45th AIAA/ASME/SAE/ASEE Joint Propulsion Conference & Exhibit 2 - 5 August 2009, Denver, Colorado AIAA 2009-5115 Tensile Tests of Paraffin Wax for Hybrid Rocket Fuel Grains John D. DeSain*, Brian B. Brady, Kelly M. Metzler, Thomas J. Curtiss and Thomas V. Albright The Aerospace Corporation 2350 E. El. Segundo Blvd., El Segundo CA 90245-4691 Abstract: The tensile strength, elastic modulus and percent elongation of paraffin wax doped with small concentrations of low density polyethylene (LDPE) where measured. The centrifugal casting process was used to create paraffin wax / LDPE wax hybrid rocket motors. Tensile tests were then performed on samples taken from these test motors. Concentrations from 0 % to 4 % LDPE added to the paraffin wax were tested. The tensile strength, and elastic modulus increased with increasing concentration of LDPE. The results show that paraffin wax motors can be created that have a greater elastic modulus and similar tensile strengths compared to current solid rocket motors based on HTPB rubber motors. However the paraffin wax motors were found to be less elastic than HTPB with a much lower percent elongation. Void formation, tiny bubbles in the paraffin wax created during the casting process, were found to affect the tensile properties measured. Keywords: hybrid rockets, paraffin wax, tensile strength, Young’s modulus * The Aerospace Corporation 2350 E. El. Segundo Blvd., El Segundo, CA 90245-4691 USA. M.S. 2-341 E-mail: [email protected] LDPE = low density polyethylene wax HTPB = hydroxyl-terminated polybutadiene Introduction Paraffin wax based hybrid rocket motors have the potential to replace current solid rocket motors functionality as boost phase launch vehicle components. Wax based hybrid rockets have several advantages to current solid rocket motors based on HTPB/ammonium perchlorate. Wax based hybrid rocket motors are non-toxic, nonhazardous, shippable as freight cargo, potentially carbon neutral1 and they can be throttled for thrust control or shut down in case of an on-pad anomaly and restarted on demand. Since the fuel is non-explosive, the fuel can be fabricated on-site and thus can save in both manufacturing and launch operation costs.2,3 One consideration for using Copyright © 2009 by The Aerospace Corporation. Published by the American Institute of Aeronautics and Astronautics, Inc., with permission. wax as a replacement material for current solid rocket motors is understanding the material properties of wax in comparison to the current motors. This is particularly important for solid rockets sense the fuel has no structural tank to hold it. The fuel material is a solid material that must be stored and held together by the material properties of the fuel grain itself. For large scale motors the tensile properties must be known in order to understand how the fuel grain will respond during storage, assembly and usage. Current solid rocket motors use HTPB rubber as the binding material. The tensile properties have been measured previously for these solid rocket motors.4-6 The material properties of the rubber vary slightly from motor to motor due to variances in the polymerization process that was used to create it. Also the average tensile strength and elastic modulus of HTPB was observed to increase with the addition of additives aluminum and ammonium perchlorate.4,6 The elastic modulus ranges from 3 MPa to 6 MPa depending on the mixture.4,5 The elastic modulus has previously been found to increase with age of the rubber.5 The maximum tensile strength was found to be from 0.75 – 0.87 MPa.4 The strain at maximum tension was found to be around 27 %. Table 1 lists the material properties for several measurements of pure and doped paraffin wax. Pure paraffin wax has a similar maximum tensile strength as HTPB rubber, but a much smaller percent elongation. The paraffin wax material properties change slightly with the melting point of the wax. As seen in table 1, the lower melting point paraffin wax has a slightly larger maximum tensile strength than the high melting point wax and a slightly larger percent elongation. Paraffin wax hybrid rocket motors are usually made by pouring liquid paraffin wax into a mold. The mold is subjected to a centrifugal force during the process of solidifying the hot liquid wax. This centrifugal casting process is used to help avoid cracking and void formation inside the solid paraffin wax as it cools.2 These voids are formed because the liquid paraffin wax shrinks upon cooling by 15-25 % depending on the grade of wax. This shrinking during the centrifugal casting process will form a natural central port through the hybrid motor. Additives have previously been used in these paraffin wax motors to modify the material properties.10 These additives are placed in the paraffin wax while it is still liquid and thus go through the centrifugal casting process. As seen on table 1 only a small addition (3 % by weight) of the additive (a Eastman Kodak proprietary LDPE) was needed to nearly double the tensile strength and increase the percent elongation. Wang et al. previously measured the Young’s modulus was for paraffin wax (326 K melting point) to be 61.4 MPa.11 LDPE is the additive10 that is commonly used to modify the material properties for paraffin wax hybrid motors. LDPE material properties depend on the exact chain lengths involved in the material. In general LDPEs have a melting point from 373 K – 393 K. LDPEs have a tensile strength that is much larger than that of paraffin waxes (4-12.5 MPa). The LDPEs percent elongation range from 90-800 % and the elastic modulus is typically around 1-0.1 GPa.12,13 Thus all the material properties of LDPEs are larger than paraffin waxes. In this study the material properties of tensile strength, elastic modulus and percent elongation were examined for paraffin wax and paraffin wax with LDPE wax added. A paraffin wax rocket motor was made by the typical centrifugal casting process. The dogbones used for the tension tests were then cut from these wax motors. Three different formulations were tested pure paraffin, 2 % LDPE added to paraffin wax and 4 % LDPE added to paraffin wax. Procedure The paraffin wax formulations were heated to 363 K to melt the paraffin wax. The LDPE wax was then added to the hot liquid paraffin wax. The wax sample continued to be heated at 363 K for several hours. The sample was stirred until all the LDPE wax flakes fully dissolved in the liquid paraffin wax. The casting mold used for making the wax motors is shown in figure 1. The mold consisted of two aluminum end caps and a phenolic tube ( 17.0 cm long with a inner diameter of 8.6 cm). To fill the mold with the hot wax, two of the brass fittings were unscrewed. The hot wax was then poured through a funnel into the rocket motor mold. The brass fittings were then reattached to the mold. The mold was heated to 363 K for ~ 2 hrs to insure the wax inside was all liquefied after the pouring. The mold was then placed into a centrifuge and spun at 1500 rpms for several hours while the wax cooled to room temperature. The temperature of the outside of the phenolic tube was monitored during the centrifugal casting process. The aluminum caps were then removed from the mold and the wax motor casting was removed from the phenolic casting tube. Figure 2 shows an end on view of the wax rocket motor after casting. The dogbone-shaped test samples used for the tension tests where then machined out of the casted rocket motor. The dogbone samples were glued to the holders using Miller-Stevens P907 Epoxy. The length of the pull section was 5.08 cm, the cross sectional area was 1.21 cm2. Stronger wax samples where modified to have smaller cross sectional areas of 0.60 cm2. Figure 3 shows an example of a wax dogbone used in the tension tests. The paraffin wax was previously tested for tensile strength and % elongation tests in accordance with ASTM D 412 .7,14,15 The main instrument used in this experiment was an Instron uniaxial testing machine. The specimen was held between two wedge grips, each attached to a crosshead. The upper crosshead was fixed to the vertical columns and remains stationary. The lower crosshead is connected to a screw and an electric motor, which caused it to move up or down, at a prescribed speed selected by the user. The experiment was set to run at two different elongation rates 5.08 mm min-1 or 50.8 cm min-1. The melting point of the paraffin wax-LDPE mixes were measured in a capillary tube. The melting point was measured for 0, 2, 4, 10, 15, 20, 25 and 100 % LDPE in paraffin wax. The paraffin wax does not have a pure melting point and melts over a small range of temperatures. The wax mixtures also do not have a pure melting point, but two rough ranges of melting points. The wax mixtures first slush at around 333 K when the paraffin wax matrix melts and then stay a slush until at higher temperatures the LDPE finally melts. The density of the mixes was also measured. The wax was cut into small pieces and weighed on an electronic scale. The pieces volume was then obtained by volume displacement of methanol in a graduated cylinder. The paraffin wax was purchased from Aldrich chemical company. It had a melting point between 331-335 K. The LDPE wax was purchased from Paplin Products and had a melting point between 372-376 K. Results Figure 4 shows a plot of the stress vs. strain on four pure paraffin wax samples pulled at two different strain rates. Figure 5 shows a plot of pure paraffin wax with the relevant areas of the stress vs. strain curve marked. The plots have a yield point from which the maximum tensile strength was obtained. The elastic modulus was obtained by a linear fit of the region of the curve exhibiting Hookean behavior. Since the beginning of the curve shows a toe, the x axis intercept of the linear fit was used as the “corrected zero” strain for obtain the percent elongation. The measured material properties are shown in table 2 and 3. Table 2 shows the measured elastic modulus (in MPa) and percent elongation for the paraffin wax samples. Table 3 shows the measured maximum tensile strength (MPa). Figure 6 shows the melting point(s) observed for paraffin wax and LDPE. The red points show the softening region of the paraffin wax. The softening point was taken as the region where the wax turns from a solid to a cloudy slush. The blue points show the final melting point of the mixture. The melting point was indicated as where the wax turns from a cloudy slush to a clear liquid. The final melting point decreased as the percentage of LDPE in the paraffin wax decreased. The final melting point was previously related to the melting of the LDPE in the paraffin wax matrix 16. The melting point previously observed for LDPE and paraffin wax is shown by the green boxes.16 Figure 7 shows the density measured for the paraffin wax and LDPE samples. There is a slight trend of increasing density with increased concentration of LDPE in the paraffin wax. However any such trend is overwhelmed by the variance between samples. The large variance in the paraffin wax density demonstrates the paraffin waxes ability to form both amorphous and crystalline areas that have significant variability in the density of the paraffin wax. Discussion Except for the 4 % data the current experimental results were in good agreement with the previous results from experiments.7 Some of the 4 % samples had extensive bubble formation, as shown in figure 8. These bubbles appear to be a result of small air leaks in the mold itself. As the wax cools inside the mold, the wax begins to contract. This contraction creates a small vacuum that will then bring in outside air. A second run of the 4 % in a mold that was checked using a high vacuum line to be air leak free was also conducted. As seen in figure 9, these samples were devoid of these tiny bubbles. The tensile strength and elastic modulus were both greater for the non-bubbled dogbones than the samples that had bubbles. Previously it was observed that as the percentage of the polyethylene waxes was increased, all physical properties increased to produce a harder, tougher wax.7 Figure 10 shows a plot of the paraffin wax tensile strength data as a function of the purity of the wax. Included in the figure is the Eastman Kodak data for waxes of similar melting points to the current experiments. In general the tensile strength was found to increase with increased concentration of LDPE in the paraffin wax. Much of the 2 % data is slightly higher than expected based on the trend. The average maximum tensile strength previously measured for HTBP solid rocket fuel was 0.89 MPa.4-6 Essentially the pure paraffin wax has similar maximum tensile strength to HTBP and the addition of small percentage of polyethylene only increases the maximum tensile strength beyond what is commonly found in HTPB based motors. Figure 11 shows a plot of the paraffin wax elastic modulus data as a function of the purity of the wax. The elastic modulus increases as the percent of LDPE was increased. The data in figure 11 was fit to a linear equation where the elastic modulus of the LDPE doped paraffin wax was determined as a function of paraffin wax purity. -48.8 (purity percentage) + 5121 = elastic modulus (MPa) (1) The average elastic modulus previously measured for HTPB solid rocket fuel was 5.44 MPa.4-6 The paraffin wax with the LDPE would have a much greater elastic modulus than the HTPB based solid rocket fuels. Figure 12 shows a plot of the paraffin wax percent elongation data as a function of the purity of the wax. The percent elongation may slightly increase as the percent of LDPE was increased. The data in figure 12 was fit to a linear equation where the percent elongation of the LDPE doped paraffin wax was determined as a function of paraffin wax purity. -0.037 (purity percentage) + 4.28 = percent elongation (%) (2) However the data trend is heavily dependent on one Kodak measurement at 3 %. Removing that point strongly suggests no significant change in percent elongation with increase LDPE. The average percent elongation previously measured for HTBP solid rocket fuel was 36.5 %.4-6 Even a pure LDPE wax motor would not have this much elongation. Thus doped paraffin wax motors do not have the same amount of elasticity that the rubber based fuels have. The advantages of modifying paraffin with polyethylene waxes are higher softening points7, increased hardness, greater tensile strength, larger elastic modulus and larger percent elongation than pure paraffin wax based motors. Another advantage of addition of polyethylene to the paraffin wax was the production of a more uniform wax. Previous work7 has found that unmodified paraffin wax when solidified contains large pieces of crystalline material and large pieces of amorphous material. The addition of small percentages of polyethylene wax caused the large crystalline and amorphous areas to become smaller and more uniform. This uniformity explains why some the physical properties such as hardness, tensile strength, and percent elongation were significantly improve with such a small addition of polyethylene. However the density measurements didn’t show a significant decrease in the variance with increased LDPE concentration. The pure LDPE has a rather large spread in density from measurement to measurement. This would indicate the LDPE probably has a large range of chain lengths in it. The addition of the LDPE wax also likely increases the surface tension in the liquid paraffin wax. The viscosity of the liquid paraffin wax was previously observed to increase with increased concentration of LDPE wax (from 3.5 MPa s for pure paraffin wax to 4.8 MPa s for 97 % paraffin wax at 394 K).7 Since they are both related to the strength of intermolecular forces of the liquid, surface tension tends to increase with increased viscosity. Surface tension encourages the evaporation of small droplets, and the collapse of small bubbles. Thus the increase in surface tension could potentially help suppress the formation of tiny bubble voids which thus aids in the aggregation of voids towards the center of the paraffin wax motor during centrifugal casting. The presents of these voids would certainly decrease the tensile strength of the tested material. As seen with the 4 % data voids clearly affected the maximum tensile strength and the elastic modulus. Bader previously observed the change in the melting point with the addition of LDPE to paraffin wax16 by using a differential scanning calorimeter (DSC). He found that the polymer had no big influence on the melting point and the melting range of the paraffin wax, but the paraffin wax seems to have a big influence on the melting point of the polymers tested. For 45 % LDPE doped in paraffin wax, the peak temperature was at about 373 K, whereas the melting point of the pure LDPE was at about 387 K. He theorized that the reason for this decrease of the melting point of the polymers seems to be the paraffin wax. The paraffin wax melts at lower temperature than the polymer. This paraffin fluid in the polymeric matrix seems to decrease the forces between the molecule chains of the polymers and with this, also the melting point. The results of the current melting point experiment agree with these previous observations. They also suggest for the small concentrations of LDPE used in hybrid motors little change in the bulk paraffin wax melting point should be expected. The current experiments suggest only a modest amount of LDPE may be beneficial to the paraffin wax motor. The addition of LDPE makes a stiffer wax motor, however the stiffest motors tested tended to also fracture at slightly lower maximum stress. Thus the stiffest motors may be too brittle for practical use as motors. Indeed the 4 % motor actually cracked in the casting process. Most common wax motors us 2% or less LDPE which has been shown to slightly increase tensile strength and the elastic modulus with no adverse effects to elasticity. There is no positive benefit to the temperature tolerances of the rocket motor at these low concentrations of LDPE. The major upside to using the LDPE would appear to be the Kodak observations of the crystal domain Conclusion The tensile strength, elastic modulus and percent elongation of paraffin wax doped with small concentrations of LDPE where successfully measured. The paraffin wax samples were prepared by the centrifugal casting process that is commonly used to cast paraffin wax hybrid motors. The maximum tensile strength and elastic modulus increased with increasing concentration of LDPE. The results show that paraffin wax motors can be created that have greater elastic modulus and similar tensile strengths to current HTPB rubber hybrid motors. However the paraffin wax motors are found to be less elastic than HTPB rubber with a much lower percent elongation. The addition of LDPE potentially has the advantage of reducing the amount of small voids in the paraffin wax. Table 1. Previous measurements of material properties of paraffin wax and doped paraffin wax. Listed are the melting point of the paraffin wax used, the additive, purity, tensile strength (MPa) and percent elongation. Paraffin Wax Additive Percent purity 52 –54 C 52 –54 C None Epolene C-15 Wax Epolene C-15 Wax Epolene C-15 Wax None Epolene C-15 Wax Epolene C-15 Wax Epolene C-15 Wax ethylene vinyl acetate 16 %/ Petroleum resin 5 % Graphite foam 100 99 .5 52 –54 C 52 –54 C 60 –63 C 60 –63 C 60 –63 C 60 –63 C 66 C 56 C 99 97 100 99 .5 99 97 Tensile Strength MPa 1.38 1.38 1.38 1.86 1.03 1.03 1.24 1.93 79 Percent Elongation Reference 0.8 0.8 7 7 0.8 7 1.6 7 0.6 0.6 7 7 0.6 7 1.1 7 8 3.10 1.30 9 Table 2. Elastic Modulus and percent elongation measured for paraffin wax samples in MPa. Sample Pull rate cm min-1 Percent elongation Elastic modulus in MPa Pure wax 50.8 0.35 239 Pure wax 0.51 0.51 192 Pure wax 0.51 0.55 207 Pure wax 50.8 0.39 260 2 % LDPE 0.51 0.71 412 2 % LDPE 0.51 0.74 379 2 % LDPE 0.51 0.59 314 2 % LDPE 0.51 0.92 362 2 % LDPE 0.51 1.02 389 2 % LDPE 50.8 0.71 365 4 % LDPE* 0.51 0.33 384 4 % LDPE* 0.51 0.56 316 4 % LDPE* 0.51 0.90 329 4 % LDPE* 0.51 0.35 356 4 % LDPE* 0.51 0.67 313 4 % LDPE 0.51 0.59 384 4 % LDPE 0.51 0.35 462 4 % LDPE 0.51 0.54 392 * Showed extensive bubble formation. Table 3. Maximum tensile strength measured for paraffin wax samples in MPa Sample Pull rate cm min-1 Pure wax 50.8 Pure wax 0.51 Pure wax 0.51 Pure wax 50.8 2 % LDPE 0.51 2 % LDPE 0.51 2 % LDPE 0.51 2 % LDPE 0.51 2 % LDPE 0.51 2 % LDPE 50.8 4 % LDPE 0.51 4 % LDPE 0.51 4 % LDPE 0.51 4 % LDPE 0.51 4 % LDPE 0.51 4 % LDPE 0.51 4 % LDPE 0.51 4 % LDPE 0.51 * Showed extensive bubble formation. Tensile strength MPa 0.863 0.885 0.994 0.920 2.511 2.513 1.863 2.602 3.008 2.437 1.28* 1.23* 1.37* 1.25* 1.26* 2.08 1.46 1.88 1. Lyne, J. E.; Naoumov, V. I.; Scholes, J.; Dodge, M.; Elton, B.; Wozniak, P. Austin, D.; Combs, C. “ First Steps in the Development and Testing of Nontoxic, Bioderived Fuels for Hybrid Rocket Motors” 43rd AIAA Aerospace Sciences Meeting and Exhibit, Reno Nevada, January 2005. 2. -, M. A.; Zilliac, G.; Cantwell, B.; De Zilwa, S. R. N.; Castellucci, P. “Scale-Up Tests of High Regression Rate Paraffin-Based Hybrid Rocket Fuels” Journal of Propulsion and Power, Vol. 20, No. 6, Nov.–Dec. 2004, pp. 1037–1045. 3. Altman, D., “Hybrid Rocket Development History,” AIAA Paper 91-2515, June 1991. 4. Maruizumi, H.; Kosaka, K.; Suzuki, S.; Fukuma, D. “Development of HTPB Binder for Solid Propellants” 24th AIAA/ASME/SAE/ASEE Joint Propulsion Conference & Exhibit 11-13, Boston Massachusettes, July 1988. 5. Kivity, M.; Hartman, G.; Achlama, A. M. “Aging of HTPB Propellant” 41st AIAA/ASME/SAE/ASEE Joint Propulsion Conference & Exhibit 10-13, Tucson Arizona, July 2005. 6. Chung , H. L.;Kawata, K.; Itabashi, M. Journal of Applied Polymer Science 1993, 50, 57-66. 7. “Epolene Waxes as Candle Additive” Eastman Chemical Company Kingsport, TN 1998. 8. Jones, Richard L. “Process for producing a petroleum wax composition” United States Patent 5010126 CONOCO INC (US) 04/23/1991. 9. Richard Wirtz, Alan Fuchs, Venkat Narla, Yuyi Shen, Tianwen Zhao and Yanyao Jiang AIAA-2003-513 41st Aerospace Sciences Meeting and Exhibit, Reno, Nevada, Jan. 6-9, 2003 10. Karabeyoglu, M. A.; Altman, D.; Cantwell, B. J “High Regression Rate Hybrid Rocket Propellant” U.S. Patent 6684624, Feb. 4 2004. 11. Wang, J.; Severtson, S. J.; Stein, A. “Significant and Concurrent Enhancement of Stiffness, Strength, and Toughness for Paraffin Wax Through Organoclay addition” Adv. Mater. 2006, 18, 1585-1588. 12. “Typical Properties of polyethylene wax” Engineering Laboratories Inc. Oakland, NJ 2008. http://www.plasticballs.com/lopoly.htm 13. “Low Density Polyethylene (LDPE)” Curbell Plastics Inc. Orchard Park, NY 2008. www.curbell.com 14. “Standard Test Methods for Vulcanized Rubber and Thermoplastic ElastomersTension” ASTM D 412 – 06a ASTM International, West Conshohocken, Pa 2006. 15. “Standard Test Method for Tensile Properties of Plastics” ASTM D 638-03 ASTM International, West Conshohocken, Pa 2003. 16. Michael Bader “Microencapsulated Paraffin in Polyethylene for Thermal Energy Storage” Department of Chemical and Material Engineering, The University of Auckland, New Zealand, February 2002. Figure 1. Photograph of the paraffin wax rocket motor casting mold. Figure 2. Photograph of the paraffin wax rocket motor after casting. Figure 3. Photograph of a dogbone made of paraffin wax used for the tension tests. Figure 4. Plot of the stress versus strain for four separate pure paraffin wax samples. The four samples were pulled at two different pulling rates 50.8 cm min-1 (samples 1 and 4) and 0.51 cm min-1 (samples 2 and 3). Figure 5. Plot of the stress versus strain for a sample of pure paraffin wax (sample 3 in figure 4). The linear fit to the Hookean region of the plot yields the elastic modulus (slope = elastic modulus = 2.07 MPa). The yield point is marked out where the maximum tensile strength was observed (0.994 MPa). The percent elongation (0.55) is obtained as the difference in the elongation at the yield point to the x-intercept of the linear fit to the Hookean region of the plot. Figure 6. The melting point of paraffin wax/ LDPE mixtures. The red points are the softening point of the paraffin wax. The blue points are the final melting point of the mixture. The green boxes are the two melting peaks observed by Bader.15 Figure 7. The density (g/cm-3) of paraffin wax/ LDPE mixtures. Figure 8. Photo of the broken dogbone for the 4 % LDPE in paraffin wax. There are clearly observed voids (tiny bubbles) throughout these dogbones. Figure 9. Photo of the dogbone for the 4 % LDPE in paraffin wax. The paraffin wax was cast after checking the mold for air leaks. There are clearly less voids (tiny bubbles) throughout these dogbones than those in figure 8. Figure 10. The tensile strength (MPa) of the LDPE doped paraffin wax samples as a function of paraffin wax purity. Figure 11. The elastic modulus (MPa) of the LDPE doped paraffin wax samples as a function of paraffin wax purity. Figure 12. The percent elongation of the LDPE doped paraffin wax samples as a function of paraffin wax purity. Brass fittings used to pour wax into mold Aluminum end cap Phenolic tubing Aluminum end cap Fig 1. Fig 2. 5.08 cm 1.27 cm 0.95 cm Fig 3. 1.0 Stress (MPa) 0.8 0.6 0.4 -1 Sample 1 50.8 cm min -1 Sample 2 0.51 cm min -1 Sample 3 0.51 cm min -1 Sample 4 50.8 cm min 0.2 0.0 0.0 Fig 4. 0.5 1.0 Strain % 1.5 2.0 1.0 Slope = elastic modulus 0.6 Stress (MPa) Corrected zero strain point removing toe Stress (MPa) 0.8 0.4 0.2 Maximum tensile strength Yield point Percent elongation 0.0 0.0 Fig 5. 0.5 1.0 Strain % 1.5 2.0 370 Temperature K 360 350 340 330 0 Fig 6. 20 40 60 Percent LDPE in paraffin wax 80 100 1.10 -3 Density (g cm ) 1.05 1.00 0.95 0.90 0.85 0 Fig 7. 20 40 60 Percent Polyethylene 80 100 Figure 8. Figure 9. 3.0 Tensile Strength (MPa) 2.5 2.0 1.5 1.0 96 Fig 10. 97 98 Percent purity of paraffin wax 99 100 450 Elastic modulus (MPa) 400 350 300 250 200 96 Fig 11. 97 98 Percent purity of paraffin wax 99 100 Percent elongation 1.0 0.8 0.6 0.4 96 Fig 12. 97 98 Percent purity of paraffin wax 99 100
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