Measurements of solids concentration and axial solids velocity in gas-solid two-phase flows.

Several techniques reported in the literature for measuring solids concentration and solids velocity in (dense) gas-solid two-phase flow have been briefly reviewed. An optical measuring system, based on detection of light reflected by the suspended particles, has been developed to measure local solids concentration and local axial solids velocity in dense gas-solid two phase flows. This system has been applied to study hydrodynamics of a cold-flow circulating fluidized bed unit operated in the dense flow regime (uD: 7.5?15 m s?1 and Gs = 100?400 kg m?2 s?). With increasing solids mass flux, at constant superficial gas velocity, lateral solids segregation became more pronounced (i.e. extent of development of core-annulus structure) while the radial profiles of axial solids velocity hardly changed. A decrease in superficial gas velocity, at constant solids mass flux, also augmented the lateral solids segregation. The axial solids velocity decreased over the entire tube radius, although the shape of the profiles showed no strong dependence with respect to the superficial gas velocity. Average solids mass fluxes calculated from the measured local values of solids concentration and solids velocity exceeded the imposed solids mass flux, a finding which could be explained by the downflow observed visually of solid particles close to the tube wall. In addition, cross-sectional averaged solids concentrations obtained on the basis of the optical measuring system and those obtained from the pressure gradient measurements showed satisfactory agreement.

[1]  Yong Jin,et al.  The axial distribution of the cross-sectionally averaged voidage in fast fluidized beds , 1992 .

[2]  Yoshinobu Morikawa,et al.  LDV measurements of an air-solid two-phase flow in a vertical pipe , 1984, Journal of Fluid Mechanics.

[3]  William H. Press,et al.  Book-Review - Numerical Recipes in Pascal - the Art of Scientific Computing , 1989 .

[4]  S. Soo,et al.  Concentration and Mass Flow Distrbutions in a Gas-Solid Suspension , 1964 .

[5]  S. Saxena,et al.  Particle velocity measurements in a circulating fluidized bed , 1993 .

[6]  R. N. Bartholomew,et al.  Measuring Solids Concentration in Fluidized Systems by Gamma-Ray Absorption , 1957 .

[7]  B. T. Chao,et al.  A novel radioactive particle tracking facility for measurement of solids motion in gas fluidized beds , 1985 .

[8]  Measurement of local fines movement in a fluidized bed of coarse particles by a fluorescent tracer technique , 1989 .

[9]  Masayuki Horio,et al.  The Clustering Annular Flow Model of Circulating Fluidized Beds , 1989 .

[10]  Filip Johnsson,et al.  Radial voidage profiles in fast fluidized beds of different diameters , 1991 .

[11]  Gabriel Wild,et al.  Gas and solid behavior in cracking circulating fluidized beds , 1992 .

[12]  L. Garnero,et al.  Mapping solid concentration in a circulating fluid bed using gammametry , 1991 .

[13]  R. Dry Radial concentration profiles in a fast fluidised bed , 1986 .

[14]  A. Nishiwaki,et al.  Measurement of the velocity and direction of flow of solid particles in a fluidized bed , 1980 .

[15]  William H. Press,et al.  The Art of Scientific Computing Second Edition , 1998 .

[16]  Tomasz Dyakowski,et al.  Measurement of particle velocity distribution in a vertical channel , 1993 .

[17]  Dimitri Gidaspow,et al.  Dense, vertical gas‐solid flow in a pipe , 1992 .

[18]  M. Yianneskis Velocity, particle sizing concentration measurement techniques for multi-phase flow , 1987 .

[19]  Hiroyuki Kage,et al.  The use of optic fiber probes for the measurement of dilute particle concentrations: calibration and application to gas-fluidized bed carryover , 1983 .

[20]  M. J. Rhodes,et al.  Modelling the flow structure of upward-flowing gas-solids suspensions , 1990 .

[21]  John-Chang Chen,et al.  Solid mass fluxes in circulating fluidized beds , 1992 .

[22]  A. Berker,et al.  Hydrodynamics of gas-solid flow in a catalytic cracker riser: Implications for reactor selectivity performance , 1986 .

[23]  Yong Jin,et al.  Investigation on slip velocity distributions in the riser of dilute circulating fluidized bed , 1992 .

[24]  J.B. Gajewski,et al.  Electrostatic method for measuring the two-phase pipe flow parameters , 1990, Conference Record of the 1990 IEEE Industry Applications Society Annual Meeting.

[25]  E. W. Grohse Analysis of gas-fluidized solid systems by x-ray absorption , 1955 .

[26]  C. A. Myler,et al.  PARTICLE VELOCITY MEASUREMENTS THROUGH ELECTROSTATIC FIELD FLUCTUATIONS USING EXTERNAL PROBES , 1987 .

[27]  L. S. Leung,et al.  A quantitative definition and flow regime diagram for fast fluidization , 1986 .

[28]  M. Louge,et al.  QUANTITATIVE CAPACITIVE MEASUREMENTS OF VOIDAGE IN GAS-SOLID FLOWS , 1989 .

[29]  M. Louge,et al.  Measurements of voidage near the wall of a circulating fluidized bed riser , 1990 .