<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">

高鐵低錳礦石氫基礦相轉化分選試驗研究

Hydrogen-based phase transformation and separation of high iron and low manganese ores

  • 摘要: 錳鐵礦石是錳、鐵選冶的重要原料,由于類質同象及微細粒嵌布等因素影響,錳與鐵難以實現高效分離并綜合利用. 針對高鐵低錳礦石制定了氫基礦相轉化–磁選工藝流程,并考察了焙燒溫度、焙燒時間、還原氣體體積分數及總氣量對錳鐵分離及二價錳轉化率效果的影響. 結果表明,在焙燒溫度660 ℃、CO與H2體積比1∶3、焙燒時間30 min、還原氣體體積分數60%、總氣量500 mL·min–1、磁場強度8.51×104 A·m–1的條件下,可獲得鐵品位55.24%、回收率91.07%的鐵精礦及全錳品位34.80%、回收率77.11%、二價錳轉化率88.79%的錳精礦. 化學成分分析、X射線衍射(XRD)分析、掃描電子顯微鏡-能譜分析(SEM-EDS)均表明錳礦物與鐵礦物實現了有效的分離,原礦中的主要金屬礦物褐鐵礦、軟錳礦轉化為磁鐵礦、金屬鐵和方錳礦,二氧化硅等脈石礦物主要富集在錳精礦中. 研究表明,通過控制氫基礦相轉化工藝條件,錳精礦中二價錳含量顯著提高,鐵礦物和錳礦物可實現高效分離,且實現了原礦石全組分利用及無尾選礦的目的. 氫基礦相轉化技術為高鐵低錳礦石的清潔高效利用提供了新方法,有望實現鐵錳礦物高溫還原過程的異步轉化和同步分離,達到“源頭減量、高效轉化、精準回收”的目標,實現良好的經濟效益和社會效益.

     

    Abstract: Ferromanganese ore is an important raw material for the beneficiation and smelting of manganese and iron. The efficient separation of manganese and iron is challenging due to the isomorphism and dispersion of fine particles. The process of hydrogen-based mineral phase transformation and magnetic separation was developed, and the effects of roasting temperature, roasting time, reduction gas concentration, and total gas flow on the separation of ferromanganese and the rate of conversion of divalent manganese were investigated. Iron concentrate with 55.24% iron grade and 91.07% recovery and manganese concentrate with 34.80% manganese grade, 77.11% recovery, and 88.79% conversion of Mn2+ were obtained under the roasting temperature of 660 ℃, roasting duration of 30 min, volume ratio of carbon monoxide to hydrogen of 1∶3, reduction gas volume fraction of 60%, total gas flow rate of 500 mL·min–1, and magnetic field intensity of 8.51 × 104 A·m–1. Chemical composition analysis, X-ray diffraction (XRD) analysis, and scanning electron microscope-energy dispersion spectra (SEM-EDS) analysis confirmed the effective separation of manganese and iron minerals. The raw ore was mainly composed of limonite, pyrolusite, and quartz. Most weakly magnetic iron ores were transformed into strong magnetic iron minerals after suspension magnetization roasting, whereas pyrolusite was transformed into manganosite after reduction roasting. The primary iron mineral in the iron concentrate was magnetite, containing a small amount of metallic iron. The main manganese mineral in manganese concentrate was manganosite, and the gangue mineral was quartz. Due to the remarkable differences in the magnetic properties of the iron and manganese minerals, efficient separation was achieved through magnetic means. The content of divalent manganese in the manganese concentrate was increased considerably by controlling the process conditions during the hydrogen-based mineral phase transformation, enabling the manganese mineral to be extracted easily by leaching. Thus, the goal of full component utilization of the raw ore and tailless beneficiation was achieved. This novel approach for the clean and efficient utilization of high iron and low manganese ores holds promise for the conversion and synchronous separation of the iron and manganese minerals, achieving the goal of “source reduction, efficient conversion, and precise recovery,” and achieving excellent economic and social benefits.

     

/

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