Synthetic zinc ferrite reduction by means of mixtures containing hydrogen and carbon monoxide

被引:29
作者
Junca, Eduardo [1 ]
de Oliveira, Jose Roberto [1 ]
Guisard Restivo, Thomaz Augusto [2 ]
Romano Espinosa, Denise Crocce [3 ]
Soares Tenorio, Jorge Alberto [3 ]
机构
[1] Fed Inst Educ Sci & Technol Espirito Santo, BR-29040780 Vitoria, ES, Brazil
[2] Univ Sorocaba, BR-18023000 Sorocaba, Brazil
[3] Univ Sao Paulo, Dept Chem Engn, BR-05424970 Sao Paulo, SP, Brazil
关键词
Kinetic analysis; Zinc ferrite; Thermogravimetric analysis; Reduction; Forced stepwise isothermal analysis; OXIDE REDUCTION; ZNO; KINETICS; ZNFE2O4; METHANE; FE2O3;
D O I
10.1007/s10973-015-4973-6
中图分类号
O414.1 [热力学];
学科分类号
摘要
Solid waste generation is one of the main problems in the steelmaking process. One of the most problematic waste products is the electric arc furnace dust, which is a by-product rich in iron and zinc and is present as zincite (zinc oxide) or franklinite (zinc ferrite). This work focuses on the reduction kinetics of synthetic zinc ferrite by gases containing hydrogen and carbon monoxide. This process was examined via forced stepwise isothermal analysis. The test was conducted at temperatures ranging from 500 to 950 A degrees C. Reduction of zinc was accomplished using a mixture of hydrogen and carbon monoxide in order to simulate reformed natural gas. The results indicated that reduction of zinc ferrite occurred in two stages (550-750 A degrees C and 800-900 A degrees C). The first stage was characterized by iron oxide reduction, where a mix control between nucleation and diffusion was determined. The apparent activation energy obtained was 71.5 kJ mol(-1). The second stage was characterized by zinc oxide reduction, where the controlling mechanism was identified as a mixed control between diffusion and phase boundary reaction. The apparent activation energy was 135.5 kJ mol(-1). The formation of a dense layer of metallic iron around the unreacted core may have caused the apparent activation energy to increase.
引用
收藏
页码:631 / 641
页数:11
相关论文
共 29 条
[11]   Carbothermal reduction of zinc ferrite [J].
Lee, JJ ;
Lin, CI ;
Chen, HK .
METALLURGICAL AND MATERIALS TRANSACTIONS B-PROCESS METALLURGY AND MATERIALS PROCESSING SCIENCE, 2001, 32 (06) :1033-1040
[12]   THE REDUCTION OF ZINC TITANATE AND ZINC-OXIDE SOLIDS [J].
LEW, S ;
SAROFIM, AF ;
FLYTZANI-STEPHANOPOULOS, M .
CHEMICAL ENGINEERING SCIENCE, 1992, 47 (06) :1421-1431
[13]   Comparison of reduction behavior of Fe2O3, ZnO and ZnFe2O4 by TPR technique [J].
Liang, Meisheng ;
Kang, Wenkai ;
Xie, Kechang .
JOURNAL OF NATURAL GAS CHEMISTRY, 2009, 18 (01) :110-113
[14]   The mechanism of reduction of iron oxide by hydrogen [J].
Lin, HY ;
Chen, YW ;
Li, CP .
THERMOCHIMICA ACTA, 2003, 400 (1-2) :61-67
[15]   Mineral phases of weathered and recent electric arc furnace dust [J].
Martins, Femanda Machado ;
dos Reis Neto, Jose Manoel ;
da Cunha, Carlos Jorge .
JOURNAL OF HAZARDOUS MATERIALS, 2008, 154 (1-3) :417-425
[16]   Study of the presence of fluorine in the recycled fractions during carbothermal treatment of EAF dust [J].
Menad, N ;
Ayala, JN ;
Garcia-Carcedo, F ;
Ruiz-Ayúcar, E ;
Hernández, A .
WASTE MANAGEMENT, 2003, 23 (06) :483-491
[17]   A STUDY OF THE MECHANISM OF REDUCTION WITH HYDROGEN OF PURE WUSTITE SINGLE-CRYSTALS [J].
MOUKASSI, M ;
STEINMETZ, P ;
DUPRE, B ;
GLEITZER, C .
METALLURGICAL TRANSACTIONS B-PROCESS METALLURGY, 1983, 14 (01) :125-132
[18]   Process simulation of natural gas steam reforming:: Fuel distribution optimisation in the furnace [J].
Olivieri, Agostino ;
Veglio, Francesco .
FUEL PROCESSING TECHNOLOGY, 2008, 89 (06) :622-632
[19]   The use of master plots for discriminating the kinetic model of solid state reactions from a single constant-rate thermal analysis (CRTA) experiment [J].
Perez-Maqueda, LA ;
Ortega, A ;
Criado, JM .
THERMOCHIMICA ACTA, 1996, 277 :165-173
[20]   The limiting process in steam methane reforming with gas diffusion into a porous catalytic wall in a flow reactor [J].
Saito, Motohiro ;
Kojima, Junichi ;
Iwai, Hiroshi ;
Yoshida, Hideo .
INTERNATIONAL JOURNAL OF HYDROGEN ENERGY, 2015, 40 (29) :8844-8855