CN106838933A - A kind of pyrolyzing sludge method of disposal being quenched based on microwave - Google Patents
A kind of pyrolyzing sludge method of disposal being quenched based on microwave Download PDFInfo
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- 239000010802 sludge Substances 0.000 title claims abstract description 39
- 238000000034 method Methods 0.000 title claims abstract description 20
- 238000000197 pyrolysis Methods 0.000 claims abstract description 208
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 67
- 238000000746 purification Methods 0.000 claims abstract description 26
- 239000002893 slag Substances 0.000 claims abstract description 22
- 238000004140 cleaning Methods 0.000 claims abstract description 19
- 239000002910 solid waste Substances 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims description 10
- 239000000463 material Substances 0.000 claims description 9
- 238000009434 installation Methods 0.000 claims 6
- 238000007599 discharging Methods 0.000 claims 1
- 230000007717 exclusion Effects 0.000 claims 1
- 239000007789 gas Substances 0.000 abstract description 123
- 238000002485 combustion reaction Methods 0.000 abstract description 68
- 229910052799 carbon Inorganic materials 0.000 abstract description 47
- 238000010791 quenching Methods 0.000 abstract description 18
- 230000000171 quenching effect Effects 0.000 abstract description 17
- 239000010813 municipal solid waste Substances 0.000 abstract description 10
- 231100000331 toxic Toxicity 0.000 abstract description 6
- 230000002588 toxic effect Effects 0.000 abstract description 6
- 238000004056 waste incineration Methods 0.000 abstract description 2
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 abstract 1
- 239000002918 waste heat Substances 0.000 description 9
- 239000003610 charcoal Substances 0.000 description 5
- 150000002013 dioxins Chemical class 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 4
- 238000007789 sealing Methods 0.000 description 4
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 3
- 230000009471 action Effects 0.000 description 3
- 239000002956 ash Substances 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000005265 energy consumption Methods 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000003440 toxic substance Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 1
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000010882 bottom ash Substances 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 238000009264 composting Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 229910001385 heavy metal Inorganic materials 0.000 description 1
- 231100001231 less toxic Toxicity 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 229910052760 oxygen Inorganic materials 0.000 description 1
- 239000001301 oxygen Substances 0.000 description 1
- 244000052769 pathogen Species 0.000 description 1
- 231100000614 poison Toxicity 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 231100001234 toxic pollutant Toxicity 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
Classifications
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/001—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals for sludges or waste products from water treatment installations
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/30—Pyrolysing
- F23G2201/302—Treating pyrosolids
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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
- F23G2201/30—Pyrolysing
- F23G2201/303—Burning pyrogases
-
- 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
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- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Water Supply & Treatment (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
本发明一种基于微波淬灭的污泥热解处置方法,包括垃圾进料装置、热解炉、微波燃烧炉、尾气净化装置以及炉渣固废清理装置,把垃圾在热解炉中热解后的残碳排入微波燃烧炉中作为强吸波介质,使其快速升温将热解炉中产生的热解气在穿过高温残碳层时充分燃烧,从而彻底消除热解气中的二恶英等有毒有害气体,更大程度地减小垃圾焚烧对环境的损害。步骤简单、操作方便、实用性强。
The present invention is a sludge pyrolysis treatment method based on microwave quenching, which includes a garbage feeding device, a pyrolysis furnace, a microwave combustion furnace, an exhaust gas purification device and a slag solid waste cleaning device. After the garbage is pyrolyzed in the pyrolysis furnace The residual carbon is discharged into the microwave combustion furnace as a strong wave-absorbing medium, so that it can quickly heat up and fully burn the pyrolysis gas generated in the pyrolysis furnace when it passes through the high-temperature residual carbon layer, thereby completely eliminating the dioxin in the pyrolysis gas. British and other toxic and harmful gases, to a greater extent reduce the damage to the environment caused by waste incineration. The steps are simple, the operation is convenient and the practicability is strong.
Description
技术领域technical field
本发明属于污泥处理领域,特别涉及一种基于微波淬灭的污泥热解处置方法。The invention belongs to the field of sludge treatment, in particular to a sludge pyrolysis treatment method based on microwave quenching.
背景技术Background technique
目前,国内污泥的数量及危害性不断增加,污泥处理方法主要有填埋、焚烧、堆肥、土地利用和建材利用,而焚烧能够最大限度的实现污泥的减量化,所有病原物均可杀灭,有毒污染物被氧化,灰泥中的重金属活性比污泥中的要低得多,卫生条件也大为提高,但核心问题是系统投资大、处理费用高、有机物燃烧产生二恶英等剧毒物质,虽然能够在一定程度上使污泥减量化,但该方法属富氧燃烧且焚烧烟尘尾气处理量大,需要配备完善的尾气净化系统。依靠的焚烧法已经不能满足当前的环保要求。在现有新的处理技术中,热解焚烧法由于具有产生二恶英等毒害物质少,尾气排放量少,剩余残渣量少,处理成本低廉等优势,得到了快速发展。然而热解焚烧产生的热解气需在燃烧室内停留足够的时间进行充分燃烧,导致焚烧系统对自动控制水平要求非常高,所需空间较大,这些成为热解焚烧法在实际应用中的不便之处。At present, the amount and harmfulness of domestic sludge are increasing continuously. The sludge treatment methods mainly include landfill, incineration, composting, land utilization and building material utilization, and incineration can maximize the reduction of sludge, and all pathogens are eliminated. It can be killed, the toxic pollutants are oxidized, the activity of heavy metals in the stucco is much lower than that in the sludge, and the sanitation conditions are greatly improved, but the core problems are large system investment, high treatment costs, and dioxins produced by the combustion of organic matter. Although highly toxic substances such as British can reduce the amount of sludge to a certain extent, this method is oxygen-enriched combustion and has a large amount of incineration soot and tail gas, so it needs to be equipped with a complete tail gas purification system. The incineration method relied on can no longer meet the current environmental protection requirements. Among the existing new treatment technologies, the pyrolysis incineration method has been rapidly developed due to its advantages of producing less toxic substances such as dioxins, less tail gas emissions, less residual residue, and low treatment costs. However, the pyrolysis gas produced by pyrolysis and incineration needs to stay in the combustion chamber for a sufficient time for full combustion, resulting in a very high level of automatic control for the incineration system and a large space required, which has become the inconvenience of the practical application of the pyrolysis incineration method place.
发明内容Contents of the invention
为了克服上述不足,一种基于微波淬灭的污泥热解处置方法,其处理污泥彻底、简单环保。利用污泥在热解炉中热解后的残碳排入微波炉中作为强吸波介质,使其快速升温将热解炉中产生的热解气在穿过高温残碳层时充分燃烧,从而彻底消除热解气中的二恶英等有毒有害气体,更大程度地减小垃圾焚烧对环境的损害,并且设备无需较高的自动控制系统、占用空间较小。In order to overcome the above-mentioned shortcomings, a sludge pyrolysis treatment method based on microwave quenching is developed, which can treat sludge thoroughly, simply and environmentally friendly. The residual carbon after the sludge is pyrolyzed in the pyrolysis furnace is discharged into the microwave oven as a strong wave-absorbing medium, so that it can be heated up rapidly and the pyrolysis gas generated in the pyrolysis furnace is fully burned when it passes through the high-temperature residual carbon layer, thereby Completely eliminate toxic and harmful gases such as dioxin in the pyrolysis gas, minimize the damage to the environment caused by waste incineration, and the equipment does not require a high automatic control system and takes up less space.
为了实现上述目的,本发明采用如下技术方案:In order to achieve the above object, the present invention adopts the following technical solutions:
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
本发明将热解后的残炭和热解气分别导入微波燃烧装置内,其中,热解残碳作为强吸波介质在反应腔内吸波快速升温,提供热量给热解气,使其达到着火温度;热解气在与一定量的助燃气体混合达到着火极限,吸收上述热解残炭释放的热量而燃烧,最大化消耗热解废料的同时,还大幅降低了燃烧能耗。实验结果表明:本发明的垃圾处理装置较现有的热解焚烧炉、废气微波燃烧炉相比能耗降低20%~30%。In the present invention, the pyrolyzed charcoal and pyrolysis gas are respectively introduced into the microwave combustion device, wherein the pyrolyzed charcoal is used as a strong wave-absorbing medium to rapidly heat up in the reaction chamber and provide heat to the pyrolysis gas to achieve Ignition temperature; the pyrolysis gas is mixed with a certain amount of combustion-supporting gas to reach the ignition limit, absorbs the heat released by the above-mentioned pyrolysis residual carbon and burns, maximizing the consumption of pyrolysis waste, and greatly reducing the combustion energy consumption. Experimental results show that: compared with the existing pyrolysis incinerator and waste gas microwave combustion furnace, the energy consumption of the waste treatment device of the present invention is reduced by 20% to 30%.
本发明中所述的“微波燃烧装置”是指:可对物料进行微波加热、使气体在其中燃烧的装置。The "microwave combustion device" mentioned in the present invention refers to a device capable of heating materials by microwaves and burning gas therein.
优选的,所述进料装置为两级进料仓。以保证热解炉的密封状态与内部负压控制要求。Preferably, the feeding device is a two-stage feeding bin. To ensure the sealing state of the pyrolysis furnace and the internal negative pressure control requirements.
优选的,所述热解气经过止回阀被风机送入微波燃烧炉顶部进风口。Preferably, the pyrolysis gas is sent to the top air inlet of the microwave combustion furnace by a fan through a check valve.
优选的,所述微波燃烧装置底部设置有用于承接热解残炭的高温板。Preferably, the bottom of the microwave combustion device is provided with a high-temperature plate for receiving pyrolysis charcoal.
优选的,所述高温板的开孔尺寸满足防止微波泄露的要求。Preferably, the opening size of the high temperature plate meets the requirements for preventing microwave leakage.
优选的,所述微波燃烧装置底部设置有螺旋出料装置。为保证整个焚烧炉系统的密封状态与内部负压控制要求,固体残渣在微波燃烧炉内烧成灰渣后,主要经过螺旋装置排除,渗漏部分经过微波炉底部排渣口排除。Preferably, a screw discharge device is provided at the bottom of the microwave combustion device. In order to ensure the sealing state of the entire incinerator system and the internal negative pressure control requirements, after the solid residue is burned into ash in the microwave incinerator, it is mainly removed through the screw device, and the leaked part is removed through the slag discharge port at the bottom of the microwave oven.
本发明还提供了一种基于微波淬灭的污泥热解处置方法,包括:The present invention also provides a sludge pyrolysis treatment method based on microwave quenching, including:
将粉碎后的污泥进行热解处理,得热解气和热解残炭;The pulverized sludge is subjected to pyrolysis treatment to obtain pyrolysis gas and pyrolysis residual carbon;
将热解残炭作为强吸波介质进行微波加热至1205~1510℃,并使穿过上述热解残炭的热解气与空气的混合气体充分燃烧,收集尾气;Use pyrolysis residual carbon as a strong wave-absorbing medium for microwave heating to 1205-1510 ° C, and fully burn the mixture of pyrolysis gas and air passing through the above pyrolysis residual carbon, and collect tail gas;
将收集的尾气进行余热利用后,净化、排除。After the collected tail gas is used for waste heat, it is purified and discharged.
本发明利用热解残碳作为微波燃烧炉内的强吸波介质,其来源主要为热解炉排入的残碳与吸附净化尾气的活性炭。The present invention utilizes pyrolysis residual carbon as a strong wave-absorbing medium in a microwave combustion furnace, and its sources are mainly residual carbon discharged into the pyrolysis furnace and activated carbon for absorbing and purifying tail gas.
本发明研究发现:1kg污泥在750℃的热解温度下可产生100L至120L热解气,可产生400g至450g热解残碳,其中热解残碳是作为强吸波介质在反应腔内吸波快速升温,提供热量给热解气,使其达到着火温度,其中450g热解残碳作为吸波介质大约可持续吸波8min,期间持续产生大量的热,而使120L的热解气完全燃烧大约仅需要2min,经换算可知,1kg残碳可以处理1000L的热解气。因此单位质量的污泥所产生的热解残碳足以提供给热解气燃烧所需的热量。The research of the present invention found that: 1kg of sludge can produce 100L to 120L of pyrolysis gas at a pyrolysis temperature of 750°C, and can produce 400g to 450g of pyrolysis residual carbon, wherein the pyrolysis residual carbon is used as a strong wave-absorbing medium in the reaction chamber The microwave absorbing heats up quickly, providing heat to the pyrolysis gas to make it reach the ignition temperature, of which 450g of pyrolysis residual carbon is used as the absorbing medium for about 8 minutes, and a large amount of heat is continuously generated during this period, so that the 120L pyrolysis gas is completely Combustion only takes about 2 minutes. After conversion, it can be seen that 1kg of residual carbon can treat 1000L of pyrolysis gas. Therefore, the pyrolysis residual carbon produced by the unit mass of sludge is sufficient to provide the heat required for pyrolysis gas combustion.
优选的,所述热解温度为710℃~806℃。Preferably, the pyrolysis temperature is 710°C to 806°C.
优选的,所述微波加热过程中,热解残炭和热解气用量比为:0.8~1kg:1000~1200L。Preferably, during the microwave heating process, the ratio of pyrolysis residual carbon to pyrolysis gas is: 0.8-1kg: 1000-1200L.
优选的,所述混合气体中,热解气与空气的体积比为3.5-8.5:2.5-7.5。实际运行过程中,空气的用量满足热解气的燃烧要求即可。本领域技术人员可根据热解气的燃烧情况进行常规选择。Preferably, in the mixed gas, the volume ratio of pyrolysis gas to air is 3.5-8.5:2.5-7.5. In the actual operation process, the amount of air used can meet the combustion requirements of the pyrolysis gas. Those skilled in the art can make routine selections according to the combustion conditions of the pyrolysis gas.
优选的,所述高温尾气先被风机送入热解炉内利用其余热热解炉内垃圾,然后再进入空气预热器内加热冷空气,尾气进行两级余热利用。Preferably, the high-temperature exhaust gas is first sent into the pyrolysis furnace by the fan to use the remaining heat to pyrolyze the garbage in the furnace, and then enters the air preheater to heat the cold air, and the exhaust gas is used for two-stage waste heat utilization.
本发明还提供了一种较优的基于微波淬灭的污泥热解处置方法,包括垃圾进料装置、热解炉、微波燃烧炉、尾气净化装置以及炉渣固废清理装置,整个热解焚烧系统密闭且处于负压状态。垃圾粉碎后,经过两级密封进料仓送入热解炉内热解,其中热解炉的形式可采用目前技术成熟的回转炉。热解气被风机抽送至微波炉顶部进风口,在此热解气与另一风机送入的预热后的空气混合燃烧,并在其穿过高温残碳层时充分燃烧,彻底消除二恶英等有毒有害气体。然后高温尾气送入热解炉进行余热利用以热解炉内垃圾,降温后的尾气从热解炉内出来,接着进入空气预热器用以加热冷空气,最后尾气经过活性炭处理装置达标后排放。The present invention also provides a better sludge pyrolysis disposal method based on microwave quenching, which includes a garbage feeding device, a pyrolysis furnace, a microwave combustion furnace, an exhaust gas purification device, and a slag solid waste cleaning device. The system is closed and under negative pressure. After the garbage is crushed, it is sent to the pyrolysis furnace for pyrolysis through the two-stage sealed feeding bin, and the form of the pyrolysis furnace can be a rotary furnace with mature technology at present. The pyrolysis gas is pumped by the fan to the air inlet on the top of the microwave oven, where the pyrolysis gas is mixed with the preheated air sent by another fan for combustion, and is fully burned when it passes through the high-temperature residual carbon layer, completely eliminating dioxins and other toxic and harmful gases. Then the high-temperature tail gas is sent to the pyrolysis furnace for waste heat utilization to pyrolyze the garbage in the furnace. The cooled tail gas comes out of the pyrolysis furnace, and then enters the air preheater to heat the cold air. Finally, the tail gas is discharged after passing through the activated carbon treatment device to meet the standard.
本发明的工作原理为:污泥在落料口处被粉碎后,送入热解炉内热解,其中热解炉的形式可采用目前技术成熟的回转炉。回转炉中产生的热解气被风机抽送至微波炉顶部进风口,在此热解气与另一风机送入的空气混合燃烧。热解残碳落至微波燃烧炉内的高温板上作为强吸波介质,加热残碳层使其温度达到1205~1510℃,高温板的开孔尺寸满足防止微波泄露的要求。热解混合气体在穿过高温残碳层时充分燃烧,彻底消除二恶英等有毒有害气体,然后高温尾气送入热解炉进行余热利用以热解炉内垃圾,降温后的尾气从热解炉内出来,接着进入空气预热器用以加热冷空气,最后尾气经过活性炭处理装置达标后排放。The working principle of the present invention is: after the sludge is pulverized at the discharge port, it is sent to a pyrolysis furnace for pyrolysis, wherein the form of the pyrolysis furnace can be a rotary furnace with mature technology at present. The pyrolysis gas generated in the rotary kiln is pumped by the fan to the air inlet on the top of the microwave oven, where the pyrolysis gas is mixed with the air sent by another fan for combustion. The pyrolysis residual carbon falls on the high temperature plate in the microwave combustion furnace as a strong microwave-absorbing medium, and the residual carbon layer is heated to a temperature of 1205-1510°C. The opening size of the high temperature plate meets the requirements for preventing microwave leakage. The pyrolysis mixed gas is fully burned when passing through the high-temperature residual carbon layer, completely eliminating toxic and harmful gases such as dioxin, and then the high-temperature tail gas is sent to the pyrolysis furnace for waste heat utilization to pyrolyze the garbage in the furnace. It comes out of the furnace, and then enters the air preheater to heat the cold air, and finally the exhaust gas is discharged after passing through the activated carbon treatment device to meet the standard.
本发明的有益效果Beneficial effects of the present invention
1、利用微波深度淬灭污泥;实现了污泥处理地减量化、无害化、资源化。1. Use microwave to quench sludge deeply; realize the reduction, harmlessness and resource utilization of sludge treatment.
2、利用在微波作用下,残碳吸热及C-C放电效应可形成局部热点温度,提高燃烧炉内的能量密度,使炉内温度达到1500℃,彻底消除二恶英等有毒有害气体;2. Under the action of microwave, the residual carbon absorbs heat and the C-C discharge effect can form a local hot spot temperature, increase the energy density in the combustion furnace, make the temperature in the furnace reach 1500 ° C, and completely eliminate toxic and harmful gases such as dioxin;
3、高温尾气两级余热利用,更节能环保;3. Two-stage waste heat utilization of high-temperature exhaust gas, which is more energy-saving and environmentally friendly;
4、热解炉与微波燃烧炉组合运行,简化自动控制要求,缩小系统占地面积。4. Combined operation of pyrolysis furnace and microwave combustion furnace simplifies automatic control requirements and reduces system footprint.
5、本发明装置简单、处理效率高、实用性强,易于推广。5. The present invention has simple device, high processing efficiency, strong practicability, and is easy to popularize.
附图说明Description of drawings
图1是基于微波淬灭的污泥热解处置装置的结构图。Figure 1 is a structural diagram of a sludge pyrolysis disposal device based on microwave quenching.
图2是基于微波淬灭的污泥热解处置方法的流程图。Fig. 2 is a flowchart of a sludge pyrolysis treatment method based on microwave quenching.
其中,1一级进料装置、2一级进料阀、3二级进料装置、4二级进料阀、5热解炉、6.热解炉出料阀、7热解炉排气阀、8提手、9微波炉、10空预器、11尾气回收装置、12微波炉排气阀、13微波炉高温板、14微波炉出料口。Among them, 1 primary feed device, 2 primary feed valve, 3 secondary feed device, 4 secondary feed valve, 5 pyrolysis furnace, 6. pyrolysis furnace discharge valve, 7 pyrolysis furnace exhaust Valve, 8 handle, 9 microwave oven, 10 air preheater, 11 exhaust gas recovery device, 12 microwave oven exhaust valve, 13 microwave oven high temperature plate, 14 microwave oven outlet.
具体实施方式detailed description
以下通过实施例对本发明特征及其它相关特征作进一步详细说明,以便于同行业技术人员的理解:The features of the present invention and other relevant features are described in further detail below through the embodiments, so as to facilitate the understanding of those skilled in the art:
实施例1Example 1
基于微波淬灭的污泥热解处置方法,包括垃圾进料装置、热解炉、微波燃烧炉、尾气净化装置以及炉渣固废清理装置,整个热解焚烧系统密闭且处于负压状态。污泥在落料口处被粉碎后,送入热解炉内热解,其中热解炉的形式采用目前技术成熟的回转炉。回转炉中产生的热解气被风机抽送至微波炉顶部进风口,然后热解气与另一风机送入的空气混合燃烧。热解残碳落至微波燃烧炉内的高温板上作为强吸波介质,加热残碳层使其温度达到1200~1500℃,高温板的开孔尺寸满足防止微波泄露的要求。热解混合气体在穿过高温残碳层时充分燃烧,彻底消除二恶英等有毒有害气体。然后高温尾气被风机送入热解炉内进行余热利用以热解炉内垃圾,降温后的尾气从热解炉内出来,接着进入空气预热器用以加热冷空气,最后尾气经过活性炭处理装置达标后排放,其中活性炭可放入微波加热腔内再生循环使用,微波燃烧炉内的残碳充分燃烧成灰渣后可从侧面螺旋出渣装置及底部落灰斗排除。The sludge pyrolysis disposal method based on microwave quenching includes garbage feeding device, pyrolysis furnace, microwave combustion furnace, tail gas purification device and slag solid waste cleaning device. The entire pyrolysis incineration system is closed and under negative pressure. After the sludge is pulverized at the discharge port, it is sent to the pyrolysis furnace for pyrolysis, and the form of the pyrolysis furnace is a rotary kiln with mature technology. The pyrolysis gas produced in the rotary kiln is pumped by the fan to the air inlet on the top of the microwave oven, and then the pyrolysis gas is mixed with the air sent by another fan for combustion. The pyrolysis residual carbon falls on the high temperature plate in the microwave combustion furnace as a strong microwave-absorbing medium, and the residual carbon layer is heated to a temperature of 1200-1500 °C. The opening size of the high temperature plate meets the requirements for preventing microwave leakage. The pyrolysis mixed gas is fully burned when passing through the high-temperature residual carbon layer, completely eliminating toxic and harmful gases such as dioxins. Then the high-temperature exhaust gas is sent into the pyrolysis furnace by the fan for waste heat utilization to pyrolyze the garbage in the furnace. The cooled exhaust gas comes out of the pyrolysis furnace, and then enters the air preheater to heat the cold air. Finally, the exhaust gas passes through the activated carbon treatment device to reach the standard. After discharge, the activated carbon can be put into the microwave heating chamber for regeneration and recycling. After the residual carbon in the microwave combustion furnace is fully burned into ash, it can be discharged from the side screw slag discharge device and the bottom ash hopper.
实施例2Example 2
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
由于在微波作用下残碳吸波升温,会达到1000℃的温度,加上微波作用下炭与炭之间会发生放电现象,并产生局部高温,残碳温度会进一步增加,这些热量使得热解气快速着火,着火产生的热量又使得炉内温度再进一步增加,使热解气充分燃烧。Due to the absorption of residual carbon under the action of microwaves, the temperature will reach 1000 ° C, and the discharge phenomenon will occur between carbon and carbon under the action of microwaves, and local high temperature will be generated, and the temperature of residual carbon will further increase. These heat will make pyrolysis The gas ignites quickly, and the heat generated by the fire further increases the temperature in the furnace, so that the pyrolysis gas can be fully burned.
实施例3Example 3
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
所述进料装置为两级进料仓。以保证热解炉的密封状态与内部负压控制要求。The feeding device is a two-stage feeding bin. To ensure the sealing state of the pyrolysis furnace and the internal negative pressure control requirements.
实施例4Example 4
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
所述热解气经过止回阀被风机送入微波燃烧炉顶部进风口。The pyrolysis gas is sent to the top air inlet of the microwave combustion furnace by the blower through the check valve.
从回转窑出口的热解气温度为710℃至806℃,热解气进入微波炉内经过一些管道,会产生温降,到达微波炉的温度,基本维持在600℃到700℃之间。The temperature of the pyrolysis gas from the outlet of the rotary kiln is 710°C to 806°C. When the pyrolysis gas enters the microwave oven and passes through some pipes, there will be a temperature drop, and the temperature reaching the microwave oven is basically maintained between 600°C and 700°C.
实施例5Example 5
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
所述微波燃烧装置底部设置有用于承接热解残炭的高温板。The bottom of the microwave combustion device is provided with a high-temperature plate for receiving pyrolysis residual carbon.
实施例6Example 6
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
所述高温板的开孔尺寸满足防止微波泄露的要求。The opening size of the high temperature plate meets the requirement of preventing microwave leakage.
实施例7Example 7
一种基于微波淬灭的污泥热解处置装置,包括:进料装置、热解装置、微波燃烧装置、尾气净化装置、炉渣固废清理装置、风机、空预器;所述进料装置、热解装置、微波燃烧装置和炉渣固废清理装置依次相连,所述热解装置与微波燃烧装置之间还设置有气体循环管道;所述热解装置还与空预器、尾气净化装置依次相连;使用时,所述热解装置产生的热解气和热解残碳分别通过风机和物料通道输入到微波燃烧装置中、充分燃烧后,产生的高温尾气依次回流到热解装置、空预器、尾气净化装置;所述热解处置装置整体密闭且处于负压状态。A sludge pyrolysis treatment device based on microwave quenching, comprising: a feeding device, a pyrolysis device, a microwave combustion device, an exhaust gas purification device, a slag solid waste cleaning device, a fan, and an air preheater; the feeding device, The pyrolysis device, the microwave combustion device and the slag solid waste cleaning device are connected in sequence, and a gas circulation pipeline is also arranged between the pyrolysis device and the microwave combustion device; the pyrolysis device is also connected in sequence with the air preheater and the tail gas purification device When in use, the pyrolysis gas and pyrolysis residual carbon produced by the pyrolysis device are respectively input into the microwave combustion device through the fan and the material channel, and after full combustion, the high-temperature tail gas produced is returned to the pyrolysis device and the air preheater in turn . Tail gas purification device; the pyrolysis treatment device is airtight and in a negative pressure state as a whole.
所述微波燃烧装置底部设置有螺旋出料装置。为保证整个焚烧炉系统的密封状态与内部负压控制要求,固体残渣在微波燃烧炉内烧成灰渣后,主要经过螺旋装置排除,渗漏部分经过微波炉底部排渣口排除。A screw discharge device is provided at the bottom of the microwave combustion device. In order to ensure the sealing state of the entire incinerator system and the internal negative pressure control requirements, after the solid residue is burned into ash in the microwave incinerator, it is mainly removed through the screw device, and the leaked part is removed through the slag discharge port at the bottom of the microwave oven.
实施例8Example 8
一种基于微波淬灭的污泥热解处置方法,包括:A method for sludge pyrolysis disposal based on microwave quenching, comprising:
将粉碎后的污泥进行热解处理,得热解气和热解残炭;The pulverized sludge is subjected to pyrolysis treatment to obtain pyrolysis gas and pyrolysis residual carbon;
将热解残炭作为强吸波介质进行微波加热至1205~1510℃,并使穿过上述热解残炭的热解气与空气的混合气体充分燃烧,收集尾气;Use pyrolysis residual carbon as a strong wave-absorbing medium for microwave heating to 1205-1510 ° C, and fully burn the mixture of pyrolysis gas and air passing through the above pyrolysis residual carbon, and collect tail gas;
将收集的尾气进行余热利用后,净化、排除。本发明利用碳作为微波燃烧炉内的强吸波介质,其来源主要为热解炉排入的残碳与吸附净化尾气的活性炭。After the collected tail gas is used for waste heat, it is purified and discharged. The invention utilizes carbon as a strong wave-absorbing medium in a microwave combustion furnace, and its sources are mainly residual carbon discharged into a pyrolysis furnace and activated carbon for absorbing and purifying tail gas.
其中,所述热解温度为705℃~810℃。Wherein, the pyrolysis temperature is 705°C-810°C.
所述微波加热过程中,热解残炭和热解气用量比为:0.8~1kg:1000~1200L。During the microwave heating process, the ratio of pyrolysis residual charcoal to pyrolysis gas is: 0.8-1kg: 1000-1200L.
所述混合气体中,热解气与空气的体积比为3.5-8.5:2.5-7.5。In the mixed gas, the volume ratio of pyrolysis gas to air is 3.5-8.5:2.5-7.5.
实施例9Example 9
一种基于微波淬灭的污泥热解处置方法,包括:A method for sludge pyrolysis disposal based on microwave quenching, comprising:
将粉碎后的污泥进行热解处理,得热解气和热解残炭;The pulverized sludge is subjected to pyrolysis treatment to obtain pyrolysis gas and pyrolysis residual carbon;
将热解残炭作为强吸波介质进行微波加热至1205~1510℃,并使穿过上述热解残炭的热解气与空气的混合气体充分燃烧,收集尾气;Use pyrolysis residual carbon as a strong wave-absorbing medium for microwave heating to 1205-1510 ° C, and fully burn the mixture of pyrolysis gas and air passing through the above pyrolysis residual carbon, and collect tail gas;
将收集的尾气进行余热利用后,净化、排除。本发明利用碳作为微波燃烧炉内的强吸波介质,其来源主要为热解炉排入的残碳与吸附净化尾气的活性炭。After the collected tail gas is used for waste heat, it is purified and discharged. The invention utilizes carbon as a strong wave-absorbing medium in a microwave combustion furnace, and its sources are mainly residual carbon discharged into a pyrolysis furnace and activated carbon for absorbing and purifying tail gas.
其中,所述热解温度为710℃~806℃。Wherein, the pyrolysis temperature is 710°C-806°C.
所述微波加热过程中,热解残炭和热解气用量比为:0.8~1kg:1000~1200L。During the microwave heating process, the ratio of pyrolysis residual charcoal to pyrolysis gas is: 0.8-1kg: 1000-1200L.
所述混合气体中,热解气与空气的体积比为3.5-8.5:2.5-7.5。In the mixed gas, the volume ratio of pyrolysis gas to air is 3.5-8.5:2.5-7.5.
所述高温尾气先被风机送入热解炉内利用其余热热解炉内垃圾,然后再进入空气预热器内加热冷空气,尾气进行两级余热利用。The high-temperature exhaust gas is first sent into the pyrolysis furnace by the fan to use the remaining heat to pyrolyze the garbage in the furnace, and then enters the air preheater to heat the cold air, and the exhaust gas is used for two-stage waste heat utilization.
最后应该说明的是,以上所述仅为本发明的优选实施例而已,并不用于限制本发明,尽管参照前述实施例对本发明进行了详细的说明,对于本领域的技术人员来说,其依然可以对前述实施例所记载的技术方案进行修改,或者对其中部分进行等同替换。凡在本发明的精神和原则之内,所作的任何修改、等同替换、改进等,均应包含在本发明的保护范围之内。上述虽然结合附图对本发明的具体实施方式进行了描述,但并非对本发明保护范围的限制,所属领域技术人员应该明白,在本发明的技术方案的基础上,本领域技术人员不需要付出创造性劳动即可做出的各种修改或变形仍在本发明的保护范围以内。Finally, it should be noted that the above descriptions are only preferred embodiments 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 the foregoing embodiments, for those skilled in the art, it is still The technical solutions described in the foregoing embodiments may be modified, or part of them may be equivalently replaced. Any modifications, equivalent replacements, improvements, etc. made within the spirit and principles of the present invention shall be included within the protection scope of the present invention. Although the specific implementation of the present invention has been described above in conjunction with the accompanying drawings, it does not limit the protection scope of the present invention. Those skilled in the art should understand that on the basis of the technical solution of the present invention, those skilled in the art do not need to pay creative work Various modifications or variations that can be made are still within the protection scope of the present invention.
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