U.S. patent number 3,731,876 [Application Number 05/126,179] was granted by the patent office on 1973-05-08 for injection spray systems.
Invention is credited to Merle Robert Showalter.
United States Patent |
3,731,876 |
Showalter |
May 8, 1973 |
INJECTION SPRAY SYSTEMS
Abstract
Injection spray systems and methods are disclosed for spraying
heated and pressurized liquid through a nozzle orifice to produce
very fine spray droplets. The pressurized liquid is heated to a
temperature above ambient temperature whereby the vapor pressure of
the liquid exceeds the pressure outside of the nozzle orifice so
that discharge of the heated and pressurized liquid through the
orifice produces very fine droplets.
Inventors: |
Showalter; Merle Robert
(Baltimore, MD) |
Family
ID: |
22423419 |
Appl.
No.: |
05/126,179 |
Filed: |
March 19, 1971 |
Current U.S.
Class: |
239/13; 239/135;
239/506; 239/533.13; 239/533.2 |
Current CPC
Class: |
B05B
17/04 (20130101); B05B 9/002 (20130101); F23D
11/24 (20130101); B05B 9/005 (20130101); F02M
53/06 (20130101) |
Current International
Class: |
F23D
11/24 (20060101); B05B 17/04 (20060101); F02M
53/06 (20060101); F02M 53/00 (20060101); B05B
9/00 (20060101); B05b 001/24 (); B05b 017/04 () |
Field of
Search: |
;239/13,135,136,5,533,534,506 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: King; Lloyd L.
Claims
What is claimed is:
1. A method of forming liquid droplets and vapor by spraying a
pressurized liquid where substantially all of the mass of the
sprayed liquid is in droplets with a mass mean diameter less than
25 microns comprising the steps of:
pressurizing the liquid,
delivering the pressurized liquid to a nozzle assembly having a
spraying orifice,
heating the liquid without involving chemical changes in said
liquid and prior to discharge through the spray orifice to a
temperature sufficiently above atmospheric temperature so that the
vapor pressure of said liquid exceeds the pressure of the space
into which the orifice sprays, controlling the heating of the
liquid so that said liquid is maintained in liquid state until
discharge through the spray orifice, and
discharging the heated and pressurized liquid through said spray
orifice shaped to produce flow streamlines without substantial
liquid entrainment on the outside surface of the spray orifice to
form spray droplets having a mass mean diameter less than 25
microns.
2. The method as set forth in claim 1 and wherein the vapor
pressure is increased to produce spray droplets having a mass mean
diameter of less than 10 microns.
3. The method as set forth in claim 1 and wherein the vapor
pressure is increased and the entrainment properties of said
orifice surface are reduced to produce spray droplets having a mass
mean diameter of less than 1 micron.
4. A method of forming droplets from a pressurized liquid said
method comprising the steps of:
pressurizing a liquid,
delivering the pressurized liquid to a nozzle assembly having a
variable orifice closed by elastic means and responsive to
pressure,
controlling the pressure of the liquid delivered to the nozzle to
determine orifice size,
heating the liquid prior to introduction into the orifice to a
temperature above the temperature outside the orifice whereby the
vapor pressure of the liquid exceeds the pressure outside the
orifice,
controlling the heating of the liquid so that the vapor pressure of
the liquid is less than the pressure required to overcome the
closing force of the elastic means, thereby insuring that the
liquid is maintained in liquid state until discharge through the
variable orifice, and
discharging the heated and pressurized liquid through the orifice,
said orifice being shaped to produce flow streamlines without
substantial liquid entrainment on the outside surface of the spray
orifice to form spray droplets having a mass mean diameter of less
than 25 microns.
5. A method of forming liquid droplets and vapor by spraying a
pressurized liquid where substantially all of the mass of the
sprayed liquid is in droplets with a mass mean diameter less than
25 microns comprising the steps of:
pressurizing the liquid,
delivering the pressurized liquid to a nozzle assembly having a
variable area spraying orifice,
heating the liquid without involving chemical changes in said
liquid and prior to discharge through the spray orifice to a
temperature sufficiently above the temperature immediately adjacent
the orifice so that the vapor pressure of said liquid exceeds the
pressure of the space into which the orifice sprays, controlling
the heating of the liquid so that said liquid is maintained in
liquid state until discharge through the spray orifice, and
discharging the heated and pressurized liquid through said spray
orifice shaped to produce flow streamlines without substantial
liquid entrainment on the outside surface of the spray orifice to
form spray droplets having a mass mean diameter less than 25
microns.
Description
SUMMARY OF THE INVENTION
The present invention relates to injection spray systems which
produce fine sprays simply and with low energy requirements. The
inexpensive production of very fine sprays is quite important to
air pollution control. In most types of burners fine sprays will
make possible complete combustion, since small fuel droplets
vaporize and mix with air more quickly and completely than large
droplets. Fine sprays also increase the efficiency of stack gas
scrubbers. Spray systems which produce fine droplets are also
important in any application where production of aerosols is
useful, or where intimate mixing of two fluids is required.
Fine spray producing systems have commonly had relatively narrow
spray flow ranges because spray nozzles capable of producing fine
sprays have had single sized orifices. Flow through an orifice of
constant area is proportional to the square root of the pressure
drop across the orifice, so that an X-fold increase in flow rate
requires an X.sup.2 -fold pressure increase. The present invention
discloses injection spray nozzles which have a characteristic
opening pressure Po where the spray orifice is elastically forced
closed below Po and opened proportional to pressure P minus Po,
where P is the pressure of the liquid in the nozzle, so that flow f
equals
F = K (P - Po) .sup.3/2 where P > Po
F = O where P .ltoreq. PoThus variable orifice spray nozzles make
possible injection spray systems with wide flow ranges for
relatively small pressure variations. For instance, with Po = 20
psia, a pressure change from 21 psi to 40 psi produces a 90 fold
flow variation. The exponent 3/2 in the flow equation can be
increased or decreased by using a nonlinear force curve spring.
In the preferred form of the invention, the fluid to be sprayed is
heated to a temperature where the vapor pressure of the fluid
exceeds the pressure in the space into which it is to be sprayed
but is less than the opening pressure Po of the nozzle. When the
liquid leaves the nozzle orifice it boils instantly, making the
effective viscosity and surface tension of the fluid in and past
the spray orifice very small whereby the liquid breaks up into
extremely small drops. Liquids can be broken up into tobacco smoke
sized droplets for high flow rates and low pressures in this way.
The size of the spray droplet distribution depends on the
difference between the pressure in the space into which the nozzle
sprays and the vapor pressure of the liquid at the spray orifice;
the greater the excess of liquid vapor pressure over ambient
pressure, the smaller the droplets. To produce smoke sized sprays
(mass mean droplet diameters of a micron and less) generally
requires that the liquid be heated to its boiling point and then
enough extra heat added to equal 5-10 percent of the heat of
vaporization of the liquid. The amount of heat required to produce
ultrafine sprays varies from liquid to liquid. For years it has
been known that a spray system spraying a liquid with a vapor
pressure insufficient alone to open the spray system but in excess
of the pressure of the space into which the system sprays will
produce fine sprays efficiently. Aerosol cans which spray
deodorant, paint, etc., work on this principle, by boiling freon or
a hydrocarbon which boils below atmospheric temperature and
pressure as it sprays into the atmosphere. However, the use of this
principle for liquids which do not boil at normal atmospheric
temperatures and pressures in new. The use of a controlled heat
input to a pressurized spray system permits the flashing principle
to be used for spraying any liquid. This is a substantial advance
in the art of spray devices, especially for spraying liquids with
low boiling points, or for spraying liquid fuels into combustion
systems.
In all spray nozzles, fluid buildup just outside the spray orifice
will impede spray performance causing nozzle drip and/or large
drops rather than the desired small drops. Heating the sprayed
liquid and the nozzle so that fluid buildup does not occur or
evaporates quickly is one way of eliminating the problem. Making
the nozzle area subject to deposits of a substance with surface
properties which resist wetting by the liquid being sprayed also
reduces the problem. The fluid buildup problem can also be attacked
by producing gas bubbles in the fluid before ejection; these
bubbles pop on fluid ejection, and the gas blows away the fluid
buildup. Bubbles can also greatly reduce mean droplet size under
certain temperature, pressure, and flow conditions. Fluid buildup
can also be reduced by vibrating the nozzle with a mechanical
oscillator arrangement.
In view of the above it is an object of this invention to provide
an injection system and method for spraying liquids from a nozzle
to form small droplets wherein pressurized liquid heated to a
temperature sufficiently high so that the vapor pressure of the
liquid exceeds the pressure outside of the nozzle is forced through
the nozzle to produce small droplets.
It is another object to provide an injection system for spraying
liquids from a nozzle having a variable orifice to form small
droplets wherein pressurized liquid is heated to a temperature
sufficiently above ambient temperatures so that vapor pressure of
the liquid exceeds the ambient pressure so that the heated and
pressurized liquid may be discharged through the variable orifice
which is responsive to the pressure of the liquid in the nozzle to
form small droplets and vapor.
It is yet another object to provide an injection system as in the
foregoing objects and wherein means are provided for controlling
the pressure of the liquid and thus control the opening of the
variable orifice.
It is a still further object to provide an injection system for
producing small droplets wherein a pressurized fluid made up of
liquid with bubbles therein is discharged through a variable
orifice which is responsive to pressure to produce small
droplets.
The above and additional objects and advantages of this invention
will become more apparent when considered in light of the foregoing
detailed description and drawing showing by way of example several
embodiments of this invention.
IN THE DRAWINGS
FIG. 1 is an assembly view of one embodiment of this invention
showing the nozzle assembly in cross section,
FIG. 2 is an assembly view of another embodiment of this invention
wherein a different type of nozzle is employed, and
FIG. 3 is an assembly view of yet another embodiment wherein a
solenoid is used to operate the pintle of the nozzle to control
orifice size.
DETAILED DESCRIPTION
Referring now to the drawings, FIG. 1 is a cross sectional view of
a spray system with a conical spray injection nozzle having a spray
orifice varying with nozzle input pressure, and with means for
heating the liquid in the spray system to a temperature where its
vapor pressure exceeds the pressure of the space into which the
system sprays. Nozzle body 1 contains and seats valve shaped nozzle
pintle 2 which is elastically forced against the open body portion
to close same by means of compression spring 3 which is compressed
between body 1 and pintle 2 by means of clamp washer 4. The
internal clearance between nozzle body 1 and pintle 2 forms fluid
chamber 5 which is fluidly connected to pressurized fluid source 9
through line 8, control valve 7, and line 6. The operation of the
system is as follows: fluid pressure in chamber 5 controlled by
means of valve 7 tends to raise pintle 2 off body 1. Any clearance
between the upper part of body 1 and pintle 2 forms a spray orifice
producing a disc shaped or conical spray pattern. Below a certain
critical pressure Po the compression of spring 3 keeps the nozzle
spray orifice closed and the nozzle produces no spray. As pressure
in chamber 5 rises above pressure Po pintle 2 rises off body 1 and
liquid is discharged therefrom. For linear constant springs a
linear pressure increase of pressure P above Po produces a linear
increase in nozzle spray orifice size, so that liquid flow through
the nozzle obeys the relation f (P - Po) .sup.3/2. The nozzle is
therefore able to spray over a large flow range for a small
pressure range.
The operation of the nozzle in FIG. 1 is sometimes impeded by fluid
buildup on the outside of the nozzle around the spray orifice,
which causes large droplets and nozzle drip. Machining so that
pintle 2 and body 1 fit smoothly around the orifice and are closely
aligned reduces this problem. In FIG. 1, outside nozzle surfaces
around the spray orifice are treated with coating 10, 11, 12 and
13. This coating is of a substance which resists wetting by the
fluid being sprayed (this substance would by hydrophobic for a
nozzle spraying water and hydrophilic for a nozzle spraying oil).
This coating resists the formation of fluid buildup.
The spray system in FIG. 1 has means for heating the liquid to be
sprayed to a temperature where the vapor pressure of the liquid
exceeds the pressure in the space into which the nozzle sprays, so
the liquid boils on ejection from the nozzle, producing extremely
small droplets. Heat is added by heating coils 14, 15 and 16.
Temperature of the liquid is controlled so that the liquid
temperature produces a vapor pressure which exceeds the pressure
into which the system sprays but is less than the nozzle opening
pressure Po. Increasing the tension of spring 3 to increase Po
increases maximum permissable temperatures and vapor pressures.
Heat can be added before the choking valve 7, as by coil 16; after
the valve but before the nozzle, as by coil 15; in the nozzle
itself, as by coil 14, or by some combination of these. A variable
thermo control element 14a may be provided in the heating coil 14
circuit and placed in the chamber 5 to control the temperature of
the liquid therein. Similar control arrangements may be used in
conjunction with heating coils 15 and 16 as required. The heat
addition and control systems can be designed in many ways, but in
any case the temperature of liquid and nozzle must be maintained so
that liquid vapor pressure at the orifice itself exceeds the
pressure into which the system sprays, or the spray will not flash,
boil and break into extremely small droplets. This in practice
often means that the nozzle should be separately heated. Vapor
pressure must be below Po or it will be impossible to turn the
system's flow off quickly. When the vapor pressure of the fluid is
within this proper range small droplets are produced, with mean
droplet size decreasing as the difference between vapor pressure
and space pressure increases, and fluid buildup outside of the
nozzle is minimized or eliminated.
By controlling the temperature and pressure ranges in the system in
FIG. 1 the fluid sprayed through the nozzle can be made to be a
mixture of liquid and gas in the form of tend These bubbles tend to
make the nozzle self cleaning and to produce small droplets.
Heating the fluid in line 16 to a temperature which corresponds to
a vapor pressure somewhat higher than the pressure in line 6 and
chamber 5 will cause many bubbles to be produced as the hot liquid
passes from valve 7, and bubbles will form until equilibrium
between pressure and vapor pressure is again established in line 6
and chamber 5. Various other means of generating bubbles are well
known to the fluidic arts and can be added to the structure of FIG.
1.
Various modifications of the structure in FIG. 1 suggest
themselves. Other structures for controlling input pressure to the
nozzle can obviously be substituted for system 6, 7, 8, and 9.
Compression spring 3 can easily be changed for a coil spring, the
shape of nozzle body 1 and pintle 2 can be modified, and various
methods of alignment of 1 and 2 can be substituted for the
alignment arrangement of FIG. 1. Effective spray nozzles need not
be radially symmetric and may spring from various shaped holes. The
heating systems of FIG. 1 can also be changed: the lines, valve, or
nozzle could be insulated to reduce heat losses to the outside, and
the electrical heating means of FIG. 1 could be replaced or
supplemented by other heating means (for instance heat pipes).
Various methods of thermostatic control for the system are well
known to the art of temperature control systems.
FIG. 2 shows a spray system with means for heating the liquid in
the spray system to a temperature above atmospheric temperature
where its vapor pressure exceeds the pressure of the space into
which bubbles. system sprays which does not necessarily include a
variable orifice nozzle. Liquid pressure source 17 is connected by
line 18 through valve 19 to line 20 and nozzle 24. The liquid in
the spray system is heated by means of heating coil 21 around or in
line 18 and/or by heating coil 22 around line 20, and/or by heating
coil 23 around nozzle 24. Nozzle 24 may be a fixed orifice or may
utilize the same principles as the nozzle in FIG. 1 if the nozzle
is made of an elastic material so that the spray orifice is closed
below a certain pressure and opens with increasing pressure.
Obviously, different nozzle types and methods of introducing heat
can be substituted for nozzle 24 and heat coils 21, 22, and 23, as
is the case in FIG. 1.
FIG. 3 shows a spray system where liquid vapor pressure is greater
than the pressure of the space into which the system sprays and
where flow may be controlled directly at the nozzle spray orifice.
Pintle 25 rests in nozzle body 26, the clearance between pintle and
body forms a liquid chamber 29 which is heated by heating coil 27
and/or by heating coil 30 whereby the liquid temperature is high
enough so that vapor pressure of the liquid is greater than the
pressure of the space into which the nozzle sprays. Pintle 25 is
held closed by the elastic tension of spring 31 and is mechanically
connected to magnet 32 which is surrounded by magnetic coil 33 to
form a solenoid assembly. Energization of coil 33 causes pintle 25
to rise and open the nozzle, this control of the current in coil 33
will control movement of the pintle and the spray volume controlled
thereby, or if fluid pressure itself opens the nozzle, current
oscillations in coil 33 can oscillate pintle 25 and disturb the
spray flow streamlines, producing smaller droplets. The spray flow
can be pulsed at various frequencies depending upon the pulsed
energy supplied to coil 33 or can be made continuous as desired.
Such pulsing can be employed to rapidly reciprocate the pintle 25
to vibrate the nozzle. If flow is pulsed, flow volume can be
controlled by varying pulse duration, frequency, or amplitude. The
opening and closing of the nozzle spray orifice can be controlled
mechanically as well as electrically. Various means of
accomplishing this are familiar to the fluidic arts, for instance
in the art of fuel injection systems for engines.
In the detailed description of the invention and the claims the
term "liquid" covers any combination of solids, liquids and gases
which will act as a liquid such as stable slurries, gels, and
colloids. The term "liquid" does not apply to the state of a
substance above the critical point on a pressure-temperature three
phase diagram.
The terms "atmospheric temperature" and "atmospheric pressure"
refer to standard temperature and pressure (0.degree. Centigrade
and 760 mm. Hg.).
The term "entrainment" with respect to the spray orifice nozzle
refers to the formation of liquid deposits adjacent or on the
nozzle, which is the amount of washing.
The term "mass mean diameter" refers to the diameter of droplets in
a spray distribution where the mass of liquid in droplets smaller
than this diameter equals the mass of liquid in droplets larger
than this diameter.
The term "stable aerosol droplets" refers to droplets so small that
the aerodynamic drag of the droplets is so small that gravitational
or ballistic settling is practically insignificant.
* * * * *