U.S. patent number 3,765,605 [Application Number 05/310,947] was granted by the patent office on 1973-10-16 for apparatus for ejecting a mixture of liquids.
Invention is credited to Frederick E. Gusmer, Joseph E. Hayes, Jr., Carl W. Sundberg, Jr..
United States Patent |
3,765,605 |
Gusmer , et al. |
October 16, 1973 |
APPARATUS FOR EJECTING A MIXTURE OF LIQUIDS
Abstract
Two mutually reactive liquids, such as the components of a
polyurethane foam, are mixed together and ejected onto a substrate
by means of apparatus that pumps the liquids separately and
remotely mixes them only at the last moment. Heretofore, the
liquids were separately pumped by means of parallel reciprocating
proportioning pumps to which the liquids are fed under pressure;
and as a result of this feed pressure the outlet pressure of the
pumps varied with respect to the direction of stroke. By
rearranging the pumps in tandem opposed relation, and driving them
by a constant pressure motor such as a double-acting fluid motor, a
counterbalancing effect is created which effectively reduces the
pressure variation as the stroking action reverses.
Inventors: |
Gusmer; Frederick E.
(Mantoloking, NJ), Sundberg, Jr.; Carl W. (Chatham, NJ),
Hayes, Jr.; Joseph E. (Manasquan, NJ) |
Family
ID: |
23204728 |
Appl.
No.: |
05/310,947 |
Filed: |
November 30, 1972 |
Current U.S.
Class: |
239/61; 239/413;
239/332; 137/565.33 |
Current CPC
Class: |
B29B
7/7626 (20130101); B29B 7/7615 (20130101); B01F
15/0462 (20130101); B29B 7/7663 (20130101); B29B
7/603 (20130101); B01F 15/0237 (20130101); B29B
7/7684 (20130101); B29B 7/7404 (20130101); Y10T
137/86163 (20150401) |
Current International
Class: |
B01F
15/04 (20060101); B29B 7/30 (20060101); B29B
7/60 (20060101); B05b 007/04 (); B05b 009/04 ();
B05b 007/12 () |
Field of
Search: |
;239/61,93,94,321,322,331,332,407,413 ;137/566,567 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Ward, Jr.; Robert S.
Claims
What is claimed is:
1. Apparatus for ejecting a mixture of liquids, comprising an
ejection head, means for separately feeding two streams of liquids
from separate sources of said liquids to said ejection head and for
mixing said streams of liquids in said ejection head, said feed
means comprising a pair of double-acting reciprocating piston pumps
one individual to each of said streams, means for supplying each of
said pumps with liquid under elevated pressure from a respective
one of said sources, means for separately delivering said liquids
from said pumps to said ejection head, and means for driving said
pumps in opposed tandem relationship comprising a double-acting
reciprocating constant pressure motor common to said pistons of
said pumps.
2. Apparatus as claimed in claim 1, said motor being a fluid motor
comprising piston means and piston rod means connected to said
pistons of said pumps.
3. Apparatus as claimed in claim 2, said fluid motor being a
hydraulic motor, and means for alternately supplying hydraulic
liquid to and exhausting hydraulic liquid from opposite sides of
said hydraulic motor.
4. Apparatus as claimed in claim 1, said motor and said pumps being
in axially aligned relationship.
5. Apparatus as claimed in claim 1, said means for supplying
liquids to said pumps under elevated pressure comprising positive
displacement transfer pumps one individual to each said stream.
Description
The present invention relates to apparatus for ejecting a mixture
of liquids, more particularly a mixture of mutually reactive
liquids such as those that form a foam on a substrate and that cure
by reacting with each other, for example, the components of a
polyurethane foam and elastomeric coatings.
Such mixtures of liquids are ejected from a mixing chamber under
pressure onto a substrate, for example by apparatus such as is
disclosed in Gusmer U.S. Pat. Nos. 2,890,836 and 3,263,928. As the
liquids are highly reactive with each other, they cannot be mixed
together in the apparatus until the last possible moment, or else
they will react in the apparatus and clog the apparatus. Therefore,
as the mixture must be ejected under pressure, it is necessary to
pump the mutually reactive liquids to elevated pressure by separate
pump means, the reactive liquids following generally parallel flow
paths from separate sources of the respective liquids to the mixing
chamber from which they are ejected onto the substrate.
The proportion of the liquids in the mixture that is ejected must
be maintained constant and must be closely controlled. Accordingly,
it is necessary carefully to regulate the quantity of each of the
liquids that is pumped to the mixing chamber; and for this purpose,
proportioning pumps of the reciprocating piston type are often
used, the valves of which pumps are arranged to create pumping
action when stroked in either direction, thus providing continuous
flow. Because the pumps are bifunctionally used as a measuring
device, it is necessary to prevent cavitation; therefore the pumps
must themselves be pressure fed.
The feeding of the proportioning pumps under pressure, however,
gives rise to a problem: During the refill stroke of the
proportioning pump, the feed pressure to the pump will add to the
outlet pressure of the pump; while during the displacement stroke
of the proportioning pump, the feed pressure becomes nullified by
the closing of the inlet valve. There is thus a fluctuating
variation in the outlet pressure of the proportioning pump, which
in magnitude, by virtue of the mechanical design of the pump,
actually is multiplied to twice the feed pressure to the
proportioning pump.
Accordingly, it is an object of the present invention to provide
such apparatus in which the outlet pressure of the proportioning
pumps tends to be much more uniform than heretofore.
Another object of the present invention is the provision of such
apparatus which will be relatively simple and inexpensive to
construct, easy to operate, maintain and repair, and rugged and
durable in use.
Briefly, the objects of the present invention are achieved by
coupling the two proportioning pumps in opposed tandem relationship
and driving them by a single double-acting fluid motor. Quite
unexpectedly, it has been found that the undesirable pressure
fluctuation at the outlet at both proportioning pumps is thus
greatly reduced and under certain circumstances virtually
eliminated.
Other objects, features and advantages of the present invention
will become apparent from a consideration of the following
description, taken in connection with the accompanying drawing,
which is a schematic view of apparatus according to the present
invention.
Referring now to the drawing in greater detail, there is shown
apparatus according to the present invention for ejecting a mixture
of liquids, comprising an ejection head 1 in the form of a barrel 3
with an elongated cylindrical mixing chamber 5 therein that is open
at its discharge end, that is, at its right hand end as seen in the
drawing. A pair of opposed inlets 7 and 9 extend through the side
walls of barrel 3 and open into chamber 5 substantially
tangentially of chamber 5. A plunger 11 is slidably disposed in
barrel 3 and is manually actuable to reciprocate between the
position shown in the drawing, in which the inlet openings 7 and 9
are both exposed for the flow of materials to be mixed into chamber
5, and a rightward position as seen in the drawing in which plunger
11 closes the inlet openings 7 and 9 fully fills the chamber 5
thereby completely to eject the reactive mixture from chamber 5.
The construction and operation of ejection head 1 is known in the
art and need not be further described. It can for example be as
disclosed in the above-mentioned Gusmer U.S. Pat. No. 3,263,928, in
which case the chamber 5 is of uniform cross sectional
configuration substantially throughout its length, including the
discharge opening, so that foam may be ejected from ejection head
1; or ejection head 1 can have the form shown in the above Gusmer
U.S. Pat. No. 2,890,836, with a discharge opening reduced in
diameter as compared to the mixing chamber, for the ejection of a
spray.
The mutually reactive liquids reach ejection head 1 along separate
paths, as mentioned above. Thus, in the case of a polyurethane
resin and the activator therefor, for example, as described in the
above Gusmer U.S. Pat. No. 3,263,928, the activator may come from a
supply container 13 maintained under a positive pressure of, say, 2
or 3 p.s.i.g., by a source of nitrogen 15 which prevents the entry
of air and water vapor into container 13. Activator flows from
container 13 through a check valve 17 and then through a piston
pump 19 by which its pressure is elevated for the purpose described
above, for example to 100 p.s.i.g. From pump 19, the activator
proceeds through a check valve 21 to the primary pump chamber of
the activator proportioning pump 23 in which a piston 25 is
reciprocable under the impetus of a displacement piston rod 27.
Piston 25 divides the double acting pump 23 into two chambers,
primary chamber 29 and displacement chamber 31. From chamber 29,
activator flows through conduit 33 and check valve 35 toward
conduit 37 which communicates with activator inlet opening 7, and
also toward conduit 39 which communicates with chamber 31 of pump
23. It is during the rightward stroke of piston 25, as seen in the
drawing, that the pressure imparted to the activator by pump 19
tends to be additive and the outlet pressure of pump 23 to be
relatively high; while it is during the leftward stroke of the
piston 25 as seen in the drawing that the pressure imparted by pump
19 becomes nullified and the outlet pressure of pump 23 is
proportionally lower. It is this periodical fluctuation of the pump
outlet pressure that the present invention largely overcomes.
On the resin side, the path of the liquid is similar, from a
container 39 maintained under positive pressure by nitrogen 41,
through a check valve 43, to higher pressure through a pump 45,
then through a check valve 47 to pump 49 including a piston 51 that
divides pump 49 into chambers 53 and 55. From chamber 53, resin
flows through conduit 57 through a check valve 59 and thence to
resin inlet conduit 61 communicating with resin inlet opening 9,
and also to conduit 63 communicating with chamber 55.
However, piston 51 is on the same piston rod 27 as piston 25 and is
axially aligned therewith, the piston rod also being the piston rod
of a double-acting fluid motor 65 comprising a double-acting piston
67 that divides motor 65 into chambers 69 and 71. In the
illustrated embodiment, fluid motor 65 is a hydraulic motor fed
from a source of hydraulic liquid in a sump 73 through a constant
pressure, variable volume pump 75 and thence through an
automatically periodically reversing spool valve 77 actuated by a
solenoid S, to conduits 79 and 81 that are alternately feed and
return conduits, the hydraulic liquid returning to sump 73 through
a return conduit 83. Alternatively, motor 65 could be an air motor
or an electric motor, so long as it remains a constant pressure
motor.
In operation, the nature of the liquids, their flow rates and
temperatures and the pressures imparted thereto by pumps 19, 29, 45
and 53, may all be conventional, for example as disclosed in the
above-identified Gusmer patents, and hence need not be further
mentioned. The activator and the resin proceed from their
respective containers 13 and 29 through their respective pumps 19
and 45, in which they are elevated in pressure; although it will be
understood that pumps 19 and 45 can be eliminated and if the
nitrogen or other dry inert gas at 15 and 41 is of sufficiently
high pressure. In any event, the liquid streams at elevated
pressure flow along parallel paths to the respective pumps 23 and
49, the activator entering chamber 29 while the resin enters
chamber 53. Piston 25 is moving to the left relative to chamber 29
at the same time that piston 51 is moving to the left relative to
chamber 53, as seen in the drawing, so that the pumps 23 and 49 are
acting in opposition to each other. During this particular stroke
of the pumps, the valve 77 is in the position shown in the drawing,
with hydraulic fluid being fed by pump 75 to chamber 71 and
discharged from chamber 69. At the end of the stroke of the piston
rod 77 with its associated pistons 25, 51 and 67, solenoid S
reverses the position of valve 77 so that hydraulic fluid under
pressure is fed to chamber 69 and exhausted from chamber 71,
whereupon piston 67 and with it the rod 27 and pistons 25 and 51 is
driven to the right as seen in the drawing, which reverses the
stroke of both pumps 23 and 49.
As a result of the pistons 25 and 51 being thus coupled in opposed
tandem relationship and actuated by the same reciprocating fluid
motor, it is found that the discharge pressure in conduits 37 and
61, which in the past might have varied from, say, about 700 to
about 900 p.s.i. depending upon the direction of stroke of the
pumps 23 and 49, now varies very little from a means pressure of
800 p.s.i.
From a consideration of the foregoing disclosure, therefore, it
will be evident that all of the initially recited objects of the
present invention have been achieved.
Although the present invention has been described and illustrated
in connection with a preferred embodiment, it is to be understood
that modifications and variations may be resorted to without
departing from the spirit of this invention, as those skilled in
this art will readily understand. Such modifications and variations
are considered to be within the purview and scope of the present
invention as defined by the appended claims.
* * * * *