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Sulfur is a low viscosity liquid between ~116° and ~159°C (Oppenheimer [1992]; Takano et al. [1994]).
In contrast, the coalescence time in a high viscosity liquid was much greater than that of a low viscosity liquid with the same Weber number.
Effects of liquid viscosity, liquid height and gas sparger have been investigated in the bubble column.
Further, the lift force acting on single bubbles rising in low viscosity liquid (corresponding to the wobbling regime, 1.1≤Eo≤8.72, −10.6≤logMo≤−14.6) was investigated.
The flow characteristics of high viscosity oil and gas flow show several significant differences with those of low viscosity liquid.
Core annular flow pattern, where a low viscosity liquid surrounds a very-viscous one, may be very interesting for heavy oil transportation.
Similar(47)
Cooling of the samples triggers a transformation from low modulus solid-like to high viscosity liquid-like behaviour and at 85% co-solute, shear moduli increase by about five decades.
However, recent studies show that two-phase flow behavior of high viscosity liquids is significantly different than that of low viscosity liquids.
This situation is typical for marbles containing low viscosity liquids (Bormashenko et al. 2010b).
Higher viscosity liquids have lower head generation at the same exit blade angle.
Atomization of high viscosity liquids for industrial processes requires the design of more efficient atomizers.
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