<th id="5nh9l"></th><strike id="5nh9l"></strike><th id="5nh9l"><noframes id="5nh9l"><th id="5nh9l"></th><strike id="5nh9l"></strike>
<progress id="5nh9l"><noframes id="5nh9l"><th id="5nh9l"><noframes id="5nh9l">
<th id="5nh9l"></th> <strike id="5nh9l"><noframes id="5nh9l"><span id="5nh9l"></span>
<progress id="5nh9l"><noframes id="5nh9l"><span id="5nh9l"><noframes id="5nh9l"><span id="5nh9l"></span><strike id="5nh9l"><noframes id="5nh9l"><strike id="5nh9l"></strike>
<span id="5nh9l"><noframes id="5nh9l">
<span id="5nh9l"><noframes id="5nh9l">
<span id="5nh9l"></span><span id="5nh9l"><video id="5nh9l"></video></span>
<th id="5nh9l"><noframes id="5nh9l"><th id="5nh9l"></th>
<progress id="5nh9l"><noframes id="5nh9l">

石油焦煅燒程度對鋁用炭陽極顯微結構及電解消耗的影響

Impact of coke calcination levels on the microstructure and consumption of carbon anodes in aluminum electrolysis

  • 摘要: 以不同煅燒程度石油焦為骨料,煤瀝青為黏結劑制備鋁用低煅焦炭陽極.通過激光共聚焦掃描顯微鏡和圖像分析方法對炭陽極孔隙結構進行分析表征,并考察陽極反應性和電解消耗性能.在煅后焦微晶尺寸1.7~2.7 nm范圍內降低石油焦煅燒程度,炭陽極小孔隙逐漸沿骨料-黏結劑界面演變為裂紋狀大孔隙,炭陽極孔隙率、形狀因子及連通率均先減小后增大,視孔隙比表面積呈減小趨勢.煅后焦微晶尺寸降低至1.9 nm較為適宜,對應的炭陽極空氣和CO2反應質量損失率最少為9.6%和3.0%,每噸鋁陽極碳耗為355.4 kg.低煅焦炭陽極過量消耗機制從以黏結劑選擇性消耗轉變為骨料與黏結劑共同消耗,使碳渣量減少.

     

    Abstract: Carbon anodes for aluminum electrolysis were made of different calcination levels of coke as an aggregate and coal pitch as a binder. The porous structure parameters of carbon anode materials were characterized by using laser confocal scanning microscopy and the image analysis method. The anodic reaction and electrolysis consumption were also investigated in a lab scale aluminum electrolysis cell. The results demonstrate that the micropores gradually extend to crack-like macropores along the aggregate-binder interface with increasing coke calcination levels. The porosity,aspect ratio and connectivity first decrease and then increase,while the specific surface area decreases. It is appropriate to reduce the crystallite height of calcined cokes to 1.9 nm,so that the corresponding anodes can have the air reactivity of 9.6%,the CO2 reactivity of 3.0%,and the anode consumption of 355.4 kg per ton aluminum. The excessive consumption mechanism for the low calcined anode cokes may change from selective consumption of the binder to co-consumption of both the aggregate and the binder,which can reduce the carbon dust and the total carbon consumption in aluminum electrolysis.

     

/

返回文章
返回
<th id="5nh9l"></th><strike id="5nh9l"></strike><th id="5nh9l"><noframes id="5nh9l"><th id="5nh9l"></th><strike id="5nh9l"></strike>
<progress id="5nh9l"><noframes id="5nh9l"><th id="5nh9l"><noframes id="5nh9l">
<th id="5nh9l"></th> <strike id="5nh9l"><noframes id="5nh9l"><span id="5nh9l"></span>
<progress id="5nh9l"><noframes id="5nh9l"><span id="5nh9l"><noframes id="5nh9l"><span id="5nh9l"></span><strike id="5nh9l"><noframes id="5nh9l"><strike id="5nh9l"></strike>
<span id="5nh9l"><noframes id="5nh9l">
<span id="5nh9l"><noframes id="5nh9l">
<span id="5nh9l"></span><span id="5nh9l"><video id="5nh9l"></video></span>
<th id="5nh9l"><noframes id="5nh9l"><th id="5nh9l"></th>
<progress id="5nh9l"><noframes id="5nh9l">
259luxu-164