U.S. patent number 3,891,121 [Application Number 05/277,998] was granted by the patent office on 1975-06-24 for method of operating a drop generator that includes the step of pre-pressurizing the liquid manifold.
This patent grant is currently assigned to The Mead Corporation. Invention is credited to Leonard G. Stoneburner.
United States Patent |
3,891,121 |
Stoneburner |
June 24, 1975 |
Method of operating a drop generator that includes the step of
pre-pressurizing the liquid manifold
Abstract
Method of operating a drop generator while avoiding spattering
during start up and termination of operations. The method includes
pressurizing the drop generator manifold with air or other gas and
with a flushing liquid formulated to leave substantially no residue
upon evaporation, before pumping coating material to the manifold.
In stopping the drop generator the flow of coating material to the
manifold is replaced with a flow of flushing liquid and the flow of
flushing liquid is then terminated and, simultaneously, an
evacuation line leading to a low pressure source is opened.
Inventors: |
Stoneburner; Leonard G.
(Chillicothe, OH) |
Assignee: |
The Mead Corporation (Dayton,
OH)
|
Family
ID: |
23063259 |
Appl.
No.: |
05/277,998 |
Filed: |
August 4, 1972 |
Current U.S.
Class: |
222/1; 347/28;
222/420; 347/89 |
Current CPC
Class: |
B41J
2/16526 (20130101) |
Current International
Class: |
B41J
2/165 (20060101); B87b 007/00 () |
Field of
Search: |
;222/420,394,108,318,109,1,334,148 ;141/119,120 ;346/75 |
References Cited
[Referenced By]
U.S. Patent Documents
Other References
IBM Technical Disclosure Bulletin Vol. 8, No. 1, June,
1965..
|
Primary Examiner: Blunk; Evon C.
Assistant Examiner: Slattery; James M.
Attorney, Agent or Firm: Biebel, French & Bugg
Claims
What is claimed is:
1. A method of commencing operation of a drop generator which
includes orifice defining means and a manifold communicating with
said orifice defining means for providing a supply of liquid
coating material thereto comprising:
a. pressurizing said manifold with a gas to a pressure above the
coating pressure necessary to cause said coating material to be
ejected from said orifice defining means as a free standing
filament which forms a series of discrete drops, and
b. thereafter introducing said coating material into said manifold
at a pressure no less than said coating pressure.
2. The method of claim 1 wherein said step of pressurizing said
manifold with gas comprises:
a. pressurizing said manifold with gas at approximately 18 psi.
3. The method of claim 1 wherein said step of introducing coating
material into said manifold comprises:
a. introducing said coating material into said manifold at
approximately 11 psi.
4. The method of claim 1 further comprising:
a. adding a flushing liquid to said manifold after said step of
pressurizing said manifold with gas and before introducing said
coating material into said manifold.
5. The method of claim 4 wherein said step of adding flushing
liquid comprises:
a. adding said flushing liquid at approximately 20 psi.
6. The method of claim 4 further comprising:
a. discontinuing said adding of said flushing liquid to said
manifold while continuing said step of introducing said coating
material into said manifold,
b. discontinuing introducing said coating material into said
manifold and commencing adding flushing liquid to said manifold,
and
c. evacuating said manifold.
7. The method of claim 6 wherein said step of evacuating said
manifold comprises:
a. evacuating said manifold at a negative pressure of approximately
15 inches of mercury below atmospheric pressure.
8. The method of claim 1 wherein said step of pressurizing said
manifold with a gas comprises:
a. pumping gas under pressure into said manifold.
9. The method of claim 8 further comprising:
a. discontinuing said pumping of said gas into said manifold after
said coating material is introduced into said manifold at said
coating pressure.
10. A method of operating a drop generator which includes an
orifice plate having means defining a plurality of small diameter
orifices therethrough, a manifold communicating with said orifices
for providing a supply of coating material thereto, and a gas port
and a liquid port communicating with said manifold comprising:
a. pumping air into said manifold through said gas port at
approximately 18 psi,
b. pumping a mixture of distilled, deionized water and denatured
alcohol through said liquid port and into said manifold at
approximately 20 psi,
c. discontinuing said pumping of air into said manifold,
d. discontinuing said pumping of said mixture after said manifold
is full of said mixture and commencing pumping of coating material
through said liquid port into said manifold at approximately 11
psi,
e. bleeding any remaining air in said manifold out through said gas
port,
f. continuing pumping of said coating material into said manifold
to cause fine filaments of said coating material to be ejected
through said orifices and form a series of discrete drops,
g. discontinuing pumping of said coating material and commencing
pumping of said mixture through said liquid port into said
manifold, and
h. substantially simultaneously discontinuing pumping of said
mixture and evacuating said manifold through said gas port at a
negative pressure of approximately 15 inches of mercury below
atmospheric pressure.
Description
BACKGROUND OF THE INVENTION
U.S. Pat. Nos. 3,560,641, 3,586,907 and 3,661,304 are directed to
noncontacting coating systems wherein a liquid coating material,
such as ink, is pumped under pressure to a manifold communicating
with a series of small diameter orifices. As the coating material
is ejected through the orifices under pressure, it forms fine
filaments of coating material which break down into series of
discrete drops. At the point where the drops break from the
filaments they pass through charging rings which, depending upon
the pattern of coating material desired on a receiving member
conveyed beneath the drop generator, either charge or do not charge
each individual drop of coating material.
An electrostatic deflecting field is set up downstream of the
charge rings and all drops which receive a charge while passing
through the charge rings are deflected from their trajectory by the
deflecting field. A catcher is also associated with the system to
catch those drops which it is desired to prevent from reaching the
receiving member. In this way it will be seen, a patterned coating,
such as printing, is applied to the receiving member.
In the operation of a drop generator of this type, it will be
apparent that it takes some discrete pressure, hereinafter termed
the operating pressure, to produce a filament of sufficient
velocity to overcome forces, such as surface tension forces,
tending to retard flow of the coating material through the
orifices.
If the flow of coating material to the drop generator is commenced
by merely opening a supply line to the manifold, it will be
apparent that the pressure build up in the drop generator from zero
to the operating pressure will occur over some finite time
period.
During this period, when the pressure acting on the coating
material has not yet reached operating pressure, a free jet will
not be produced, but instead, a pendulous mass of coating material
will collect at each orifice which weeps liquid coating material
therefrom. As the pressure acting on the coating material increases
a jet will eventually be produced inside the mass of liquid and
finally break from the mass in an uncontrolled manner, only
stabilizing after the excess liquid at the orifice has been drawn
away by entrainment in the jet.
Obviously this will result, not only in a more lengthy start up
procedure, but also in spattering of the coating and the collection
of coating material on the components of the generator. Since the
coating material is electrically conductive this can result in
shorting of the various electrical components, such as the charge
rings and deflecting field electrodes. Additionally, the
evaporation of the coating material will leave a residue on the
components of the drop generator which will eventually affect its
operation.
It will also be apparent that if drop generation is terminated by
merely terminating the supply of coating material, the pressure in
the manifold will decrease over a finite time period, again causing
masses of coating material to collect at the orifice.
SUMMARY OF THE INVENTION
In method and apparatus in accordance with the present invention
the coating material does not contact the filament forming orifices
until the pressure necessary to form a free filament of coating
material has been reached in the manifold. This is accomplished by
first pressurizing the manifold with a gas, such as air, to a
pressure at least equal to or preferably substantially above the
operating pressure required for production of a free standing
filament of coating material.
Thereafter, the coating material is pumped to the manifold at or
above operating pressure and, since the manifold has already been
pressurized before introducing the coating material, the coating
material arrives at each of the orifices at or above operating
pressure and immediately forms a free standing filament issuing
from the orifice and forming a series of discrete drops.
By this method the collection of pendulous masses of coating
material at the orifice and the contamination of the generator
components is substantially avoided. There may, however, be a fine
spray associated with the transition from gas to liquid coating
material at each of the orifices as the coating is ejected
therefrom. If this momentary spray or misting is found
objectionable, it may also be substantially eliminated by
interposing an additional step before the pumping of the coating
material to the manifold.
Thus, a flushing liquid characterized by a substantial absence of
residue upon evaporation, may be pumped to the manifold before the
coating material is pumped thereto. Thus, if any misting or
spraying occurs during the transition from gas to liquid at the
orifices the liquid will quickly evaporate, with negligible residue
resulting. After free standing filaments of flushing liquid are
established at each of the orifices the supply of flushing liquid
to the manifold is terminated and simultaneously replaced with a
flow of coating material at or above operating pressure. Also, at
this point any gas which remains entrained in the manifold may be
bled therefrom.
In terminating operation of the drop generator the supply of
coating material is terminated and simultaneously replaced with a
supply of the flushing liquid. Thereafter, the supply of flushing
liquid is terminated and simultaneously a line is opened from the
manifold to a waste sump operating at a pressure substantially
below atmospheric. This sudden reduction of pressure in the
manifold is sufficient to terminate the jets of flushing liquid
without producing masses of liquid at the orifices or the formation
of erratic drops.
Air may conveniently be used as the pressurizing gas and the
flushing liquid may be any liquid which evaporates without
appreciable deposit of residue. In this regard, a mixture of
approximately 50 percent distilled, deionized water and 50 percent
denatured alcohol appears satisfactory.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is a somewhat schematic showing of a drop generator in
accordance with the present invention;
FIG. 2 is a cross sectional view taken on line 2--2 of FIG. 1;
FIG. 3 is an enlarged cross sectional view showing the formation of
coating material accumulations that result when pressure is allowed
to build up gradually at the orifices; and
FIG. 4 is an enlarged cross sectional view similar to FIG. 3 but
showing the formation of filaments and drops of coating material in
accordance with the present invention.
DESCRIPTION OF THE PREFERRED EMBODIMENTS
As seen in FIGS. 1 and 2 of the drawings, a drop generator 10 in
accordance with the present invention may include manifold 12
having a chamber 14 formed therein. Mounted beneath the manifold 12
is an orifice plate 16, a spacer plate 18, a charge ring plate 20,
a pair of deflecting electrodes 22 attached to the charge ring
plate, as at 23, and a catcher 24 spaced from the electrodes by
mounting means 26.
Coating material supplied to the chamber 14 will be ejected through
the orifices 28 to form fine filaments which break up into discrete
drops of coating material. It is desirable that if a charge is to
be applied to a particular drop it is applied at approximately the
point at which the drops break from the filaments. Thus, the spacer
plate 18, having a series of openings 30 formed therethrough,
spaces the charge ring plate 20 at the proper distance from the
orifice plate 16 such that the charge rings 32 charge each of the
drops of coating material just as they break from their respective
filaments of coating material.
Thereafter, the electrodes 22 deflect all charged drops toward the
blade 34 of the catcher 24 while uncharged drops are allowed to
impinge on a receiving member 36 conveyed in any convenient manner
past the drop generator, as indicated by the arrow in FIG. 2 of the
drawings. The above description is merely for purposes of
background and for a more detailed description reference may be had
to the two above noted U.S. Pat. Nos. 3,560,641 and 3,586,907.
With regard to the present invention, it will be seen that if the
supply of coating material to the chamber 14 is commenced by merely
opening a valve from a source of coating material, it will take
some finite time interval until the pressure in the chamber 14 has
built up to operating pressure, that is the pressure at which the
coating material will overcome forces, such as surface tension
forces, tending to prevent its being ejected from the orifices as
free standing jets.
Thus, until pressure builds up to operating pressure the coating
material will tend to form pendulous masses, as indicated at 38 in
FIG. 3 of the drawings, which weep coating material downwardly,
contaminating other components of the generator, such as the charge
rings 32. To avoid this, chamber 14 is prepressurized with the
system shown somewhat schematically in FIG. 1 of the drawings.
Thus, a gas port 40 is provided leading to one end of the chamber
14 while a liquid port 52 communicates with the opposite end of the
chamber. A gas, such as air, is pumped through line 44 and valve 46
by means indicated at 48. A second line 50 also communicates with
the gas port 40 and is provided with a valve 52 and a source of
negative pressure as indicated at 54. A bleed line 55 also branches
from port 40, controlled by valve 56.
Liquid port 42 may be fed by line 57, which includes a valve 58 and
is connected with means, as indicated at 60, for pumping a flushing
liquid through the line 57. Also connected to port 42 is a line 62,
controlled by valve 64, and through which coating material may be
pumped by pump 66.
With the above system the sequence of operation is as follows. All
lines leading to the chamber 14 are closed. Next, valve 46 is
opened, allowing air or other pressurizing gas to be pumped through
line 44 by means of pump 48 at a pressure in excess of operating
pressure. The pressure and flow rate of gas is such that the
pressure in the chamber 14 quickly rises to a pressure above normal
operating pressure, despite the escape of gas through the orifices
28.
Coating material may then be introduced into the system by opening
valve 64 and pumping the coating at or above operating pressure
through liquid port 42. The coating material will advance through
the chamber 14 in a coherent wave, from right to left as seen in
FIG. 1 of the drawings. Since it is at or above operating pressure
as it reaches each of the orifices, free standing jets are formed,
as seen at 70 in FIG. 4 of the drawings, which break down into
series of discrete drops 72. Preferably, valve 46 is closed about
0.3 seconds after the opening of valve 64.
As the flow at each of the orifices transfers from gas to liquid, a
slight misting may be experienced. If this is found to be
objectionable, a flushing liquid may be introduced into the
manifold before the introduction of coating material. Thus, the
above procedure may be modified as follows.
With all valves initially closed, valves 46 and 58 are opened,
allowing gas to be pumped from source 48 and a flushing liquid to
be pumped from source 60, both the gas and flushing liquid being at
a pressure in excess of operating pressure. Again, the liquid
entering the chamber 14 will advance as a coherent wave, replacing
the gas flow at each of the orifices 28 with a liquid flow at or
above operating pressure.
While the transfer from gas to flushing liquid may also result in a
fine mist or spray at each of the orifices 28, this will not affect
or contaminate the components of the generator since the flushing
liquid is formulated such that it leaves virtually no residue upon
evaporation.
After the free standing jets of flushing liquid are formed at each
of the orifices 28 and the valve 46 has been closed, valve 64 is
opened and simultaneously valve 58 is closed. This allows coating
material at or above operating pressure to flow through line 62 and
liquid port 42 into the chamber 14, displacing any flushing liquid
therein with coating material. Thereafter, any air or other gas
which may remain in the system may be bled out through line 55 and
valve 56.
When it is desired to terminate operation of the drop generator,
valve 64 is closed and valve 58 opened, causing the flow of coating
material to be replaced by a flow of flushing liquid. Thereafter,
valve 58 is closed and valve 52 is simultaneously opened, causing
both the flow of flushing liquid to terminate and the evacuation of
the system to a waste sump operating at a pressure substantially
below atmospheric pressure. This sudden reduction in pressure in
the system is sufficient to terminate the jets 70 without producing
erratic drops below the orifices or allowing coating material to
collect in pendulous masses about the orifices.
Under normal operating conditions, providing pressurizing gas at
approximately 18 psi, flushing liquid at approximately 20 psi and
coating at approximately 11 psi has been found satisfactory for the
usual range of viscosities found in coating materials such as ink
and with an orifice plate having 600 orifices of 1.5 mil diameter.
Additionally, evacuating the drop generator upon termination of
operations to a waste sump at approximately 15 inches of mercury
below atmospheric pressure has been found satisfactory.
From the above it will be apparent that the present invention
provides method and apparatus for operating a drop generator
without the problems normally associated with start up and shut
down procedures.
While the methods and forms of apparatus herein described
constitute preferred embodiments of the invention, it is to be
understood that the invention is not limited to these precise
methods and forms of apparatus, and that changes may be made
therein without departing from the scope of the invention.
* * * * *