Download - RISE Fire Research

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TABLE OF CONTENTS

1

INTRODUCTION ................................................................................................................. 3

2

SUMMARY AND CONCLUSIONS ....................................................................................3

3

MEASUREMENT PROGRAMME ..................................................................................... 4

4

MEASUREMENT TECHNIQUES AND UNCERTAINTY .............................................7 4.1 k-factor .......................................................................................................................... 7 4.2 Area distribution............................................................................................................... 8 4.3 Droplet sizes and velocities............................................................................................ 10 4.4 Droplet size terminology ................................................................................................ 18 4.5 Droplet velocity.............................................................................................................. 18

5

CALCULATION OF DROPLET TRAJECTORIES ...................................................... 19

6

RESULTS ......................................................................................................................... 22 6.1 k-factor for the nozzles................................................................................................... 22 6.2 Exit velocity ................................................................................................................... 23 6.3 Droplet sizes measured by two institutes ....................................................................... 25 6.4 Individual nozzle characteristics .................................................................................... 29 6.4.1 Nozzle HV K26............................................................................................... 29 6.4.2 Nozzle HVK44................................................................................................ 37 6.4.3 Nozzle MVK18 ............................................................................................... 45 6.4.4 Nozzle MVK41 ............................................................................................... 49 6.4.5 Nozzle MVK59 ............................................................................................... 54 6.4.6 Nozzle MVK80 ............................................................................................... 56

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EVALUATION .................................................................................................................... 61 7.1 Measurement techniques ................................................................................................ 61 7.2 Differences between nozzles .......................................................................................... 62

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REFERENCES.....................................................................................................................65

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APPENDIX A.1 NOZZLE HVK26 - 2,6 bar.....................................................................66

10 APPENDIX A.2 NOZZLE HVK 26 – 5,3 bar ...................................................................93 11 APPENDIX A.3 NOZZLE HVK44 – 4,9 bar ..................................................................119 12 APPENDIX A.4 NOZZLE MVK18 -2,6 BAR................................................................143 13 APPENDIX A.5 NOZZLE MVK80 -2,1 BAR.................................................................150 14 APPENDIX B: Drawing of ADD apparatus....................................................................158

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1 INTRODUCTION Deluge nozzles have traditionally been characterised by the spray pattern and the exit velocity, and flow characteristics have been described by the k-factor. Design has been carried out to fulfil the requirements of area coverage, in most cases an application density over a certain area. Little information is available on the droplet sizes and the distribution of droplets in sprays, and when one wants to calculate the behaviour of water droplets in a fire zone or in the vicinity of a fire, the droplet size distribution is really important. In this report, several techniques and approaches to obtain the real droplet size and velocity distribution is used. At present, no single technique presents all the important features, but a combination of two techniques makes it possible to make a good estimate of flow-field, droplet sizes and velocities within a water spray.

2 SUMMARY AND CONCLUSIONS A comprehensive measurement programme to characterise sprays of water from deluge nozzles have been carried out. No method is available to measure all characteristics in one single operation. SINTEF has developed a method to quantify water application during fire, an Actual Delivered Density apparatus, (ADD apparatus). k-factor measurements (relation between nozzle pressure and water flow) have been carried out by different test set-up, including a standardised method. Two different laboratories (TelTek, Porsgrunn, Norway and IdF, Magdeburg, Germany) have been engaged to characterise droplet sizes and velocities. The measurement of k-factor shows minor variations between different laboratories and the manufacturers nominal k-factors are within the acceptance criteria of such measurements. The water application density is in one set of experiments measured by a special apparatus developed by SINTEF (ADD apparatus). The measurement technique allows measurement of Actual Delivered Density of water even during fire conditions, and is useful for research purpose. Used in an open space without any fire, some water is displaced by the airflow above the fixed surface, which leads to a discrepancy of maximum 20% between measured supply and collected water. This discrepancy is normal for this type of technique. Droplet size, velocity and area distribution for 5 deluge nozzles at different pressure have been examined. Two types of Laser Doppler and Phase Doppler anemometry have been used. The examined nozzles have been used in earlier medium-to-large-scale fire tests. The nozzle characteristics are used as input in simulation of the interaction of water droplet and fire development. The used measurement technique for droplet sizes gives a picture of deluge nozzles that produces a large amount of very small water droplets, in contrast to what is earlier reported. The reason for this discrepancy may be the better resolution of the measurement technique, but the presented results may also indicate uncertainties connected to the same technique.

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3 MEASUREMENT PROGRAMME In the tests carried out to quantify the effect of deluge systems, two main types of nozzles have been used. These are High Velocity (HV) and Medium Velocity (MV) nozzles. The tested HV nozzles produce the water spray by break-up of the flow at the edge of the nozzle orifice, after creating a rotation inside the nozzle body. The MV nozzles are equipped with deflectors that break up the water stream from the orifice. The nozzles used in the former fire tests carried out by SINTEF /1, 2/ has been tested at two different laboratories for droplet characterisation. The two laboratories are Teltek, (Porsgrunn, Norway) /3/ and IdF –Institut der Feuerwehr – Sachsen-Anhalt, (Magdeburg, Germany) /4/. Water flow characteristics and area distribution have been measured by SINTEF. Table 1 shows the tested nozzles and under which conditions they have been tested.

Table 1.

Nozzle identification and test programme for droplet characterisation.

SINTEF fire tests Nozzle id HV K26 HV K44 MV K18 MV K41 MV K59 MV K80

Figure 1.

IdF droplet characterization Pressure [bar] 2,6 2,4 3,5 4,9 5 2,6 1,9 2,1

Teltek droplet characterization Nozzle id Pressure [bar] 5,3 8

N7

2,4

2,6

N1

2

2,5

The High-velocity nozzles HV K44 and HV K26 used in the tests.

5

8 7

5

Figure 2.

The High-velocity nozzle HV K44 dismantled.

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Figure 3.

The Medium-velocity nozzles MV K18, MV K41, MV K59 and MV K80 used in the tests.

Table 2.

Specifications of the nozzles used in the SINTEF tests.

SINTEF fire tests Nozzle id HV K26 HV K44 MV K18 MV K41 MV K59 MV K80

GW Sprinkler identification Bore diameter [mm] Fyrhed type C 8 Fyrhed type D 10 Thermospray 6,3 Thermospray 8,5 Thermospray 11 Thermospray 12,4

Spray angle Operating pressure max min 5 2,8 80-90° 6 2,8 60° 3,5 1,4 ~60° 3,5 1,4 90° 3,5 1,4 ~120° 3,5 1,4 ~135°

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4 MEASUREMENT TECHNIQUES AND UNCERTAINTY The characterisation of water spray nozzles is normally done by the correlation between flow rate and pressure (k-factor) and application density (litres/m2 min). In some cases, measurement of the area distribution of water is also carried out. However, when the interaction between water droplets and a fire plume is to be simulated by mathematical models, more information is needed. Ultimately, the volume distribution of droplets is what is needed to quantify the action of water in relation to fire. Figure 4 shows different aspects of a water spray used to characterise water distribution. The top two aspects are normally what are presented by nozzle manufacturers.

Spray angle

k-factor Spacing

Area distribution Droplet velocity distribution Droplet size distribution Volume distribution

Figure 4.

Different aspects of water sprays used to characterise water distribution.

An overview of measurement techniques and an assessment of uncertainty connected to the different methods of characterisation are presented in this chapter. 4.1 k-factor The nozzle manufacturers characterise the nozzles by the k-factor. The correlation of flow through the nozzle and the pressure drop is characterised by the equation •

Q=k⋅

∆p

The k in the equation is called the k-factor for nozzle, and has a dimension [litre/min bar1/2]. It represents the loss factor in hydraulic calculations, and for low flow velocities, the factor is quite insensitive to pressure differences. This holds for the type of nozzles used in normal deluge systems. The set-up for the measurements is described by ISO 6182-1:1993(E) /5/, which includes piping arrangement, measurement programme and presentation of measured data. The results of a kfactor measurement series then include a presentation of the variation of k-factor with pressure.

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Measurement of k-factor has been carried out by IdF, Teltek and SINTEF. Only the SINTEF measurements were done according to a set-up like the ISO standard. Only single pressure measurements have been carried out. A sketch of this set-up is shown in Figure 5. Measurement uncertainty for the set-up at SINTEF is calculated to ± 0,6% for single point kfactor measurement. 4.2 Area distribution In the tests carried out during the first phase of the Deluge project /1/, different nozzles at different spacing and elevations were used to obtain a pre-described water application density. However, neither the application density nor the area distribution was available from manufacturers. A special apparatus for characterisation of area distribution of water from spray nozzles was designed and constructed by SINTEF. The apparatus consists of 10 concentric circular sectors with equal surface area. The apparatus is divided in two by a wall, making it possible to measure unsymmetrical distribution. The water supply through the nozzle is also measured by a flow meter and a pressure tap. The k-factors of the nozzles were measured with a setup similar to ISO 61821:1993(E). The principle of the ADD apparatus is to collect all the water of a spray at a surface area. The apparatus is water cooled and is constructed to be used in conjunction with a fire source, and to be able to measure the loss of water between the spray nozzle and the collector In the present tests the ADD apparatus is used to characterise area distribution of single nozzles, when no fire interacts with the spray and there is no loss due to evaporation of water. A check on the accuracy of measurements is then possible by comparing the flow measured at the nozzle and at the ADD apparatus. In practise, some loss of water occurs when a spray nozzle is mounted above the collector. Some droplets flow outside the outskirts of the tray and some of the water leaves as very small airborne droplets. The nozzles differ in spray angle, so the height between the nozzle and the collector was varied to match the spray pattern. The height is denoted H in Figure 5.

Figure 5.

Measurements set-up for the area distribution of water from deluge nozzles. The piping and pressure measurement of the k-factor measurements is indicated at the top left in the sketch.

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Figure 6.

The ADD apparatus for measurement of the area distribution of water from deluge nozzles. Each segment of the collecting area has equal surface area.

Tests were carried out with the different nozzles and pressures as described in Table1 and the water flow rate and pressure was measured in a set-up as indicated in Figure 5. Collection of water at a horizontal surface is a challenge, and the fraction of water that is “lost” during the measurement period is shown in Figure 7. The difference between applied and collected water is shown in percentage of applied water. It seems that for similar nozzles, the loss fraction is increasing with increasing pressure. This is coincident with a larger fraction of smaller droplets and higher exit velocity of the droplets.

Lost water [%]

ADD-apparatus measurements

Figure 7.

100 90 80 70 60 50 40 30 20 10 0

26

26

44

44

44

18

41

41

59

80

80

2,6

5,2

2,7

4,9

7,8

2,6

1,9

2,6

2,5

2,1

2,5

“Lost water” during ADD tests. The first number below each bar is the k-factor of the nozzle, the second number is the pressure (bar).

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4.3 Droplet sizes and velocities The droplets sizes measurement technique has developed over the last decennium, from different types of photographic methods to the laser Phase Doppler technique. The first presentations of droplet size distributions were based on a sampling technique where a glass plate covered with Glycerine was passed through a spray and then photographed. This technique certainly presented a photograph that might be studied and analysed, but it is thought that this sampling actually changed the droplet size distribution. The smaller droplets tended to agglomerate and hence disappear in the distribution. It is also believed that the larger droplets may have gone through the same process and formed larger droplets at the collection plate than in the spray. Later photographic techniques are based on high-speed film of droplets in a spray. One method based on automatic image analysis was recently published at the Third International Symposium on Water Mist, /6/. The advantage of this is that calibration with well-known mono-disperse particles is possible. The disadvantage is a problem with the illumination of a certain area of the spray and a time-consuming picture analysis connected to the early versions of the technique. The use of high-frequency light (stroboscope technique) has made it possible to analyse the velocity of droplets as well as the size distribution, but it has been a problem to define a precise plane that is illuminated. Laser light has reduced these problems, and auto-analysis of video pictures has also reduced the time consumption. The photographic techniques have its main limitation in the range of droplet sizes to be detected, as the resolution of the photographic film and especially TV screens is limited. In actual sprays the diameter variation may vary from less than 50 µm up to several millimetres, which imposes a challenge to available systems. A laser-based photographic technique called Particle Image Velocimetry (PIV) measures the velocity vector of particles in a flow-field. This technique was checked out but discarded in this test programme, since the photographic resolution to be used for particle size measurement was too limited. The present most used technique to measure droplet size and droplet velocity of sprays is the Phase Doppler Anemometry, an extension of the Laser Doppler Anemometry. This technique is widely used to characterise droplet size distributions, but has its limitations and practical problems, /7/. Since the tested sprays have different spray angles, it was decided to carry out droplet characterisation at a fixed distance from the orifice. In all the tests at IdF and at Teltek, the distance was 1 m below the orifice. Figure 8 illustrates the problem that will occur if the data from the droplet size measurements is to be extrapolated to a new level. An assumption of droplet trajectory has to be made. The simplest form of extrapolation is to assume straight lines from the orifice to the new level, through the positions of the droplet measurements. This leaves out the gravity influence on the droplets. The further away this extrapolation is used, the larger error occurs.

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Droplet size measurement

Actual Delivered Density Apparatus

Figure 8.

Illustration of the principle of extrapolation of droplet size measurements to a different position.

The Phase –Doppler Anemometry exhibits a new type of measurement technique, as it is based on the refraction of a laser beam inside a droplet. In this technique, droplets passing through a probe volume formed by the intersection of two laser beams scatter light which is imaged by a collection onto a pair of detectors. The droplets act as a lens which magnifies the fringe pattern formed by the intersecting laser beams. The detectors measure the magnified fringe spacing as a temporal phase shift, which is linearly dependent on droplet size. The strength of the system is that it is totally non-intrusive and the number of characterised droplets inside the probe volume is limited of measurement time only. If the measurement time is increased, the number of droplets may become statistically reliable. The uncertainty lies in the software; since some received signals from on “burst” is discarded because it does not fulfil the criteria of a signal from a recognisable droplet. The signal that is counted as a recognised droplet has to be in a range that is expected from a spherical droplet inside the probe volume. A number of signals are discarded because the software can not discriminate if it is a small droplet inside the probe volume or it is a large droplet in the outskirts of the volume. A droplet that is non-spherical may also be discarded. In the reports from IdF two sets of measurements are presented, one by the originally counted droplets and one Probe Volume Corrected (PVC) value. The in-built software of the measurement apparatus is not available for a user, and it is not possible to quantify the uncertainty of the total measurement technique. The test setup with the crossing laser beams as installed in the laboratory of IdF is shown in Figure 9.

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Figure 9.

Phase-Doppler Anemometry used for droplet size and velocity measurements in the IdF laboratories, Magdeburg, Germany.

The droplet velocity is measured at the same position as the droplet sizes. Only the vertical component of the velocity is measured. At distances away from the nozzle opening this velocity component is more and more equal to the total velocity, as gravity forces the droplet into vertical direction. The data from the IdF measurements were presented in tables, as shown in Table 3 and 4. Table 3 gives the Original data, Table 4 gives the corrected PVC-data. The tables give information of: Nr: the test number at IdF, the coordinates of the measurement (x,y) in cm, d10, d20, d30,d32 which are the mean diameters (see Chapter 4.4 for explanation), v10 which is the mean vertical velocity, v_std which is the standard deviation of the mean velocity, vfd which is a Volume Flux Density, Rate which is the number of measured droplets, Zeit which is the time of measurement and finally, Druck which is the pressure (bar).

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Even if the tables give numbers for volume flux density, number of droplets and time of measurement, no meaningful correlation is found when these numbers are presented. The reason for this is not fully explained, but the fact that not all droplets are measured explains the lack of correlation between droplet number, time of measurement and flow rate. If one should expect that the measurements would give an application density or a total flow rate, the technique should assure that all droplets within a certain are were measured.

Table 3.

The format of data tables as obtained from the IdF tests. The example is valid for nozzle HV K26, with the original data.

Tabelle: PDA-Messergebnisse (Originaldaten) für die Düse HVK26 Nr. 90 91 92 93 94 95 96 97 98 99 100 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116 117 118 119 120 121 122 123 124 125 126

x 0 10 20 30 40 50 60 -10 -20 -30 -40 -50 -60 0 0 0 0 0 0 0 0 0 0 0 0 0 0 10 20 30 40 50 60 -10 -20 -30

y 0 0 0 0 0 0 0 0 0 0 0 0 0 0 10 20 30 40 50 60 -10 -20 -30 -40 -50 -60 0 0 0 0 0 0 0 0 0 0

d10 103.3 150.7 185.6 226.5 281.5 286.4 281.4 129.3 159.8 191.2 230.2 264.3 184.9 110.9 119.7 120.3 156.5 226.9 286.8 329.1 106.6 136.7 189.6 236.7 303.7 359.4 104.3 128.7 142.0 175.7 219.7 256.5 292.9 113.0 136.8 166.3

d20 132.7 178.7 210.4 251.0 302.5 306.4 304.2 158.0 181.0 213.2 251.7 287.6 221.5 142.3 154.6 156.1 191.2 260.2 313.9 350.8 141.8 168.8 221.1 266.8 330.3 375.9 132.3 158.7 167.3 199.2 240.0 275.0 308.4 134.2 154.3 187.0

d30 167.4 209.6 234.7 272.3 320.5 323.7 324.6 192.0 204.2 235.5 272.4 307.2 253.0 179.3 194.0 194.5 225.6 288.7 336.8 368.7 180.7 204.6 250.9 293.7 353.2 390.2 163.5 191.0 193.5 221.3 259.7 291.9 321.9 160.4 173.8 207.9

d32 266.3 288.5 292.0 320.7 359.6 361.1 369.5 283.7 259.9 287.5 319.0 350.3 330.0 284.6 305.6 301.9 314.0 355.4 387.6 407.3 293.1 300.7 322.8 355.9 403.8 420.7 250.0 276.7 258.9 273.4 304.3 328.9 350.7 229.0 220.7 256.8

v10 6.6 4.0 3.2 3.0 3.1 3.0 3.2 3.9 3.1 3.0 3.0 3.2 2.1 6.6 6.9 7.4 5.3 4.7 4.2 3.5 7.7 6.4 5.2 4.6 4.2 3.8 10.0 6.1 4.6 3.9 3.6 3.5 3.4 5.1 4.3 4.3

v_std 1.9 2.0 1.7 1.6 1.6 1.6 1.7 2.6 1.5 1.6 1.5 1.6 1.2 1.9 2.1 2.1 2.1 2.3 2.0 1.5 1.9 2.1 2.3 2.2 1.9 1.7 2.9 2.9 2.4 2.2 2.1 2.0 1.7 2.1 1.7 2.0

vfd 0.019 0.023 0.026 0.019 0.018 0.019 0.011 0.006 0.009 0.010 0.010 0.009 0.010 0.018 0.018 0.017 0.026 0.031 0.020 0.010 0.015 0.017 0.022 0.019 0.013 0.006 0.032 0.041 0.037 0.039 0.032 0.025 0.016 0.021 0.022 0.028

Rate 111 63 48 23 12 10 7 22 23 17 12 8 16 85 65 66 63 35 13 5 69 51 38 19 7 2 204 157 134 89 37 19 8 133 105 75

Zeit 219 124 113 98 90 88 91 109 91 123 97 95 98 116 100 94 97 92 90 102 96 94 87 90 90 74 114 113 89 101 96 176 87 106 75 93

Druck 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3

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127 128 129 130 131 132 133 135 136 137 138 139 140 141 142

-40 -50 -60 0 0 0 0 0 0 0 0 0 0 0 0

Table 4.

0 0 0 10 20 30 40 60 50 -10 -20 -30 -40 -50 -60

210.2 254.7 160.3 124.7 124.4 161.1 223.8 338.3 294.4 121.6 128.2 174.7 248.6 308.3 335.9

231.7 274.7 195.1 154.3 154.8 189.5 251.1 357.1 317.3 154.8 158.5 206.3 279.5 326.9 358.5

251.0 292.1 227.6 185.9 187.6 218.4 277.0 373.5 337.0 191.0 189.4 236.2 305.3 342.9 376.8

294.5 330.3 310.0 269.9 275.4 290.1 336.9 408.6 380.0 290.8 270.6 309.5 364.5 377.3 416.5

3.8 3.7 2.2 9.7 8.3 7.4 6.1 4.3 4.9 12.6 8.8 6.6 5.4 5.0 4.3

2.1 2.0 1.5 3.5 3.4 3.2 2.9 2.1 2.3 3.2 3.1 3.2 2.7 2.1 2.3

0.038 0.023 0.016 0.031 0.035 0.040 0.048 0.010 0.030 0.025 0.032 0.049 0.034 0.012 0.004

47 20 33 130 145 99 53 5 19 98 127 100 32 7 2

89 89 90 92 92 94 92 93 93 98 91 92 77 70 74

5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3

The format of data tables as obtained from the IdF tests. The example is valid for nozzle HV K26, with the PVC values.

Tabelle: PDA-Messergebnisse (PVC-Werte) für die Düse HVK26 Nr. 90 91 92 93 94 95 96 97 98 99 100 102 103 104 105 106 107 108 109 110 111 112 113 114 115 116

x 0 10 20 30 40 50 60 -10 -20 -30 -40 -50 -60 0 0 0 0 0 0 0 0 0 0 0 0 0

y 0 0 0 0 0 0 0 0 0 0 0 0 0 0 10 20 30 40 50 60 -10 -20 -30 -40 -50 -60

d10 68.4 103.4 129.7 157.8 208.0 222.0 208.8 90.7 120.3 141.8 169.9 193.2 119.8 74.8 78.6 79.4 105.2 157.4 211.3 264.5 68.3 92.0 129.7 168.8 224.1 305.0

d20 88.7 126.9 154.4 188.9 239.4 243.9 240.3 107.5 135.1 162.0 197.0 229.3 158.7 96.9 102.4 106.7 138.5 198.7 251.5 301.8 91.2 115.7 164.1 206.8 264.6 333.2

d30 117.1 154.6 179.5 216.3 265.2 262.6 267.1 132.5 152.8 183.0 221.5 257.5 195.3 127.6 135.3 141.4 173.6 234.3 283.4 328.5 123.7 146.4 197.3 239.9 296.8 354.5

d32 204.1 229.7 242.7 283.7 325.2 304.2 330.2 201.2 195.5 233.7 280.2 324.9 295.7 221.4 236.5 248.2 273.0 325.6 360.0 389.0 227.3 234.8 285.2 323.0 373.6 401.2

v10 6.6 4.0 3.2 3.0 3.1 3.0 3.2 3.9 3.1 3.0 3.0 3.2 2.1 6.6 6.9 7.4 5.3 4.7 4.2 3.5 7.7 6.4 5.2 4.6 4.2 3.8

v_std 1.9 2.0 1.7 1.6 1.6 1.6 1.7 2.6 1.5 1.6 1.5 1.6 1.2 1.9 2.1 2.1 2.1 2.3 2.0 1.5 1.9 2.1 2.3 2.2 1.9 1.7

vfd 0.028 0.036 0.045 0.031 0.029 0.045 0.017 0.010 0.019 0.020 0.017 0.013 0.013 0.025 0.025 0.023 0.035 0.041 0.027 0.013 0.021 0.025 0.031 0.026 0.018 0.009

Rate 111 63 48 23 12 10 7 22 23 17 12 8 16 85 65 66 63 35 13 5 69 51 38 19 7 2

Zeit 219 124 113 98 90 88 91 109 91 123 97 95 98 116 100 94 97 92 90 102 96 94 87 90 90 74

Druck 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6 2.6

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117 118 119 120 121 122 123 124 125 126 127 128 129 130 131 132 133 135 136 137 138 139 140 141 142

0 10 20 30 40 50 60 -10 -20 -30 -40 -50 -60 0 0 0 0 0 0 0 0 0 0 0 0

0 0 0 0 0 0 0 0 0 0 0 0 0 10 20 30 40 60 50 -10 -20 -30 -40 -50 -60

70.0 84.7 96.6 121.2 170.3 203.3 240.4 81.9 102.2 119.6 163.8 188.6 101.0 83.5 83.0 112.3 156.8 277.8 226.4 80.5 83.9 117.6 177.8 255.7 253.3

90.8 108.8 120.3 147.4 187.6 220.4 255.4 96.8 117.4 139.7 181.5 214.9 128.8 106.5 106.2 138.0 186.2 310.3 261.8 104.4 108.6 150.1 219.4 285.3 293.4

118.0 138.2 146.2 172.4 204.6 236.2 268.6 116.9 134.6 160.6 197.8 237.8 160.8 135.1 135.5 166.6 215.2 334.2 289.6 135.9 137.9 182.6 253.3 307.7 321.7

199.4 222.8 215.9 236.0 243.3 271.1 297.0 170.6 177.1 212.4 234.8 291.1 250.6 217.3 220.6 243.0 287.6 387.6 354.2 230.3 222.4 270.4 337.7 357.9 386.6

10.0 6.1 4.6 3.9 3.6 3.5 3.4 5.1 4.3 4.3 3.8 3.7 2.2 9.7 8.3 7.4 6.1 4.3 4.9 12.6 8.8 6.6 5.4 5.0 4.3

2.9 2.9 2.4 2.2 2.1 2.0 1.7 2.1 1.7 2.0 2.1 2.0 1.5 3.5 3.4 3.2 2.9 2.1 2.3 3.2 3.1 3.2 2.7 2.1 2.3

0.047 0.061 0.058 0.063 0.082 0.067 0.049 0.038 0.044 0.052 0.115 0.041 0.024 0.046 0.052 0.060 0.075 0.014 0.042 0.036 0.047 0.069 0.045 0.016 0.006

204 157 134 89 37 19 8 133 105 75 47 20 33 130 145 99 53 5 19 98 127 100 32 7 2

114 113 89 101 96 176 87 106 75 93 89 89 90 92 92 94 92 93 93 98 91 92 77 70 74

5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3 5.3

The measured data from each test run was captured and saved by special routine defined by SINTEF. An example of the data is shown in Table 5. Only original data were captured this way, which means that numbers are as detected during the test. No Probe Volume Correction was applied during the measurement time. This correction was done after the test run, with no possibility of capturing the total amount of data. The data in Table 5 makes it possible to present the full detailed graphs of droplet size distribution needed for simulation. Accumulated volume diameter, which is the basis for calculation of the Median Volume Diameter, is also shown in Figure 10.

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Table 5 .

The format of data tables as specified by SINTEF. The example is valid for nozzle HV K26 with original data. Only data for the first position (test 90, position x=0, y=0 and the first four data points at position (in cm) x=10, y=0, is shown.

Nozzle

Test No

HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26 HVK26

90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 90 91 91 91 91

PDA-Messergebnisse(Originaldaten), Häufigkeiten mit Klasseneinteilung Lower Upper class Number of droplets x y Class No cliameter diameter [micrometer] [micrometer] 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 10 10 10 10

0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0 0

1 2 3 4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 1 2 3 4

0 20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560 580 600 620 640 660 680 700 720 740 760 0 20 40 60

20 40 60 80 100 120 140 160 180 200 220 240 260 280 300 320 340 360 380 400 420 440 460 480 500 520 540 560 580 600 620 640 660 680 700 720 740 760 780 20 40 60 80

0 3489 4499 4211 3358 2522 1725 1051 672 499 349 309 258 203 159 164 126 121 134 81 90 62 65 48 41 27 18 14 6 12 12 8 1 2 0 5 1 1 0 0 381 593 674

17

Volume mean diameter for position Volume median diameter for position X= 0 Y= 0

Fraction number [%]

HVK 26 2,6

167 358

bar 90

20 15 10 5 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0

0

0

0

0

0

0

0

0

0

0

0

0

Upper class diameter [micrometer]

Fraction volume [%]

HVK 26 2,6

bar 90

7 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0


Accumulated volume [%]

HVK 26 2,6

bar 90

100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

800

900

Mean class diameter

Figure 10.

Example of the full detailed droplet size distribution at one single position (x=0, y=0) of nozzle HVK26, 2,6 bar. The graphs are based on original data from IdF.

All detailed information of droplet distribution is presented in Appendixes to this report, and is available as Excel spreadsheets by SINTEF.

18

4.4 Droplet size terminology From the droplet size distribution, the linear (arithmetic) mean diameter, the surface area mean diameter and the volume mean diameter are calculated, respectively by:

N is the number of measured droplets. In the characterisation of water spray properties, the volume mean diameter is frequently used. As a measure of a water spray, the volume median diameter, which represents a diameter of which half of the mass or volume of the spray, has a diameter that is smaller than that diameter, is frequently used. 4.5 Droplet velocity Droplet velocities are also available as Excel spreadsheets, and an example of such measurements is shown in Figure 11. One can see that the velocities close to the centre show some dependency of exit pressure, but further away from the centre, the velocities are more similar. One anomaly is the high velocity measured at the outskirts of the spray, with a velocity well above the maximum velocity at the centre. No explanation exists for such anomaly, but they occur for all nozzles.

m/s

Velocities of HVK26 14 12 10 8 6 4 2 0 0

100

200

300

400

500

600

700

Distance from centre [mm] Pressure [bar]

Figure 11.

2,6

5,3

Example of vertical velocities measured at various distances from the spray centre, for nozzle HVK26, 2,6 and 5,3 bar.

19

5 CALCULATION OF DROPLET TRAJECTORIES The equation of droplet velocity in a gravity field is governed by the drag force and the gravity term. This is shown in the equation :

md

dVd 1 = − Cd Ad ρ g (Vd − Vg ) ⋅ Vd − Vg + md ⋅ g dt 2

where md : mass of droplet Vd : velocity of droplet dt : time increment Cd : drag coefficient Ad : projected area of droplet ρg : density of gas Vg : velocity of gas g : acceleration of gravity µg : dynamic viscosity of gas The drag coefficient can be expressed by the Reynolds number as shown in the equation:

Cd =

Re =

24 (1 + 0.15 ⋅ Re 0, 687 ) Re

ρ g ⋅ Vd − Vg ⋅ Dd µg

Calculations have been carried out for droplets leaving an orifice vertically downwards, to illustrate the time before terminal velocity is reached. This is shown for 25 and 10 m/s in Figure 12 and 13, respectively.

20

Droplet velocity vs time Droplet velocity,downwards [m/s]

Diameter (micromete r)

30

250 300 500 700 900 1100

25 20 15 10 5 0 0

0,1

0,2

0,3

0,4

0,5

0,6

Time [s]

Figure 12.

Velocity of droplets with different diameter as a function of time. The exit velocity vertically downwards is 25 m/s.

One can see that the velocity is reduced significantly within fractions of a second. The smallest droplets looses their initial velocity almost immediately. Figure 14 shows the travel distance of droplets of different diameters when drag and gravity works. A droplet of 1100 µm (1,1 mm) travels about 4 m within the first second, and a smaller droplet, with diameter 200 µm travels less than 1 m within the first second. To quantify the density of water in a specified volume, one has to consider the supply of droplets, the different travel patterns and time and finally the droplets that are hitting surfaces, either the floor, walls or other objects. The flow inside a volume, either induced by ventilation, wind or a fire, or induced by the spray nozzles themselves introduces more complex travel patterns than gravity-driven transport only, and this also have to be considered.

21

Droplet velocity vs time Droplet velocity,downwards [m/s]


12

150 200 250 300 500 700 900 1100

10 8 6 4 2 0 0

0,2

0,4

0,6

0,8

1

1,2

1,4

Time [s]

Figure 13.

Velocity of droplets with different diameter as a function of time. The exit velocity vertically downwards is 10 m/s.

Travel distance of droplet Exit velocity vertically downwards

10 m/s

m


10,00

200

8,00

250 300

6,00

500

4,00

700

2,00

900

0,00

1100 0

0,5

1

1,5

2

2,5

3

Time [sec] Figure 14.

Travel distance of droplets with different diameter as a function of time. The exit velocity vertically downwards is 10 m/s.

22

6 RESULTS 6.1 k-factor for the nozzles The tested nozzles delivered by NORFASS were all well within the acceptance criterion recommended in the standard for characterisation of such nozzles /5/. This is shown in Figure 15, where the red line shows the match exactly for the nominal k-factor given by the manufacturer, and the two different markers represent tests carried out by SINTEF and IdF, respectively. One single measurement carried out by TelTek is also included, for nozzle HV K44.

Measured k-factor

100 80 60 40 20 0 0

20

40

60

80

100

Nominal k-factor SINTEF measurements IdF measurements

Figure15.

Manufactureres k-factor Tel-Tek measurement

Measured k-factors [litre/min bar1/2] for the nozzles .

23

6.2 Exit velocity The nozzles used in the SINTEF tests were denoted Medium or High velocity nozzles. Figure 16 shows the calculated exit velocities based on average velocity at the orifice, not measured values. The velocities are calculated at the minimum and maximum recommended operating pressure. 25

Exit velocity [m/s]

20 HV min HV max MV min MV max

15 10

5

0 0

20

40

60

80

100

k-factor

Figure 16.

Calculated exit velocities for the nozzles at minimum and maximum recommended pressure.

No significant difference in exit velocity from the nozzle orifice seems to exist between the Highand Medium-velocity nozzles. However, the main difference is the construction of the nozzles. The Medium-velocity nozzles have a deflector plate that spreads the water and lowers the velocity in downwards direction, and the droplet will tend to fall freely shortly after leaving the nozzle. Table 6.

Velocity distribution 1 m below nozzle MVK41, measured by TelTek.

24

Table 7.

Velocity distribution 1 m below nozzle HVK44, measured by TelTek.

Table 6 and 7 show the measured droplet velocity 1 m below the nozzles MVK41 and HVK44, respectively. The High-velocity nozzle exhibits velocities above 5 m/s and above 25 m/s at maximum, with 8 bar pressure and near the centre. Higher pressure leads to higher velocities. The Medium-velocity nozzle exhibits velocities in the order of 1-2 m/s, with some maximum velocities of about 6 m/s at the outskirts of the spray.

25

6.3 Droplet sizes measured by two institutes

Figure 17.

Mean diameter profile as measured by TelTek, for nozzle HVK44 at 2,4 bar. HVK44 pvc 500 400 300 200 100 0 -600

-450

-300

-150

d30pvc

Figure 18.

0

150

d20pvc

300

450

600

d10pvc

Mean diameter profile as measured by IdF, for nozzle HVK44 at 2,4 bar ,pvcvalues. HVK44 ori 500 400 300 200 100 0 -600

-450

-300

-150 d10ori

Figure 19.

0 d20ori

150

300

450

600

d30ori

Mean diameter profile as measured by IdF, for nozzle HVK44 at 2,4 bar, orivalues.

26

Comparison of the measurements of the same parameters at two different institutes shows both similarities and differences. Figures 17-19 show mean diameter profiles for the nozzle HVK44 at 2,4 bar pressure. We first look at volume mean diameters variation with distance from centre. The TelTek measurement shows diameters less than 150 µm at the centre, as the two measurement from IdF shows about 200 µm and 300 µm, pvc- and ori-values, respectively. At a distance 400-500 mm from the centre, the TelTek measurements are somewhat unsymmetrical, with diameters of 400 µm on one side, and 300 µm at the other side. The IdF measurements show diameters from about 350 to 450 µm with the pvc-values, and from about 400 to 500 µm with the ori-values. For this case, the pvc-values of IdF seem more similar to the TelTek values.

Figure 20.

Mean diameter profile as measured by TelTek, for nozzle HVK44 at 5 bar.

HVK44 pvc 500 400 300 200 100 0 -600

-450

-300

-150

d30pvc

Figure 21.

0

d20pvc

150

300

450

600

d10pvc

Mean diameter profile as measured by IdF, for nozzle HVK44 at 5 bar, pvc-values.

27

HVK44 ori 500 400 300 200 100 0 -600

-450

-300

-150 d10ori

Figure 22.

0 d20ori

150

300

450

600

d30ori

Mean diameter profile as measured by IdF, for nozzle HVK44 at 5 bar, ori-values.

Figures 20-22 show mean diameter profiles for the nozzle HVK44 at 5 bar pressure. We again first look at volume mean diameters variation with distance from centre .The TelTek measurement shows diameters larger than 300 µm at the centre, as the two measurement from IdF shows about 200 µm and 300 µm, pvc- and ori-values, respectively. At a distance 400-500 mm from the centre, the TelTek measurements again are somewhat unsymmetrical, with diameters of 450 µm on one side, and 300 µm at the other side. The IdF measurements show diameters from about 250 to 350 µm with the pvc-values, and from about 300 to 400 µm with the ori-values. For this case, the total shape and numbers of the ori-values of IdF seem more similar to the TelTek values. The TelTek measurements are given in detail in Tables 8 – 10. Table 8.

Mean and Median, Max and Minimum diameters measured by TelTek, nozzle HVK44, at 2,6 bar pressure.

28

Table 9.

Mean and Median, Max and Minimum diameters measured by TelTek, nozzle HVK44, at 5 bar pressure.

Table 10.

Mean and Median, Max and Minimum diameters measured by TelTek, nozzle HVK44, at 7,8 bar pressure.

29

6.4 Individual nozzle characteristics 6.4.1

Nozzle HV K26

Figure 23.

Nozzle HV K26.

Figure 24.

Spray pattern of HV K26 at 2,6 bar.

The nominal spray angle of this nozzle is 80 - 90°.

30

Figure 25. 6.4.1.1

Spray pattern of HV K26 at 5,3 bar.

Application density HV K26 HV K26

Height

1,87

m

Pressure

2,6

bar

9,0

Water application [litre/m2 min]

8,0 7,0 6,0 5,0 4,0 3,0 2,0 1,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500

Distance from centre [mm] A

Figure 26.

B

Average

Measured application density by ADD apparatus for nozzle HVK26, height 1,87 m, 2,6 bar.

31

HV K26

Height 1,87

Pressure 5,3

m

bar

20,0


18,0 16,0 14,0 12,0 10,0 8,0 6,0 4,0 2,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure27.

B

Average

Measured application density by ADD apparatus for nozzle HV K26, height 1,87 m, 5,3 bar. Variance of application density Application density [l/m2 min]

HV K26

1,87

m height

20 15 2,6 bar 5,3 bar

10 5 0 0

250

500

750

1000

1250

1500

Distance from centre [mm]

Figure28.

Measured application density by ADD apparatus for nozzle HV K26.

32

HVK26 1 m height 12

Velocity [m/s]

10 8 2,6 bar

6

5,3 bar

4 2 0 0

100

200

300

400

500

600


Figure29. 6.4.1.2

Measured average droplet velocity by PDA for nozzle HV K26.

Nozzle HV K26 : Droplet size distribution

Figure 30.

Droplet size distribution of nozzle HV K26 at 2,6 bar. The values of the droplet sizes represent the D10 pvc diameter (Number of droplets). The diameter (d) is in micrometer, the coordinates (x,y) in cm. Measurements with PDA-technique by IdF.

33

Figure 31.

Droplet size distribution of nozzle HV K26 at 5,3 bar. The values of the droplet sizes represent the D10 pvc diameter (Number of droplets). The diameter (d) is in micrometer, the coordinates (x,y) in cm. Measurements with PDA-technique by IdF.

HVK26 - 2,6 bar Distance from centre [mm] 0

0,7 Number fraction

0,6 0,5

100

0,4

200

0,3

300

0,2

400

0,1

500

0

600 0

200

400

600

800

1000

Droplet diameter [micrometer]

Figure 32.

Droplet size distribution of nozzle HV K26 at 2,6 bar. The graph presents the number fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data).

34

HVK26 - 2,6 bar Distance from centre [mm]

0,7 Volume fraction

0,6 0,5

0

0,4

100 200

0,3

300

0,2

400

0,1

500

0

600 0

200

400

600

800

1000


Figure 33.

Droplet size distribution of nozzle HV K26 at 2,6 bar. The graph presents the volume fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data). HVK26 - 5,3 bar Distance from centre [mm] 0

0,7 Number fraction

0,6 0,5

100

0,4

200

0,3

300

0,2

400

0,1

500

0

600 0

200

400

600

800

1000


Figure 34.


35

HVK26 - 5,3 bar Distance from centre [mm] 0

0,7 Volume fraction

0,6 0,5

100

0,4

200

0,3

300

0,2

400

0,1

500

0

600 0

200

400

600

800

1000


Figure 35.

Droplet size distribution of nozzle HV K26 at 5,3 bar. The graph presents the volume fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data).

36

Volume mean diameter for position Volume median diameter for position X= -40 Y= 0

Fraction number [%]

HVK 26 2,6

272 331

bar 100

14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK 26 2,6

bar 100

8 7 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0



HVK 26 2,6

bar 100

100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

800

900

Mean class diameter

Figure 36

Example of individual position measured droplet size distribution of nozzle HVK 26 at 2,6 bar. The graph presents the volume fraction of the droplet sizes at one single distance from the centre of the spray, denoted position 100. x =-4 0, y = 0 means distance from centre in two directions, in (cm). Measurements with PDAtechnique by IdF, original data without correction (ori-data).

37

6.4.2

Nozzle HVK44

Figure 37.

Nozzle HV K44.

Figure 38.

Spray pattern of HV K44 at 2,7 bar pressure, 3,6 m height.

38

Figure 39.

Spray pattern of HV K44 at 7,8 bar pressure, 5,7 m height.

39

6.4.2.1

Application density HV K44 HV K44

Height

3,6

Pressure 2,7

m

bar

45,0 Average application density 8,0 l/m2 min


40,0 35,0 30,0 25,0 20,0 15,0 10,0 5,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 40.

B

Average

Measured application density by ADD apparatus for nozzle HV K44, height 3,6 m, 2,7 bar.

HV K44

Height

3,6

Pressure 4,9

m

bar

45,0 Average application density 10,0 l/m2 min


40,0 35,0 30,0 25,0 20,0 15,0 10,0 5,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 41.

B

Average

Measured application density by ADD apparatus for nozzle HV K44, height 3,6 m, 4,9 bar.

40

HV K44

Height

5,7

Pressure 7,8

m

bar

45,0


40,0 35,0 30,0 25,0 20,0 15,0 10,0 5,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 42.

B

Average

Measured application density by ADD apparatus for nozzle HV K44, height 5,7 m, 7,8 bar. Variance of application density Application density [l/m2 min]

HV K44

3,6 - 5,7

m height

50 40 2,7 bar 4,9 bar 7,8 bar

30 20 10 0 0

250

500

750

1000

1250

1500


Figure43.

Measured application density by ADD apparatus for nozzle HV K44.

41

HVK44

N7 - HV K44

Velocity [m/s]

30 25 2,7 bar

20

4,9 bar 15

7,8 bar

10 5 0 0

100

200

300

400

500

600

Mean velocity [m/s]

35

35 30 25 20 15 10 5 0 -450

N7 2,4 bar N7 5 bar N7 8 bar

-300 -150

Figure44.

6.4.2.2

0

150

300

450

Radial position [mm]


Measured average droplet velocity for nozzle HV K44. The graph to the left is measured by by PDA tecnique, by IdF, and the graph to the left is measured by LD technique by TelTelk.

Droplet size distribution HVK44


0,7 Number fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400 500

0 0

200

400

600

800

1000


Figure 45.


42


0,7 Volume fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400 500

0 0

200

400

600

800

1000


Figure 46.

Droplet size distribution of nozzle HV K44 at 2,7 bar. The graph presents the volume fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data). HVK44 - 4,9 bar Distance from centre [mm]

0,7 Number fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400 500

0 0

200

400

600

800

1000


Figure 47.


43


0,7 Volume fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400 500

0 0

200

400

600

800

1000


Figure 48.



Number fraction

0,7 0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400 500

0 0

200

400

600

800

1000


Figure 49.


44


0,7 Volume fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400 500

0 0

200

400

600

800

1000


Figure 50.


45

6.4.3

Nozzle MVK18

Figure 51.

Nozzle MV K18.

Figure 52.

Spray pattern of nozzle MVK18 at 2,6 bar pressure.

46

6.4.3.1

Application density MV K18

MV K18

Height

1,02

m

2,6

Pressure

bar

8,0


7,0 6,0 5,0 4,0 3,0 2,0 1,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 53.

B

Average

Measured application density by ADD apparatus for nozzle MV K18, height 1,02 m, 2,6 bar. Variance of application density Application density [l/m2 min]

MV K18 7 6 5 4 3 2 1 0

2,6 bar

0

250

500

750

1000

1250

1500


Figure54.

Measured application density by ADD apparatus for nozzle MV K18.

47

MV K18 12 10

m/s

8 6

2,6 bar

4 2 0 0

200

400

600

800

1000

1200


Figure 55.

Measured mean droplet velocity at different distances from centre, for nozzle MV K18, at height 1 m. Measured by PDA technique by IdF.

48

6.4.3.2

Droplet size distribution MV K18

MVK18 - 2,6 bar Distance from centre [mm]

0,7 Number fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 56.

Droplet size distribution of nozzle MV K18 at 2,6 bar. The graph presents the number fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data). MVK18 - 2,6 bar Distance from centre [mm]

0,7 Volume fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 57.

Droplet size distribution of nozzle MV K18 at 2,6 bar. The graph presents the volume fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data).

49

6.4.4

Nozzle MVK41

Figure 58.

Nozzle MV K41.

Figure 59.

Spray pattern of MV K41 at 2,6 bar pressure.

50

6.4.4.1

Application density MV K41 MV K41

Height 1,87

Pressure 1,9

m

bar

10,0


9,0 8,0 7,0 6,0 5,0 4,0 3,0 2,0 1,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 60.

B

Average

Measured application density by ADD apparatus for nozzle MV K41, height 1,87 m, 1,9 bar. MV K41

Height 1,87

Pressure 2,6

m

bar

10,0


9,0 8,0 7,0 6,0 5,0 4,0 3,0 2,0 1,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 61.

B

Average

Measured application density by ADD apparatus for nozzle MV K41, height 1,87 m, 2,6 bar.

51

Variance of application density Application density [l/m2 min]

MV K41 8 7 6 5 4 3 2 1 0

1,9 bar 2,6 bar

0

250

500

750

1000

1250

1500


Figure 62.

Measured application density by ADD apparatus for nozzle MV K41, at height 1,87 m.

N1 - MV K41

Mean velocity [m/s]

35 30 25 20

N1 2 bar

15

N1 7 bar

10 5 0 -800 -600 -400 -200

0

200

400

600

800


Figure 63.

Measured velocity profile for nozzle MV K41, with LD technique, by TelTek.

52

6.4.4.2



0,7 Number fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 64.


0,7 Volume fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 65.


53

MVK41 - 2,6bar Distance from centre [mm] 0

0,7 Number fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 66.

Droplet size distribution of nozzle MV K41 at 2,6 bar. The graph presents the number fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data). MVK41 - 2,6bar Distance from centre [mm] 0

0,7 Volume fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 67.


54

6.4.5

Nozzle MVK59

Figure 68.

Nozzle MV K59.

Figure 69.

Spray pattern of MVK59 at 2,5 bar pressure

55

6.4.5.1


Height 1,27

Pressure 2,5

m

bar

16,0


14,0 12,0 10,0 8,0 6,0 4,0 2,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 70.

B

Average

Measured application density by ADD apparatus for nozzle MV K59, height 1,27 m and at pressure 2,5 bar. Variance of application density Application density [l/m2 min]

MV K59

1,27 m height

14 12 10 8 6 4 2 0

2,5 bar

0

250

500

750

1000

1250

1500


Figure 71.

Measured application density by ADD apparatus for nozzle MV K59.

Droplet size measurements are not carried out for this nozzle.

56

6.4.6

Nozzle MVK80

Figure 72.

Nozzle MV K80.

Figure73.

Spray pattern of nozzle MV K80 at 2,1 bar pressure.

57

6.4.6.1


Height

1,1

m

Pressure

2,1

bar

18,0


16,0 14,0 12,0 10,0 8,0 6,0 4,0 2,0 0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 74.

B

Average

Measured application density by ADD apparatus for nozzle MV K80, height 1,1 m and at pressure 2,1 bar.

MV K80

Height

1,1

Pressure 2,5

m

bar

30,0


25,0

20,0

15,0

10,0

5,0

0,0 475

670

820

950

1060

1160

1255

1340

1425

1500


Figure 75.

B

Average

Measured application density by ADD apparatus for nozzle MV K80, height 1,1 m and at pressure 2,5 bar.

58

Variance of application density Application density [l/m2 min]

MV K80 20 15 2,1 bar 2,5 bar

10 5 0 0

250

500

750

1000

1250

1500


Figure 76.

Measured application density by ADD apparatus for nozzle MV K80, at height 1,1 m. MV K80 12

Mean velocity (m/s)

10 8 2,1 bar 2,5 bar

6 4 2 0 0

200

400

600

800

1000

1200

Distance from centre (mm)

Figure 77.

Measured mean droplet velocity at different distances from centre, for nozzle MV K80, at height 1 m. Measured by PDA technique by IdF.

59

6.4.6.2



0,7 Number fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 78.


0,7 Volume fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 79.


60

MVK80 - 2,5bar Distance from centre [mm] 0

0,7 Number fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 80.

Droplet size distribution of nozzle MV K80 at 2,5 bar. The graph presents the number fraction of the droplet sizes at different distances from the centre of the spray. Measurements with PDA-technique by IdF, original data without correction (ori-data). MVK80 - 2,5bar Distance from centre [mm] 0

0,7 Volume fraction

0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600

800

1000


Figure 81.


61

7 EVALUATION The evaluation of the measurement of spray characteristics is divided into two parts. The first part evaluates the different measurement techniques, as the second part covers the differences of the tested nozzles. 7.1 Measurement techniques Since none of the existing techniques for characterisation of sprays contain a full scheme to quantify both applied density and droplet sizes and velocities, it is still necessary to carry out two different tests to fully characterise what is needed. The tests of k-factor of the nozzles are carried out both by SINTTEF NBL and by TelTek, for some of the nozzles. The k-factor ids the correlation of water flow rate as a function of nozzle pressure. The measurement set-up at SINTEF NBL is according to the ISO standard 6182-1, /5/. The measured k-factor for the tested nozzles is in accordance with the minimum requirements of the ISO standard. Deviations in measurement technique and test set-up may introduce errors in such measurements, and it is recommended to use the ISO method. The ADD-apparatus constructed by SINTF NBL and used in the characterisation of area density distribution has some features which is favourable to use in single nozzle characterisation. The problem of collecting small droplets that follow air flow reduces the accuracy of such measurements, and a fraction of 20-40% is “lost”. However, this problem is seen with all types of measurements that collect water at floor level, since air flow is directed away from the collectors when a fixed barrier is reached. In measurements where all water is collected, the inaccuracy is related to the distribution. The measurement of droplet characteristics is based on Laser Doppler and Phase Doppler anemometry. This type of measurement is fully automatic, and a software package from the manufacturer transfers the measured signals to droplet sizes and velocities. The measurements converge to a fixed distribution when a sufficiently large number of droplets have been identified. The calculation procedure influences the resulting droplet size distribution. For the IdF measurement equipment, the original measured data was captured by the computer and kept for later analysis, as a special arrangement for this project. The data were continuously processed and stored as so-called pvc-values (probe volume correction). To be able to compare and utilise droplet size measurements, it is of great importance to use the correct denotations of measured values. For instance, the mean diameter is different from median diameter, and it is a great difference between number based, surface area based and volume based distributions. The most common and recommended characteristic is the Median Volume Diameter, MVD, which is the cumulative volume median diameter. Two different laboratories have measured similar nozzles, and some discrepancies are seen in the measured data. With one High-velocity nozzle HV K44, the measured MVD at different locations from the spray centre. The TelTek measurement shows diameters larger than 300 µm at the centre, as the two measurements from IdF shows about 200 µm and 300 µm, pvc- and ori-values, respectively.

62

At a distance 400-500 mm from the centre, the TelTek measurements again are somewhat unsymmetrical, with diameters of 450 µm on one side, and 300 µm at the other side. The IdF measurements show diameters from about 250 to 350 µm with the pvc-values, and from about 300 to 400 µm with the ori-values. For this case, the total shape and numbers of the ori-values of IdF seem more similar to the TelTek values. The characterisation of droplet sizes seems to be sensitive to location of the probes, and probably also to the algorithm use to judge the goodness of each single “burst”. A “burst” is the electrical signal connected to the detection of one single droplet, and the algorithm decides if the “burst” represent a real droplet or not. Droplets deviating from spherical may give signals that make the algorithm vote the droplet out, and if there are many droplets of this type, the presented size distribution may be unrealistic. Imaging techniques may treat this differently.

7.2 Differences between nozzles Figure 82 shows a comparison between high-velocity and medium-velocity nozzles, with regard to distribution of droplet sizes at different distances from the spray centre. The main impression is that the MV-nozzles show a larger variation of droplet sizes along the diameter, with a surplus of smaller droplets in the central part of the spray, and larger droplets further away from the centre. Apart from that, the same droplet sizes are present in both medium- and high-velocity nozzles.

High-velocity nozzles

Medium-velocity nozzles MVK18 - 2,6 bar

HVK26 - 2,6 bar 0,7 Volume fraction

0,6 0,5

100

0,4

200

0,3

300

0,2

400

0,1

0,6

200

400

600

800

100

0,4

300

0,3

500

0,2

700 900

0

600 0

0,5

0,1

500

0


0,7 Volume fraction

Distance from centre [mm] 0

0

1000

200

Volume fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400

800


0,6 0,5

100

0,4

300

0,3

500

0,2

700

0,1

500

0 600

900

0 0

1000

200

HVK26 - 5,3 bar

0,5

100

0,4

200

0,3

300

0,2

400

0,1

500

0

600 600


800

1000

800

1000


0,7 0,6 Volume fraction

Volume fraction

0,6

400

600

MVK41 - 1,9 bar Distance from centre [mm] 0

0,7

200

400



0

1000

0,7 Volume fraction


400

800

MVK41 - 2,6bar

HVK44 - 2,7 bar 0,7

200

600



0

400

0,5 100

0,4

300

0,3

500

0,2

700

0,1

900

0 0

200

400

600


800

1000

63

HVK44 - 4,9 bar

MVK80 - 2,1 bar

0,7 Volume fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1

400

0,6

0

200

400

600

800

0,5 100

0,4

300

0,3

500

0,2

700

0,1

500

0


0,7 Volume fraction


900

0 0

1000

200

400

HVK44 - 7,8 bar

Volume fraction

0,6 0,5

0

0,4

100

0,3

200

0,2

300

0,1 0 600

800


0,7 0,6 Volume fraction

0,7

400

0,5

100

0,4

300

0,3

500

0,2

400

0,1

500

0

700 900 0

1000

200

400

600

800

1000



Figure 82.

1000

MVK80 - 2,5bar Distance from centre [mm]

200

800



0

600

A collection of volume fractions of droplets of different sizes measured at different distances from the spray centre, with varied nozzle pressure. High-velocity nozzles are shown in the left column, as medium-velocity nozzles are shown in the righthand column.

Figure 83 shows mean droplet velocities measured for the different nozzles, as a function of distance from spray centre. These velocities are measured 1 m below the nozzle, and one can clearly see the difference between the high- and the medium-velocity nozzles.


Medium-velocity nozzles

HVK26 1 m height

MV K18

12

12 10

8

8

2,6 bar

6

5,3 bar

4

m/s

Velocity [m/s]

10

6

2,6 bar

4

2

2

0 0

100

200

300

400

500

600


0 0

200

400

600

800

1000

1200


#

MV K80 12

Mean velocity (m/s)

10 8 2,1 bar 2,5 bar

6 4 2 0 0

200

400

600

800

Distance from centre (mm)

1000

1200

64

N1 - MV K41

35 30 25 20 15 10 5 0 -450

35

N7 2,4 bar N7 5 bar N7 8 bar

-300 -150

0

150

300

Mean velocity [m/s]

Mean velocity [m/s]

N7 - HV K44

30 25 20

N1 2 bar

15

N1 7 bar

10 5 0

450

-800 -600 -400 -200


Figure 83.

400

600

800

Droplet velocities measured at different distances from the spray centre, with varied nozzle pressure. High-velocity nozzles are shown in the left column, as medium-velocity nozzles are shown in the right-hand column. Medium-velocity nozzles Variance of application density

Variance of application density 1,87

MV K41

m height

20 15 2,6 bar 5,3 bar

10 5

Application density [l/m2 min]

HV K26 Application density [l/m2 min]

200



8 7 6 5 4 3 2 1 0

0

1,9 bar 2,6 bar

0

0

0

250

500

750

1000

1250

250

1500

500

750

1000

1250

1500



Variance of application density

Variance of application density 3,6 - 5,7

MV K80

m height

40 2,7 bar 4,9 bar 7,8 bar

30 20 10



HV K44 50

20 15 2,1 bar 2,5 bar

10 5 0 0

0 0

250

500

750

1000

1250

1500

250

500

750

1000

1250

1500



Figure 84.

Water application density measured at different distances from the spray centre, with varied nozzle pressure. High-velocity nozzles are shown in the left column, as medium-velocity nozzles are shown in the right-hand column.

Figure 84 shows water application densities measured for the different nozzles, as a function of distance from spray centre. The high-velocity nozzles have a higher application density at the centre, and the density increases there as pressure is increased. It has to be noted that the nozzles are tested for higher pressures than design pressure, as shown in Chapter 3. The medium-velocity nozzles show a more uniform application density over the cover area, even with higher density at a distance away from the centre.

65

8 REFERENCES 1.

Are W. Brandt, Kristen Opstad and Ragnar Wighus: Documentation of active fire fighting systems as a fire safety design parameter - Tests with different deluge nozzles in 3 m diameter rig. SINTEF report STF22 F99845, Trondheim 2000-01-10.

2.

Kristen Opstad, Ragnar Wighus and Are Brandt: Documentation of active fire fighting systems as a fire safety design parameter - Tests in large-scale 3350m3 SINTEF report NBL10 F01104, Trondheim 2001-11-08.

3.

Vidar Mathiesen and Britt Halvorsen: Laser Measurements of Droplet Size and –Velocity. Tel-Tek report number 510390-1, Porsgrunn, September 2000.

4.

H. Starke, F. Wienecke: Bestimmen der Tropfenverteilung für Wassernebeldüsen (Typen HV und MV). Institut der Feuerwehr , Sachsen-Anhalt (IdF LSA), Heyrothsberge, Germany, 2002.

5.

ISO 6182-1, First Edition, 1993-07-01. “Fire protection – Automatic sprinkler systems – Part 1: Requirements and test methods for sprinklers”. Reference Number: ISO 61821:1993(E).

6.

Tsai, R.F., Lee, C.K., Liang, B.C.: The Use of a Visual System to Quantify Geometric characteristics of Sprays. The 3rd International Water Mist Conference, Madrid, Spain, September 2003. International Water Mist Association. IWMA, http://www.iwma.de/

7.

P.A.Starkey, D.G. Talley and W.D. Bacalao: Phase Doppler Measurements in Dense Sprays, ILASS-Americas ’98 – Sacramento, CA 17-20 May 1998.

8.

ASTM E 799-92: Standard Practice for Determining Data Criteria and Processing for Liquid Drop Size Analysis,

66

9 APPENDIX A.1 NOZZLE HVK26 - 2,6 bar DROPLET SIZE DISTRIBUTION FOR NOZZLES ORIGINALLY MEASURED DATA BY PDA at IdF, reduced and presented by SINTEF

67

Volume mean diameter for position Volume median diameter for position

167 350

HVK26 2,6 bar x=0 y=0 (90)

Fraction number [%]

20 15 10 5 0 20

80

140 200 260 320 380 440 500 560 620 680 740 Upper class diameter [micrometer]

HVK26 2,6 bar x=0 y=0 (90)

Fraction volume [%]

7 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740 Upper class diameter [micrometer]


HVK26 2,6 bar x=0 y=0 (90) 100 90 80 70 60 50 40 30 20 10 0 20

80


68


210 350

HVK26 2,6 bar x=10 y=0 (91)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


HVK26 2,6 bar x=10 y=0 (91)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 2,6 bar x=10 y=0 (91) 100 90 80 70 60 50 40 30 20 10 0 20

80


69


235 330

HVK26 2,6 bar x=20 y=0 (92)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


HVK26 2,6 bar x=20 y=0 (92)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=20 y=0 (92) 100 90 80 70 60 50 40 30 20 10 0 20

80


70


273 330

HVK26 2,6 bar x=30 y=0 (93)

Fraction number [%]

12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=30 y=0 (93) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=30 y=0 (93) 100 90 80 70 60 50 40 30 20 10 0 20

80


71


320 370

HVK26 2,6 bar x=40 y=0 (94)

Fraction number [%]

10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=40 y=0 (94) 9 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=40 y=0 (94) 100 90 80 70 60 50 40 30 20 10 0 20

80


72


324 370

HVK26 2,6 bar x=50 y=0 (95)

Fraction number [%]

12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=50 y=0 (95) 9 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=50 y=0 (95) 100 90 80 70 60 50 40 30 20 10 0 20

80


73


325 390

HVK26 2,6 bar x=60 y=0 (96)

Fraction number [%]

12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=60 y=0 (96) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=60 y=0 (96) 100 90 80 70 60 50 40 30 20 10 0 20

80


74


192 350

HVK26 2,6 bar x=-10 y=0 (97)

Fraction number [%]

25 20 15 10 5 0 20

80


HVK26 2,6 bar x=-10 y=0 (97)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=-10 y=0 (97) 100 90 80 70 60 50 40 30 20 10 0 20

80


75


206 290

HVK26 2,6 bar x=-20 y=0 (98)

Fraction number [%]

20 15 10 5 0 20

80


HVK26 2,6 bar x=-20 y=0 (98)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=-20 y=0 (98) 100 90 80 70 60 50 40 30 20 10 0 20

80


76


237 310

Fraction number [%]

HVK26 2,6 bar x=-30 y=0 (99) 16 14 12 10 8 6 4 2 0 20

80


HVK26 2,6 bar x=-30 y=0 (99)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=-30 y=0 (99) 100 90 80 70 60 50 40 30 20 10 0 20

80


77


228 330

HVK26 2,6 bar x=-40 y=0 (100)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 2,6 bar x=-40 y=0 (100)

Fraction volume [%]

6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 Upper class diameter [micrometer]


HVK26 2,6 bar x=-40 y=0 (100) 100 90 80 70 60 50 40 30 20 10 0 20

80


78


320 390

HVK26 2,6 bar x=-50 y=0 (102)

Fraction number [%]

10 8 6 4 2 0 20

80


HVK26 2,6 bar x=-50 y=0 (102)

Fraction volume [%]

10 8 6 4 2 0 20



HVK26 2,6 bar x=-50 y=0 (102) 100 90 80 70 60 50 40 30 20 10 0 20

80


79


256 370

HVK26 2,6 bar x=-60 y=0 (103)

Fraction number [%]

10 8 6 4 2 0 20

80


HVK26 2,6 bar x=-60 y=0 (103)

Fraction volume [%]

10 8 6 4 2 0 20



HVK26 2,6 bar x=-60 y=0 (103) 100 90 80 70 60 50 40 30 20 10 0 20

80


80


180 370

HVK26 2,6 bar x=0 y=0 (104)

Fraction number [%]

20 15 10 5 0 20

80


HVK26 2,6 bar x=0 y=0 (104)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=0 (104) 100 90 80 70 60 50 40 30 20 10 0 20

80


81


194 370

HVK26 2,6 bar x=0 y=10 (105)

Fraction number [%]

20 15 10 5 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=10 (105) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=10 (105) 100 90 80 70 60 50 40 30 20 10 0 20

80


82


194 370

Fraction number [%]

HVK26 2,6 bar x=0 y=20 (106) 18 16 14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=20 (106) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=20 (106) 100 90 80 70 60 50 40 30 20 10 0 20

80


83


226 370

HVK26 2,6 bar x=0 y=30 (107)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 2,6 bar x=0 y=30 (107)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=30 (107) 100 90 80 70 60 50 40 30 20 10 0 20

80


84


289 390

Fraction number [%]

HVK26 2,6 bar x=0 y=40 (108) 9 8 7 6 5 4 3 2 1 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=40 (108) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=40 (108) 100 90 80 70 60 50 40 30 20 10 0 20

80


85


337 390

Fraction number [%]

HVK26 2,6 bar x=0 y=50 (109) 8 7 6 5 4 3 2 1 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=50 (109) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=50 (109) 100 90 80 70 60 50 40 30 20 10 0 20

80


86


370 410

HVK26 2,6 bar x=0 y=60 (110)

Fraction number [%]

10 8 6 4 2 0 20

80


HVK26 2,6 bar x=0 y=60 (110)

Fraction volume [%]

12 10 8 6 4 2 0 20



HVK26 2,6 bar x=0 y=60 (110) 100 90 80 70 60 50 40 30 20 10 0 20

80


87


181 350

HVK26 2,6 bar x=0 y=-10 (111)

Fraction number [%]

25 20 15 10 5 0 20

80


HVK26 2,6 bar x=0 y=-10 (111)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=-10 (111) 100 90 80 70 60 50 40 30 20 10 0 20

80


88


204 370

Fraction number [%]

HVK26 2,6 bar x=0 y=-20 (112) 16 14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=-20 (112) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=-20 (112) 100 90 80 70 60 50 40 30 20 10 0 20

80


89


251 370

HVK26 2,6 bar x=0 y=-30 (113)

Fraction number [%]

12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=-30 (113) 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=-30 (113) 100 90 80 70 60 50 40 30 20 10 0 20

80


90


294 370

Fraction number [%]

HVK26 2,6 bar x=0 y=-40 (114) 9 8 7 6 5 4 3 2 1 0 20

80


HVK26 2,6 bar x=0 y=-40 (114)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=-40 (114) 100 90 80 70 60 50 40 30 20 10 0 20

80


91


354 410

Fraction number [%]

HVK26 2,6 bar x=0 y=-50 (115) 9 8 7 6 5 4 3 2 1 0 20

80


Fraction volume [%]

HVK26 2,6 bar x=0 y=-50 (115) 9 8 7 6 5 4 3 2 1 0 20



HVK26 2,6 bar x=0 y=-50 (115) 100 90 80 70 60 50 40 30 20 10 0 20

80


92


405 430

HVK26 2,6 bar x=0 y=-60 (116)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 2,6 bar x=0 y=-60 (116)

Fraction volume [%]

10 8 6 4 2 0 20



HVK26 2,6 bar x=0 y=-60 (116) 100 90 80 70 60 50 40 30 20 10 0 20

80


93

10 APPENDIX A.2 NOZZLE HVK 26 – 5,3 bar DROPLET SIZE DISTRIBUTION FOR NOZZLE HVK26 -5,3 BAR ORIGINALLY MEASURED DATA BY PDA

94


164 310

HVK26 5,3 bar x=0 y=0 (117)

Fraction number [%]

25 20 15 10 5 0 20

80


HVK26 5,3 bar x=0 y=0 (117)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=0 (117) 100 90 80 70 60 50 40 30 20 10 0 20

80


95


191 330

HVK26 5,3 bar x=10 y=0 (118)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=10 y=0 (118)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=10 y=0 (118) 100 90 80 70 60 50 40 30 20 10 0 20

80


96


194 290

HVK26 5,3 bar x=20 y=0 (119)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=20 y=0 (119)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=20 y=0 (119) 100 90 80 70 60 50 40 30 20 10 0 20

80


97


221 290

HVK26 5,3 bar x=30 y=0 (120)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=30 y=0 (120)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=30 y=0 (120) 100 90 80 70 60 50 40 30 20 10 0 20

80


98


260 310

HVK26 5,3 bar x=40 y=0 (121)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=40 y=0 (121) 9 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=40 y=0 (121) 100 90 80 70 60 50 40 30 20 10 0 20

80


99


292 330

HVK26 5,3 bar x=50 y=0 (122)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=50 y=0 (122) 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=50 y=0 (122) 100 90 80 70 60 50 40 30 20 10 0 20

80


100


322 350

HVK26 5,3 bar x=60 y=0 (123)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=60 y=0 (123)

Fraction volume [%]

12 10 8 6 4 2 0 20



HVK26 5,3 bar x=60 y=0 (123) 100 90 80 70 60 50 40 30 20 10 0 20

80


101


161 290

HVK26 5,3 bar x=-10 y=0 (124)

Fraction number [%]

20 15 10 5 0 20

80


HVK26 5,3 bar x=-10 y=0 (124)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=-10 y=0 (124) 100 90 80 70 60 50 40 30 20 10 0 20

80


102


174 230

Fraction number [%]

HVK26 5,3 bar x=-20 y=0 (125) 18 16 14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=-20 y=0 (125) 9 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=-20 y=0 (125) 100 90 80 70 60 50 40 30 20 10 0 20

80


103


208 270

HVK26 5,3 bar x=-30 y=0 (126)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=-30 y=0 (126) 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=-30 y=0 (126) 100 90 80 70 60 50 40 30 20 10 0 20

80


104


251 290

HVK26 5,3 bar x=-40 y=0 (127)

Fraction number [%]

12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=-40 y=0 (127) 9 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=-40 y=0 (127) 100 90 80 70 60 50 40 30 20 10 0 20

80


105


292 330

HVK26 5,3 bar x=-50 y=0 (128)

Fraction number [%]

12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=-50 y=0 (128) 9 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=-50 y=0 (128) 100 90 80 70 60 50 40 30 20 10 0 20

80


106


228 350

HVK26 5,3 bar x=-60 y=0 (129)

Fraction number [%]

14 12 10 8 6 4 2 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=-60 y=0 (129) 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=-60 y=0 (129) 100 90 80 70 60 50 40 30 20 10 0 20

80


107


186 310

Fraction number [%]

HVK26 5,3 bar x=0 y=10 (130) 18 16 14 12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=10 (130)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=10 (130) 100 90 80 70 60 50 40 30 20 10 0 20

80


108


188 330

Fraction number [%]

HVK26 5,3 bar x=0 y=20 (131) 18 16 14 12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=20 (131)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=20 (131) 100 90 80 70 60 50 40 30 20 10 0 20

80


109


218 330

HVK26 5,3 bar x=0 y=30 (132)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=30 (132)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=30 (132) 100 90 80 70 60 50 40 30 20 10 0 20

80


110


277 370

HVK26 5,3 bar x=0 y=40 (133)

Fraction number [%]

10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=40 (133)

Fraction volume [%]

6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=40 (133) 100 90 80 70 60 50 40 30 20 10 0 20

80


111


373 410

Fraction number [%]

HVK26 5,3 bar x=0 y=60 (135) 9 8 7 6 5 4 3 2 1 0 20

80


HVK26 5,3 bar x=0 y=60 (135)

Fraction volume [%]

12 10 8 6 4 2 0 20



HVK26 5,3 bar x=0 y=60 (135) 100 90 80 70 60 50 40 30 20 10 0 20

80


112


337 390

Fraction number [%]

HVK26 5,3 bar x=0 y=50 (136) 9 8 7 6 5 4 3 2 1 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=0 y=50 (136) 9 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=50 (136) 100 90 80 70 60 50 40 30 20 10 0 20

80


113


191 350

HVK26 5,3 bar x=0 y=-10 (137)

Fraction number [%]

20 15 10 5 0 20

80


HVK26 5,3 bar x=0 y=-10 (137)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=-10 (137) 100 90 80 70 60 50 40 30 20 10 0 20

80


114


189 310

Fraction number [%]

HVK26 5,3 bar x=0 y=-20 (138) 16 14 12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=-20 (138)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=-20 (138) 100 90 80 70 60 50 40 30 20 10 0 20

80


115


236 350

HVK26 5,3 bar x=0 y=-30 (139)

Fraction number [%]

10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=-30 (139)

Fraction volume [%]

7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=-30 (139) 100 90 80 70 60 50 40 30 20 10 0 20

80


116


305 390

Fraction number [%]

HVK26 5,3 bar x=0 y=-40 (140) 8 7 6 5 4 3 2 1 0 20

80


Fraction volume [%]

HVK26 5,3 bar x=0 y=-40 (140) 8 7 6 5 4 3 2 1 0 20



HVK26 5,3 bar x=0 y=-40 (140) 100 90 80 70 60 50 40 30 20 10 0 20

80


117


348 390

HVK26 5,3 bar x=0 y=-50 (141)

Fraction number [%]

12 10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=-50 (141)

Fraction volume [%]

10 8 6 4 2 0 20



HVK26 5,3 bar x=0 y=-50 (141) 100 90 80 70 60 50 40 30 20 10 0 20

80


118


377 430

HVK26 5,3 bar x=0 y=-60 (142)

Fraction number [%]

10 8 6 4 2 0 20

80


HVK26 5,3 bar x=0 y=-60 (142)

Fraction volume [%]

10 8 6 4 2 0 20



HVK26 5,3 bar x=0 y=-60 (142) 100 90 80 70 60 50 40 30 20 10 0 20

80


119

11 APPENDIX A.3 NOZZLE HVK44 – 4,9 bar

120


237 420

Fraction number [%]

HVK44 4,9 bar 75 20 15 10 5 0 20

100

180

260

340

420

500

580

660

740

820

900

980

0

0

900

980

0

0


Fraction volume [%]

HVK44 4,9 bar 75 6 5 4 3 2 1 0 20

100

180

260

340

420

500

580

660

740

820



HVK44 4,9 bar 75 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

121


224 399

Fraction number [%]

HVK44 4,9 bar 76 16 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 76 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980 Upper class diameter [micrometer]


HVK44 4,9 bar 76 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

122


227 375

Fraction number [%]

HVK44 4,9 bar 77 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 77 6 5 4 3 2 1 0 20



HVK44 4,9 bar 77 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

123


273 379

Fraction number [%]

HVK44 4,9 bar 78 8 7 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 78 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 78 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

124


343 415

Fraction number [%]

HVK44 4,9 bar 79 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 79 8 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 79 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

125


378 412

Fraction number [%]

HVK44 4,9 bar 80 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 80 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 Upper class diameter [micrometer]


HVK44 4,9 bar 80 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

126


233 373

Fraction number [%]

HVK44 4,9 bar 81 20 15 10 5 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 81 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 81 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

127


218 385

Fraction number [%]

HVK44 4,9 bar 82 20 15 10 5 0 20

100

180

260

340

420

500

580

660

740

820

900

980

0

0

900

980

0

0


Fraction volume [%]

HVK44 4,9 bar 82 7 6 5 4 3 2 1 0 20

100

180

260

340

420

500

580

660

740

820



HVK44 4,9 bar 82 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

128


208 337

Fraction number [%]

HVK44 4,9 bar 83 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 83 6 5 4 3 2 1 0 20



HVK44 4,9 bar 83 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

129


227 293

Fraction number [%]

HVK44 4,9 bar 84 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 84 7 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 Upper class diameter [micrometer]


HVK44 4,9 bar 84 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

130


291 361

Fraction number [%]

HVK44 4,9 bar 85 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 85 10 8 6 4 2 0 20



HVK44 4,9 bar 85 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

Mean class diameter

600

700

800

900

131


346 354

Fraction number [%]

HVK44 4,9 bar 86 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 86 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620

0

0

0



HVK44 4,9 bar 86 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

Mean class diameter

500

600

700

132


253 373

Fraction number [%]

HVK44 4,9 bar 87 14 12 10 8 6 4 2 0 20

100

180

260

340

420

500

580

660

740

820

900

980

0

0

900

980

0

0


Fraction volume [%]

HVK44 4,9 bar 87 7 6 5 4 3 2 1 0 20

100

180

260

340

420

500

580

660

740

820



HVK44 4,9 bar 87 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

133


238 381

Fraction number [%]

HVK44 4,9 bar 88 16 14 12 10 8 6 4 2 0 20

100

180

260

340

420

500

580

660

740

820

900

980

0

0

900

980

0

0


Fraction volume [%]

HVK44 4,9 bar 88 7 6 5 4 3 2 1 0 20

100

180

260

340

420

500

580

660

740

820



HVK44 4,9 bar 88 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

134


215 331

Fraction number [%]

HVK44 4,9 bar 90 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 90 6 5 4 3 2 1 0 20



HVK44 4,9 bar 90 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

135


240 336

Fraction number [%]

HVK44 4,9 bar 91 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 91 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 91 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

136


301 376

Fraction number [%]

HVK44 4,9 bar 92 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 92 8 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 92 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

137


349 392

Fraction number [%]

HVK44 4,9 bar 93 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 93 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0



HVK44 4,9 bar 93 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

Mean class diameter

600

700

800

138

Volume mean diameter for position Volume median diameter for position X= 0 Y= -10

217 384

Fraction number [%]

HVK44 4,9 bar 94 16 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 94 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 94 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

139


210 342

Fraction number [%]

HVK44 4,9 bar 95 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 95 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 95 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

140


249 357

Fraction number [%]

HVK44 4,9 bar 96 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 96 7 6 5 4 3 2 1 0 20



HVK44 4,9 bar 96 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

141


329 371

Fraction number [%]

HVK44 4,9 bar 97 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 97 10 8 6 4 2 0 20



HVK44 4,9 bar 97 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

700

Mean class diameter

800

900

1000

1100

142


365 411

Fraction number [%]

HVK44 4,9 bar 98 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

HVK44 4,9 bar 98 8 7 6 5 4 3 2 1 0 20

80 140 200 260 320 380 440 500 560 620 680 740

0



HVK44 4,9 bar 98 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

Mean class diameter

600

700

800

900

143

12 APPENDIX A.4 NOZZLE MVK18 -2,6 BAR

144


118 173

Fraction number [%]

MVK18 2,6 bar 1 25 20 15 10 5 0 20

80 140 200 260 320 380

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK18 2,6 bar 1 25 20 15 10 5 0 20

80 140 200 260 320 380

0

0

0

0

0

0

0



MVK18 2,6 bar 1 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

145


110 154

Fraction number [%]

MVK18 2,6 bar 2 25 20 15 10 5 0 20

80 140 200 260 320 380 440 500

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK18 2,6 bar 2 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500

0

0

0

0

0



MVK18 2,6 bar 2 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

146


212 283

Fraction number [%]

MVK18 2,6 bar 3 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK18 2,6 bar 3 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500

0

0

0

0

0



MVK18 2,6 bar 3 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

147


232 257

Fraction number [%]

MVK18 2,6 bar 4 16 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK18 2,6 bar 4 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500

0

0

0

0

0



MVK18 2,6 bar 4 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

148


285 307

Fraction number [%]

MVK18 2,6 bar 5 20 15 10 5 0 20

80 140 200 260 320 380 440

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK18 2,6 bar 5 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440

0

0

0

0

0

0



MVK18 2,6 bar 5 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

149


310 354

Fraction number [%]

MVK18 2,6 bar 6 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680

0

0

0

0

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK18 2,6 bar 6 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680

0

0



MVK18 2,6 bar 6 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

150

13 APPENDIX A.5 NOZZLE MVK80 -2,1 BAR

151


160 288

Fraction number [%]

MVK80 2,1 bar 1 20 15 10 5 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860

0

0

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK80 2,1 bar 1 6 5 4 3 2 1 0 20



MVK80 2,1 bar 1 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

152


146 303

Fraction number [%]

MVK80 2,1 bar 2 25 20 15 10 5 0 20

100

180

260

340

420

500

580

660

740

820

900

980

0

0

900

980

0

0


Fraction volume [%]

MVK80 2,1 bar 2 6 5 4 3 2 1 0 20

100

180

260

340

420

500

580

660

740

820



MVK80 2,1 bar 2 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

153


235 399

Fraction number [%]

MVK80 2,1 bar 3 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK80 2,1 bar 3 7 6 5 4 3 2 1 0 20



MVK80 2,1 bar 3 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

154


265 374

Fraction number [%]

MVK80 2,1 bar 4 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920 980

0

0

0

0

0

0


Fraction volume [%]

MVK80 2,1 bar 4 6 5 4 3 2 1 0 20



MVK80 2,1 bar 4 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

155


391 464

Fraction number [%]

MVK80 2,1 bar 5 7 6 5 4 3 2 1 0 20

100

180

260

340

420

500

580

660

740

820

900

980

0

0

900

980

0

0


Fraction volume [%]

MVK80 2,1 bar 5 10 8 6 4 2 0 20

100

180

260

340

420

500

580

660

740

820



MVK80 2,1 bar 5 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

156


406 446

Fraction number [%]

MVK80 2,1 bar 6 14 12 10 8 6 4 2 0 20

80 140 200 260 320 380 440 500 560 620 680 740 800 860 920

0

0

0

0

0

0

0

0


Fraction volume [%]

MVK80 2,1 bar 6 14 12 10 8 6 4 2 0 20



MVK80 2,1 bar 6 100 90 80 70 60 50 40 30 20 10 0 0

100

200

300

400

500

600

Mean class diameter

700

800

900

1000

157

158

14 APPENDIX B: Drawing of ADD apparatus

Diameter D1 D2 D3 D4 D5 D6 D7 D8 D9 D10

[mm] 955 1345 1640 1900 2125 2325 2520 2685 2850 2985

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