U.S. patent number 3,901,184 [Application Number 05/491,031] was granted by the patent office on 1975-08-26 for pneumatic powder flow diverting device.
This patent grant is currently assigned to Continental Can Company, Inc.. Invention is credited to James G. Buck, Robert D. Payne.
United States Patent |
3,901,184 |
Payne , et al. |
August 26, 1975 |
Pneumatic powder flow diverting device
Abstract
This invention is directed to a pneumatic flow switching device
particularly adapted for the electrostatic coating of tubular
workpieces, particularly can bodies, and includes a generally
cylindrical chamber, a conduit for peripherally delivering a
fluidized admixture of powder and air into the chamber, means for
peripherally exhausting the powder-air admixture from the chamber,
means adjacent the conduit for directing air tangentially into the
chamber whereby the powder-air admixture is directed toward the
exhausting means, and means for pneumatically traversing the
powder-air admixture generally axially of the chamber for the
delivery to an article intended to be treated thereby.
Inventors: |
Payne; Robert D. (Countryside,
IL), Buck; James G. (Western Springs, IL) |
Assignee: |
Continental Can Company, Inc.
(New York, NY)
|
Family
ID: |
23950519 |
Appl.
No.: |
05/491,031 |
Filed: |
July 23, 1974 |
Current U.S.
Class: |
118/629; 118/308;
239/124; 239/698; 118/312; 239/693 |
Current CPC
Class: |
B05B
5/032 (20130101); B05B 7/1468 (20130101); B05B
5/1683 (20130101) |
Current International
Class: |
B05B
5/025 (20060101); B05B 5/03 (20060101); B05B
5/00 (20060101); B05B 5/16 (20060101); B05B
7/14 (20060101); B05B 005/02 () |
Field of
Search: |
;118/629,627,308,312,309
;222/193 ;239/3,15,124,125,127 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Stein; Mervin
Assistant Examiner: Salser; Douglas
Attorney, Agent or Firm: Diller, Brown, Ramik &
Wight
Claims
We claim:
1. A pneumatic flow switching device comprising a generally
cylindrical chamber, means delivering a fluidized admixture of
powder and air into said chamber, means for exhausting the
powder-air admixture from said chamber, first means contiguous said
delivering means for pneumatically directing said powder-air
admixture from said delivering means toward said exhausting means,
and second means for pneumatically traversing said powder-air
admixture during its movement between said delivering and
exhausting means for directing said powder-air admixture primarily
axially from said chamber.
2. The pneumatic flow switching device as defined in claim 1
wherein said first delivering means introduces air into said
chamber in a generally tangential direction relative to said
cylindrical chamber.
3. The pneumatic flow switching device as defined in claim 1
wherein said exhausting means exhausts the powder-air admixture in
a generally tangential direction relative to said cylindrical
chamber.
4. The pneumatic flow switching device as defined in claim 1
wherein said delivering means and said exhausting means are
separated from each other by at least 90.degree..
5. The pneumatic flow switching device as defined in claim 1
including venturi means into which said axially exhausted
powder-air admixture is delivered by said second pneumatic
means.
6. The pneumatic flow switching device as defined in claim 1
including means for supporting an article to be coated by the
powder of said powder-air admixture adjacent the axial output
thereof from said chamber.
7. The pneumatic flow switching device as defined in claim 1
including a source for said powder-air admixture, and means for
returning said peripherally exhausted powder-air admixture to said
powder-air source.
8. The pneumatic flow switching device as defined in claim 1
including means for supporting an article to be coated by the
powder of said powder-air admixture adjacent the axial output
thereof from said chamber, and means for charging the powder prior
to reaching the article whereby the latter is electrostatically
coated.
9. The pneumatic flow switching device as defined in claim 2
wherein said exhausting means exhausts the powder-air admixture in
a generally tangential direction relative to said cylindrical
chamber.
10. The pneumatic flow switching device as defined in claim 2
wherein said delivering means and said exhausting means are
separated from each other by at least 90.degree..
11. The pneumatic flow switching device as defined in claim 2
including venturi means into which said axially exhausted
powder-air admixture is delivered by said second pneumatic
means.
12. The pneumatic flow switching device as defined in claim 2
including means for supporting an article to be coated by the
powder of said powder-air admixture adjacent the axial output
thereof from said chamber, and means for charging the powder prior
to reaching the article whereby the latter is electrostatically
coated.
13. The pneumatic flow switching device as defined in claim 3
wherein said delivering means and said exhausting means are
separated from each other by at least 90.degree..
14. The pneumatic flow switching device as defined in claim 3
including venturi means into which said axially exhausted
powder-air admixture is delivered by said second pneumatic
means.
15. The pneumatic flow switching device as defined in claim 3
including means for supporting an article to be coated by the
powder of said powder-air admixture adjacent the axial output
thereof from said chamber, and means for charging the powder prior
to reaching the article whereby the latter is electrostatically
coated.
16. The pneumatic flow switching device as defined in claim 112
including a source of said powder-air admixture, and means for
returning said peripherally exhausted powder-air admixture to said
powder-air source.
17. The pneumatic flow switching device as defined in claim 12
including a source of said powder-air admixture, and means for
returning said peripherally exhausted powder-air admixture to said
powder-air source.
Description
This invention relates to coating articles, and in particular, to
electrostatically coating tubular articles such as can bodies or
the like.
Can bodies have the interior surfaces thereof coated with an enamel
where the cans are intended to contain beverages or varieties of
food products. A thin coating of enamel is usually applied to the
interior metal surface of the can by a roller coating process
before it is shaped to form the can. During the shaping operation
the enamel is usually scratched or otherwise subjected to minor
damage which exposes small areas of the metal, rendering the
interior can surface liable to corrosion by the contents thereof.
The damage affected to the interior enamel coating during can
shaping is generally repaired by spraying the interior of the can
with a coating of lacquer after fabrication and before attachment
of an end thereto. This process is extremely wasteful of lacquer
because not only is the lacquer sprayed on to the damaged areas but
it is also sprayed on those areas which are undamaged and thus
consequently do not require further coating.
The enamel coating and/or the lacquer is heated and until recent
developments organic solvents were driven off by the heat creating
undesirable atmospheric emissions which presently are becoming
increasingly regulated by States as well as by the Federal
Government. The latter factor has increased the use of coatings
without organic solvents for protective or decorative applications,
and since the appearance on the market of the latter materials
powder coatings have held a strong position among competitive
technologies. Flame spraying, fluid bed and similar means have been
used for at least twenty years to apply powders and other
solvent-free protective coatings.
Approximately one-half dozen years ago electrostatic deposition
technology was employed to stripe welded can bodies on a commercial
basis and the success thereof has served as a basis for the
development of electrostatic powder technology for coating the
inside of beer and soft drink containers. The favorable economics
associated with electrostatic coating, either full coat, full
overcoat, and/or repair coat, is mainly due to lower material costs
on a per can body basis, the reduction in air pollution control
equipment and, in some instances, reduction of steps in earlier
conventional processes (i.e., the elimination of the two coat
system).
In the practice of what is termed the "single" mode operation beer
can bodies are entirely electrostatically coated in a single step
to give a defect-free coating. Since the deposition occurs after
the can body blanks are fabricated into cylindrical bodies
subsequent scratching does not occur and again conventional lacquer
coating operations are eliminated.
In the "single mode" of operation a powder gun pneumatically
discharges an admixture of the electrically charged coating powder
and air through the can body resulting in a very thin over-all
coating. When operating on a commercial basis the can bodies must
be rapidly moved into and out of the spray area and of prime
concern is the powder flow to the powder gun which must be
accurately controlled in order not to waste powder between
cans.
In keeping with the foregoing a primary object of this invention is
to provide a novel device for pneumatically switching the flow of
the powder, the device including a cylindrical chamber, means for
delivering a fluidized admixture of powder and air into the
chamber, means for exhausting the powder-air admixture from the
chamber, first means contiguous to the delivering means for
pneumatically directing the powder-air admixture from the
delivering means toward the exhausting means, and second means for
pneumatically traversing the powder-air admixture during its
movement between the delivering and exhausting means for directing
the powder-air admixture primarily axially from the chamber toward
an area at which an article is to be coated or otherwise effected
by the powder portion of the powder-air admixture.
A further object of this invention is to provide a novel pneumatic
flow switching device of the type immediately heretofore set forth
wherein the first-mentioned directing means is a port opening
generally tangentially into the cylindrical chamber whereby air
directed into the chamber therethrough tends to propel the
powder-air admixture in a circular pattern within the chamber.
A further object of this invention is to provide a novel pneumatic
flow switching device for activating the second directing means
only when an article is at a position to be effected by the powder
portion of the powder-air admixture.
yet another object of this invention is to provide a novel
pneumatic flow switching device including means for supporting an
article, preferably a tubular can body, adjacent the axial output
of the chamber whereby the article will be coated by the powder of
the powder-air admixture.
Still another object of this invention is to provide a novel
pneumatic flow switching device of the type aforesaid wherein means
are provided for charging the powder and/or article whereby the
latter is electrostatically coated.
With the above and other objects in view that will hereinafter
appear the nature of the invention will be more clearly understood
by reference to the following detailed description, the appended
claimed subject matter, and the several views illustrated in the
accompanying drawings.
IN THE DRAWINGS
FIG. 1 is a perspective view of the pneumatic flow switching device
of this invention, and illustrates powder-air delivery and exhaust
port spaced peripherally with respect to a generally cylindrical
chamber, an air input port disposed tangentially with respect to
the delivery port, and an axially disposed air input port for
propelling the normally circularly flowing powder-air admixture to
and through a powder gun for subsequent deposition upon an
associated article.
FIG. 2 is a fragmentary front elevational view looking from
right-to-left in FIG. 1, and illustrates constructional details of
the switching device including an annular discharge orifice for the
powder-air admixture.
FIG. 3 is a cross-sectional view taken generally along the line
3--3 of FIG. 2, and illustrates details of the chamber construction
and a venturi downstream of the axially disposed air inlet
port.
FIG. 4 is a cross-sectional view taken generally along line 4--4 of
FIG. 3, and illustrates details of the powder-air admixture flow
when the axially disposed air inlet port is cut off from a
pressurized air source during a non-coating cycle of the
device.
The pneumatic flow switching device of this invention is generally
designated by the reference numeral 10, and as is best illustrated
in FIG. 1, the over-all construction includes a housing 11 defined
by a pair of rectangular preferably transparent plates 12, 13 (FIG.
3) secured together by bolts 15 in a conventional manner. The
plates are centrally contoured to define a generally cylindrical or
circular chamber 16 having a peripheral wall surface 17. Means 18
in the form of a generally radially disposed port functions to
deliver an admixture of powder and air into the chamber 16 at
approximately the 12 o'clock position thereof, as viewed in FIG. 4.
Means, generally designated by the reference numeral 20, in the
form of another port is provided for exhausting the powder-air
admixture from the chamber in a continuous fashion irrespective of
whether or not an article is being coated at a station S (FIG. 3)
or being transported to or removed therefrom, in the manner to be
described more fully hereinafter. Additional means 21 in the form
of another port or conduit is disposed such that air is directed
generally tangentially into the chamber 16 at approximately the 12
o'clock position and adjacent the port 18 resulting in the
powder-air admixture traveling in a generally circular path
augmented by the curvature of the surface 17 from the 12 o'clock
position of the chamber 16 to approximately the 7-8 o'clock
position at which it is exhausted through the port 20.
Reference is made once again particularly to FIG. 1 in order to
indicate the manner in which the switching device 10 is part of a
circulating system, generally designated by the reference numeral
25 which includes a source of pressurized air, such as a pump 26
coupled by a conduit 27 to a conventional switch 28. The switch 28
is, in turn, coupled by a conduit 30 to a source 31 of powder, the
particular nature of which will be described more fully
hereinafter. The air introduced into the powder source 31 through
the conduit 32 maintains the powder-air admixture therein in a
fluidized state in order that it might be pneumatically moved
through the system 25 with its delivery into the interior of the
chamber 16 being under the control of an adjustable valve 32 in a
conduit 33 which is in turn coupled to the conduit or delivery port
18.
By the same token the air input port 21 is a conduit which is
likewise coupled to the valve 28 whereas the exhaust port or
conduit 20 is fed back to the powder source 31 for subsequent
recirculation. Fresh powder, as necessary, may be fed into the
powder source or fluidized bed from any other area through a
conduit 34. Thus, in the non-coating or non-application mode of
operation the powder-air admixture from the source 31 follows a
closed path defined by the conduit 33, the adjustable valve 32, the
conduit 18, the interior of the chamber 16, and the conduit 20
augmented by air introduced into the chamber 16 through the conduit
21 with the bed 31 being maintained in a fluidized condition by air
introduced thereinto through the conduit 30.
The "normal" generally circular path of travel of the powder-air
admixture within the chamber 16 just described is interrupted in
order to disrupt the flow path of the powder-air admixture within
the chamber 16 and instead redirect the same axially outwardly
therefrom. The change in travel of the powder-air admixture is
effected by a generally axially disposed nozzle or air inlet port
35 which projects through a bore 36 of the plate 12 into the
chamber 16 and is positioned with a discharge opening 37 thereof
closely adjacent an inlet end 38 of a venturi tube 40 having a
leftwardly (as viewed in FIG. 3) converging tubular passage 41. The
venturi 40 has a reduced end 42 received within a bore 43 of the
plate 13 and is held therewithin by a tubular flanged member 44
whose flange 45 is conventionally secured to the plate 13. An end
portion 46 of a powder nozzle or gun 47 is sandwiched and held
captive between the venturi 40 and the tubular member 44 and
terminates at its leftmost end in a circular opening 48. Housed
within the powder nozzle 47 is a conductive element 50 having a
generally bell-shaped end 51 projecting beyond the circular opening
48 and having a maximum diameter as defined by a circular edge 52
slightly less than the circular opening 47 thereby defining a
generally annular discharge area 53 between the bell 51, the
projecting leftward end of the element 50, and the circular opening
48. This configuration is designed to achieve a generally annular
"cloud-like" flow of the powder-air admixture as it departs the
orifice 48 for subsequent application to an article supported to
the left as viewed in FIG. 3.
Assuming that an article, such as an open-ended tubular can body,
is supported to the left of the gun 47 as indicated by the
reference numeral S, and preferably coaxial therewith, the "normal"
flow of the powder-air admixture heretofore described is
interrupted by operating the valve 28 such that air from the pump
26 is additionally directed through the nozzle or conduit into the
chamber 16 and/or the inlet 38 of the passage 41 of the venturi
tube 40. So long as sufficient air is emitted from the nozzle or
jet 35 the powder-air admixture continuously delivered into the
chamber 16 will be delivered by the powder gun 47 and particularly
through the orifice toward and into the can body in the desired
configuration as determined by the particular contour of the area
generally designated at 53. It is emphasized that during the
redirection of the powder-air admixture from its normal path
(generally circular) to a path axial thereto there need be no
stoppage of the flow of air to the source 31 through the conduit 30
nor air into the chamber 16 through the conduit 21. The effect of
air issuing from the jet 35 simply redirects the powder-air
admixture along an axial path to perform the desired coating
operation, and upon the termination of air flow to the jet 35 by
appropriately operating the switch 28 the "normal" path is
reestablished and the powder-air admixture resumes flow from the
chamber through the conduit 20 to the source 31 with the latter
being augmented by an exhaust pump (not shown) in the line 20.
As was stated earlier the particular use to which the device 11 is
applicable is that of electrostatically coating in the single mode
of operation. In this mode of operation and variations thereof the
fundamental laws of electrostatics apply, namely, like charged
bodies repel each and unlike charged bodies attract. Applied first
to the coating of a can body this can be interpreted to mean that
if charged coating particles are introduced into the inside of the
can body at the support S they will be attracted with an
appreciable force to an oppositely charged can body. Inasmuch as no
particular can body and/or powder charging system forms part of
this invention, that for the can body is indicated in FIG. 3
diagrammatically by simply illustrating the support S as part of an
electrical system. Insofar as the charging of the powder is
concerned, this may be readily effected by a conductor 54
conventionally connected to the element 50 which in turn is
preferably insulated by, for example, an insulated spider from the
powder nozzle 47. Irrespective of the particular charging system
employed the electrostatic forces are desirably sufficiently strong
to hold the powder in place against the bare interior surface of
the can body in order that the powder will not be displaced during
transportation from the coating station to a final fusing station
in an oven, an induction heat unit, or the like.
It is further appreciated that all powder directed into the can
body by the powder gun 47 will not be attracted to the can body
interior by electrostatic forces and the exodus of excess powder
therefrom would be costly if simply wasted. Accordingly, the end of
the can body most remote from the powder gun 47 is preferably
encircled by a hood connected to a vacuum source which is in turn
connected to the powder source 31. If as described earlier the
conduit 20 includes a vacuum source the conduit may simply be
extended and coupled to the hood such that both the chamber 16 and
the hood, as well as any can body thereat, are continuously under
the effect of the vacuum source to return excess powder to the
source 31.
The following are merely typical examples of the type of powders
which may be utilized in accordance with the present invention:
Type Code Supplier ______________________________________ Epoxy 71
AP 14 Armstrong Products Company, Inc. Epoxy F100C Oxyplast, Ltd.
Polyamide Nylon 11 Aquitaine-Organics Polyethylene- Butene SK 4002
Sinclair-Koppers Company Polyethylene SK 7007 Sinclair-Koppers
Company ______________________________________
While preferred forms and arrangement of parts have been shown in
illustrating the invention, it is to be clearly understood that
various changes in details and arrangement of parts may be made
without departing from the scope and spirit of this disclosure.
* * * * *