Salva Flashcards
What is two-phase flow, flow patterns?
Two-phase flow involves the flow of a mixture of two phases: gas, solid or liquid. Flow patterns are the ways in which the phases are distributed over the cross section of the pipe or duct. Dependent on the flow of each component, the physical properties of phases e.g viscosity, surface tension, density, and the geometry and dimensions of the pipe or vessel.
To consider
- Drag force
- Gravitational force
- Drag force:
Transfer of energy from the faster to the slower phase
Because of gravity, density will be v important so lighter phase will move faster in vertical flow -> slip between phases - Gravitational force:
In vertical flow, we will have axial symmetry
In horizontal flow, gravity acts perpendicular to the direction of flow so no axial symmetry.
List of vertical flow patterns
Bubbly, slug (plug), churn, wispy annular and annular, mist
bubbly -> mist, increase of flow of gas from left to right
What happens when bubbles larger than 30% of diameter of pipe?
They start to coalesce, transitions occur due to bubble coalescence (bubbly to slug) and film flooding (when suddenly liquid goes down) (slug to churn)
Characteristics of:
- slug or plug
- churn
- wispy annular
- annular
- slug or plug:
bubbles characterised by spherical nodes, and occupy almost entire cross section of the pipe - churn:
you have oscillations in the liquid (going up and down), irregular shaped portions of gas and liquid - wispy annular:
has portions of liquid around sides of pipe and also some in the middle
annular:
less oscillations, all of the liquid touching the walls
Difference in vertical DOWNWARD co-current flow, to UPWARDS
when does vertical counter current occur?
In vertical downward co-current, similar patterns are obtained but the pattern is very sensitive to the upstream distributor. Drag force and gravitational force are in the same direction. Counter current (gas up, liquid down) is difficult to obtain. Most typically is annular flow, only happens w low gas velocities, if higher velocity then it will change the liquid direction.
List horizontal flow patterns
bubbly, plug, stratified, wavy, slug, annular, spray or dispersed
lowest flow of gas -> highest flow of gas
Characteristics of
- plug
- stratified
- wavy
- slug
- annular
CONSTANT LIQUID FLOW RATES
- plug:
bubbles are at the top - Stratified:
all the bubbles have coalesced, completed separation of has and liquid (g at top) - wavy:
more instability - slug:
eventually waves will touch the top of the pipe - crest of waves touching the top - annular:
liquid touching walls with layer thicker at bottom due to gravity
Two phase flow in bend-coils
A bend can induce coalescence to form slug flow. In general, a bend will act as a phase separator. In condition of annular flow, situation is not as bad as intuitively expected:
- liquid continues to bubble as a film on inside surface of the bend
- momentum of gas phase is high
Single stage bubble column reactor applications and important parameters to know
Applications: absorption, catalytic slurry reactors, bioreactors, coal liquefaction Important parameters: - residence time - bubble size -> interfacial area - rate of mass transfer
Gas bubbles in fermenters
- Small bubbles «1mm diameter can become a nuisance as they are slow to rise.
- d < 2 -3 mm, surface tension effects dominate behaviour of the bubble surface. They behave as rigid spheres with immobile surfaces and low internal gas circulation. kL will decrease w decreasing bubble diameter due to surface tension effects.
- > 3mm diameter, bubbles are able to wobble, this increases kL
Example of kLa use, aerobic fermentation
- cells in aerobic culture take up oxygen from the liquid
- oxygen solubility approx 10 ppm at ambient T and P
- at high cell densities, cell growth may become limited by availability of oxygen in the liquid phase
- when cells are dispersed and well mixed, the major resistance to oxygen transfer is the liquid film surrounding the gas bubbles
Taylor flow
Two phase flow characteristics of capillaries are different from flow in larger channels, capillary forces are significant in monolith channels:
0.5 mm < dchannel < 5mm
Surface tension forces (which are stronger than gravity) tend to render the flow characteristics independent of channel orientation.
Taylor flow is characterised by elongated bullet-shaped has bubbles that almost fill the entire cross section of a channel section, separated by liquid slugs. A thin liquid film separates these bubbles from the wall and also connects the two successive liquid slugs separated by the gas bubble.
The liquid slugs are free from gas entrainment. There is a recirculating flow in the liquid slugs, which improves heat and mass transfer. The separation of liquid slugs reduces axial dispersion. Very important for microreactor applications.
Taylor flow practical example:
benzaldehyde -> benzylalcohol -> toluene + H2O
Monolithic catalysts compared to a trickle-bed reactor in mass-transfer limited reactions
- Higher productivity:
Taylor flow internal circulations and shape of bubbles etc (characteristics) allowed conversion as improves both heat and mass transfer (both solid-liquid and liquid-gas) - Higher selectivity:
Residence time better controlled (through length of reactor) so can stop before toluene is produced. Gas and liquid have sharp residence time distributions, also gets rid of non-selective stagnant zones, thin catalyst wall due to monolith diameter limitations so reactant doesn’t stay in too long.
What is cavitation?
The pressure driven process of vapour bubble formation and collapse in a liquid
What is NPSHa
The excess of pressure head over the vapour pressure of the pumped liquid at the suction nozzle. Greater than zero -> no cavitation
What are pumps/compressors
Equipment used to deliver fluids from one location to another.
Pumps for liquids, compressors for gases
Classification of pumps
a) positive displacement
- rotary e.g gear, peristaltic
- reciprocating e.g diaphragm, piston/plunger
b) kinetic
- centrifugal
- peripheral
- special