Faculty of Science – Chemistry Ó William L. Primrose, 2019 Matrix and pH Effects on the Degradation Kinetics of Xanthates in Mining Waters William L. Primrose, Adrian M. Batista. Supervisor: Dr. Kingsley Donkor ARTICLE INFO ABSTRACT Date of Submission: Determination of optimal pH conditions for a xanthate solution representative of a real matrix in an industrial setting (such as a flotation tank or a tailings pond) was researched to help ensure mill efficiency in mines. The primary method for analysis was the use of headspace GC-MS. Aqueous samples of xanthates in basic solutions without minerals were tested for degradation by testing for the generation of carbon disulfide (CS2). Potassium isopropyl xanthate (PIPX) and potassium amyl xanthate (PAX) were primarily studied and rate constants were compared to determine optimal pH conditions for the slowest degradation of individual xanthates. The rate constant for 110.6 ppm PIPX was found to be 5.79 x 10-5 h-1 at pH 7.73; at the same pH, the rate constant was found to be 3.91 x 10-6 h-1 for 1075.2 ppm. The rate constant for PAX was found to be 5.43 x 10-5 h-1 at pH 9.08, 1.23 x 10-5 h-1 at pH 9.26, 8.12 x 10-6 h-1 at pH 9.34, and 4.36 x 10-5 h-1 at pH 9.48. 30 May 2019 Keywords: Xanthate Decomposition Rate Carbon disulfide Gas Chromatography-Mass Spectrometry Introduction mineral via xanthate with 100 % efficiency; Xanthates are a class of chemical that are consistently used in the mining industry one of the leading problems with xanthates in the mill processes of large mines is that during their mill process as a way to collect they are used in aqueous conditions minerals from ore samples by way of floatation. They are popular due to their low wherein water is a key factor in the degradation of the xanthates in solution. cost and their efficient ability to bind to metals of interest such as copper, nickel, This degradation releases carbon disulphide which in turn renders the ability zinc, and iron (Shen et al., 2016). Xanthates of that molecule to bind to a mineral inert share similarities in their dithiocarbonate without the presence of a negatively groups and vary in their alkyl chains, written as R-OCS2- (Shen et al., 2016). The charged sulphur. Thus, a deeper understanding of xanthate kinetics in negatively charged sulphur is what binds to aqueous conditions is necessary to the metals in the floatation tanks and is optimize mill processes. frothed to float it to the top for collection (Kemppinen et al., 2014). However, the Carbon disulphide (CS2) is a liquid at room temperature but is highly toxic and volatile process is not a simple extraction of with a vapour pressure of 48.210 kPa at 25 1 Faculty of Science – Chemistry Ó William L. Primrose, 2019 °C (World Health Organization, 2005). As such, minimizing the generation of CS2 not Aldrich Canada Ltd., Oakville, Ontario, Canada. New Afton Gold Mine in Kamloops, only has an economic impact through lessened use of xanthates over time, it also BC, Canada provided solid xanthate samples. Nearly all samples were dissolved has a health and environmental implication if less CS2 is produced due to its in 18 MW water; where 18 MW water was unavailable, deionized water was used tendency to accumulate thus posing a risk to workers nearby as well as the instead. environment surrounding a given mine (Shen et al., 2016). Instrumentation Due to the high volatility of CS2, testing for its presence is easily done in a sealed Agilent 7890B-GC coupled 5977A-MS using an Agilent PAL3 auto sampler with a headspace vial. As such, in this project xanthate degradation was studied using headspace injection tool. An HP-5MS 5% phenyl methyl silox capillary column was headspace Gas Chromatography-Mass Spectrometry (GC-MS). The GC was used for used. For the remainder of the instrument parameters, see Table 1. the quantification of CS2 generated and the MS was used for confirming the presence Table 1. Instrument and Method Parameters of CS2 by looking for a peak at 76 m/z. Following the previous study by Batista (2018) which showed xanthate decomposition follows first order kinetics, this project’s goal was to study the effects of pH on the decomposition behaviour of xanthates in aqueous solution. In particular, this research is focused on the comparison of different xanthates using the same method, something not currently found in the literature. After developing the method for detection of CS2 under varying pH, the goal was to compare four different xanthates; two were primarily studied and the rest will be studied in future trials. Reagents Pure, analytical-grade CS2 was readily available from the Thompson Rivers University (TRU) Chemistry Department and was originally purchased from Sigma- All trials were isothermal and run on TRU’s Sample Volume (mL): 0.075 Incubation Time (min): 15 Heat Agitator: On Incubation Temperature (°C): 30 Heat Syringe: On Syringe Temperature (°C): 46 Pre Injection Flush Time (s): 10 Sample Sample Vial Penetration Depth (mm): 15 Sample Vial Penetration Speed (mm/s): 50 Sample Aspirate Flow Rate (mL/min): 12 Sample Post Aspirate Delay (s): 1 Injection Signal Mode: Plunger Up Inlet Penetration Depth (mm): 45 Inlet Penetration Speed (mm/s): 50 Pre Inject Time Delay (s): 0.5 Injection Flow Rate (mL/min): 1 Post Inject Time Delay (s): 0.5 Flush Time (s): 60 Continuous Flush: On Advanced Agitator Speed (rpm): 250 Agitator On Time (s): 15 Agitator Off Time (s): 5 2 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Run time for the sample was set to 5 min and the GC oven was set to 33 °C; the intent Sample Preparation was to set a temperature close to ambient temperature to replicate mill conditions. was added to a 500 mL volumetric flask and diluted to the mark with 18 MW water to However, cooling the oven to 25 °C proved to be difficult, so 33 °C was a choice made prepare stock solutions of approximately 100 ppm. Stock solutions we remade after a from instrumental limitations. The GC was run with a split ratio of 100:1 and a split flow solution was a week old and were made from 98% pure potassium isopropyl of 100 mL/min. The MS began its scan at 1.75 min following xanthate (PIPX) and 97% pure potassium amyl xanthate (PAX) Each sample vial was the 1.75 min solvent delay and scanned between BLANK and BLANK m/z. a 20 mL headspace vial with 10 mL of stock solution added to it. The pH level was Calibration – Preparation of CS2 adjusted using 0.012 M sodium hydroxide; Shen et al. used sodium hydroxide to set pH Stock solution of CS2 was made by adding 79.4 µL of pure CS2 to 100 mL of 18 MW in their method and as such their method was applied here, though a buffer solution water, forming 100 ppm solution. Then, 10 mL of the 100 ppm stock solution was may also be a viable method of pH control for future studies. The pH level was diluted with 18 MW water in a 100 mL adjusted to various levels as per Tables 3 – volumetric flask to form 10 ppm stock 6. Approximately 0.0500 g of solid xanthate solution. The 10 ppm stock solution was used to generate the standards for the Results and Discussion calibration curve as per Table 2. Calibration Table 2. Preparation of Calibration Curve The calibration curve, shown in Figure 1, Volume Stock Final Volume Concentration added (mL) (mL) (ppm) 0.5 100.0 0.05 shows the concentration of CS2 in ppm of the standards and the respective peak area 1.0 100.0 0.10 5.0 100.0 0.50 10.0 100.0 1.00 15.0 100.0 1.50 was found to be 0.0023 ppm and the limit of quantification (LOQ) was found to be 0.023 20.0 100.0 2.00 ppm. observed; the calibration curve showed good linearity. The limit of detection (LOD) As per the recommendation of Li et al. Minimizing Loss of CS2 (2015), the standards were agitated in their vials for 15 min prior to injection. One goal of the method development was to increase the reproducibility of the trials. Headspace vials with a 20 mL capacity A concern was raised that due to its volatility, some CS2 may have been were used for all standards and 10 mL of the stock solutions were added to the vials. escaping the headspace vials each time a vial cap was pierced by the heated injection 3 Faculty of Science – Chemistry Ó William L. Primrose, 2019 syringe. Thus, trials a – f were done in the following manner: for each pH level, 8 the R2 values become 0.9033, 0.8727, and 0.9518, respectively. This observation is left separate vials were created under the same conditions (10 mL aliquot of xanthate as an aside to show the projected correlation because the values go closer to sample in same pH condition) and sealed with brand new headspace caps with the unity, however statistical determination of which data points to remove was not intention that each cap would only be pierced once. Therefore, vial 1 would be completed and so the data herein is reported as recorded. Data for trials g – p pierced at hour 1, vial 2 at hour 2, and so on and so forth. Assuming that the rate of are shown in Figure 3 and Table 8. decomposition remains constant between trials, then the data from each vial should Final Results still follow a linear, first-order curve. Further, if it was true that the use of an evolution increases as pH is decreased and furthermore, the rate follows a linear trend. individual vial was skewing the precision, then the R2 value on the corresponding Shen et al. (2016) also showed a similar trend with sodium isobutyl xanthate (SIBX) curve would be expected to increase compared to a curve from a method using wherein the xanthates decomposed to the greatest extent at approximately pH 2 and only one vial being pierced every hour. decomposed less and less as pH increased. However, increased reproducibility was not Their research was primarily focused on observed. Instead, trials a – f heralded developing a method to act as a foundation erratic results from data point to data point for researching these compounds further, and no discernable trend was found as seen in Figure 2 (Table 7). whereas the aim of this project was to begin filling in specific gaps in the Overall, the data shows that the rate of CS2 literature regarding rate constants. Using a method which used a single vial per trial which is pierced multiple times over a set time interval drastically The rate constant for 110.6 ppm PIPX was found to be 5.79 x 10-5 h-1 at pH 7.73; at the improved results and a trend was found. Over time, CS2 evolved in a manner same pH, the rate constant was found to be 3.91 x 10-6 h-1 for 1075.2 ppm. While the rate consistent with first order kinetics and the reproducibility was within reasonable is noticeably smaller at the higher concentration, and assuming a constant limits (R2 = 0.8641 – R2 = 0.9811). In trials n rate, is should follow that the rate constant through p, however, an instrument error resulted in the data being skewed for the will decrease as per the equation Rate = k[xanthate] i.e. as the xanthate first data point in each series. For trials n, o, and p, the R2 values observed were 0.7394, concentration increases, a constant rate will cause a decrease in rate constant. As 0.7383, and 0.8554, respectively. However, if the first data point in each set is discarded, such, no major difference in rate between 4 Faculty of Science – Chemistry Ó William L. Primrose, 2019 concentrations was observed at this level of experimentation. by by-products such as carbon disulphide gas. This will help ensure that mines can The rate constants for potassium amyl create environmentally sustainable procedures and processes to keep their xanthate (PAX) are shown in Table 8 and 9, but Table 9 shows the trend as pH level workers in safe conditions and their mills operating at peak efficiency. rises. The slowest rate constant appears at pH = 9.34. The rate constant begins to Future Work increase again slightly at pH 9.48 which may be a result of the alkaline conditions The next step for this project is to run more trials with additional xanthates, namely facilitating the appearance of dixanthogen compounds or dithiocarbonates which sodium isobutyl xanthate (SIBX) and sodium ethyl xanthate (SEX) for further have been detected in more basic solutions (Shen et al., 2016). This suggests that there comparison of common xanthates used in the industry. As well, calculation of figures exists a “sweet spot” for pH level such that higher pH slows the rate of decomposition, of merit and validation of the method will be done in the next stages of the research. but pH that is too high allows side reaction rates to increase, thus using up xanthates Additionally, trials should be done in a buffer solution as well to determine the anyway. Further trials will have to be efficiency of adjusting the pH using solely conducted over smaller pH intervals to NaOH. Lastly, further trials will have to be prove this. conducted over smaller pH intervals to prove where the minimum rate constant Conclusion exists for each xanthate. This project has shown that xanthate decomposition rate constants tend to decrease at higher pH levels which is in line with literature that suggested an increased rate of degradation in more acidic conditions. However, highly alkaline conditions may also be increasing the rate of xanthate decomposition. The implications of this research include increase in mineral yield such that mining companies (like New Gold New Afton Mine) can further develop their industrial processes to make better use of xanthates. As well, mining companies will be able to minimize and potentially decrease environmental and health hazards posed Acknowledgements I would like to thank Dr. Kingsley Donkor and Dr. Dipesh Prema for their support as well as Trent Hammer for his instrument expertise and guidance. Thank you to Dayton Shaw for helping keep the lab spaces safe and organized and thank you to TRU’s Chemistry Department for continued support. A big thank you to New Afton Gold Mine for support and providing samples, and to NSERC for providing funds to make this project possible. Finally, thank you to the TRU Research Office (UREAP) for funding my project. This has been an invaluable experience and I am grateful to all those involved for making this project a success. 5 Faculty of Science – Chemistry Ó William L. Primrose, 2019 References 1. Kemppinen J, Aaltonen A, Sihvonen T, Leppinen J, Sirén H. 2015. Xanthate degradation occurring in flotation process waters of a gold concentrator plant. Elsevier [Internet]. 25 September 2018; Minerals Engineering Volume 80: 1 – 7. Available from https://link.springer.com/article/10.1007%2Fs11270-010-0598-3 DOI http://dx.doi.org/10.1016/j.mineng.2015.05.014 2. Li N, Chen Y, Zhang C, Zhou W, Fu M, Chen W, Wang S. 2015. Highly Sensitive Determination of Butyl Xanthate in Surface and Drinking Water by Headspace Gas Chromatography with Electron Capture Detector. Chromatographia [Internet]. Volume 78: 1305 – 1310. Available from https://link.springer.com/content/pdf/10.1007%2Fs10337-015-2940-9.pdf DOI 10.1007/s10337-015-2940-9 3. Michaud D. [Internet]. 2015. Flotation Collectors. 911 Metallurgist: 911metallurgist.com; [updated 10 August 2015; cited 25 September 2018]. Available from https://www.911metallurgist.com/blog/flotation_collectors 4. Mustafa, S., Hamid, A., Naeem, A., Sultana, Q. (2004). Journal of the Chemical Society of Pakistan. 26(4): 363-366 5. Rostad C E, Schmitt C J, Schumacher J G, Leiker T J. 2010. An Exploratory Investigation of Polar Organic Compounds in Waters from a Lead–Zinc Mine and Mill Complex. Water, Air, & Soil Pollution [Internet]. Volume 217 (1 – 4): 431 – 443. Available from https://link.springer.com/article/10.1007%2Fs11270-010-0598-3 DOI 10.1007/s11270-010-0598-3 6. Shen Y, Nagaraj D R, Farinato R, Somasundaran P. 2016. Study of xanthate decomposition in aqueous solutions. Elsevier [Internet]. 25 September 2018; Minerals Engineering Volume 93: 10 – 15. Available from https://www.sciencedirect.com/science/article/pii/S0892687516300863 DOI https://doi.org/10.1016/j.mineng.2016.04.004 7. World Health Organization | Institutional Repository for Information Sharing [Internet]. 12 April 2005. Geneva: World Health Organization. Available from http://apps.who.int/iris/handle/10665/42554 6 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Tables and Figures Table 1. Instrument and Method Parameters Sample Volume (mL): 0.075 Incubation Time (min): 15 Heat Agitator: On Incubation Temperature (°C): 30 Heat Syringe: On Syringe Temperature (°C): 46 Pre Injection Flush Time (s): 10 Sample Sample Vial Penetration Depth (mm): 15 Sample Vial Penetration Speed (mm/s): 50 Sample Aspirate Flow Rate (mL/min): 12 Sample Post Aspirate Delay (s): 1 Injection Signal Mode: Plunger Up Inlet Penetration Depth (mm): 45 Inlet Penetration Speed (mm/s): 50 Pre Inject Time Delay (s): 0.5 Injection Flow Rate (mL/min): 1 Post Inject Time Delay (s): 0.5 Flush Time (s): 60 Continuous Flush: On Advanced Agitator Speed (rpm): 250 Agitator On Time (s): 15 Agitator Off Time (s): 5 Table 2. Preparation of Calibration Curve Volume Stock Final Volume Concentration added (mL) (mL) (ppm) 0.5 100.0 0.05 1.0 100.0 0.10 5.0 100.0 0.50 10.0 100.0 1.00 15.0 100.0 1.50 20.0 100.0 2.00 7 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Table 3. Development of PIPX standards (a - f) Xanthate PIPX PIPX [Xanthate] Sample ppm 100.8 100.2 label Volume 0.012 pH pOH M NaOH added (L) Volume 0.012 M NaOH (mL) Total Volume (L) a b 10.95 10.24 3.05 3.76 0.000800 0.000150 0.8000 0.1500 0.01080 0.01030 c 9.77 4.23 0.000050 0.0500 0.01010 d 9.31 4.69 0.000017 0.0170 0.01002 e 9.01 4.99 0.0000085 0.0085 0.01009 f 8.49 5.51 0.0000025 0.0025 0.01003 Table 4. Development of PIPX standards (g - h) Xanthate [Xanthate] Sample ppm label Volume 0.012 pH pOH M NaOH added (L) Volume 0.012 M NaOH (mL) Total Volume (L) PIPX 110.6 g 7.72 6.28 0.000022 0.0220 0.50002 PIPX 1075.2 h 7.72 6.28 0.000022 0.0220 0.50002 Table 5. Development of PIPX standards (i - j) Xanthate [Xanthate] Sample ppm label Volume 0.012 pH pOH M NaOH added (L) Volume 0.012 M NaOH (mL) Total Volume (L) PAX 103.2 i 9.48 4.52 0.000025 0.0250 0.01003 PAX 103.2 j 9.08 4.92 0.000010 0.0100 0.01001 Table 6. Development of PIPX standards (k - p) for triplicate trials Xanthate PAX PAX [Xanthate] Sample ppm 102.6 102.6 label Volume 0.012 pH pOH M NaOH added (L) Volume 0.012 M NaOH (mL) Total Volume (L) k 9.26 4.74 0.000015 0.0150 0.01002 l 9.26 4.74 0.000015 0.0150 0.01002 m 9.26 4.74 0.000015 0.0150 0.01002 n 9.34 4.66 0.000018 0.0180 0.01002 o p 9.34 9.34 4.66 4.66 0.000018 0.000018 0.0180 0.0180 0.01002 0.01002 8 Faculty of Science – Chemistry Table 7. Raw data for trials a – f Series a Injection Time (h) Ó William L. Primrose, 2019 Series b Concentration (ppm) Peak Area Series c Injection Time (h) Concentration (ppm) Peak Area Injection Time (h) Concentration (ppm) Peak Area 1 2 3 4 5 6 7 2.65 3.70 4.75 5.80 6.85 7.90 8.95 0.0330 0.0301 0.0336 0.0355 0.0323 0.0327 0.0341 510077 421051 526675 583833 486876 499509 540455 1 2 3 4 5 6 7 2.03 3.08 4.13 5.18 6.23 7.28 8.33 0.0348 0.0352 0.0336 0.0365 0.0363 0.0362 0.0358 563759 576239 526561 613296 606902 605391 594096 1 2 3 4 5 6 7 1.00 2.05 3.10 4.15 5.20 6.25 7.30 0.0358 0.0327 0.0361 0.0380 0.0339 0.0394 0.0364 593947 499156 601537 659226 534699 700135 612135 8 Series d 10.0 0.0333 519315 8 Series e 9.38 0.0347 560915 8 Series f 8.35 0.0392 696003 Concentration (ppm) Peak Area Concentration (ppm) Peak Area Concentration (ppm) Peak Area 0.0537 0.0213 0.0224 0.0266 0.0294 0.0296 0.0316 0.0292 1E+06 159278 190057 318131 400850 405423 465506 395405 0.0265 0.0265 0.0246 0.0227 0.0267 0.0285 0.0294 0.0284 313608 313124 255370 199555 320194 375162 400962 370079 0.0340 0.0261 0.0228 0.0298 0.0255 0.0300 0.0408 0.0746 540093 301743 203706 413101 285044 418546 741993 2E+06 Injection Time (h) 1 2 3 4 5 6 7 8 1.53 2.58 3.63 4.68 5.72 6.77 7.82 8.87 Injection Time (h) 1 2 3 4 5 6 7 8 1.53 2.58 3.63 4.68 5.72 6.77 7.82 8.85 Injection Time (h) 1 2 3 4 5 6 7 8 1.53 2.58 3.63 4.68 5.72 6.77 7.82 8.85 Table 8. Summary of Results Series pH level [Xanthate] Xanthate Rate Constant (ppm) Used k (h ) -1 -1 Average k (h ) a b c d e f g h i 10.95 10.24 9.77 9.31 9.00 8.48 7.73 7.73 9.48 100.8 100.8 100.8 100.8 100.8 100.2 110.6 1075.2 103.2 PIPX PIPX PIPX PIPX PIPX PIPX PIPX PIPX PAX 5.79E-05 3.91E-06 4.36E-05 - j 9.08 103.2 PAX 5.43E-05 - k l m 9.26 9.26 9.26 102.6 102.6 102.6 PAX PAX PAX 1.27E-05 8.77E-06 1.56E-05 1.23E-05 n o p 9.34 9.34 9.34 102.6 102.6 102.6 PAX PAX PAX 1.27E-05 1.27E-05 1.27E-05 1.27E-05 9 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Table 9. Summary of Results Sorted by Ascending pH Level Series pH level [Xanthate] (ppm) Xanthate Used -1 -1 g 7.73 110.6 PIPX Rate Constant k (h ) 5.79E-05 Average k (h ) - h 7.73 1075.2 PIPX 3.91E-06 - f 8.48 100.2 PIPX - - e 9.00 100.8 PIPX - - j 9.08 103.2 PAX 5.43E-05 - k 9.26 102.6 PAX 1.27E-05 l 9.26 102.6 PAX 8.77E-06 m 9.26 102.6 PAX 1.56E-05 d 9.31 100.8 PIPX - n 9.34 102.6 PAX 7.80E-06 o 9.34 102.6 PAX 7.80E-06 p 9.34 102.6 PAX 8.77E-06 1.23E-05 8.12E-06 i 9.48 103.2 PAX 4.36E-05 - c 9.77 100.8 PIPX - - b 10.24 100.8 PIPX - - a 10.95 100.8 PIPX - - Figure 1. Calibration curve for carbon disulphide observed via gas chromatography 6.00E+07 5.00E+07 y = 3E+07x - 986108 R² = 0.9681 Peak Area 4.00E+07 3.00E+07 2.00E+07 1.00E+07 0.00E+00 0.00 -1.00E+07 0.50 1.00 1.50 2.00 2.50 [Carbon disulfide] in solution (ppm) 10 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Figure 2. Concentration of CS2 evolved (ppm) over time (h) for series a – f and their reproducibility values Series a Series b 0.036 0.0370 R² = 0.0909 0.035 R² = 0.0866 0.0365 0.0360 0.034 0.0355 0.033 0.0350 0.032 0.0345 0.031 0.0340 0.03 0.0335 0.029 0 2 4 6 8 10 12 0.0330 0.000 2.000 Series c 4.000 6.000 8.000 10.000 Series d 0.0400 0.0600 0.0390 0.0500 R² = 0.346 0.0380 R² = 0.0782 0.0400 0.0370 0.0360 0.0300 0.0350 0.0200 0.0340 0.0100 0.0330 0.0320 0.00 2.00 4.00 6.00 8.00 10.00 0.0000 0.00 2.00 Series e 4.00 6.00 8.00 10.00 8.00 10.00 Series f 0.03000 0.0800 0.02900 0.0700 0.02800 0.0600 0.02700 0.0500 0.02600 R² = 0.4226 0.0400 R² = 0.3323 0.02500 0.0300 0.02400 0.0200 0.02300 0.0100 0.02200 0.00 2.00 4.00 6.00 8.00 10.00 0.0000 0.00 2.00 4.00 6.00 11 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Figure 3. Concentration of CS2 evolved (ppm) over time (h) for series g – p and their reproducibility values Series g Series h 0.095 0.070 R² = 0.9811 0.065 R² = 0.9392 [CS2] evolved (ppm) [CS2] evolved (ppm) 0.085 0.075 0.065 0.055 0.045 0.035 0.060 0.055 0.050 0.045 0.040 0.035 0.025 0.030 0.00 2.00 4.00 6.00 8.00 10.00 0.00 2.00 4.00 Time (h) 6.00 8.00 10.00 8.00 10.00 Time (h) Series i Series j 0.08000 0.09500 R² = 0.8942 0.07500 R² = 0.8641 0.08500 0.07000 0.06500 0.07500 0.06000 0.06500 0.05500 0.05000 0.05500 0.04500 0.04500 0.04000 0.03500 0.03500 0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 0.00 2.00 4.00 Series k 6.00 Series l 0.04300 0.03700 R² = 0.9425 R² = 0.943 0.04100 0.03500 0.03900 0.03700 0.03300 0.03500 0.03100 0.03300 0.03100 0.02900 0.02900 0.02700 0.02700 0.02500 0.02500 0.00 2.00 4.00 6.00 8.00 10.00 12.00 0.00 2.00 4.00 Series m 6.00 8.00 10.00 12.00 14.00 Series n 0.05500 0.04200 R² = 0.7394 0.04100 R² = 0.8984 0.05000 0.04000 0.03900 0.04500 0.03800 0.04000 0.03700 0.03600 0.03500 0.03500 0.03000 0.03400 0.00 2.00 4.00 6.00 8.00 10.00 12.00 14.00 0.00 1.00 2.00 Series o 3.00 4.00 5.00 6.00 7.00 Series p 0.04200 0.04200 R² = 0.7383 0.04100 0.04100 0.04000 0.04000 0.03900 0.03900 R² = 0.8554 0.03800 0.03800 0.03700 0.03700 0.03600 0.03600 0.03500 0.03500 0.03400 0.03400 0.03300 0.03300 0.03200 0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 0.00 1.00 2.00 3.00 4.00 5.00 6.00 7.00 8.00 12 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Figure 4. Chromatogram for Series g sample at 5 hours (pH 7.73, 110.6 ppm PIPX) Figure 5. Chromatogram for Series n sample at 6 hours (pH 9.34, 102.6 ppm PAX) Figure 6. Chromatogram for CS2 standard 6 (1.50 ppm) Figure 7. Mass spectrum for Series g sample at 5 hours (pH 7.73, 110.6 ppm PIPX) 13 Faculty of Science – Chemistry Ó William L. Primrose, 2019 Figure 8. Mass spectrum for Series n sample at 6 hours (pH 9.34, 102.6 ppm PAX) Figure 9. Mass spectrum for CS2 standard 6 (1.50 ppm) 14