# Experimental Study on the Atomization and Chemiluminescence Characteristics of Ethanol Flame

Authors: Qing Zhang; Xudong Song; Qinghua Guo; Yan Gong; Chonghe Hu; Guangsuo Yu
Journal: Journal of Spectroscopy
 (2017)

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## Abstract

The breakup regime in ethanol diffusion flame under different conditions was studied by the high speed camera system combined with the UV camera system. Spray angle and Weber number (We) were used to represent the change of breakup regime. With the increases of spray angle and We, the breakup mode changes from the Rayleigh-type breakup regime to the superpulsating regime. The reaction area and intensity of ethanol flames under different breakup regimes could be discussed by theOH⁎ distribution. From Rayleigh-type breakup regime to superpulsating breakup regime, the OH⁎ distribution increased and the oxidation-reduction reaction area expanded. At the condition of superpulsating breakup mode, the intensity of OH⁎ was significantly higher than that of other modes. The flame luminous length can be obtained by the OH⁎ emission, and OH⁎ distribution reflects the structure of flame. When the breakup regime changes from the fiber-type breakup regime to the superpulsating regime, the flame luminous length increases suddenly.


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## Body

## 1. Introduction

The heterogeneous flame is widely used in many facilities such as internal combustion engines, rockets, gas turbines, boilers, gasifier, and heaters [1–6]. Compared with the homogeneous flame, the heterogeneous flame system is more complex and there are still some important mechanisms that need to be studied. For instance, in the liquid fuel flame, the transformation of liquid into spray is of importance in the combustion process; the size and distribution of liquid droplets affect the flame stability and combustion efficiency [7, 8]. Reducing the evaporation time of droplets is an effective way to improve combustion efficiency of liquid fuel flames. Good atomization performance can significantly reduce the droplet size, thus shortening the droplet evaporation time. Therefore, the atomization plays a key role in the liquid fuel combustion process [8, 9].Liquid atomization under cold flow conditions has been widely studied both experimentally and theoretically by many researchers, including Rayleigh [10], Reitz and Bracco [9], Villermaux [11], Liu et al. [12], and Zhao et al. [13, 14]. In these atomization studies, the gas Weber number (We), the Reynolds number (Re), and the momentum flux ratio (M) have been considered as the crucial parameters with respect to atomizing the liquid jet. These three parameters can be defined by the following equations [7, 15]:(1)We=ρgug-ul2Dlσ,Reg=ρgDgugμg,M=ρgug2ρlul2,where ul and ρl are the velocity and density of liquid, respectively, Dl is the exit diameter of liquid jet, and σ is the surface tension. ug, μg, and ρg are the velocity, dynamic viscosity, and density of gas, respectively. Dg is the equivalent exit diameter of gas jet.Farago and Chigier [16] applied these parameters to analyze the coaxial air-water jets photographs obtained in the experiment and divided the atomization regime into four modes: the Rayleigh-type breakup, the membrane-type breakup, the fiber-type breakup, and the superpulsating breakup. Lasheras and Hopfinger [17] proposed a breakup regime in the parameter space We-Re after summarizing the results in the literature. Lasheras et al. [18] studied the atomization characteristics of liquid jet and their breakup regime results do not agree with the results of Farago and Chigier. Leroux et al. [15] found that injector geometry has some influence on the breakup regimes.The above researchers have done a lot of studies on liquid atomization and obtained many results; however, most of them are conducted under cold flow conditions. Investigations on hot conditions are relatively less, and the detailed properties of atomization in the flame have not been completely known yet. The major question is whether and how results from cold flow tests can be transferred to hot conditions. Although some researches have made significant contributions to the understanding of the effects of flame and spray behavior, those studies are commonly focused on liquid rocket propulsion system, and the object of study is LOX/H2 or LOX/CH4 spray combustion [8, 19–21]. From this discussion, the limitations of cold flow tests in predicting hot fire atomization become evident, especially the atomization and combustion characteristics of liquid fuel flames.In the present study, the ethanol flame is used to investigate the characteristics of atomization and chemiluminescence under hot conditions by the high speed camera system combined with the UV camera system. The breakup regimes of ethanol flame were obtained and the application ofOH∗ chemiluminescence in ethanol flames has been discussed.


## 2. Experimental Setup

### 2.1. Detection System

Figure1 shows the schematic diagram of the experimental setup, which contains two parts: jet atomization system and flame detection system. A two-channel burner is used to supply the fuel (absolute ethanol) and oxidizer (pure oxygen). A gear pump (Cole-Parmer, A-73004-00#) is used to control the ethanol flow rate and transport ethanol into the center channel of the burner; oxygen is transported into the annular channel. The diameter of the center channel is 1.5 mm, and the inner and outer diameters of the oxygen channel are 2.2 mm and 4.0 mm. The high speed oxygen shears ethanol with an angle of 60° in the annular channel to start the atomization.Figure 1
The schematic diagram of the experimental setup.Flame detection system contains high speed camera system andOH∗ detection system. The model of the high speed camera is Photron Fastcam APX-RS. The image resolution is 1024 × 1024 pixels, the frame rate is set to 3000 fps, and the exposure time is 1/20000 s. The OH∗ emission data was collected by a UV imaging system (Isuzu Optics), which contains three parts: a UV CCD camera (EX-3011B), a UV lens, and a 310 nm bandpass filter. This UV CCD camera is equipped with a cooling system in order to reduce the dark current. An achromatic ultraviolet quartz lens is used to focus the luminescence of the flame. OH∗ chemiluminescence is then extracted through a 10 nm wide bandpass filter centered at 310 nm. More detailed information about this UV imaging system can be found elsewhere [22, 23].


### 2.2. Experimental Conditions

When the burner structure is fixed, the atomization effect is related to the gas velocity and liquid flow rate. So variable gas velocity and constant gas velocity are used to investigate the change of breakup regime and spectral radiation characteristics in heterogeneous flame.The oxygen to carbon (O/C) equivalence ratio ([O/C]e) is defined by the following equation:(2)O/Ce=O/CaO/Cs,where [O/C]a is the actual mole ratio of oxygen to carbon (O/C) calculated from the feeding flows of fuel and oxygen, and [O/C]s is the stoichiometric O/C. The [O/C]e is adjusted by the O2 flow rate. Table 1 listed the experimental conditions. The oxygen velocity in the constant gas velocity conditions is 80, 100, and 120 m/s, respectively. The flow rate of ethanol in variable gas velocity conditions is 1, 2, and 3 kg/h, respectively.Table 1
Experimental conditions of ethanol flames.
Condition O / C e Ethanol flow rate (kg/h) Oxygen flow rate (L/min) Oxygen velocity (m/s) Variable gas velocity  1 0.60 1.0 15 28 2 0.70 17 32 3 0.80 19 37 4 0.90 22 42 5 1.00 24 46 6 1.10 27 51 7 1.20 29 56  8 0.60 2.0 29 56 9 0.70 34 65 10 0.80 39 74 11 0.90 44 83 12 1.00 49 93 13 1.10 54 102 14 1.20 58 111  15 0.60 3.0 44 83 16 0.70 51 91 17 0.80 58 111 18 0.90 66 125 19 1.00 73 139 20 1.10 80 153 21 1.20 88 167  Constant gas velocity  22 0.60 2.88 42 80 23 0.70 2.47 24 0.80 2.16 25 0.90 1.92 26 1.00 1.73 27 1.10 1.57 28 1.20 1.44  29 0.60 3.60 53 100 30 0.70 3.09 31 0.80 2.70 32 0.90 2.40 33 1.00 2.16 34 1.10 1.96 35 1.20 1.80  36 0.60 4.32 63 120 37 0.70 3.70 38 0.80 3.24 39 0.90 2.88 40 1.00 2.59 41 1.10 2.36 42 1.20 2.16


## 2.1. Detection System

Figure1 shows the schematic diagram of the experimental setup, which contains two parts: jet atomization system and flame detection system. A two-channel burner is used to supply the fuel (absolute ethanol) and oxidizer (pure oxygen). A gear pump (Cole-Parmer, A-73004-00#) is used to control the ethanol flow rate and transport ethanol into the center channel of the burner; oxygen is transported into the annular channel. The diameter of the center channel is 1.5 mm, and the inner and outer diameters of the oxygen channel are 2.2 mm and 4.0 mm. The high speed oxygen shears ethanol with an angle of 60° in the annular channel to start the atomization.Figure 1
The schematic diagram of the experimental setup.Flame detection system contains high speed camera system andOH∗ detection system. The model of the high speed camera is Photron Fastcam APX-RS. The image resolution is 1024 × 1024 pixels, the frame rate is set to 3000 fps, and the exposure time is 1/20000 s. The OH∗ emission data was collected by a UV imaging system (Isuzu Optics), which contains three parts: a UV CCD camera (EX-3011B), a UV lens, and a 310 nm bandpass filter. This UV CCD camera is equipped with a cooling system in order to reduce the dark current. An achromatic ultraviolet quartz lens is used to focus the luminescence of the flame. OH∗ chemiluminescence is then extracted through a 10 nm wide bandpass filter centered at 310 nm. More detailed information about this UV imaging system can be found elsewhere [22, 23].


## 2.2. Experimental Conditions

When the burner structure is fixed, the atomization effect is related to the gas velocity and liquid flow rate. So variable gas velocity and constant gas velocity are used to investigate the change of breakup regime and spectral radiation characteristics in heterogeneous flame.The oxygen to carbon (O/C) equivalence ratio ([O/C]e) is defined by the following equation:(2)O/Ce=O/CaO/Cs,where [O/C]a is the actual mole ratio of oxygen to carbon (O/C) calculated from the feeding flows of fuel and oxygen, and [O/C]s is the stoichiometric O/C. The [O/C]e is adjusted by the O2 flow rate. Table 1 listed the experimental conditions. The oxygen velocity in the constant gas velocity conditions is 80, 100, and 120 m/s, respectively. The flow rate of ethanol in variable gas velocity conditions is 1, 2, and 3 kg/h, respectively.Table 1
Experimental conditions of ethanol flames.
Condition O / C e Ethanol flow rate (kg/h) Oxygen flow rate (L/min) Oxygen velocity (m/s) Variable gas velocity  1 0.60 1.0 15 28 2 0.70 17 32 3 0.80 19 37 4 0.90 22 42 5 1.00 24 46 6 1.10 27 51 7 1.20 29 56  8 0.60 2.0 29 56 9 0.70 34 65 10 0.80 39 74 11 0.90 44 83 12 1.00 49 93 13 1.10 54 102 14 1.20 58 111  15 0.60 3.0 44 83 16 0.70 51 91 17 0.80 58 111 18 0.90 66 125 19 1.00 73 139 20 1.10 80 153 21 1.20 88 167  Constant gas velocity  22 0.60 2.88 42 80 23 0.70 2.47 24 0.80 2.16 25 0.90 1.92 26 1.00 1.73 27 1.10 1.57 28 1.20 1.44  29 0.60 3.60 53 100 30 0.70 3.09 31 0.80 2.70 32 0.90 2.40 33 1.00 2.16 34 1.10 1.96 35 1.20 1.80  36 0.60 4.32 63 120 37 0.70 3.70 38 0.80 3.24 39 0.90 2.88 40 1.00 2.59 41 1.10 2.36 42 1.20 2.16


## 3. Results and Discussion

### 3.1. Breakup Regimes of Ethanol Flame

Yang et al. [19] found that, with the presence of combustion, atomization becomes more complex with respect to the atomization process in cold flow sprays and there are several controlling parameters that affect the atomization under hot test conditions. In order to find the atomization characteristics in the presence of flame, the photographs of ethanol flames under each experimental condition were captured by the high speed camera.Figure2 shows the representative photographs of different atomization regimes obtained from various experimental conditions. It can be seen that, in the presence of flame, the atomization morphology is similar to that observed under cold flow conditions, which can be classified into four regimes: Rayleigh-type breakup, membrane-type breakup, fiber-type breakup, and superpulsating breakup. For cold flow experiments, the We number, Reg number, and momentum flux ratio M are very important parameters in the classification of atomization modes. Many researchers used these three parameters to obtain the breakup regime map, such as We-Reg map, We-M map, andM-Reg map, and the results are good. However these results obtained from cold flow tests cannot be transferred to hot conditions directly. Only using these three parameters is unable to obtain a proper breakup regime map under the experimental conditions of the present study; new parameters should be introduced to characterize the breakup regimes in ethanol flame.Figure 2
Representative photographs of four breakup regimes under hot conditions ((a) condition 5, (b) condition 12, (c) condition 33, and (d) condition 19).
(a)
Rayleigh-type breakup,We=209,M=98,Reg=5795 (b)
Membrane-type breakup,We=836,M=98,Reg=11589 (c)
Fiber-type breakup,We=975,M=98,Reg=12517 (d)
Superpulsation breakup,We=1880,M=98,Reg=17384Figure3 shows the instantaneous and average images of flame under condition 33. The average image is obtained from 5000 instantaneous images. It can be seen from the average image in Figure 3 that the oxygen shears the ethanol and produces the flame spray angle. The breakup regime can be reflected by the flame spray angle.Figure 3
The instantaneous and average images of flame (condition 33).Figure4 shows the flame spray angle as a function of We number. The results show that increasing We number results in an increasing flame spray angle. The data shown in this figure can be divided into four parts, that is, the four breakup regimes of ethanol flame: I, the Rayleigh-type breakup (spray angle < 10°, We<500); II, the membrane-type breakup (10°< spray angle < 25°, 500<We<900); III, the fiber-type breakup (25°< spray angle < 50°, 900<We<1300); and IV, the superpulsating breakup (spray angle > 50°, We>1300). When the We number and the flame spray angle are both smaller (spray angle < 10°, We<500), the Rayleigh-type breakup regime occurs. While the We number and the flame spray angle are both larger (spray angle > 50°, We>1300), the superpulsating breakup regime occurs. The We number and the flame spray angle can reflect the breakup regime clearly. Unlike for We number, no significant correlation of the flame spray angle with either the momentum flux ratio M or the Reg number has been found.Figure 4
Flame spray angle as function of We.


### 3.2. Reaction Regions of Ethanol Flame

In the ethanol flame, the oxygen has two functions: shearing the ethanol and reacting with the droplet. Different breakup regimes will produce different droplets, and different size of droplets will have different reaction time. The gas velocity is very high, and the pace time of droplet is less than 1 s, so the atomization effect influences the reaction in ethanol flame.Figure5 shows the OH∗ distribution and emission intensity in ethanol flame at different breakup regimes. From the distribution of OH∗, the size of reaction area of the flame can be obtained. In the Rayleigh-type breakup regime (Figure 5(a)), OH∗ exists from the burner exit to the downstream. Because of the low oxygen velocity, the size of droplets is very big, and the effect of gravity force cannot be neglected. In this case, the droplet has the tendency to downward, so the reaction area of the flame is not symmetrical. With the increase of velocity, the size of droplet becomes smaller and the effect of gravity force is neglected, so the reaction area becomes symmetrical. Compared with different breakup regimes, the OH∗ intensity first increases and then decreases along the flame propagation direction. At the position about 10 mm to 30 mm away from the burner exit (10mm<X<30mm), the OH∗ peak intensity occurs, and the OH∗ radial distribution is the widest. It indicates that more droplet and oxygen react at 10mm<X<30mm, and a clear reaction center occurs. when X>30 mm, the fuel and oxygen are consumed gradually, and OH∗ intensity decreases, so oxidation-reduction reaction disappears. From Rayleigh-type breakup regime to superpulsating breakup regime, the OH∗ distribution increases and the oxidation-reduction reaction area expands. At the condition of superpulsating breakup the intensity of OH∗ (Figure 5(d)) is higher than that of other modes.Figure 5
O H ∗ distribution and emission intensity in ethanol flame.
(a)
Condition 5 (b)
Condition 12 (c)
Condition 33 (d)
Condition 19Figure6 shows the changes of instantaneous images in flame at different conditions. As the OH∗ distribution shown in Figure 5(a), OH∗ peak intensity exists at the position about X=20 mm and the droplet also occurs at this position. At the exit of the burner, more high speed oxygen reacts with the droplet, which makes the heat accumulate and produces impulse. The impulse then takes the droplet to the downstream. Figure 6(a) shows the change of Rayleigh-type breakup regime at different times. At t+0 ms, the liquid column begins to fragment at the position X=20 mm due to the influence of impulse and shear force. Part of the oxygen reacts with the droplet and produces huge heat. Until t+9 ms, the liquid column fragment process finishes, and part of hot oxygen reacts with the droplet at the downstream. The flame in the membrane-type breakup regime is similar to that of Rayleigh-type breakup regime. As shown in Figure 6(b), the high velocity has the entraining effect on the droplet and makes the oxygen mix with the droplet. The influence of impulse and shear force makes the reaction expend to the radial direction and then influence the size of the flame spray angle.Figure 6
The change of instantaneous images in ethanol flame.
(a)
Condition 5 (b)
Condition 33Figure7 shows OH∗ peak emission intensity in ethanol flame under different conditions. When the gas velocity is constant, the OH∗ peak intensity changes smaller with the increase of [O/C]e. According to the atomization photographs obtained by the high speed camera, the atomization morphology changes very little with the increase of [O/C]e under the same gas velocity, so the OH∗ intensity changes rarely. What is more, although the ethanol flow rate decreases (the oxygen flow rate and velocity are constant) with the increase of [O/C]e, the OH∗ intensity changes little, which indicates that, under constant gas velocity conditions, the change of ethanol flow rate has little effect on the atomization performance and reaction intensity. The OH∗ peak intensity changes a lot when the gas velocity is variable. When the ethanol flow is 1 kg/h, the OH∗ peak intensity has no change, while when the ethanol flow becomes larger, OH∗ peak intensity increases with the increase of [O/C]e. Combining with the difference of breakup regimes in Figure 4, the gas velocity influences the atomization effect under variable gas velocity conditions. There are different breakup regimes at different gas velocities, which makes OH∗ intensity vary greatly.Figure 7
O H ∗ peak emission intensity in ethanol flame.Figure8 shows the comparison of flame luminous lengths obtained by the OH∗ emission and flame images. The length of flame is the maximal radial distance between the burner exit and the boundary of flame. Flame length gained by the flame image is based on the theory of image segmentation. The image can be divided into two parts by the gray value: the flame region and the background region, and then the length can be calculated. The length obtained by the OH∗ emission is the maximal radial distance measured from the OH∗ distribution profile. From Figure 8, the lengths gained by the OH∗ emission and flame image are almost the same, and the error is less than 5%. In the ethanol flame, the droplets are wrapped by the oxygen, and reactions occur around the droplets. OH∗ exists all over the flame, so the OH∗ distribution can reflect the structure of the flame.Figure 8
Comparison of flame luminous lengths obtained byOH∗ emission and flame images.Figure9 shows the comparison of flame luminous lengths gained by the OH∗ emission at different conditions. When the velocity of oxygen is constant, the flame length decreases with the increase of [O/C]e, and when the velocity of oxygen is variable, the flame length shows no regular change with the increase of [O/C]e. When the velocity is constant, the ethanol decreases with the increase of [O/C]e. The breakup regime has no changes, so the number of droplets produced by the ethanol decreases, and the reaction of flame decreases; then the length of flame decreases. When the velocity of oxygen is variable, the breakup regime changes from the Rayleigh-type breakup to the superpulsating breakup with the increase of [O/C]e. When the velocity is low, the type of breakup regime mainly contains the Rayleigh-type breakup and the membrane-type breakup; the size of the droplets is too big to react with the oxygen clearly, so the flame luminous length changes a little with the [O/C]e. When the flow rate of ethanol is 3 kg/h, the breakup regime changes from the fiber-type breakup to the superpulsating breakup with the increase of [O/C]e, and more droplets react with the oxygen, so the luminous length increases.Figure 9
Comparison of flame luminous lengths at different conditions.


## 3.1. Breakup Regimes of Ethanol Flame

Yang et al. [19] found that, with the presence of combustion, atomization becomes more complex with respect to the atomization process in cold flow sprays and there are several controlling parameters that affect the atomization under hot test conditions. In order to find the atomization characteristics in the presence of flame, the photographs of ethanol flames under each experimental condition were captured by the high speed camera.Figure2 shows the representative photographs of different atomization regimes obtained from various experimental conditions. It can be seen that, in the presence of flame, the atomization morphology is similar to that observed under cold flow conditions, which can be classified into four regimes: Rayleigh-type breakup, membrane-type breakup, fiber-type breakup, and superpulsating breakup. For cold flow experiments, the We number, Reg number, and momentum flux ratio M are very important parameters in the classification of atomization modes. Many researchers used these three parameters to obtain the breakup regime map, such as We-Reg map, We-M map, andM-Reg map, and the results are good. However these results obtained from cold flow tests cannot be transferred to hot conditions directly. Only using these three parameters is unable to obtain a proper breakup regime map under the experimental conditions of the present study; new parameters should be introduced to characterize the breakup regimes in ethanol flame.Figure 2
Representative photographs of four breakup regimes under hot conditions ((a) condition 5, (b) condition 12, (c) condition 33, and (d) condition 19).
(a)
Rayleigh-type breakup,We=209,M=98,Reg=5795 (b)
Membrane-type breakup,We=836,M=98,Reg=11589 (c)
Fiber-type breakup,We=975,M=98,Reg=12517 (d)
Superpulsation breakup,We=1880,M=98,Reg=17384Figure3 shows the instantaneous and average images of flame under condition 33. The average image is obtained from 5000 instantaneous images. It can be seen from the average image in Figure 3 that the oxygen shears the ethanol and produces the flame spray angle. The breakup regime can be reflected by the flame spray angle.Figure 3
The instantaneous and average images of flame (condition 33).Figure4 shows the flame spray angle as a function of We number. The results show that increasing We number results in an increasing flame spray angle. The data shown in this figure can be divided into four parts, that is, the four breakup regimes of ethanol flame: I, the Rayleigh-type breakup (spray angle < 10°, We<500); II, the membrane-type breakup (10°< spray angle < 25°, 500<We<900); III, the fiber-type breakup (25°< spray angle < 50°, 900<We<1300); and IV, the superpulsating breakup (spray angle > 50°, We>1300). When the We number and the flame spray angle are both smaller (spray angle < 10°, We<500), the Rayleigh-type breakup regime occurs. While the We number and the flame spray angle are both larger (spray angle > 50°, We>1300), the superpulsating breakup regime occurs. The We number and the flame spray angle can reflect the breakup regime clearly. Unlike for We number, no significant correlation of the flame spray angle with either the momentum flux ratio M or the Reg number has been found.Figure 4
Flame spray angle as function of We.


## 3.2. Reaction Regions of Ethanol Flame

In the ethanol flame, the oxygen has two functions: shearing the ethanol and reacting with the droplet. Different breakup regimes will produce different droplets, and different size of droplets will have different reaction time. The gas velocity is very high, and the pace time of droplet is less than 1 s, so the atomization effect influences the reaction in ethanol flame.Figure5 shows the OH∗ distribution and emission intensity in ethanol flame at different breakup regimes. From the distribution of OH∗, the size of reaction area of the flame can be obtained. In the Rayleigh-type breakup regime (Figure 5(a)), OH∗ exists from the burner exit to the downstream. Because of the low oxygen velocity, the size of droplets is very big, and the effect of gravity force cannot be neglected. In this case, the droplet has the tendency to downward, so the reaction area of the flame is not symmetrical. With the increase of velocity, the size of droplet becomes smaller and the effect of gravity force is neglected, so the reaction area becomes symmetrical. Compared with different breakup regimes, the OH∗ intensity first increases and then decreases along the flame propagation direction. At the position about 10 mm to 30 mm away from the burner exit (10mm<X<30mm), the OH∗ peak intensity occurs, and the OH∗ radial distribution is the widest. It indicates that more droplet and oxygen react at 10mm<X<30mm, and a clear reaction center occurs. when X>30 mm, the fuel and oxygen are consumed gradually, and OH∗ intensity decreases, so oxidation-reduction reaction disappears. From Rayleigh-type breakup regime to superpulsating breakup regime, the OH∗ distribution increases and the oxidation-reduction reaction area expands. At the condition of superpulsating breakup the intensity of OH∗ (Figure 5(d)) is higher than that of other modes.Figure 5
O H ∗ distribution and emission intensity in ethanol flame.
(a)
Condition 5 (b)
Condition 12 (c)
Condition 33 (d)
Condition 19Figure6 shows the changes of instantaneous images in flame at different conditions. As the OH∗ distribution shown in Figure 5(a), OH∗ peak intensity exists at the position about X=20 mm and the droplet also occurs at this position. At the exit of the burner, more high speed oxygen reacts with the droplet, which makes the heat accumulate and produces impulse. The impulse then takes the droplet to the downstream. Figure 6(a) shows the change of Rayleigh-type breakup regime at different times. At t+0 ms, the liquid column begins to fragment at the position X=20 mm due to the influence of impulse and shear force. Part of the oxygen reacts with the droplet and produces huge heat. Until t+9 ms, the liquid column fragment process finishes, and part of hot oxygen reacts with the droplet at the downstream. The flame in the membrane-type breakup regime is similar to that of Rayleigh-type breakup regime. As shown in Figure 6(b), the high velocity has the entraining effect on the droplet and makes the oxygen mix with the droplet. The influence of impulse and shear force makes the reaction expend to the radial direction and then influence the size of the flame spray angle.Figure 6
The change of instantaneous images in ethanol flame.
(a)
Condition 5 (b)
Condition 33Figure7 shows OH∗ peak emission intensity in ethanol flame under different conditions. When the gas velocity is constant, the OH∗ peak intensity changes smaller with the increase of [O/C]e. According to the atomization photographs obtained by the high speed camera, the atomization morphology changes very little with the increase of [O/C]e under the same gas velocity, so the OH∗ intensity changes rarely. What is more, although the ethanol flow rate decreases (the oxygen flow rate and velocity are constant) with the increase of [O/C]e, the OH∗ intensity changes little, which indicates that, under constant gas velocity conditions, the change of ethanol flow rate has little effect on the atomization performance and reaction intensity. The OH∗ peak intensity changes a lot when the gas velocity is variable. When the ethanol flow is 1 kg/h, the OH∗ peak intensity has no change, while when the ethanol flow becomes larger, OH∗ peak intensity increases with the increase of [O/C]e. Combining with the difference of breakup regimes in Figure 4, the gas velocity influences the atomization effect under variable gas velocity conditions. There are different breakup regimes at different gas velocities, which makes OH∗ intensity vary greatly.Figure 7
O H ∗ peak emission intensity in ethanol flame.Figure8 shows the comparison of flame luminous lengths obtained by the OH∗ emission and flame images. The length of flame is the maximal radial distance between the burner exit and the boundary of flame. Flame length gained by the flame image is based on the theory of image segmentation. The image can be divided into two parts by the gray value: the flame region and the background region, and then the length can be calculated. The length obtained by the OH∗ emission is the maximal radial distance measured from the OH∗ distribution profile. From Figure 8, the lengths gained by the OH∗ emission and flame image are almost the same, and the error is less than 5%. In the ethanol flame, the droplets are wrapped by the oxygen, and reactions occur around the droplets. OH∗ exists all over the flame, so the OH∗ distribution can reflect the structure of the flame.Figure 8
Comparison of flame luminous lengths obtained byOH∗ emission and flame images.Figure9 shows the comparison of flame luminous lengths gained by the OH∗ emission at different conditions. When the velocity of oxygen is constant, the flame length decreases with the increase of [O/C]e, and when the velocity of oxygen is variable, the flame length shows no regular change with the increase of [O/C]e. When the velocity is constant, the ethanol decreases with the increase of [O/C]e. The breakup regime has no changes, so the number of droplets produced by the ethanol decreases, and the reaction of flame decreases; then the length of flame decreases. When the velocity of oxygen is variable, the breakup regime changes from the Rayleigh-type breakup to the superpulsating breakup with the increase of [O/C]e. When the velocity is low, the type of breakup regime mainly contains the Rayleigh-type breakup and the membrane-type breakup; the size of the droplets is too big to react with the oxygen clearly, so the flame luminous length changes a little with the [O/C]e. When the flow rate of ethanol is 3 kg/h, the breakup regime changes from the fiber-type breakup to the superpulsating breakup with the increase of [O/C]e, and more droplets react with the oxygen, so the luminous length increases.Figure 9
Comparison of flame luminous lengths at different conditions.


## 4. Conclusions

Spray angle and Weber number (We) were used to represent the change of liquid fuel breakup regime. When the spray angle and We were small (spray angle< 10°, We<500), the Rayleigh-type breakup mode appeared. While the spray angle and We were big enough (spray angle > 50°, We>1300), the breakup mode changed into the superpulsating regime. The reaction area and intensity of ethanol flames under different breakup regimes could be discussed by the OH∗ distribution. From Rayleigh-type breakup regimes to superpulsating breakup regimes, the OH∗ distribution increased and the oxidation-reduction reaction area extended. At the condition of superpulsating breakup mode, the intensity of OH∗ was higher than that of other modes. The flame luminous lengths can be obtained by the OH∗ emission. When the velocity of oxygen is constant, the flame luminous length decreases with the increase of [O/C]e, and when the velocity of oxygen is variable, the flame length shows no regular change with the increase of [O/C]e. When the breakup regime changes from the fiber-type breakup to the superpulsating one, the flame luminous length increases suddenly.



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*Source: 2106376-2017-01-19.xml*