CN110186052A - Cool waste gasification and melting processing system and its method in movable small - Google Patents
Cool waste gasification and melting processing system and its method in movable small Download PDFInfo
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- 238000002844 melting Methods 0.000 title claims abstract description 90
- 230000008018 melting Effects 0.000 title claims abstract description 90
- 238000002309 gasification Methods 0.000 title claims abstract description 33
- 238000000034 method Methods 0.000 title claims abstract description 23
- 239000002699 waste material Substances 0.000 title claims abstract description 17
- 238000012545 processing Methods 0.000 title claims abstract description 15
- 238000009272 plasma gasification Methods 0.000 claims abstract description 48
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 31
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 29
- 239000003546 flue gas Substances 0.000 claims abstract description 29
- 238000002485 combustion reaction Methods 0.000 claims abstract description 28
- 239000007789 gas Substances 0.000 claims abstract description 21
- 239000000919 ceramic Substances 0.000 claims abstract description 17
- 238000001179 sorption measurement Methods 0.000 claims abstract description 13
- 239000011521 glass Substances 0.000 claims abstract description 7
- 238000006243 chemical reaction Methods 0.000 claims abstract description 6
- 238000010309 melting process Methods 0.000 claims abstract 4
- 239000002910 solid waste Substances 0.000 claims description 15
- 230000015572 biosynthetic process Effects 0.000 claims description 11
- 239000010808 liquid waste Substances 0.000 claims description 11
- 230000002285 radioactive effect Effects 0.000 claims description 11
- 238000003786 synthesis reaction Methods 0.000 claims description 11
- 230000006698 induction Effects 0.000 claims description 8
- 229910000831 Steel Inorganic materials 0.000 claims description 5
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- 238000005201 scrubbing Methods 0.000 claims 3
- 239000000463 material Substances 0.000 claims 2
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- 239000002901 radioactive waste Substances 0.000 abstract description 22
- 239000006060 molten glass Substances 0.000 abstract description 15
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 abstract description 7
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- 238000004017 vitrification Methods 0.000 abstract 1
- 239000002956 ash Substances 0.000 description 9
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- 239000002893 slag Substances 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 238000009792 diffusion process Methods 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
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- 238000011105 stabilization Methods 0.000 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 description 1
- 239000000809 air pollutant Substances 0.000 description 1
- 231100001243 air pollutant Toxicity 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
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- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 210000004127 vitreous body Anatomy 0.000 description 1
- 239000002912 waste gas Substances 0.000 description 1
- 239000002351 wastewater 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
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/027—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment pyrolising or gasifying stage
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
- F23G7/06—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals of waste gases or noxious gases, e.g. exhaust gases
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J1/00—Removing ash, clinker, or slag from combustion chambers
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23J—REMOVAL OR TREATMENT OF COMBUSTION PRODUCTS OR COMBUSTION RESIDUES; FLUES
- F23J15/00—Arrangements of devices for treating smoke or fumes
- F23J15/02—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material
- F23J15/022—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow
- F23J15/025—Arrangements of devices for treating smoke or fumes of purifiers, e.g. for removing noxious material for removing solid particulate material from the gasflow using filters
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Gasification And Melting Of Waste (AREA)
Abstract
本发明公开了一种移动式小型中低放射性废物气化熔融处理系统及其方法,包含破碎机、气动隔膜泵、等离子体气化熔融炉、熔融玻璃体接收器、燃烧室、一级直接换热器、陶瓷过滤器、二级直接换热器、活性炭吸附塔、脱酸洗涤塔、高效空气过滤器、烟囱和移动设备。废物经过前处理后输送至等离子体气化熔融炉中,在炉内气化区进行气化反应后产生合成气进入燃烧室充分燃烧分解后送入烟气净化处理系统,灰渣进入熔融区进行玻璃化熔融处理,使放射性核素被固定在熔融玻璃体中,玻璃体经冷却后由自动接收系统装桶储存后送中低放废物填埋场近地表填埋。本发明减容效果好、安全可靠性高、核素稳定性好、系统工艺集成度高。
The invention discloses a mobile small-scale low-to-medium radioactive waste gasification melting treatment system and its method, comprising a crusher, a pneumatic diaphragm pump, a plasma gasification melting furnace, a molten glass body receiver, a combustion chamber, and a first-stage direct heat exchange filter, ceramic filter, secondary direct heat exchanger, activated carbon adsorption tower, deacidification scrubber, high efficiency air filter, chimney and mobile equipment. After pre-treatment, the waste is transported to the plasma gasification melting furnace. After the gasification reaction in the gasification zone of the furnace, the synthetic gas is generated and enters the combustion chamber for full combustion and decomposition, and then sent to the flue gas purification treatment system. The ash enters the melting zone for further processing. The vitrification melting process fixes the radionuclides in the molten glass body, and after the glass body is cooled, it is stored in drums by the automatic receiving system and then sent to the low- and medium-level radioactive waste landfill for near-surface burial. The invention has good volume reduction effect, high safety and reliability, good nuclide stability and high system process integration.
Description
技术领域technical field
本发明涉及一种气化熔融处理系统及其方法,特别是一种移动式小型中低放射性废物气化熔融处理系统及其方法。The invention relates to a gasification and melting treatment system and a method thereof, in particular to a mobile small-scale gasification and melting treatment system for medium and low radioactive waste and a method thereof.
背景技术Background technique
核设施每年产生数吨的低中放射性废物,固体废物采用超级压缩+水泥固化的处理方式,液体废物采用蒸发+水泥固化技术路线处理,最终装入200L钢桶中储存。虽然水泥固化技术能够对放射性废物能够做到无害化处理,虽然超级压缩机对废物进一步压缩减容,但是水泥固化为增容技术,海上核设施空间有限,增容处理低中放射性废物增加暂存压力,且不能从根本上解决废物中核素浸出和扩散的问题。焚烧法处理中低放废物虽然对可燃废物有比较显著的减容效果,但焚烧过程中所产生的二噁英污染问题一直是备受人们关注的焦点。且由于焚烧产生大量的烟气,不仅增加了尾气处理的负担及成本,而且极易造成放射性核素随烟气进一步扩散,不利于对放射性核素的捕集和控制,焚烧法所产生的灰渣不能被熔融,无法捕集及固化对环境有严重污染的放射性核素及其它重金属。Nuclear facilities produce several tons of low- and medium-level radioactive waste every year. Solid waste is treated by super compression + cement solidification, and liquid waste is treated by evaporation + cement solidification technology, and finally stored in 200L steel drums. Although the cement solidification technology can achieve harmless treatment of radioactive waste, and although the super compressor can further compress and reduce the waste, cement solidification is a capacity-enhancing technology, and the space of offshore nuclear facilities is limited. However, it cannot fundamentally solve the problem of nuclide leaching and diffusion in waste. Although the incineration method for treating low-level and medium-level radioactive waste has a relatively significant volume reduction effect on combustible waste, the problem of dioxin pollution generated during the incineration process has always been the focus of attention. And because the incineration produces a large amount of flue gas, it not only increases the burden and cost of tail gas treatment, but also easily causes the further diffusion of radionuclides with the flue gas, which is not conducive to the capture and control of radionuclides. The slag cannot be melted, and cannot capture and solidify radionuclides and other heavy metals that seriously pollute the environment.
发明内容Contents of the invention
本发明所要解决的技术问题是提供一种移动式小型中低放射性废物气化熔融处理系统及其方法,减容化程度高。The technical problem to be solved by the present invention is to provide a mobile small-scale gasification and melting treatment system and method for medium and low radioactive waste, which have a high degree of volume reduction.
为解决上述技术问题,本发明所采用的技术方案是:In order to solve the problems of the technologies described above, the technical solution adopted in the present invention is:
一种移动式小型中低放射性废物气化熔融处理系统,其特征在于:包含破碎机、气动隔膜泵、等离子体气化熔融炉、熔融玻璃体接收器、燃烧室、一级直接换热器、陶瓷过滤器、二级直接换热器、活性炭吸附塔、脱酸洗涤塔、高效空气过滤器、烟囱和移动设备,破碎机出料口通过无轴螺旋进料器与等离子体气化熔融炉进料口连接,气动隔膜泵的输出端通过管道与等离子体气化熔融炉的进料口连接,熔融玻璃体接收器设置在等离子体气化熔融炉的下端灰渣出口,等离子体气化熔融炉的合成气出口通过管道与燃烧室进口连接,燃烧室出口通过管道与一级直接换热器入口连接,一级直接换热器出口通过管道与陶瓷过滤器入口连接,陶瓷过滤器出口通过二级直接换热器入口连接,二级直接换热器出口通过管道与活性炭吸附塔入口连接,活性炭吸附塔出口通过管道与脱酸洗涤塔入口连接,脱酸洗涤塔出口通过管道与高效空气过滤器入口连接,高效空气过滤器出口与烟囱连接,破碎机、气动隔膜泵、等离子体气化熔融炉、熔融玻璃体接收器、燃烧室、一级直接换热器、陶瓷过滤器、二级直接换热器、活性炭吸附塔、脱酸洗涤塔、高效空气过滤器和烟囱设置在移动设备上。A mobile small-scale low-to-medium radioactive waste gasification and melting treatment system, characterized in that it includes a crusher, a pneumatic diaphragm pump, a plasma gasification and melting furnace, a molten glass body receiver, a combustion chamber, a first-stage direct heat exchanger, a ceramic Filters, secondary direct heat exchangers, activated carbon adsorption towers, deacidification scrubbers, high-efficiency air filters, chimneys and mobile equipment, crusher outlets are fed through shaftless screw feeders and plasma gasification melting furnaces port connection, the output end of the pneumatic diaphragm pump is connected to the feed port of the plasma gasification melting furnace through a pipeline, and the molten glass body receiver is arranged at the lower end of the plasma gasification melting furnace. The gas outlet is connected to the inlet of the combustion chamber through pipes, the outlet of the combustion chamber is connected to the inlet of the first-stage direct heat exchanger through pipes, the outlet of the first-stage direct heat exchanger is connected to the inlet of the ceramic filter through pipes, and the outlet of the ceramic filter is connected through the second-stage direct heat exchanger. The inlet of the heat exchanger is connected, the outlet of the secondary direct heat exchanger is connected to the inlet of the activated carbon adsorption tower through a pipeline, the outlet of the activated carbon adsorption tower is connected to the inlet of the deacidification scrubber through a pipeline, and the outlet of the deacidification scrubber is connected to the inlet of a high-efficiency air filter through a pipeline. High-efficiency air filter outlet is connected with the chimney, crusher, pneumatic diaphragm pump, plasma gasification melting furnace, molten glass body receiver, combustion chamber, primary direct heat exchanger, ceramic filter, secondary direct heat exchanger, activated carbon Adsorption towers, deacidification scrubbers, high-efficiency air filters and chimneys are set on mobile equipment.
进一步地,所述等离子体气化熔融炉包含炉盖和炉身,炉盖扣设在炉身上端,炉盖上设置有与炉膛连通的固体废物进料口和液体废物进料口,炉身内壁上设置有隔热保温层,炉身一侧侧壁上设置有空气导入孔,炉身另一侧侧壁上设置有合成气出口,炉身内设置有炉排,炉排水平设置并固定在炉身内壁上将炉膛分割为炉排上侧的气化区和炉排下侧的熔融区,熔融区下端设置有熔池坩埚,熔池坩埚内设置有两根热等离子体炬,熔池坩埚下端开有与炉身外侧贯穿的排放通孔。Further, the plasma gasification melting furnace includes a furnace cover and a furnace body, the furnace cover is buckled on the upper end of the furnace body, and the furnace cover is provided with a solid waste feeding port and a liquid waste feeding port communicating with the furnace, and the furnace body The inner wall is provided with a heat insulation layer, the side wall of one side of the furnace body is provided with an air inlet hole, the side wall of the other side of the furnace body is provided with a synthesis gas outlet, and the furnace body is provided with a fire grate, which is set horizontally and fixed on the The inner wall of the furnace body divides the furnace into a gasification zone on the upper side of the grate and a melting zone on the lower side of the grate. There is a melting pool crucible at the lower end of the melting zone, and two thermal plasma torches are arranged in the melting pool crucible. The lower end is provided with a discharge through hole penetrating with the outer side of the furnace body.
进一步地,所述炉盖上还设置有观察测量窗口。Further, an observation and measurement window is also provided on the furnace cover.
进一步地,所述固体废物进料口上设置有进料仓和控制阀门,进料仓为圆形漏斗并且进料仓下端与固体废物进料口上端固定连接,控制阀门设置在进料仓下端用于控制投料量。Further, the solid waste feed port is provided with a feed bin and a control valve, the feed bin is a circular funnel and the lower end of the feed bin is fixedly connected to the upper end of the solid waste feed port, and the control valve is set at the lower end of the feed bin for To control the feeding amount.
进一步地,所述热等离子体炬一端从炉身外侧穿过炉身侧壁设置在熔池坩埚内,两根热等离子体炬对称设置在炉身两侧。Further, one end of the thermal plasma torch is arranged in the melting pool crucible from the outside of the furnace body through the side wall of the furnace body, and two thermal plasma torches are arranged symmetrically on both sides of the furnace body.
进一步地,所述排放通孔周围布有感应线圈,热阀贯穿炉身下端并且环绕设置在排放通孔和感应线圈外侧。Further, an induction coil is arranged around the discharge through hole, and the thermal valve penetrates through the lower end of the furnace body and is arranged around the discharge through hole and the outside of the induction coil.
一种移动式小型中低放射性废物气化熔融处理方法,其特征在于包含以下步骤:A mobile small-scale low-to-medium radioactive waste gasification melting treatment method is characterized in that it comprises the following steps:
步骤一:低中放射性劳保用品经破碎机粉碎后由无轴螺旋进料器送入等离子体气化熔融炉,低中放射性液体废物通过气动隔膜泵送入等离子体气化熔融炉;Step 1: The low and medium radioactive labor protection products are crushed by the crusher and sent to the plasma gasification melting furnace by the shaftless screw feeder, and the low and medium radioactive liquid waste is sent into the plasma gasification melting furnace through the pneumatic diaphragm pump;
步骤二:低中放射性劳保用品和低中放射性液体废物进入等离子体气化熔融炉内气化区,在1000-1200℃条件下发生气化反应形成合成气和灰渣;Step 2: Low and medium radioactive labor protection products and low and medium radioactive liquid waste enter the gasification zone of the plasma gasification melting furnace, and gasification reaction occurs at 1000-1200 ° C to form synthesis gas and ash;
步骤三:产生的合成气经引风机送入燃烧室进行燃烧处理,形成无害化的小分子气体;Step 3: The generated synthetic gas is sent to the combustion chamber by the induced draft fan for combustion treatment, forming harmless small molecular gas;
步骤四:灰渣落入等离子体气化熔融炉内的熔融区进行熔融,在1200-1400℃条件下捕集和固化放射性核素最终生成无害化的熔融玻璃体,经冷却后在200L混凝土钢桶密封存储;Step 4: Ash and slag fall into the melting zone of the plasma gasification melting furnace for melting, capture and solidify radionuclides under the condition of 1200-1400°C, and finally generate harmless molten glass body, which will be cooled in 200L concrete steel barrel sealed storage;
步骤五:步骤三产生的高温烟气送入后续烟气净化处理系统处理,达标后排放。Step 5: The high-temperature flue gas generated in step 3 is sent to the subsequent flue gas purification treatment system for treatment, and discharged after reaching the standard.
进一步地,所述步骤五具体为从燃烧室出来的高温烟气通过与冷空气直接换热将温度降至700℃,然后通过三级高温陶瓷过滤器对颗粒物进行深度捕集,除尘后的烟气再次与冷空气进行换热,通过过量的空气将烟气温度急冷到200±20℃后进入活性炭吸附装置进行气体放射性核素脱除,然后进入脱酸系统对烟气中的酸性物质进行处理,然后利用HEPA高效空气过滤器对烟气中的细微粉尘进行再次的拦截处理,最后烟气通过引风机送入烟囱排到大气中。Further, the fifth step is specifically that the temperature of the high-temperature flue gas coming out of the combustion chamber is reduced to 700°C through direct heat exchange with cold air, and then the particulate matter is deeply collected through a three-stage high-temperature ceramic filter, and the dust-removed flue gas The gas is exchanged with cold air again, and the temperature of the flue gas is rapidly cooled to 200±20°C by excess air, and then enters the activated carbon adsorption device for gas radionuclide removal, and then enters the deacidification system to treat the acidic substances in the flue gas , and then use the HEPA high-efficiency air filter to intercept the fine dust in the flue gas again, and finally the flue gas is sent into the chimney through the induced draft fan and discharged into the atmosphere.
进一步地,所述步骤五中产生的飞灰经收集后统一送入等离子体气化熔融炉处理。Further, the fly ash generated in the fifth step is collected and sent to the plasma gasification melting furnace for processing.
本发明与现有技术相比,具有以下优点和效果:本发明利用热等离子体能量密度高,可处理高熔点的废物的特点,对低中放射性废物在气化区进行气化反应后形成的合成气送入燃烧室中进行燃烧形成小分子无害物质,产生的灰渣与玻璃体形成剂在熔融区进行熔融,将放射性核素稳定的固定在熔融玻璃体中,产生的烟气经净化处理满足空气质量标准的排放要求。相比于现有技术能够达到95%以上的减容比,大幅减少放射性废物处理存储空间,利用等离子体气化熔融炉处理放射性废物,有效减少处理成本和风险性,且便于灵活控制监控。本发明提供了一种减容效果好、安全可靠性高、核素稳定性好、系统工艺集成度高的环境友好型处理低中放射性固体废物的系统及方法,符合国家处理低中放射性固体废物的处理标准,达到低中放射性废物的最小化和稳定化处理的目的。Compared with the prior art, the present invention has the following advantages and effects: the present invention utilizes the characteristics of high energy density of thermal plasma and can process high-melting-point wastes, and the low- and medium-radioactive wastes are gasified in the gasification zone. The synthesis gas is sent into the combustion chamber for combustion to form small molecular harmless substances, and the generated ash and glass body forming agent are melted in the melting zone, and the radionuclides are stably fixed in the molten glass body, and the generated flue gas is purified to meet the Emission requirements of air quality standards. Compared with the existing technology, it can achieve a volume reduction ratio of more than 95%, greatly reducing the storage space for radioactive waste treatment, and using plasma gasification melting furnace to process radioactive waste, effectively reducing processing costs and risks, and facilitating flexible control and monitoring. The invention provides an environment-friendly system and method for treating low- and medium-radioactive solid waste with good volume reduction effect, high safety and reliability, good nuclide stability, and high system process integration, which meets the requirements of the national treatment of low- and medium-radioactive solid waste. The standard of treatment to achieve the purpose of minimization and stabilization of low and medium radioactive waste.
附图说明Description of drawings
图1是本发明的移动式小型中低放射性废物气化熔融处理系统的示意图。Fig. 1 is a schematic diagram of a mobile small-scale gasification and melting treatment system for low- and medium-level radioactive waste according to the present invention.
图2是本发明的移动式小型中低放射性废物气化熔融处理系统的连接原理图。Fig. 2 is a schematic connection diagram of the mobile small-scale gasification and melting treatment system for low- and medium-level radioactive waste of the present invention.
图3是本发明的等离子体气化熔融炉的示意图。Fig. 3 is a schematic diagram of the plasma gasification melting furnace of the present invention.
图4是本发明的移动式小型中低放射性废物气化熔融处理方法的流程图。Fig. 4 is a flowchart of the gasification and melting treatment method for mobile small-scale and low-level radioactive waste according to the present invention.
具体实施方式Detailed ways
下面通过实施例对本发明作进一步的详细说明,以下实施例是对本发明的解释而本发明并不局限于以下实施例。The present invention will be described in further detail below through examples, and the following examples are explanations of the present invention and the present invention is not limited to the following examples.
如图1或2所示,本发明的一种移动式小型中低放射性废物气化熔融处理系统,包含破碎机1、气动隔膜泵2、等离子体气化熔融炉3、熔融玻璃体接收器4、燃烧室5、一级直接换热器6、陶瓷过滤器7、二级直接换热器8、活性炭吸附塔9、脱酸洗涤塔10、高效空气过滤器11、烟囱12和移动设备13,破碎机1出料口通过无轴螺旋进料器与等离子体气化熔融炉3进料口连接,气动隔膜泵2的输出端通过管道与等离子体气化熔融炉3的进料口连接,熔融玻璃体接收器4设置在等离子体气化熔融炉3的下端灰渣出口,等离子体气化熔融炉3的合成气出口通过管道与燃烧室5进口连接,燃烧室5出口通过管道与一级直接换热器6入口连接,一级直接换热器6出口通过管道与陶瓷过滤器7入口连接,陶瓷过滤器7出口通过二级直接换热器8入口连接,二级直接换热器8出口通过管道与活性炭吸附塔9入口连接,活性炭吸附塔9出口通过管道与脱酸洗涤塔10入口连接,脱酸洗涤塔10出口通过管道与高效空气过滤器11入口连接,高效空气过滤器11出口与烟囱12连接,破碎机1、气动隔膜泵2、等离子体气化熔融炉3、熔融玻璃体接收器4、燃烧室5、一级直接换热器6、陶瓷过滤器7、二级直接换热器8、活性炭吸附塔9、脱酸洗涤塔10、高效空气过滤器11和烟囱12均设置在移动设备13上。As shown in Fig. 1 or 2, a kind of mobile small-scale medium and low radioactive waste gasification and melting treatment system of the present invention includes a crusher 1, a pneumatic diaphragm pump 2, a plasma gasification and melting furnace 3, a molten glass body receiver 4, Combustion chamber 5, primary direct heat exchanger 6, ceramic filter 7, secondary direct heat exchanger 8, activated carbon adsorption tower 9, deacidification washing tower 10, high efficiency air filter 11, chimney 12 and mobile equipment 13, broken The discharge port of machine 1 is connected to the feed port of plasma gasification melting furnace 3 through a shaftless screw feeder, the output end of pneumatic diaphragm pump 2 is connected to the feed port of plasma gasification melting furnace 3 through a pipeline, and the glass body is melted The receiver 4 is set at the ash outlet at the lower end of the plasma gasification melting furnace 3, the synthesis gas outlet of the plasma gasification melting furnace 3 is connected to the inlet of the combustion chamber 5 through a pipeline, and the outlet of the combustion chamber 5 directly exchanges heat with the first stage through a pipeline The inlet of the first-stage direct heat exchanger 6 is connected to the inlet of the ceramic filter 7 through a pipe, the outlet of the ceramic filter 7 is connected to the inlet of the second-stage direct heat exchanger 8, and the outlet of the second-stage direct heat exchanger 8 is connected to the inlet of the ceramic filter 7 through a pipe. The inlet of the activated carbon adsorption tower 9 is connected, the outlet of the activated carbon adsorption tower 9 is connected to the inlet of the deacidification washing tower 10 through a pipeline, the outlet of the deacidification washing tower 10 is connected to the inlet of the high-efficiency air filter 11 through a pipeline, and the outlet of the high-efficiency air filter 11 is connected to the chimney 12 , crusher 1, pneumatic diaphragm pump 2, plasma gasification melting furnace 3, molten glass receiver 4, combustion chamber 5, primary direct heat exchanger 6, ceramic filter 7, secondary direct heat exchanger 8, activated carbon The adsorption tower 9 , the deacidification washing tower 10 , the high-efficiency air filter 11 and the chimney 12 are all arranged on the mobile device 13 .
破碎机1用于对固体废物进行破碎,破碎到一定大小后送入无轴螺旋进料器。无轴螺旋进料器密封运行,设计具有防爆、防堵塞、耐高温的特点,将破碎后的废物送入等离子体气化熔融炉3。气动隔膜泵2用于直接将放射性液体废物输送至等离子体气化熔融炉3。等离子体气化熔融炉进料口上方连接的进料装置包括相连的进料仓,并设有对应的控制阀。Crusher 1 is used for crushing solid waste, which is sent to a shaftless screw feeder after being crushed to a certain size. The shaftless screw feeder operates in a sealed manner, and is designed to be explosion-proof, anti-clogging, and high-temperature resistant, and feeds the crushed waste into the plasma gasification melting furnace3. The pneumatic diaphragm pump 2 is used to directly transport the radioactive liquid waste to the plasma gasification melting furnace 3 . The feed device connected above the feed inlet of the plasma gasification melting furnace includes a connected feed bin and is provided with a corresponding control valve.
如图3所示,等离子体气化熔融炉3包含炉盖301和炉身302,炉盖301扣设在炉身302上端,炉盖301上设置有与炉膛连通的固体废物进料口303、液体废物进料口304和观察测量窗口305,固体废物进料口303上设置有进料仓305和控制阀门306,进料仓305为圆形漏斗并且进料仓305下端与固体废物进料口303上端固定连接,控制阀门306设置在进料仓305下端用于控制投料量。As shown in Figure 3, the plasma gasification melting furnace 3 comprises a furnace cover 301 and a furnace body 302, the furnace cover 301 is buckled on the upper end of the furnace body 302, and the furnace cover 301 is provided with a solid waste feed port 303 communicating with the furnace, Liquid waste feed port 304 and observation measurement window 305, solid waste feed port 303 is provided with feed bin 305 and control valve 306, feed bin 305 is a circular funnel and feed bin 305 lower end and solid waste feed port The upper end of 303 is fixedly connected, and the control valve 306 is arranged at the lower end of the feeding bin 305 for controlling the feeding amount.
炉身302内壁上设置有隔热保温层311,炉身302一侧侧壁上设置有空气导入孔308,炉身302另一侧侧壁上设置有合成气出口309,炉身302内设置有炉排312,炉排312水平设置并固定在炉身302内壁上将炉膛分割为炉排上侧的气化区310和炉排下侧的熔融区313,熔融区313下端设置有熔池坩埚314,熔池坩埚314设置在炉身下端中心位置并且采用耐火材料制成,熔池坩埚314内设置有两根热等离子体炬315,熔池坩埚314下端开有与炉身302外侧贯穿的排放通孔316。热等离子体炬315一端从炉身外侧穿过炉身302侧壁设置在熔池坩埚314内,两根热等离子体炬315对称设置在炉身302两侧。排放通孔316周围布有感应线圈318,热阀317贯穿炉身302下端并且环绕设置在排放通孔316和感应线圈318外侧。通过中频电源感应加热控制热阀317开启与关闭,热阀317下端对接有熔融玻璃体接收器4用于承载熔融玻璃体并运输至储存间。The inner wall of the furnace body 302 is provided with a thermal insulation layer 311, the side wall of the furnace body 302 is provided with an air inlet hole 308, the other side wall of the furnace body 302 is provided with a synthesis gas outlet 309, and the furnace body 302 is provided with a Fire grate 312, the fire grate 312 is arranged horizontally and fixed on the inner wall of the furnace body 302 to divide the furnace into a gasification area 310 on the upper side of the fire grate and a melting area 313 on the lower side of the fire grate, and a melting pool crucible 314 is provided at the lower end of the melting area 313 The melting pool crucible 314 is set at the center of the lower end of the furnace body and is made of refractory material. There are two thermal plasma torches 315 inside the melting pool crucible 314, and the lower end of the melting pool crucible 314 is provided with a discharge channel penetrating the outside of the furnace body 302. Hole 316. One end of the thermal plasma torch 315 is arranged in the melting pool crucible 314 through the side wall of the furnace body 302 from the outside of the furnace body, and two thermal plasma torches 315 are symmetrically arranged on both sides of the furnace body 302 . An induction coil 318 is arranged around the discharge through hole 316 , and a thermal valve 317 passes through the lower end of the furnace shaft 302 and is arranged around the discharge through hole 316 and outside the induction coil 318 . The opening and closing of the thermal valve 317 is controlled by the induction heating of the intermediate frequency power supply. The lower end of the thermal valve 317 is docked with a molten glass body receiver 4 for carrying the molten glass body and transporting it to the storage room.
热等离子体炬315为非转移弧直流等离子体炬,采用氮气、空气作为等离子体工作介质。直流等离子体炬被均布于等离子体气化熔融炉熔池坩埚侧上方,其轴向方向与炉体的中心轴成小于90°的夹角,直流等离子体炬的使用个数为2个,分别外接等离子体控制电源。等离子体气化熔融炉的轴向布有多个热电偶用于炉膛内轴向温度分布的监测。热阀317的排放通孔采用高功率石墨,周围布有感应线圈,外接中频电源。The thermal plasma torch 315 is a non-transferred arc DC plasma torch, using nitrogen and air as the plasma working medium. The DC plasma torches are evenly distributed above the crucible side of the plasma gasification melting furnace, and the axial direction forms an angle of less than 90° with the central axis of the furnace body. The number of DC plasma torches used is 2, Connect the plasma control power supply externally. A plurality of thermocouples are arranged in the axial direction of the plasma gasification melting furnace for monitoring the axial temperature distribution in the furnace. The discharge through hole of the thermal valve 317 is made of high-power graphite, surrounded by an induction coil, and externally connected with an intermediate frequency power supply.
本系统中的等离子体气化熔融炉为全密闭装置,在微负压工作状态下运行,系统装置全过程自动控制操作。所处理的低中放射性废物在等离子体气化熔融炉的气化区反应,反应产生的合成气送入燃烧室,产生的灰渣与玻璃体形成剂在熔融区经热等离子体高温熔融处理后产生可有效捕集放射性核素、重金属或其它有毒有害物质、浸出率极低的熔融玻璃体。The plasma gasification melting furnace in this system is a fully enclosed device, which operates under a slight negative pressure working condition, and the whole process of the system device is automatically controlled and operated. The treated low and medium radioactive waste reacts in the gasification zone of the plasma gasification melting furnace, and the synthesis gas produced by the reaction is sent into the combustion chamber, and the ash and glass forming agent produced are produced after the high-temperature melting treatment of thermal plasma in the melting zone. It can effectively capture radionuclides, heavy metals or other toxic and harmful substances, and the molten glass body with extremely low leaching rate.
一种移动式小型中低放射性废物气化熔融处理方法,包含以下步骤:A mobile small-scale low-to-medium radioactive waste gasification melting treatment method, comprising the following steps:
步骤一:低中放射性劳保用品经破碎机粉碎后由无轴螺旋进料器送入等离子体气化熔融炉,低中放射性液体废物通过气动隔膜泵送入等离子体气化熔融炉;Step 1: The low and medium radioactive labor protection products are crushed by the crusher and sent to the plasma gasification melting furnace by the shaftless screw feeder, and the low and medium radioactive liquid waste is sent into the plasma gasification melting furnace through the pneumatic diaphragm pump;
步骤二:低中放射性劳保用品和低中放射性液体废物进入等离子体气化熔融炉内气化区,在1000-1200℃条件下发生气化反应形成合成气和灰渣;Step 2: Low and medium radioactive labor protection products and low and medium radioactive liquid waste enter the gasification zone of the plasma gasification melting furnace, and gasification reaction occurs at 1000-1200 ° C to form synthesis gas and ash;
步骤三:产生的合成气经引风机送入燃烧室进行燃烧处理,形成无害化的小分子气体,灰渣收集后返送至等离子体气化熔融炉处理;Step 3: The generated synthesis gas is sent to the combustion chamber by the induced draft fan for combustion treatment to form harmless small molecular gas, and the ash is collected and returned to the plasma gasification melting furnace for processing;
步骤四:灰渣落入等离子体气化熔融炉内的熔融区进行熔融,在1200-1400℃条件下捕集和固化放射性核素最终生成无害化的熔融玻璃体,经冷却后在200L混凝土钢桶密封存储;Step 4: Ash and slag fall into the melting zone of the plasma gasification melting furnace for melting, capture and solidify radionuclides under the condition of 1200-1400°C, and finally generate harmless molten glass body, which will be cooled in 200L concrete steel barrel sealed storage;
步骤五:步骤三产生的高温烟气送入后续烟气净化处理系统处理,达标后排放。产生的飞灰经收集后统一送入等离子体气化熔融炉处理。Step 5: The high-temperature flue gas generated in step 3 is sent to the subsequent flue gas purification treatment system for treatment, and discharged after reaching the standard. The generated fly ash is collected and sent to the plasma gasification melting furnace for treatment.
从燃烧室出来的高温烟气通过与冷空气直接换热将温度降至700℃,然后通过三级高温陶瓷过滤器对颗粒物进行深度捕集,除尘后的烟气再次与冷空气进行换热,通过过量的空气将烟气温度急冷到200±20℃后进入活性炭吸附装置进行气体放射性核素脱除,然后进入脱酸系统对烟气中的酸性物质进行处理,然后利用HEPA高效空气过滤器对烟气中的细微粉尘进行再次的拦截处理,最后烟气通过引风机送入烟囱排到大气中。The high-temperature flue gas from the combustion chamber reduces the temperature to 700°C through direct heat exchange with the cold air, and then passes through the three-stage high-temperature ceramic filter to deeply capture the particulate matter, and the dust-removed flue gas exchanges heat with the cold air again, The temperature of the flue gas is rapidly cooled to 200±20°C through excess air, and then enters the activated carbon adsorption device for gas radionuclide removal, and then enters the deacidification system to treat the acidic substances in the flue gas, and then uses the HEPA high-efficiency air filter to treat the acidic substances in the flue gas. The fine dust in the flue gas is intercepted again, and finally the flue gas is sent into the chimney through the induced draft fan and discharged into the atmosphere.
本方法全程采用自动化操作,产生的固体废弃物熔融玻璃体经接收器接样产生的玻璃体冷却后装入200L混凝土钢桶中进行储存,产生的废气经CEMS在线监测满足大气污染物综合排放标准后排放至大气,整个流程中的废水满足核电厂防辐射规定达标排放。This method adopts automatic operation in the whole process, and the solid waste molten glass produced by the receiver is cooled and stored in a 200L concrete steel drum, and the waste gas produced is discharged after being monitored online by CEMS to meet the comprehensive emission standard of air pollutants To the atmosphere, the wastewater in the whole process meets the radiation protection regulations of nuclear power plants and discharges up to standard.
本发明利用热等离子体能量密度高,可处理高熔点的废物的特点,对低中放射性废物在气化区进行气化反应后形成的合成气送入燃烧室中进行燃烧形成小分子无害物质,产生的灰渣与玻璃体形成剂在熔融区进行熔融,将放射性核素稳定的固定在熔融玻璃体中,产生的烟气经净化处理满足空气质量标准的排放要求。相比于现有技术能够达到95%以上的减容比,大幅减少放射性废物处理存储空间,利用等离子体气化熔融炉处理放射性废物,有效减少处理成本和风险性,且便于灵活控制监控。本发明提供了一种减容效果好、安全可靠性高、核素稳定性好、系统工艺集成度高的环境友好型处理低中放射性固体废物的系统及方法,符合国家处理低中放射性固体废物的处理标准,达到低中放射性废物的最小化和稳定化处理的目的。The invention utilizes the characteristics of high energy density of thermal plasma and can process wastes with high melting points, and sends the synthesis gas formed after the gasification reaction of low and medium radioactive wastes in the gasification zone into the combustion chamber for combustion to form small molecular harmless substances , the generated ash and vitreous body forming agent are melted in the melting zone, and the radionuclide is stably fixed in the molten glass body, and the generated flue gas is purified to meet the emission requirements of the air quality standard. Compared with the existing technology, it can achieve a volume reduction ratio of more than 95%, greatly reducing the storage space for radioactive waste treatment, and using plasma gasification melting furnace to process radioactive waste, effectively reducing processing costs and risks, and facilitating flexible control and monitoring. The invention provides an environment-friendly system and method for treating low- and medium-radioactive solid waste with good volume reduction effect, high safety and reliability, good nuclide stability, and high system process integration, which meets the requirements of the national treatment of low- and medium-radioactive solid waste. The standard of treatment to achieve the purpose of minimization and stabilization of low and medium radioactive waste.
本说明书中所描述的以上内容仅仅是对本发明所作的举例说明。本发明所属技术领域的技术人员可以对所描述的具体实施例做各种修改或补充或采用类似的方式替代,只要不偏离本发明说明书的内容或者超越本权利要求书所定义的范围,均应属于本发明的保护范围。The above content described in this specification is only an illustration of the present invention. Those skilled in the technical field to which the present invention belongs can make various modifications or supplements to the described specific embodiments or adopt similar methods to replace them, as long as they do not deviate from the content of the present invention specification or exceed the scope defined in the claims, all should Belong to the protection scope of the present invention.
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CN112664948A (en) * | 2020-12-23 | 2021-04-16 | 华中科技大学 | Nitrogen non-transferred arc plasma ship solid waste heat treatment method and system |
CN114963200A (en) * | 2022-05-27 | 2022-08-30 | 中国船舶重工集团公司第七一一研究所 | Melting combustion type solid waste treatment device |
CN115355504A (en) * | 2022-08-15 | 2022-11-18 | 浙江大学台州研究院 | Multiphase alternating current plasma torch and solid waste treatment device |
CN115355504B (en) * | 2022-08-15 | 2025-04-11 | 浙江大学台州研究院 | A multiphase AC plasma torch and solid waste treatment device |
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CN114963200A (en) * | 2022-05-27 | 2022-08-30 | 中国船舶重工集团公司第七一一研究所 | Melting combustion type solid waste treatment device |
CN115355504A (en) * | 2022-08-15 | 2022-11-18 | 浙江大学台州研究院 | Multiphase alternating current plasma torch and solid waste treatment device |
CN115355504B (en) * | 2022-08-15 | 2025-04-11 | 浙江大学台州研究院 | A multiphase AC plasma torch and solid waste treatment device |
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