行业的可持续发展战略的改革更加推进了污泥的处理处置与其资源化技术的研究进程。Municipal sludge is an inevitable product of urban sewage treatment. How to achieve a good balance between sludge disposal and environmental protection is a major issue currently facing. Municipal sludge is a common solid pollutant, but if properly processed, it can be a useful resource. At present, it is an important research topic for municipal sludge treatment and disposal methods and its deepening utilization, which has positive significance for environmental protection. The scientific and reasonable utilization of sludge can avoid the extreme waste of resources, which has very important practical significance and economic and social value. In addition, my country's reform of the sustainable development strategy of the existing industry has further promoted the research process of sludge treatment and recycling technology.
城市污泥如果处理不当进入环境,会对周围环境造成一定的危害。污泥经过减容、稳定和无害化处理后,可以作为资源加以综合利用。尽管城市污泥处理处置方法多种多样,我们应根据污泥量,污泥性质,重金属含量等具体情况作具体分析;同时,要考虑环境生态,经济效益,处理成本,技术发展趋势等因素,还要积极探索污泥处理的新方法,新技术,新工艺。从长远观点来看,搞好污泥的处理处置及其无害化,作为再生资源有效综合利用是世界各国共同重视的问题。If municipal sludge enters the environment improperly, it will cause certain harm to the surrounding environment. After volume reduction, stabilization and harmless treatment, the sludge can be comprehensively utilized as a resource. Although there are many ways to treat and dispose of urban sludge, we should make a specific analysis according to the specific conditions such as the amount of sludge, sludge properties, and heavy metal content; at the same time, we must consider factors such as environmental ecology, economic benefits, treatment costs, and technological development trends. It is also necessary to actively explore new methods, new technologies, and new processes for sludge treatment. From a long-term point of view, doing a good job in the treatment and disposal of sludge and its harmlessness, as well as the effective and comprehensive utilization of renewable resources are issues that all countries in the world attach importance to.
我国是一个农业大国,经济基础较为薄弱,污泥的资源化利用尤其是农业利用不但可以节省大量的污泥终端处置费用,更可以为肥力低下的农田增添有机质、提高肥力,促进农业生产发展、实现农业生态环境的良性循环。因此,污泥的资源化利用将成为符合我国国情的污泥处置发展方向。my country is a large agricultural country with a relatively weak economic foundation. The resource utilization of sludge, especially agricultural utilization, can not only save a lot of sludge terminal disposal costs, but also add organic matter to low-fertility farmland, improve fertility, and promote the development of agricultural production. Realize the virtuous circle of agricultural ecological environment. Therefore, the resource utilization of sludge will become the development direction of sludge disposal in line with my country's national conditions.
为了解决污水厂的污泥问题,一些地区的环保部门将市政污泥送到垃圾焚烧厂进行混烧。在污泥与垃圾混烧的过程中,污泥粒径很细,很容易被风携带出去,造成了飞灰(危险废弃物)的大量增加,由于飞灰的处理成本很高,严重影响了垃圾焚烧电厂处理污泥的积极性。In order to solve the problem of sludge in sewage plants, environmental protection departments in some areas send municipal sludge to waste incineration plants for co-combustion. In the process of co-combustion of sludge and garbage, the sludge particle size is very fine, and it is easily carried out by the wind, resulting in a large increase in fly ash (hazardous waste). Due to the high cost of fly ash treatment, it seriously affects the The enthusiasm of waste incineration power plants to treat sludge.
发明内容Contents of the invention
污水处理厂运到垃圾电厂污泥仓库的污泥含水率一般在60%左右,在垃圾电厂经过初步的余热干燥后,含水率一般在20%-30%,满足污泥气化的条件,在此基础上,本发明提供一种固定式污泥气化除焦除灰耦合垃圾焚烧发电装置及方法。本发明可以有效的降低垃圾焚烧炉直接混烧污泥带来的飞灰含量过高的问题,也可以充分利用污泥的热值。The moisture content of the sludge transported from the sewage treatment plant to the sludge warehouse of the garbage power plant is generally about 60%. On this basis, the present invention provides a fixed sludge gasification decoking and ash removal coupled with waste incineration power generation device and method. The invention can effectively reduce the problem of excessively high fly ash content caused by direct co-combustion of sludge in garbage incinerators, and can also make full use of the calorific value of sludge.
为实现上述目的,本发明采用的技术方案为:To achieve the above object, the technical solution adopted in the present invention is:
一种固定式污泥气化除焦除灰耦合垃圾焚烧发电装置,包括污泥料仓、计量装置、螺旋给料器、气化炉、旋风分离器、高温风机、阻火器、垃圾焚烧炉、氧化风机、拨渣器、破渣机、闸板阀、收渣仓、炉箅子;所述污泥料仓通过计量装置经螺旋给料器与气化炉连接,所述气化炉包括气化炉一区和气化炉二区,气化炉一区底部侧方连接氧化风机,气化炉一区底部设有拨渣器,气化炉二区的底部侧方连接旋风分离器,旋风分离器顶端通过高温风机与垃圾焚烧炉连接,高温风机与垃圾焚烧炉之间设有阻火器;气化炉二区下方设有炉箅子,炉箅子下方设有破渣机,破渣机经闸板阀连接收渣仓。A fixed sludge gasification decoking and ash removal coupling waste incineration power generation device, including sludge silo, metering device, screw feeder, gasifier, cyclone separator, high temperature fan, flame arrester, waste incinerator, Oxidation fan, slag remover, slag breaker, gate valve, slag collection bin, furnace grate; the sludge silo is connected to the gasifier through a metering device through a screw feeder, and the gasifier includes a gasifier The first zone of the gasification furnace and the second zone of the gasifier, the side of the bottom of the first zone of the gasifier is connected to the oxidation fan, the bottom of the first zone of the gasifier is equipped with a slag remover, the side of the bottom of the second zone of the gasifier is connected to the cyclone separator, and the cyclone is separated The top of the gasifier is connected to the garbage incinerator through a high-temperature fan, and a flame arrester is installed between the high-temperature fan and the garbage incinerator; a furnace grate is installed under the second zone of the gasification furnace, and a slag breaker is installed under the furnace grate. The gate valve is connected to the slag collection bin.
进一步,所述拨渣器包括电机,变速器,旋转杆。Further, the slag remover includes a motor, a transmission, and a rotating rod.
进一步,所述炉箅子是开有若干通风孔的钢板,并设有下渣口。Further, the grate is a steel plate with several ventilation holes and a slag discharge port.
一种固定式污泥气化除焦除灰耦合垃圾焚烧发电方法,具体为:污泥料仓的污泥通过计量装置经螺旋给料器输送至气化炉中,污泥在气化炉一区完成干燥、干馏、还原、氧化后在拨渣器的拨动下进入气化炉二区,拨到气化炉二区的高温灰渣在炉箅子上积聚,并与气化炉一区上部经污泥的干燥、干馏、还原、氧化出来的含水汽和焦油的可燃气反应,反应后,气化合成气通过钢板之间的通风孔出去,进入旋风分离器,反应后的冷渣通过炉箅子的下渣口落入破渣机,最终进入收渣仓,经旋风分离器进一步除去小颗粒飞灰,除尘后的气化合成气通过高温风机的引送,通过阻火器后进入垃圾焚烧炉中焚烧发电。A fixed sludge gasification decoking and ash removal coupled with waste incineration power generation method, specifically: the sludge in the sludge silo is transported to the gasifier through a metering device through a screw feeder, and the sludge in the gasifier one After completion of drying, dry distillation, reduction and oxidation, the slag remover enters the second zone of the gasifier, and the high-temperature ash transferred to the second zone of the gasifier accumulates on the grate and is separated from the first zone of the gasifier. The combustible gas containing water vapor and tar produced by sludge drying, dry distillation, reduction and oxidation in the upper part reacts. After the reaction, the gasification synthesis gas goes out through the ventilation holes between the steel plates and enters the cyclone separator. The cold slag after the reaction passes through the The lower slag opening of the furnace grate falls into the slag breaker, and finally enters the slag collection bin, and the small particles of fly ash are further removed by the cyclone separator. Incineration in the incinerator to generate electricity.
与现有技术相比,本发明的有益效果为:Compared with prior art, the beneficial effect of the present invention is:
1、本发明可以将污泥彻底气化,而且合成气热值较高,约4200 kJ/m3,焦油含量极低(焦油含量不到30mg/m3),粉尘量极小(含量不到0.1g/m3),完全满足垃圾电厂焚烧的要求。1. The present invention can completely gasify the sludge, and the synthetic gas has a high calorific value of about 4200 kJ/m 3 , an extremely low tar content (the tar content is less than 30 mg/m 3 ), and an extremely small amount of dust (the content is less than 0.1g/m 3 ), fully meet the requirements of waste power plant incineration.
2、本发明装置的结构简单、使用方便,运行稳定,可以连续运行,负荷调节方便,根据污泥的进料量和拨渣器的频率来调节负荷,方便操作。2. The device of the present invention has the advantages of simple structure, convenient use, stable operation, continuous operation, and convenient load adjustment. The load can be adjusted according to the amount of sludge feed and the frequency of the slag remover, which is convenient for operation.
3、本发明的合成气进入垃圾焚烧炉后可以起到稳定燃烧和脱除氮氧化物的作用。3. After the synthetic gas of the present invention enters the garbage incinerator, it can play the role of stable combustion and removal of nitrogen oxides.
4、本发明可以有效的降低垃圾焚烧炉直接混烧污泥带来的飞灰含量过高的问题,也可以充分利用污泥的热值。4. The present invention can effectively reduce the problem of high fly ash content caused by direct co-combustion of sludge in garbage incinerators, and can also make full use of the calorific value of sludge.
附图说明Description of drawings
图1为本发明装置的结构示意图;Fig. 1 is the structural representation of device of the present invention;
图2为本发明装置中拨渣器的结构示意图;Fig. 2 is the structural representation of the slag remover in the device of the present invention;
图3为本发明装置中炉箅子的结构示意图;Fig. 3 is the structural representation of fire grate in the device of the present invention;
图4为本发明装置中污泥气化炉的结构示意图;Fig. 4 is the structural representation of sludge gasification furnace in the device of the present invention;
其中,1、污泥料仓,2、计量装置,3、螺旋给料器,4、气化炉,41、气化炉一区,42、气化炉二区,5、旋风分离器,6、高温风机,7、阻火器,8、垃圾焚烧炉,9、氧化风机,10、拨渣器,101、电机,102、变速器,103、旋转杆,104、拨渣杆,11、破渣机,12、闸板阀,13、收渣仓,14、炉箅子,141、下渣口,142、通风孔,143、钢板。Among them, 1. Sludge silo, 2. Metering device, 3. Screw feeder, 4. Gasifier, 41.
具体实施方式Detailed ways
下面结合附图和具体的实施例对本发明的技术方案及效果做进一步描述,但本发明的保护范围并不限于此。The technical solutions and effects of the present invention will be further described below in conjunction with the accompanying drawings and specific embodiments, but the protection scope of the present invention is not limited thereto.
实施例1Example 1
如图1所示,本实施例的一种固定式污泥气化除焦除灰耦合垃圾焚烧发电装置,包括污泥料仓1、计量装置2、螺旋给料器3、气化炉4、旋风分离器5、高温风机6、阻火器7、垃圾焚烧炉8、氧化风机9、拨渣器10、破渣机11、闸板阀12、收渣仓13、炉箅子14;所述污泥料仓1通过计量装置2经螺旋给料器3与气化炉4连接,所述气化炉4包括气化炉一区41和气化炉二区42,气化炉一区41底部侧方连接氧化风机9,气化炉一区41底部设有拨渣器10,气化炉二区42的底部侧方连接旋风分离器5,旋风分离器5顶端通过高温风机6与垃圾焚烧炉8连接,高温风机6与垃圾焚烧炉8之间设有阻火器7;气化炉二区42下方设有炉箅子14,炉箅子14下方设有破渣机11,破渣机11经闸板阀12连接收渣仓13。As shown in Figure 1, a fixed sludge gasification decoking and ash removal coupling waste incineration power generation device in this embodiment includes a sludge silo 1, a
进一步,所述拨渣器10包括电机101,变速器102,旋转杆103,拨渣杆104,在电机101的驱动下,通过变速器102调速,旋转杆103按照一定速度开始旋转,并带动拨渣杆104转动。Further, the
进一步,所述炉箅子14是开有若干通风孔142的钢板143,并设有下渣口141。Further, the
本实施例的固定式污泥气化除焦除灰耦合垃圾焚烧发电装置中,污泥料仓1储存一定量污泥,保障污泥不断料,计量装置2主要是保证进料的均匀性和连续性,可以有效的调剂负荷,螺旋给料器3向上倾斜,保证螺旋给料器内充满污泥,阻止空气进入,污泥料仓1中的污泥通过计量装置2经螺旋给料器3输送至气化炉4中;气化炉4包括气化炉一区41和气化炉二区42,气化炉一区41主要完成污泥的干燥、干馏、还原、氧化,气化炉二区42主要完成焦油的裂解气化和固定碳的水化反应,提高污泥气化合成气的热值;气化炉一区41底部侧方连接氧化风机9,污泥进入气化炉一区41经干燥、干馏、还原后,与氧化风机9送入的空气进行氧化反应,氧化风机主要是保证气化炉一区41底部的物料燃烧气化,为整个炉子的运行提供能量;气化炉一区41底部设有拨渣器10,气化炉一区41气化后的高温含碳灰渣,在拨渣器10的拨动下进入气化炉二区42,具体过程是:如图2所示,在电机101的驱动下,通过变速器102调速,旋转杆103按照一定速度开始旋转,并带动拨渣杆104转动,将高温含一定量炭的灰渣拨到气化炉二区42;拨到气化炉二区42的高温灰渣与在炉箅子14(如图3所示)上积聚,并与气化炉一区41上部经污泥的干燥、干馏、还原、氧化出来的含水汽和焦油的可燃气反应,反应后,通过钢板143之间的通风孔142出去,进入旋风分离器5,炉箅子14是开有若干通风孔142的钢板143,主要是能保证合成气的通过,并阻止炉渣的通过,进入旋风分离器5的飞灰大大降低;反应后的冷渣通过炉箅子14的下渣口141落入破渣机11,破渣机11主要是把反应完全的灰渣破碎排出,打开闸板阀12进入收渣仓13,闸板阀12主要是防止空气从下部进入,对破渣机进行密封,收渣仓13主要是收集从气化炉排出的灰渣;旋风分离器5主要是收集从气化炉4携带出的细小飞灰,进一步除去小颗粒飞灰,除尘后的气化合成气通过高温风机6的引送,通过阻火器7后进入垃圾焚烧炉8中焚烧发电。高温风机6主要是从气化炉4引出合格的污泥气化合成气,送入垃圾焚烧炉燃烧,阻火器7主要是阻止火焰从燃烧炉反到管道中,进入气化,4,垃圾焚烧炉8是指目前正运行的垃圾炉排焚烧炉或垃圾焚烧流化床炉。In the fixed sludge gasification decoking and ash removal coupling waste incineration power generation device of this embodiment, the sludge silo 1 stores a certain amount of sludge to ensure continuous sludge feeding, and the
一种固定式污泥气化除焦除灰耦合垃圾焚烧发电方法,具体为:污泥料仓1的污泥通过计量装置2经螺旋给料器3输送至气化炉4中,污泥在气化炉一区41完成干燥、干馏、还原、氧化后在拨渣器10的拨动下进入气化炉二区42,拨到气化炉二区42的高温灰渣在炉箅子14上积聚,并与气化炉一区41上部经污泥的干燥、干馏、还原、氧化出来的含水汽和焦油的可燃气反应,反应后,气化合成气通过钢板143之间的通风孔142出去,进入旋风分离器5,反应后的冷渣通过炉箅子14的下渣口141落入破渣机11,最终进入收渣仓13,京旋风分离器5进一步除去小颗粒飞灰,除尘后的气化合成气通过高温风机6的引送,通过阻火器7后进入垃圾焚烧炉8中焚烧发电。A fixed sludge gasification decoking and ash removal coupled with waste incineration power generation method, specifically: the sludge in the sludge silo 1 is transported to the gasifier 4 through the
本发明的原理为:把经过烟气余热干燥后的20%-30%水分的污泥储存到污泥料仓中,污泥料仓里的污泥通过计量装置计量后,经过螺旋给料器进入污泥气化炉,底层的污泥在氧化风机送入空气的条件下进行燃烧气化(氧化区),污泥可燃物燃烧气化完成后,变成含部分固定碳的无机高温灰渣,在拨渣器的作用下,进入完全还原区;氧化区上部是经过干馏后的污泥,主要残留物是焦炭和少量粘土等不可燃物,在850℃高温下,经过化学反应产生一氧化碳和氢气等可燃物(还原区);还原区上部的污泥在200-400℃的灼热燃气的烘烤下,发生干馏反应,生产烷类(CmHn)、一氧化碳、焦油等可燃气体(干馏区);干馏区的上部是从顶部落入气化炉的污泥,与80-120℃的可燃气体接触,水分蒸发变成水蒸气,一起进入可燃气体中(干燥区);从炉顶侧面出来的可燃气与从炉底侧面出来的高温灰渣接触反应(完全还原区),水蒸气与高温灰渣的固定碳反应生成一氧化碳和氢气,焦油在经过高温灰渣的过程中发生裂解反应,生成小分子可燃物,并消耗掉可燃气中的氧气和水蒸气,经过反应最终形成污泥气化合成气(焦油含量不到30mg/m3)。污泥气化合成气在高温风机的引送下,进入旋风分离器除掉大部分的飞灰,洁净的合成气通过阻火器后进入垃圾焚烧炉焚烧。污泥气化合成气的热值大约4200kJ/m3,在污泥焚烧炉内一方面可以起到稳定燃烧的作用,另一方面可以在燃烧炉的中部形成还原性气氛,把在燃烧区形成的氮氧化物进行还原,可以大大减少烟气中的氮氧化物排放量。The principle of the present invention is: store the sludge with 20%-30% moisture after being dried by the waste heat of the flue gas into the sludge silo, and the sludge in the sludge silo is measured by the metering device and then passed through the screw feeder. Entering the sludge gasification furnace, the sludge at the bottom is combusted and gasified (oxidation zone) under the condition that the oxidation fan sends air into it. After the combustibles of the sludge are combusted and gasified, they become inorganic high-temperature ash containing part of fixed carbon , under the action of the slag remover, it enters the complete reduction zone; the upper part of the oxidation zone is the sludge after dry distillation, and the main residues are coke and a small amount of non-combustible materials such as clay. At a high temperature of 850 ° C, carbon monoxide and Hydrogen and other combustibles (reduction zone); the sludge on the upper part of the reduction zone is baked by hot gas at 200-400°C, and undergoes dry distillation reaction to produce alkanes (CmHn), carbon monoxide, tar and other combustible gases (carbon distillation zone); The upper part of the carbonization zone is the sludge that falls into the gasifier from the top, contacts with the combustible gas at 80-120°C, the water evaporates into water vapor, and enters the combustible gas together (drying zone); the combustible gas coming out from the side of the furnace top The gas contacts and reacts with the high-temperature ash coming out from the side of the furnace bottom (complete reduction zone), the water vapor reacts with the fixed carbon of the high-temperature ash to generate carbon monoxide and hydrogen, and the tar undergoes cracking reaction during the process of passing through the high-temperature ash to form small molecules combustible, and consume the oxygen and water vapor in the combustible gas, and finally form sludge gasification synthesis gas (tar content is less than 30mg/m 3 ) after reaction. Sludge gasification synthesis gas is guided by a high-temperature fan and enters a cyclone separator to remove most of the fly ash. The clean synthesis gas passes through a flame arrester and then enters a waste incinerator for incineration. The calorific value of sludge gasification synthesis gas is about 4200kJ/m 3 . On the one hand, it can play a role in stabilizing combustion in the sludge incinerator, and on the other hand, it can form a reducing atmosphere in the middle of the combustion furnace, and form a The reduction of nitrogen oxides can greatly reduce the emission of nitrogen oxides in the flue gas.
本发明气化炉一区为气化炉提供总热量,并为气化炉二区提供高温的灰渣和含水汽和焦油的可燃气,在气化炉二区发生充分的裂解和气化反应,保证了合成气的低焦油、高热值;为后续的与生活垃圾焚烧炉耦合燃烧提供保障,即降低了垃圾燃烧炉的氮氧化物含量,也保证了燃烧炉的稳定燃烧,减少了天然气补燃,提高了垃圾焚烧炉的效率,节约了成本。The first zone of the gasifier of the present invention provides total heat for the gasifier, and provides high-temperature ash and combustible gas containing water vapor and tar for the second zone of the gasifier, where sufficient cracking and gasification reactions occur in the second zone of the gasifier, It ensures the low tar and high calorific value of the syngas; it provides guarantee for the subsequent coupled combustion with the domestic waste incinerator, which reduces the nitrogen oxide content of the waste incinerator, ensures the stable combustion of the incinerator, and reduces the supplementary combustion of natural gas , Improve the efficiency of the waste incinerator and save the cost.
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although the embodiments of the present invention have been shown and described, those skilled in the art can understand that various changes, modifications and substitutions can be made to these embodiments without departing from the principle and spirit of the present invention. and modifications, the scope of the invention is defined by the appended claims and their equivalents.
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