Local and average heat transfer coefficients for heat transfer from internal tubes to a fluidized bed were investigated. A fluidized bed heat exchanger was compared to a baffled and an unbaffled exchanger in terms of power and heat transfer surface area requirements. The fluidized bed heat exchanger consisted of a...
Momentum transfer in an annular duct with upward gas-Iiquid
flow was studied under the condition that the liquid flowed as a film
only on the inner core of the annulus, the outer wall remaining dry.
Previous workers have studied climbing and falling liquid
films in tubes or on vertical planes....
Incipient boiling and burnout heat fluxes were studied for sub-cooled forced convection annular flow. Small wires varying from 0.010
to 0.020 inch in diameter were used as the inner core of the annulus
and a one inch ID glass tube 24 inches long was used as the outer tube.
This...
An analysis of the velocity and the shape of large gas bubbles
rising through tubes filled with viscous liquids is presented. Four
tubes, with diameters ranging from 0. 446 inches to 3. 97 inches, and
three liquids, with viscosities ranging from one to 200 centipoise,
were used in the study....
The purpose of this research was to study the effect of capillary
tube dimensions on the apparent viscosity of an unstable dispersion
of two immiscible liquids. The study was limited to laminar
flow at a constant temperature.
The dispersions were composed of a commercial solvent,
Shellsolv 360, manufactured by the...