TECHNICAL FIELD
[0001] The proposed group of inventions relates to the field of water spraying and firefighting
and may be used for automatic and manual extinguishing of fires, in stationary and
mobile firefighting appliances.
PRIOR ART
[0002] A method is known from the prior art for producing water vapour by forced ejection
of water at a pressure of 140-200 atm through spray heads [
US5944113, IPC A62C31/05, A62C37/11, A62C37/14, B05B1/14, publ. 31.08.1999]. To provide the
possibility of spraying mist with fine droplets in known nozzles of spray heads, through-holes
are made, in which various mechanical obstacles are fitted. These mechanical obstacles
may be, for example, a rotating component, a fixed blocking element of a particular
shape, a helicoidal spring, etc.
[0003] A significant drawback when using such obstacles is that they reduce the efficiency
of the spray head. This means that to obtain spraying of the required type it is necessary
to provide considerable working power. Moreover, the presence of obstacles in the
nozzles has the effect that the designs of the nozzles and spray heads become quite
complex. Such nozzles are difficult to manufacture, and they must be enclosed in special
nozzle housings, mounted in the body of the spray head. The result is an increase
in the cost of manufacture of the spray head.
[0004] Another patent [
US5881958, IPC A62C31/02, B05B1/02, B05B1/04, publ. 16.03.1999] describes a nozzle for delivering
a mixture of finely dispersed liquids, similar to a mist. To obtain a uniformly dispersed
mixture throughout spraying, surfaces with recesses are made in the nozzles, causing
the liquid streams to create regions of negative pressure, remote from the surface
of the front end of the nozzle tip. Formation of these surfaces with recesses requires
special machining, due to their configuration.
[0005] A mist-forming nozzle is known [
US2813753, IPC A62C31/22, B05B1/14, publ. 19.11.1957], which has through-holes ending in corresponding
recesses, which are inclined at an angle relative to the corresponding through-holes.
The recesses have a small ratio of length to diameter, which in conjunction with said
slope makes it impossible to create a mist spray with high moment of momentum even
at high pressures. Three mist forming mechanisms are described in the known document.
In the first mechanism, water is discharged asymmetrically from a small through-hole
opposite the wall of a recess at the periphery of the nozzle; in the second mechanism,
water is discharged from small convergent through-holes for discharge, located opposite
one another; in the third mechanism, water is discharged from a small through-hole
for forcing at high pressure relative to the recess without colliding with the recess.
The first two mechanisms make it possible to create a mist at relatively low pressure,
but the mist has a low moment of momentum even when the pressure is increased. The
third mechanism only allows a mist to be created at high pressure.
[0006] A patent is known [
RU2248826, IPC A62C31/02, 27.03.2005] in which several variants are described for creating
a water mist with small particles (fire extinguishant) by means of various spray heads,
in which channels that are interdependent with respect to length and width, produced
by drilling, are located successively, one after another. Liquid that is forced out
of a chamber at high pressure, 80-100 atm, passes through a channel of smaller diameter
(water stream feed channel) onto the walls of a channel of larger diameter (nozzle)
via a tapered transition from one diameter to another. Maximum turbulent dispersion
of the liquid that is forced out is created utilizing the effect of surface tension
in the larger-diameter channel. Maximum dispersion of the turbulent water stream in
the method and devices described in said patent takes place on the outer edge of the
larger of the two channels, i.e. on the outside of the spray head.
[0007] The drawbacks of said method and devices for implementation thereof are: 1. High
pressure is required in the system (140-200 atm) to provide a pressure at sprayer
inlet of 80-100 atm. Observation of the operation of these devices showed that at
lower pressure, despite the opposite assertion in the patent, a mist effect is not
achieved, for the reasons described in that patent itself. The most accurate description
of the condensate state of the sprayed water at a pressure below 80 atm on a sprayer
using said method and devices is a dew. 2. Requirement of maximum concentricity of
the interdependent spray ducts, made by drilling. 3. Fixed interlinked dependence
of lengths and diameters of the interdependent spray ducts. 4. Considerable consumption
of water per specific unit of heat transfer of the seat of combustion. 5. High power
consumption of the electric motors (15-37kW per 100 litres of water) for operating
the high-pressure pumps at 140-200 atm.
DISCLOSURE OF THE INVENTION
[0008] The technical solutions described in this patent are taken as the closest prior art
for the claimed technical solutions. Thus, in essence, the known method of producing
a fire extinguishant consists of creating a water stream and passing it through at
least one spray duct, and with a tapered transition for creating turbulence of the
water stream provided inside each spray duct.
[0009] A known spray duct used for implementing the method described is in essence formed
from two communicating, concentrically arranged channels for feed of the water stream
and a nozzle, the diameter of the nozzle being larger than the diameter of the channel
for feed of the water stream. Moreover, a conical transition of the water stream is
formed at the point of transition from the channel for feed of the water stream into
the nozzle.
[0010] The problem to be solved by the present group of inventions is to create a novel
method of producing a fire extinguishant and a spray duct used for implementation
thereof, achieving the following general technical result: increase in the efficiency
of extinguishing local and volumetric seats of fire of classes A and B of any category
of complexity by increasing the penetrating power of the fire extinguishant created.
[0011] This problem is solved with respect to the method in that in the known method of
producing a fire extinguishant, comprising creating a water stream and passing it
through at least one spray duct, according to the present invention, at least one
edge for break-away of the water stream is formed inside each spray duct, after passing
over which the water stream is broken up into a plurality of individual microdroplets
moving together with subsequent initiation of a process of chaotic repulsion thereof
from the inside walls of the spray duct and collision with one another, obtaining
a finely divided water mist on discharge from the spray duct to the outside.
[0012] A variant is possible, in which, after break-up of the water stream, it is saturated
with atmospheric air by drawing atmospheric air into the spray duct after the edge
for break-away of the water stream, but before discharge from the spray duct to the
outside.
[0013] The problem with respect to the spray duct is solved in that, in a known spray duct
used for producing a fire extinguishant, formed from at least one channel for feed
of the water stream and a nozzle, communicating and located one after another, the
diameter of the nozzle being larger than the diameter of the channel for feed of the
water stream, according to the present invention, the nozzle is a cylinder, through
the bottom of which each channel for feed of the water stream passes, moreover the
minimum angle between the inside wall of the cylinder and its bottom is not more than
90 degrees.
[0014] A variant is possible, in which at least one channel for feed of air, communicating
with the nozzle near the bottom thereof, is additionally introduced.
[0015] Thus, by means of the claimed group of inventions, the efficiency of extinguishing
local and volumetric seats of fire of classes A and B of any category of complexity
is increased by increasing the penetrating power of the fire extinguishant created,
owing to the ability of the substance created, which is a super-dense, finely divided
water mist, to fill the protected volume of the premises instantly, and high efficiency
of extinguishing local and volumetric seats of fire of classes A and B of any category
of complexity, which is mainly characteristic of gaseous volumetric fire extinguishing
systems.
[0016] It should be noted that with possible mixing of the finely divided water mist with
atmospheric air by drawing it into the stream of finely divided droplets of the sprayed
water stream, there is an increase in efficiency of the fire extinguishant obtained
by means of the main technical solution.
[0017] Moreover, compliance of the claimed group of inventions with the criterion of inventive
step is substantiated by the following.
[0018] The liquid medium sprayed by the present method, in contrast to all the methods and
devices described above, is defined as a stream of a plurality of individual microdroplets
moving together, receiving an excess charge of kinetic energy by excess pressure,
forcing the droplets of the water stream into translational motion and their tendency
to release the accumulated energy. Release of the accumulated energy of each individual
microdroplet occurs at the moment it emerges, on the edge for break-away of the water
stream, which is formed by passage through the channel for feed of the water stream
through the bottom of the nozzle, located at an angle of not more than 90 degrees
to the inside wall of the nozzle. Moreover, the stream of fine droplets that have
broken away from the edge impinges on the inside walls of the nozzle. Each microdroplet
acquires an individual acceleration and trajectory of motion, depending on the amount
of accumulated kinetic energy. In the physical sense, all the droplets tend to repel
one another, increasing the runaway distance. The further trajectory of motion of
the vast majority of the individual droplets is deflected by nozzle walls, directing
the reflected droplets towards one another. There is then further collision of droplets
moving towards one another, with even greater dispersion and increase in the number
of droplets moving freely and chaotically. The process of chaotic repulsion and collision
of free droplets continues with increasing intensity. On leaving the spray duct they
form a finely dispersed fire extinguishant, formulated as a super-dense finely divided
water mist, possessing high penetrating power, the ability to fill the protected volume
of a room instantly and high efficiency of extinguishing local and volumetric seats
of fire of classes A and B, of any category of complexity.
[0019] When atmospheric air enters the nozzle, the microdroplets, possessing a high charge
of kinetic energy, capture weakly charged air molecules from the air stream, drawn
in by injection into the stream of charged microdroplets, thereby increasing the intrinsic
volatility. Thus, a process of injection of air into the nozzle is formed, with subsequent
formation of an air/droplet finely dispersed fire extinguishant.
[0020] In contrast to other methods previously described, where formation of a finely divided
aqueous substance is achieved by the effect of surface tension and the associated
vortical turbulence of the water stream, which is at a pressure of 80-100 atm at sprayer
inlet, sprayed on the outer edge of known sprayers. It is only by adhering to the
stated conditions of the proposed method, according to the claims, that a finely dispersed
fire extinguishant is formed, formulated as a super-dense finely divided water mist,
possessing high penetrating power, the ability to fill the protected volume of a room
instantly and high efficiency of extinguishing local and volumetric seats of fire
of classes A and B, of any category of complexity. In essence, a suspension is formed
by the claimed method, i.e. a plurality of water droplets, covering and enveloping
the seat of the fire, the conditions for their dispersal being created by means of
the spray duct.
[0021] Moreover, if air is drawn in, a two-component substance is formed (mixture), since
the water and air interact, in contrast to the prior art, in which they form a one-component
substance.
[0022] It was established experimentally that the effect of the super-dense finely divided
water mist, able to fill the volume of a protected room instantly, is achieved at
significantly lower pressure of the substance, equal to 30-60 atm (and pressure in
the fire-fighting system of 50-80 atm, respectively), which ensures much lower electric
power consumption required for the operation, as a minimum, of one pump unit forming
the water stream supplied to the break-away edge.
BRIEF DESCRIPTION OF THE DRAWINGS
[0023] The essential features of the claimed group of inventions and the possibility of
practical implementation thereof are explained by the following description and drawings.
Figs. 1-7 show variant embodiments of a general type of spray duct (sectional side
view).
Figs. 8-9 show the nozzle used in various types of spray heads.
Fig. 10 shows the application of the claimed group of inventions as a conical spray
head of the sprinkler type (sectional side view).
Fig. 11 shows the application of the claimed group of inventions as a cylindrical
spray head of the sprinkler type (sectional side view).
Fig. 12 shows the application of the claimed group of inventions as a conical spray
head of the drencher type (sectional side view).
Fig. 13 shows the application of the claimed group of inventions as a cylindrical
spray head of the drencher type (sectional side view).
IMPLEMENTATION OF THE INVENTION
[0024] The method of producing a fire extinguishant (Figs. 1-13) comprises creating a water
stream and passing it through at least one spray duct, formed from at least one channel
1, communicating and located one after another both concentrically and non-concentrically
at an angle different from 180°, for feed of a water stream (designed with possibility
of communicating with the valve channel of the spray head) and a nozzle 2, the diameter
of the nozzle 2 being larger than the diameter of each channel 1 for feed of the water
stream. Nozzle 2 is in general a cylinder, through the bottom of which each channel
1 for feed of the water stream passes, the angle between the inside wall of the cylinder
and its bottom being not more than 90 degrees (≤ 90°), aiming at the smallest of the
angles formed. Thus, inside each spray duct, at least one edge 3 for break-away of
the water stream is formed, after passing over which the water stream is broken up
into a plurality of individual microdroplets moving together with subsequent initiation
of the process of their chaotic repulsion from the inside walls of the spray duct
and collision with one another, obtaining a finely divided water mist on discharge
from the spray duct to the outside.
[0025] After break-up of the water stream it can be saturated with atmospheric air by drawing
atmospheric air into the spray duct after the edge 3 for break-away of the water stream,
but before discharge from the spray duct to the outside. For this, at least one air
feed channel 4 may additionally be introduced into the spray duct, said air feed channel
communicating with the nozzle 2 near the bottom thereof, namely between the bottom
and the place where the main stream of droplets collides with the inside walls of
the nozzle. The channel 1 for feed of the water stream enters the bottom of nozzle
2 at an angle such as to prevent most of the water stream going into the air feed
channel 4, i.e. the relative disposition of the air feed channels 4 and of the channels
1 for feed of the water stream is taken into account when designing the spray duct.
A variant is possible in which the air feed channel 4 meets the wall of nozzle 2 immediately
after the edge 3 for break-away of the water stream (Figs. 1, 2, 4-7, 10-13). In this
case the air feed channel 4 is usually formed with a drill. It may be composite, i.e.
in the form of a set of several communicating channels, leading externally into the
nozzle 2. Another variant is possible, in which there is an air chamber 5 (Figs. 2,
4, 9, 10, 12), formed by means of an upright 6, in which holes are made for passage
of air into nozzle 2, located between channel 1 for feed of the water stream and nozzle
2, and the air feed channel 4 is formed around the nozzle 2. Moreover, there may be
several air feed channels 4 and they may be arranged in a circle around nozzle 2 (Fig.
8).
[0026] It should be noted that in the closest prior art, the nozzle is manufactured used
a drilling method, which results in formation of a taper therein. In the claimed spray
duct, the nozzle 2 is formed by milling, which precludes formation of a taper and
allows several variants of design of the bottom, for example flat (Figs. 1,2,6, 7)
(not taking into account process rounding at the edges owing to the use of a milling
cutter), concave or of any other shape for which the minimum angle between the bottom
and the inside wall of the cylinder of nozzle 2 is not more than 90 degrees (≤ 90°).
That is, in the case when a concave bottom is formed, the angle is reckoned between
the wall and the tangent to the circle containing the bottom, and in the case of a
sloping bottom (Fig. 6) it is the smallest of two angles between the bottom and the
wall; there is also a possible variant embodiment of the bottom in the form of a depressed
cone (Figs. 3-5), with the channel 1 for feed of the water stream passing through
its vertex. Moreover, the walls of the nozzle 2 may also be sloping (Fig. 6). There
may be several channels 1 for feed of the water stream (Fig. 7), with an edge 3 for
break-away of the water stream formed at the point of transition from each channel
1 into the nozzle 2.
[0027] Moreover, the angle at which the channel 1 for feed of the water stream passes through
the bottom of the nozzle 2 does not affect achievement of the technical result, nor
does the shape of the bottom and the concentricity or non-concentricity of the disposition
of the channel 1 for feed of the water stream and of the nozzle 2. Because what is
most important is the edge 3 for break-away of the water stream that is formed on
passage of the channel 1 for feed of the water stream through the bottom of the nozzle
2, actually inside the spray duct, in contrast to the closest prior art, where a break-away
edge is formed at the outlet from the spray duct to the outside, for a water stream
already made turbulent by means of a tapered transition. In the claimed technical
solution, everything is done so that, at the point of transition from the channel
1 for feed of the water stream into the nozzle 2, there is no swirling of the water
stream, and on the contrary there is multiple break-up thereof.
[0028] The nozzle 2 and the air feed channels 4 may be formed both in the body of the spray
head, and may be made in the form of a separate nozzle 7 (Figs. 8, 9), inserted or
screwed into the spray head with respect to the channel 1 for feed of the water stream.
[0029] In the spray head it is possible both to use spray ducts separately (Fig. 3), and
together with the air feed channel 4 (Figs. 1-2, 4-7, 10-13), as well as various combinations
thereof (Figs. 10, 12).
[0030] By means of the claimed group of inventions, it is proposed to create a fire extinguishant
containing, as active components, fresh water or desalinated seawater and atmospheric
air (if it is drawn in).
[0031] At least one spray duct is used in a fire-fighting system (not shown in the drawing),
comprising spray heads (Figs. 10-13), the system (not shown in the drawing) made up
of the elements listed above, a connecting pipeline (not shown in the drawing), pipe
joints (not shown in the drawing), hoses (not shown in the drawing) and connections
(not shown in the drawing), control valve devices (not shown in the drawing) and pump
units (not shown in the drawing) with electric and pneumatic drive, together providing
feed of fire extinguishant to the source of combustion.
[0032] Figs. 10-13 show the application of the claimed group of inventions for various types
of spray heads.
[0033] Fig. 10 shows a conical spray head of the sprinkler type. The conical shape of the
body 8 of the head is due to the need to direct the outlet orifice of the nozzle 2,
located inside the screw-in nozzle 7, which also has an air chamber 5 and at least
one air feed channel 4, at an angle of 75-30 degrees to the surface to be protected.
The nozzle 7 is threaded and is screwed into the body 8 of the spray head or the channel
1 for feed of the water stream. The body 8 is provided with a seal 9 and a thread
(shown conventionally in the drawing) for assembling the head in a pipe adapter (not
shown in the drawing). On the opposite side, a threaded nut 10 is screwed into the
body 8, with at least one through-hole (not shown in the drawing), providing feed
of water from the pipe (not shown in the drawing), through a pipe adapter (not shown
in the drawing) into the valve channel 11 of the head, a rubber seal 12 and a gauze
filter 13 preventing any mechanical impurities or suspended matter getting into the
head. Inside the head, a valve channel 11 is drilled, allowing movement of the stem
14 of the shut-off valve and communicating with the channel 1 for feed of the water
stream. The stem 14 of the shut-off valve with rubber seals 15 is arranged inside
the body 8, lengthwise to the valve channel 11, together with the nut 10 of the body
8, ensuring retention of water in the pipeline (not shown in the drawing) until the
time of operation (rupture) of the heat-dependent bulb 16. The heat-dependent bulb
16 is arranged in the holder of the body 8, which has at least one milled window 17
for ensuring that air heated by the seat of the fire is supplied to the bulb 16. The
bulb 16 retains the stem 14 of the shut-off valve inside the nut 10 and is fixed by
a set screw 18. The set screw 18, which has a thread and is screwed into the end face
of the holder of the body 8, is intended for retaining and locking the heat-dependent
bulb 16 in the working position. On rupture of the bulb 16, the stem 14 of the shut-off
valve is released and water at a pressure of 40-60 kg/cm
2 is discharged from nut 10, thereby providing feed of water through the valve channel
11 into at least one spray duct, and the fire extinguishant formed therein is expelled
towards the surface to be protected.
[0034] Fig. 11 shows an embodiment of the claimed group of inventions for the example of
a cylindrical spray head of the sprinkler type. The operating principle of this head
fully coincides with the operating principle of the conical head of the sprinkler
type described above. The cylindrical shape of the body 8 is due to the need for interlinked
arrangement of the channel 1 for feed of the water stream, to connect it with the
nozzle 2, and the associated air chamber 5 and air feed channel 4 strictly with respect
to one another, and to direct the outlet orifice of the nozzle at an angle of 75-30
degrees to the surface to be protected.
[0035] Fig. 12 shows an embodiment of the claimed group of inventions for the example of
a conical spray head of the drencher type. The conical shape of the body 19 is due
to the need to direct the outlet orifice of the nozzle 2, located inside the screw-in
nozzle 7, which also has an air chamber 6 and at least one air feed channel 4, at
an angle of 75-30 degrees to the surface to be protected. The nozzle 7 is threaded
and is screwed into the body 19 of a conical spray head of the drencher type or the
channel 1 for feed of the water stream. The body 19 is provided with a seal 20 and
a thread for assembling the head in a pipe adapter (not shown in the drawing). The
threaded nut 21, with at least one through-hole (not shown in the drawing) is screwed
into the body 19, to provide feed of water from a pipe (not shown in the drawing),
through a pipe adapter (not shown in the drawing) into the valve channel 22 of the
head, a rubber seal (not shown in the drawing) and a gauze filter 23 preventing any
mechanical impurities or suspended matter getting into the head. An internal chamber
(valve channel 22) is drilled inside the head. On command, after opening of the external
shut-off device (not shown in the drawing), the head of water, at a pressure of 40-60
kg/cm
2, passes through the nut 21, the internal chamber (valve channel 22) and at least
one channel 1 for feed of the water stream to the edge 3 for break-away of the water
stream as a plurality of individual microdroplets, impelled towards the walls of the
nozzle 2. By means of the air chamber 5 and at least one air feed channel 4, located
together with the nozzle 2 inside the nozzle 7 screwed into the body 19, atmospheric
air is fed in, captured by the chaotically moving microdroplets, the whole constituting
the stream that is drawn in and mixed, which in its turn rushes out of the head, releasing
the accumulated potential energy of the microdroplets, thereby forming a highly dispersed
cloud of water mist saturated with air molecules, otherwise called a "dense finely
divided water mist".
[0036] Fig. 13 shows an embodiment of the claimed group of inventions for the example of
a cylindrical spray head of the drencher type. The operating principle of this head
fully coincides with the operating principle of the conical head of the drencher type
described above. The cylindrical shape of the body 19 is due to the need for interlinked
arrangement of the channel 1 for feed of the water stream, and the respective arrangement
of the nozzle 2, with the associated air chamber 5 and air feed channel 4 strictly
with respect to one another, and to direct the outlet orifice of the nozzle 2 at an
angle of 75-30 degrees to the surface to be protected.
[0037] Release of the accumulated energy of each individual microdroplet occurs through
the valve channel 6 of the spray head 7 at the moment of discharge from the outlet
channel 4. Each microdroplet acquires an individual acceleration and trajectory of
motion, depending on the amount of accumulated kinetic energy. In the physical sense,
all the droplets tend to repel one another, increasing the runaway distance. The further
trajectory of motion of the vast majority of the individual droplets is deflected
by the walls of the mixing chamber 5, directing the deflected droplets towards one
another. There is then further collision of the droplets moving towards one another,
with even greater dispersion and increase in the number of droplets moving freely
and chaotically. The process of chaotic repulsion and collision of the free droplets
continues with increasing intensity. The microdroplets, possessing a high charge of
kinetic energy, capture the weakly charged air molecules from the air stream, thereby
increasing the intrinsic volatility. There is thus development of a process of air
injection through channel 3 for feed of atmospheric air into the mixing chamber 5,
with subsequent formation of an air/droplet finely dispersed fire extinguishant, formulated
as a super-dense finely divided water mist, possessing high penetrating power, the
ability to fill the protected volume of a room instantly and high efficiency for extinguishing
local and volumetric seats of fire of classes A and B, of any category of complexity.
[0038] After carrying out a number of experimental studies, it was established that the
most effective size for the diameter of the channel 1 for feed of the water stream
is 0.5-1.0 mm, and the diameter of the nozzle 2 must be a multiple of the diameter
of the channel 1 for feed of the water stream in the proportions 1:5 - 1:10. The length
of the channel 1 for feed of the water stream must be at least 2 mm and at most 10
mm, and the length of the nozzle 2 must be 2-3 times its diameter. To ensure formation
of the air stream and effective drawing-in of air molecules into the stream of charged
microdroplets at a pressure of 30-60 atm, at least one air feed channel 4 is arranged
as close as possible, but not closer than 1.0 mm to the edge 3 for break-away of the
water stream, at an angle of 35-45° to the plane of the edge 3 for break-away of the
water stream. The effective diameter of the air feed channel 4 must be 1.0-3.0 mm.