Reduction behavior of zinc ferrite in EAF-dust recycling with CO gas as a reducing agent.

EAF-dust containing metal oxides can be regarded as an important source for zinc and iron. In this study, the reduction behavior of zinc ferrite with CO gas as a reducing agent under different temperatures was investigated to develop a new process for the recovery of zinc and iron from EAF-dust. The results of the phase studies with synthetic franklinite show that zinc substituted wustite, and spinel with low zinc content formed at lower temperatures from 450 to 850 °C due to incomplete zinc-iron-separation. Zinc ferrite was completely reduced to metallic zinc and iron at 950 °C. After evaporation and condensation, metallic zinc was collected in the form of zinc powder while iron, the reduction residue, was obtained in the form of direct reduced iron (DRI). The mass balance indicates a high zinc recovery ratio of over 99%. The new treatment process by thermal reduction with CO gas as a reducing agent achieved higher recovery and metallization grade of both zinc and iron from EAF-dust at lower temperatures than other commercial processes. The metallic products can be used directly as semi-products or as raw materials for refinery.

Removal of chloride from MSWI fly ash.

The high levels of alkali chloride and soluble metal salts present in MSWI fly ash is worth noting for their impact on the environment. In addition, the recycling or reuse of fly ash has become an issue because of limited landfill space. The chloride content in fly ash limits its application as basis for construction materials. Water-soluble chlorides such as potassium chloride (KCl), sodium chloride (NaCl), and calcium chloride hydrate (CaCl(2) · 2H(2)O) in fly ash are easily washed away. However, calcium chloride hydroxide (Ca(OH)Cl) might not be easy to leach away at room temperature. The roasting and washing-flushing processes were applied to remove chloride content in this study. Additionally, air and CO(2) were introduced into the washing process to neutralize the hazardous nature of chlorides. In comparison with the water flushing process, the roasting process is more efficient in reducing the process of solid-liquid separation and drying for the reuse of Cl-removed fly ash particles. In several roasting experiments, the removal of chloride content from fly ash at 1050°C for 3h showed the best results (83% chloride removal efficiency). At a solid to liquid ratio of 1:10 the water-flushing process can almost totally remove water-soluble chloride (97% chloride removal efficiency). Analyses of mineralogical change also prove the efficiency of the fly ash roasting and washing mechanisms for chloride removal.

Removal of chloride from electric arc furnace dust.

Electric arc furnace (EAF) dust with high chloride content increases the threat of dioxin emissions and the high chloride content reduces the value of recycled zinc oxide produced by EAF dust recycling plants. This study conducts a number of laboratory experiments to determine the technical feasibility of a new dechlorination method. These methods consist of a series of roasting processes and water washing processes. In the roasting process, EAF dust was heated in a tube furnace to evaluate the parameters of atmospheric conditions, roasting temperature, and roasting time. Results indicate that sulfation roasting is more efficient in reducing chloride content than other roasting processes. The water washing process can totally remove water-soluble chloride at a solid to liquid ratio of 1:10. However, the remaining water-insoluble substance is difficult to dechlorinate. For example, lead chloride forms a hydroxyl-halide (PbOHCl) and lead chloride carbonate (Pb(2)CO(3)Cl(2)) agglutinative matrix that is hard to wash away.

The characteristics of organic sludge/sawdust derived fuel.

A fundamental study of the characteristics of a sludge refuse-derived fuel (RDF) and the combustion behaviors were done. The test data demonstrate good results for the development of energy recovery technology of organic sludge or waste. The ash deposit formation propensity has been based on pretreatment, temperature and the ratio of organic sludge to sawdust. The usage of organic sludge and waste as an alternative fuel is cost effective and has environmental benefits.

Pore size and adsorptive capacity of unburned carbon affected by gasification with carbon dioxide.

Gasification of unburned carbon by using CO2 gas at temperatures of 950-1100 degrees C was performed, in order to modify the pore size distribution and adsorptive capacity of the carbon. Equipments such as N2 adsorption apparatus, mercury pore size analyzer, and SEM were used, where yield, specific surface area and methylene blue number for adsorptive capacity, pore size, and appearance of the carbon were analyzed. Results show that gasification of unburned carbon produces larger adsorptive capability as well as a larger specific surface area. While reacting with CO2 at 1100 degrees C for 45 min, the methylene blue numbers reach to 54-154 mg/g, and the specific surface areas reach to 113-235 m2/g, which signify the actual utility. All carbons in gasification form new pores in a mutual size approximately 0.1-0.01 microm, whose majority affects the adsorptive capacity and specific surface area of the carbon. Besides, their group appearance complies with the obvious flow-like pattern, containing carbon ingredients with various degrees of crystallinity in the surface of unburned carbon. The new pore, conclusively, forms from the lower crystalline carbon ingredient that gasified with CO2 earlier, in the flow-like pattern.