Mixing and segregation of binary oxygen carrier mixtures in a cold flow model of a chemical looping combustor

Abstract In a typical chemical looping combustion process, the oxygen for fuel combustion is supplied by circulating metal based oxygen carriers between two interconnected fluidised bed reactors. The redox characteristics of oxygen carriers and hence the overall performance of the process can be significantly improved by utilising binary mixtures of oxygen carrier particles. The full potential of such multi-species particle systems however can be only realised when particles segregation is minimised. This study is concerned with gaining an understanding of the mixing and segregation behaviour of binary mixtures of oxygen carrier particles with different sizes and densities in a cold flow model representing a 10 kWth chemical looping combustor. The hydrodynamics of such systems were investigated and compared with a typical chemical looping combustion process where single species are used. This was followed by investigating the solids mixing and segregation behaviour in terms of segregation intensity and species weight percentage at each reactor as a function of operating parameters. It was shown that increasing the total solid inventory, particle terminal velocity ratio, composition, and air reactor superficial velocity increases the riser pressure, solid circulation rates, and riser solid holdup. Mixing and segregation regimes of the fuel reactor and the component segregation between the two reactors were also mapped. The results showed that, for mixtures of species with low terminal velocity to high terminal velocity ratios of greater than 0.7, a good mixing in the fuel reactor can be achieved by maintaining the superficial gas velocity to the mixture minimum fluidisation velocity ratio above 5. For the tested conditions, the component segregation between the two reactors was avoided by maintaining the ratio of the riser superficial velocity to the terminal velocity of the species with a high terminal velocity between 1.25 and 2.

[1]  Aibing Yu,et al.  An analysis of the chaotic motion of particles of different sizes in a gas fluidized bed , 2006 .

[2]  RajenderKumar Gupta,et al.  Oxy-fuel combustion technology for coal-fired power generation , 2005 .

[3]  L. G. Gibilaro,et al.  A model for a segregating gas fluidised bed , 1974 .

[4]  J. Werther,et al.  Factors affecting solids segregation in circulating fluidized‐bed riser , 1998 .

[5]  Giuseppe Olivieri,et al.  Segregation of fluidized binary mixtures of granular solids , 2004 .

[6]  B. Moghtaderi,et al.  Redox Characteristics of Fe–Ni/SiO2 Bimetallic Oxygen Carriers in CO under Conditions Pertinent to Chemical Looping Combustion , 2012 .

[7]  H. Hofbauer,et al.  Design of a Chemical Looping Combustor using a Dual Circulating Fluidized Bed (DCFB) Reactor System , 2009 .

[8]  A. W. Nienow,et al.  A quantitative analysis of the mixing of two segregating powders of different density in a gas-fluidised bed , 1978 .

[9]  B. Moghtaderi Application of Chemical Looping Concept for Air Separation at High Temperatures , 2010 .

[10]  G. Kwant,et al.  Particle mixing and separation in a binary solids floating fluidized bed , 1995 .

[11]  S. Su,et al.  Post combustion CO2 capture by carbon fibre monolithic adsorbents , 2009 .

[12]  Hermann Hofbauer,et al.  Cold Flow Model Study on a Dual Circulating Fluidized Bed (DCFB) System for Chemical Looping Processes , 2009 .

[13]  C. Wen,et al.  A generalized method for predicting the minimum fluidization velocity , 1966 .

[14]  Dimitri Gidaspow,et al.  Investigation of mixing/segregation of mixture particles in gas-solid fluidized beds , 2007 .

[15]  D. Zheng,et al.  Evaluation of a chemical-looping-combustion power-generation system by graphic exergy analysis , 1987 .

[17]  Mohammad Asif,et al.  Minimum Fluidization Velocities of Binary-Solid Mixtures: Model Comparison , 2010 .

[18]  H. Richter,et al.  Reversibility of combustion processes , 1983 .

[19]  Craig Hawthorne,et al.  Hydrodynamic analysis of a 10 kWth Calcium Looping Dual Fluidized Bed for post-combustion CO2 capture , 2010 .

[20]  K. G. Palappan,et al.  Studies on segregation of binary mixture of solids in a continuous fast fluidized bed: Part I. Effect of particle density , 2008 .

[21]  Aibing Yu,et al.  Effect of Bed Thickness on the Segregation Behavior of Particle Mixtures in a Gas Fluidized Bed , 2010 .

[22]  Hongguang Jin,et al.  A Novel Chemical-Looping Combustor without NOx Formation , 1996 .

[23]  Anders Lyngfelt,et al.  The GRACE project. Development of oxygen carrier particles for chemical-looping combustion. Design and operation of a 10 kW chemical-looping combustor , 2004 .

[24]  Leon R. Glicksman,et al.  Simplified scaling relationships for fluidized beds , 1993 .

[25]  B. Moghtaderi Review of the Recent Chemical Looping Process Developments for Novel Energy and Fuel Applications , 2012 .

[26]  H. Jang,et al.  Mixing–segregation phenomena of binary system in a fluidized bed , 2010 .

[27]  J. C. Villar,et al.  A study of segregation in a gas-solid fluidized bed: Particles of different density , 1989 .

[28]  B. Moghtaderi,et al.  Thermodynamic Assessment of a Novel Concept for Integrated Gasification Chemical Looping Combustion of Solid Fuels , 2012 .

[29]  Mohammad. M. Hossain,et al.  Chemical-looping combustion (CLC) for inherent CO2 separations—a review , 2008 .

[30]  A. Nienow,et al.  STUDIES OF SEGREGATION/MIXING IN FLUIDISED BEDS OF DIFFERENT SIZE PARTICLES , 1987 .

[31]  He Yurong,et al.  Size segregation of binary mixture of solids in bubbling fluidized beds , 2003 .

[32]  O. Levenspiel,et al.  Drag coefficient and terminal velocity of spherical and nonspherical particles , 1989 .

[33]  S. Uchida,et al.  Minimum fluidization velocity of binary mixture of particles with large size ratio , 1986 .

[34]  T. Takarada,et al.  Segregation of particles in binary solids circulating fluidized beds , 1994 .

[35]  B. Moghtaderi,et al.  Reduction properties of physically mixed metallic oxide oxygen carriers in chemical looping combustion , 2010 .

[36]  Pontus Markström,et al.  Designing and operating a cold-flow model of a 100 kW chemical-looping combustor , 2012 .

[37]  M. Das,et al.  Segregation and mixing effects in the riser of a circulating fluidized bed , 2007 .

[38]  Anders Lyngfelt,et al.  Design and Fluid Dynamic Analysis of a Bench-Scale Combustion System with CO2 Separation−Chemical-Looping Combustion , 2005 .

[39]  B. Pruden,et al.  Liquid fluidisation of binary particle mixtures—III Stratification by size and related topics , 1999 .

[40]  J. R. Huang,et al.  Segregation of wide size range particle mixtures in fluidized beds , 1989 .

[41]  Derek Geldart,et al.  Segregation in beds of large particles at high velocities , 1981 .

[42]  D. Weng,et al.  Effect of Manganese Doping on Oxygen Storage Capacity of Ceria-Zirconia Mixed Oxides , 2006 .

[43]  K. G. Palappan,et al.  Studies on segregation of binary mixture of solids in continuous fast fluidized bed: Part III. Quantification of performance of the segregator , 2008 .

[44]  Colin Thornton,et al.  The effects of air and particle density difference on segregation of powder mixtures during die filling , 2011 .

[45]  J. Baeyens,et al.  Segregation by size difference in gas fluidized beds , 1998 .