By Melvyn Pell; J C Williams; Terence Allen

Sustainable agriculture is a swiftly turning out to be box aiming at generating meals and effort in a sustainable means for people and their youngsters. Sustainable agriculture is a self-discipline that addresses present concerns corresponding to weather swap, expanding meals and gas costs, poor-nation hunger, rich-nation weight problems, water pollutants, soil erosion, fertility loss, pest regulate, and biodiversity depletion. Novel strategies are Read more...

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Extra resources for Handbook of powder technology / Volume 8, Gas fluidization / Mel Pell

Example text

4. The temperature differential across the densely packed tube bank A was 136 °C versus only 41 °C for longer tube bank C. It is possible for the heat transfer coefficient to be according to design and for the overall heat removal to be poor if the particles are not at the assumed temperature. Consider a particle circulating in tube bank A. It is at the nominal bed temperature at the b o t t o m and is moving up slowly due to reduced circulation. Since heat transfer is good, the particle cools as it continues to rise.

F . Davidson and D. Harrison,"Fluidized Particles" Cam­ bridge Univ. Press (1963). 4. M. Matsen, Evidence of Maximum Stable Bubble Size in Fluidized Beds AIChE Symp. Ser. 69, 30 (1973). 5. J. Werther, Hydrodynamics and Mass Transfer Between the Bubble and Emulsion Phases in Fluidized Beds of Sand and Cracking Catalyst, in "Fluidization" ed. by D. Kunii and R. Toei, Engineering Foundation (1973) New York. 6. M. Horio and A. Nonaka, A Generalized Bubble Diameter Cor­ relation and Its Application to Fluidized Bed Reactor Model­ ing, Presented at AIChE meeting, San Francisco, November, 1984.

Consequently, performance tends to be poorer since solids circulation is reduced by the baffle effect of the tubes. 1 show two heat transfer banks which were tested in the pressurized fluid bed boiler plant at Grimethorpe, England (7). 4. The temperature differential across the densely packed tube bank A was 136 °C versus only 41 °C for longer tube bank C. It is possible for the heat transfer coefficient to be according to design and for the overall heat removal to be poor if the particles are not at the assumed temperature.

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