An experimental investigation of the ignition properties of hydrogen and carbon monoxide mixtures for syngas turbine applications

Abstract Ignition studies of simulated syngas mixtures of hydrogen (H2), carbon monoxide (CO), oxygen (O2), nitrogen (N2), and carbon dioxide (CO2) were performed using a rapid compression facility. Experiments were conducted using pressure time-histories and high-speed imaging to measure ignition delay times (τign), over a broad range of conditions relevant to current and proposed gas-turbine technologies, and which included fuel compositions consistent with typical gasification facilities. Specifically, the τign data spanned pressures from P = 7.1 to 26.4 atm, temperatures from T = 855 to 1051 K, equivalence ratios from ϕ = 0.1 to 1.0, oxygen mole fractions from χ O 2 = 15 % to 20% and H2:CO ratios from H2:CO = 0.25 to 4.0 (mole basis). Regression analysis yielded the following best-fit to the composite data set: τ ign = 3.7 × 10 - 6 P - 0.5 ϕ - 0.4 χ O 2 - 5.4 exp ( 12 , 500 / R [ cal/mol/K ] T ) In this expression, τign is the ignition delay time [ms], P is pressure [atm], T is temperature [K], ϕ is the equivalence ratio (based on the H2 and CO to O2 molar ratio), and χ O 2 is the oxygen mole fraction. The uncertainty in the measured values for τign is estimated as less than 30%. The experimental data are in good agreement with model predictions based on a recently proposed detailed reaction mechanism for H2 and CO.

[1]  Douglas M. Todd,et al.  Demonstrated Applicability of Hydrogen Fuel for Gas Turbines , 2001 .

[2]  Bradley T. Zigler,et al.  A rapid compression facility study of OH time histories during iso-octane ignition , 2006 .

[3]  Bradley T. Zigler,et al.  Demonstration of a Free-Piston Rapid Compression Facility for the Study of High Temperature Combustion Phenomena , 2004 .

[4]  G. Adomeit,et al.  Self-ignition of S.I. engine model fuels: A shock tube investigation at high pressure ☆ , 1997 .

[5]  I. Wierzba,et al.  Flammability limits of hydrogen–carbon monoxide mixtures at moderately elevated temperatures , 2001 .

[6]  C. Sung,et al.  Ignition of CO/H2/N2 versus heated air in counterflow: experimental and modeling results , 2000 .

[7]  A. K. Oppenheim,et al.  Auto-ignition of hydrocarbons behind reflected shock waves , 1972 .

[8]  W. W. Haskell,et al.  Non-uniform ignition processes in rapid-compression machines , 1969 .

[9]  F. Egolfopoulos,et al.  An optimized kinetic model of H2/CO combustion , 2005 .

[10]  Giovanni Lozza,et al.  Using Hydrogen as Gas Turbine Fuel , 2003 .

[11]  Simone Hochgreb,et al.  Hydrogen autoignition at pressures above the second explosion limit (0.6-4.0 MPa) , 1998 .

[12]  Richard A. Yetter,et al.  FLOW REACTOR STUDIES AND KINETIC MODELING OF THE H2/O2/NOX AND CO/H2O/O2/NOX REACTIONS , 1999 .

[13]  W. C. Gardiner,et al.  Initiation rate for shock-heated hydrogen-oxygen-carbon monoxide-argon mixtures as determined by OH induction time measurements , 1971 .

[14]  Xin He,et al.  An experimental and modeling study of iso-octane ignition delay times under homogeneous charge compression ignition conditions , 2005 .

[15]  Anthony M. Dean,et al.  A shock tube study of the H2/O2/CO/Ar and H2/N2O/CO/Ar Systems: Measurement of the rate constant for H + N2O = N2 + OH , 1978 .

[16]  D. Gray,et al.  The pioneer plant concept: co-production of electricity and added-value products from coal , 1999 .

[17]  Robert H. Williams,et al.  Co-production of hydrogen, electricity and CO2 from coal with commercially ready technology. Part A: Performance and emissions , 2005 .

[18]  R. Williams,et al.  Co-production of hydrogen, electricity and CO2 from coal with commercially ready technology. Part B: Economic analysis , 2005 .

[19]  Ennio Macchi,et al.  A Thermodynamic Analysis of Different Options to Break 60% Electric Efficiency in Combined Cycle Power Plants , 2004 .

[20]  Tamás Turányi,et al.  Uncertainty analysis of updated hydrogen and carbon monoxide oxidation mechanisms , 2004 .