Study in reduction-roast leaching manganese from low-grade manganese dioxide ores using cornstalk as reductant
Introduction
Manganese plays an important role in many fields, such as steel production, preparation of dietary additives, fertilizers, cells and fine chemicals (Sahoo et al., 2001, Hazek et al., 2006). Hence, many efforts have applied to develop a economical and efficient process to recover manganese from low-grade manganese dioxide ores. Because manganese dioxide is stable in acid or alkaline oxidizing conditions, the leaching of manganese must be carried out under reducing condition (Abbruzzese et al., 1990, Das et al., 1982). Coal is used as reductant in traditional technology in order to convert manganese dioxide to manganese oxide which can be leached by sulfuric acid (Sahoo and Rao, 1989). But this kind of method produces a great deal of smoke-dust, oxysulfide, nitrogen oxides, and so on, which pollute environment greatly. In addition, this method requires over 800 °C as reaction temperature, which is so high that most of reactors can not bear (Abbruzzese, 1990, Jiang et al., 2004, Ismail et al., 2004). There are also some new reduction methods reported, such as sucrose reduction leaching (Beolchini et al., 2001), H2O2 reduction leaching in HCl (Hazek et al., 2006), molasses reduction leaching (Su et al., 2008), glucose reduction leaching in acidic medium (Trifoni et al., 2001, Vegliò et al., 2001, Pagnanelli et al., 2004, Furlani et al., 2006). Recently, our research group found that low-grade manganese dioxide ores can be reduced fully by biomass cornstalk roasting at temperature of only 500 °C. Using sulfuric acid as the leaching agent, the manganese can be leached from the roasted product. Though the crude cornstalk is lighter than coal, it can be pulverized and compressed to the same volume with coal while their weights are identical. Hence, it is feasible to substitute cornstalk for coal with the roasters and storage facilities used in conventional industrialization production.
As we know, biomass cornstalk resource is abundant renewable resource. In 2007, the global total output of cornstalk was about 1.8 billion ton, which equalled to 900 million ton standard coal. It is expected that the global total output of cornstalk reaches 2.6 billion ton in 2010 which equals to 1.3 billion ton standard coal (Zhang and Zhou, 2007). Making use of cornstalk to reduce manganese dioxide ores can not only widen the channels of energy to lower the cost, but also comply with the requirement of green economy.
In this paper, using the low-grade manganese dioxide ore from Guangxi (China) and cornstalk from Beijing (China) as raw material, the effects of roasting and leaching condition on the leaching recovery were investigated. Manganese recovery of 90.2% was obtained under the experimental condition: manganese dioxide ore to cornstalk weight ratio of 10:3, ore size of 150 μm, roasting temperature of 500 °C, roasting time of 80 min, leaching stirring speed of 400 rpm, sulfuric acid concentration of 3 mol/L, leaching time of 40 min at 50 °C. For proving this technology can be applied widely due to the nature of cornstalk, not due to the particularity of Guangxi manganese ore, experimental conditions applicability of cornstalk as reductant to other types of low-grade manganese dioxide ores were also tried.
Section snippets
Low-grade manganese dioxide ore
The sample of low-grade manganese dioxide ore was obtained from Guangxi, China. The ore was crushed, ground and screened to provide raw material with particle size of 100% from 50 μm to 300 μm. The ore material was chemically analyzed for its major and minor elements (Table 1).
Cornstalk
The reductant employed in the experiment was cornstalk which had been processed by pulverizer. Its shape took on acicular and powder-like with diameter smaller than 2 mm, length smaller than 10 mm. The proximate analysis
Chemical reaction
The chemical reaction of biomass cornstalk during the roasting is as follow (Zhang et al., 2005):CxHyOz → CO + H2O
The reducing gas CO produced in the Eq. (1) provides a deoxidized ambience, which promotes the reduction reaction of low-grade manganese dioxide ores. The oxides of manganese are reduced from high-valent to low-valent (Ren, 1993, Momade and Momade, 1999):MnO2 → Mn2O3 → Mn3O4 → MnO
The chemical reactions involved in reduction process are in turn:MnO2 + CO → Mn2O3 + CO2Mn2O3 + CO → Mn3O4 + CO2Mn3O4 + CO → MnO + CO
Effect of weight ratio of manganese dioxide ore to cornstalk
Initial experiments were carried out by varying the weight ratio of manganese dioxide ore to cornstalk. The amount of ore was varied from 10 g to 30 g while keeping the roasting condition as: biomass cornstalk 6 g, 150 μm ore particle size, roasting temperature 500 °C for 80 min, and the leaching condition as: sulfuric acid 3 mol/L, liquid-to-solid ratio 5, leaching temperature 50 °C, stirring speed 400 rpm for 1 h. Namely, varied the weight ratio of manganese dioxide ore to biomass cornstalk
Conclusions
A reductive roasting process followed by leaching for low-grade manganese dioxide ores has been successfully demonstrated using cornstalk as reductant. The results indicated that cornstalk can reduce manganese dioxide fully at only 500 °C. The weight ratio of manganese dioxide ore to biomass cornstalk, the roasting time, ore particle size, the concentration of sulfuric acid and leaching temperature affected the leaching recovery significantly. The optimal condition for reduction-roast leaching
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