Results 201 to 210 of about 755 (262)
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Fluidised bed drying of soybeans

Journal of Stored Products Research, 2001
The fluidised bed drying characteristics of soybeans at high temperatures (110-140 degrees C) and moisture contents, 31-49% dry basis, were modelled using drying equations from the literature. Air speeds of 2.4-4.1 m/s and bed depths from 10 to 15 cm were used. The minimum fluidised bed velocity was 1.9 m/s.
, Soponronnarit   +3 more
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The expansion of gas-fluidised beds in bubbling fluidisation

Chemical Engineering Science, 1997
The expansion of gas-fluidised beds has been examined in the range of Archimedes number from 100 to 105 using five grades of glass ballotini and two grades of lead shot of narrow size distribution, and Diakon particles of wide size distribution. A porous plastic distributor plate was used in beds of diameters 89 and 290 mm.
D.J. Gunn, N. Hilal
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The fluidised bed

Intensive Care Medicine, 1995
The process of fluidisation involves blowing warm air through small solid microspheres thus creating a liquid, without wetness. The warmth provides some important properties including reducing the metabolic rate in thermal injury which has a beneficial effect on mortality, modifying catabolism after surgery, providing gradual vasodilation in shock and ...
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Electroheated fluidised beds

Proceedings of the Institution of Electrical Engineers, 1969
Use of electroheated fluidised beds is a fast-growing branch of electroheating, but this growth has been hampered because the models available hitherto were incomplete, in that they ignored flow and mode dependence and were unnecessarily complicated for the engineer concerned with practical industrial processes.
W.K. Roots, Ersin Tulunay
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Thermal degradation of PMMA in fluidised beds

Waste Management, 2004
In recent years, the production and consumption of plastics have increased significantly and wastes are commonly incinerated or dumped in a landfill. Plastics pyrolysis, on the other hand, may provide an alternative means for disposal of plastic wastes with recovery of valuable gasoline-range hydrocarbons or the monomer.
Smolders, K., Baeyens, J.
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Characteristics of fluidisation behaviour in a pressurised bubbling fluidised bed

The Canadian Journal of Chemical Engineering, 2012
AbstractThe experiments were carried out in a bench‐scale fluidised bed of 90 mm in diameter to determine the influence of pressure on fluidisation characteristics of Geldart A and B particles over the range of pressure 0.1–4.5 MPa. For Geldart B particles, the results indicate that minimum fluidisation velocity (umf) was found to decrease with ...
Haoyu Li   +3 more
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A circulating fluidised bed

Powder Technology, 1976
Abstract Induced particle circulation was studied in a 0.3 m diam. air fluidised bed of sand with central draught tubes of 0.2 m and 0.15 m diam. and 0.6 m and 1.2 m in length. A “two-dimensional” bed, 0.3 m in width, of similar cross-section, was also used to study catalyst particle circulation.
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Circulating fluidised-bed combustion

Applied Energy, 1990
Abstract A mathematical model for the steady-state combustion of char in a circulating fluidised bed (CFB) has been developed by taking into account the bed's hydrodynamic conditions, chemical-reaction rates, and combustion mechanism and the conservation of mass and energy. The model is an improvement over the simplified combustion model developed by
Asit Das, S.C. Bhattacharya
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Fluidised beds as ‘coolth’ stores

Applied Energy, 1991
Abstract High energy-density thermal storage at low temperatures is feasible using phase-change materials. Thus an energy-storage device has been conceived which uses water-absorbing cross-linked polymers, known as hydrophilic materials. These were produced in the form of particles, which can be hydrated.
D. Kay   +3 more
openaire   +1 more source

Flow patterns in fluidised beds

Rheologica Acta, 1965
The characteristics of the behaviour of the particles in a liquid fluidised bed in which the influence of the bubbles of fluid is small, depends at a particular liquid flowrate, on the size and size range of the particles.
B. Scarlett   +2 more
openaire   +1 more source

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