2009
DOI: 10.2355/isijinternational.49.1874
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Removal Behavior of Zn, Pb, K and Na from Cold Bonded Briquettes of Metallurgical Dust in Simulated RHF

Abstract: Removal behavior of Zn, Pb, K and Na from cold bonded briquettes made by mixing four typical metallurgical wastes, as blast furnace dust, converter dust, electric arc furnace dust and converter sludge with proper proportions, in a simulated RHF (Rotary Hearth Furnace) were investigated in this paper. Effects of temperature and C/O molar ratio on metallization rate of iron oxides, and effect of temperature on removal rate of elements Zn, Pb, K and Na were checked respectively. The results show that when reducti… Show more

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Cited by 31 publications
(11 citation statements)
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“…Furthermore, the binder determines whether the quality of the CBB can directly charge in the furnaces. Various kinds of binders such as pitch, molasses, starch, bentonite, sodium silicate and cement, or mixtures of these, have been used as binders [ 1 , 9 , 10 ]. For example, EI-Hussiny et al [ 1 ].…”
Section: Introductionmentioning
confidence: 99%
See 1 more Smart Citation
“…Furthermore, the binder determines whether the quality of the CBB can directly charge in the furnaces. Various kinds of binders such as pitch, molasses, starch, bentonite, sodium silicate and cement, or mixtures of these, have been used as binders [ 1 , 9 , 10 ]. For example, EI-Hussiny et al [ 1 ].…”
Section: Introductionmentioning
confidence: 99%
“…used pitch as a binder for the mixture of mill scale and blast furnace flue dust. Cui et al [ 9 ] used 2% bentonite as a binder for the mixture of blast furnace dust, converter dust, electric arc furnace dust and converter sludge. Kumar et al [ 7 ] investigated molasses, starch and sodium silicate as binders for the mixture of several types of dust and mill scale.…”
Section: Introductionmentioning
confidence: 99%
“…Depending on the atmospheric conditions in the off-gas treatment system, iron or iron oxide particles can be returned to the EAF. Thermodynamically, this treatment step drastically outperforms any HTMR natural gas RHF [5][6][7][8][9] 1250-1300°C Rotary hearth furnace Coke, binder, CZO, DRI/HBI Commercial* 200 (high Zn EAFD) natural gas Primus 10,11 1000-1100°C Multiple hearth Coal, air CZO, pig iron Commercial 100 furnace + EAF Ausmelt [12][13][14] 1250-1300°C Top Submerged Coal, CZO, Fe-slag Commercial 100 Lance furnace O 2 -enriched air (waste) ESRF 15,16 1300-1500°C EAF Binder, air, CZO, Pig iron, Commercial 36 electricity and slag Submerged 1300-1400°C Submerged plasma Coke, natural gas, CZO, Fe-slag (waste) Commercial 40 -60 Plasma [17][18][19] reactor fluxes, air, electricity PIZO [20][21][22] 1300-1500°C Induction furnace Coal, air, electricity CZO, pig iron Commercial 50 OxiCup 23 1500-1600°C Shaft furnace Coke, scrap, bricks CZO, molten Commercial 200 (dust (waste + cement + C) metal, and slag and sludge) Coke Packed Bed 24,25 1500-1600°C Shaft furnace Coke, fluxes, CZO, molten metal, Pilot Plant 10 O 2 -enriched air and slag LAMS 26,27 900-1100°C -CaCO 3 + heat CZO, Ca 2 Fe 2 O 5 for Lab-scale use in blast furnace EAFD+PVC pellets 28,29 800°C -PVC + heat ZnCl 2 , Fe+C pellets Lab-scale -* First large proof-of-concept plant is still ramping up to full production.…”
Section: Us Environmental Protection Agencymentioning
confidence: 99%
“…The reaction mechanism would be discussed in detail in the following section. If CaSO 4 was insufficient to react with K 2 O, K 2 O may volatilize into the gaseous phase,25 resulting in a lower recovery ratio of K.3.3. Mechanism of K-Feldspar Decomposition.…”
mentioning
confidence: 99%