Solid hold up in gas fluidised beds

Chemical Engineering and Processing

Volumn 41, Issue 4, 2002, Pages 373-379

  Hilal, N ^a   Gunn, D J ^b  

^a UNIVERSITY OF NOTTINGHAM   (United Kingdom)

^b Process Engineering Systems   (United Kingdom)

Author keywords

Distributor; Fluidisation; Hold up; Particles

Indexed keywords

CORRELATION METHODS; GAS FUEL ANALYSIS; PARTICLE SIZE ANALYSIS;

GAS FLUIDISED BEDS;

PARTICLES (PARTICULATE MATTER);

FLUIDIZED BED; HOLD-UP;

EID: 0036532696     PISSN: 02552701     EISSN: None     Source Type: Journal    
DOI: 10.1016/S0255-2701(01)00158-1     Document Type: Article

References (22)

1. Heat transfer from vertical surfaces to dense gas-fluidised beds
2. Heat transfer from vertical surfaces to dense gas-fluidised beds
3. The expansion characteristics of bubbling fluidised beds
4. Flow regimes and void fraction distribution in gas fluidisation of large particles in beds without tube banks
5. Large particles fluidisation
6. The expansion of bubbling fluidised beds
7. Scaling up of gas-fluidised bed reactors
8. Effect of distributors on gas-solid fluidisation
9. Effect of distributor design on heat transfer from an immersed horizontal tube in a fluidised bed
10. The influence of gas distributor on bed expansion, bubble size and frequency in fluidised beds
11. Effect of bed diameter, distributor and inserts on minimum fluidization velocity
12. Transient multi gas-solid reactions in a bubbling fluidized bed
13. Comparison of commonly used correlations for minimum fluidisation velocity of small solid particles
14. Deviation of actual minimum fluidisation velocities from theoretical prediction at different temperatures
15. A generalised methodology for estimating minimum fluidisation velocity at elevated pressure and temperature
16. Minimum fluidisation velocities and pressure drop in fluidised beds
17. The expansion of gas-fluidised beds in bubbling fluidisation
18. Uber die grundlegenden berechnungen bei der schwerkraftaufbereitung
19. The resistance to motion of a solid sphere in a fluid
20. Fluid-particle interactions and flow characteristics of fluidized beds and settling suspensions of spherical particles
21. Correlating distributor effect on expansion of particles in fluidized beds with inserts