Journal Home Online First Current Issue Archive For Authors Journal Information 中文版

Engineering >> 2015, Volume 1, Issue 1 doi: 10.15302/J-ENG-2015008

Fundamental and Technical Challenges for a Compatible Design Scheme of Oxyfuel Combustion Technology

State Key Laboratory of Coal Combustion, Huazhong University of Science and Technology, Wuhan 430074, China

Received: 2015-02-02 Revised: 2015-02-25 Accepted: 2015-03-25 Available online: 2015-03-31

Next Previous

Abstract

Oxyfuel combustion with carbon capture and sequestration (CCS) is a carbon-reduction technology for use in large-scale coal-fired power plants. Significant progress has been achieved in the research and development of this technology during its scaling up from 0.4 MWth to 3 MWth and 35 MWth by the combined efforts of universities and industries in China. A prefeasibility study on a 200 MWth large-scale demonstration has progressed well, and is ready for implementation. The overall research development and demonstration (RD&D) roadmap for oxyfuel combustion in China has become a critical component of the global RD&D roadmap for oxyfuel combustion. An air combustion/oxyfuel combustion compatible design philosophy was developed during the RD&D process. In this paper, we briefly address fundamental research and technology innovation efforts regarding several technical challenges, including combustion stability, heat transfer, system operation, mineral impurities, and corrosion. To further reduce the cost of carbon capture, in addition to the large-scale deployment of oxyfuel technology, increasing interest is anticipated in the novel and next-generation oxyfuel combustion technologies that are briefly introduced here, including a new oxygen-production concept and flameless oxyfuel combustion.

Figures

Fig. 1

Fig. 2

Fig. 3

Fig. 4

Fig. 5

Fig. 6

Fig. 7

Fig. 8

Fig. 9

Fig. 10

Fig. 11

Fig. 12

Fig. 13

References

[ 1 ] United Nations Statistics Division, Millennium Development. Goals indicators: carbon dioxide emissions (CO2), thousand metric tonnes of CO2. http://mdgs.un.org/unsd/mdg/SeriesDetail.aspx?srid=749&crid

[ 2 ] Department of Social Development, The Ministry of Science and Technology (MOST) of China. Carbon capture, utilization and storage technology development in China. 2011

[ 3 ] I. Hadjipaschalis, G. Kourtis, A. Poullikkas. Assessment of oxyfuel power generation technologies. Renew. Sust. Energy Rev., 2009, 13: 2637–2644 link1

[ 4 ] M. B. Toftegaard, J. Brix, P. A. Jensen, P. Glarborg, A. D. Jensen. Oxyfuel combustion of solid fuels. Prog. Energy Combust., 2010, 36: 581–625 link1

[ 5 ] F. L. Horn, M. Steinberg. Control of carbon dioxide emissions from a power plant (and use in enhanced oil recovery). Fuel, 1982, 61: 415–422 link1

[ 6 ] C. G. Zheng. Greenhouse Effects and Its Control Strategy. Beijing: China Electric Power Press, 2001 (in Chinese)

[ 7 ] B. J. P. Buhre, L. K. Elliott, C. D. Sheng, R. P. Gupta, T. F. Wall. Oxyfuel combustion technology for coal-fired power generation. Prog. Energy Combust. 2005, 31: 283–307 link1

[ 8 ] S. Santos. Oxy-coal combustion power plant with CCS-current status of development. In: Proceedings of the 39th International Technical Conference on Clean Coal & Fuel Systems. Clearwater, Fl., USA, 2014

[ 9 ] T. Nozaki, S. Takano, T. Kiga, K. Omata, N. Kimura. Analysis of the flame formed during oxidation of pulverized coal by an O2/CO2 mixture. Energy, 1997, 22(2¯3): 199–205 link1

[10] N. Kimura, K. Omata, T. Kiga, S. Takano, S. Shikisima. The characteristics of pulverized coal combustion in O2/CO2 mixtures for CO2 recovery. Energy Convers. Manage., 1995, 36: 805–808 link1

[11] L. Chen, S. Z. Yong, A. F. Ghoniem. Oxyfuel combustion of pulverized coal: Characterization, fundamentals, stabilization and CFD modeling. Prog. Energy Combust., 2012, 38: 156–214 link1

[12] T. Kiga, Characteristics of pulverized-coal combustion in the system of oxygen/recycled flue gas combustion. Energy Convers. Manage., 1997, 38: S129–S134 link1

[13] R. H. Essenhigh, M. K. Misra, D. W. Shaw. Ignition of coal particles: A review. Combust. Flame, 1989, 77(1): 3–30 link1

[14] C. R. Shaddix, A. Molina. Particle imaging of ignition and devolatilization of pulverized coal during oxy-fuel combustion. Proc. Combust. Inst., 2009, 32(2): 2091–2098 link1

[15] X. Huang, J. Li, Z. Liu, M. Yang, D. Wang, C. Zheng. Ignition and devolatil­ization of pulverized coals in lower oxygen content O2/CO2 atmosphere. In: Cleaner Combustion and Sustainable World, 2013: 99–104

[16] X. Huang. Oxyfuel combustion characteristics of pulverized coal based on flat-flame assisted entrained flow reactor (Dissertation for the Doctoral Degree). Wuhan: Huazhong University of Science and Technology, 2013 (in Chinese)

[17] Y. Qiao, L. Zhang, E. Binner, M. Xu, C. Z. Li. An investigation of the causes of the difference in coal particle ignition temperature between combustion in air and in O2/CO2. Fuel, 2010, 89(11): 3381–3387 link1

[18] J. Liu. A study of numerical optimization design and experiment on oxycoal burner. Dissertation for the Doctoral Degree. Wuhan: Huazhong University of Science and Technology, 2012 (in Chinese)

[19] J. Liu, Mathematical modeling of air- and oxy-coal confined swirling flames on two extended eddy-dissipation models. Ind. Eng. Chem. Res., 2012, 51(2): 691–703

[20] J. Guo, Numerical investigation on oxy-combustion characteristics of a 200 MWe tangentially fired boiler. Fuel, 2015, 140: 660–668 link1

[21] T. Kangwanpongpan, F. H. R. França, R. C. Silva, P. S. Schneider, H. J. Krautz. New correlations for the weighted sum of gray gases model in oxy-fuel conditions based on HITEMP 2010 database. Int. J. Heat Mass Transfer, 2012, 55: 7419–7433

[22] R. Johansson, B. Leckner, K. Andersson, F. Johnsson. Account for variations in the H2O to CO2 molar ratio when modelling gaseous radiative heat transfer with the weighted-sum-of-grey-gases model. Combust. Flame, 2011, 158: 893–901 link1

[23] C. Yin, L. C. R. Johansen, L. A. Rosendahl, S. K. Kær. New weighted sum of gray gases model applicable to computational fluid dynamics (CFD) mod­eling of oxy-fuel combustion: Derivation, validation, and implementation. Energy Fuels, 2010, 24: 6275–6282 link1

[24] K. Andersson, R. Johansson, S. Hjärtstam, F. Johnsson, B. Leckner. Radiation intensity of lignite-fired oxyfuel flames. Exp. Therm. Fluid Sci., 2008, 33: 67–76 link1

[25] J. P. Smart, P. O’ Nions, G. S. Riley. Radiation and convective heat transfer, and burnout in oxy-coal combustion. Fuel, 2010, 89(9): 2468–2476 link1

[26] S. Black, Effects of firing coal and biomass under oxy-fuel conditions in a power plant boiler using CFD modelling. Fuel, 2013, 113: 780–786 link1

[27] T. Yamada, T. Uchida, T. Gotou, T. Kiga, C. Spero. Operation experience of oxyfuel boiler. In: The 3rd Oxy-fuel Combustion Conference. Spain, 2013

[28] G. Steffen. Tests and results of Vattenfall’s oxyfuel pilot plant. In: The 3rd Oxy-fuel Combustion Conference. Spain, 2013

[29] M. Habermehl, J. Erfurth, D. Toporov, M. Förster, R. Kneer. Experimental and numerical investigations on a swirl oxycoal flame. Appl. Therm. Eng., 2012, 49: 161–169 link1

[30] A. H. Al-Abbas, J. Naser, D. Dodds. CFD modelling of air-fired and oxy-fuel combustion in a large-scale furnace at Loy Yang A brown coal power station. Fuel, 2012, 102: 646–665 link1

[31] W. Terry, S. Rohan, S. Stanley. Demonstrations of coal-fired oxyfuel technology for carbon capture and storage and issues with commercial deployment. Int. J. Greenh. Gas Control, 2011, 5: S5–S15 link1

[32] F. Kluger, B. Prodhomme, P. Mönckert, A. Levasseur, J. F. Leandri. CO2 capture system-confirmation of oxy-combustion promises through pilot operation. Energy Procedia, 2011, 4: 917–924 link1

[33] K. McCauley, Commercialization of oxy-coal combustion: Applying results of a large 30 MWth pilot project. Energy Procedia, 2009, 1: 439–446 link1

[34] W. Luo, Q. Wang, X. Huang, Z. Liu, C. Zheng. Dynamic simulation and transient analysis of a 3 MWth oxy-fuel combustion system. Int. J. Greenh. Gas Control, 2015, 35: 138–149 link1

[35] W. Luo, Q. Wang, Z. Liu, C. Zheng. Dynamic simulation of the transition process in a 3 MWth oxy-fuel test facility. Energy Procedia, 2014, 63: 6281–6288 link1

[36] I. Guedea, Control system for an oxy-fuel combustion fluidized bed with flue gas recirculation. Energy Procedia, 2011, 4: 972–979 link1

[37] D. X. Yu, W. J. Morris, R. Erickson, J. O. L. Wendt, A. Fry, C. L. Senior. Ash and deposit formation from oxy-coal combustion in a 100 kW test furnace. Int. J. Greenh. Gas Control, 2011, 5: S159–S167 link1

[38] C. D. Sheng, J. Lin, Y. Li, C. Wang. Transformation behaviors of excluded pyrite during O2/CO2 combustion of pulverized coal. Asia-Pac. J. Chem. Eng., 2010, 5(2): 304–309 link1

[39] T. Zhang, Slagging behavior of selected coals under oxy-combustion, final report for HUST-ALSTOM collaboration project on oxyfuel combustion. 2015

[40] S. Chen, An experimental investigation of SO3 determination under oxyfuel combustion, final report for HUST-ALSTOM collaboration project on oxyfuel combustion. 2015

[41] J. Davison. Performance and costs of power plants with capture and storage of CO2. Energy, 2007, 32(7): 1163–1176 link1

[42] Q. Yang, Y. S. Lin, M. Bülow. High temperature sorption separation of air for producing oxygen-enriched CO2 stream. AIChE J., 2006, 52(2): 574–581 link1

[43] Z. H. Yang, Y. S. Lin. High-temperature oxygen sorption in a fixed bed packed with perovskite-type ceramic sorbents. Ind. Eng. Chem. Res., 2003, 42(19): 4376–4381 link1

[44] Z. Rui, J. Ding, Y. Li, Y. S. Lin. SrCo0.8Fe0.2O3−δ sorbent for high-temperature production of oxygen-enriched carbon dioxide stream. Fuel, 2010, 89(7): 1429–1434 link1

[45] S. Guntuka, S. Banerjee, S. Farooq, M. P. Srinivasan. A- and B-site substituted lanthanum cobaltite perovskite as high temperature oxygen sorbent. 1. Thermogravimetric analysis of equilibrium and kinetics. Ind. Eng. Chem. Res., 2008, 47(1): 154–162

[46] Q. Shen, Y. Zheng, C. Luo, C. Zheng. Development and characterization of Ba1−xSrxCo0.8Fe0.2O3−δ perovskite for oxygen production in oxyfuel combustion system. Chem. Eng. J., 2014, 255: 462–470

[47] J. A. Wünning, J. G. Wünning. Flameless oxidation to reduce thermal NO-formation. Prog. Energy Combust., 1997, 23: 81–94 link1

[48] A. Cavaliere, M. de Joannon. Mild combustion. Prog. Energy Combust., 2004, 30: 329–366 link1

[49] P. Sabia, M. de Joannon, M. Lubrano Lavadera, P. Giudicianni, R. Ragucci. Autoignition delay times of propane mixtures under MILD conditions at atmospheric pressure. Combust. Flame, 2014, 161(12): 3022–3030 link1

[50] P. Li, Progress and recent trend in MILD combustion. Sci. China Technol. Sci., 2011, 54(2): 255–269

[51] Y. Minamoto, N. Swaminathan. Scalar gradient behaviour in MILD combustion. Combust. Flame, 2014, 161(4): 1063–1075 link1

[52] P. Li, B. B. Dally, J. Mi, F. Wang. MILD oxy-combustion of gaseous fuels in a laboratory-scale furnace. Combust. Flame, 2013, 160(5): 933–946 link1

[53] H. Stadler, D. Toporov, M. Förster, R. Kneer. On the influence of the char gasification reactions on NO formation in flameless coal combustion. Combust. Flame, 2009, 156(9): 1755–1763. link1

[54] M. Saha, B. B. Dally, P. R. Medwell, E. M. Cleary. Moderate or intense low oxygen dilution (MILD) combustion characteristics of pulverized coal in a self-recuperative furnace. Energy Fuels, 2014, 28(9): 6046–6057. link1

[55] P. Li, Moderate or intense low-oxygen dilution oxy-combustion characteristics of light oil and pulverized coal in a pilot-scale furnace. Energy Fuels, 2014, 28(2): 1524–1535 link1

Related Research