Hydro-Flo Technologies offers systems to separate liquid
hydrocarbons (oils) from water by means of coalescing plate pack
systems, down to 5 ppm. This page will explain the function and
technical aspects of the DynaPac™ Cross Corrugated Coalescing Plate
Pack.
General Description:
The high efficiency of the Coalescing Plate Pack system is based
on a limited rise distance of 6 mm or 12 mm for the oil droplets.
For example, an oil droplet of 20 micron diameter at a density of 850 kg/m³
and a temperature of 20° has a rise velocity of 2 mm/min. After 3
min. retention time within the plate pack, the oil droplet will be
captured by the underside of the next plate, ensuring separation.
The configuration of the plates will force hydrodynamic
coalescence. The merging of very small oil droplets into larger ones
will create extremely enhanced coalescence. Rising oil droplets are
captured by the next higher plate. The oliophilic material of the
plates ensures that oil droplets will never reach the separator
outlet. They are concentrated at the top of the corrugated plates
and will rise through the weep holes to the developed oil layer
above the plate packs. The rise velocity is a function of the square
of the oil droplet diameter. A twice as large oil droplet will rise
four times faster, a triple size oil droplet will rise nine times
faster etc. An oil droplet of 3 mm will rise with a velocity of 0,74
m/s through the weep holes (when the density is 850 kg/m³ and the
temperature is 20°C).
Theory of the Coalescing Action and the
Separation Process:
In 1845, an English mathematician named George Stokes first
described the physical relationship that governs the settling solid
particles in a liquid (Stokes 1845). This same relationship also
governs the rising of light liquid droplets within a different,
heavier liquid. This function, simply stated is:
Where: Vp = particle rising or settling velocity, cm/sec
G = gravitational constant, 980 cm/sec2
h = absolute viscosity of continuous fluid, poise
dp = density of particle (or droplet), gm/cm2
dc = density of continuous fluid, gm/cm2
D = diameter of particle, cm
A negative velocity is referred to as the particle (or droplet)
rise velocity.
Assumptions Stokes made in this calculation are:
1) Particles are spherical
2) Particles are the same size
3) Flow is laminar, both horizontally and vertically.
Laminar flow, in this context, means flowing gently, smoothly, and
without turbulence.
From the above it may be seen that the variables are the
viscosity of the continuous liquid, specific gravity difference
between the continuous liquid and the particle, and the particle
size.
The rise rate of oil droplets is also governed by Stokes' law. If
the droplet size, specific gravity, and viscosity of the continuous
liquid are known, the rise rate may be calculated.
To calculate the size of an empty vessel gravity separator, it is
first necessary to calculate by the use of Stokes' Law the rise
velocity of the oil droplets. The size of the separator is then
calculated by considering the path of a droplet entering at the
bottom of one end of the separator and exiting from the other end of
the separator. Sufficient volume (residence time) must be provided
in the separator so that an oil droplet entering the separator at
the bottom of the inlet end of the separator has time to rise to the
surface, before the water carrying the droplet exits the opposite end
of the separator.
Calculation of rise rate by this method is a gross simplification of
actual field conditions because oil droplets are not all the same
size, and they tend to coalesce into larger droplets. Furthermore,
turbulence within a separator makes an orderly rise of very small
droplets impossible.
Droplets will rise following Stokes' law so long as laminar flow
conditions prevail.
When the particle size exceeds that which causes a rise rate
greater than the velocity of laminar flow, the flow around them as they
rise begins to be turbulent. Particles of this size and larger do
not rise as rapidly as would be expected from calculations based on
Stokes' law because of the hydrodynamic drag. They do, however,
rise very quickly in relationship to smaller droplets, and so are
removed by a properly designed separator.
Very small particles such as those of 8 microns (micrometers) and
less in diameter do not rise according to Stokes’ law (or hardly at
all) because the random motion of the molecules of the water is
sufficient to overcome the force of gravity, and therefore they move
in random directions. This random motion is known as Brownian
Motion. Fortunately, the volume of a droplet decreases according to
the cube of the diameter, so these very small droplets tend to
contain very little oil by volume, and unless there are very large
quantities of very small droplets (such as would be created by using
a centrifugal pump to pump the water) they contain negligible
amounts of oil.
When the droplets coalesce, they do not form flocs as the solid
particles can, but coalesce into larger droplets. Interfacial
tension, (sometimes referred to as surface tension), of the liquid
tends to make the droplets assume spherical shapes, since this is the
smallest possible shape for a given mass. This is convenient for a
separator designer because it is one of the conditions of Stokes’
Law. Several types of separators that utilize this principle have
been designed, including API Separators, and Corrugated Plate
Interceptors (CPI), and others. In general, the most efficient and
predictable of these systems are the Coalescing Plate Module type.
Contact us for the efficient and economical solution of your
oil-in-water problem.