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Received January 6, 2022
Accepted April 2, 2022
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Techno-economic analysis of methanol and ammonia co-producing process using CO2 from blast furnace gas
School of Chemical Engineering, University of Ulsan, 93, Daehak-ro, Nam-gu, Ulsan 44610, Korea
jdonghwi@ulsan.ac.kr
Korean Journal of Chemical Engineering, August 2022, 39(8), 1999-2009(11), 10.1007/s11814-022-1129-9
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Abstract
In steel manufacturing plants, blast furnace gas is generated from a furnace in which steel ore, coke and limestone are heated and melted. It is commonly used to produce electricity or released to the atmosphere in general; however, it can be utilized as a carbon source to produce C1 value-added chemicals. In this study, we propose two production schemes for methanol production and co-production of methanol and ammonia from blast furnace gas. Both cases were simulated using Aspen Plus V12 and economics was evaluated using Aspen Process Economic Analyzer (APEA). As a result, the methanol production case produced 99.4 wt% 232 t/day of methanol and the co-production case produced 97.7 wt%, 453.4 t/day of ammonia and 99.8 wt%, 263 t/day of methanol. The total annual cost of the methanol production case is US 121.6M$/y and US 222.1M$/y at the co-production case. The NPVs are -810.4M$ in the methanol production case and -981.3M$ in the co-production case, respectively. By sensitivity analysis, it is shown that the co-production case can be more economically feasible in the aspect of NPV when the raw material cost decreases 30%.
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References
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Kalbani HA, Wang H, Appl. Energy, 165, 809 (2016)
Matzen M, Demirel Y, Energy, 93, 1 (2015)
Alarifi A, Croiset E, Ind. Eng. Chem. Res., 55, 1164 (2016)
Graaf GH, Stamhuis EJ, Beenackers AACM, Chem. Eng. Sci., 43, 3185 (1988)
Nyári J, Aarnio AS, J. CO2 Util., 39, 101106 (2020)
Spath PL, Dayton DC, NREL, Golden (CO, USA) (2003).
Encyclopedia Britannica, https://www.britannica.com/technology/Haber-Bosch-process (2020).
Christiansen LJ, Ammonia: Catalysis and manufacture, Springer-Verlag, Lyngby, Denmark (1995).
Lim YI, Choi J, Moon HM, Kim G, Korean Chem. Eng. Res., 54, 3 (2016)
Ruthven DM, Farooq S, Knaebel KS, Pressure swing adsorption, Wiley, New York, USA (1994).
Zhang C, Kang SC, Fuel, 157, 285 (2015)
Peters MS, Timmerhaus K, West R, Plant design and economics for chemical engineers, McGraw-Hill Professional, New York, USA (2002).
Turton RA, Analysis, synthesis, and design of chemical processes, Prentice Hall, Hoboken, New Jersey, USA (2003).
Chemical engineering, https://www.chemengonline.com (2021).
Seider WD, Seader JD, Product and process design principles, Wiley, New York, USA (2010).
The Engineering ToolBox, https://www.engineeringtoolbox.com/fuels-higher-calorific-values-d_169.html (2021).
METGroup, https://group.met.com/en/media/energy-insight/calorific-value-of-natural-gas (2021).
Ebrahimi A, Ziabasharhagh M, Energy, 126, 868 (2017)
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Douglas JM, Conceptual design of chemical processes, McGraw- Hill New York, USA (1988).