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Regulation of carbon deposition during preparation process of hydrogen-rich reducing gas by natural gas reforming ——An application example of H-C-O system mass balance and chemical equilibrium diagram |
SHEN Fengman1, ZHANG Weiling1,2, ZHENG Aijun3, ZHENG Haiyan1, DING Zhimin1, LI Ji1 |
1. School of Metallurgy, Northeastern University, Shenyang 110819, Liaoning, China; 2. Department of Technical Management, Baosteel Zhanjiang Iron and Steel Co., Ltd., Zhanjiang 524072, Guangdong, China; 3. Xuanhua Iron and Steel Group Co., Ltd., HBIS, Xuanhua 075100, Hebei, China |
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Abstract If the operating parameters in the process of preparing hydrogen-rich reducing gas are not properly controlled, the problem of carbon deposition will occur, which will affect the stability of the process of preparing hydrogen-rich reducing gas by using natural gas or coke oven gas as the gas source. Therefore, it is necessary to investigate and control the problem of carbon deposition in the process of preparing hydrogen-rich reducing gas that meets the requirements of the direct reduction iron process. The problem of "carbon deposition" in the process of preparing hydrogen-rich reducing gas from natural gas reforming or coke oven gas reforming process was discussed by using the "H-C-O system mass and chemical balance diagram" and the principle of chemical equilibrium. Assuming that the natural gas reforming or coke oven gas reforming system is at the critical state of carbon deposition, the relationships between the carbon deposition curve and the factors of nH2/nCO of the reduction gas, reforming temperature, and total system pressure were determined, the critical carbon deposition curve in the process of reforming natural gas or coke oven gas to hydrogen-rich reducing gas was given from the perspective of thermodynamics, the "carbon deposition region" and "non-carbon deposition region" were obtained, and the process parameters, such as the reforming temperature of hydrogen-rich reducing gas and the total system pressure, which can inhibit the carbon deposition and meet the required nH2/nCO of direct reduction iron, were given. The results show that in order to ensure nH2/nCO and the total amount of the effective composition of φ(H2)+φ(CO)simultaneously meet the requirements for the composition of the direct reduction gas, the reforming temperature must be higher than 800 ℃ under Ptot=0.1 MPa; The conversion of CH4 decreased with the increase of total system pressure; For low nH2/nCO (=2), the carbon deposition region will increase with the increase of the total system pressure and for nH2/nCO (=5), with the increase of the total pressure of the system, the carbon deposition region becomes smaller, which is because the gasification reaction of carbon is the mainstream reaction when nH2/nCO is low and increasing the total system pressure will enhance the carbon deposition; However, when nH2/nCO is high, the methane decomposition reaction is the mainstream reaction, and increasing pressure rise will hinder the methane decomposition and inhibit the carbon deposition. In addition, if the total system pressure is too high, it will not be able to obtain the reducing gas with the effective composition of φ(H2)+φ(CO) to meet the requirements of the direct reduction iron process.
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Received: 06 December 2022
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[1] 中国冶金百科全书总编辑委员会.中国冶金百科全书(钢铁冶金)[M]. 北京: 冶金工业出版社, 1992.(Editorial Board of China Metallurgical Encyclopedia. Encyclopedia of China Metallurgy (Ferrou Metallurgy)[M]. Beijing: Metallurgical Industry Press, 1992.) [2] INADA Y. Improvements in the MIDREX direct reduction process[J]. Research and Development Kobe Steel Engineering Reports, 2000, 50(3): 86. [3] CHEELEY R, LEU M. Coal gasification for DRI production—An Indian solution[R]. Steel Times International, 2010, (4):1. [4] NATSUI S, KIKUCHI T, SUZUKI R O. Numerical analysis of carbon monoxide-hydrogen gas reduction of iron ore in a packed bed by an Euler-Lagrange approach[J]. Metallurgical and Materials Transactions B, 2014, 45(6): 2395. [5] 张琦,沈佳林,许立松. 中国钢铁工业碳达峰及低碳转型路径[J]. 钢铁,2021,56(10):152. (ZHANG Q,SHEN J L,XU L S. Carbon peak and low-carbon transition path of China′s iron and steel industry[J]. Iron and Steel, 2021, 56(10):152.) [6] 陆亚男,吴胜利,王来信,等. 炉渣成分对COREX铁水脱硫效果的影响[J]. 钢铁,2019,54(9):33.(LU Y N, WU S L, WANG L X, et al. Effect of slag composition on desulfurization effect of COREX hot metal[J]. Iron and Steel, 2019, 54(9):33.) [7] 李颖,李正一,狄瞻霞,等. 还原条件对COREX球团显气孔率和金属率的影响[J]. 钢铁, 2018, 53(2):10.(LI Y, LI Z Y, DI Z X, et al. Effect of reduction conditions on porosity and metal percentage of COREX pellets[J]. Iron and Steel,2018,53(2):10.) [8] 张建良,张冠琪,刘征建,等. 山东墨龙HIsmelt工艺生产运行概况及主要特点[J]. 中国冶金,2018,28(5):37.(ZHANG J L, ZHANG G Q, LIU Z J, et al. Production overview and main characteristics of HIsmelt process in Shandong Molong[J]. China Metallurgy, 2018, 28(5):37.) [9] 潘聪超,庞建明.氢冶金技术的发展溯源与应用前景[J]. 中国冶金,2021,31(9):73.(PAN C C,PANG J J. Development trace and application prospect of hydrogen metallurgy technology[J]. China Metallurgy, 2021, 31(9):73.) [10] 高建军,齐渊洪,严定鎏.中国低碳炼铁技术的发展路径与关键技术问题[J].中国冶金,2021,31(9):64.(GAO J J, QI Y H, YAN D L, et al. Development path and key technical problems of low carbon ironmaking in China[J]. China Metallurgy,2021, 31(9):64.) [11] 陈健,苏敏,张新波,等. 氢冶金还原性气体的制备研究进展[J]. 中国冶金,2023,33(1):24.(CHEN J, SU M, ZHANG X B, et al. Research progress in preparation of reducing gases for hydrogen metallurgy[J]. China Metallurgy, 2023, 33(1):24.) [12] 董跃,乔星星,刘改换,等. 气基直接还原铁工艺还原气研究现状[J]. 能源与节能, 2016(3): 2.(DONG Y, QIAO X X, LIU G H, et al. Research situation of reduction gas used in gas-based direct reduction iron technology[J]. Energy and Energy Conservation, 2016(3): 2.) [13] 于恒,周继程,郦秀萍,等. 气基竖炉直接还原炼铁流程重构优化[J]. 中国冶金, 2021, 31(1): 31.(YU H, ZHOU J C, LI X P, et al. Reconstruction optimization of gas-based shaft furnace direct reduction ironmaking process[J]. China Metallurgy, 2021, 31(1): 31.) [14] WU J, GUO S Q, DING W Z. Investigation on the application of reformed coke oven gas in direct reduction iron production with a mathematical model[J]. Advances in Manufacturing,2013, 1(3): 276. [15] 梁之凯,黄柱成,易凌云. 焦炉煤气竖炉法生产DRI的煤气用量及利用率[J]. 中国冶金,2017,27(11):18.(LIANG Z K, HUANG Z C, YI L Y. Coke oven gas consumption and its utilization ratio for DRI production in shaft furnace[J]. China Metallurgy,2017, 27(11):18.) [16] 张福明,曹朝真,徐辉. 气基竖炉直接还原技术的发展现状与展望[J]. 钢铁, 2014, 49(3): 1.(ZHANG F M, CAO C Z, XU H. Current status and prospects of gas-based shaft furnace direct reduction technology[J].Iron and Steel, 2014, 49(3): 1.) [17] SEETHARAMAN S. Treatise on Process Metallurgy (Vol. 3) [M]. Boston: Elsevier, 2014. [18] ADAM P, ANDREW E. Exergy analysis of hydrogen production via steam methane reforming[J]. International Journal of Hydrogen Energy, 2007, 32(18): 4811. [19] QIMIN M, TODD H, LLOYD A, et al. Steam reforming of hydrocarbon fuels[J]. Catalysis Today, 2002, 77(1/2): 51. [20] SEO H O, SIM J K, KIM K D, et al. Carbon dioxide reforming of methane to synthesis gas over a TiO2-Ni inverse catalyst[J]. Applied Catalysis A: General, 2013, 451: 43. [21] BRADFORD M C J, VANNICE M A. CO2 reforming of CH4[J]. Catalysis Reviews-Science and Engineering, 1999, 41(1): 1. [22] LI B T, ZHANG S Y. Methane reforming with CO2 using nickel catalysts supported on yttria-doped SBA-15 mesoporous materials via sol-gel process[J]. International Journal of Hydrogen Energy, 2013, 38(33): 14250. [23] LIU C J, YE J Y, JIANG J J, et al. Progresses in the preparation of coke resistant Ni-based catalyst for steam and CO2 reforming of methane[J]. Chemical Europe, 2011, 42(27):529. [24] FRENI S, CALOGERO G, CAVALLARO S. Hydrogen production from methane through catalytic partial oxidation reactions[J]. Journal of Power Sources, 2000, 87(1/2): 28. [25] TONG G C M, FLYNN J, LECLERC C A. A dual catalyst bed for the autothermal partial oxidation of methane to synthesis gas[J]. Catalysis Letters, 2005, 102(3/4): 131. [26] 沈峰满. H-C-O体系质量及化学平衡衡算图的开发[J]. 钢铁, 2023, 58(6):12.(SHEN F M. Development of H-C-O system mass balance and chemical equilibrium diagram[J]. Iron and Steel, 2023, 58(6):12.) [27] 沈峰满. 一种用于制备氢基还原气的工艺参数确定方法:中国, ZL202110727435.6[P]. 2021-06-09.(SHEN F M. A Method for Determining Process Parameters for Preparing Hydrogen-based Reducing Gas: China, ZL202110727435.6[P]. 2021-06-09.) [28] 沈峰满,郑海燕,丁智敏. 基于控制析碳的制备氢基还原气工艺的工艺参数确定方法:中国, CN202210932708.5[P]. 2022-08-04.(SHEN F M, ZHENG H Y, DING Z M. Determination of Process Parameters for Preparing Hydrogen-based Reducing Gas Based on the Control of the Carbon Deposition: China, CN202210932708.5[P]. 2022-08-04.) [29] 沈峰满. 冶金物理化学[M]. 北京: 高等教育出版社, 2017.(SHEN F M. Physical Chemistry for Metallurgy[M]. Beijing: Higher Education Press, 2017.) [30] 沈峰满,郑艾军,郑海燕,等. 关于直接还原铁工艺及还原气制备的若干思考[J]. 钢铁, 2022, 57(3): 10. (SHEN F M, ZHENG A J,ZHENG H Y,et al. Thoughts on preparation of hydrogen-based reduction gas and process of direct reduction iron[J]. Iron and Steel, 2022, 57(3): 10.) |
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