U.S. patent number 3,558,052 [Application Number 04/772,320] was granted by the patent office on 1971-01-26 for method and apparatus for spraying electrostatic dry powder.
This patent grant is currently assigned to F.I.N.D. Inc.. Invention is credited to John P. Dunn.
United States Patent |
3,558,052 |
Dunn |
January 26, 1971 |
METHOD AND APPARATUS FOR SPRAYING ELECTROSTATIC DRY POWDER
Abstract
Dry nonconductive powder passes from a hopper by means of a
vibrating plate through an adjustable, nonclogging eductor and is
directed by means of a current of air issuing through a rectangular
orifice from a variable volume plenum chamber into a venturi. The
powder particles pass into the entrance of the venturi in a stream
of air having a rectangular flow pattern or cross section and from
the venturi through a discharge nozzle and from the discharge
nozzle onto a substrate to be coated. Corona wires are located in
the proximity of the issuing end of the discharge nozzle so as to
charge the powder particles in order to direct them onto a
substrate. A positive draft is maintained downstream from the
venturi entrance and serves to pick up excess powder particles
which are pneumatically conveyed back to the feed hopper.
Inventors: |
Dunn; John P. (Elmira, NY) |
Assignee: |
F.I.N.D. Inc. (Elmira,
NY)
|
Family
ID: |
25094673 |
Appl.
No.: |
04/772,320 |
Filed: |
October 31, 1968 |
Current U.S.
Class: |
239/3; 239/124;
427/477 |
Current CPC
Class: |
B05B
5/1683 (20130101); B05B 5/032 (20130101); B05B
7/1468 (20130101); B05B 7/1477 (20130101) |
Current International
Class: |
B05B
5/03 (20060101); B05B 5/025 (20060101); B05B
5/00 (20060101); B05B 5/16 (20060101); B05B
7/14 (20060101); B05b 005/02 () |
Field of
Search: |
;239/3,15,379,124
;222/193,318 ;51/8,11 ;118/308--311,(Church),93.4 ;117/17 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: King; Lloyd L.
Assistant Examiner: Church; Gene A.
Claims
I claim:
1. A dry powder spray apparatus comprising;
a. a spray housing including a venturi with a powder-gas
entrance;
b. a gas inlet for admitting gas under pressure to the housing, a
gas inlet chamber directly communicating with the gas inlet and
located ahead of the venturi, the gas from said inlet directed
toward the venturi through the gas inlet chamber;
c. a powder inlet to the spray housing above the inlet chamber,
positioned such that the powder falling by gravity from the powder
inlet is picked up by the gas flowing from the gas inlet into the
venturi, and
d. an excess powder exit from the spray housing below the powder
inlet and the gas inlet chamber so that the excess powder which has
not been picked up by the entering gas may flow from the
housing.
2. Apparatus as in claim 1 further comprising a nozzle attached to
the venturi exit.
3. Apparatus as in claim 2 wherein the nozzle is interchangeable
with other nozzles having different cross-sectional outlet openings
and the same inlet openings cooperating with the venturi exit
end.
4. Spray apparatus as in claim 1 wherein the venturi is rectangular
in cross section and the venturi entrance is rectangular in
section.
5. Apparatus as in claim 1 wherein one wall of the gas inlet
chamber has an orifice therein through which gas is directed into
the venturi entrance, the wall being adjustable to vary the gas
flow pattern of the gas entering the venturi entrance.
6. A spray apparatus as in claim 5 wherein the adjustable wall is
movable relative to the venturi entrance.
7. A spray apparatus as in claim 1 wherein one wall of the gas
inlet chamber has an orifice therein through which gas is directed
into the venturi entrance, the gas inlet chamber movably mounted
within the spray housing, whereby said wall is adjustably
positioned relative to the falling powder so as to vary the pattern
of gas entering the venturi entrance.
8. A spray apparatus as in claim 1 further comprising a return
eductor connected to the excess powder exit for returning excess
powder to a powder feed means.
9. A spray apparatus as in claim 8 further comprising: a gas inlet
in the excess powder exit prior to the return system whereby said
inlet creates a positive draft serving to guide the excess powder
into he return eductor system.
10. A spray apparatus as in claim 1 wherein the powder feed means
includes a powder hopper, a vibratory screen, and a conduit
connected to the powder inlet.
11. An apparatus as in claim 1 wherein particle charging conductors
are mounted adjacent the powder exit but upstream from the powder
exit.
12. An apparatus as in claim 9 wherein said conducting wires are
mounted so as to completely surround the powder exit.
13. An apparatus as defined in claim 12 wherein said conductors are
arranged in a rectangular configuration.
14. A spray apparatus as defined in claim 13 wherein the conductors
are adjustably attached to the outside of the spray housing.
15. A spray apparatus as defined in claim 14 wherein a conductor is
supported by an arm pivotally mounted on the spray housing so as to
be capable of positioning said conductor in one of a number of
positions along an arcuate path in the proximity of the powder
exit.
16. An apparatus as in claim 1 wherein there are a number of spray
housings connected in series with a single feed hopper and a common
eductor system.
17. A method for the electrostatic spraying of dry particles onto a
substrate, said method comprising:
a. feeding by gravity a uniform ribbon of powder particles past a
directed gas flow;
b. forming a directed gas flow having a specifically and uniformly
shaped cross section;
c. directing said gas flow onto the flow of particles traveling
transversely to said directed gas flow;
d. directing a portion of said powder particles carried by said gas
flow and said gas flow into a venturi;
e. conveying powder particles not carried by the gas flow into the
venturi to recycle the powder particled;
f. separating the powder particles in the venturi from each other
through the action of the venturi;
g. guiding the particles into an electrical charging zone adjacent
the venturi outlet, and
h. charging said particles and directing them onto a substrate.
18. A method of spraying particles as described in claim 17 further
comprising forming said gas flow so as to have a rectangular cross
section whereby said flow of particles in the venturi has a
rectangular cross section.
19. Apparatus as in claim 1, wherein the gas flow for carrying
powder is less than 600 feet per second.
Description
BACKGROUND OF THE INVENTION
1. Field of the Invention
The present invention relates broadly to the field of spraying dry
nonconductive powders onto various substrates for coating purposes
and, more particularly, to an apparatus which pneumatically conveys
the powder particles in a patterned flow through a discharge
nozzle, into an area were the powder particles are charged and
finally directed onto the surface of a substrate to be coated.
2. Prior Art
The broad concept of directing dry particles of powder or like
material onto a substrate through the use of a directed flow of air
or like conveying fluid is generally well-known in the art.
However, in the practice of these prior art methods and associated
devices directed to the electrostatic spraying of dry nonconductive
powders, difficulties are often encountered in attempting to apply
coating of uniform thickness and density. It is generally
recognized that uniformity of the deposited coating of powder can
best be accomplished if the spray consists of discrete and evenly
dispersed particles, flowing through and from the discharge nozzle
at a uniform rate.
Prior art systems encounter problems of uniform coating in that the
resultant spray is a mixture of discrete and agglomerated
particles. A number of limitations on the existing spray systems
are caused directly by the high specific gravity of the powder or
like materials being sprayed. A powder having a high specific
gravity has a tendency to settle and collect or buildup within the
apparatus of the spray system. This, of course, tends to clog the
discharge nozzles and other delivery conduits through which the
powders are being pneumatically conveyed. To overcome this settling
problem, prior art-spraying systems have utilized high velocity
fluid flow for conveying the powder particles. This, in turn, has
created a number of additional problems which also leads to a
nonuniform coating of the particles onto the desired substrate. To
overcome this settling problem, the velocities of the conveying air
or fluid, and consequently, the velocities of the conveyed powder
particles, are normally greater than 600 feet per minute and often
reach a velocity in excess of 1000 feet per minute. The flow of air
and powder at this velocity through the discharge nozzles of the
spraying devices, while eliminating the problem of settling within
the nozzles, created turbulence and resulted in the particles
striking the desired substrate with such force as to bounce off or
ricochet from the surface of the substrate thereby creating an
uneven coating. Consequently, the existing spray systems are
limited to spraying powders having a specific density in a somewhat
limited range because spraying powders having a relatively high
specific density necessitates the need of a high velocity air flow
resulting in the above-mentioned problems.
SUMMARY OF THE INVENTION
This invention relates to a spray system for spraying dry
nonconductive powder particles uniformly onto various substrates.
The apparatus of the invention includes a feed bin containing dry
powder particles which is delivered into the air stream of an
eductor system. The powder cascades, in the shape of a
substantially uniform ribbon of powder, downwardly through the
eductor system to a point where it is picked up by an air jet
issuing from a variable volume plenum chamber through a rectangular
orifice. The air jet directs the powder particles into the entrance
of a rectangular-shaped venturi where the particles are evenly
dispersed through the action of the air jet and the pressure
differential created by the venturi. The powder continues to flow
through a rectangular-shaped issuing nozzle and the particles are
eventually charged by corona or like conducting wires arranged in
the proximity of the issuing end of the nozzle. The charge
particles are then attracted to the oppositely charged substrate to
provide an even coating on the surface of the substrate.
The quantity of powder delivered to the surface of the substrate is
proportional to the rate of powder feed into the eductor system, to
the velocity of the air or other conveying fluid and to the volume
of conveying fluid which is a function of the plenum chamber
orifice. Consequently, in the present invention, the necessity for
a high velocity gas flow is eliminated through the use of a gas
plenum orifice having a rectangular-shape and by delivering a
uniform curtain or ribbon of powder to the entrance to the venturi
section.
The purpose of combining a system using a ribbon of powder and a
powder delivery system having a rectangular cross section is to
overcome the problems encountered when converting a flow of powder
having a circular cross section into a flow powder having a
rectangular flow pattern or cross section. When converting a
circular flow pattern to a rectangular flow pattern, a larger
pressure differential occurs causing a particle velocity
differential across the section or pattern of the flow. This
results in a nonuniform flow and also in a nonuniform deposition of
the powder onto the substrate. The present invention minimizes this
pressure differential and creates an even laminar flow of powder by
forming the desired cross-sectional pattern in the flow of powder
at the entrance to the venturi and accordingly designing the nozzle
section following the venturi so as to maintain the laminar
flow.
If the powder delivered to the venturi has a circular
cross-sectional pattern, then the flow of powder traveling in the
marginal portions of the circular cross section are traveling at a
slower velocity than the flow of powder traveling in the central
portion of the circular cross section. If the powder traveling
through the system has a sufficiently high specific gravity, the
slower velocity powder has a tendency to settle which results in
clogging of the system as previously mentioned. Consequently, to
prevent settling, the velocity of the powder in the slower
traveling portions of the circular pattern flow is increased
resulting in a proportional increase of the powder in the central
portion of the circular pattern. This greatly increased powder
velocity creates the problem of bounding or ricocheting of the
particles from the substrate as previously described. When a
relatively uniform rectangular cross section of powder is delivered
to the venturi the powder in all portions of the cross-sectional
pattern are traveling at approximately the same rate, consequently,
the conveying gas may be allowed to travel at a relatively lower
velocity without the worry of clogging of the system due to the
settling of powders having a high specific gravity. While it is
recognized that when spraying powders having a relatively high
specific gravity, the velocity of the conveying gas will have to be
increased, the present invention eliminates the need of a
relatively high velocity gas which results in the problems
previously described.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 s a side elevation view of the spray system with a partial
sectional view of the eductor and delivery portions of the
apparatus;
FIG. 2 is a top plan view of the nozzle and corona wire support
means;
FIG. 3 is a cross-sectional view taken on line 3-3 of FIG. 1
through the plenum chamber viewing the plenum chamber orifice;
FIG. 4 is an enlarged top longitudinal sectional view taken on line
4-4 of fig. 1 of the plenum chamber, plenum chamber orifice and
venturi portion;
FIG. 5 is a side sectional view of a delivery nozzle arranged to
coat a substrate passing the discharge end of the nozzle in a
horizontal plane;
FIG. 6 is a top plan view of FIG. 5;
FIGS. 7 and 8 are perspective views of two embodiments of a corona
wire or like electrode structure which may be used with the present
invention;
FIG. 9 is a perspective view of yet another embodiment of a corona
wire arranged in the proximity of the discharge end of the nozzle,
and
FIG. 10 is a side elevational partially schematic view of a
plurality of discharge nozzles operated from a central eductor.
DESCRIPTION OF PREFERRED EMBODIMENTS
The apparatus of the present invention comprises a feed hopper 10
arranged above a vibrating pan 12 which is activated into vibrating
movement by a vibrating source 14, FIG. 1. The vibrating pan 12
communicates directly with the upper portion of eductor 16. The
width of the eductor can be adjusted to vary in proportion to the
size of the substrate and accordingly the quantity of powder to be
ejected. The eductor communicates and leads past orifice plate 34
in which is located rectangular orifice 32. During operating, a jet
of air is directed from variable volume chamber 24 through
rectangular orifice 32 into the entrance 35 of venturi 36. The
rectangular orifice 32 and the entrance 35 of the venturi 36 are
axially aligned and are located on opposite sides of the eductor
16. The variable volume plenum chamber 24 includes an air inlet
conduit 26 channeling air into the variable volume chamber 24 from
a source which is not shown. The conduit 26 is supported within the
housing 22 by a support member 28 and is maintained in proper
position by set screw 30.
FIG. 4 is an enlarged view of the plenum chamber and orifice plate
34. The orifice plate 34 is removably mounted within the spray
housing so as to be able to change the size of the orifice opening
32. The adjustable mounting means include various notches 36 formed
by a plurality of ribs 38 arranged on each of the internal walls of
housing 22. Alternately to the embodiment shown in FIG. 4, the air
plenum chamber itself may be movably mounted within the spray
housing by mechanically securing together plates 28 and 34 which
define the chamber 24 so that they may be movably mounted as a unit
but immovable relative to one another. In other words, plate 28
could be mechanically connected to orifice plate 3 that
longitudinal sliding movement of plate 28 would result in the
movement of plate 34 either towards or away from the falling ribbon
of powder 18. The effect of the relative position of plate 34 to
the ribbon of falling powder 18 will be described in greater detail
later.
The eductor 16 has a lower portion 17 in which a positive draft is
created through an air flow entering through conduit 19 and check
valve 21 from a source which is not shown. A second venturi 23 is
connected by coupling 37 to the lower portion 17 of the eductor. A
current of air is directed into the entrance of venturi 23 through
conduit 27 from a source which is not shown. Coupled to the exiting
orifice 31 is a funnel or conical-shaped member 39 and a powder
return conduit 29. The return conduit 29 extends from the second
venturi to the feed hopper 10 and serves to deliver by
recirculation the excess powder particles which were not taken into
the entrance 35 of the first venturi 36. The feed hopper has a vent
such as a screen top 41 so that pressure of the delivery stream can
be relieved.
As previously mentioned, the entrance 35 of the venturi 36 is
arranged in axial alignment and on opposite sides of eductor 16. A
discharge nozzle 38 having a rectangular cross section has a
connection 40 to the diverging outlet 43 of the venturi 36.
Corona wires or like conducting wires 42 are mounted on a forklike
structure 4 in close proximity and behind the outlet 46 of nozzle
38. The forklike mounting structure 44 of corona wire 42 is itself
supported by arm member 48 which is adjustably attached by pivotal
mount 50 secured to the housing of the venturi by braces 52, or
like mounting means, and which may be manually adjusted by knob
54.
FIGS. 5 and 6 show an additional embodiment of the present
invention comprising another shaped nozzle 55 attached to venturi
36. The nozzle 55 of this embodiment also has a rectangular cross
section and is positioned to coat a substrate passing the exit 58
of the nozzle in a horizontal direction. Consequently, the
longitudinal sides of orifice 58 are arranged in a vertical plan
rather than in a horizontal plane as shown in FIGS. 1 and 2. It
should be noted that entrance 57 to nozzle 55, as well as any other
nozzle useable with the device of the present invention, has the
same configuration as nozzle 38 of FIGS. 1 and 2, so as to allow
rapid removal and insertion of different nozzles when a change in
nozzles is desired.
FIGS. 8 and 9 are directed to different embodiments of a corona or
like conductor used to create the ionization field between the
outlet of the discharge nozzle and the substrate. FIG. 8 shows a
plurality of electrodes 60 arranged on a crossbar support 62 which
is attached to a supporting arm 64 in a manner similar to that
previously described in the embodiments shown in FIGS. 1 and 2.
FIG. 9 is an embodiment of the present invention which includes the
arrangement of corona wires 66 in a rectangular-shape in the
proximity of but behind the exit 46 of discharge nozzle 38. The
wires 66 are supported in a generally rectangular-shape by means of
support arms 68 which may or may not be attached to the housing of
the spray device. The designations .DELTA.L indicated in FIGS. 8
and 9 represent the length of the corona wires or distances between
the electrodes which may be varied in order to effect the spray
pattern issuing from the orifice 46 of the nozzle, as will be more
fully explained later.
FIG. 10 discloses another embodiment of the present invention which
includes a plurality of nozzles 70, 72 and 74 directing powder or
like material onto a vertically traveling substrate 76. Each of the
nozzles is associated with a separate variable volume plenum
chamber and venturi generally indicated at 76, 78 and 80, and
operate in the same manner as the embodiment shown in FIG. 1. All
of the nozzles, however, can operate from a common feed hopper 84
and common eductor arrangement 82 and are serviced by a common
return system generally indicated at 86.
The operation of the preferred embodiment shown in FIG. 1 will now
be described and will substantially the same as the operation of
the system utilizing the various embodiments shown in FIGS. 5
through 10.
The powder particles are delivered by means of gravity from feed
hopper 10 into the fibrating screen or tray 12. The dry powder
particles are delivered into the upper portion of eductor 16 in a
substantially uniform curtain or ribbon 18. The uniform ribbon of
powder then passes into the air jet issuing from variable volume
plenum chamber 24 through rectangular orifice 32. As explained
previously, the position of orifice plate 34 may be varied relative
to the position of the falling ribbon of powder 18 and the entrance
35 to the venturi. By adjusting the distance between the orifice
plate 34 and the ribbon of falling powder, the position of the
intersection between the air stream issuing from orifice 32 and the
powder curtain is changed. Accordingly, the point of intersection
between the issuing stream of air and the powder curtain determines
the air flow pattern entering the venturi entrance 35.
Consequently, a regulation of the powder transfer and the powder
dispersion is established by changing the intersection between the
directed flow of air and the falling curtain of powder.
For example, considering that the position of the falling curtain
of powder is relatively fixed in relation to the air chamber
orifice 32 and the venturi entrance 35 and further assuming that
the cross-sectional area of the falling curtain of powder is
generally constant, then by adjusting the air chamber orifice plate
34 closer to or away from the powder curtain, the ratio of powder
sprayed into the entrance to the venturi in relation to the amount
returned through the return portion of the eductor 17 can be
regulated. It is obvious that the current of air issuing from
orifice 32 starts to diverge immediately upon clearing orifice 32.
Consequently, it is apparent that the farther away orifice plate 34
is from the falling curtain of powder, the larger the air flow
pattern of the issuing air current will be when it intersects the
falling curtain of powder. This results in a larger patter and
increased cased amount of particles traveling in the air flow
beyond the point of intersection.
A flow of particles having the desired cross-sectional flow pattern
then enters the venturi 36 where separation of the particles
occurs. The principle of using a converge-diverge member or venturi
section is to cause particle separation by virtue of the air
velocity differential and the shear force established by the
venturi. The particles then flow into the entrance of nozzle 38
which also has a rectangular cross section as described above. the
dry nonconductive powder particles issue from orifice 46 of nozzle
38 where they may be charged due to the action on the particles by
a corona wire 42 or like conductive wire.
The charging electrodes have been made adjustable and
interchangeable to control the patterns of the flow of particles as
they issue from the exit 46 and are deposited onto the surface of a
substrate (not shown). By changing the dimensions and/or position
of the charging electrode, the electric field distribution
established between the electrode and the substrate is also
changed, resulting in the ability to establish various spray
patterns which may adequately serve to coat difficulty shaped parts
or substrates. It is also important to note that the charging
electrodes 42 are arranged behind the nozzle orifice in order to
prevent powders from adhering to the fine wires. Dust or powders
accumulating on these electrodes reduce their operating efficiency
which eventually results in wire breakdown and a nonuniform
coating. In the specific embodiment shown in FIG. 1, the arms 48
are connected directly to a pivoted mount 50 which may be manually
adjusted by means of knob 54. Consequently, the conducting wires 42
are allowed to move in an arc which, as previously mentioned,
varies the pattern of the issuing powder particles. The pattern of
the issuing particles may also be varied by changing the length
.DELTA.L (FIGS. 8 and 9) of the conductor wires thereby changing
the ionization field between the issuing orifice 46 of the nozzle
and the substrate.
Only a portion of those particles cascading from vibrating screen
12 into the upper portion of eductor 16 are picked up by the air
jet issuing from orifice 32. The excess particles fall through the
lower portion 17 of the eductor and, if necessary, their travel may
be aided by a positive draft by an air flow-entering portion 17
through an inlet conduit 19. The air is provided from a source
which is not shown and may be controlled by check valve 21. Due to
the positive draft, the excess particles fall into a second venturi
23 into which a stream of air is directed from a source not shown
through inlet conduit 27. The particles are directed into return
conduit 29 through which they are conveyed back to the feed hopper
10 for reuse. Although air has been mentioned as the carrier gas,
it will be apparent that other gases, preferably inert to the
powder and substrate, could be used. Further, the invention can, if
desired, be utilized without the corona discharge wires.
* * * * *