U.S. patent number 3,658,289 [Application Number 04/887,268] was granted by the patent office on 1972-04-25 for control of fluid dynamics in spiraling gas streams.
This patent grant is currently assigned to Cities Service Company. Invention is credited to Richard L. Hodges.
United States Patent |
3,658,289 |
Hodges |
April 25, 1972 |
CONTROL OF FLUID DYNAMICS IN SPIRALING GAS STREAMS
Abstract
Spin rate and volume flow rate of spiraling gas streams are
regulated to control the fluid dynamics thereof. At constant supply
pressure, either the spin rate or the volume flow rate of the
spiraling stream can be changed without altering the other rate.
Should the supply pressure change, both rates can be maintained
constant. In addition, the spin rate can be increased even if the
static pressure is lowered and can on the other hand be decreased
if the static pressure is raised. These effects are accomplished by
regulating the spin rate and the volume flow rate of a spiraling
gas stream independently of one another.
Inventors: |
Hodges; Richard L. (Seagraves,
TX) |
Assignee: |
Cities Service Company (New
York, NY)
|
Family
ID: |
25390795 |
Appl.
No.: |
04/887,268 |
Filed: |
December 22, 1969 |
Current U.S.
Class: |
251/118; 55/447;
137/613; 251/212; 431/182; 55/418; 239/407; 422/224 |
Current CPC
Class: |
F16K
49/00 (20130101); F16K 3/34 (20130101); F23C
7/008 (20130101); Y10T 137/87917 (20150401) |
Current International
Class: |
F23C
7/00 (20060101); F16K 3/34 (20060101); F16K
3/00 (20060101); F16K 49/00 (20060101); F16k
047/00 (); F16k 003/00 () |
Field of
Search: |
;210/512
;251/118,212,205 ;137/613,614.16 ;55/238,418,419 ;261/79
;239/407,413,416.5 ;23/209.4,209.6,259.5,277 ;431/182,183,184 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Klinksiek; Henry T.
Claims
Therefore, what is claimed is:
1. Apparatus for regulating the fluid dynamic characteristics of a
spiraling gas stream comprising:
a. a barrel wherein a gas stream flows as a spiraling stream,
b. a flow control valve through which said gas stream is supplied
to said barrel, said valve having:
1. a casing, at least a portion of the casing being in a plane
substantially tangent to the barrel,
2. a first gate seated within said casing and guidedly positionable
therein transversally with respect to normal flow of gas through
the valve and also transversally with respect to a plane through
the longitudinal axis of said barrel to the gate, the gate abutting
said portion of the casing when the gate is closed,
3. a second gate seated within said casing and guidedly
positionable therein transversally with respect to normal flow of
gas through the valve and parallel with respect to the longitudinal
axis of the barrel so that each of the gates is movable
transversally to the movement of the other,
4. a gas passageway which is established in said valve when both of
said gates are partially open and from which said gas stream is
directed tangentially into said barrel at controlled
cross-sectional width and length dependent upon the relative
position of said gates to one another,
5. means connected to the gates for positioning each gate within
said casing and for retaining the gates in location after the
positioning thereof.
2. The apparatus of claim 1 wherein the width of said passageway is
dependent upon the position of said first gate in said casing and
the length of said passageway is dependent upon the position of
said second gate in said casing.
3. The apparatus of claim 1 wherein said barrel is the mixing
barrel of a burner into which air is fed through said valve, and
further comprising means for supplying a fluid fuel to the air
which flows through said barrel, and means at the discharge end of
said barrel for burning the resulting mixture of air and fuel.
Description
BACKGROUND OF THE INVENTION
A flowing stream of gas can be formed into a spiraling stream in
order to better utilize the kinetic energy of the stream. For
instance, the turbulence and shearing actions which occur within
spiraling gas streams enhances mixing and reaction with another
fluid, e.g. the mixing of air and a fluid fuel in a combustion
process. In other cases, the momentum of the gaseous spiral is
imparted to still another material for the processing thereof, e.g.
centrifugal separation of entrained solids or liquids, or fluid
energy grinding of entrained solids. Also, the momentum of a
spiraling gas stream can be transferred to an even larger body of
gas for imparting a spiraling or swirling motion thereto, e.g. a
process as described in U.S. Pat. No. 3,301,639.
Heretofore, the average spiraling velocity (spin rate) and volume
flow rate of spiraling gas streams have been interdependent since
it has not been readily possible to alter one without directly
affecting the other. Thus, at constant supply pressure, the volume
flow rate of a gas spiral could not be lowered without lowering the
spin rate. On the otherhand, if supply pressure changed, the volume
flow rate and the spin rate could not be maintained at
preestablished conditions. Furthermore, the spin rate could not be
increased when the supply pressure was reduced, and the spin rate
could not be reduced when the supply pressure was increased. As a
consequence, the kinetic energy potential of a spiraling gas stream
could not be developed and utilized to the desired extent in many
cases.
SUMMARY OF THE PRESENT INVENTION
It is therefore an object of the present invention to control the
spin rate and the volume flow rate of a spiraling gas stream
independently of one another.
It is another object of the present invention to provide control
over the fluid dynamic conditions of a spiraling gas stream.
In accordance with the present invention independent means are
therefore provided for regulating both the spin rate and the volume
flow rate of a spiraling gas stream. The spiraling gas stream can
be produced by introducing the gas tangentially into a cylindrical
chamber or barrel. The barrel can, for instance, have an elongated
circumferential wall with a closure at one end and a discharge
outlet at the other end, and it can be provided with a gas inlet
located at a distance far enough upstream of the outlet to permit
adequate formation of the spiraling stream as the gas traverses the
length of the barrel. The gas which is shaped into a spiral can
then be fed into the barrel by means of a gas supply conduit which
communicates with the aforesaid inlet.
For controlling the spin rate and the volume flow rate of spiraling
gas stream, a dual gated valve can be placed in the gas supply
conduit and located proximal to the gas inlet of the aforesaid
barrel. Both of the valve gates should be movable in crosswise
relation to each other and in a direction which is transverse in
relation to the normal direction of gas-flow through the valve.
More particularly, one gate can be movable at angle which is about
90.degree. in relation to the direction in which the other gate is
moved. When constructed in such a fashion, the valve can be
arranged in the gas supply conduit so that one gate moves
transversally and the other axially in relation to the longitudinal
axis of the barrel.
When using the above-identified arrangement, the transversally
movable gate of the valve can be positioned so that the gas inlet
is partially obstructed, thus forcing the gas stream to enter
predominately to one side of the barrel, i.e. tangentially, and
form a spiral therein. At the same time the axially movable gate is
positioned to establish a passageway in the valve of sufficient
open area to permit a desired volume flow rate at the existing
supply pressure. At any given supply pressure, the axially movable
valve gate can be repositioned to alter the volume flow rate of gas
in the spiraling stream without materially affecting the spin rate.
On the otherhand, the transversally movable gate may be
repositioned to alter the spin rate, i.e. the smaller the opening
created by closure of the gate the faster the spin, and vice versa.
At constant pressure this also has the effect of lowering volume
flow rate, but this can be compensated for by further opening of
the axially movable gate, thus increasing the total open area of
the passageway through the valve. It will nonetheless be
appreciated that this repositioning of the axially movable gate
primarily alters the volume flow rate of the spiral and does not
materially effect the spin rate thereof.
It will be understood that the control means just described can
also be employed to maintain a desired volume flow rate or spin
rate by repositioning of the valve gates upon change in the supply
pressure. Thus, at a given setting of the two gates the desired
spin rate can be maintained by opening or closing the first gate as
the pressure decreases or increases, respectively. In the same
fashion, the desired volume flow rate can be maintained by opening
or closing the second gate as the supply pressure decreases or
increases, respectively.
As previously indicated, the present invention can also be utilized
for increasing the spin rate of a spiraling stream even when the
stream supply pressure is lowered; or, on the other hand, to
decrease the spiraling rate when the supply pressure is raised. To
increase spin rate after reduction in the supply pressure, the
transversally movable valve gate is closed further than before, and
the axially movable gate can be repositioned to establish a desired
volume flow rate. A reverse procedure is employed for reducing the
spin rate when the supply pressure increases, i.e. the
transversally movable valve gate is opened further than before and
the axially movable gate can be repositioned to establish a desired
volume flow rate.
Each component of the previously described control system should be
sized large enough, of course, to permit accomplishment of desired
spin velocities and flow rates at the available gas stream supply
pressures.
BRIEF DESCRIPTION OF THE DRAWINGS
FIG. 1 is an illustration, mostly in section, of one form of
apparatus, which can be employed in the practice of the
invention.
FIG. 2 is a sectional view along the lines 2--2 of FIG. 1.
FIG. 3 is a sectional view along the lines 3--3 of FIG. 1.
DESCRIPTION OF PREFERRED EMBODIMENT
The present invention will be described with particular reference
to a spiral mixer-burner which can be employed in the formation and
ignition of combustion mixtures, but it will be understood that the
invention can be employed for controlling the dynamic
characteristics of any spiraling gas stream.
FIG. 1 depicts a cylindrical mixing barrel assembly having an
elongated circumferential wall with a closure plate 2 at one end, a
discharge outlet 3 at the other end, and a gas inlet 4
substantially upstream of the discharge outlet. The end closure
plate 4 is affixed to the barrel by means of a flange 5 and
fasteners 6.
For feeding a gaseous component of a fuel mixture into the barrel,
a gas supply conduit 7 intercommunicates with the inlet 4 through a
valve, generally represented at 8. For supplying a second gaseous
or liquid component of the combustion mixture, a conduit 9 passes
through a guide 10 affixed to plate 2 and extends axially into the
barrel. The conduit 9 can be provided with an atomizing nozzle or
gas distributor 11 at the tip end thereof.
In the illustrated case, the mixer barrel assembly is shown
attached to a burner block 12 which is constructed of a
high-temperature refractory and wherein ignition of the combustible
mixture can be initiated. The burner block can, of course, be
located in the wall of a furnace chamber wherein ignition of the
mixture can be either initiated or carried forward thereafter.
Alternately, the circumferential wall 1 of the barrel can be
constructed of a refractory material when it is desirable to
initiate and carry on combustion therein.
The valve, generally represented at 8, is provided with a first
gate 13 which is movable transversally with respect to the
longitudinal axis 14 of the barrel, and a second gate 15 which is
movable axially with respect to the axis. Other components of the
valve are end plates 16a and 16b, whereby the valve assembly is
attached to the gas supply conduit 7 and the gas inlet 4,
respectively; sealing gaskets 17a, 17b, and 17c; and spacers 18a
and 18b, whereby the valve is made gastight while providing means
for guided movement of the gates. The valve assembly is held
together by means of fasteners 19. Thus, the aforementioned end
plates, gaskets and spacers of the valve form a casing when all are
securely fastened together, the purpose of the casing being to
retain the gas within the system while holding the gates in place.
Accordingly, the gaskets and spacers bound channels, or seats, for
guiding movement of the gates within the casing while also forming
a relatively tight seal with the edges of the gates. In the
illustrated case the gates are rectangular plates, but it will be
understood that even other shapes can be adapted to the purpose,
e.g. circular discs.
The transversally movable gate 13 can be positioned and retained in
location by means of a threaded screw 20 in a threaded member 21,
the latter of which is affixed to the plate 13. The outer end of
the screw 19 is provided with a crank 22. The screw 19 is stablized
with a mounted bearing affixed to a support plate 24. The axially
movable gate 15 is equipped with equivalent positioning means,
generally represented at 25.
As can be seen from the drawings, and especially FIG. 3, the valve
gates 13 and 15 are arranged to move transversally with respect to
normal flow of a fluid through the valve while also being arranged
to move crosswise in relation to each other. Arranged thus, a fluid
passageway 26 in the valve is established by opening and/or closing
the gates, and the open area and configuration of the passageway is
thus dependent upon positioning of the gates in relation to one
another. With respect to the longitudinal axis 14 of the barrel,
gate 13 thus controls the width of the inlet 4, while gate 15
controls the length thereof.
It will be appreciated that closing of the gate 13 so that it
extends inwardly beyond the longitudinal axis of the barrel creates
a passageway 26 which provides tangential injection of gas into the
barrel. The further gate 13 is closed, the faster will be the
spiraling velocity, at any given volume flow rate, of the gaseous
spiral within the barrel. As previously pointed out, closure of
gate 13 also has the effect of reducing volume flow, but this can
be reestablished by opening ate 15. Thus, both the volume flow rate
and the velocity of the gas which passes through the valve can be
finely controlled by means of the dual gates. Advantageously, the
gates can be arranged, as illustrated, to cross at about a right
angle, but it will be appreciated that equivalent effects can be
obtained with other angles.
The spiraling gas stream that is produced in the mixing barrel has
been generally depicted at 27 in the drawings. Upon discharge from
the end of the barrel, or the burner block 12, the gas stream will
have a predominate momental direction which is to one side of the
axis of the barrel, and can thus be employed as described in U.S.
Pat. No. 3,301,639 for imparting a spiral to the gaseous contents
of a furnace. It will also be appreciated that the conduit 9 can be
positioned axially within the barrel so as to effect mixing of the
second fluid component with spiraling gas stream, either within the
barrel, beyond it, or at the discharge outlet thereof.
In operation at fixed gas supply pressure, the movable gate 13 is
positioned to lend a width to the passageway 26 which will impart a
desired spiraling velocity to the gas stream which enters the
barrel through the inlet 4. Narrowing the width of the passageway
forces the gas stream to flow in a more proximal relationship with
the circumferential wall 1, thus increasing the average rotational
velocity of the stream. As the width of the passageway is increased
by opening gate 13, the average rotational velocity of the gas
stream is reduced since it is permitted to occupy a larger part of
the cross-sectional area of the barrel. The spiraling stream can
thus be visualized as an annulus, the "eye" of which is increased
and decreased in size by transversal movement of the first
gate.
Volume flow to the spiraling stream is regulated by axial movement
of gate 15 which controls the length of passageway 26. Once the
desired rotational velocity of the stream has been established by
positioning the transversally movable gate, the axially movable
gate is positioned to effect the desired volume flow rate. Should
the gas pressure change in conduit 7, the gates can be repositioned
to maintain the desired spin and volume flow rates.
The present invention can also be employed to either increase the
spin rate of the spiraling stream upon reduction in the gas supply
pressure, or to reduce the spin rate when the pressure is
increased, by positioning of gate 13 to control the spin rate.
Advantageous use of the present invention mixing process will be
further described. Air, at a relatively constant pressure, can be
supplied to the barrel assembly by means of a blower or compressor.
Either a gaseous or a liquid fuel can be supplied through conduit
9. The atomizing nozzle or gas distributor can be positioned within
the barrel to effect mixing therein followed by initiation of
combustion in the burner block 12. When it becomes desirable to
reduce the input of air, i.e. to turn down the burner, the mixing
pattern can become considerably altered unless the spin velocity is
maintained or even increased. By means of the present invention,
the mixing pattern can thus be finely regulated by maintaining or
increasing spin rate at reduced volume flow rate or supply
pressure. Furthermore, the momentum of the spiraling stream, as is
valuable for instance in imparting a spiraling or motion to an even
larger body of gas, can be more closely controlled. Conversally,
spin rate and momentum of the spiraling stream can be reduced when
desired by means of the gate 13, since the spiral formation will
gradual diminish as this gate is progressively opened; and can, in
fact, be entirely eliminated if opened substantially beyond the
longitudinal axis of the barrel.
While the invention has been described with reference to particular
materials, apparatus and process conditions, it will be understood
that still others may be employed without departing from the spirit
or scope of the invention as expressed in the appended claims.
* * * * *