CN111336526A - A multi-electrode plasma melting furnace - Google Patents
A multi-electrode plasma melting furnace Download PDFInfo
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- 238000002844 melting Methods 0.000 title claims abstract description 55
- 230000008018 melting Effects 0.000 title claims abstract description 55
- 239000007788 liquid Substances 0.000 claims abstract description 28
- 238000010438 heat treatment Methods 0.000 claims abstract description 26
- 238000005192 partition Methods 0.000 claims abstract description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims abstract description 6
- 238000005485 electric heating Methods 0.000 claims abstract description 6
- 239000003546 flue gas Substances 0.000 claims abstract description 6
- 239000011449 brick Substances 0.000 claims description 9
- 239000012774 insulation material Substances 0.000 claims description 3
- 238000002955 isolation Methods 0.000 claims 1
- 239000010881 fly ash Substances 0.000 abstract description 16
- 238000012423 maintenance Methods 0.000 abstract description 5
- 238000004017 vitrification Methods 0.000 abstract description 5
- 238000004519 manufacturing process Methods 0.000 abstract description 2
- 239000000463 material Substances 0.000 abstract 1
- 235000019353 potassium silicate Nutrition 0.000 abstract 1
- 239000000155 melt Substances 0.000 description 10
- 239000011521 glass Substances 0.000 description 8
- 238000000034 method Methods 0.000 description 7
- 238000005516 engineering process Methods 0.000 description 4
- 229910001385 heavy metal Inorganic materials 0.000 description 4
- 239000002893 slag Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 239000006060 molten glass Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 150000002013 dioxins Chemical class 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000002920 hazardous waste Substances 0.000 description 2
- 238000012986 modification Methods 0.000 description 2
- 230000004048 modification Effects 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 230000008023 solidification Effects 0.000 description 2
- 239000002918 waste heat Substances 0.000 description 2
- 239000002956 ash Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 239000013522 chelant Substances 0.000 description 1
- 239000000498 cooling water Substances 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000003344 environmental pollutant Substances 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000011810 insulating material Substances 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 231100000719 pollutant Toxicity 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000010791 quenching Methods 0.000 description 1
- 230000000171 quenching effect Effects 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 239000000779 smoke Substances 0.000 description 1
- 239000002910 solid waste Substances 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/085—High-temperature heating means, e.g. plasma, for partly melting the waste
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/442—Waste feed arrangements
- F23G5/444—Waste feed arrangements for solid waste
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/50—Control or safety arrangements
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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
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- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Plasma & Fusion (AREA)
- Environmental & Geological Engineering (AREA)
- Gasification And Melting Of Waste (AREA)
- Furnace Details (AREA)
Abstract
本发明公开了一种多电极等离子熔融炉,包括炉体,所述炉体内设置有熔融池,所述熔融池包括至少两呈直线排列的隔离加热区,各加热区的底部相互连通,各加热区上对应设置有至少一等离子炬,各等离子炬沿熔融池径向排布,所述炉体上设置有进料口以及熔融液出料口,进料口上连接有进料装置,熔融液出料口上可拆卸连接有出料装置,末端加热区顶部设置有烟气孔,用长方形的熔融池和两个以上的等离子炬,等离子炬间有分隔墙,能够更加有效控制飞灰熔融与玻璃化的加热过程,提高热效率,减少二次飞灰量,另外,可拆卸的电加热玻璃液出料装置,结构简单、模块化程度高,降低了设备制造与维护成本。
The invention discloses a multi-electrode plasma melting furnace, comprising a furnace body, a melting pool is arranged in the furnace body, the melting pool includes at least two isolated heating zones arranged in a straight line, the bottoms of the heating zones are communicated with each other, and each heating zone is At least one plasma torch is correspondingly arranged on the area, and each plasma torch is arranged along the radial direction of the melting pool. The furnace body is provided with a feeding port and a molten liquid discharge port. A discharge device is detachably connected to the material port, and a flue gas hole is arranged at the top of the end heating zone. A rectangular melting pool and two or more plasma torches are used. There is a partition wall between the plasma torches, which can more effectively control the melting and vitrification of fly ash. In addition, the detachable electric heating liquid glass discharge device has a simple structure and a high degree of modularity, which reduces the cost of equipment manufacturing and maintenance.
Description
技术领域technical field
本发明涉及固态废弃物无害化处理技术领域,具体为一种多电极等离子熔融炉及处理方法。The invention relates to the technical field of harmless treatment of solid waste, in particular to a multi-electrode plasma melting furnace and a treatment method.
背景技术Background technique
目前,我国生活垃圾的年处理量为20000万吨以上,接近50%采用焚烧发电的处理方法,焚烧炉飞灰产生量约为入炉垃圾量的3-5%,取4%计算,每年需要处理的飞灰量达到400万吨以上。At present, the annual processing volume of domestic waste in my country is more than 200 million tons, nearly 50% of which are treated by incineration power generation. The amount of fly ash processed reaches more than 4 million tons.
焚烧飞灰作为危险废物,二噁英和重金属含量都较高,其治理技术受到人们的广泛关注。目前处理的主要方式是飞灰螯合稳定化进入危险废物安全填埋场处置,这种处理方式成本高,需要土地资源大,不能从根本上解决问题,因此寻找一项既能减少灰渣体积、有效除去毒性又能使处理后的产物可以再利用的技术已成为一项紧迫的任务。Incineration fly ash, as a hazardous waste, has high content of dioxins and heavy metals, and its treatment technology has received extensive attention. At present, the main method of treatment is to chelate and stabilize fly ash and put it into a safe landfill for disposal of hazardous waste. This treatment method is costly and requires a lot of land resources, and cannot fundamentally solve the problem. Therefore, it is necessary to find a solution that can reduce the volume of ash , The technology that effectively removes toxicity and makes the treated product reusable has become an urgent task.
等离子高温熔融技术是把垃圾焚烧飞灰在1300℃以上的高温状态下熔化成液态,再将液态熔渣经过气冷或水淬处理,产生玻璃态熔渣,飞灰中的二噁英等有机污染物受热分解破坏,飞灰中的重金属有效地固溶在玻璃态熔渣中。焚烧飞灰经过熔融后,密度大大增加,减容可达2/3以上,而且稳定的熔渣可作为路基等建筑材料,达到有效利用的目的。The plasma high-temperature melting technology is to melt the waste incineration fly ash into a liquid state at a high temperature above 1300 °C, and then process the liquid slag through air cooling or water quenching to produce glassy slag, dioxins and other organic compounds in the fly ash. The pollutants are destroyed by thermal decomposition, and the heavy metals in the fly ash are effectively dissolved in the glassy slag. After the incineration fly ash is melted, the density is greatly increased, the volume reduction can reach more than 2/3, and the stable slag can be used as roadbed and other building materials to achieve the purpose of effective utilization.
然而,等离子体熔融炉炉体结构复杂、稳定性差、耗电量大,高昂的运行与维护成本等问题严重阻碍了该项技术的推广应用由此可见,有必要为飞灰处置提供一种性能稳定、能效高、运行成本低的等离子熔融炉,以解决上述技术问题。However, the complex structure of the plasma melting furnace body, poor stability, high power consumption, high operation and maintenance costs and other problems have seriously hindered the popularization and application of this technology. It can be seen that it is necessary to provide a performance for fly ash disposal. Plasma melting furnace with stable, high energy efficiency and low operating cost to solve the above technical problems.
发明内容SUMMARY OF THE INVENTION
本发明的目的在于提供一种多电极等离子熔融炉,用以解决上述背景技术中提出的问题。The purpose of the present invention is to provide a multi-electrode plasma melting furnace to solve the above-mentioned problems in the background art.
为实现上述目的,本发明提供如下技术方案:To achieve the above object, the present invention provides the following technical solutions:
一种多电极等离子熔融炉,包括炉体,所述炉体内设置有熔融池,所述熔融池包括至少两呈直线排列的隔离加热区,各加热区的底部相互连通,各加热区上对应设置有至少一等离子炬,各等离子炬沿熔融池径向排布,所述炉体上设置有进料口以及熔融液出料口,进料口上连接有进料装置,熔融液出料口上可拆卸连接有出料装置,末端加热区顶部设置有烟气孔。A multi-electrode plasma melting furnace, comprising a furnace body, a melting pool is arranged in the furnace body, the melting pool includes at least two isolated heating zones arranged in a straight line, the bottoms of each heating zone are connected with each other, and correspondingly arranged on each heating zone There is at least one plasma torch, each plasma torch is arranged along the radial direction of the melting pool, the furnace body is provided with a feeding port and a molten liquid discharge port, the feeding port is connected with a feeding device, and the molten liquid discharge port is detachable A discharge device is connected, and a flue gas hole is arranged at the top of the end heating zone.
优选的,所述熔融池为长方形结构,所述等离子炬位于加热区的顶部,并沿熔融池长度方向排布。Preferably, the melting pool has a rectangular structure, and the plasma torch is located at the top of the heating zone and is arranged along the length of the melting pool.
优选的,通过隔墙将所述熔融池分隔成至少两所述加热区,隔墙的底部与熔融池底面之间形成熔融液通道,熔融液通过所述熔融液通道,隔墙的底部与熔融液之间存在间隙。Preferably, the melting pool is divided into at least two heating zones by a partition wall, a melt channel is formed between the bottom of the partition wall and the bottom surface of the melting pool, the melt passes through the melt channel, and the bottom of the partition wall is connected to the melt channel. There is a gap between the liquids.
优选的,所述间隙的高度为50毫米--300毫米。Preferably, the height of the gap is 50 mm to 300 mm.
优选的,所述熔融液出料口位于熔融液面的下方,其顶面至少低于熔融液面6毫米。Preferably, the molten liquid outlet is located below the molten liquid level, and its top surface is at least 6 mm lower than the molten liquid level.
优选的,所述熔融液出料口上设置有电加热棒。避免玻璃液流出等离子熔融炉前凝固。Preferably, an electric heating rod is provided on the molten liquid discharge port. Avoid solidification of the molten glass before it flows out of the plasma melting furnace.
优选的,所述炉体包括耐火砖,所述耐火砖的外部设置有外壳,所述外壳与耐火砖的外壁之间填充有保温材料。Preferably, the furnace body includes refractory bricks, an outer casing is provided on the outside of the refractory bricks, and a thermal insulation material is filled between the outer casing and the outer wall of the refractory bricks.
优选的,所述炉体包括下部腔体以及设置于下部腔体上方的顶盖。Preferably, the furnace body includes a lower cavity and a top cover disposed above the lower cavity.
与现有技术相比,本发明的有益效果是:Compared with the prior art, the beneficial effects of the present invention are:
本发明提供一种多电极等离子熔融炉,用长方形的熔融池和两个以上的等离子炬,等离子炬间有分隔墙,能够更加有效控制飞灰熔融与玻璃化的加热过程,提高热效率,减少二次飞灰量,另外,可拆卸的电加热玻璃液出料装置,结构简单、模块化程度高,降低了设备制造与维护成本。The invention provides a multi-electrode plasma melting furnace, which uses a rectangular melting pool and two or more plasma torches, and there is a partition wall between the plasma torches, which can more effectively control the heating process of fly ash melting and vitrification, improve thermal efficiency, and reduce two In addition, the detachable electric heating glass liquid discharge device has a simple structure and a high degree of modularity, which reduces the cost of equipment manufacturing and maintenance.
附图说明Description of drawings
图1为本发明的结构示意图;Fig. 1 is the structural representation of the present invention;
图2为本发明的俯视结构示意图。FIG. 2 is a schematic top view of the structure of the present invention.
具体实施方式Detailed ways
下面将结合本发明实施例中的附图,对本发明实施例中的技术方案进行清楚、完整地描述,显然,所描述的实施例仅仅是本发明一部分实施例,而不是全部的实施例。基于本发明中的实施例,本领域普通技术人员在没有做出创造性劳动前提下所获得的所有其他实施例,都属于本发明保护的范围。The technical solutions in the embodiments of the present invention will be clearly and completely described below with reference to the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, but not all of the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention.
请参阅图1-2,本发明提供一种技术方案:Please refer to Figure 1-2, the present invention provides a technical solution:
一种多电极等离子熔融炉,包括炉体100,所述炉体内设置有熔融池,所述熔融池包括两呈直线排列的隔离加热区,两加热区的底部相互连通,两加热区上分别对应设置有第一等离子炬120和第二等离子炬121,所述炉体上设置有进料口以及熔融液出料口116,进料口上连接有进料装置130,熔融液出料口上可拆卸连接有出料装置118,末端加热区顶部设置有烟气孔;所述炉体由内到外依次为耐火砖、保温材料以及外壳110;具体的所述耐火砖的外部设置有外壳,所述外壳与耐火砖的外壁之间填充有保温材料113,所述炉体包括下部腔体112以及设置于下部腔体上方的顶盖111,下部腔体形成所述熔融池,分体式的结构便于安装维护;进料口设置在顶盖左侧,下部腔体右侧设置有熔融液出料口,所述熔融液出料口位于熔融液面的下方,其顶面至少低于熔融液面6毫米。具体的,所述熔融池为长方形结构,所述等离子炬位于加热区的顶部,并沿熔融池长度方向排布,通过隔墙115将所述熔融池分隔成至少两所述加热区,隔墙的底部与熔融池底面之间形成熔融液通道,熔融液通过所述熔融液通道,隔墙的底部与熔融液液面150之间存在间隙,所述间隙的高度为50毫米--300毫米;隔墙115的顶部与顶盖111紧密安装。为了解决玻璃液出口的保温与出料口的维护问题,采用可拆卸的电加热出料装置,在熔融液出料口上设置有电加热棒117,优选硅钼棒作为加热元件,可以精度控制出料口的温度,避免玻璃液流出等离子熔融炉前凝固。A multi-electrode plasma melting furnace includes a
本申请的工作原理为:需处理的飞灰由进料装置130加入熔融池,在等离子炬120的加热下快速熔化,向出料装置118方向流动。等离子炬121对玻璃液进一步加热,使其进一步玻璃化与均质化,保证玻璃体对重金属的有效固化,等离子炬120和等离子炬121的隔墙实现加热空间的分隔,提高了加热效率。同过,通过对进料量与等离子炬功率的控制,可以有效控制飞灰熔化与玻璃化的温度,控制飞灰玻璃化过程,提高熔融处置效率。同时,不同熔融池尺寸与等离子炬功率的配置,使本实例的熔融炉能够适应从几吨到100吨每天的飞灰处理量;其次,等离子炬120为飞灰的熔化提供热量,产生的烟气通过隔墙115与玻璃液150间的间隙进入右边空间,与等离子炬121产生的烟气混合后从烟气孔114排出进入后续处理系统,隔墙115对熔融工作空间的分隔,实现了烟气的除尘,有效减少了玻璃化过程产生的二次飞灰。The working principle of the present application is as follows: the fly ash to be treated is fed into the melting pool from the
本实例还增设了一个能够使玻璃液快速冷却与固化的水喷射冷却出料装置140,冷却水喷嘴141喷射的冷水使玻璃液快速冷却与固化,获得能有效固化重金属的惰性玻璃体,送入玻璃体存储装置142中,冷却产生的蒸汽通过余热蒸汽回收系统可以在后续进行余热利用。This example also adds a water jet cooling and
尽管已经示出和描述了本发明的实施例,对于本领域的普通技术人员而言,可以理解在不脱离本发明的原理和精神的情况下可以对这些实施例进行多种变化、修改、替换和变型,本发明的范围由所附权利要求及其等同物限定。Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, and substitutions can be made in these embodiments without departing from the principle and spirit of the invention and modifications, the scope of the present invention is defined by the appended claims and their equivalents.
Claims (8)
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Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112728560A (en) * | 2021-01-28 | 2021-04-30 | 重庆新离子环境科技有限公司 | Plasma melting furnace device based on molten salt heating |
| CN112902192A (en) * | 2021-02-19 | 2021-06-04 | 中广核研究院有限公司 | Plasma melting furnace for recycling flue gas and working method thereof |
| CN113551236A (en) * | 2021-08-27 | 2021-10-26 | 上海中川国宇环境有限公司 | Plasma melting furnace and method of using the same |
| CN113566202A (en) * | 2021-07-08 | 2021-10-29 | 北京建筑材料科学研究总院有限公司 | Solid waste pretreatment system and method |
| CN114260297A (en) * | 2022-03-02 | 2022-04-01 | 中国恩菲工程技术有限公司 | Device and method suitable for fly ash melting and flue gas purification treatment |
| CN115138658A (en) * | 2022-07-21 | 2022-10-04 | 北京中科润宇环保科技股份有限公司 | Harmless reduction method and device for fly ash of waste incineration power plant |
Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4571259A (en) * | 1985-01-18 | 1986-02-18 | Westinghouse Electric Corp. | Apparatus and process for reduction of metal oxides |
| US4989522A (en) * | 1989-08-11 | 1991-02-05 | Sharpe Environmental Services | Method and system for incineration and detoxification of semiliquid waste |
| US5226949A (en) * | 1992-07-30 | 1993-07-13 | Retech, Inc. | Method and apparatus for removal of floating impurities on liquid |
| JPH11211053A (en) * | 1998-01-22 | 1999-08-06 | Ishikawajima Harima Heavy Ind Co Ltd | Ash melting furnace |
| JPH11270834A (en) * | 1998-03-25 | 1999-10-05 | Ishikawajima Harima Heavy Ind Co Ltd | Ash melting furnace |
| TW424080B (en) * | 1995-03-07 | 2001-03-01 | Canon Kk | Molten glass material and method and apparatus for manufacturing the same |
| KR20010026585A (en) * | 1999-09-07 | 2001-04-06 | 이종훈 | System and Treatment Method for Low-and Intermediate-Level Radioactive Waste |
| CN105344695A (en) * | 2015-10-28 | 2016-02-24 | 长安大学 | Waste incineration fly ash treatment method and device |
| CN109469910A (en) * | 2018-12-05 | 2019-03-15 | 航天环境工程有限公司 | A continuous overflow slag discharge plasma melting furnace and its application |
| CN212005699U (en) * | 2020-03-31 | 2020-11-24 | 浙江大凡智能科技有限公司 | Multi-electrode plasma melting furnace |
-
2020
- 2020-03-31 CN CN202010244989.6A patent/CN111336526A/en active Pending
Patent Citations (10)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US4571259A (en) * | 1985-01-18 | 1986-02-18 | Westinghouse Electric Corp. | Apparatus and process for reduction of metal oxides |
| US4989522A (en) * | 1989-08-11 | 1991-02-05 | Sharpe Environmental Services | Method and system for incineration and detoxification of semiliquid waste |
| US5226949A (en) * | 1992-07-30 | 1993-07-13 | Retech, Inc. | Method and apparatus for removal of floating impurities on liquid |
| TW424080B (en) * | 1995-03-07 | 2001-03-01 | Canon Kk | Molten glass material and method and apparatus for manufacturing the same |
| JPH11211053A (en) * | 1998-01-22 | 1999-08-06 | Ishikawajima Harima Heavy Ind Co Ltd | Ash melting furnace |
| JPH11270834A (en) * | 1998-03-25 | 1999-10-05 | Ishikawajima Harima Heavy Ind Co Ltd | Ash melting furnace |
| KR20010026585A (en) * | 1999-09-07 | 2001-04-06 | 이종훈 | System and Treatment Method for Low-and Intermediate-Level Radioactive Waste |
| CN105344695A (en) * | 2015-10-28 | 2016-02-24 | 长安大学 | Waste incineration fly ash treatment method and device |
| CN109469910A (en) * | 2018-12-05 | 2019-03-15 | 航天环境工程有限公司 | A continuous overflow slag discharge plasma melting furnace and its application |
| CN212005699U (en) * | 2020-03-31 | 2020-11-24 | 浙江大凡智能科技有限公司 | Multi-electrode plasma melting furnace |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN112728560A (en) * | 2021-01-28 | 2021-04-30 | 重庆新离子环境科技有限公司 | Plasma melting furnace device based on molten salt heating |
| CN112902192A (en) * | 2021-02-19 | 2021-06-04 | 中广核研究院有限公司 | Plasma melting furnace for recycling flue gas and working method thereof |
| CN112902192B (en) * | 2021-02-19 | 2024-03-22 | 中广核研究院有限公司 | Plasma melting furnace for recycling flue gas and working method thereof |
| CN113566202A (en) * | 2021-07-08 | 2021-10-29 | 北京建筑材料科学研究总院有限公司 | Solid waste pretreatment system and method |
| CN113551236A (en) * | 2021-08-27 | 2021-10-26 | 上海中川国宇环境有限公司 | Plasma melting furnace and method of using the same |
| CN114260297A (en) * | 2022-03-02 | 2022-04-01 | 中国恩菲工程技术有限公司 | Device and method suitable for fly ash melting and flue gas purification treatment |
| CN115138658A (en) * | 2022-07-21 | 2022-10-04 | 北京中科润宇环保科技股份有限公司 | Harmless reduction method and device for fly ash of waste incineration power plant |
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