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鋁電解槽廢陰極炭塊電?熱耦合處理過程數值模擬

盧婷婷 李榮斌 趙洪亮 謝明壯 劉風琴

盧婷婷, 李榮斌, 趙洪亮, 謝明壯, 劉風琴. 鋁電解槽廢陰極炭塊電?熱耦合處理過程數值模擬[J]. 工程科學學報, 2020, 42(6): 731-738. doi: 10.13374/j.issn2095-9389.2019.06.10.002
引用本文: 盧婷婷, 李榮斌, 趙洪亮, 謝明壯, 劉風琴. 鋁電解槽廢陰極炭塊電?熱耦合處理過程數值模擬[J]. 工程科學學報, 2020, 42(6): 731-738. doi: 10.13374/j.issn2095-9389.2019.06.10.002
LU Ting-ting, LI Rong-bin, ZHAO Hong-liang, XIE Ming-zhuang, LIU Feng-qin. Numerical simulation of electro?thermal coupling process for spent cathode carbon block from aluminum electrolysis cell[J]. Chinese Journal of Engineering, 2020, 42(6): 731-738. doi: 10.13374/j.issn2095-9389.2019.06.10.002
Citation: LU Ting-ting, LI Rong-bin, ZHAO Hong-liang, XIE Ming-zhuang, LIU Feng-qin. Numerical simulation of electro?thermal coupling process for spent cathode carbon block from aluminum electrolysis cell[J]. Chinese Journal of Engineering, 2020, 42(6): 731-738. doi: 10.13374/j.issn2095-9389.2019.06.10.002

鋁電解槽廢陰極炭塊電?熱耦合處理過程數值模擬

doi: 10.13374/j.issn2095-9389.2019.06.10.002
基金項目: 中央高校基本科研業務費專項資金資助項目(2302018FRF-TP-18-095A1);寧夏回族自治區重點研發計劃資助項目(2018BDE02050)
詳細信息
    通訊作者:

    E-mail:liufq@ustb.edu.cn

  • 中圖分類號: TF09

Numerical simulation of electro?thermal coupling process for spent cathode carbon block from aluminum electrolysis cell

More Information
  • 摘要: 廢陰極炭塊是鋁電解槽大修時產生的一種危險固體廢棄物,對其進行安全處置和資源化利用的關鍵是深度分離其中的有價組分炭和氟化鹽。采用火法工藝對廢陰極炭塊進行處理,明確了氟化鹽的揮發溫度。基于氟化鹽的揮發析出性質,設計了高溫熱處理電阻爐,并對其傳熱特性、控溫規律以及氟化鹽有效揮發區域進行了三維數值解析。實驗確定氟化物的有效揮發溫度為≥1700 ℃,該溫度段下其揮發率可達93.1%以上。通過模擬不同供電模式下爐內溫度場的演變規律,得到:在12 V升溫24 h,9 V保溫12 h的供電條件下,升溫階段爐內最高溫度可達2250 ℃,氟化鹽理論揮發區域占比可達98%;采用逐級遞減的電壓供給制度可以保證1700 ℃以上溫度區域維持20 h,大幅度延長了有效熱處理時間,有利于廢陰極炭塊中炭與氟化鹽的深度分離。

     

  • 圖  1  高溫電阻爐結構示意圖及爐膛內部細節

    Figure  1.  Schematic of the high temperature resistance furnace and its interior detail

    圖  2  高溫電阻爐沿x軸方向(x=1.605 m)的橫截面

    Figure  2.  Cross-section of the high temperature resistance furnace in x direction (x=1.605 m)

    圖  3  不同處理溫度與廢陰極炭塊燒損及氟化鹽揮發的關系

    Figure  3.  Relationship between burning loss of SCCB and volatilization of fluoride salts at different temperatures

    圖  4  不同加熱時間下中心截面溫度云圖(Z=0.89 m).(a)4 h;(b)8 h;(c)12 h;(d)16 h;(e)24 h;(f)36 h

    Figure  4.  Contours of temperature distribution in the cross section (Z=0.89 m) of the furnace at different heating time: (a) 4 h; (b) 8 h; (c) 12 h; (d) 16 h; (e) 24 h; (f) 36 h

    圖  5  監測線1溫度隨時間變化曲線

    Figure  5.  Variation in temperature of monitoring line with changing of heating time

    圖  6  沿監測線方向五層耐火保溫層隨時間溫度分布(X=1.605 m).(a)24 h;(b)28 h;(c)32 h;(d)36 h

    Figure  6.  Variations in temperature of refractory insulation along monitoring line at different heating time (X=1.605 m): (a) 24 h; (b) 28 h; (c) 32 h; (d) 36 h

    圖  7  供壓曲線

    Figure  7.  Modes of power supply

    圖  8  監測點溫度隨時間變化

    Figure  8.  Variations in temperature with heating time at monitoring point

    圖  9  氟化鹽揮發率隨時間變化

    Figure  9.  Volatilization rate of fluoride salts at different time

    表  1  爐型結構尺寸

    Table  1.   Structure size of the high temperature resistance furnace mm

    ParametersNumbers
    Length3210
    Height1680
    Width1780
    Thickness of carbon brick230
    Thickness of insulating filler65
    Thickness of high alumina brick230
    Thickness of insulating brick230
    Thickness of rock wool50
    Dimensions of electrode300×300×805
    Dimensions of furnace hearth500×500×1600
    Dimensions of furnace core50×50×1600
    下載: 導出CSV

    表  2  熱物性參數

    Table  2.   Thermophysical properties used in this study

    ParametersDensity /(kg?m?3Specific heat /(J?kg?1?K?1Thermal conductivity /(W?m?1?K?1Conductivity /(S?m?1
    Carbon block1500800101×10?10
    Insulating filler45014650.651×10?10
    High alumina brick150011000.7861×10?10
    Insulating brick100012000.31×10?10
    Rock wool1359000.061×10?10
    Graphite felt14009000.011×10?10
    SCCB85084062.127×103
    Electrode160070012.41.13×10?5
    下載: 導出CSV

    表  3  廢陰極炭塊的元素組成與含量

    Table  3.   Composition and the content of various elements in SCCB %

    CFNaAlCaFeElse
    59.216.7313.627.871.430.940.21
    下載: 導出CSV
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  • 收稿日期:  2019-06-10
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