张传福
冶金新工艺及其基础理论、有色冶金过程计算机模拟与优化控制、增值冶金、特种粉体的制备新方法及其形貌控制、环境材料与环境工程等
个性化签名
- 姓名:张传福
- 目前身份:
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学术头衔:
博士生导师
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学科领域:
有色金属冶金
- 研究兴趣:冶金新工艺及其基础理论、有色冶金过程计算机模拟与优化控制、增值冶金、特种粉体的制备新方法及其形貌控制、环境材料与环境工程等
张传福教授是我国知名冶金、材料学专家,日本东京大学工学博士,中南大学博士生导师,湖南省第八、九届政协委员,中国有色金属学会重冶学术委员会副主任,日本资源素材学会会员,长期致力于冶金新工艺及其基础理论、有色冶金过程计算机模拟与优化控制、增值冶金、特种粉体的制备新方法及其形貌控制、环境材料与环境工程等方面的研究与实践,取得了杰出成就。近年来,负责国家自然科学基金、国家“八•五”、“九•五”攻关等26项重大课题,获国家级、省部级奖5项,专利5项。从事教学科研工作三十多年来,已培养博士生12人,硕士生22人,博士后6人,出版专著两部,教材一部,在国内外发表论文150余篇。
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【期刊论文】Selective dissolution of gold in an alkaline thiourea solution by electrolysis
张传福
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-1年11月30日
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张传福
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-1年11月30日
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张传福
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【期刊论文】NON-POLLUTION PROCESS FOR COMPLEX REFRACTORY SILVER-GOLD ORES①
张传福, Xu Shengming, Zhang Chuanfu, Zhao Tiancong, Li Zuogang
Vol. 5 No. 4 TRANSACTIONS OF NFsoc Dec. 1995,-0001,():
-1年11月30日
Chemistry of lime roasting process for complex sulfided concentrate was described briefly, the chemical phases of gold, silver and carbonaceous substances in the concentrate were also in vestigated, and the influences of roasting temperature, time and stoichiometic ratio of hydrated lime on sulfur retention and silver extraction of the calcine were studied finally. Under the optimized conditions, gold-silver extractions exceeded 93% and 83%, respectively.
complex ore, carbonaceous substances, silver-gold concentrate, lime roasting
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张传福, 王智, 曾德文, 谭鹏夫
矿冶工程,1998,18(3):41-43,-0001,():
-1年11月30日
测定了半合成的不同成分的FeO-MgO-SiO2系炉渣粘度。在w(MgO)为6%~10%,w(Fe)/w(SiO2)为1.1~1.4,温度为1200~1500℃时,炉渣粘度随w(MgO)和w(Fe)/w(SiO2)的提高而增大;在w(MgO)<6%时,冶炼温度控制在1300℃即能保证顺利生产;当w(MgO)>10%时,镍冶炼炉渣的温度应控制在1360℃以上;在MgO含量较高时,可通过降低w(Fe)/w(SiO2)得到粘度较低的炉渣。金川闪速炉炉渣的合理w(Fe)/w(SiO2)为1.2左右。
氧化镁, 炉渣, 粘度
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【期刊论文】Electric arc furnace dust non2isothermal reduction kinetics①
张传福, ZHANG Chuan-fu, PENG Bing, PENG Ji, J. Lobel, A. K. Janusz
Vol. 10 No.4 Trans. Nonferrous Met. Soc. China Aug. 2000,-0001,():
-1年11月30日
Kinetic studies of the electric arc furnace (EAF) dust reduction process have been carried out under non-isothermal temperature condition. EAF dust pellets were made with carbon as the reducing agent and dolomite as the binder. A Thermo-Gravimetric Analyzer (TGA) was used to determine the mass loss of pellets, which were heated at an average rate of 40K/min up to 1500℃. The reduction degree was calculated by consideration of the pellet mass loss, evaporation of moisture, dust, zinc and lead at high temperature. The reduction process of EAF dust was divided into three steps related to the change in temperature and time. The non-isothermal reduction kinetics equations were set up to describe every step. The kinetics parameters such as apparent activation energies and frequency factors were established at the same time. It was found that the first step is chemically controlled, the second step is diffusion-controlled and the third step is strongly dependent on the initial content of carbon in the pellet. CrO can be reduced only in the last step by high temperature and high initial carbon content.
EAF dust recycles, chemical kinetics, non-isothermal reduction
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