The Modeling of Cement Rotary Kiln Based on Spang Model for Investigation of CO2 Emission in Cement Production Process

Authors

1 Msc. student of Mechanical engineering/Tarbiat modares university

2 Professor in Mechanical engineering/Tarbiat modares university

Abstract

Cement rotary kilns are extensively used to change raw material into clinker. Complex phenomenon is observed in cement rotary kilns resulting from conduction, convection and radiation heat transfer, interactions between bed materials and hot gas flow and kiln rotation. Therefore, the modeling of cement rotary kiln have difficulty due to non-linear and stiff set of equations. Regards to over prediction of the maximum inner temperature of the kiln in Spang model; a one dimensional, steady state model is developed based on Spang model to investigate the operation of a cement kiln. In the present work, temperature distribution of hot gases is predicted using two-step methane kinetic to calculate the heat of combustion. Since the amount of CO2 emission in cement kiln processes is very important, CO2 emission generated by both bed material reactions and combustion process are calculated and compared. Modeling results showed that approximately half of CO2 emission is in result of combustion process and other one is from bed material reactions.

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Main Subjects


[1] Blumberg JM (1970) Modeling and control of the cement manufacturing process. PhD thesis. The University of Manchester.
[2] Spang HA (1972) A Dynamic model of a cement kiln. Int J Automatica 8(3): 309-323.
[3] Gorog JP, Adams TN, Brimacombe JK (1983) Heat transfer from flames in a rotary kilns. Metall Trans 14(3): 411-424.
[4] Boateng AA, Barr PV (1996) A thermal model for rotary kiln including heta transfer within the bed. Int J Heta Mass Transfer 39(10): 2131-2147
[5] Withsel A C, Renotte  C, Remy  M (2001) New dynamic model of a rotary cement kiln. Control Department, Mons, Belgium.
[6] Mintus  F, Hamel  S, Krumm  W (2006) Wet process rotary cement kilns:modleing and simulation. Int J Clean Techn Eviron Policy 8(2): 112-122.
[7] Mujumdar KS, Ganesh KV, Kulkarni SB, Ranade VV (2007) Rotary cement kiln simulator (RoCKS): Integrated modleing of pre-heater, calciner, kiln and clinker cooler. Chem Eng Sci 62(9): 2590-2607.
[8] Pisaroni M, Sadi R, Lahaye D (2012) Counteracting ring formation in rotary kilns. Springer open Journal of Mathematical in Industry.
[9] Mikulcic H, Vujanovic M, Fidaros DM, Priesching P, Minic I, Tatschl R, Duic N, Stefanovic G (2012) The application of CFD modeling to support the reduction of CO2 emissions in cement industry. J Energy (45): 464-473.
[10] www.karripentill.com (visited at December 2012) Rotary kiln simulation.
[11] Paul W (2007) Rotary kilns: Transport phenomena and transport process. vancouver, British columbia.
[12] Worrell E, Price L, Martin  N, Hendriks  C, Media  LO (2001) Carbon dioxide emissions from the global cement industry. Int J Annu Rev Energy Environ 26(1): 303-329.
[13] Frassoldati A, Cuoci A, Faravelli T, Ranzi E, Candusso C, Tolazzi D (2009) Simplified kinetic schemes for oxy-fuel combustion. 1st International confrence on sustainable fossil fuels for future energy, Italy.
[14] Turns SR (2000) An introduction to combustion-concepts and application. Chap 6. 2nd edn. McGraw-Hill Series in Mechanical Engineering.
[15] Sonntag RE, Brogknakke C, Van Wylen GJ (1983) Fundamental of thermodynamics. 5th edn. John Wiley & sons INC, New York.
[16] Kaddatz KT, Rasul MG, Rahman A (2013) Alternative fuels for use in cement kilns: process impact modeling. Procedia Engineering 56:413-420.
[17] Mirza Mohammad TA (2012) Composition and phase mineral variation of portland cement in mass factory sulaimani-kurdestan region NE-Iraq. J Basic Appl Sci 12(6): 109-118.