U.S. patent number 3,704,962 [Application Number 05/176,080] was granted by the patent office on 1972-12-05 for fluidized material pump.
This patent grant is currently assigned to N. L. Industries, Inc.. Invention is credited to Wyatt Weeks.
United States Patent |
3,704,962 |
Weeks |
December 5, 1972 |
FLUIDIZED MATERIAL PUMP
Abstract
A pump for pumping fluidized pulverulent material such as clay
or barite from a point of supply to a point of discharge, the pump
undergoing a cycle comprising a filling cycle and a discharge
cycle, the cycling being self-automated, being actuated by
pneumatic controls and control valves solely by the air used for
pressurizing the entire device. The changeover from the filling
portion of the cycle to the discharge portion of the cycle and
thence back to the filling portion of the cycle when the discharge
portion has been completed, and so on repeatedly, is self-regulated
by the device itself, so that no other source of power such as
electricity is needed. The rate at which the pump cycles may be
regulated by the operator, this regulation involving again a
strictly pneumatic control.
Inventors: |
Weeks; Wyatt; J. (Houston,
TX) |
Assignee: |
N. L. Industries, Inc. (New
York, NY)
|
Family
ID: |
22642891 |
Appl.
No.: |
05/176,080 |
Filed: |
August 30, 1971 |
Current U.S.
Class: |
417/143;
417/146 |
Current CPC
Class: |
B65G
53/22 (20130101) |
Current International
Class: |
B65G
53/22 (20060101); B65G 53/04 (20060101); F04f
001/06 (); F04f 003/00 () |
Field of
Search: |
;417/900,143,145,146,114,115 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Croyle; Carlton; R.
Assistant Examiner: Gluck; Richard E.
Claims
Having described the invention, I claim:
1. A pump for fluidized pulverulent material comprising in
combination;
an air supply;
chamber means for receiving and discharging said material;
one-way entry means for ingress of material into said chamber;
discharge outlet means for said material;
aeration means in said chamber for fluidizing and expelling said
material from said chamber;
vent means for venting air from said chamber while said chamber is
receiving material;
vent closure means for said vent operatively connected with said
chamber and responding to air pressure within said chamber so as to
permit said vent to open while said chamber is receiving material
and causing said vent to close while material is being discharged
from said chamber;
main valve control means actuated by resistance to air flow in said
aeration means resulting from said chamber containing said material
and under such conditions supplying air to said aeration means,
said valve means operating to close said aeration means air supply
when said chamber has discharged said material;
three-way control valve means operatively connected with said air
supply and comprising a control air chamber, said control air
chamber receiving air from said air supply through an adjustable
orifice when said transient air supply pressure is greater than the
pressure in said control chamber and discharging said air through
said adjustable orifice when the air pressure in said control
chamber is greater than said transient air pressure;
said three-way control valve supplying air to said main valve so as
to close said main valve so as to create a material-filling
condition in said chamber means and operating to release air from
said main valve as a consequence of build-up of pressure within
said three-way valve control chamber so as to open said main valve
and thereby create a material-discharge condition in said chamber
means.
2. A pump for fluidized pulverulent material comprising, in
combination:
chamber means for receiving and discharging material;
air pad means in the bottom of said chamber;
material inlet means discharging into the upper part of said
chamber;
check valve means in said inlet means preventing egress of material
from said chamber;
discharge outlet means leading from the vicinity of said air pad
means to exterior of said chamber;
vent cap means communicating with said chamber means;
vent pipe means communicating from said vent cap to outside of said
chamber;
air pressure diaphragm closure means releaseably closing said
communication between said vent cap and said vent pipe means;
air supply means;
relief valve means;
main air valve means comprising a diaphragm means an receiving air
from said air supply means and discharging said air through a
releaseable closure means operatively connected with said diaphragm
means to said relief valve and to said vent communication closure
diaphragm means and to said air pad means;
a three-way control valve means having a bistable toggle action and
supplied with air from said air supply means, in a first position
permitting air to flow to diaphragm means on said main air valve so
as to close said releaseable closure, and in a second position
closing off said air supply but venting said main air valve
diaphragm to atmosphere so as to permit said releaseable closure to
open;
control valve actuating diaphragm means comprising an air control
chamber, spring means, and actuating rod to said bistable toggle
means, so that when said control chamber is pressurized with air,
said control diaphragm is forced against said spring means so as to
move said actuating rod so as to move said toggle action to said
second position, and so that when said control chamber is not
pressurized, said spring means forces said actuating rod so as to
move said toggle means into said first position and to force said
air out of said control chamber; and
adjustable orifice means interposed between said air supply means
and said control chamber, so that the rate of ingress and egress of
air from said control chamber may be regulated.
Description
This invention relates to devices for the pumping of fluidized
pulverulent material, and more particularly to a pump for this
purpose operated entirely by air pressure.
In recent decades, advantage has been taken of the fact that
pulverulent materials generally, such as clays, silica flour,
catalysts in finely divided form, barite, and the like, behave in
many respects like liquids if a mass of the powdered material is
maintained in a so-called aerated or fluidized state, which is
generally accomplished by passing air upwardly through the mass of
material from a plenum below the mass of powdered material. The
material may rest on a porous membrane, which may simply be canvas
or the like, this structure together with means for providing
pressurized air immediately below it often being referred to as an
air pad.
In many fields of application, it is convenient to store powdered
material for use, particularly intermittent use, in a tank from
which it may be pumped from time to time as may be needed to a
point of use. A particular instance is the employment of tanks at
the locale of wells being drilled for oil and gas by the rotary
method, where it becomes necessary from time to time to add
powdered material, such as bentonite, other clays, barite, ground
limestone, and the like to the circulating fluid used in the
drilling. A similar requirement arises in many diverse fields in
connection with the employment of Portland cement, where a supply
is provided in a suitable tank at the point of use.
Various devices have been used and proposed for pumping powdered
materials in the fashion described. One type involves the use of a
chamber which is filled with the fluidized material and then
emptied, this cycle being repeated as long as desired. This is
generally accomplished by a more or less complicated control
mechanism, nearly always operated by electromagnetic devices, in
which the filling of the chamber is sensed by any of several means,
which then operates electromagnetic or electronic controls in such
a fashion as to cycle the apparatus. Such devices require an air
supply and a reliable source of electrical power. Difficulties are
often encountered from relay contacts, solenoid actuators, and the
like failing to operate properly, since a completely dust-free
operation is seldom attainable from the very nature of the
materials pumped.
An object of the present invention is to provide a self-contained
air pump of the type described which is operated solely by air
pressure and which is characterized by high capacity and reliable
operation over long periods of use.
Another object of the invention is to provide a pump of the type
described which even with a high capacity may yet be constructed in
a form light enough to be readily transported from one location to
another, by virtue of the relative mechanical simplicity of the
assembly.
Other objects of the invention will appear as the description
thereof proceeds.
In the drawings:
FIG. 1 is a general view showing the inventive device connected to
a source of material.
FIG. 2 is a top view of the pump.
FIG. 3 is a cross sectional view of the pump, taken as shown by the
arrows on FIG. 2.
FIG. 4 is a fluid circuit diagram of the device, and shows two of
the valve mechanisms in detail, as vertical sections.
Generally speaking, and in accordance with an illustrative
embodiment of my invention, I provide a chamber for receiving and
discharging the pulverulent material, the chamber having an air pad
in the bottom. The chamber has an inlet means for receiving the
powdered material, for example from a supply tank and most
desirably from gravity flow therefrom. This inlet has a check valve
so that the material can flow freely into the chamber, but is
prevented from flowing in the opposite direction, so that egress of
such material from the chamber is prevented thereby through the
inlet. The chamber also has an outlet means communicating from the
vicinity of the air pad means to the exterior of the chamber. I
provide an air supply, which has a number of cooperative functions
in the inventive assembly. Before proceeding with a general
discussion of the inventive device, the drawings will now be
referred to.
In FIG. 1, the pump assembly is shown as 9, a principal feature of
which is the chamber 10, which may conveniently be a generally
cylindrical tank, preferably of aluminum, constructed so as to
withstand a working pressure of the order of 15 to 20 pounds per
square inch, and naturally a test pressure somewhat higher than
this figure. The upper part of the chamber 10 bears a feed inlet
18, shown in FIGS. 1, 2, and 3, which in FIG. 1 is shown in a
typical connection to a supply tank 11 containing a supply of the
powdered material to be pumped, and fluidized in the supply tank 11
by an air pad 13 as a conventional fitting. The feed connection 12
may be a large diameter flexible hose.
The feed inlet 18 bears a check valve 19, which may be of a simple
diaphragm type as shown in FIG. 3. The lower part of the chamber 10
bears an air pad 20, arranged as a false bottom, as shown in FIG.
3, so as to provide an air plenum 21. Passage of powdered material
into the plenum 21 is prevented by the covering 22 of the air pad,
which may be canvas, fiberglass, cloth, or stainless steel filter
cloth, or the like, having sufficient permeability to permit the
passage of air into the chamber proper. A discharge outlet 16 in
the form of a pipe of large diameter in elbow shape as shown in
FIG. 3 is welded to the side of the chamber 10, and communicates
with the chamber in the vicinity of the air pad, as shown.
Exteriorly, the discharge outlet may be connected to a discharge
hose 17, as shown, which is led to the point at which the
discharged material is to be used or otherwise pumped. In the
filling of the chamber with powdered material, as will be described
in more detail below, air is naturally displaced from the chamber,
and an exit for this displaced air is provided by vent pipe 23
which is concentric with vent cap 24. The displaced air from the
top of the chamber passes into vent cap 24 and then downwardly
through vent pipe 23 and out discharge 16, as shown in FIGS. 1 and
4. This air can gain access to vent pipe 23 only when control
chamber 45 is not pressurized, so that flexible diaphragm 25 is not
pressed down against the top of vent pipe 23.
Turning now to FIG. 4, this shows main valve 27 and control valve
28. Each of these valves has essentially two positions, one being
assumed during the chamber filling part of the pumping cycle, and
the other being assumed during the chamber emptying part of the
pumping cycle. FIG. 4 shows these two valves in the chamber
emptying position.
As will be seen from the drawings, the air supply, furnished
through an air hose 15 to main air inlet 29 in the bottom of main
valve 27 furnishes a supply of air under pressure, for which 15
pounds per square inch gauge is suitable and preferred, to several
points in the inventive assembly. With the main valve in open
position as shown in FIG. 4, air is passed to plenum 21 through
supply hose 30. Also, with main valve 27 in the open position, air
pressure is supplied via vent hose 26 to vent cap 24. Thus, the
chamber is pressurized from below, the powdered material therein is
fluidized, and is caused to exit through discharge outlet 16. Check
valve 19 prevents any upward flow of the material through feed
inlet 18. Also, air cannot escape through vent pipe 23 because the
pressure-operated closure in vent cap 24 as already described is
closed.
Referring to control valve 28, which in FIG. 4 is in the discharge
position as already noted, it will be seen that the valve portion
31 thereof is in such a position that air from main inlet 29 and
inlet pipe 32 is blocked, so that air pressure is not supplied via
conduit 33 to diaphragm 34 of main valve 27. Accordingly, this
permits the pressure of the air in 29 to raise control valve 27
into the position shown.
During the discharge portion of the cycle as has been described, it
will be clear that some resistance to flow is furnished by the
material exiting through discharge outlet 16 during the major part
of the discharge portion of the cycle. This flow restriction causes
the pressure in inlet 29 and consequently in control conduit 35 to
be relatively high. This has the effect of admitting air under
substantial pressure through orifice 42 to diaphragm chamber 36 of
control valve 28, thus raising diaphragm 37 upwardly against the
pressure of spring 38, which may be adjusted by screw 39. This
maintains push rod 40 in the elevated position shown in FIG. 4, and
which consequently actuates toggle lever 41 so as to maintain valve
portion 31 in the position shown in FIG. 4.
However, when all of the material in the chamber has been
discharged therefrom by the action described, then the air supplied
to plenum 21 meets little resistance in exiting from the chamber.
This causes a pressure drop at 29, and consequently a pressure drop
in control conduit 35, so that spring 38, being properly adjusted,
forces control diaphragm 37 downwardly and pushes the air in
diaphragm chamber 36 out and eventually into 29. When this happens,
push rod 40 is pushed downwardly by the force of spring 38, so that
toggle lever 41 is moved into the alternate position from that
shown in FIG. 4, which has the effect of admitting air from inlet
pipe 32 to conduit 33, whence it flows into main valve 27, exerting
pressure against diaphragm 34, and closing the main valve. When the
main valve is thus closed, it is clear that control chamber 45 in
vent cap 24 is no longer supplied with air pressure through vent
control line 26, and moreover, air is no longer supplied to plenum
21, the main valve being closed. Accordingly, a fresh supply of
aerated pulverulent material is free to fall downwardly through
check valve 19 and feed inlet 18 into chamber 10. A relief valve 46
prevents any build-up in pressure above the selected operating
pressure, e.g., 15 pounds per square inch. While this filling
action is taking place, however, with main valve 27 closed, full
air pressure is once more supplied to diaphragm chamber 36 through
control conduit 35, restricted, however, by adjustable orifice 42.
This orifice is adjusted so that for the particular powdered
material being supplied to the chamber, by the time the chamber is
approximately full, enough air will have traversed orifice 42 and
entered diaphragm chamber 36 so as once more to overcome the force
of spring 38 and to raise diaphragm 37, thus raising push rod 40
once again into the position shown in FIG. 4. This initiates a new
discharge cycle, which takes place precisely as has been described
before. The cycles of filling and discharging continue
indefinitely, at the will of the operator.
It will be seen, in accordance with the foregoing description, that
as the pumping continues through a full cycle of filling and
discharging, air passes in and out of diaphragm chamber 36, first
in one direction and then in the other, in response to the pressure
differential between chamber 36 and air inlet 29, this differential
being first in one direction and then in the other. However, the
rate of this ebb and flow of air in and out of chamber 36 may be
controlled by adjusting orifice 42, as already noted. Over and
above the regulating action of this orifice, however, the pressure
differential switches over from the discharge part of the cycle to
the filling part of the cycle essentially as a result of the actual
duration of the discharging operation, so that the inventive pump
assembly is remarkably self-automated, particularly considering
that the sole source of energy is air pressure, which serves not
only to effect the pumping action, but to operate the various
controls so as to cycle the device and all in accordance with
ambient conditions. For example, depending upon length of the
discharge hose 17 in a given application, and the density and
fluidized flow properties of the material to be discharged, the
discharge portion of the cycle will vary in duration from one
instance to another. Yet, as will be clear from the foregoing
description, the variance of the duration of the discharge is
automatically taken care of by the pneumatic actions described.
Likewise, as has been explained, the opening and closing of the
vent is automatically controlled by the cycling operation
itself.
The materials of construction call for no special comment, being
conventional in the art. Thus, the housings and operating portions
of the valve mechanisms may be of aluminum or brass, or the like.
The diaphragms may be of synthetic rubber such as neoprene, and the
spring elements of steel, phosphor bronze, or beryllium copper. In
a preferred embodiment, the outside diameter of the cylindrical
chamber 10 is 24 inches, with the dimensions being to scale as
shown in FIGS. 1, 2, and 3.
In practice, the filling cycle is typically from two to three
seconds, while the pumping cycle is from two to three times this
duration, viz., from about four to nine seconds, so that something
of the order of six to eight complete cycles per minute take
place.
I wish it to be understood that I do not desire to be limited to
the exact details of construction shown and described, for obvious
modifications will occur to a person skilled in the art.
* * * * *