The invention relates to a device and a method for extinguishing fires and/or for suppressing explosions, and also to a nozzle for producing a spray of liquid.
A known device for extinguishing fires and suppressing explosions comprises a chamber and a nozzle defining a discharge pathway from the chamber. The chamber has an inlet for the pressure driven introduction of a liquid into the chamber. In use, liquid is introduced into the chamber, usually driven by a compressed gas, and the liquid is subsequently discharged through the nozzle so as to produce a spray of liquid droplets. The spray acts to extinguish the fire or suppress the explosion. Generally, before the device is activated by introduction of the liquid into the chamber, the chamber contains air, and this gives rise to a problem associated with this known device. Specifically, when the device is activated by introduction of the liquid into the chamber, the air is driven through the nozzle before the liquid. This is undesirable because the expelled air contains oxygen which feeds the fire or the explosion before any water droplets are sprayed from the nozzle.
In accordance with a first aspect of the invention, there is provided a fire extinguishing or explosion suppression device comprising, a chamber and a nozzle defining a discharge pathway from the chamber, the chamber having an inlet for pressure-driven introduction of a liquid into the chamber, the chamber being shaped so that a gas contained in the chamber before the introduction of the liquid is entrained into the liquid during the pressure driven introduction of the liquid such that a mixture of the liquid and the gas is discharged through the nozzle to create a mist for extinguishing a fire or suppression of an explosion.
In accordance with a second aspect of the invention, there is provided a method of extinguishing a fire or suppressing an explosion, comprising providing a chamber containing a gas, forcing a liquid into the chamber, the chamber being shaped so that the gas becomes entrained within the liquid as the liquid is forced into the chamber to produce a mixture of the gas and the liquid, discharging the mixture of the gas and the liquid through a nozzle to produce a mist for extinguishing a fire or suppressing an explosion.
Accordingly, the first and second aspects of the invention may allow a reduction or elimination in discharge of air alone from the device.
Nozzles known for suppressing explosions or extinguishing fires tend to produce sprays which are homogenous in terms of droplet size distribution. Another known type of nozzle produces a spray having a core consisting of relatively small liquid droplets, the core being surrounded by relatively large liquid droplets.
In accordance with a third aspect of the invention, there is provided a nozzle for producing a spray of liquid, the spray having a core of larger liquid droplets and the core being surrounded by smaller liquid droplets.
Nozzles in accordance with this aspect of the invention may be particularly effective at suppressing explosions and extinguishing fires.
In accordance with a fourth aspect of the invention, there is provided a fire extinguishing or explosion suppressing device in accordance with the first aspect of the invention, wherein the or each nozzle is in accordance with the third aspect of the invention.
Such a combination may be particularly effective at suppressing explosions.
In accordance with a fifth aspect of the invention, there is provided a method of extinguishing a fire or suppressing an explosion, comprising directing a liquid spray at the fire or explosion, the spray having a core of large liquid droplets and the core being surrounded by smaller liquid droplets.
As used herein the terms “extinguish” and “extinguishing” include the case where a fire is only partially extinguished.
The following is a more detailed description of embodiments of the invention, by way of example only, reference being made to the accompanying drawings in which:
a and 6b show pressure within a closed space during simulated explosions;
a and 7b show temperature within the closed space during simulated explosions;
a is a schematic side elevation showing an outer annular insert forming part of the nozzle;
b is a schematic cross-sectional view of the outer annular insert of
c is a schematic end elevation of the outer annular insert of
a is a schematic side elevation of an inner annular insert forming part of the nozzle;
b is a schematic cross-sectional representation of the inner annular insert of
c is a schematic end elevation of the inner annular insert of
a is a schematic side elevation of an inner insert forming part of the nozzle;
b is a schematic side elevation of the inner insert of
The explosion suppression system shown in
Referring first to
In operation, if one or more of the explosion sensors 10 detect an explosion, a signal is sent via the detection unit 12 to the control unit 14. In turn, the control unit 14 passes a signal to the extinguisher unit 20 which activates all of the extinguishers 22 to discharge liquid mist into the closed space.
Apart from the extinguishers 22, all of the components of the explosion suppression system are well know. Each extinguisher 22 consists of a liquid container 24 and a discharge head 26 which will now be described in greater detail.
As shown in
As best seen in
Importantly, as shown in
The discharge chamber body 28 also has an inlet 40 in the form of an annular flange which extends upwardly from the second wall 32 and which opens into the chamber 38. The inlet 40 is threaded on the inside for connection to the corresponding liquid container 24 so that liquid from the container 24 can be introduced into the chamber 38 through the inlet 40.
Remaining with
Finally, the discharge chamber body 28 also has four small outlet mounts, two of which are shown in
As best seen in
For the avoidance of any doubt, the space between the first wall 30 and the planar wall 34 is a closed space and plays no part in the operation of the current invention.
Each discharge head 26 is connected via its inlet 40 to a respective one of the liquid containers 24 via a respective valve (not shown) which is operated by the extinguisher unit 20. Each liquid container 24 contains a liquid 46 lying underneath a pressurized gas 48. The liquid containers 24 are of known construction.
The large nozzle 29 is best seen in
The large nozzle 29 is formed from four parts which are concentric around an axis 107 and which are best seen in
The radially outermost one of these parts is a casing 72 shown in
An outer annular insert 88 is shown in
Eight grooves 106 are cut into the outer surface of the outer annular insert 88 (see
Looking now at
Referring now to
Firstly, the inner annular insert 122 is radially smaller than the outer annular insert 88 so that the inner annular 122 can fit within the outer annular insert 88. Further, the body portion 118a of the inner annular insert 122 is shorter in the axial direction than the body portion 118 of the outer annular insert 88, so that the body portion 118a of the inner annular insert 122 can fit within the body portion 118 of the outer annular insert 88. Also, the tubular portion 120a of the inner annular insert 122 is longer and narrower than the tubular portion 120 of the outer annular insert 88, so that the tubular portion 120a of the inner annular insert 122 can extend through the tubular portion 120 of the outer annular insert 88. The manner in which the inner annular insert 122 fits within the outer annular insert 88 is best shown in
The inner annular insert 122 does not have an annular wall similar to the annular wall 102 of the outer annular insert 88. Instead, the outer end of the tubular portion 120a of the inner annular insert 122 is provided with a radially outwardly directed annular flange 124. The annular flange 124 has a frusto-conical surface 126 which extends radially and axially outwards from the tubular portion 120a of the inner annular insert 122.
Finally, the grooves 106a provided in the outer surface of the body portion 118a of the inner annular insert 122 are similar to the grooves 106 of the outer annular insert 88. However, the grooves 106a of the inner annular insert 122 differ in two respects from the grooves 106 of the outer annular insert 88. Firstly, the grooves 106a of the inner annular insert 122 are deeper, in the radial direction, as compared to the grooves 106 of the outer annular insert 88. Secondly, at the ends of the grooves 106, 106a, located towards the outlet end 62 of the large nozzle 29, the angular extension around the axis 107 for a given unit length in the axial direction of each groove 106a in the inner annular insert 122 is less than the corresponding angular extension of each groove 106 in the outer annular insert 88. In other words, at the ends of the grooves 106, 106a closest to the outlet end 62 of the large nozzle 29, the angle between the groove 106, 106a, relative to the axis 107, is less for the grooves 106a in the inner annular insert 122 as compared to the grooves 106 in the outer annular insert 88. The surfaces of the grooves 106a may be roughened for a purpose described below.
The last of the four concentric parts making up the nozzle 29 is shown in
The manner in which the four concentric parts making up the large nozzle 29 fit together is best shown in
In turn, the first annular passageway 156 then opens into a formation for directing droplets from the outlet end 62 of the large nozzle 29 at an acute angle from the axis 107. The droplet directing formation is formed by the axially outwardly facing concave surface 86 provided on the casing 72 together with the radially extending annular wall 102 provided on the outer annular insert 88. As shown in
The flange portion 92a of the outer surface of the inner annular insert 122 fits within the recess portion 108 of the inner surface of the outer annular insert 88 so as to locate the inner annular insert 122 within the outer annular insert 88. The first cylindrical portion 96a of the outer surface of the inner annular insert 122 fits closely within the first cylindrical portion 112 of the inner surface of the outer annular insert 88 so that the inner surface of the outer annular insert 88 closes the grooves 106a in the inner annular insert 122 so as to form eight corresponding radially intermediate channels 158. This is best seen in
The flange portion 132 of the surface of the inner insert 128 fits within the recess portion 108a of the inner surface of the inner annular insert 122 so as to locate the inner insert 128 within the inner annular insert 122. The first cylindrical portion 136 of the surface of the inner insert 128 lies closely within the first cylindrical portion 112a of the inner surface of the inner annular insert 122 so that the inner surface of the inner annular insert 122 closes the grooves 144 provided in the inner insert 128. The six grooves 144 when closed in this way form six corresponding radially inner channels 164, which are best seen in
One of the small nozzles 32a is shown in
In operation, when the control unit 14 passes an activating signal to the extinguisher unit 20, the extinguisher unit 20 causes the valves to open between the discharge heads 26 and the liquid containers 24. The processes that take place in the discharge heads 26 are identical and so this process will only be described with reference to one of the discharge heads 26.
Before activation, the chamber 38 is already full of air. When the valve between the discharge head 26 and the corresponding liquid container 24 is opened, the pressurized gas 48 in the liquid container 24 forces the liquid 46 through the inlet 40 to the chamber 38 of the discharge chamber body 28. The speed at which the liquid 46 is introduced into the chamber 38 is preferably very fast, and may be in the order of 500 litres per second.
Liquid 46 entering the chamber 38 via the inlet 40 impinges first on the convex surface 36 of the first wall 30. As the liquid impinges against the convex surface 36, the liquid is directed by the convex surface 36 in a plurality of directions around the chamber 38, including towards the large nozzle 29. The shape of the chamber 38, and in particular the shape of the convex surface 36 of the first wall 30 is such so as to maximise turbulence within the chamber 38. Turbulence is also increased by the roughness of the convex surface 36 and the concave surface 37. The result of the turbulence is that the air already contained within the chamber 38 before introduction of the liquid 46 is commenced, is very rapidly and thoroughly entrained into the liquid 46 entering the chamber 38.
In view of this rapid entrainment of the air into the liquid 46, the air is not pushed on its own through the nozzles 29, 32a to 32d. Instead, the mixture of air and liquid 46—the air being entrained within the liquid 46—is discharged almost immediately through the nozzles 29, 32a to 32d.
When the mixture of the liquid 46 and the air is discharged through the nozzles 29, 32a to 32d, the nozzles produce a mist consisting of small water droplets which are relatively homogenous in size and distribution. This fine mist, shown at 50 in
After all the air which was originally contained within the chamber 38 before introduction of the liquid 46 has been discharged from the discharge head 26, there is no gas left within the chamber 38. At this stage, liquid 46 is still being forced into the chamber 38 and the liquid 46 is discharged from the nozzles 29, 32a to 32d in the form of a conical spray of liquid droplets. This is shown at 52 in
The way in which each nozzle 29, 32a-32d produces, from liquid alone (after the gas has been discharged from the chamber 38), a conical spray with larger droplets 54 at the axis of the cone, smaller droplets 56 at the outside of the cone, and intermediate sized droplets 58 between the larger and smaller droplets is now described. This process will be described for the large nozzle 29 only, as the process is substantially identical in each of the small nozzles 32a-32d.
Referring to
The liquid which enters the radially intermediate channels 158 eventually forms the intermediate sized droplets 58 in the spray. This liquid passes through the intermediate channels 158 gaining rotational momentum in view of the generally spiral curvature of the intermediate channels 158. This liquid exits the radially intermediate channels 158 into the second annular space 160 formed between the outer and inner annular inserts 88, 122. Again, the shape of the second annular space 160 forces the liquid to move radially inwardly and this increases the rotational velocity of the liquid. The liquid then passes into the second annular passageway 162 to the droplet directing formation formed by the frusto-conical surface 126 and the annular wall 102. This droplet directing formation directs the intermediate size droplets 58 outwardly from the outlet end 62 of the nozzle 29 through a range of angles extending from about 30 to 50° from the axis 107. This portion of the conical spray is seen at 192 in
The liquid that enters the radially inner channels 164 forms the core of relatively large droplets 54. Again, as this liquid passes through the radially inner channels 164, it acquires a rotational momentum from the generally spiral curvature of the radially inner channels 164. As the liquid exits the radially inner channels 164 it enters the third annular space 166 which, again, directs the liquid radially inwardly thereby increasing the rotational speed of the liquid. From the third annular space 166, the liquid passes into the cylindrical passageway 168 from which it is discharged at the outlet end 62 of the nozzle 29. The liquid which is discharged from the cylindrical passageway 168 forms an inner component of the conical spray consisting of the smallest droplets 54. This inner component extends to about 20° from the axis 107. This component is shown at 194 in
As will be appreciated from the description of the spiral grooves 106, 106a and 144 above, the radially outer channels 150 have the smallest depth in the radial direction, the radially inner channels 164 have the greatest depth in the radial direction, and the intermediate channels 158 have an intermediate depth in the radial direction. It has been found that the depth of the channels in the radial direction is related to droplet size in that deep channels produce large droplets and shallow channels produce smaller droplets.
It will also be appreciated from the discussion of the grooves 106, 106a and 144 above, that the generally spiral curvatures of the channels 150, 158, 164 differ from one another. Specifically, at the ends of the channels 150, 158, 164 that open into the corresponding annular spaces 156, 160, 166, the radially outer channels 150 undergo a greater angular extension around the axis 107 for a given unit length in the axial direction as compared to the radially inner channels 164. The radially intermediate channels 158 undergo an intermediate angular extension around the axis 107 for the same unit distance along the axis 107. In other words, when comparing the angles of the channels 150, 158, 164 at their outlets, the radially outer channels 150 have a greater angle relative to the axis 107, the radially intermediate channels 158 have an intermediate angle relative to the axis 107 and the radially inner channels 164 have a smaller angle relative to the axis 107. The greater the angular extension for a given unit length in the axial direction (in other words the greater the angle compared to the axis 107) the greater the rotational momentum that is given to the liquid passing through the channels. It has been found that a greater rotational momentum leads to the formation of smaller droplets.
Hence, it will be appreciated that the shallow depth and the relatively large angular momentum corresponding to the radially outer channels 150 help to produce the small droplets 56. The intermediate depth and the intermediate rotational momentum corresponding to the intermediate channels 158 help to produce the intermediate size of the droplets 58. The large depth and the relatively low angular momentum corresponding to the radially inner channels 164 help to generate the large droplets 54 at the core of the conical spray 52.
Droplet size is also affected by roughness of the surfaces of the channels. The rougher the surface the greater the turbulence and the smaller the droplets.
The nozzles 29, 32a-32d are constructed to withstand relatively high pressures. During discharge, the pressures experienced by the chamber and the nozzles may be in the region of 20-60 bar, preferably 40-60 bar.
The channels 150, 158, 164 through the nozzles 29, 30a-30d have no sharp bends and this helps to maximise liquid flow rate through the nozzles 29, 30a-30d.
As will be appreciated from
It will be appreciated that the discharge head 26 described above gives rise to very significant advantages. Firstly, as the shape of the chamber 38 leads to rapid and thorough entrainment of the air within the liquid 46, this in turn leading to almost immediate discharge of a fine mist from the nozzles 29, 32a to 32d, the explosion suppressing system starts to suppress an explosion almost immediately. Additionally, there is almost no discharge of air alone from the discharge heads 26—discharge of air alone being disadvantageous by providing oxygen to the explosion. The explosion suppression system described above may discharge all of the liquid 46 and suppress an explosion within as little as 200 milliseconds.
Additionally, the droplet size distribution in the sprays, after the gas contained in the chamber 38 has been discharged, has been found to be highly advantageous, particularly in suppressing explosions. The large droplets 54 at the core of each spray have sufficient momentum to penetrate rapidly and deeply into a developing fireball (or a fire). The small droplets 56 at the outside of the spray are very effective at flooding an area—i.e. forming a generally homogenous uninterrupted mist which can completely fill an enclosed space. This helps both in suppressing an explosion (or a fire) and also in preventing re-ignition after a fireball (or a fire) has been extinguished. The intermediate sized droplets are optional and help with both functions.
In many cases, the liquid 46 might be pure water. However, other liquids may be used. For example, it is often desirable to use, as the liquid 46, an aqueous solution of an alkali salt. Aqueous solutions of alkali salts have been found to cool fires and explosions at higher rates as compared to pure water. Suitable alkali salts are potassium bicarbonate and potassium acetate. A particularly advantageous liquid is an aqueous solution of potassium lactate. The potassium lactate depresses the freezing point of the water, and the potassium lactate solution can remain a liquid at as low as minus 40° C. It is clearly advantageous to discharge a mist at a low temperature as this will tend to be more effective in suppressing explosions or extinguishing fires.
Non-aqueous liquids can also be used. Any non-aqueous liquid suitable for fire or explosion suppression may be used. For example, the liquid may be CF3CF2C(O)CF(CF3)2 which is sold under the trade mark NOVEC 1230 by 3M Corporation.
Preferably, liquids used in the explosion suppression system described above will have a boiling point in the range of 20° C.-100° C. Of particular interest are fire or explosion suppressing liquids having a boiling point in the range of 20° C.-60° C., more particularly in the range 20° C.-40° C.
The nozzles described above may be particularly advantageous for discharging non-aqueous fire or explosion suppressing liquids having boiling points in the range of 20° C.-100° C., and more particularly 20° C.-60° C. or 20° C.-40° C. One specific liquid that can be discharged from nozzles of the type described above is the aforementioned CF3CF2C(O)CF(CF3)2.
It will be appreciated that the explosion suppression system described above can be modified in a large number of ways.
Firstly, instead of being used to suppress an explosion, the system may be used, possibly with lower discharge rates, to extinguish fires. In this case the discharge pressures may be in the range of 4 to 12 bar.
The discharge chamber body 28 need not be exactly as described above. The chamber 38 may be any shape which increases turbulence as the liquid 46 is introduced into the chamber 38 so as to cause entrainment of air into the liquid 46.
While it is advantageous for the convex surface 36 of the first wall 30 to be spherical, other convex shapes may be used, such as elipsoid shapes. Similarly, other concave shapes, such as elipsoid shapes, may be used for the concave surface 37 of the second wall 32.
It is not necessary for the first wall 30 to be angled in relation to the inlet 44 by the precise angle shown in
It will be appreciated that any suitable number of nozzles may be used. Additionally, whereas it is preferred to use a nozzle or nozzles which, after the air has been exhausted from the chamber 38, produce a conical discharge with course droplets at the centre and fine droplets at the outside, this is not essential. Any suitable nozzles may be used. The combination of the discharge body 28 and the nozzles 29, 30a-30d has been found to be particularly effective in suppressing explosions.
Other nozzles which produce sprays with larger droplets at the inside and smaller droplets at the outside may also be used.
The extinguishers 22 may be connected to any suitable control unit and any suitable explosion or fire sensors may be used.
Tests carried out have demonstrated that the explosion suppression system described above is very effective at suppressing an explosion.
An explosion was simulated in a closed space having a volume of 6.9 m3. The explosion was simulated using 1.11 diesel fuel at a temperature of 82° C. and a pressure of 82.7 bar (g). The diesel fuel was discharged into the closed space through a TACOM fuel dispersion nozzle and ignited using a 5 KJ pyrotechnic igniter after 90 ms of initiation of the discharge.
The explosion suspension system was as described above and had the following specific characteristics. Three extinguishers 22 were spaced evenly in the close space. The pressure in the liquid containers 24 was 50 bar(g). Various amounts of liquid were used in different tests and the liquid was an aqueous solution of 50% (wt/vol) potassium lactate. Introduction of the liquid into the discharge heads 26 was initiated after 11 ms from ignition of the diesel fuel.
The closed space contained four human sized manequins each fitted with a temperature sensors.
The results using the suppression system are shown in
As seen by comparing
As seen by comparing
Tests showed that a liquid volume of 0.911 per m3 of closed space successfully suppressed the simulated explosion. Lower volumes could also be effective (down to 0.68 l/m3) if the stored energy within the suppression system was above 40 bar.1.kg−1.
Number | Date | Country | Kind |
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0510773.5 | May 2005 | GB | national |
0604499.4 | Mar 2006 | GB | national |
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Number | Date | Country | |
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20060278411 A1 | Dec 2006 | US |