U.S. patent number 3,760,598 [Application Number 05/168,440] was granted by the patent office on 1973-09-25 for process for making artificial snow.
This patent grant is currently assigned to Linde Aktiengesellschaft. Invention is credited to Fritz Jakob, Karl-Heinz Kuhnlenz, Gerold Tesar.
United States Patent |
3,760,598 |
Jakob , et al. |
September 25, 1973 |
PROCESS FOR MAKING ARTIFICIAL SNOW
Abstract
Water under high pressure and at a low temperature is fed to a
set of nozzles, after it has been mixed with a high-pressure air
flow. On leaving the nozzles the water is atomized into fine
droplets and is rapidly depressurized on being discharged into a
low-pressure air stream of subfreezing temperature generated by a
fan. The weight ratio of high-pressure air and water, ahead of the
nozzle orifices, is on the order of 1 : 400.
Inventors: |
Jakob; Fritz (Wolfratshausen,
DT), Tesar; Gerold (Pullach/Isarital, DT),
Kuhnlenz; Karl-Heinz (Eurasburg, DT) |
Assignee: |
Linde Aktiengesellschaft
(Wiesbaden, DT)
|
Family
ID: |
3550809 |
Appl.
No.: |
05/168,440 |
Filed: |
August 2, 1971 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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810711 |
Mar 26, 1969 |
3596476 |
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Foreign Application Priority Data
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Apr 8, 1968 [OE] |
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A 3459/68 |
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Current U.S.
Class: |
62/74; 239/2.2;
239/14.2 |
Current CPC
Class: |
F25C
3/04 (20130101); F25C 2303/0481 (20130101); F25C
2303/046 (20130101) |
Current International
Class: |
F25C
3/04 (20060101); F25C 3/00 (20060101); F25c
003/04 () |
Field of
Search: |
;62/74,121,347
;239/2,424.5 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Wayner; William E.
Parent Case Text
This application is a continuation-in-part of our copending
application Ser. No. 810,711 filed Mar. 26, 1969, now U.S. Pat. No.
3,596,476.
Claims
We claim:
1. A process for making artificial snow, comprising the steps of
feeding a continuous flow of water under high pressure and at a low
temperature to at least one orifice, continuously admixing with
said flow of water a stream of compressed air at a rate amounting
to a minor proportion by weight of said air with reference to the
water and discharging the resulting water/air mixture from said
orifice in the form of small droplets into a low-pressure air
stream of subfreezing temperature generated by a fan and flowing
past an edge of a generally transverse land bearing said orifice,
the proportion of high-pressure air to water ahead of said orifice
ranging substantially between 1 and 4 m.sup.3 STP of air per
m.sup.3 of water.
2. A process as defined in claim 1 wherein said compressed air is
fed into a conduit conveying said flow of water to said
orifice.
3. A process as defined in claim 1 wherein the water has a
nucleating agent admixed therewith.
4. A process as defined in claim 3 wherein said nucleating agent is
silver iodide.
5. A process as defined in claim 4 wherein the concentration of
said silver iodide is on the order of 10.sup.-.sup.4 N.
6. A process as defined in claim 1 wherein the proportion of air to
water ahead of said orifice is substantially 3 m.sup.3 STP of air
per m.sup.3 of water.
7. A process as defined in claim 1 wherein said orifice has a
diameter between substantially 0.5 and 2.5 mm, the pressure of the
water at said orifice being upward of substantially 5 atmospheres
absolute.
8. A process as defined in claim 1 wherein a surfactant is admixed
with the water ahead of said orifice.
9. A process as defined in claim 1 wherein said land is annular and
said low-pressure air stream is blown along the axis of said land
past the inner peripheral edge thereof.
10. A process for making artificial snow, comprising the steps of
feeding a continuous flow of water under high pressure and at a low
temperature to at least one orifice, continuously admixing with
said flow of water a stream of compressed air at a rate amounting
to a minor proportion by weight of said air with reference to the
water, and discharging the resulting water/air mixture from said
orifice in the form of small droplets into a low-pressure air
stream of subfreezing temperature generated by a fan, the quotient
W.sub.o c.sub.o /W.sub.w (Wo = mass-flow rate of low-pressure air,
Ww = mass-flow rate of water, given in kg/h, and C.sub.o = flow
velocity of low-pressure air given in m/sec) lying between 56 and
670.
11. A process for making artifical snow, comprising the steps of
feeding a continuous flow of water under high pressure and at a low
temperature to at least one orifice, continuously admixing with
said flow of water a stream of compressed air at a rate amounting
to a minor proportion by weight of said air with reference to the
water, further admixing with said water a surfactant ahead of said
orifice, and discharging the resulting water/air mixture from said
orifice in the form of small droplets into a low-pressure air
stream of subfreezing temperature, the proportion of high-pressure
air to water ahead of said orifice ranging substantially between 1
and 4 m.sup.3 STP of air per m.sup.3 of water.
Description
Our present invention relates to a process for making artificial
snow.
In conventional systems of this type, large quantities of
compressed air are admixed with relatively small amounts of
entrained water which, upon subsequent expansion of the mixture
into an atmosphere of sufficiently low temperature and high
humidity, crystallizes as snow flakes. The successful operation of
a snow machine based on this principle is generally possible only
at ambient temperatures well below freezing, e.g., less than -5
.degree.C, and requires an air compressor of large capacity to
deliver a constant flow of compressed air at the rate heretofore
considered necessary.
The general object of our present invention is to provide an
improved method of operating a snow machine, based upon a novel
process of making artificial snow, which avoids the above drawbacks
and which is effective at ambient temperatures just below the
freezing mark while being substantially insensitive to veriations
in relative humidity.
We have found in accordance with the present invention that the
aforestated object can be realized by allowing a continuous flow of
water under high pressure to issue from one or more expansion
orifices in the form of small droplets into a low-pressure air
stream of subfreezing temperature, i.e., a temperature up to about
0 .degree.C. The temperature of the water should be as close to 0
.degree.C as possible to provide a satisfactory operation, but we
have found that the temperature of the water may be several degrees
above 0 .degree.C if the temperature of the surrounding air is low.
As a rule of thumb it can be stated that the temperature of the
water may be approximately as many degrees above 0 .degree.C as the
temperature of the air is below 0 .degree.C.
We have further found, in accordance with the present invention,
that the aforestated object can be realized more efficiently by
adding a high-pressure gas, such as air, to the water before its
discharge from the expansion orifices. While the air which is
contained in the water in tiny bubbles before reaching the
expansion orifices does not play a part in atomizing the water, it
expands suddenly after having left the orifices, thus lowering its
temperature down to -70 .degree. or -80 .degree.C. This lowering of
the temperature leads to a quick formation of ice crystals in the
boundary layers between the bubbles of expanded air and the
surrounding small droplets of water, thereby generating nuclei for
the promotion of the transformation of water into snow. The
high-pressure air is preferably under a pressure slightly higher
than that of the water flow to which it is added, in a proportion
ranging between substantially 1 and 4 m.sup.3 STP per m.sup.3 of
water. A particularly advantageous ratio is 3 m.sup.3 STP of air
for each cubic meter of water.
Another adjuvant capable of promoting the snow formation is a
nucleating agent admixed with the air-permeated water flow in
finely comminuted crystalline form. While ice could be used for
this purpose if injected into the flow at a location close to the
discharge orifices, other compounds of similar crystalline
structure (such as silver iodide) are more stable so as to be
admixable with the water ahead of the high-pressure pump. The
quantity of such nucleating agent should substantially exceed the
saturation rate of the water and, in the case of silver iodide, is
advantageously on the order of the equivalent of 10.sup.-.sup.4
N.
Alternatively, or in addition, a surfactant in powered or liquid
form may be added to the water to reduce its surface tension,
thereby facilitating its dispersion into fine droplets. Any
commercially available household detergent may be used for this
purpose. In the case of a powder, such as an alkylaryl sulfonate, a
quantity of about 10 - 15 grams per m.sup.3 of water has been found
highly satisfactory; in the case of liquid detergents, such as an
ester of polyethylene glycol, a proportion of roughly 100 ml per
m.sup.3 of water is suitable.
The above and other features of our invention will become more
fully apparent hereinafter from the following detailed description
given with reference to the accompanying drawing in which:
FIG. 1 illustrates, somewhat diagrammatically and in axial
sectional view, the basic structure of a snow machine operable by
the process according to our invention;
FIG. 2 is a side-elevational view, partly in section and on an
enlarged scale, of a nozzle forming part of the machine of FIG.
1;
FIG. 3 is a graph illustrating the dependence of the quantitative
ratio of high-pressure air and water upon the amount of water fed
to the snow machine in the process according to the invention;
and
FIG. 4 is a graph illustrating the decrease of the amount of
high-pressure air needed in comparison with high-pressure water
with decreasing temperatures in the process according to the
invention.
In FIG. 1 we have shown a tubular nozzle carrier 35 of cylindrical
configuration whose inner bore 37 accommodates an electric fan 36
driven by a motor 41. Fan 36 generates a circulation of air passing
axially through the front end 38 of body 35 which carries an
annular array of nozzles 1 with discharge orifices 7 pointing in
the direction of the air flow; the air velocity may range between
about 20 and 50 m/sec, being preferably 33 m/sec. The nozzles 1 are
connected in parallel, via internal conduits 42, to a manifold 40
in the form of an annular channel to which water is continually
supplied under high pressure by a pump 43, followed by a cooler 44,
via a pipe 48.
Conduits 42, which represent the inlets to the nozzles 1, also
communicate via passages 45 with another manifold 39 which is
connected to the output end of an air compressor 46 by way of a
pipe 49, the output pressure of blower 46 being slightly higher
than the delivery pressure of pump 43.
The restricted passages 45 exert a throttling effect upon the air
flow entering the nozzles 1 from annular channel 39. This
throttling effect is desirable to insure a substantially uniform
rate of air flow at each nozzle, despite the fact that the several
passages 45 are at different distances from the supply line 49.
A similar but less pronounced throttling action is exerted upon the
water flow by the passages 42 linking the nozzles 1 with the
annular channel 40.
The circulation of air generated by fan 36 creates a suction effect
on the surrounding atmospheric air due to friction in the boundary
layers between the stream generated by the fan and the surrounding
air. As a result, atmospheric air is sucked into the stream which
helps spread the water/air mixture from the nozzle 1 over the
transverse land 35' of the carrier 35 along the axis of the land
past the inner peripheral edge thereof. Moreover, it promotes a
quick evaporation of water from the surfaces of the small droplets
whereby an intense cooling of the droplets is achieved, thereby
transforming them into snow, without requiring additional cooling
of the system. The maximum initial diameter of these droplets,
under the operating conditions specified above, is on the order of
0.1 mm. The desired ratio of water to air, within the range
previously set forth, can be varied by adjusting the relative
speeds of pump 43 and blower 46.
FIG. 2 shows a preferred construction of any of the nozzles 1
illustrated schematically in FIG. 1. The nozzle 1 of FIG. 2 has a
tubular housing 11 terminating at its front end in the orifice 7,
housing 11 being formed with internal threads 47 engaged by mating
threads on a tubular insert 15 and on a locking ring 17. Insert 15
defines with the inner front wall of housing 11 a vortex chamber 16
into which water, with the admixed air, flows by way of lateral
apertures 19 in insert 15 after entering same from the rear through
ring 17. The apertures 19 (only one shown) are centered on
generally tangentially inclined axes, as is well known per se, so
as to impart to the exiting fluid a swirling motion in its travel
toward orifice 7. Male threads 13 on the rear of housing 11 enable
the nozzle 1 to be screwed into a threaded seat in the carrier 35
of FIG. 1 or in the outer surface of an annular carrier member
supplied from within and discharging into a surrounding
low-pressure air stream as described more fully in our copending
application and patent identified above; the midportion 14 of the
nozzle housing is formed for this purpose into a polygonal flange
engageable by a wrench.
In the operation of the illustrated machine, the discharged
droplets of water, especially if charged with a nucleating agent
and/or a surfactant as described above, crystallize upon contact
with the atmosphere so as to turn into snow flakes.
If the volumetric ratio of high-pressure air to water has a value
corresponding to the lower limit of the range given above, i.e., 1
: 1, the weight ratio can be calculated as 1 : 775; at the top of
the range, with a volumetric ratio of 4 : 1, the weight ratio
becomes 1 : 194. Thus, the quotient
R = W.sub.w /W.sub.a
is on the order of 400 (this value equaling approximately the
geometric mean of the upper and lower range limits), W.sub.w being
the weight of the water and W.sub.a being the weight of the
high-pressure air ahead of expansion point 7.
FIG. 3 shows the effect of the amount of water delivered by pump 43
to nozzles 1 upon the proportion of water to high-pressure air
ahead of the nozzles 1. As can be seen, the proportion is the
higher the more water is delivered to the nozzles. It should be
remarked that the quality of the snow produced increases with a
decrease in the proportion of water to high-pressure air.
The graph shown in FIG. 3 was taken from measurements with a
snow-making machine having 180 nozzles, each having a diameter of
approximately 1 mm. The pressure of the water amounted to 14
atm.abs. while the pressure of the high-pressure air amounted to 15
atm.abs. The temperature of the water was +2 .degree.C, and the
temperature of the surrounding air was -2 .degree.C. The speed of
the low-pressure air stream generated by the fan 36 amounted to 33
m/sec.
FIG. 4 shows the effect of the variation of ambient temperature
upon the proportion of water to high-pressure air. As can be seen,
the proportion becomes the greater the lower the temperature of the
ambient atmosphere.
This graph was also taken with a snow-making machine having 180
nozzles each having a diameter of approximately 1 mm. Water was fed
to the nozzles in an amount of 150 liters/min which corresponds to
an amount of 9 m.sup.3 /h. The temperature of the water fed to the
nozzles was varied within a small range according to the
temperature of the ambient air. It was possible to produce snow of
satisfactory quality with water temperatures up to 10 .degree.C if
the temperature of the ambient air was -10 .degree.C or lower.
The mass-flow rate W.sub.o of the available low-pressure air and
its flow velocity c.sub.o also affect the conversion rate. Thus,
the quotient
A = W.sub.o c.sub.o /W.sub.w
should range, with W.sub.o and W.sub.w given in comparable units
such as kg/h, between 6.6 and 1,300 (m/sec) if c.sub.o is given in
m/sec. The preferred range is 56 to 670; in the tests represented
by FIG. 3 the value of A approximated 160.
* * * * *