2016
DOI: 10.1252/jcej.15we080
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Relationship between Solid Flow Rate and Pressure Drop in the Riser of a Pressurized Circulating Fluidized Bed

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Cited by 17 publications
(3 citation statements)
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“…Signifcant diferences are observed between BFB and CFB, which are mainly shown in the following three aspects: (1) Te combustion fraction of BFB is up to 75-95%, while the combustion fraction of CFB is generally 50-60%. (2) However, compared with BFB, temperature of CFB furnace is more uniform and gas-solid contact efciency is higher, which lead to higher combustion efciency obtained for CFB [30]. (3) Compared with CFB, BFB fts for various fuels with particle size in a wide range of 0-50 mm and lower calorifc value, such as straw, peat, lignite, and coke powder [31].…”
Section: Efect Of Type Of Fluidizationmentioning
confidence: 99%
“…Signifcant diferences are observed between BFB and CFB, which are mainly shown in the following three aspects: (1) Te combustion fraction of BFB is up to 75-95%, while the combustion fraction of CFB is generally 50-60%. (2) However, compared with BFB, temperature of CFB furnace is more uniform and gas-solid contact efciency is higher, which lead to higher combustion efciency obtained for CFB [30]. (3) Compared with CFB, BFB fts for various fuels with particle size in a wide range of 0-50 mm and lower calorifc value, such as straw, peat, lignite, and coke powder [31].…”
Section: Efect Of Type Of Fluidizationmentioning
confidence: 99%
“…To address the large number of variables that affect the fluid-particle drag, a number of correlations have been developed for determining the solids mass flux ( G s ), or W s , from riser operating variables and particle properties. As an example, Alghamdi et al developed a kinetic model that uses pressure drop measurements and an estimate of the mass fraction ( x ) of upward flowing solids relative to the sum that is moving both upward and downward. The value of x is obtained from a semiempirical model developed by Rhodes et al This analysis was extended to determining the solids holdup in the upper section of a riser in circulating and interconnected fluidized beds .…”
Section: Introductionmentioning
confidence: 99%
“…In CFBC, some solid particles blown out and circulate again through cyclone in the boiler. The major issue to be addressed in CFBC is that the solid circulation rate in boiler is measured by conventional methods which are unable to provide reliable accuracy at high pressure because of non-linearity [21,22]. So, there is a need to design a soft computing base controller.…”
Section: Introductionmentioning
confidence: 99%