Effect of combustion products recycling system on temperature distribution and performance of flameless combustion furnace

Document Type : Original Article

Authors

Department of Mechanical Engineering, Tarbiat Modares University, Tehran, Iran

10.22034/jfnc.2024.447927.1375

Abstract

In this study, the conditions governing a flameless natural gas and air combustion furnace with an internal recirculation system equipped with an arm to increase the recirculation coefficient is numerically investigated on a laboratory scale. The effect of changing its angle on parameters of flameless combustion such as released heat, temperature distribution and internal recirculation coefficient was investigated. The simulation results show that by increasing the angle of the arm and opening the geometry up to 60 degrees, the flow is better directed into the furnace, and the volume of the recirculation area is the largest in the arrangement with an arm angle of 60 degrees. By comparing the value of the recirculation coefficient in the whole furnace, it is observed that its main effect is on the recirculation area, which leads to changes in the uniformity of temperature and released heat. By examining the maximum released heat, it can be concluded that the geometry design with an arm angle of 30 degrees is the best proposed geometry for heat treatment applications. By examining the temperature results, it was concluded that as the angle of the arm of the system is lower (the system becomes more closed) and the accumulation of the combustion flow inside it is greater, The temperature increases from 1727 K (for armless geometry) to 1738 K (for arm angle of 15 degrees).

Keywords

Main Subjects


[1] Li, P. Mi, J. Dally, B. Wang, F. Wang, L. Liu, Z. Chen, S and Zheng, C, “Progress and recent trend in MILD combustion,” Science China Technological Sciences, vol. 54, no. 2. Springer Science and Business Media LLC, pp. 255–269, Feb 2011.
[2] A. A. A. Abuelnuor, M. A. Wahid, H. A. Mohammed, and A. Saat, “Flameless combustion role in the mitigation of NOXemission: a review,” International Journal of Energy Research, vol. 38, no. 7. Hindawi Limited, pp. 827–846, Feb 2014.
[3] S. Kumar, P. J. Paul, and H. S. Mukunda, “Studies on a new high-intensity low-emission burner,” Proceedings of the Combustion Institute, vol. 29, no. 1. Elsevier BV, pp. 1131–1137, Jan 2002.
[4] J. Wünning, “Flameless oxidation to reduce thermal no-formation,” Progress in Energy and Combustion Science, vol. 23, no. 1. Elsevier BV, pp. 81–94, Feb 1997.
[5] P. Gupta, R. S. Singh, A. Sachan, A. S. Vidyarthi, and A. Gupta, “Study on biogas production by anaerobic digestion of garden-waste,” Fuel, vol. 95. Elsevier BV, pp. 495–498, May 2012.
[6] B. A. FLECK, A. SOBIESIAK, and H. A. BECKER, “Experimental and Numerical Investigation of the Novel Low NOxCGRI Burner,” Combustion Science and Technology, vol. 161, no. 1. Informa UK Limited, pp. 89–112, Dec 2000. 
[7] A. Sobiesiak, S. Rahbar, and H. A. Becker, “Performance Characteristics of the Novel Low-NOx CGRI Burner For Use with High Air Preheat,” Combustion and Flame, vol. 115, no. 1–2. Elsevier BV, pp. 93–125, Oct 1998.
[8] J. Mi, P. Li, B. B. Dally, and R. A. Craig, “Importance of Initial Momentum Rate and Air-Fuel Premixing on Moderate or Intense Low Oxygen Dilution (MILD) Combustion in a Recuperative Furnace,” Energy & Fuels, vol. 23, no. 11. American Chemical Society (ACS), pp. 5349–5356, Nov 2009.
[9] S. E. Hosseini and M. A. Wahid, “Investigation of bluff-body micro-flameless combustion,” Energy Conversion and Management, vol. 88. Elsevier BV, pp. 120–128, Dec 2014.
[10] B. Liu, Y.-H. Wang, and H. Xu, “Mild combustion in forward flow furnace of refinery-off gas for low-emissions by deflector,” Applied Thermal Engineering, vol. 91. Elsevier BV, pp. 1048–1058, Dec. 2015.
[11] F. Wang, P. Li, J. Mi, and Z. Shu, “A novel method to improve stability of MILD combustion in a highly heat-extracted furnace,” Fuel, vol. 292. Elsevier BV, p. 120315, May 2021.
[12] F. Mohammadzadeh Pormehr and M. Zabetian Targhi, “Deflector design to improve internal gas recirculation in a MILD combustion laboratory furnace,” Fuel, vol. 360. Elsevier BV, p. 130542, Mar 2024.
[13] G. SZEGO, B. DALLY, and G. NATHAN, “Scaling of NOx emissions from a laboratory-scale mild combustion furnace,” Combustion and Flame, vol. 154, no. 1–2. Elsevier BV, pp. 281–295, Jul 2008.
[14] S. Cao, C. Zou, Q. Han, Y. Liu, D. Wu, and C. Zheng, “Numerical and Experimental Studies of NO Formation Mechanisms under Methane Moderate or Intense Low-Oxygen Dilution (MILD) Combustion without Heated Air,” Energy & Fuels, vol. 29, no. 3. American Chemical Society (ACS), pp. 1987–1996, Feb 2015.
[15] S. Xu et al., “Effects of wall temperature on methane MILD combustion and heat transfer behaviors with non-preheated air,” Applied Thermal Engineering, vol. 174. Elsevier BV, p. 115282, Jun 2020.
[16] I. R. GRAN and B. F. MAGNUSSEN, “A Numerical Study of a Bluff-Body Stabilized Diffusion Flame. Part 2. Influence of Combustion Modeling And Finite-Rate Chemistry,” Combustion Science and Technology, vol. 119, no. 1–6. Informa UK Limited, pp. 191–217, Oct 1996.
[17] A. Mardani, “Optimization of the Eddy Dissipation Concept (EDC) model for turbulence-chemistry interactions under hot diluted combustion of CH4/H2,” Fuel, vol. 191. Elsevier BV, pp. 114–129, Mar 2017.
[18] D. He, Y. Yu, Y. Kuang, and C. Wang, “Analysis of EDC constants for predictions of methane MILD combustion,” Fuel, vol. 324. Elsevier BV, p. 124542, Sep 2022.
[19] C. Galletti, A. Parente, M. Derudi, R. Rota, and L. Tognotti, “Numerical and experimental analysis of NO emissions from a lab-scale burner fed with hydrogen-enriched fuels and operating in MILD combustion,” International Journal of Hydrogen Energy, vol. 34, no. 19. Elsevier BV, pp. 8339–8351, Oct 2009.
[20] M. De Joannon, A. Saponaro, and A. Cavaliere, “Zero-dimensional analysis of diluted oxidation of methane in rich conditions,” Proceedings of the Combustion Institute, vol. 28, no. 2. Elsevier BV, pp. 1639–1646, Jan 2000.
[21] W. P. Jones and R. P. Lindstedt, “Global reaction schemes for hydrocarbon combustion,” Combustion and Flame, vol. 73, no. 3. Elsevier BV, pp. 233–249, Sep 1988.
[22] G. D. Raithby and E. H. Chui, “A Finite-Volume Method for Predicting a Radiant Heat Transfer in Enclosures With Participating Media,” Journal of Heat Transfer, vol. 112, no. 2. ASME International, pp. 415–423, May 1990.
[23] J. R. Howell, M. P. Mengüç, K. Daun, and R. Siegel, Thermal Radiation Heat Transfer. CRC Press, 2020.
[24] M. A. Rajhi, R. Ben-Mansour, M. A. Habib, M. A. Nemitallah, and K. Andersson, “Evaluation of gas radiation models in CFD modeling of oxy-combustion,” Energy Conversion and Management, vol. 81. Elsevier BV, pp. 83–97, May 2014.
[25] J. Wünning, “Flameless oxidation to reduce thermal no-formation,” Progress in Energy and Combustion Science, vol. 23, no. 1. Elsevier BV, pp. 81–94, Feb 1997.
[26] P. Li, F. Wang, J. Mi, B. B. Dally, and Z. Mei, “MILD Combustion under Different Premixing Patterns and Characteristics of the Reaction Regime,” Energy & Fuels, vol. 28, no. 3. American Chemical Society (ACS), pp. 2211–2226, Mar 2014.
[27] Z. Zhao et al., “Effect of steam addition on turbulence-chemistry interaction behaviors of pulverized coal MILD-oxy combustion,” Fuel, vol. 294. Elsevier BV, p. 120496, Jun 2021.
[28] S. Jeon and Y. Kim, “Multi-environment Probability Density Function Modeling for Turbulent CH4 Flames under Moderate or Intense Low-Oxygen Dilution Combustion Conditions with Recirculated Flue Gases,” Energy & Fuels, vol. 31, no. 8. American Chemical Society (ACS), pp. 8685–8697, Jul 2017.