 |
Figure
1: Conventional Cyclone Separator Theory of Operation |
With
the possibility of many different system configurations, the economic
advantages or disadvantages of any single- or multiple-system configuration
would need to be comparatively analyzed relative to desired throughput,
number of colors, frequency of color changes, operating costs, initial
capital expenditure and return on investment. At some point, however,
a cartridge filter type system with its associated cost of additional
color modules and/or the cost of spraying to waste and not reclaiming,
plus the added operating cost of relatively longer color-change
times, may exceed the initial capital expenditure and operating
costs of a cyclone separator system.
Relatively
recent technological advances in powder booth and recovery designs
have shown that cyclone separator systems can achieve color-change
times ranging from 8-20 min with two operators. This capability
provides finishers spraying numerous colors a potential economic
advantageresulting in reduced operating costs and higher throughput.
Cyclone
SeparatorsTheory of Operation
Relative to powder system operations, a cyclone separator is a device
used to separate powder particles from an incoming air stream within
a conical cylinder, using the principle of centrifugal acceleration.
(See Figure 1) The air stream is injected at high velocities into
the inlet pipe, which is positioned tangentially to the body of
the cyclone. The shape of the cone induces the high velocity air
stream to spin, thus creating a vortex within the conical cylinder.
The larger particles within the air stream are forced outward toward
the wall of the cyclone, where the drag of the spinning air and
ensuing gravitational forces cause them to fall down the sides of
the cyclone into an outlet at the base of the cyclone. Simultaneously,
the smaller, lighter particles are captured within the center of
the spiral-like air stream and are drawn out or discharged through
an outlet at the top of the cyclone.
Table
I: Cyclone Separator Efficiencies |
|
Powder
'A'
|
Powder
'B'
|
Powder
'C'
|
Cycle
1 |
94.6%
|
98.6%
|
91.3%
|
Cycle
2 |
98.3%
|
98.9%
|
97.7%
|
Cycle
3 |
99.6%
|
99.3%
|
98.3%
|
Cycle
4 |
99.9%
|
99.9%
|
99.9%
|
This
separation process requires a continuous, steady flow of air, free
from fluctuations or intermittent variations in flow rate. Therefore,
the finer particles that exit the top of the cyclone are drawn by
and extracted to an after-filter with exhaust fan and motor, downstream
of the cyclone separator. This after-filter is the source of the
high-velocity air stream that is drawn into the spray booth and
through the cyclone, ensuring adequate containment of oversprayed
powder within the system.Another separation process occurs within
the after-filter, whereby the fine particles that were extracted
from the cyclone separator are captured by primary cartridge-style
filters in the after-filter. Finally, the air stream is then exhausted
into the room through final HEPA style filters.
 |
Nordson
Sure Clean™ System with Compact Twin Cyclone Separator |
Cyclone
Separator Efficiency
The purpose of measuring cyclone separator efficiency relative to
powder spray systems is to understand the ratio of separated powder
particles. In other words, what percentage of larger powder particles
are being extracted at the base of the cyclone and reclaimed for
re-spray? And, what percentage of finer powder particles is being
extracted at the top of the cyclone and ultimately collected by
the after-filter?
The
amount of powder particles captured within a truly efficient cyclone
separator and conveyed back to the spray guns should be in the high
90-percentile range. As stated previously, the powder particles
that are extracted through the top of the cyclone are finer particles.
The powder particles captured at the base of the cyclone are relatively
larger particles.
It
has been claimed that larger powder particles tend to take on an
electrostatic charge better than finer powder particles. In addition,
it has been claimed that finer particles do not fluidize well, and
consequently do not pump and convey as effectively as larger particles.
Therefore, it is important to remove or separate the finer particles
from the powder spray system to improve overall system efficiency.
An
important design feature included in the design of experiment that
affects cyclone separator efficiency, as well as system efficiency,
is the method used to extract powder from the base of the cyclone
and the speed it is removed. For maximum cyclone and system efficiency,
it is required to remove the powder captured within the cyclone
separator at a high rate of volume.
Efficiency
Test Parameters
Efficiency testing was performed using three powders from various
sources. The following equipment developed by Nordson Corporation
was used for the test
- Sure
Clean™ Powder Spray System with rotating floor and Apogee™
canopy
- Sure-Max™
Powder Transfer System
- Spectrum®
Powder Feed Center
- Sure
Clean™ Compact Twin Cyclone Separator (Figure
2)
Table
II: Particle Size Analysis
|
Powder
|
Median
Particle Size (Micron)
|
Volume
Percent Under 9.82 Microns
|
Volume
Percent Under 5.43 Microns
|
Cycle
1 - Virgin
|
|
|
|
A
|
38
|
9.9
|
2.1
|
B
|
84
|
4.0
|
0.2
|
C
|
33
|
18.8
|
7.9
|
Cycle
2
|
|
|
|
A
|
37
|
6.1
|
0
|
B
|
80
|
3.0
|
0
|
C
|
39
|
6.5
|
0
|
Cycle
3
|
|
|
|
A
|
42
|
2.0
|
0
|
B
|
83
|
2.1
|
0
|
C
|
41
|
4.0
|
0
|
Cycle
4
|
|
|
|
A
|
43
|
1.4
|
0
UNDER 6.3
|
B
|
86
|
1.1
|
0
UNDER 6.3
|
C
|
42
|
2.2
|
0
|
Each
test began with a 15-lb charge of powder that was poured onto the
rotating Sure Clean booth floor while the booth was in operation.
The Sure-Max Powder Transfer System was also in operation at this
time. As the booth floor rotated underneath the extraction duct
suspended above it, the powder was then drawn into the duct and
through the cyclone. Any powder that was recovered in the cyclone
was then extracted at the base of the cyclone by the Sure-Max powder
transfer system, and conveyed from the cyclone separator to the
Spectrum Powder Feed Center. The floor was allowed to make several
revolutions to ensure that all the powder had been recovered. An
air lance was also used to remove any residual agglomerated powder
on the booth floor that occurred when powder was dumped, rather
than sprayed, into the spray booth. The system after-filter was
then turned off as the Sure-Max Powder Transfer System continued
to run. Several foam cylinders were then run through the Sure-Max
transfer line to remove any residual powder that was contained within
it. The feed center was then turned off and the Sure-Max conveyor
was disassembled. The filter was weighed and any remaining powder
residue in the body of the Sure-Max Transfer System was brushed
into the recovery container. Powder in the recovery container was
then weighed and added to the weight of any powder captured on the
Sure-Max filter. This total weight represents the yield of the cyclone
and was divided into the starting weight (15 lbs.) to determine
cyclone efficiency. See Table I for results.
Further
Analysis
Three powders were run through the system for a total of four "cycles"
each. No virgin powder was added to any of the individual test runs.
The yield weight was included in each subsequent efficiency calculation.
Particle size analysis illustrates the role of the cyclone separator
as classifier, with almost all particles under five microns removed
from the recovered powder on the first cycle (See Table II). The
result in subsequent cycles was an increase in cyclone efficiency,
typically exceeding 98% in the first cycle and 99.5% within three
cycles when tested with virgin powders containing less than 10%
of their mass under 10 microns and a median particle size of 28
microns.
Conclusion
Cyclone separator efficiency plays an integral role in overall system
efficiency. To achieve optimum overall system efficiency, it is
also important to have the highest possible first-pass transfer
efficiencygreatest level of powder particles attracted to
the part. Furthermore, the amount of powder "in process"
during operation plays a key role in system efficiency. In other
words, all powder systems will have some amount of overspray. The
key is to first minimize the amount of overspray, and to keep any
overspray circulating through the system, without allowing it to
reside in either the spray booth or the cyclone separator. Achievement
of these goals will result in optimum overall system efficiency.
To define your system needs and understand them better, it is recommended
that you contact a knowledgeable powder equipment supplier to determine
the most economical and efficient system configuration for your
operational goals.
Serving
the Finishing Industries. Since 1936.
PF Onine and all contents are properties of Gardner Publications,
Inc.
All Rights Reserved.