3;: w 's» ”why . a. ' if». = 2;? i211 VHE‘BB / . 9081/ J" ‘7 .N' 77 a E e r: g 0.2 - ~~ 6 o 8 '6 Ma‘fli-‘VWi‘Qg-fiefi’fiufl‘fig-J‘Ifitk“ 4 g > o - 'E 2 .— ‘O.2 r r r 0 O 50 100 150 200 Time [ms] —— Injector #1 velocity ——-——.—- Voltage Figure 25: Cycle-averaged centerline velocity plot with injector voltage. 34 Injector #2 Individual Cycle (5-14-04) 0.8 0.6 0.4 (I 0.2 [+ Cycle 1 l -o.2 - -o.4 Centerline Velocity [mls] 0 50 100 1 50 200 Time [ms] Injector #2 Individual Cycle (5-14-04) 0.8 0.6 0.4 i L—o— Cycle 2 0 2 Centerline Velocity [mls] -0.2 . i 0 50 100 150 200 Time [ms] Injector #2 Individual Cycle (5-14-04) 0.8 0.6 0-2 b-CYEE‘ET -o.2 I 43.4 Centerline Velocity [mls] 0 50 100 1 50 200 Time [m s] Figure 26: Three consecutive cycles from Injector #2. 35 Injector 2- Calculated mass injected (5-14-04) Mass Injected [mg] mekms-OOLONO) MID n—r-v-V-P NN NO) NN ‘5. Injection Average: 30.6147 mg, Standard deviation: 1.44552 mg Coefficient of variation: 3.94499. Measured mass (cycle avg): 33.24 mg Figure 27: Mass injected chart for Injector #2. Again, significant variability can be observed in the individual velocity traces. Initially, the bar graph shows great variability. The injector was allowed to run for several cycles before data was collected, so this variability at the beginning should not be attributed to some kind of startup condition. It is believed that this is simply a display of the varied nature of the injector. Note that the standard deviation is greater for Injector #2 than it is for the #1. 4.2 Discussion 4.2.1 Comparison of Injectors #1 and #2 Figure 28 shows the average centerline velocity plots from Injectors #1 and #2 as well as the voltage applied. It very interesting to note how similar the pressure wave 36 Injector Comparison (5-14-04) 14 .3 C .0 .O .O N co Injector Voltage A it ”747’ “*Ts’t-fifiwv‘t—awe ii: Centerline Velocity [mls] O c'> '_. omemoo .5 N 0 50 1 00 1 50 200 Time [ms] _"- InjeCtor 1 —— Injector 2 ———— Voltage Figure 28: Average centerline velocities and applied voltage. oscillation is. The most notable difference is that Injector #2 flows considerably more fuel. This is expected, as the cylinder displacement of a Chrysler Hemi is about twice that of the Toyota Prius. The standard deviation of mass injected for Injector #1 was 1.0664 milligrams as compared to 1.4552 milligrams for Injector #2. It appears as though the Prius injector was designed with more precise fuel control in mind. This is not surprising because the Prius is a car whose designers were concerned with fuel economy. Also plotted are plots of the probability density functions. 37 Injector #1- PDF Plot of Mass Injected I. 115 Injections Number of Injectlons o a B 8 B 8 8 24 25 26 27 28 29 30 31 less Injected [my Figure 29: PDF of mass injected for Injector #1. Injector #2- PDF Plot of Mass Injected [.115 Injections] Number of Injection: 0 m a a B at 8 81 e a 171819 20 2122 23 24 25 26 2728 29 30 3132 33 less Injected [my Figure 30: PDF of mass injected by Injector #2. A useful way of viewing the injector precision is to assume that this injector variability could translate into fuel/air ratio variability. If the average were taken to be the amount of fuel required for a stoichiometric mixture, then the maximum and minimum fuel/air ratios would be as follows. This is a large range and would be highly 38 Table 2: Fuel/Air ratio range. jlnjectorlrnjector 1 2 Max 15.54 15.85 [Min 13.27 13.48 undesirable from an emissions and fuel economy standpoint. For port injection systems, however, the fuel/air ratio may not fluctuate quite as much. There is a phenomenon whereby the fuel film on the intake runner, port, and intake valve serves as a cycle-to- cycle filter. In other words, the extreme variations in fuel injected may not result in sharp variations in the in-cylinder fuel/air ratios for port injection systems [7],[10]. This is not the case for direct injection gasoline engines, however. These engines require precise fuel metering for smooth operation. Variation in the amount of fuel injected can also have dramatic effects on the emissions produced, particularly oxides of nitrogen (NOx) and hydrocarbons (HC). 4.2.2 Sources of Variability 4.2.2.1 Cosworth Variability A great deal of effort was taken to isolate the injector so that only the variability of the injector would be measured. Nevertheless, there is still the possibility of variability from the Cosworth control module. To investigate this, the control module was monitored using an oscilloscope to measure and plot the voltage. Three injection events are shown in the following figure. One can observe slight variations in the peak voltage. To better quantify this variability, a table was constructed from the statistics 39 Cosworth Voltage Plots 14 12 ——« r— 11 r1 2 10 «I - o 3 j °’ I g 6 l O i . ‘ 1 . . ,. - 1 > 4 tier-“+4; . , ...4 f 1 125% t c #14" 4‘54»;‘14“‘1-5'1421-3‘13’1 2 0 T F T T 0 100 200 300 400 Time [ms] 500 Figure 31: Voltage plot of the injection control system. recorded by the oscilloscope. These values were recorded over a series of about 200 injection events. It would be interesting to find out if this variability had any effect on the motion of the needle inside the injector. It is possible that this variability Table 3: Injection control system variability statistics. I tandard "J Mean Deviation lMinimum Maximu [Volts peak-to-peakl7.965 V 111 mV 7.87 V 8.92 V [Period I199.998 m 32 us 199.61 m 200.03ms IFrequency I5.0004 Hz 794.459 sz 4.9994 Hz'5.0098 Hz [like Time I442 us 24 us 320 us 2.15 ms had an affect the performance of the injector. For that reason, the variability presented should be considered the variability of the injector and the control module. 40 4.2.2.2 Sources of Error As with any experiment, there is always the potential of errors affecting the end result. The uncertainty errors and systematic errors associated with this experiment will be discussed at this time. Uncertainty errors in this experiment arose from the measurements of the quartz tube diameter, centerline velocity, as well as the temperature measurements needed to determine the fluid density. Recall that the general form of the equation used to solve for the mass flow rate was m(t)=,0°(fl°R2)'U(t) (4) where 1 d * U(t)—§uc,(t)+E(uc,(t)) W(t) . (5) The uncertainty associated with the quasi-steady portion (gut, (1)) is given by taking the partial differential of (4) using the following equation dn'z=-;—[(p-u~dA)+(p-A-du)+(A-u-dp)]. (7) The uncertainty from the radius measurements is i: 0.005 mm, from the velocity measurements (LDA precision) i 0.0005 m/s, and from the density i 0.05 kg/m3. The resulting uncertainty from this quasi-steady calculation is i 0.001839 mg/ms. To put that into perspective, the quasi-steady mass flow rates varied from 0 to 2.07416 mg/ms. Thus, the uncertainty contributions from measurements and tabulated values were quite low. Systematic errors are likely present, though their direct contributions may be more difficult to quantify. One key assumption that was made was that the quartz tube was 41 perfectly circular and that it had a uniform cross-sectional area throughout its length. Obviously the calculations are quite sensitive to the diameter measurement as it is squared in the area calculation. There are also some errors associated with measuring the centerline velocity. As previously stated, the recorded velocities were assumed to be centerline velocities. In reality, these are the probe volume-averaged velocities. While the probe volume area is small compared to the flow area, the length of the probe volume is approximately 1/3 of the diameter. This could contribute to some error as a result of this averaging. With the assumed parabolic profile, it is reasonable to assume that the error in the measured velocity introduced as a result of the probe volume is 0-5%. A key parameter that affects the accuracy of the velocity is the measurement of the angle between the laser beams. Based on previous experiments, the velocity is likely affected by this parameter by about i- 2%. Finally, processing error could also come into effect. The documentation on the LDA system indicated that the processor accuracy was i 0.5% full spectrum. Since the velocity range was from —1 .2-1.2 m/s, this translates to 0.006 m/s. It is likely that these errors would average out since several tens of thousands of samples were taken. While these certainly are not all the potential sources of error, they were thought to be the major contributors. Having discussed the potential sources of error, however, it should be understood that for the experiments run, the agreement was very good with the cycle-averaged measurements. The table on the following page shows this agreement. The LDA measurements of the mass injected by Injector #1 was typically within 6% and Injector #2 within 8% of the cycle-averaged measured values from the mass balance. Moreover, 42 the relative cycle-to-cycle variability shown by the previous bar graphs is unaffected by this uncertainty. The only change is in the magnitude of the mass injected. The reason for this is that the calculation procedure for the mass injected for each cycle is the same and the LDA equipment was not moved between measurements. Any error present should be consistent. Table 4: Comparison between mass balance and LDA measurements ln'ector £1 Injector 52 Mass Balance LDA Injection Percent Mass Balance LDA Injection Percent Measurement (mg) Average (mg) Difference Measurement (mg) Average (mg) Difference I 28.84 27.343 5.191 33.24 30.7676 W l 28.84 27.2857 5.389 33.24 30.4943 8.260] I 28.84 27.0378 6.249 33.24 30.6147 7.89% 43 CHAPTER 5 CONCLUSIONS In this study, the real time cycle-to-cycle variability of a fuel injector and its control system was quantified. The approach was quite different from traditional measurement techniques as it involved measuring the centerline velocity before the injector using LDA as opposed to making measurements after the injector. It was also found that good time resolution is necessary, and the seed used to scatter the laser light must not plug the injector if the results are to be trusted. The results of these experiments have shown that there is a significant amount of cycle-to-cycle variation for the two injectors used. The Toyota Prius injector (Inj. #1) had an observed standard deviation of 1.0664 mg while that for the Chrysler Hemi (Inj. #2) injector was 1.4552 mg. If the variability in mass injected was directly related to the fuel/air ratio, this would result in a large amount of variation and would be highly undesirable for clean, efficient combustion. For port injection systems, this may not be the case because of fuel film that is a result of wetting on the valves and/or intake ports. This causes a filtered or damped response so that the actual fuel/air ratio seen in the cylinder may not show as much variability as the fuel injector [7],[10]. In the case of directly injected engines, however, this variability is much more closely related to the in- cylinder fuel/air ratio. There have also been some recent developments in fuel-injected two-stroke engines. More precise electronic fuel control could make these engines cleaner and more acceptable in the near future [I 7]. The measurement technique outlined 44 in this report could prove to be a useful tool for companies striving to design more precise and consistent fuel injector performance for such applications. While developing and perfecting this measurement method, several important discoveries were made. These discoveries are discussed in detail in Appendix C and will be summarized at this time. First, the microbubble seeding technique used in this experiment proved to be extremely effective. By introducing thousands of these tiny bubbles into the working fluid, excellent data rates were achieved without plugging the fuel injector. Because of the small size of these bubbles, they did little or nothing to affect the velocity profile and bulk fluid density (proved experimentally). The second useful discovery was the presence of air in the fuel injector and the effects it has on the centerline velocity. Figure 30 shows the difference in the centerline velocity profile with and without air in the injector. These oscillations affect the Injector #1: Centerline Velocity and Voltage Plots (4-8-04) 1 14 . ,g‘ 1 12. g 05 7 7 7 777 777 7 7m7 7 77 105 i E o A 4— ' .I 3 g e 1 V 5 g -o.5 g. 0 _ o -1 Time [ms] l—— purged injectorj I i ~77 unpurged injectorl _ git/9113,99 , , l Figure 32: Velocity plots for Injector #1 with and without air. 45 consistency of the injector. In some cases, the oscillation did not die out before the next injection event, adding to injector variability. Even though it was initially thought that these bubbles would dissolve or “work themselves out” of the system, this was not observed over the course of several days of intermittent testing. Lastly, it was determined that a fuel injector is only as good as the control system that actuates it. If there are fluctuations in the voltage sent to the injector, increased variability is inevitable. Stable control systems must be developed to minimize this problem. 46 CHAPTER 6 RECOMMENDATIONS After completing this project, it was clear that there were several other areas that would be worth to investigating. 0 Use gasoline in test rig and automotive injection control unit as well as stock fuel delivery setup to simulate more realistic conditions. Is there any variability introduced by the addition of a fuel pump? How much? 0 Find a way to quantify the variability of the injector with air inside. How much of an improvement is there when the air is evacuated? o Evacuate air from injectors in an engine on a dynamometer/emissions test cell to see how performance and emissions changes as a result. 0 Measure variability in high-pressure diesel injectors. It is difficult to design a quartz window that can withstand these high pressures. Such a window has already been developed here at the Michigan State University Engine Research Laboratory, however. This window has been tested up to about 30,000 psi [8]. - Streamline software for sale to companies which develop fuel injectors for commercial use. 0 Compare similar injectors made by the same company to measure variability from one injector to another. Is the manufacturing process consistent enough? 0 Measure variability in a piezoelectric injector (Siemens). Are they more consistent? What is the consistency for multiple injection systems? 47 0 Test injectors for D1, HCCI engines. Since there is no wall-wetting filtering effect, precise fuel metering is more important. Great strides have been made in fuel injection technology since the 1920’s, but there is still much more that can be explored in this field. More precisefuel injectors and control systems will enable automotive manufacturers to achieve greater fuel efficiency and cleaner emissions than ever before. 48 Appendices 49 APPENDIX A Details of the Mass Flow Equation The exact unsteady solution of the laminar Navier-Stokes equations is discussed in this section as developed by Brereton [14]. As previously mentioned, the general expression for calculating the mass flow rate in uniform density flow is mow-(8129479) (4) 2 (‘I d, (.I where W (t) is a known weighting function and * the convolution operator. This exact solution applies to laminar, fully developed, constant property duct flow undergoing arbitrary unsteadiness from an initially steady state. Recall that the é—ud (t) term is simply the momentary velocity term for a steady laminar parabolic velocity profile. The g—(uc,(t))* W (t) term is an unsteady correction term. By definition of the convolution t operator *, d :1: _ Ifi _ ' . ' . 5W”) mn— 0j dt (t t) W(t) du (7) For simplicity of evaluation, the following non-dimensional term is now introduced: V't 72?. (8) Here, v is viscosity, t is time, and R is the measurement tube radius. W (2’) is an inverse convolution integral term which can be described as follows: For 1 < 0.01, W(r) = 0.5 — 2.2567J1+ 1.1251 (9) (gt-73'7” (0.253393 cos(26. 1 2881) + 0.499595 sin(26. 12881)) + (””05“ (0.0816947 cos(58.5689z') + 0.289019sin(58.56891)) For 1 2 0.01, W(1) = + e7377»58'5°’((0.0402422 cos(94.02701) + 0.200663 sin(94.02701)) + 1376629727” ((0.0240313cos(13 1 .5101) + 0.153211sin(131.5101)) + 61°27'47“)”((0.0160209cos(l 70.5211) + 0.123770 sin(1 705211)) as given in Brereton, Schock, Rahi, and Bedford [15]. In this solution, the angles are in radians. Once this “modified” area-averaged velocity in (5) is developed from the measured centerline velocity history, the mass injected can then be calculated by carrying out the convolution integral, at each instant in the time series, and multiplying 17(1) by the fluid density and the cross-sectional area of the tube. It was determined that the unsteady correction term contributes nearly as much (~ 45%) to the calculation of the total mass injected as the quasi-steady laminar parabolic profile portion. 51 APPENDIX B Calculation of the LDA Probe Volume In an LDA system, two laser beams cross in a fluid flow. The drawing below shows the general layout of an LDA system and shows the ellipsoidal shape of the probe volume. The intersecting lasers produce a series of fringes. As particles cross this Transmitting W system w...»- fmfifiz D a... . ,, f I X . /1\ IntenSIty lie 2) \X distribution 52 A 5,, Z ..... ,------- Measurement ‘ volume Y Figure 33: Probe volume diagram and intensity distribution [16]. probe volume, light is scattered. The fluid velocity can then be determined based on the Doppler shifi of the light reflected from the moving particle. When calculating the probe volume, the following diagram and equations are very useful. 52 Length: Width: Height: Fringe separation: Number of fringes: X Figure 34: Probe volume dimensions [16]. 4F}. (10) 6, — (11) 6 =——— (12) 5] =_— (13) (14) 53 Table 5: Probe volume variables. mm 514.5 nm beam 4.684 nder ratio 1.95 diameter of laser 1.350 mm When the test fluid is air, these equations can be used as they are. For the case of fluid flowing through a quartz tube, refraction must be considered. The refractive index of quartz and the working fluid, water in this case, must be known and the effective beam angle must be modified according to the following equation: nl sin, = 712 sin 6, (15) In this equation, 11 is the refractive index of the medium, i stands for incidence, and t stands for transmitted. The following diagram shows how the angle changes as it passes through each medium. Now that all the variables are known, the dimensions can be 0002926 .3315? .45843 Figure 35: Beam refraction sketch and values. calculated and finally the probe volume, using the equation for the volume of an ellipsis shown below. V . = _7[ ..... _ ellipse 3 2 2 2 ( l 6) 54 The results are shown for calculating the probe volume in air as well as inside a quartz tube with water. Table 6: Results of probe volume calculations. [Dimension Value in air Value in quartz tube/water By (mm) 0.077217 0.077217 I8x 0.077475 0.077345 I62 0.945584 1 .34233 Volume (mm"3) 0.002926 0.004198 IFringe Separation 0.1m) 3.15 3.15 Number of Fringes 24 24 55 APPENDIX C Evolution of Experimental Technique Over the course of this project, several discoveries were made that were quite significant. This section discusses these discoveries and the lessons learned from them. Fuel Delivery Tube Early in the experimental phase, the test rig was designed with a rubber fuel injection hose that connected to the quartz tube and supplied the injector with fuel. The working fluid was mineral spirits because it possessed a density and viscosity that was similar to gasoline but is safer to work with. The mineral spirits was then seeded with the previously mentioned Dantec polyamid seed. The initial plots looked like the one shown on the following page. After overlaying the voltage plot on top of the velocity plot, it __—_.——.___.—————~— Cosworth/E PA Injector measurements (1 -1 5-04) Volts Velocity [mls] 0 50 100 Figure 36: Average plot of early experiments. 56 was proposed early on that the first spike corresponded to the injector opening and that the remaining oscillations were due to pressure waves. This was later found to be partially correct. At the time, it was thought that the pressure waves reflected back to the surface of the beaker containing the fuel. However, when wave speeds were estimated using the following equation and, it was determined that the speed oscillations was far to c: E_h (17) slow. In this equation E is the Young’s modulus, h is the wall thickness, p is the density of the liquid, and R is the inner radius of the tube. At that point in time, the cause of this oscillation was unclear. In order to observe the effects of pressure waves, the fuel supply line was modified. Two tests were designed: the first tube was a 20-inch rubber tube, the second a 15-inch copper tube. The resulting velocity plots are shown in Figures 35 and 36. From these graphs, it was evident that the type of fire] delivery line affects the rate and duration of oscillation. The copper tube shows the greatest amplitude and longest duration of oscillation, while the rubber tube has the smallest amplitude and shortest duration. The reason for this is that the walls of the rubber tube appear to absorb pressure fluctuations while the rigid walls of the copper tube do little to absorb them. Because the purpose of this investigation is to isolate the variability of the fuel injector, the long rubber tube is preferred. This was later changed to a clear nylon tube for viewing purposes. 57 Injector Centerline Velocity using a 15" copper fuel delivery tube 11 d .0 0'1 Centedine Velocity [rer] O . .6 .. 01 1:1 1—— l 50 100 150 ‘ 200 Timelms] Figure 37: Velocity profiles for a 15-inch copper fuel delivery line. Injector Centerline Velocity using a 20" rubber fuel delivery tube 1:11:01: .0151: manomumcn-n 1 1 Centerline Velocity [mls] 1 .0 CD I I 1 I | I I 0 ’ 50 100 ‘ 150200 Figure 38: Velocity profile for a 20-inch rubber fuel delivery line. Seeding Another interesting observation was that the shape of the velocity profile had a tendency to change throughout time. Several causes were proposed. One thought was 58 that as the fuel beaker emptied, the distance traveled by the pressure waves was shortened. Another possible explanation was that the seed was building up in the injector and plugging it. This theory was developed after observing a thin film of seed that remained on the walls of the beaker that supplied fuel to the system. To test this theory, STP Super Concentrated Fuel Injector Cleaner was run through the injector undiluted. The cleaner was allowed to soak in the injector and then purged the following day. After cleaning the injector, data was again collected. These velocity profiles resembled earlier profiles, so it was determined that the injector was in fact plugging due to seeding the flow. To remedy this problem, a microbubble seeding technique was devised. To accomplish this, water was placed in a high-speed blender with a small amount of concentrated liquid soap. When the blender was turned on, air was entrained and finely distributed into the water. The soap coated these bubbles and slowed down diffusion allowing the bubbles to remain suspended in the water for several minutes. This method resulted in greater data rates and much more consistent velocity profiles. The size distribution of these bubbles can be seen in the PDA bar graph that follows. Counts 200 7 0.000 200.000 400.000 PDA 0 [pm] Figure 39: Bubble sizes used to seed the flow. 59 The following profiles show how seed eventually plugs the injector, alters the velocity profile, and how the use of bubbles remedies this problem. 1 PDA U1-Meon[m/s] PDA U1 -Meon [m/s] 1.0‘ .7 ; ID] 1 : I 0.87 777777777 t 7777777777777777 7: 77777 0.8 ---------- ------- 7 -------- ----- 0.6:} 77777777 i 7777777 t 777777 i 77777 0.6:: -------- E --------------- 7: ----- 1..., -------- 1 ------- - ------ a ----- 0.4:: ........ 1 ................ a ..... 02.. ........ g ....... .. 021: ........ 1 ............... 1: ..... 00; E ‘ ‘é 0.0? l . . 41277 77777777 f 77777777 7 771: 77777 41.2: -------- i -------- 1: -------- 1: ----- ---------- ------ - 100.000 200.000 300.000 . 100000 . 200000 . 3001000 - Angle Bin [deg] Angle Bin [deg] PDA UI-Meon [mls] 3 PDA U1-Meon[m/s] 4 100 j I I 1-0 I i if 0.8:: -------- j 7777777 ' 77777777 7: 77777 0.8:: -------- :1 ------- I -------- i ----- 0.5; 77777777 777777777777777 77777 0.63> } ------- ' -------- 7: ----- 0.47 777777777 t 777777777777777 1 77777 0.4“ -------- f --------------- 7, ----- 0.2:; -------- j ------------ i ----- 0.2: -------- j -------------- a: ----- 00 i . 0.0? : -0.2< --------- 1 -------- . ------ 1' ----- 02:1 -------- l -------- 1' ------- 1: ----- 4.41 ----- . 3.4:: -------- é -------- ----- 100.000 200.000 300.000 - 100000 . 200000 - 300000 Angle Bin [deg] Angle Bin [deg] PDA U1-Meon[m/s] 5 1.00 f T f 0.8;: 77777777 :r 7777777 i 77777777 i 77777 0.5: --------- ,1 --------------- 7: ----- 0.4;L i“ """"""""" ‘E “““ 021 --------- 1 ------------ J. ----- 0.0? i -ll : 1.2:: ........ 1 ........ ll ....... .= ..... ----- 100.000 200.000 300.000 Angle Bin [deg] Figure 40: Velocity profiles taken through time with seed and water. 60 PDA Ul-M eon [mls] PDA U1-Meon[m/s] 1.0 . 7’ : 1.0 . v r 0.87 --------- r -------- " I ‘* l 0.87 777777777 r 0.5‘ """"" ‘ """"" 0 I 7L I 0.67 --------- f 0.4‘ ““““ ‘ """" ‘ 1 1 I 0.47 --------- f ._ ........ i. ........ o . "72.. : | 0.24 t 0.0' ' I ' " ‘ e .. . 0.07 -0.27 --------- ' -------- 17 ; [ r l -0.27 --------- r -0.47 ---------------- " : e i e i e . ‘ -0.47---------r . A - A . . 20 . 300.000 ' ‘ ' ' ' ' ‘ 100 0T" l B' 0 :00 100.000 200.000 300.000 9 e '"l 99] Angie Bin [deg] PDA U1-Meon[m/s] 4 1 0 PDA U1-Meon[m/s] ' 7’ : 1.0 f . . 0.87 --------- 7 4 ; ' g " . 087 --------- e ---------------- 1 ----- 0.6‘ """"" t 0 : : 0 i 06' --------- t --------------- 7" ----- 0.4? -------- f 'i I I 'i I 04‘ --------- t -------------- Jl ----- 0.2" """" If ‘1 r I ‘f I 0.24 --------- t ----------- J. ..... 0-0‘ 1 1+ . " ; 0.0 v‘:~‘w *1 W74 7 . -0.2‘ """"" r 1* 1 : ‘* : -0.277 77777777 i 7777777777 7i 77777 —0_471 -------- r 1f : j 5 C 5 3 5 ‘ .0‘411. -------- f ........ 1 ..... 1 ..... 100.000 200.000 300.000 100:000 7 2005000 7 3005000 7 Angle Bin [deg] ' _ ' ‘ Angle Bin [deg] PDA UI-Meon [m/s] 5 1.0 I T r 0.87 --------- f 0.67 --------- :~ 0.4 --------- i 0.27 777777777 f 0.07 ' 70.27 777777777 '1 1t : 0471-7777777: _ 100.000 200.000 300.000 Angle Bin [deg] Figure 41: Velocity profiles taken through time with water and bubbles. 6] Air Pockets Up until this point, mass flow calculations were performed assuming plug flow. As mentioned earlier, this assumption proved to be inaccurate and did not agree well with cycle-averaged measurements made with the mass balance (over-predicted by 60 %). Assuming the flow was quasi-steady and assuming a laminar parabolic profile was also inaccurate, under-predicting by 45%. At this point, it was determined that the flow could not be assumed as quasi-steady. The equations developed by Brereton [14] and outlined in Section 1.5 and Appendix A of this report were then employed. After the program written to perform these calculations was completed and debugged, it was run using centerline velocity data to find the mass injected per cycle. These results over-predicted the mass injected by about 30%. It was then proposed that the system might have air in the injector. The equations used determine the mass flow at the location of the centerline velocity measurement. In order to find the mass injected by the injector, it was assumed that what went into the injector must exit. Since the calculations were performed during the duration of the voltage applied to the injector, air in the injector could allow more fuel to exit than entered due to compression of the air pocket. To test this theory, a vacuum pump was connected to the fuel line. The rubber fiiel line was replaced with a clear nylon line so that air bubbles could be observed. The water was also dyed for the same reason. The system was also equipped with extra valves to facilitate the removal of air without removing excessive amounts of liquid. Once the setup was modified, the pump was turned on. It was immediately obvious that there was in fact air in the injector, as bubbles came out of the injector. This was viewed through the quartz tube. It was also clear that air tended to remain in the fuel line. After 62 all the air was removed from the system, new data was collected. The resulting velocity trace did not look anything like previous traces. It did, however, have a very close resemblance to the trace of the voltage applied to the injector. A plot of velocity traces with and without air in the lines is shown on the following page along with the voltage trace. The data from this run was run through the program to find the mass injected per cycle. The average outputted by the program was within 6% of the cycle—averaged measurement from the mass balance. Also, the sharp oscillation at the peak and just after the velocity returns to zero on the purged injector plot have wave speeds similar to the pressure wave speeds calculated earlier. Injector #1: Centerline Velocity and Voltage Plots (4-8-04) .0 or Centerline Velocity [mls] O l -1 i ‘ 0 50 100 150 200 l 1 Time [ms] :— purged injector l —~—- unpurged injector ! L [ -——- voltage j Figure 42: Velocity plots for Injector #1 with and without air. After seeing these results, one obvious question arose: How does this air remain in the fuel injector? It does not appear that this air is simply flushed out of the injector or diffused into the water, because weeks of testing yielded the same oscillating velocity profile. Only when a vacuum was attached to the fuel line did the air come out of the injector. In order to investigate this, a spare Chrysler Hemi injector was milled to reveal the internal components and passages of the injector. The picture of this injector can be seen below. Looking at this picture, there appears to be a fairly large crevice. Further inspection reveals that this is the location where the lower nozzle portion of the injector joins with the upper portion. This could very well be the location where air pockets are trapped inside the injector. / Supply from ECU [ Solenoid windings Valve needle “I Pintle 7H? Figure 43: Cutaway of Injector #2. Note crevice zoom. 64 It would be very interesting to see how the removal of this air influences the variability of the fuel injector. This technique does not allow for that comparison directly. In order to measure the mass injected using centerline velocity measurements, it was assumed that what goes into the injector comes out. If air is present, this is not the case as the bubble is capable of compressing. Thus it is impossible to determine the precise mass injected for comparison with air in the injector using this technique. In conclusion, air located in the fuel system and/or the injector itself drastically changes centerline velocity. Since most previous studies measure the fuel spray, these bubble dynamics have gone largely unnoticed. Removing the bubbles produces an accurate centerline velocity profile that can then be used as an input to solve more precisely for the mass injected for each injection event. 65 References 66 REFERENCES [l] Nixon, M., littp;//www.motorcycleproiect.com/motorcycle/tcxt/iniect.html . [2] Sparks, L., http:(Velma/thunder.com/fuel‘ib201njccti0119112011istoryhtm . [3] Woron, W. “Road Test: 1957 Chevrolet Corvette,” Motor Trend, April 2003. [4] HowStuffVVorkscom educational website, http:/'/auto.liowstuffworks.com/fuel- iniectionhtm . [5] Heywood, J. 3., Internal Combustion Engine Fundamentals, MCGraw-Hill Publishing Company, 1988. 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