中国有色金属学报
中國有色金屬學報
중국유색금속학보
THE CHINESE JOURNAL OF NONFERROUS METALS
2013年
6期
1732-1738
,共7页
牛丽萍%张廷安%周爱平%吕国志%赫冀成
牛麗萍%張廷安%週愛平%呂國誌%赫冀成
우려평%장정안%주애평%려국지%혁기성
氧化镁%直接热解%熔融氯化镁%动力学
氧化鎂%直接熱解%鎔融氯化鎂%動力學
양화미%직접열해%용융록화미%동역학
MgO%direct pyrolysis%molten state MgCl2%dynamics
利用 Kroll 法冶炼钛过程中还原蒸馏产生的熔融氯化镁,在通氧条件下,直接热解制备出超细的氧化镁粉体。考察热解温度、热解时间、氧气分压对熔融氯化镁热解效率的影响。通过单因素实验确定的最佳工艺条件如下:热解温度1000℃,输入氧分压0.08 MPa,热解时间50 min。优化条件下氯化镁的热解率达93.5%。实验制备的样品氧化镁经X射线衍射和扫描电镜分析:其平均粒径为80~100 nm,粒度分布均匀,分散性好,纯度很高,获得的氧化镁颗粒为不规则六面体形。热解反应的动力学研究表明:氯化镁热解过程的初始阶段受化学反应控制,表观活化能为93.7 kJ/mol;反应后期受扩散与化学反应混合控制,表观活化能为26.3 kJ/mol。
利用 Kroll 法冶煉鈦過程中還原蒸餾產生的鎔融氯化鎂,在通氧條件下,直接熱解製備齣超細的氧化鎂粉體。攷察熱解溫度、熱解時間、氧氣分壓對鎔融氯化鎂熱解效率的影響。通過單因素實驗確定的最佳工藝條件如下:熱解溫度1000℃,輸入氧分壓0.08 MPa,熱解時間50 min。優化條件下氯化鎂的熱解率達93.5%。實驗製備的樣品氧化鎂經X射線衍射和掃描電鏡分析:其平均粒徑為80~100 nm,粒度分佈均勻,分散性好,純度很高,穫得的氧化鎂顆粒為不規則六麵體形。熱解反應的動力學研究錶明:氯化鎂熱解過程的初始階段受化學反應控製,錶觀活化能為93.7 kJ/mol;反應後期受擴散與化學反應混閤控製,錶觀活化能為26.3 kJ/mol。
이용 Kroll 법야련태과정중환원증류산생적용융록화미,재통양조건하,직접열해제비출초세적양화미분체。고찰열해온도、열해시간、양기분압대용융록화미열해효솔적영향。통과단인소실험학정적최가공예조건여하:열해온도1000℃,수입양분압0.08 MPa,열해시간50 min。우화조건하록화미적열해솔체93.5%。실험제비적양품양화미경X사선연사화소묘전경분석:기평균립경위80~100 nm,립도분포균균,분산성호,순도흔고,획득적양화미과립위불규칙륙면체형。열해반응적동역학연구표명:록화미열해과정적초시계단수화학반응공제,표관활화능위93.7 kJ/mol;반응후기수확산여화학반응혼합공제,표관활화능위26.3 kJ/mol。
The molten magnesium chloride, from reduction-distillation process in Kroll method of titanium metallurgy, was used to produce ultra fine magnesia powder under the condition of oxygen by direct pyrolysis. The effects of pyrolysis temperature, pyrolysis time and oxygen pressure on the pyrolysis efficiency of molten MgCl2 were investigated. The single factor experiments show that the optimum reaction conditions are as follows:pyrolysis temperature 1 000℃, pyrolysis oxygen partial pressure 0.08 MPa and pyrolysis time 50 min. The pyrolysis rate of molten MgCl2 can reach 93.5%under the optimum conditions. The obtained MgO powder was analyzed by XRD and SEM. These MgO powders, showing an irregular hexahedral shape, have an average diameter of 80?100 nm with uniform size distribution, good dispersity and high purity. The dynamic study of pyrolysis reaction show that this reaction is controlled by chemical reaction at the initial stage of reaction, with the apparent activation energy Ea=93.7 kJ/mol. At the later reaction stage, both diffusion and chemical reaction become the restricting factors with the apparent activation energy Ea=26.3 kJ/mol.