Coke behavior with H2O in a hydrogen-enriched blast furnace: A review
Feng Zhou, Daosheng Peng, Kejiang Li, Alberto N. Conejo, Haotian Liao, Zixin Xiong, Dongtao Li, Jianliang Zhang
Coke behavior with H2O in a hydrogen-enriched blast furnace: A review
Hydrogen-enriched blast furnace ironmaking has become an essential route to reduce CO2 emissions in the ironmaking process. However, hydrogen-enriched reduction produces large amounts of H2O, which places new demands on coke quality in a blast furnace. In a hydrogen-rich blast furnace, the presence of H2O promotes the solution loss reaction. This result improves the reactivity of coke, which is 20%–30% higher in a pure H2O atmosphere than in a pure CO2 atmosphere. The activation energy range is 110–300 kJ/mol between coke and CO2 and 80–170 kJ/mol between coke and H2O. CO2 and H2O are shown to have different effects on coke degradation mechanisms. This review provides a comprehensive overview of the effect of H2O on the structure and properties of coke. By exploring the interactions between H2O and coke, several unresolved issues in the field requiring further research were identified. This review aims to provide valuable insights into coke behavior in hydrogen-rich environments and promote the further development of hydrogen-rich blast furnace ironmaking processes.
hydrogen ironmaking / coke behavior / blast furnace / gasification / microstructure / kinetics
[1] |
|
[2] |
|
[3] |
|
[4] |
Q. Shi, B. Zheng, Y. Zheng, et al., Co-benefits of CO2 emission reduction from China’s clean air actions between 2013–2020, Nat. Commun., 13(2022), No. 1, art. No. 5061.
|
[5] |
|
[6] |
L. Holappa, A general vision for reduction of energy consumption and CO2 emissions from the steel industry, Metals, 10(2020), No. 9, art. No. 1117.
|
[7] |
|
[8] |
|
[9] |
|
[10] |
|
[11] |
|
[12] |
|
[13] |
|
[14] |
X.B. Yu, Z.J. Hu, and Y.S. Shen, Modeling of hydrogen shaft injection in ironmaking blast furnaces, Fuel, 302(2021), art. No. 121092.
|
[15] |
J. Tang, M.S. Chu, F. Li, et al., Mathematical simulation and life cycle assessment of blast furnace operation with hydrogen injection under constant pulverized coal injection, J. Cleaner Prod., 278(2021), art. No. 123191.
|
[16] |
|
[17] |
|
[18] |
|
[19] |
A.M. Heikkilä, A.M. Koskela, M.O. Iljana, et al., Coke Gasification in blast furnace shaft conditions with H2 and H2O containing atmospheres, Steel Res. Int., 92(2021), No. 3, art. No. 2000456.
|
[20] |
|
[21] |
|
[22] |
Y. Ono, Y. Fukuda, Y. Sumitani, et al., Experimental and numerical study on degradation behavior of coke with CO2 or H2O gasification reaction at high temperature, Fuel, 309(2022), art. No. 122061.
|
[23] |
|
[24] |
|
[25] |
|
[26] |
M.W. Chapman, R.J. Nightingale, and B.J. Monaghan, Influence of coke ash on blast furnace hearth behaviour, [in] Australasian Conference on Chemical Engineering, 2011, P. 1.
|
[27] |
|
[28] |
|
[29] |
|
[30] |
|
[31] |
|
[32] |
|
[33] |
|
[34] |
|
[35] |
|
[36] |
|
[37] |
|
[38] |
|
[39] |
|
[40] |
|
[41] |
|
[42] |
|
[43] |
X.M. Zhang, S.Q. Wang, H. Chen, et al., Observation of carbon nanostructure and evolution of chemical structure from coal to graphite by high temperature treatment, using componential determination, X-ray diffraction and high-resolution transmission electron microscope, Fuel, 332(2023), No. 1, art. No. 126145.
|
[44] |
|
[45] |
|
[46] |
|
[47] |
Z.Z. Ding, Z. Sun, Q. Lu, et al., Boudouard reaction accompanied by graphitization of wrinkled carbon layers in coke gasification: A theoretical insight into the classical understanding, Fuel, 297(2021), art. No. 120747.
|
[48] |
|
[49] |
R. Guo, C. Duan, Z. Sun, et al., Effect of pore structure and matrix reactivity on coke reactivity and post-reaction strength, Metall. Res. Technol., 114(2017), No. 5, art. No. 504.
|
[50] |
|
[51] |
|
[52] |
|
[53] |
|
[54] |
|
[55] |
|
[56] |
|
[57] |
|
[58] |
|
[59] |
|
[60] |
|
[61] |
|
[62] |
W. Wang, B.W. Dai, R.S. Xu, Schenk, J. Wang, and Z.L. Xue, The Effect of H2O on the Reactivity and Microstructure of Metallurgical Coke, Steel Res. Int., 88(2017), No. 8, art. No. 1700063.
|
[63] |
L. Liang, Z. Sun, H. Zhang, et al., Theoretical insight into the competitive effect of CO2 and additive H2O in coke gasification, Chem. Eng. J., 461(2023), art. No. 142003.
|
[64] |
|
[65] |
|
[66] |
|
[67] |
|
[68] |
|
[69] |
|
[70] |
|
[71] |
|
[72] |
|
[73] |
|
[74] |
|
[75] |
|
[76] |
|
[77] |
|
[78] |
|
[79] |
|
[80] |
|
[81] |
|
[82] |
|
[83] |
|
[84] |
|
[85] |
|
[86] |
|
[87] |
|
[88] |
|
[89] |
|
[90] |
|
[91] |
M. Acik and Y.J. Chabal, Nature of Graphene Edges: A Review, Jpn. J. Appl. Phys., 50(2011), art. No. 070101.
|
[92] |
|
[93] |
|
[94] |
|
[95] |
|
[96] |
|
[97] |
|
[98] |
|
[99] |
|
[100] |
|
[101] |
|
[102] |
B. Van Der Velden, J. Trouw, R. Chaigneau, and J. Van Den Berg, Coke reactivity under simulated blast furnace conditions. [in] The 58 th Ironmaking Conference, Chicigo, 1999, p. 275.
|
[103] |
|
[104] |
|
[105] |
|
/
〈 | 〉 |