[A+] Final-lab report for Fixed and Fluidized beds (파이널 레포트 고정층과 유동층)

소개글

"[A+] Final-lab report for Fixed and Fluidized beds (파이널 레포트 고정층과 유동층)"에 대한 내용입니다.

목차

1. Results
2. Discussion
3. Reference

본문내용

Through the Carman-Kozeny equation, the theoretical value of pressure drop was obtained and the error between the theoretical value and the actual value was calculated. In addition, the pressure drop and height could determine the range of fixed and fluidized beds.

As the flow rate increases, the bed height is constant in the fixed bed and the pressure drop is constant in the fluidized bed. In the air case, the height is constant from 0 to 8L/min and the pressure drop value is constant from 10 to 20L/min. The range after 10L/min is in the fluidized bed state.

참고 자료

Dwivedi, P. N., & Upadhyay, S. N. (1977). Particle-fluid mass transfer in fixed and fluidized beds. Industrial & Engineering Chemistry Process Design and Development, 16(2), 157-165. doi:10.1021/i260062a001
McCabe, W. L., Smith, J. C., & Harriott, P. (2005). Unit Operations of Chemical Engineering (7th ed.). New York: McGraw-Hill Education.
Holdich, R. G. (2002). Fundamentals of particle technology. Shepshed: Midland Information Technology and Publ.
CEL-MKII fixed And fluidised Bed Apparatus. (2020, September 23). Retrieved March 28, 2021, from https://armfield.co.uk/product/cel-mkii-fixed-and-fluidised-bed-apparatus/
Minimum Fluidization velocity. (n.d.). Retrieved March 28, 2021, from https://www.sciencedirect.com/topics/engineering/minimum-fluidization-velocity