Fluid Particle Technology: Analysis and ApplicationsAlan Wesley Weimer |
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Page 76
... Combustion , Vol . 2 , pp . 777- 786 , April 21-24 ( 1991 ) . Daw , C.S. and J.S. Halow , " Modelling Deter- ministic Chaos in Fluidized Beds , " AIChE Symposium Series 289 , Vol . 88 , pp . 61-69 ( 1992 ) . Daw , C.S. and J.S. Halow ...
... Combustion , Vol . 2 , pp . 777- 786 , April 21-24 ( 1991 ) . Daw , C.S. and J.S. Halow , " Modelling Deter- ministic Chaos in Fluidized Beds , " AIChE Symposium Series 289 , Vol . 88 , pp . 61-69 ( 1992 ) . Daw , C.S. and J.S. Halow ...
Page 120
... Combustion of Char " , Canadian Journal of Chemical Eng . , 69 Aug. 1991 , pp 860 868. ( 1991 ) 4. Hyppanen , T. , Y. Y. Lee and Raimio " A Three Dimensional Model for Circulating Fluidized Bed Combustion " , in Circulating Fluidized ...
... Combustion of Char " , Canadian Journal of Chemical Eng . , 69 Aug. 1991 , pp 860 868. ( 1991 ) 4. Hyppanen , T. , Y. Y. Lee and Raimio " A Three Dimensional Model for Circulating Fluidized Bed Combustion " , in Circulating Fluidized ...
Page 152
... combustion modifications and other devices . However , many controls which reduce NO cause an increase in the concentration of incomplete combustion products such as hydrocarbons , carbon monoxide , and soot because NO is a product of ...
... combustion modifications and other devices . However , many controls which reduce NO cause an increase in the concentration of incomplete combustion products such as hydrocarbons , carbon monoxide , and soot because NO is a product of ...
Contents
Foreword | 1 |
Expansion Behavior of Gas Fluidized Beds in the Turbulent Regime | 31 |
The Introduction and Measurement of Rheological Parameters for the Characterization of Emulsion Phase | 45 |
Copyright | |
7 other sections not shown
Common terms and phrases
added mass annulus Auton average axial bed expansion bed voidage behavior bottom zone bubble trajectories calculated carbon centrifugal fluidized bed char Chem circulating fluidized bed coefficient combustion crossing cylinder dense phase density Diatomaceous earth dimensional distributor drag coefficient effect emulsion phase equations of motion fast bed flow field fluid Fluidized Bed Combustion fluidized bed reactor furnace gas and solids gas fluidized beds Geldart glass beads H₂ increase interparticle force Jaraiz kg/m³ MAJFM measured method minimum fluidization Multiphase Flow Odar packed bed parameters phase-space trajectories potential flow predicted radial profiles reaction recirculation zone region Reynolds number riser shown in Figure shows silicon nitride slip velocity slugging solids concentration solids volume concentration solution soot sorbent splash zone spray zone superficial gas velocity temperature terminal velocity tracer turbulent bed Unconverted H2S upflow values variation vibration Werther zeolite