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CN111957127A - Skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas - Google Patents

Skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas Download PDF

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CN111957127A
CN111957127A CN202010845366.4A CN202010845366A CN111957127A CN 111957127 A CN111957127 A CN 111957127A CN 202010845366 A CN202010845366 A CN 202010845366A CN 111957127 A CN111957127 A CN 111957127A
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flue gas
organic solid
solid waste
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gasification
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杨竹
王伟
徐帆帆
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Research Institute For Environmental Innovation (suzhou) Tsinghua
Suzhou Yunqing Environmental Energy Technology Co Ltd
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Suzhou Yunqing Environmental Energy Technology Co Ltd
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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D46/00Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
    • B01D46/10Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces
    • B01D46/12Particle separators, e.g. dust precipitators, using filter plates, sheets or pads having plane surfaces in multiple arrangements
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/02Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
    • B01D53/04Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
    • B01D53/14Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by absorption
    • B01D53/1456Removing acid components
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    • B01D53/1456Removing acid components
    • B01D53/1481Removing sulfur dioxide or sulfur trioxide
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D53/00Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
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    • B01DSEPARATION
    • B01D2253/00Adsorbents used in seperation treatment of gases and vapours
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    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
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    • B01D2257/2045Hydrochloric acid
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/40Nitrogen compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/60Heavy metals or heavy metal compounds
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2257/00Components to be removed
    • B01D2257/90Odorous compounds not provided for in groups B01D2257/00 - B01D2257/708
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D2258/00Sources of waste gases
    • B01D2258/02Other waste gases
    • B01D2258/0283Flue gases

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Abstract

本发明公开了有机固废气化‑焚烧烟气撬装式净化装备及方法,涉及烟气除尘净化技术领域。该撬装式一体化装备将烟气净化的处理单元以模块化的形式集中在集装箱中,包括耐高温过滤模块、活性炭吸附模块、两级喷淋模块、尾气排放模块等。有机固废气化烟气由进气口进入净化装备后,依次经过耐高温过滤模块、活性炭吸附模块和两级喷淋装置进行烟气除尘净化,最后从烟囱风管排出。本发明的优点在于撬装式处理设备灵活机动,适用于有机固废分布式或分散性的就地热解气化处理或应急处理的烟气净化;各处理单元以模块化形式组装在集装箱内,便于安装、维护、检修以及耗材更换;撬装式设备还具备投资成本低、运行维护成本低、操作简单等优点。

Figure 202010845366

The invention discloses a skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas, and relates to the technical field of flue gas dust removal and purification. The skid-mounted integrated equipment centralizes the processing units for flue gas purification in the container in a modular form, including a high temperature resistant filter module, an activated carbon adsorption module, a two-stage spray module, and a tail gas emission module. After the organic solid waste gasification flue gas enters the purification equipment from the air inlet, it sequentially passes through the high temperature filter module, the activated carbon adsorption module and the two-stage spray device for dust removal and purification of the flue gas, and finally is discharged from the chimney air duct. The advantages of the invention are that the skid-mounted treatment equipment is flexible and maneuverable, and is suitable for the distributed or dispersed in-situ pyrolysis gasification treatment of organic solid waste or the flue gas purification of emergency treatment; each treatment unit is assembled in a container in a modular form, which is convenient for Installation, maintenance, overhaul and replacement of consumables; skid-mounted equipment also has the advantages of low investment cost, low operation and maintenance cost, and simple operation.

Figure 202010845366

Description

一种有机固废气化-焚烧烟气撬装式净化装备及方法A skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas

技术领域technical field

本发明属于烟气除尘净化技术领域,特别涉及一种有机固废气化-焚烧烟气撬装式净化装备及方法。The invention belongs to the technical field of dust removal and purification of flue gas, and particularly relates to a skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas.

背景技术Background technique

随着中国经济社会的迅猛发展,我国的有机固废产量也逐渐增加。有机固废的气化-焚烧技术是一种新型热处理技术,能够实现有机固废减量化、资源化、无害化处理。气化-焚烧技术是指经过预处理过后的有机固废在热解气化炉中进行干燥、热解、氧化还原等过程,产生的合成气或可燃气通入燃烧室进行燃烧,产生的热量通过余热锅炉或内燃机等进行热电联用。与传统的焚烧技术相比,传统焚烧技术容易因为反应不充分而引起以二噁英为代表的二次污染问题,而有机固废气化-焚烧技术通过控制贫氧或缺氧等反应条件,能够从原理上减少二噁英等污染物的产生,同时具有烟气排放量低、能量利用率高等优势。With the rapid development of China's economy and society, my country's organic solid waste production has gradually increased. The gasification-incineration technology of organic solid waste is a new heat treatment technology, which can realize the reduction, recycling and harmless treatment of organic solid waste. Gasification-incineration technology refers to the process of drying, pyrolysis, redox and other processes of pretreated organic solid waste in a pyrolysis gasifier, and the generated syngas or combustible gas is passed into the combustion chamber for combustion, and the generated heat Combine heat and power with waste heat boilers or internal combustion engines. Compared with the traditional incineration technology, the traditional incineration technology is easy to cause secondary pollution problems represented by dioxins due to insufficient reaction, while the organic solid waste gasification-incineration technology can control the reaction conditions such as oxygen depletion or oxygen deficiency. In principle, it can reduce the production of pollutants such as dioxin, and at the same time, it has the advantages of low flue gas emission and high energy utilization rate.

有机固废热化学处理过程中产生的烟气组成成分十分复杂,其中包括了粉尘颗粒物、酸性气体、重金属和有机污染物等二次污染物。因此,在采用气化-焚烧技术处理有机固废时,必须经过烟气除尘净化的处理,以使其达到排放标准和避免二次污染。不同于直接焚烧的烟气,气化-焚烧烟气中的二氧化硫、氮氧化物等污染物含量相对较低,其原因是在有机固废热解气化过程中,氮、硫元素极少被氧化而残留在固态灰渣中,并没有随着挥发分一起进入二燃室。The composition of flue gas generated during the thermal chemical treatment of organic solid waste is very complex, including secondary pollutants such as dust particles, acid gases, heavy metals and organic pollutants. Therefore, when using gasification-incineration technology to treat organic solid waste, it must be treated by flue gas dust removal and purification to make it meet the emission standard and avoid secondary pollution. Different from the flue gas of direct incineration, the content of pollutants such as sulfur dioxide and nitrogen oxides in the gasification-incineration flue gas is relatively low. It is oxidized and remains in the solid ash, and does not enter the secondary combustion chamber with the volatile matter.

现有的烟气除尘净化设备,多数都是针对传统焚烧技术,少有针对有机固废气化技术的处理设备与方法,而且已有的技术与装备存在着烟气处理效率低、净化效果不彻底的问题。此外,现有的处理设备多为固定式,安装复杂,移动不便,并不适用于需要进行移动的应急处理或就地处置设施。Most of the existing flue gas dust removal and purification equipment are for traditional incineration technology, and there are few treatment equipment and methods for organic solidification waste gas treatment technology, and the existing technologies and equipment have low flue gas treatment efficiency and incomplete purification effect. The problem. In addition, most of the existing treatment equipment is fixed, which is complicated to install and inconvenient to move, and is not suitable for emergency treatment or on-site treatment facilities that need to be moved.

发明内容SUMMARY OF THE INVENTION

为了克服上述现有技术的缺点,本发明的目的在于提供一种有机固废气化-焚烧烟气撬装式净化装备及方法,可灵活应用于生活垃圾、医疗废物、有机危险废物、工业有机固废等热解气化应急处理设施的烟气/废气处理,以解决应急处理或就地处理设施的环保问题。In order to overcome the shortcomings of the above-mentioned prior art, the object of the present invention is to provide a skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas, which can be flexibly applied to domestic waste, medical waste, organic hazardous waste, industrial organic solid waste Flue gas/waste gas treatment of waste and other pyrolysis gasification emergency treatment facilities to solve the environmental protection problems of emergency treatment or on-site treatment facilities.

为了实现上述目的,本发明采用的技术方案是:In order to achieve the above object, the technical scheme adopted in the present invention is:

一种有机固废气化-焚烧烟气撬装式净化装备,烟气净化的处理单元以模块化的形式集中在集装箱中,沿有机固废气化烟气的流向,所述处理单元包括:A skid-mounted purification equipment for organic solid waste gasification-incineration flue gas, the processing units for flue gas purification are centralized in a container in a modular form, and along the flow direction of organic solid waste gasification flue gas, the processing unit includes:

耐高温过滤模块,由板式过滤器组成;High temperature resistant filter module, composed of plate filter;

活性炭吸附模块,由进风段、炭纤维过滤段和出风段组成,其中炭纤维过滤段由若干活性炭纤维过滤筒组成;The activated carbon adsorption module is composed of an air inlet section, a carbon fiber filter section and an air outlet section, wherein the carbon fiber filter section is composed of several activated carbon fiber filter cartridges;

两级喷淋模块,包括串联的一级喷淋洗涤塔和二级喷淋洗涤塔;Two-stage spray module, including a series-connected first-stage spray-washing tower and two-stage spray-washing tower;

尾气排放模块,由玻璃钢离心风机、可拆卸烟囱风管以及备用的可更换风管构成。The exhaust emission module is composed of a FRP centrifugal fan, a removable chimney air duct and a spare replaceable air duct.

所述板式过滤器为表面氧化铝挤型材内部铺以滤料骨架的板式过滤器,滤料采用聚酯合成纤维,其进风面蓬松,出风面紧实,板式过滤器与有机固废气化烟气的流向垂直,其边沿可通过螺栓螺丝等结构安装于集装箱内壁。The plate filter is a plate filter with a filter material skeleton laid on the surface of the alumina extruded profile. The filter material is made of polyester synthetic fibers. The air inlet surface is fluffy and the air outlet surface is tight. The flow direction of the flue gas is vertical, and its edge can be installed on the inner wall of the container through bolts and screws.

所述活性炭纤维过滤筒的过滤层厚度为50~100mm,活性炭纤维过滤筒的轴向与有机固废气化烟气的流向垂直,各活性炭纤维过滤筒呈阵列式分布。The thickness of the filter layer of the activated carbon fiber filter cartridge is 50-100 mm, the axial direction of the activated carbon fiber filter cartridge is perpendicular to the flow direction of the organic solid waste gasification flue gas, and each activated carbon fiber filter cartridge is distributed in an array.

所述活性炭吸附模块的进风段在竖直方向上位于集装箱的中下部,出风段在竖直方向上位于进风段的下方。The air inlet section of the activated carbon adsorption module is located in the middle and lower part of the container in the vertical direction, and the air outlet section is located below the air inlet section in the vertical direction.

所述一级喷淋洗涤塔和二级喷淋洗涤塔的结构相同,主体采用玻璃钢材质,塔体表面采用进口抗紫外线胶衣,喷嘴为低压大流量细雾螺旋喷嘴,喷管采用PVC管,填料选用纯PP特拉瑞带刺花环。The structure of the first-level spray washing tower and the second-level spray washing tower is the same, the main body is made of glass fiber reinforced plastic, the surface of the tower body is made of imported anti-ultraviolet gel coat, the nozzle is a low-pressure large-flow fine mist spiral nozzle, and the nozzle is made of PVC pipe. The filler is made of pure PP Terrary barbed wreath.

所述一级喷淋洗涤塔的烟气入口在竖直方向上位于集装箱的中上部,烟气出口在竖直方向上位于集装箱的中上部,所述二级喷淋洗涤塔的烟气入口在竖直方向上位于集装箱的中下部,烟气出口在竖直方向上位于集装箱的中上部。The flue gas inlet of the first-stage spray washing tower is located in the middle and upper part of the container in the vertical direction, and the flue gas outlet is located in the middle and upper part of the container in the vertical direction. The vertical direction is located in the middle and lower part of the container, and the flue gas outlet is located in the middle and upper part of the container in the vertical direction.

所述玻璃钢离心风机的机壳为高强度、耐酸碱纤维增强复合材料(FRP)材质构成的蜗壳型结构;进风口为玻璃钢制成的整体收敛式,用螺栓固定在机壳侧;叶轮采用碳素钢为骨架,外表面用耐酸碱纤维增强复合材料(FRP)材质进行复合保护;电机、皮带轮配有保护罩,可拆卸烟囱风管和备用的可更换风管均采用耐酸碱纤维增强复合材料(FRP)材质,外表面使用进口抗紫外线胶衣保护。The casing of the FRP centrifugal fan is a volute type structure made of high-strength, acid and alkali resistant fiber reinforced composite material (FRP) material; the air inlet is an integral convergent type made of FRP, and is fixed on the casing side with bolts; the impeller Carbon steel is used as the skeleton, and the outer surface is protected by acid and alkali-resistant fiber reinforced composite material (FRP). Fiber reinforced composite material (FRP) material, the outer surface is protected by imported anti-ultraviolet gel coat.

本发明集装箱采用40尺货柜,内径尺寸为:长12032mm×宽2352mm×高2393mm。The container of the present invention adopts a 40-foot container, and the inner diameter dimension is: length 12032mm×width 2352mm×height 2393mm.

本发明还提供了基于所述有机固废气化-焚烧烟气撬装式净化装备的净化方法,所述有机固废气化烟气在引风机作用下通过集装箱内的处理单元,依次进行耐高温初效过滤、活性炭纤维吸附、两级喷淋酸雾洗涤后,由离心风机抽出至风管烟囱达标排放。The present invention also provides a purification method based on the organic solid waste gasification-incineration flue gas skid-mounted purification equipment. After high-efficiency filtration, activated carbon fiber adsorption, and two-stage acid mist washing, the centrifugal fan is extracted to the air duct and chimney for discharge up to the standard.

所述有机固废气化烟气在进入集装箱之前温度控制在150℃-200℃之间,若温度高于200℃,则先进行风冷,通过补给新风来降低温度,烟气中的颗粒物经过耐高温初效过滤后被有效处理掉,之后再进入活性炭纤维吸附,除去烟气中的重金属,通过两级喷淋酸雾洗涤,吸收二氧化硫、氮氧化物、硫化氢、氯化氢等气体,最后净化后的烟气通过烟囱达标排放。The temperature of the organic solid waste gasification flue gas is controlled between 150°C and 200°C before entering the container. If the temperature is higher than 200°C, air cooling is performed first, and the temperature is lowered by supplying fresh air. The high-temperature primary filter is effectively treated, and then enters into activated carbon fiber for adsorption to remove heavy metals in the flue gas. It is washed by two-stage spraying acid mist to absorb sulfur dioxide, nitrogen oxides, hydrogen sulfide, hydrogen chloride and other gases, and finally purified. The flue gas is discharged through the chimney up to the standard.

与现有技术相比,本发明具有的优点主要体现在:所述的撬装式烟气净化处理设备机动性较强,能够灵活运用到小规模分散化的有机固废(包括生活垃圾、有机危险废物、医疗废物、工业有机固废等)处理设施或应急处理设施上,确保尾气达标排放;各个处理部件以模块化的形式集成在集装箱内,方便添加药品、更换耗材以及设备检修或替换;相比于传统的有机固废气化或焚烧的烟气处理成套装备,所述的撬装式装备还具备占地面积小、操作便捷、运行维护成本低、高效节能等优势。Compared with the prior art, the advantages of the present invention are mainly reflected in: the skid-mounted flue gas purification and treatment equipment has strong mobility, and can be flexibly applied to small-scale dispersed organic solid waste (including domestic waste, organic waste, etc.). Hazardous waste, medical waste, industrial organic solid waste, etc.) treatment facilities or emergency treatment facilities to ensure that the exhaust gas is discharged up to the standard; each treatment component is integrated in the container in a modular form to facilitate the addition of drugs, the replacement of consumables, and the maintenance or replacement of equipment; Compared with the traditional complete set of flue gas treatment equipment for organic solidification waste gas treatment or incineration, the skid-mounted equipment also has the advantages of small footprint, convenient operation, low operation and maintenance cost, high efficiency and energy saving.

附图说明Description of drawings

图1为本发明提供的所述的有机固废气化-焚烧烟气撬装式净化装备的整体结构示意图。1 is a schematic diagram of the overall structure of the skid-mounted purification equipment for organic solid waste gasification-incineration flue gas provided by the present invention.

图2为本发明提供的所述的有机固废气化-焚烧烟气撬装式净化装备的俯视图。FIG. 2 is a top view of the skid-mounted purification equipment for organic solid waste gasification-incineration flue gas provided by the present invention.

上述附图中的有关标记为:1进气口,2补气口,3耐高温过滤模块,4活性炭吸附模块,5喷淋装置,6循环泵,7喷淋水箱,8加药箱,9电控系统,10可拆卸烟囱风管,11风机,12备用烟囱风管。The relevant marks in the above drawings are: 1 air inlet, 2 air supply port, 3 high temperature resistant filter module, 4 activated carbon adsorption module, 5 spray device, 6 circulating pump, 7 spray water tank, 8 dosing box, 9 electricity Control system, 10 detachable chimney ducts, 11 fans, 12 spare chimney ducts.

具体实施方式Detailed ways

下面结合附图和实施例详细说明本发明的实施方式。The embodiments of the present invention will be described in detail below with reference to the accompanying drawings and examples.

一种有机固废气化-焚烧烟气撬装式净化装备,烟气净化的处理单元以模块化的形式集中在集装箱中,沿有机固废气化烟气的流向,其中,处理单元包括:A skid-mounted purification equipment for organic solid waste gasification-incineration flue gas, the processing units for flue gas purification are centralized in a container in a modular form, along the flow direction of organic solid waste gasification flue gas, wherein the processing unit includes:

耐高温过滤模块,由采用表面氧化铝挤型材内部铺以滤料骨架的板式过滤器组成。滤料采用优质聚酯合成纤维,其进风面蓬松,出风面紧实,在保证效率的同时,提供了较大的容尘量、合理的滤芯褶数设计,增加了有效的过滤面积。使用一段时间后,过滤器拆卸下来用气枪吹清洗,可以重复利用。板式过滤器与有机固废气化烟气的流向垂直,其边沿可通过螺栓螺丝等结构安装于集装箱内壁。The high temperature resistant filter module is composed of a plate filter with a filter material skeleton covered inside the aluminum oxide extruded profile on the surface. The filter material is made of high-quality polyester synthetic fiber. The air inlet surface is fluffy and the air outlet surface is tight. While ensuring the efficiency, it provides a large dust holding capacity, a reasonable filter element pleat design, and increases the effective filtration area. After a period of use, the filter can be removed and cleaned with an air gun, which can be reused. The plate filter is perpendicular to the flow direction of the organic solidified waste gas, and its edge can be installed on the inner wall of the container through bolts and screws.

活性炭吸附模块,由进风段、炭纤维过滤段和出风段组成,其中进风段在竖直方向上位于集装箱的中下部,出风段在竖直方向上位于进风段的下方。炭纤维过滤段由若干活性炭纤维过滤筒组成,过滤层厚度为50~100mm,活性炭纤维的吸附性能优于活性炭,它具有高度发达的微孔结构,吸附速度快、净化效果好,且还具备不怕碳碱的耐腐蚀性能。有机固废气化-焚烧烟气从进风段进入箱体经由滤筒吸附净化后,由出风段通入下一模块。活性炭纤维过滤筒的轴向与有机固废气化烟气的流向垂直,各活性炭纤维过滤筒呈阵列式分布。The activated carbon adsorption module is composed of an air inlet section, a carbon fiber filter section and an air outlet section. The air inlet section is located in the middle and lower part of the container in the vertical direction, and the air outlet section is located vertically below the air inlet section. The carbon fiber filter section is composed of several activated carbon fiber filter cartridges, and the thickness of the filter layer is 50-100mm. The adsorption performance of activated carbon fiber is better than that of activated carbon. It has a highly developed microporous structure, fast adsorption speed, good purification effect, and also has the Corrosion resistance of carbon-alkali. Organic solid waste gasification-incineration flue gas enters the box from the air inlet section and is adsorbed and purified by the filter cartridge, and then passes into the next module from the air outlet section. The axial direction of the activated carbon fiber filter cartridge is perpendicular to the flow direction of the organic solid waste gasification flue gas, and each activated carbon fiber filter cartridge is distributed in an array.

两级喷淋模块,包括串联的一级喷淋洗涤塔和二级喷淋洗涤塔。一级喷淋洗涤塔和二级喷淋洗涤塔的结构相同,主体采用玻璃钢材质,塔体表面采用进口抗紫外线胶衣;洗涤塔喷淋系统中的喷嘴为低压大流量细雾螺旋喷嘴,喷管采用优质PVC管,保证较好的气液相接触和喷雾效果;洗涤塔的填料选用纯PP特拉瑞带刺花环,该填料比表面积大,可充分解决气液交换问题,具有阻力小、操作弹性大等特点。一级喷淋洗涤塔的烟气入口在竖直方向上位于集装箱的中上部,烟气出口在竖直方向上位于集装箱的中上部,所述二级喷淋洗涤塔的烟气入口在竖直方向上位于集装箱的中下部,烟气出口在竖直方向上位于集装箱的中上部。The two-stage spraying module includes a series-connected first-stage spraying and washing tower and a second-stage spraying and washing tower. The structure of the first-level spray washing tower and the second-level spray washing tower is the same, the main body is made of glass fiber reinforced plastic, and the surface of the tower body is made of imported anti-ultraviolet gel coat; The pipe is made of high-quality PVC pipe to ensure better gas-liquid contact and spray effect; the packing of the washing tower is made of pure PP Terrary barbed garland, which has a large specific surface area and can fully solve the problem of gas-liquid exchange. Features such as flexibility. The flue gas inlet of the first-stage spraying and washing tower is located in the middle and upper part of the container in the vertical direction, and the flue gas outlet is located in the middle and upper part of the container in the vertical direction. It is located in the middle and lower part of the container in the vertical direction, and the flue gas outlet is located in the middle and upper part of the container in the vertical direction.

尾气排放模块,由玻璃钢离心风机、可拆卸烟囱风管以及备用的可更换风管构成。玻璃钢离心风机的机壳为高强度、耐酸碱纤维增强符合材料(FRP)材质构成的蜗壳型结构;进风口为玻璃钢制成的整体收敛式,经过精加工后用螺栓固定在机壳侧;叶轮采用碳素钢为骨架,外表面用FRP材质进行符合保护;电机、皮带轮等配有保护罩。可拆卸烟囱风管和备用的可更换风管均采用FRP材质,外表面使用进口抗紫外线胶衣保护。The exhaust emission module is composed of a FRP centrifugal fan, a removable chimney air duct and a spare replaceable air duct. The casing of the FRP centrifugal fan is a volute type structure made of high-strength, acid and alkali resistant fiber reinforced composite material (FRP). ; The impeller adopts carbon steel as the skeleton, and the outer surface is protected by FRP material; the motor and pulley are equipped with protective cover. The detachable chimney air duct and the spare replaceable air duct are made of FRP material, and the outer surface is protected by imported anti-ultraviolet gel coat.

上述撬装式烟气净化装备涉及的核心部件按照过滤、吸附、喷淋、排放的顺序以模块化的形式放置在集装箱(40尺货柜,内径尺寸:12032mm(长)×2352mm(宽)×2393mm(高),外部尺寸:12192mm(长)×2438mm(宽)×2438mm(高))内。该尺寸的集装箱符合我国现行国家标准《集装箱外部尺寸和额定质量》(GB 1413—2008),能够由货车直接运输。相比于固定式的烟气净化装备,撬装式装备通过运输,能够灵活运用于应急处理设施或者就地处理设施的烟气净化,使得尾气达标排放。The core components involved in the above skid-mounted flue gas purification equipment are placed in a modular form in the order of filtration, adsorption, spraying, and discharge (height), external dimensions: 12192mm (length) × 2438mm (width) × 2438mm (height)). Containers of this size conform to my country's current national standard "External Dimensions and Rated Mass of Containers" (GB 1413-2008), and can be directly transported by trucks. Compared with fixed flue gas purification equipment, skid-mounted equipment can be flexibly used for flue gas purification in emergency treatment facilities or on-site treatment facilities through transportation, so that the exhaust gas can be discharged up to the standard.

本发明的净化方法,有机固废气化烟气(气化炉尾气/烟气)在引风机作用下通过集装箱内的处理单元,依次进行耐高温初效过滤、活性炭纤维吸附、两级喷淋酸雾洗涤后,由离心风机抽出至风管烟囱达标排放。In the purification method of the present invention, the organic solidified waste gas (gasifier tail gas/flue gas) passes through the processing unit in the container under the action of the induced draft fan, and sequentially performs high temperature resistant primary filtration, activated carbon fiber adsorption, and two-stage acid spraying After the mist is washed, it is extracted by the centrifugal fan to the air duct and chimney for discharge up to the standard.

具体过程如下:烟气在进入撬装式烟气净化装置之前温度需要控制在150℃-200℃之间,在引风机作用下通过风管将气体引入处理净化设施。若气体温度仍然高于200℃,则需要先进行风冷,通过补给新风来降低烟气温度。烟气中的颗粒物经过耐高温初效过滤段后被有效处理掉,之后再进入活性炭纤维吸附,除去烟气中的重金属,通过两级喷淋洗涤段,吸收二氧化硫、氮氧化物、硫化氢、氯化氢等气体,最后净化后的烟气通过烟囱达标排放。The specific process is as follows: before the flue gas enters the skid-mounted flue gas purification device, the temperature needs to be controlled between 150°C and 200°C, and the gas is introduced into the treatment and purification facility through the air duct under the action of the induced draft fan. If the gas temperature is still higher than 200°C, air cooling is required first, and the flue gas temperature is reduced by supplying fresh air. The particulate matter in the flue gas is effectively treated after the high temperature resistant primary filter section, and then enters the activated carbon fiber for adsorption to remove heavy metals in the flue gas. Hydrogen chloride and other gases, and finally the purified flue gas is discharged through the chimney up to the standard.

本发明进一步提供一个具体实施例如下:The present invention further provides a specific embodiment as follows:

参考图1和图2,在集装箱左侧中部位置设置进气口1用于烟气或废气的引入,在进气口的下方位置预留有补气口2,目的是补新风对温度过高的烟气进行风冷。烟气进入净化装备后,通过耐高温过滤模块3进行初效过滤,除去烟气中的颗粒物;过滤后的烟气通过活性炭吸附模块4左侧中下方的风管进入活性炭纤维过滤吸附筒,除去烟气中的重金属和异味。Referring to Figures 1 and 2, an air inlet 1 is set at the middle position on the left side of the container for the introduction of flue gas or exhaust gas, and a supplementary air outlet 2 is reserved at the lower position of the air inlet, in order to make up for the fresh air to the temperature too high. The flue gas is air-cooled. After the flue gas enters the purification equipment, it is filtered through the high temperature resistant filter module 3 to remove the particulate matter in the flue gas. Heavy metals and odors in flue gas.

处理过后的烟气由活性炭吸附模块4右侧下方的风管排出并进入两级喷淋洗涤塔;一级喷淋洗涤塔和二级喷淋洗涤塔构造上没有区别,均主要由喷淋装置5、循环泵6、喷淋水箱7和加药箱8构成;烟气通过一级喷淋洗涤塔的左侧中上部进入一次喷淋段后从右侧上方排出,一级喷淋后的烟气通过二级喷淋洗涤塔的下方进入二次喷淋段充分气液接触后,由二级喷淋洗涤塔右侧上方风管引出,二氧化硫、氮氧化物、硫化氢、氯化氢等气体在该阶段被吸收。The treated flue gas is discharged from the air duct below the right side of the activated carbon adsorption module 4 and enters the two-stage spray washing tower; there is no difference in the structure of the first-stage spray washing tower and the second-stage spray washing tower, and both are mainly composed of the spray device. 5. The circulating pump 6, the spray water tank 7 and the dosing tank 8 are composed; the flue gas enters the primary spray section through the upper left side of the primary spray washing tower and is discharged from the upper right side. The gas enters the secondary spray section through the lower part of the secondary spray washing tower after full gas-liquid contact, and is drawn out from the upper air duct on the right side of the secondary spray washing tower. stage is absorbed.

经过过滤、吸附、喷淋处理后的烟气在烟囱风机11的作用下,引入到可拆卸烟囱风管10中高空排放。可拆卸烟囱风管10的设计高度为20m,在运输过程中或装备不工作状态下可以分段拆卸放置在备用烟囱风管12处。在可拆卸烟囱风管10和备用烟囱风管12中预留有检测点位,用于检测分析排放烟气中的氮氧化物、二氧化硫、颗粒物等排放是否低于排放限值。The flue gas after being filtered, adsorbed and sprayed is introduced into the detachable chimney air duct 10 under the action of the chimney fan 11 for high-altitude discharge. The design height of the detachable chimney air duct 10 is 20m, and it can be disassembled in sections and placed at the spare chimney air duct 12 during transportation or when the equipment is not working. Detection points are reserved in the detachable chimney air duct 10 and the spare chimney air duct 12 for detecting and analyzing whether the emission of nitrogen oxides, sulfur dioxide, and particulate matter in the exhaust gas is lower than the emission limit.

电控系统9位于加药箱8和可拆卸烟囱风管10之间,用于控制喷淋洗涤塔的循环泵6、加药箱8和烟囱的风机11以及配套的照明和消防设施。The electronic control system 9 is located between the dosing box 8 and the detachable chimney air duct 10, and is used to control the circulating pump 6 of the spray washing tower, the dosing box 8 and the fan 11 of the chimney, as well as supporting lighting and fire-fighting facilities.

与烟气净化装备相对应,本发明提供的有机固废气化-焚烧烟气撬装式净化方法,包括如下步骤:Corresponding to the flue gas purification equipment, the organic solidified waste gasification-incineration flue gas skid-mounted purification method provided by the present invention comprises the following steps:

1)烟气的初效过滤;1) Primary filtration of flue gas;

2)烟气的活性炭吸附;2) Activated carbon adsorption of flue gas;

3)烟气的两级喷淋洗涤。3) Two-stage spray washing of flue gas.

具体地,结合烟气净化装备,有机固废气化-焚烧烟气撬装式净化方法具体实施如下:气化-焚烧烟气通过进气口1进入净化装备中,若烟气温度过高,则开启补气口2进行新风补给将气体温度降低至200℃以下;烟气通过布置在集装箱内的风管依次经过耐高温过滤模块3、活性炭吸附模块4和喷淋装置5进行烟气净化,除去烟气中的粉尘颗粒物、酸性气体、重金属和有机污染物等;最后净化后的烟气通过可拆卸烟囱风管10高空达标排放。Specifically, combined with the flue gas purification equipment, the organic solid waste gasification-incineration flue gas skid-mounted purification method is specifically implemented as follows: the gasification-incineration flue gas enters the purification equipment through the air inlet 1, and if the flue gas temperature is too high, then Open the air supply port 2 for fresh air supply to reduce the gas temperature to below 200 °C; the flue gas passes through the high temperature filter module 3, the activated carbon adsorption module 4 and the spray device 5 in turn through the air duct arranged in the container to purify the flue gas to remove the smoke Dust particles, acid gases, heavy metals and organic pollutants in the gas; the final purified flue gas is discharged through the detachable chimney air duct 10 at high altitude.

本发明提供的装备和方法可应用于多种有机固废气化-焚烧处理后的烟气净化,包括生活垃圾、医疗废物、有机危险废物、工业有机固废等。其优点在于撬装式处理设备灵活机动,适用于有机固废分布式或分散性的就地热解气化处理或应急处理的烟气净化;各处理单元以模块化形式组装在集装箱内,便于安装、维护、检修以及耗材更换;撬装式设备还具备投资成本低、运行维护成本低、操作简单等优点。The equipment and method provided by the present invention can be applied to the purification of flue gas after a variety of organic solid waste gasification-incineration treatment, including domestic waste, medical waste, organic hazardous waste, industrial organic solid waste and the like. The advantage is that the skid-mounted treatment equipment is flexible and maneuverable, and is suitable for the distributed or dispersed in-situ pyrolysis gasification treatment of organic solid waste or the flue gas purification of emergency treatment; each treatment unit is assembled in a modular form in a container, which is easy to install, Maintenance, overhaul and replacement of consumables; skid-mounted equipment also has the advantages of low investment cost, low operation and maintenance cost, and simple operation.

Claims (10)

1. The utility model provides an organic solid useless gasification-incineration flue gas sled dress formula purification is equipped which characterized in that, the processing unit of gas cleaning concentrates on the container in the form of modularization in, along the flow direction of organic solid useless gasification flue gas, processing unit includes:
the high-temperature resistant filtering module consists of a plate type filter;
the active carbon adsorption module consists of an air inlet section, a carbon fiber filtering section and an air outlet section, wherein the carbon fiber filtering section consists of a plurality of active carbon fiber filtering cylinders;
the two-stage spraying module comprises a first-stage spraying washing tower and a second-stage spraying washing tower which are connected in series;
the tail gas emission module consists of a glass fiber reinforced plastic centrifugal fan, a detachable chimney air pipe and a standby replaceable air pipe.
2. The skid-mounted purification equipment for organic solid waste gasification-incineration flue gas as recited in claim 1, wherein the plate filter is a plate filter with a surface alumina extruded section bar and a filter material framework laid inside, the filter material is made of polyester synthetic fiber, an air inlet surface of the plate filter is fluffy, an air outlet surface of the plate filter is compact, and the plate filter is perpendicular to the flow direction of the organic solid waste gasification flue gas.
3. The skid-mounted purification equipment for the organic solid waste gasification-incineration flue gas as claimed in claim 1, wherein the thickness of the filter layer of the activated carbon fiber filter cartridge is 50-100 mm, the axial direction of the activated carbon fiber filter cartridge is perpendicular to the flow direction of the organic solid waste gasification flue gas, and the activated carbon fiber filter cartridges are distributed in an array manner.
4. The organic solid waste gasification-incineration flue gas skid-mounted purification equipment as claimed in claim 1 or 3, wherein the air inlet section of the activated carbon adsorption module is located at the middle lower part of the container in the vertical direction, and the air outlet section is located below the air inlet section in the vertical direction.
5. The skid-mounted purification equipment for gasification-incineration flue gas of organic solid waste according to claim 1, wherein the first-stage spray washing tower and the second-stage spray washing tower have the same structure, the main body is made of glass fiber reinforced plastic, the surface of the tower body is made of an inlet anti-ultraviolet gel coat, the nozzles are low-pressure large-flow fine mist spiral nozzles, the spray pipes are made of PVC pipes, and the filler is made of pure PP terai with barbed wreath.
6. The organic solid waste gasification-incineration flue gas skid-mounted purification equipment as claimed in claim 1 or 5, wherein the flue gas inlet of the primary spray washing tower is located at the middle upper part of the container in the vertical direction, the flue gas outlet of the primary spray washing tower is located at the middle upper part of the container in the vertical direction, the flue gas inlet of the secondary spray washing tower is located at the middle lower part of the container in the vertical direction, and the flue gas outlet of the secondary spray washing tower is located at the middle upper part of the container in the vertical direction.
7. The skid-mounted purification equipment for organic solid waste gasification-incineration flue gas as recited in claim 1, wherein the casing of the glass fiber reinforced plastic centrifugal fan is of a volute structure made of high-strength, acid and alkali resistant Fiber Reinforced Plastic (FRP) material; the air inlet is of an integral convergent type made of glass fiber reinforced plastics and is fixed on the side of the machine shell by bolts; the impeller adopts carbon steel as a framework, and the outer surface of the impeller is compositely protected by an acid-base-resistant Fiber Reinforced Plastic (FRP) material; the motor and the belt pulley are provided with the protective covers, the detachable chimney air pipe and the standby replaceable air pipe are made of acid and alkali resistant Fiber Reinforced Plastic (FRP) materials, and the outer surface of the detachable chimney air pipe is protected by an imported ultraviolet resistant gel coat.
8. The skid-mounted purification equipment for organic solid waste gasification-incineration flue gas as claimed in claim 1, wherein the container is a 40-foot container, and the inside diameter size is as follows: length × width × height 12032mm × 2352mm × 2393 mm.
9. The purification method of the skid-mounted purification equipment for the gasification-incineration flue gas of organic solid waste according to claim 1, wherein the gasification flue gas of organic solid waste passes through a treatment unit in the container under the action of a draught fan, and after high temperature resistant primary filtration, activated carbon fiber adsorption and two-stage spraying acid mist washing are sequentially carried out, the gasification flue gas of organic solid waste is pumped out by a centrifugal fan to an air pipe chimney to reach the standard and be discharged.
10. The purification method of claim 1, wherein the temperature of the organic solid waste gasification flue gas is controlled to be 150-200 ℃ before entering the container, if the temperature is higher than 200 ℃, air cooling is performed firstly, fresh air is supplied to reduce the temperature, particulate matters in the flue gas are effectively treated after high temperature resistant primary filtration, then the flue gas enters activated carbon fibers for adsorption, heavy metals in the flue gas are removed, two-stage spraying acid mist washing is performed to absorb gases such as sulfur dioxide, nitrogen oxides, hydrogen sulfide and hydrogen chloride, and finally the purified flue gas is discharged through a chimney after reaching standards.
CN202010845366.4A 2020-08-20 2020-08-20 Skid-mounted purification equipment and method for organic solid waste gasification-incineration flue gas Pending CN111957127A (en)

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Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113713497A (en) * 2021-08-14 2021-11-30 刘小方 Exhaust-gas treatment equipment for oil refining production process

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN204522709U (en) * 2015-02-04 2015-08-05 绿色动力环保集团股份有限公司 The combination depickling dust pelletizing system of incineration flue gas of household garbage
CN105114955A (en) * 2015-08-18 2015-12-02 江苏鼎新环保科技有限公司 Preparation method based on rotary kiln-type continuous distillation pyrolysis and gasification incinerator
CN105935531A (en) * 2016-06-06 2016-09-14 浙江文国重工机械有限公司 Industrial solid waste cracking burning tail gas treatment method
CN207024929U (en) * 2017-05-17 2018-02-23 东莞市云峰环保设备有限公司 A device for purifying organic tail gas by activated carbon fiber
CN111442286A (en) * 2020-04-26 2020-07-24 上海第升环保科技有限公司 A plasma skid-mounted treatment device and process for treating medical waste
CN212348090U (en) * 2020-08-20 2021-01-15 苏州允清环境能源科技有限公司 Skid-mounted purification equipment for organic solid waste gasification-incineration flue gas

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN204522709U (en) * 2015-02-04 2015-08-05 绿色动力环保集团股份有限公司 The combination depickling dust pelletizing system of incineration flue gas of household garbage
CN105114955A (en) * 2015-08-18 2015-12-02 江苏鼎新环保科技有限公司 Preparation method based on rotary kiln-type continuous distillation pyrolysis and gasification incinerator
CN105935531A (en) * 2016-06-06 2016-09-14 浙江文国重工机械有限公司 Industrial solid waste cracking burning tail gas treatment method
CN207024929U (en) * 2017-05-17 2018-02-23 东莞市云峰环保设备有限公司 A device for purifying organic tail gas by activated carbon fiber
CN111442286A (en) * 2020-04-26 2020-07-24 上海第升环保科技有限公司 A plasma skid-mounted treatment device and process for treating medical waste
CN212348090U (en) * 2020-08-20 2021-01-15 苏州允清环境能源科技有限公司 Skid-mounted purification equipment for organic solid waste gasification-incineration flue gas

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113713497A (en) * 2021-08-14 2021-11-30 刘小方 Exhaust-gas treatment equipment for oil refining production process
CN113713497B (en) * 2021-08-14 2023-12-22 南京维克环保科技有限公司 Waste gas treatment equipment for oil refining production process

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Application publication date: 20201120