Managing Heat Transfer Intensity in a Fluidized Particle-in-Tube Solar Receiver

Abstract

Particle flow structure and associated heat transfer coefficient are examined as a function of temperature in a single-tube fluidized bed solar receiver operating in upward particle flow mode. It is found that temperature has a strong effect on both fluidization regimes and wall-to-bed heat transfer coefficient that varies in the range 800-1200 W/(m2.K). Turbulent fluidization regime results in the most intense heat transfer between the irradiated wall and the fluidized particle.

Keywords

• Particle-Driven CSP
• Solar Receiver
• Fluidized Bed
• Heat Transfer