Todays powder systems typically use one of two major types of recovery
systemscartridge filter systems or cyclone separator systems. New powder
system customers may often explore the pros and cons of both types of designs
when deciding what type of system to purchase. With the trend toward more colors,
more frequent color changes and faster color-change times, more and more, new
and existing, powder coaters want to understand the differences between the
two types of systems. Note that this discussion assumes a one-to-one cartridge
system vs. cyclone separator system comparison. It does not intend to discount
the possibility of multiple systems, power-and-free conveyors, or roll on/roll
off systems.
 |
| 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.