Nonmetal selective liquid chromatographic detection utilizing ultrasonic nebulization and membrane desolvation with a helium microwave -induced plasma
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Photographs included in the original manuscript have been reproduced xerographically in this copy. Higher quality 6” x 9” black and white photographic prints are available for any photographs or illustrations appearing in this copy for an additional charge. Contact UMI directly to order. ProQuest Information and Learning 300 North Zeeb Road. Ann Arbor, Ml 48106-1346 USA 800-521-0600 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. ABSTRACT Name: Debashis Das Department: Chemistry and Biochemistry Title: Nonmetal Selective Liquid Chromatographic Detection Utilizing Ultrasonic Nebulization and Membrane Desolvation with a Helium Microwave-Induced Plasma Major: Chemistry Degree: Doctor of Philosophy Approved by: Date: cu 7 A^/oi Dissertation Director NORTHERN ILLINOIS UNIVERSITY Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. ABSTRACT Atomic emission spectroscopy (AES) detection for chromatographic separations offers excellent selectivity and sensitivity and provides elemental information. The helium-microwave induced plasma atomic emission spectroscopy (He-MIP AES), suitable for detection o f nonmetals (Cl, Br, I, S, P), has been successfully employed in conjunction with gas chromatography. However, with liquid chromatography (HPLC), the performance o f MIPs is severely affected due to solvent loading. Membrane desolvators provide high analyte transport and desolvation efficiencies with most solvents. This dissertation focuses on application o f the ultrasonic nebulizer (USN)-membrane desoIvator-He MIP system as a detector for reverse-phase HPLC. Transport o f the volatile organic analytes was maximized by temperature optimization of the membrane desolvator. Temperature in the 50°C range provided efficient desolvation while minimizing analyte loss due to transport through the membrane. Modifying the solvent with dilute H2S04served to maximize analyte transport by reducing the volatility o f the solvent The inability o f USN with a fixed frequency (1.4 MHz) automatic transducer to nebulize certain HPLC solvents (aqueous solutions o f 10 -70% methanohwater and acetonitrile:water) was remedied by Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. frequency optimization using a manual transducer controller. Separation and detection of a mixture o f 2,6 dichlorobenzamide (DCB) and 4 chlorobenzamide (CB) using a 60% aqueous solution o f methanol was achieved by the HPLC-MIP AES detector. The detection limits were 36 and 47 ng/s for DCB and CB, respectively. The selectivity of the HPLC-MIP AES system was demonstrated with the detection o f vitamin B,2 in a mixture o f vitamin B„ B6, and Bl2. Superior sensitivity of the plasma AES detection over UV detection systems was exhibited via separation and detection o f a mixture o f P-glycerophosphate and triphenylphosphene. UV inactive Pglycerophosphate could be detected using the P emission line at 253.7 nm by MIP AES. Detection limits were 3.3 ng/s. Usually difficult by plasma spectrometry, detection o f high molecular weight compounds could be achieved. Greater than 10 kb, DNA samples from salmon testes were successfully detected. MIP AES with membrane desolvation is a viable detection technique for reverse-phase HPLC. However, studies to further improve the detection limits are necessary. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. NORTHERN ILLINOIS UNIVERSITY NONMETAL SELECTIVE LIQUID CHROMATOGRAPHIC DETECTION UTILIZING ULTRASONIC NEBULIZATION AND MEMBRANE DESOLVATION WITH A HELIUM MICROWAVE-INDUCED PLASMA A DISSERTATION SUBMITTED TO THE GRADUATE SCHOOL IN PARTIAL FULFILLMENT OF THE REQUIREMENTS FOR THE DEGREE DOCTOR OF PHILOSOPHY DEPARTMENT OF CHEMISTRY AND BIOCHEMISTRY BY DEBASHIS DAS DEKALB, ILLINOIS AUGUST 2001 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. UMI Number 3023682 UMI* UMI Microform 3023682 Copyright 2001 by Bell & Howell Information and Learning Company. All rights reserved. This microform edition is protected against unauthorized copying under Title 17, United States Code. Beil & Howell Information and Learning Company 300 North Zeeb Road P.O. Box 1346 Ann Arbor, Ml 48106-1346 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. Certification: In accordance with departmental and Graduate School policies, this dissertation is accepted in partial fulfillment o f degree requirements. rtation Director H o tg ANY U9E Of MATWM CONTAIN® ua m UUST K DULY ACKNOWliDGtD. rw AUTHOR'S P&M1SSJON K^TAtNEC W ANY PORTION JS TO II °* INCIUO® IN A PUBLICATION Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. ACKNOWLEDGMENTS I would like to thank my research advisor, Dr. Jon W. Carnahan, for his valuable guidance and support through the years, both as a research advisor and as a personal friend. I am deeply indebted to him for the knowledge I have acquired under his tutelage. My gratitude to all the faculty and staff members in the Department of Chemistry and Biochemistry, Northern Illinois University, for their immense help and support. A special thanks to my dissertation committee members and some of the technical staff members: Dr. David Ballantine, Dr. Lee Sunderlin, Dr. Narayan Hosmane, Dr. David Changnon, Dan Edwards, Larry Gregersen, and Charlie Caldwell, without whose assistance the research could not have been carried out. Many a thanks to my friends, Pamela Keating and Gary White, for their relentless support through thick and thin, for which I will always cherish their friendship. Finally, my deepest gratitude to my mother, Ms. Ranjita Das; father, Dr. Hrusikesh Das Berma; brother, Debjit Das; and all my relatives for believing in me and for their endless love and affection. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. DEDICATION To Maa, Daddy and Pintu, with gratitude Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. TABLE OF CONTENTS LIST OF TABLES................................................................................................. Page vii LIST OF FIGURES............................................................................................... ix Chapter 1. BACKGROUND....................................................................................... 1 1.1 Introduction.................................................................................... I 1.2 Advantages o f AES Detection for HPLC Systems ......................... 4 1.3 ICP, DCP, and He-MIP as Excitation Sources ............................... S 1.3.1 1.4 1.5 1.6 He - MIP Nonmetal Excitation Phenomenon .................... 7 Liquid Sample Introduction D evices............................................... 11 1.4.1 Pneumatic Nebulization.................................................... 12 1.4.2 Ultrasonic Nebulizer ........................................................ 13 Desolvation Devices ....................................................................... 15 1.5.1 Cryogenic Desolvation...................................................... 18 1.5.2 Hydraulic High-Pressure Nebulizer Desolvation............... 18 1.5.3 Membrane Desolvation System s........................................ 20 Research Objective ......................................................................... 23 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. vi Chapter Page 2. HELIUM MICROWAVE INDUCED PLASMA-USN-MEMBRANE DESOLVATOR ATOMIC EMISSION SYSTEM CHARACTERIZATION........................................................................... 25 2.1 Introduction.................................................................................... 25 2.2 Fate o f the Analyte as It Passes Through the System....................... 27 2.3 System Specifications .................................................................... 29 2.3.1 He-MIP Plasma System ...................................................... 29 2.3.2 Sample Introduction System ............................................. 31 2.3.3 Aerosol Desolvation S ystem ............................................. 32 2.3.4 O ptics................................................................................. 32 2.3.5 Data A nalysis..................................................................... 33 2.3.6 Reagents............................................................................. 33 2.4 Experimental .................................................................................. 34 2.5 System Optim ization...................................................................... 37 2.5.1 Inorganic Analytes in Water ............................................. 37 2.5.2 Inorganic Analyte in Methanol ......................................... 43 2.5.3 Characterization o f the System with Organic A nalytes 44 2.6 Examination of Background Emission with Membrane Desolvation ................................................................................... 53 2.7 Examination o f a 500 W Plasma for D etection............................... 62 2.8 Summary ........................................................................................ 68 3. INTERFACING HPLC WITH THE MIP AES USING USN AND MEMBRANE DESOLVATION................................................................ 69 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. vii Chapter page 3.1 Introduction.................................................................................... 69 3.2 Experimental .................................................................................. 71 3.3 Separation Using HPLC-MIP AES ................................................. 73 3.3.1 Effects of Anlyte on Background....................................... 76 3.3.2 Investigation of Analyte Loss in the S ystem ...................... 78 3.4 Nebulization o f LC Solvents with USN........................................... 87 3.5 Assessment ofFixed-Frequency Transducer B ehavior.................... 94 3.6 HPLC-MIP AES Using Solvent M odifiers...................................... 100 3.7 Summary ......................................................................................... 104 4. HPLC-MIP AES APPLICATIONS............................................................ 106 4.1 Introduction..................................................................................... 106 4.2 Examination o f Br, I, S, and P Em ission.......................................... 107 4.3 Sensitivity o f MIP-AES Detectors.................................................... 114 4.4 HPLC-MIP AES Applications.......................................................... 119 4.4.1 Detection of DNA ............................................................. 119 4.4.2 Detection of Vitamin Bi2 ................................................... 124 4.4.3 Detection of Nucleotides................................................... 132 Summary ......................................................................................... 136 5. CONCLUSIONS AND FUTURE DIRECTIONS...................................... 137 REFERENCES ..................................................................................................... 140 4.5 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. LIST OF TABLES Table page 1. Unoptimized Conditions Used for Preliminary Experiments ............... 35 2. Optimum Operating Conditions for Inorganic and Organic Analytes..................... 52 3. USN Nebulization Efficiency o f Binary Solvent Mixtures (v/v) With Automatic and Manual Transducer Controllers.......................... 90 4. Nebulization Frequency o f Water:methanol and Water:acetonitrile Mixtures Using USN with Manual Transducer.................................... 92 5. Nonmetal Detection Limits Using MIP AES......................................... 113 4 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. LIST OF FIGURES Figure page 1. Energy diagram for nine nonmetals. The horizontal lines represent ionization energies o f Ar and He. The dots indicate the energies of the ion states of the respective nonmetals. The energies are calculated as the energy o f ionization plus the energy o f ion excitation................ 10 2. Comparison o f primary pneumatic (a) and primary ultrasonic (b) volume distributions for water. ..................................................... 16 3. Ultrasonic nebulizer-membrane desolvator........................................... 17 4. (a) Cryogenic desolvation device used with the ultrasonic nebulizer and (b) desolvation set-up used witth the hydraulic high-pressure nebulizer............................................................................................... 19 5. Schematic for the MIP-USN-membrane desolvator atomic emission system ........................................................................................... 26 6. Fate o f the liquid droplet as it passes through the USN-MIP AES system................................................................................................... 28 7. CETAC MDX-100 tubular membrane desolvator................................. 30 8. (a) Spectrum obtained from aqueous solution of 500 ppm Cl as MgCL without (b) and with membrane desolvator. ........................................ 36 9. Cl signal as a function o f plasma gas flow rate....................................... 38 10. Cl signal as a function o f USN gas flow. ............................................. 40 11. Cl signal as a function o f membrane desolvator countercurrent gas flow ra te s ............................................................................................. 41 12. Cl calibration plot under optimized conditions........................................ 42 13. Cl signal as a function o f membrane desolvator countercurrent gas flow ...................................................................................................... 45 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. X Figure page 14. Inorganic and organic Cl signal vs membrane desolvator temperature ......................................................................................... 47 15. Organic Cl signal vs membrane desolvator tem perature..................... 48 16. Cl signal vs membrane desolvator countercurrent gas flow .................... SO 17. Cl S/N vs membrane desolvator countercurrent gas flo w ........................ SI 18. Five hundred ppm Cl signal from 2,6 dichlorobenzamide in methanol without membrane desolvator................................................................... 54 19. Five hundred ppm Cl spectrum from 2,6 dichlorobenzamide in methanol.................................................................................................... 55 20. (a) Image of the original plasma (nothing is being nebulized), (b) image o f the plasma when methanol is being nebulized with membrane desolvator and (c) image of the plasma when methanol is being nebulized without the membrane desolvator. A 500 W generator was used for this study.............................................................. 56 21. Methanol background with and without membrane desolvator 58 22. Plasma background spectrum at different membrane desolvator temperaturess while methanol is being nebulized...................................... 60 23. Plasma gas vs Cl S/B.................................................................................. 63 24. USN gas flow vs Cl S/B............................................................................. 65 25. Membrane desolvator countercurrent gas flow vs Cl signal. 500 ppm Cl as DCB in methanol used. Plasma operated at 400 W. USN gas flow was set at 1.8 L/m in.......................................................................... 66 26. Plasma power vs Cl S/B............................................................................. 67 27. System schematic for the HPLC-MIP A E S .............................................. 72 28. Chromatogram o f DCB.............................................................................. 74 29. DCB calibration plot using HPLC-MIP AES............................................. 75 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. xi Figure 30. CB calibration plot using HPLC-MIP AES.......................................... page 77 31. (a) DCB chromatogram when monochromator is set for 479.S Cl emission line and (b) DCB chromatogram when the monochromator is set at 479.6 nra, off the Cl emission line................................................ 79 32. Cl calibration plot using DCB with direct solution nebulization 80 33. Cl calibration plot using DCB at reduced USN “U” tube temperature . 82 34. Cl calibration plot from 2,6 dichlorobenzamide dissolved in methanolic 1% H2S04, 1% CH3COOH, and 1% HN03.......................... 84 35. Cl S/B from 500 ppm of DCB in 0.01 and 0.1% H2S04 in methanol solution.................................................................................................. 86 36. (a) Chromatogram of DCB and CB using 100% methanol as mobile phase and (b) separation of DCB and CB using 70% methanol as mobile phase. Flow rate was 0.8 m L/m in............................................ 88 37. Plot o f percent methanol in the solvent versus Cl S/B from solutions o f500 ppm Cl as DCB solution............................................................. 93 38. Plot of percent methanol versus density with respect to water. All density values were taken from reference 133...................................... 95 39. Plot o f percent methanol versus corresponding surface tensions 97 40. Plot o f percent methanol versus corresponding viscosity relative to w ater.................................................................................................... 98 41. Plot o f percent IPA versus corresponding viscosity with respect to w ater....................................................................... 99 42. System schematic o f the HPLC-MIP AES showing post column addition o f dilute H2S04 ....................................................................... 101 43. Chromatogram showing Cl peaks from 30 |ig 2 ,6-dichlorobenzamide and 30 pg 4-chIorobenzamide ...................... 102 44. Calibration plots from 2 ,6-dichlorobenzamide and 4-chlorobenzamide................................................................................ 103 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. xii Figure 45. One ppt Br, MIP AES spectrum from aqueous KBr03 ....................... page 108 46. One ppt I, MIP AES spectrum from aqueous KI03 ............................. 109 47. One ppt S, MIP AES spectrum from aqueous (NH4)2S04 ................... 110 48. One ppt P, MIP AES spectrum (213-216 nm) from aqueous H3P 04 . . . I ll 49. One ppt P, MIP AES spectrum (252-257 nm) from aqueousH3P 04 . . . 112 50. LC-MIP AES chromatogram o f P-glycerophosphate (500 ppm P) and triphenyl phosphene (500 ppm P).......................................................... 115 51. LC-MIP AES calibration plots for GP and TPP.................................... 117 52. Chromatogram of GP (500 ppm P) and TPP (500 ppm P) using the UV-Vis detector. ................................................................................. 118 53. Structure of tetranucleotide................................................................... 120 54. Diagram of a double-stranded DNA..................................................... 121 55. LC-MIP AES chromatogram obtained from 500 ppm DNA, extracted from salmon testes................................................................................. 123 56. UV picture o f electrophoretic bands from the molecular weight strands (in slots 2,3, and 12) and the DNA sample from salmon testes (in slots 5 ,7 ,9 ,1 0 ) on the agarose gel................................................... 125 57. Molecular structure o f (a) vitamin B„ (b) vitamin B6 and (c) vitamin Bl2. ................................................................................... 127 58. Chromatograms obtained from vitamin Bl2 (10 ppm P) using (a) UV-Vis detector and (b) MIP AES.................................................. 128 59. Chromatogram from a mixture o f vitamin Bt (10 ppm), vitamin B6 (10 ppm), and vitamin B,2 (10 ppm P) using (a) UV-Vis detector and (b) MIP AES.......................................................................................... 130 60. UV-Vis spectrum o f vitamins (250-400 nm )B l,B 6, and B 1 2 ............ 131 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. xiii Figure 61. Molecular structures o f (a) cytidine S' monophosphate disodium salt, (b) uridine S' monophosphate in free acid form, and (c) guanosine S' monophosphate disodium s a lt............................................................. 62. Chromatogram o f a mixture o f CMP, UMP and GMP using the UV-Vis 4etector at 254 nm.................................................................... Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. page 134 135 CHAPTER 1 BACKGROUND 1.1 Introduction In recent years plasmas have been extensively used as ionization and excitation sources for atomic emission (AES), fluorescence (AFS), and mass spectrometric (MS) systems. Among the different types of plasmas, inductively coupled plasmas (ICP), microwave-induced plasmas (MIP), and direct-current plasmas (DCP) are most common. Some of the important properties which make these sources desirable are high temperatures (2000 -10000 K), few interferences, the capability for simultaneous multielement analysis, high sensitivities, low detection limits, and large linear calibration ranges.1'5 These traits make plasmas ideal sources for trace metal analyses for solid, liquid, and gaseous samples. While maintaining many o f the aforementioned properties, helium MIPs have the unique property of producing intense nonmetal line emissions.**7 Hence, the source warrants investigation for determinations o f organic analytes. MIP atomic emission spectroscopy (AES) as a detector for various chromatographic techniques has been investigated by many authors.8*10 Helium MIP-AES is ideally suited for interfacing with gas chromatography (GC)11'17because helium is used both as the MIP support gas and the GC mobile phase. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. However, due to the inherent poor solvent tolerance o f plasmas, direct organic solution nebulization often causes complications such as carbon deposition on the plasma torch, significant spectral interferences, reduction of analytical signals, or even plasma extinguishment.1*'27 To avoid these solvent-related problems, the analyte is often desolvated before being introduced to the plasma. O f the many available desolvation techniques, membrane desolvation has shown great promise.2*'34 Although He MIP-AES systems possess desirable characteristics for the detection o f nonvolatile analytes, high-performance liquid chromatography (HPLC) interfaces have seen limited success. This approach is hindered by two fundamental drawbacks. First, typical LC mobile-phase solvents (methanol, acetonitrile, THF, etc.) are not compatible with optimal plasma performance. Additionally, liquid mobile phases do not lend themselves to efficient analyte transport. The problem due to solvent introduction can be minimized with the use of various desolvation devices. These devices remove a significant portion o f the solvent from the analyte stream before introduction into the plasma. Mason et al.3Ssuccessfully used a moving-band sample introduction system to interface an LC with the MIP. Operation o f this interface occurs in five steps. In the first step the eluent from the HPLC is deposited on a moving polyimide band (3.2 mm wide and 0.0S mm thick moving at a speed o f 2.5 cm/s), hi the second step the solvent evaporates as the band passes under an infrared heater. Third, the effluent passes into a vacuum region where residual solvent vapors are removed. The dry Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 3 analyte is then is earned to the vaporization chamber in the fourth step. In this step, flash vaporization of the analyte is achieved by a nichrome heater. The vaporized analyte is directed to the plasma for detection. The fifth step involves cleaning o f the band for the next run as it passes under the clean-up heater, where the residual analyte is removed. While solvent removal is efficient, the system is difficult to operate and maintain. Excellent detection limits could be achieved with this interface ( between 31 and 97 ng for Cl). However, the analytical reproducibility (relative standard deviation [RSD] achieved -12%) is somewhat poor. Preliminary successful studies with a flat-sheet membrane desolvator interface have been carried out by Akinbo and Carnahan.34,36 About 99.9% o f the solvent could be removed using these devices. The Cl detection limits achieved with the LC-MIPflat-sheet membrane desolvator were between 2 and 7 Jig, about one order of magnitude higher than that obtained with the moving-band interface. On the other hand, the reproducibility obtained was much better (RSDs o f 2.5 - 6.7%). Analyte transport problems caused calibration plots to exhibit non-zero intercepts.36 In this dissertation, an extensive study o f the development o f detection systems based upon the combination of HPLC, ultrasonic nebulization (USN), membrane desolvation, and a He MIP will be discussed. Detection limits, linearity o f calibration plots, and precision will also be presented. Particular effort is directed toward enhancing analyte transport. Various applications to demonstrate the analytical performance o f this detector are illustrated. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 4 1.2 Advantages of AES Detection for HPLC Systems The commonly used detectors for HPLC systems are based upon UV spectrometry and refractive index measurements. These detectors utilize the bulk physical and chemical properties of the analyte molecule as a basis for detection. In general, detectors o f this type lack exceptional selectivity or sensitivity. Conversely, AES detectors are inherently selective because, when excited, all elements emit radiation at their characteristic wavelengths. Also, the emission features are very narrow ( line widths are typically in the range o f 0.01 nm or less) compared to UV absorption bands. Hence, if the chromatographic column does not separate two or more analytes o f interest, the detector may be able to distinguish and quantify them by monitoring emissions from unique atoms that constitute the molecules. Another AES advantage for HPLC detection is the ability to provide elemental content information. Under ideal conditions, part per trillion detection limits can be achieved by AES. Plasma AES systems are sensitive to almost all types o f compounds present in complicated matrices. With all these advantages, the suitability o f a helium microwave-induced plasma atomic emission system for reverse-phase HPLC detection is worth exploring. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 5 1JICP, DCP, and He-MIP as Excitation Sources Direct-current plasma, inductively coupled plasma, and microwave-induced plasma are the commonly used plasma sources for atomic emission spectroscopy. The typical DCP is produced by a DC discharge between a three-electrode array. The plasma is sustained by a flow o f argon over the electrodes. Ar is also used for sample nebulization. Typical combined gas flow rates are about 8 L/min.37 DCPs are operated at power levels between 500 - 700 W3*with a voltage of 10 to 50 V. The excitation temperatures can reach 6000 K in DCPs. Some o f the attractive properties o f DCP are its ability to handle organic solvents as well as aqueous solutions with high solid content and its low power consumption. DCPs are effective excitation sources for most metals. However, intense molecular background from the graphite electrodes is a problem and sample volatilization is often not complete because o f the short residence times o f the analyte in the plasma. The ICP is the most extensively used plasma source for atom excitation and ionization.39 The plasma is maintained by a radio frequency field (between 5 to 50 MHz) interacting with a 12 to 18 L/min argon flow. The typical powers at which ICPs are operated are 1 to 1.5 kW. The plasma temperature at the hottest region is between 9000 to 10,000 K. Because of their high thermal energies, ICPs are excellent Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. sources for almost all metals.40 The analyte residence times in the plasma are fairly long (2-3 ms). ICPs have very high electron densities; hence, ICP performance is not significantly affected by the addition of easily ionized elements. Detection limits of part per trillion levels are often achieved under ideal conditions. However, ICPs do not possess sufficient thermal energy to produce UV or visible nonmetal atomic emission. Compared to all other plasmas, helium MIPs exhibit a unique characteristic of producing intense atomic emission from nonmetals C, H, O, S, P, Cl, Br, I, and F41,43 in the 200 to 800 nm spectral range. MIP discharges most commonly are formed in a quartz or a ceramic tube placed in the center of a Beenakker TM0I0 resonant cavity. Power is supplied to the cavity via a coaxial cable from a 2.4S GHz microwave generator. Impedance matching o f the plasma system may be done with the help of tuning stubs and MIPs are most commonly operated at powers from 20 to 500 W. Typical He gas flow rates for sustainance o f the plasma are from 1 to 15 L/min. Like ICPs, a microwave plasma is initiated by providing “seed” electrons from a spark. In the microwave field the electrons gain sufficient momentum and ionize the support gas by collisions. More and more electrons and ions are formed in a cascade, and stable atmospheric pressure plasma temperatures range from 2000 to 5000 K. Compared to other types of plasmas, MIPs consume less gas.43 Since MIPs are usually smaller than ICPs and impedance matching is somewhat more difficult, MIPs are less tolerant to liquid sample introduction. The lower power plasmas (<120 W) are often extinguished Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. when significant amounts o f solvent are introduced. However, MIPs are very well suited for gas phase sampling and have been successfully used in conjunction with gas chromatographic systems.44 Because strong emission lines are observed for nonmetals with MIPs, they are suitable for determinations of organics which are mostly composed of nonmetals. However, their intolerance to solvents, especially organic solvents, must be addressed. 1.3.1 He - MIP Nonmetal Excitation Phenomenon Examples of intense nonmetal ion emission in He-MIPs have been reported in the literature. However, calculations o f nonmetal electronic-state emissions using thermodynamic and kinetic theory do not suggest strong nonmetal emission from MIPs.7 Published detection limits o f GC-MIP for Br at the 478.6 nm ion emission line have been reported to be 106 pg and that o f Hg at the 2S3.7 nm atom line is 60 pg." These masses translate to 8.0 x 10u Br atoms and 1.8 x 10n Hg atoms, respectively. Calculations from the Boltzmann relationship (equation 1.1 below) using a He MIP temperature o f5000 K and electron density of 5 x 1014cm*3 indicate that the ratio of excited Br ions to ground-state Br atoms should be 4.1 x 10*20. Similar calculations of the Hg atom excited-state to ground-state ratio yielded a value o f 1.7 x 10*4. Applying transition probabilities, the detection limit photon flux was calculated to be 3.0 s*1for Br and 2.5 x 1014s'1for H g45 Although the calculated number o f photons that should Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. be produced by Br is 14 orders o f magnitude less than that o f the Hg, the detection limits observed were very similar. This discrepancy between calculated and observed detection limits, and, thus, emission intensities suggest phenomena other than thermal excitation o f atoms or ions. A number o f theories have been proposed to explain this He MIP behavior. The most accepted theory, however, is that of the charge transfer mechanism proposed by Carnahan and colleagues.4*’47 As shown in equation 1.1, the theory is based upon simultaneous nonmetal ionization and excitation by the interaction with ionized helium, where N is a nonmetal. N(0eV) + He\2A.5*eV) -> N+'(xeV) + He(0eV) + A £(24.58-xe^ (1.1) This process is known as charge transfer. The energy defect (AE) represents the energy difference between the ionization energy of He and the energy required to promote the nonmetal from the ground-state atom to the excited-state ion. Small energy defects enhance the likelihood of charge transfer occurrence. Rapp and Francis4* stated that the ionization cross-section for one electron transfer, such as that above where only one electron o f the species to be ionized is affected, is maximized when the reaction is near resonant. The ionization cross-section (for the effective rate constant) may be estimated as shown by equation 1.2. 0 = 0 .0 0 2 2 1 - ^ 1 (1 2 ) Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. where o is ionization cross-sectional area, T is the square root o f the ionization energy o f the element to be ionized divided by the ionization energy of hydrogen, v is the velocity, a is the Bohr radius, AE is the energy defect, and h is the Planck’s constant As an example, equation 1.3 shows the excitation o f Cl ion in He-MIP via one-electron charge transfer. The difference between the ionization energy of He and Cl+* is very small (AE = 0.01 eV). The most intense Cl emission line is that o f an ion and is observed at 479.45 nm. ClQs1 3p 5) + fle * (U 1) - C r 'O s 1 3p s) * ffe (U 2) + 0.0leV (1.3) Similar behavior is seen for other nonmetals. Figure 1 shows the energies o f all electronic states for singly charged C, N, O, F, P, S, Cl, Br, and I. Values were calculated by adding the element ionization energy to the energy of the specific ion state. The energies are arranged vertically above the symbol for the element. The two horizontal lines represent the ionization energies o f Ar and He. Close energy matches are seen with He* for elements I, S, P, Cl, and Br. Strong ion emission lines in the UV and visible spectral regions are seen for these elements in the He-MIP. C also participates in the charge transfer process, but C* emits in the vacuum UV region. On the other hand N, 0 , and i do not have any excited ion states close to the ionization energy of He. In accord with the charge transfer theory, these elements do not show strong ion emission lines in the He - MIP. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 10 130 C Figure I. N O F P $ Cl Br I Energy diagram for nine nonmetals. The horizontal lines represent ionization energies o f Ar and He. The dots indicate the energies of the ion states o f the respective nonmetals. The energies are calculated as the energy of ionization plus the energy of ion excitation. (This figure is taken from Brandi and Carnahan.7) Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 11 1.4 Liquid Sample Introduction Devices The sample introduction method plays an important role in the performance of plasma-based atomic and mass spectrometric techniques.49,30 To utilize the full atomization, excitation, and ionization powers of plasmas, suitable sample introduction devices and methods must be used. Gaseous analytes are the ideal samples for plasmabased spectrometry because analyte transport is very efficient.51 In most cases, nearly 100% o f the gaseous sample can be introduced to the plasma. No desolvation or volatilization is necessary; hence, most o f the plasma energy may be used for excitation and ionization.32'34 For liquid sampling, pneumatic and ultrasonic nebulizers are commonly used. These devices typically disperse the liquid sample into droplets o f a fine aerosol, which are transported to the plasma by a carrier gas. With USN, more than 90% o f the sample is typically discarded. That value is approximately 99% with pneumatic nebulizers. Because o f the large amounts o f solvent associated with the analyte, much energy is used for desolvation. Plasma energy is also used for isolation o f the analyte from the residual solid analyte matrix. Matrix effects often diminish or interfere with the analytical signal. These inherent difficulties with liquid sampling have prompted a great deal o f research toward understanding the formation o f aerosols by various nebulization devices as well as analyte desolvation before introduction to the plasma. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 12 In the following sections, various pneumatic55,36and ultrasonic nebulizer57,51 properties will be discussed. Emphasis will be given to key aerosol characterization parameters. 1.4.1 Pneumatic Nebulization Pneumatic nebulizers are operated most commonly in two basic configurations, crossflow and concentric type arrangements. In the concentric arrangement the sample solution passes through a capillary surrounded by a high-velocity gas stream parallel to the capillary axis. In the crossflow type, the sample-carrying capillary is at right angles to the gas stream. In both systems a pressure differential is created at the sample capillary tip and the amount of liquid drawn through it is described by Poiseuille’s equation (equation 1.4). e= — * 8q l ci.4) where Q is the flow rate o f the liquid, R is the capillary radius, P is the pressure differential, TJ is the viscosity o f the liquid, and L is the overall length of the capillary. The relationship between the aerosol droplet diameter and the solution properties in conjunction with nebulizer parameters given by Nukiyama and Tanasawa59 is shown in equation 1.5. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 13 585 v(o/p)w + 597[ *1 l 0-45 ( 1000^ \ 1.5 (op)'* (1.5) Q ". where d0 - mean droplet diameter (pm), v = velocity o f gas (m/s), 0 = surface tension (dyne, cm), p = density o f liquid (g/mL), T] = viscosity (poises), and QKqand = volume flows o f the liquid and gas, respectively. 1.4.2 Ultrasonic Nebulizer With an ultrasonic nebulizer, the sample solution is typically introduced onto an inert surface attached to a piezoelectric transducer. The transducer is driven by an ultrasonic generator at frequencies o f200 kHz to 10 MHz. The ultrasonic generator produces longitudinal waves that propagate from the surface of the crystal, through the inert material (usually quartz or glass), toward the liquid-air interface. Aerosol formation occurs when the amplitude of the wave becomes large enough to significantly disrupt the surface o f the liquid film. The wavelength o f the surface wave is given by Kelvin’s formula60,61 (equation 1.6): (1.6) P/ 2 where X is wavelength, 0 is surface tension, p is liquid density, an d /is ultrasonic Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 14 frequency. The average droplet size (D) is given by equation 1.7. D = 0 .3 4 1 = 0.34 (17) P/2 As is evident from equation 1.7, the average particle size is dependent on the liquid properties and the frequency o f excitation. However, from the atomic spectrometry point o f view, the average droplet diameter is not very useful. It does not give any information about the mass distribution. The Sauter mean diameter represents a value based on volume to surface area ratio (equation 1.8), i E(d3 An) « = - L- — ~ s E(d2A«) (1.8) where d, is the Sauter mean diameter, d is the diameter of drops, and An is the number of drops o f diameter d. This representation is an excellent approximation of the mass median diameter. In plasma techniques, it is important to rapidly and efficiently convert analyte within droplets into atomic and ionic species. A droplet distribution with a smaller Sauter mean diameter means it has a larger surface area per unit mass, which translates to easier atomization and ionization. Recent studies show that droplets with diameters smaller than 8 iim contribute significantly to the analyte signal produced with Ar ICP.56,62 Analytes within larger Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 15 droplets do not undergo complete desolvation-vaporization-atomization-ionization. Larger droplets may actually pass through the plasma unaffected.63 To assess the efficiency o f a nebulizer system, parameters like droplet size and mean diameter, cumulative percent volume o f aerosol under a certain droplet size, span of a distribution, axial velocity, radial velocity, droplet number density, and volume flux are often examined. Figure 2Mshows the particle size distribution of a primary aerosol (aerosol just after nebulization) from a pneumatic nebulizer and a USN using 100% water. The volume percent of droplets less than 8 |im in diameter from USN is much higher (roughly 9 times) than that observed for the pneumatic nebulizer. The amount o f solvent converted to droplets by the USN was also about 8 times higher than that o f the pneumatic nebulizer.64 Hence, desolvation of the analyte is necessary when USN is used. Typically, the aerosol from the USN spray chamber is passed through a heated tube for droplet vaporization and subsequently through a cold condenser for solvent vapor condensation to minimize solvent load. Such an apparatus is shown in Figure 3. The approach is generally sufficient during aqueous sample introduction. However, with organic solvents, additional desolvation is requited. 1.5 Desolvation Devices Various devices have been used for analyte desolvation. Some common Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 16 25 20 h 15 5 0 1 10 100 1,000 Diameter (jim) Figure 2. Comparison o f primary pneumatic (a) and primary ultrasonic (b) volume distributions for water. Liquid uptake rate and argon nebulizer gas flow rates were 1.0 mL/min and 1.0 L/min respectively. Laser Fraunhofer diffraction was used to obtain these data. (This figure is taken from Tarretal.64) Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. fnrfCPgas ana vapor out i Argon carrier Sas Plasma fte te d u-rube Spray chamber If I , / / ?£ * 0 elc ctric J transducer Figure 3. Tj, lVasf= n 'a i“ ,fiD“CS 'C San,.,,. s°httion ? ,,hao'* * ./v ator. ^ ® n ie /s ReProduced Wmpsm'i^ 0 „ 0fth it ;; ;j 18 examples o f desolvation techniques are cooled spray chambers,6346 cryogenic desolvation,22,23 heated - cooled condenser devices,67*71 and membrane desolvation.34,72 Some o f the other means o f desolvation used are jet separation,73 acid desiccation,74 and moving-band devices.31,35 1.5.1 Cryogenic Desolvation Houk and coworkers73*77and Montaser et al.7* have done significant studies with cryogenic desolvation devices for ICP MS. A schematic o f this device is shown in Figure 4a. This device transports the aerosol several cycles alternately through heated tube (140 tol50°C) and condenser (0 to -10°C) regions. This repeated cooling (-80°C) and heating (140°C) eliminates most o f the associated solvent. The dry analyte particulates are then transferred to the plasma for detection. This system is equally efficient for both aqueous and organic solvents. 1.5.2 Hydraulic High-Pressure Nebulizer Desolvation This nebulizer-desolvation (Figure 4b) device79,80 uses a high-pressure pump to force the liquid through a 5 to 30 |im orifice. Aerosol is formed as this high-velocity jet exits through the small opening and subsequently collides with an impact bead to form an aerosol cloud. -The aerosol passes through a heated tube and two-stage Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 19 / Second cryocondenser ' (glass) ^ Heating coils (140°C) To plasma Aerosol in Absolute ethanol (-80°C) Cooling coiis (a) Heated tube Spray chamber/ Coolant To plasma Liquid condeaser (25-30 °C) Peltier condenser (15 to -40°C) To waste * ■ u Heat sink Coolant in Temperature controller and power supply 0» Figure 4. (a) Cryogenic desolvation device used with the ultrasonic nebulizer and (b) desolvation set-up used with the hydraulic high-pressure nebulizer. (The figures were taken from Montaser.40) Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 20 condensation chamber. The efficiencies o f condensation for aqueous and methanol solutions were found to be 97% and 94%, respectively. Analyte transport efficiencies were approximately 24%. Compared to pneumatic nebulization, order o f magnitude improvements in detection limits were observed. However, with organic solvents, small amounts of 0 2 must be added to reduce carbon deposition in the torch. 1.5.3 Membrane Desolvation Systems Desolvation using membrane desolvators has shown great promise for both plasma atomic emission and plasma mass spectrometric systems. Membrane desolvators selectively allow the transport o f either analyte or associated solvent across a semipermeable membrane. Typically, the wet aerosol originating from a nebulizer is transported by the carrier gas into the central membrane channel. The desolvator unit is maintained at a temperature higher than the boiling point of the solvent (usually 150°C for water). The solvent goes into vapor form and diffuses through the membrane to the outer channel. A sweep gas or a vacuum pump is used to flush the solvent from the outer channel. The analyte, which usually has a boiling point much higher than that o f the solvent, remains in a solid particulate form and does not undergo membrane transport. These dry analyte particulates may then be directed to the plasma. With hydride,*1"*? carbon dioxide,** sulfur dioxide,*9 and ammonia*9,90 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. generation schemes, the volatile analyte undergoes membrane transport This mode has also been used for plasma introduction o f volatile organic analytes such as phenols, aldehydes, ketones, and carboxylic acids in aqueous matrices.91*96 However, for aerosols originating from nebulizers, the solvent is usually converted to vapor form and the vapor undergoes membrane transport This mode is more suitable for plasma excitation sources and this discussion will be focused on such. In terms o f types o f the membrane used, there are four major classes: porous, nonporous, mixed nonporous-porous, and ion exchange. The mechanisms o f solvent or analyte transport across these membranes are distinct from each other. For a nonporous membrane, transmembrane transport occurs by permeation. Permeation involves analyte or matrix solubilization followed by diffusion across the membrane.97 With porous-type membranes, however, the transport is strictly diffusion. The desolvation efficiency and selectivity is governed by pore size, membrane thickness, and its chemical characteristics (hydrophobicity or hydrophillicity).9* Some common examples o f membrane materials are silicone,72,96,9* fluoroplastics (polytetrafluoroethylene [PTFE], polyvinylidenedifluoride [PVDF]),99*105 cellulose,106* 101polypropylene,,09*UI and ion-exchange membranes"2 like Nafion."3*"5 Gustavsson and coworkers9M12 developed a planar nonporous silicone membrane separator116,117for use with ICP-AES for both organic and aqueous solutions. The aerosol was heated to form solid analyte particulates and solvent vapor. This mixture was passed over the semipermeable membrane. The solvent Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 22 vapor permeated through the membrane because o f the negative pressure on the other side maintained by a vacuum pump. Eighty to 100% desolvation was observed for solvents like freon, chloroform, and water. Carrier gas flow rates were 0.5 >1.0 L/min and solvent uptake rates were 0.5 tol.7 mL/min. Membrane desolvation in conjunction with thermospray nebulizers has been used to introduce samples a into plasma mass spectrometer by Montaser.40 A tubular microporous teflon membrane desolvator was used with an ultrasonic nebulizer by Butto and Zhu.111 Diffusion o f solvent vapor across the membrane was facilitated by employing a gas flow in a direction opposite to the flow of analyte. Aqueous, organic solvents and petroleum products with boiling points below 100°C have been successfully desolvated using this system. Bemer and co workers (in Montaser40) have used this system for oxide-ion reduction interference for ICP-MS measurements. Tao and Miyazaki119have explored the application o f a hollow non-porous polyimide membrane separator. This device was used with a pneumatic nebulizer for ICP-MS applications. Significant decreases in MCT/M+ ratios and ArCT signals indicated water loading reduction. Naflon membranes also have been utilized by many researchers because o f their unique selectivity properties. The hydrophilic sulphonic groups on the surface o f the membrane are extremely efficient in eliminating associated aqueous solvent from the analyte. Yang et al.113have successfully used this desolvator for thermospray ICP-AES applications and 99.9% desolvation efficiency was observed for 1% (v/v) HN03. In addition to superior Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 23 desolvation efficiencies, these desolvators were found to be pulse dampeners, eliminating plasma flicker often seen with thermospray nebulizers. Cairns et al."4 used Nafion membranes with methanol and acetonitrile for use with HPLCICP-AES. Desolvation efficiencies o f 89% were observed, which minimized baseline drift during gradient elution. Akinbo and Carnahan34 investigated the use of a hydrophobic nonporous polypropylene membrane for desolvation with ultrasonic nebulization for MIP-AES applications. The desolvation efficiencies for both aqueous and organic solvents were observed to be 99.99%. Compared to other desolvation devices, the membrane separation devices are advantageous for their superior desolvation efficiencies, ease of operation, inertness, convenient optimization procedures, and ruggedness. However, design and choice of membrane is extremely important for desirable desolvation efficiency for each application of concern. 1.6 Research Objective In this dissertation the analytical performance characterization and optimization o f a microwave-induced plasma atomic emission system with ultrasonic nebulizer sample introduction and membrane desolvation will be discussed. The application of this system as a detector for reverse-phase HPLC is also addressed. For the sake o f clarity the thesis has been divided into four parts. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 24 The second chapter discusses the characterization and optimization o f the MIP, ultrasonic nebulizer, and membrane desolvator conditions for nonmetal (Cl, Br, I, S, and P) atomic emission maximization in inorganic and organic analytes in aqueous and organic solvents. Parameters such as plasma, carrier and countercurrent gas flows, as well as plasma power are emphasized. The third chapter focuses upon organic analyte transport studies through the MIP-ultrasonic nebulizer-membrane desolvator system. Membrane desolvator conditions for low-boiling-point organic analytes and ultrasonic nebulization problems for different HPLC solvent compositions are discussed. The fourth chapter details applications o f reverse-phase HPLC-MIP AES. Figures of merit o f this detector with respect to common LC detectors (UV and refractive index) are presented. Applications of this system for detection of biologically active and pharmaceutical products are demonstrated. The last section suggests steps that should be taken to further enhance the performance of this system. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. CHAPTER 2 HELIUM MICROWAVE-INDUCED PLASMA-USN-MEMBRANE DESOLVATOR ATOMIC EMISSION SYSTEM CHARACTERIZATION 2.1 Introduction The primary objective o f this project is to utilize a membrane desolvator in conjunction with a USN-He-MIP system for element-selective nonmetal detection o f organic analytes present in aqueous and organic solutions. Once the system is optimized it is intended to be used as a detector for reverse-phase HPLC. As discussed in section l.l, organic solvents severely diminish the analytical performance o f the plasma. Hence, desolvation of the analyte is imperative before introduction to the plasma. Membrane desolvators have been effectively used with aqueous solutions. In this chapter the efficiency o f the membrane desolvation for organic analytes will be investigated. Also, the optimized operating conditions o f the plasma, USN, and the desolvator will be presented. Figure 5 shows a general diagram o f the MIP-USN-membrane desolvator system. The sample solution was introduced to the USN with a peristaltic pump. A helium carrier gas is used to drive the resultant aerosol through the heated tube-cold Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 26 Analyte Flow Gas Flow ...... \ He.: Coaatcr Carreat Gai Mcatbraae Desolvator Moaockroaiator Peristaltic Parap Ncbalbter He ;► Microwave Gcaerator Carrier Gas Figure 5. Schematic for the MIP-USN-membrane desolvator atomic emission system. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 27 condenser combination of the USN. The solvent evaporation/condensation step serves to partially desolvate the analyte. Passing the analyte stream through the membrane desolvator further desolvated the analyte. The dry analyte particulates were then directed to the plasma for detection. Emission from the plasma was focused onto a monochromator for wavelength selection. The detection was done using a photomultiplier tube (PMT). Data was acquired and manipulated by a computer. 2.2 Fate of the Analyte as It Passes Through the System Figure 6 depicts the evolving matrix of the analyte as it passes through a conventional USN system from the point o f aerosol formation. The primary aerosol from the USN is directed through a heated solvent vaporizaton tube followed by a cooled solvent condenser tube. The partially desolvated analyte exiting the condenser is introduced to the plasma. Thermal heat transfer from the plasma atomizes the analyte and, subsequently, additional energy transfer in the MIP produces excited atoms and excited ions. However, even after this partial desolvation of the analyte stream, a sufficient amount o f solvent still remains to alter the plasma properties. This is evidenced by intense OH emission bands in the case o f aqueous solvents. A myriad o f molecular emission bands (CH, CO, CN, etc.) appear when organic solvents are utilized. Hence, further desolvation o f the analyte stream is desirable. A viable approach is the use o f membrane desolvation. A schematic diagram o f the Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 28 Thermal evaporation followed by condensation in USN Thermal heat transfer in plasma M * Particulate plus solvent vapor M Free atoms plus solvent vapor \ Additional energy transfer in plasma M* X M* X** Excited atoms and ions and solvent vapor chemistry Figure 6. Fate of the liquid droplet as it passes through the USN-MIP AES system. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 29 CETAC MDX-100 membrane desolvator is shown in Figure 7. In the normal configuration, the desolvator is placed between the outlet of the USN condenser and the plasma. For aqueous sample mists, the membrane desolvator module is maintained at a temperature o f 150°C. The wet analyte particulates enter the hot central channel, encased by a microporous PTFE membrane. Ideally, residual solvent is converted to the vapor form and diffuses through the membrane to the outer channel. The driving force for this process is the osmotic pressure of the solvent vapor. A helium countercurrent gas is used to flush the solvent from the outer channel. The heavier nonvolatile analyte particulates do not undergo membrane transport and exit the desolvator with a minimum amount of associated solvent. The dry analyte is then introduced to the plasma for detection. 2 3 System Specifications The experimental system was similar to that used by Akinbo and Carnahan36 with a number o f modifications. The reader should refer to the block diagram shown in Figure S. A description o f important system components follows. 2.5.7 He-MIP Plasma System A 120 W maximum power output, 2.45 GHz microwave generator (model Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 30 Partially desolvated analyte en terin g m em b ran e deso lv ato r , ( OOOOOOOOQQQOO . • . .. 1 * • ». • Sample inlet (from USN) D esolvated analyte e x itin g m em brane d eso lv ato r Sample outlet (To H e-M IP ) |UCXXXX30CX300001f H e a te r Solvent diffusion Figure 7. C ountercurrent He gas + solvent vapor I Countercurrent gas(PureHe) CETAC MDX-100 tubular membrane desolvator. Adapted from literature - Cetac Technologies. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 31 MP6-4m-229, Kiva Instruments, Rockville, MD) was used. For some o f the experiments a 500 W generator (model 420 B, Micro-Now Instrument Co. Inc., Chicago, IL) was used. For the lower power system the plasma was maintained in a 5 mm i.d., 7mm o.d., tangential flow quartz tube with a threaded teflon insert. For the 500 W plasma, an 8 mm i.d., 10 mm o.d. quartz tube was used. The torch was inserted through the center o f a copper Beenakker TM010cavity with an inner diameter o f 89 mm and a depth of 11 mm. Impedance matching was accomplished with a three-stub tuner (model 1878B, Maury Microwave, Cucamonga, CA). The forward power was 120 W and the reflected power was between 0 and 1 W. 2.3.2 Sample Introduction System A Cetac U 5000 (Cetac Technologies, Omaha, NE) ultrasonic nebulizer with a manual transducer (operated at 1.39 MHz) was used for solution nebulization. A Rabbit peristaltic pump (Rainin Instruments, Wobum, MA) was employed for direct solution nebulization of bulk samples. For the HPLC studies, a dual-pump HPLC system (Dynamax, model SD200, Rainin Instruments) and a C „ reverse-phase column (4.6 X 250 mm, 5|im particle size, Microsorb-MV™ from Rainin Instruments) were used. A six port injector with a 20 JiL sample loop (Rheodyne, Cotati, CA) delivered the analyte to the column. Eluates were directed to the USN via a 0.01 inch i.d. PEEK tube (Rainin Instruments, Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 32 Woburn, MA). The mobile-phase flow rate was maintained at 0.55 mL/min. For certain experiments, 0.5 mL/min 0.1% H2S04 in methanol was mixed with the effluent from the column through a post column “T” junction and the mixed solution was directed to the USN. 2.3.3 Aerosol Desolvation System Two-stage aerosol desolvation was utilized. The USN mist was initially directed through the Cetac U5000 desolvator where it was heated to 140°C and then condensed at -10°C with the water-ethyiene glycol-cooled condenser. The second stage consisted o f a CETAC MDX-100 microporous tubular PTFE membrane desolvator. Some o f the membrane dimensions are i.d = 0.5 cm, length = 2 m, pore size = 1 |im . 2.3.4 Optics A 10-cm focal length fused silica lens was used to focus the axial plasma image on the entrance slit o f a 1-m focal length spectrometer (model 1000 M, Spex, Edison, NJ). A 1200 grooves/mm grating blazed at 500 nm was used. Slit widths were set at 10 |im . The photomultiplier tube (PMT) (model IP 28, Hamamatsu, Middlesex, NJ) was biased at -850 V. For preliminary experiments, a low-resolution Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 33 0.35-m focal length GCA/McPherson (model EU/E-700, Acton, MA) spectrometer was used. The grating had 1200 grooves/mm with a blaze wavelength o f250 nm. 2.3.5 Data Analysis Signal from the PMT was acquired by a 486 DX, 33 MHz computer using Spex autoscan software. Data integration time was 1 second per point. Quattro Pro* software was used for data analysis. All measurements were obtained in triplicate. Detection limits were calculated as the Cl concentration yielding a signal 3 times the standard deviation o f the background. 2.3.6 Reagents Greater than 99.99% pure He with a flow rate o f 12.3 L/min was used to sustain the plasma. Reagent-grade MgCL (J.T. Baker Chemical Co., Phillipsburg, NJ), 2 ,6-dichlorobenzamide (DCB), 4-chlorobenzamide (CB), and 2,4,6trichlorobenzoic acid (TCBA) (Aldrich, Milwaukee, WI) were used. Reagent-grade methanol (Mallinckrodt Specialty Chemicals Co., Paris, Kentucky) was used for making organic analyte-containing stock solutions and for the HPLC mobile phase. Methanol and water mobile phases were boiled and sonicated for 30 minutes each to remove dissolved gases. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 2.4 Experimental For initial characterization, bulk samples were delivered to the nebulizer with the peristaltic pump. Five hundred ppm chlorine was introduced as MgCl2in pure water. Each sample was introduced with and without the membrane desolvator “in line.” Characteristic Cl emission lines were monitored at 479.5,481.0, and 481.9 nm. The operating conditions for this experiment are listed in Table 1. Effects o f the membrane desolvator on aqueous Cl signal intensity were studied by comparing the Cl signal at 479.5 nm, with and without the membrane desolvator. Figure 8a illustrates chlorine emission without the membrane desolvator in place. As shown in Figure 8b, use o f the membrane desolvator results in a 4-fold increase in signal. Additionally, a significant decrease in background noise was seen when using the membrane desolvator. A 100-fold improvement o f the detection limit, from 200 to 2 ppm, was seen with the membrane desolvator. Observed enhancement of signal with membrane desolvator established the fact that solvent loading adversely affects the analytical performance o f the plasma, and membrane desolvators can effectively reduce this problem with aqueous solution nebulization. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 35 Table 1. Unoptimized Conditions Used for Preliminary Experiments. Plasma Power Plasma gas flow 120 watt lOL/min Peristaltic pump Uptake rate 1.5 mL/min USN Carrier gas flow rate Heated tube Condenser temperature 0.5 L/min 140°C 5°C Membrane desolvator Countercurrent gas flow Desolvator temperature 1 L/min 160°C PMT Voltage - 900 volts Monochromator Focal length Slit width Integration time - 0.35 m 100 pm 0.1s Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 36 100 Is " | 40 20 479 460 461 482 483 Wavelength (nm) (») 100 80 1 60 ? 40 20 479 480 481 482 483 WavatmgSi (nm) (b) Figure 8. (a) Spectrum obtained from aqueous solution of 500 ppm Cl as MgCl2 without and (b) with membrane desolvator. Three characteristic Cl lines at 479.5,481.0, and 481.9 nm are seen. All the peaks are normalized against the highest peak in spectrum 8b. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 37 2.5 System Optimization Three independent He gas sources were used in the system. The plasma was sustained by the plasma gas. A carrier gas was used to drive the aerosol produced at the USN through the system, hi the membrane desolvator, a countercurrent gas flowing opposite in direction to the flow of the analyte is used in the outer channel to flush out the solvent (Figure 6). The flow rates o f these three gases are critical for optimal system performance. These flow rates were optimized for inorganic analytes in aqueous and organic solutions and Anally for organic analytes in methanol and acetonitrile solutions. 2.5.1 Inorganic Analytes in Water Cl signals from aqueous MgCl: solutions were observed as each o f the flow rates was varied. Figure 9 is a plot o f Cl signal as a function o f plasma gas flow rate with the carrier gas flow set at 0.5 L/min. For this experiment the membrane desolvator was not used. The greatest Cl signal was observed at a plasma gas flow rate o f 12.5 L/min. Any further increase in the flow rate caused a reduction in signal, probably due to a combination o f decreased residence time o f the analyte in the plasma, analyte dilution, and plasma flicker due to nonlaminar gas flow through the torch. Flow increases beyond 14.5 L/min resulted in extinguishment o f the plasma. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 38 a § 120 , ---------------------------------------------------------------------------------------- 100 | I gg : USN gas flow = 0.5 L/min '35 O 60 o z 40 20 10 11 12 13 14 15 Gas flow rate (L/min) Figure 9. Cl signal as a function of plasma gas flow rate. The USN gas flow is set at 0.5 L/min. For this experiment the membrane desolvator is off-line. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 39 From this experiment 12.5 L/min was determined to be the optimum flow rate for the plasma gas. The optimum carrier gas flow with and without membrane desolvator was determined at a plasma flow rate of 12.5 L/min. Aqueous Cl signal was observed as the carrier gas flow rate was varied. The results o f this experiment are determined and shown in Figure 10. When the membrane desolvator was removed from the system, the optimum flow rate was observed to be 0.5 L/min. Increasing the flow rate beyond 1.75 L/min caused extinguishment o f the plasma due to excessive solvent loading. However, with the membrane desolvator, the optimum carrier gas flow rate was at 2.25 L/min. Any further increase in the flow rate caused plasma flicker and extinguishment. The membrane desolvator countercurrent gas flow rate was optimized in a similar fashion at a plasma flow rate o f 12.5 L/min and a carrier gas flow o f 2.25 L/min. The results are shown in Figure 11. The Cl signal peaked at 1.25 L/min and declined gradually with subsequent increases in the flow rate. While purely speculation, it is possible that the decline in signal at flow rates higher than 1.25 L/min could be attributed to analyte collisions with the tube wall due to the introduction of turbulence in the outer membrane desolvator channel. A Cl concentration calibration plot was obtained with aqueous MgCL solution under the optimized conditions. The calibration plot is shown in Figure 12. The plot was linear with a correlation coefficient (r2) value o f0.99994. The slope and the intercept o f the plot were calculated to be 0.26 counts/ppm and 5.01 counts Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. \ 100 i Plasma gas flow = I2.S L/min Countercurrent gas flow = 1 L/min with membrane desolvator 80 I n §> I 10 i S 60 .M • i i O 40 ! Z Without MDX 20 -m - With MDX o i0 Figure 10. 0.5 1 1.5 USN gas flow (L/min) 2 2.5 Cl signal as a function o f USN gas flow. The plasma flow rate is set at 12.5 mL/min. Membrane desolvator countercurrent gas flow rate is set at 1 L/min. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 41 ,--------------- Normalized Cl signal 120 Plasma gas flow rate = 12.5 L/min 100 ; 80 j 60 i 40 i 20 ■ * 0 / • -------------------------- 0 Figure 11. 0.5 1 1.5 countercurrent gas flow rate (L/min) 2 Cl signal as a function o f membrane desolvator countercurrent gas flow rates. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 Figure 12. 50 100 150 Concentration in ppm 200 250 Cl calibration plot under optimized conditions. Cl introduced as aqueous MgCl? solution. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 43 respectively. The Cl detection limit (DL) was calculated using the formula of equation 2.1 and was found to be 1 ppm. DL = 3 * C * ( | ) (2.1) where C = analyte concentration, N = noise (standard deviation o f the background), and S = background corrected signal. The detection limits achieved for aqueous Cl solution were similar to those obtained by Akinbo and Carnahan using a flat-sheet polypropylene membrane desolvator with a USN-MIP AES system.34,36 2.5.2 Inorganic Analyte in Methanol The objective o f the project is to use the MIP AES system for reverse-phase HPLC applications. Hence, investigation of the plasma behavior with organic solvent nebulization is necessary. For this experiment, a solution of MgCL in methanol was introduced to the plasma without the membrane desolvator. To facilitate better desolvation o f the analyte in the USN, the condenser was set at -S°C. Upon introduction o f methanol without the membrane desolvator, the plasma changed from its usual color of pink (due to H|T] 656 nm emission) to an intense blue (due primarily to C2 and CH emission bands) and was extinguished within a minute. However, with the membrane Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 44 desolvator, the plasma could be sustained without extinguishment. Optimizations o f gas flows in the system were also performed for the organic solvent solutions. The optimum plasma and USN gas flow rates were similar to those observed for aqueous solution nebulization. The optimal countercurrent flow was found to be 3.S L/min, much higher than the 1.25 L/min optimal flow rate with aqueous solutions. Figure 13 shows Cl signal intensity from a methanolic 500 ppm MgCl2 solution in methanol as the membrane desolvator countercurrent gas flow is varied. Using the (organic MgCL solution) optimized conditions, Cl detection limits were 1 ppm. This value is the same as that determined for the aqueous MgCL solution. These results show that membrane desolvation is effective even with organic solvents. 2.5.3 Characterization o f the System with Organic Analytes The system showed promising performance with inorganic analyte salts in both aqueous and organic solvents. In this section, the behavior of the system with organic analytes in organic HPLC-type solvents such as methanol-acetonitrile-water, methanol-water, and acetonitrile mixtures are discussed. A 500 ppm Cl solution as 2 ,6 dichlorobenzamide in methanol was introduced with the membrane desolvator incorporated into the system. The spectrometer was scanned from 470.0 to 483.0 nm to observe the three characteristic Cl lines at 479.5, 481.0, and 481.9 nm. However, no Cl signal was observed using optimum Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 45 55 Cl signal in arbritary units 50 Plasma= I2.S L/min USN = 2.25 L/min 45 40 35 30 25 20 0.75 Figure 13. 1.25 1.75 2.25 2.75 3.25 Countercurrent gas flow (L/min) 3.75 4.25 Cl signal as a function of membrane desolvator countercurrent gas flow. Five hundred ppm MgCl2 in methanol is used. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 46 conditions. Similar behavior with organic analytes was observed by Akinbo and Carnahan.36 They solved the problem by adding 0.125 M NaOH to the analyte. NaOH enhanced the transport o f the volatile organics. However, large amounts of NaOH caused plasma flicker, which led to increased noise. Also, NaOH quickly deteriorated the plasma torch. Hence, addition of NaOH is not a viable option for routine analysis. It was thought that the low-boiling-point organic analytes might volatilize as they passed through the 150°C membrane desolvator and diffuse through the PTFE membrane with the solvent vapor. To investigate these possible effects, the temperature of the membrane desolvator was varied and methanol solutions containing 500 ppm Cl as DCB and MgCU were introduced. Results are shown in Figure 14. The inorganic chlorine signal increased as the desolvation temperature was increased. High temperatures facilitate efficient desolvation and the inorganic analyte exists as nonvolatile particulates. Contrary to the observations for the MgCl, solution, at temperatures o f 90°C and greater, the DCB Cl signal decreased significantly. At higher temperatures, it appears that the more volatile DCB is lost via transport through the membrane, resulting in a decline in the organic Cl signal. Similar trends were seen with 4-chlorobenzamide and trichlorobenzoic acid (Figure 15). These results indicate that a membrane desolvator temperature between 20° and 50°C provides the maximum signal for the organic analytes. However, temperatures below 50°C caused plasma to flicker after 20*30 minutes of operation, due to less efficient desolvation and the increased amount o f organic solvent being directed to the Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 47 70 , ------------------------------------------------------------------------------------------ ----------------- g0 i • 50 Sig MgCI2 ■' Sig DCB « 40 ' c ™ « • O 30 20 t 10 • --------------------------------------------------- 0 20 40 60 80 100 120 140 a ---160 Temperature in Centigrade Figure 14. Inorganic and organic Cl signal vs membrane desolvator temperature. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 10 #___________________m * * 5 ! TCBA (mp -164) ' ■ " - « 0 20 Figure 15. 30 40 50 60 MO temperature 70 80 Organic Cl signal vs membrane desolvator temperature. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 49 plasma. Hence, the desolvation temperature was set at S0°C for subsequent experiments with organic analytes. Under these conditions the effects of membrane desolvator countercurrent flow rates on the signal were studied. Results are shown in Figure 16. Five hundred ppm Cl as 2 ,6 dichlorobenzamide and 4-chlorobenzamide in methanol was examined. Both analytes exhibited similar tendencies. The peak signal was observed at a counter current gas flow rate o f 4.0 L/min. A plot o f Cl S/N versus countercurrent gas flow is shown in Figure 17. The S/N increased gradually with increases in countercurrent gas flow rates and peaked at 3.5 L/min, similar to what was observed in the signal versus counter current flow plot (Figure 16). This behavior can be attributed to increased analyte desolvation with increases in countercurrent gas flow to a flow rate of 3.5 L/min. A decline was seen at 4 L/min. Further increases in the countercurrent gas flow rate introduced carrier gas turbulence resulting in increased background (baseline) noise. A countercurrent gas flow rate of 3.5 L/min was used for subsequent experiments. Complete optimization conditions for organic and inorganic analytes are shown in Table 2. Detection limits determined, based on concentrations yielding signal-to-noise ratios 3 times the standard deviation of the baseline noise, for 2,6 dichlorobenzamide and 4 chlorobenzamide were 2 and 1.5 ppm respectively. Under these conditions, similar detection limits were observed from DCB and CB in acetonitrile solutions. These detection limits were comparable to those observed with the aqueous Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 50 60 Sig 2,6 DCB 50 ! Sig 4 CB _40 ac e» M a 30 20 10 Figure 16. 1.5 2 2.5 3 3.5 Countercurrent flow (L/min) 4 Cl signal vs membrane desolvator countercurrent gas flow. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 51 1200 S/N DCB 1000 i ! j ■S/N CB 800 §600 400 200 0.75 Figure 17. 1.25 1.75 2.25 2.75 3.25 Countercurrent flow (L/min) 3.75 4.25 Cl S/N vs membrane desolvator countercurrent gas flow. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 52 Table 2. Optimum Operating Conditions for Inorganic and Organic Analytes. Plasma gas (L/min) Carrier gas (L/min) Countercurrent gas (L/min) Membrane desolvator temp. (°C) Condenser temp. (°C) Cl as aqueous MgCl2 without membrane desolvator 12.3 0.8 — — 5 Cl as aqueous MgCI2 with membrane desolvator 12.3 1.8 1.4 160 5 Cl as DCB in methanol with membrane desolvation 12.3 1.8 3.5 50 -10 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 53 inorganic Cl solutions. These results indicate that the efficiency o f solvent removal by the CETAC MDX-100 membrane desolvator for both aqueous and organic solvents is similar. For organic solvents, membrane desolvation is necessary to obtain signal. Figure 18 shows a Cl spectrum from a 500 ppm Cl as DCB solution in methanol without the membrane desolvator. No Cl signal is observed. Figure 19 is a 500 ppm Cl spectrum from a DCB in methanol solution with the membrane desolvator under the optimized conditions listed in Table 2. The three characteristic Cl emission lines are clearly seen in Figure 19. 2.6 Examination of Background Emission with Membrane Desolvation A series o f experiments was performed to examine general effects o f the membrane desolvation and lower desolvation temperatures on the spectral background. Preliminarily behavior o f the plasma was visually inspected as methanol was nebulized. Figure 20 shows pictures o f the plasma plume captured through a digital camera. Figure 20a is the picture o f the He plasma without solution nebulization. As seen in the figure, the plasma has a pink core with a blue outline. The pink coloration is due to H(I) 656 nm emission and the blue emission at the edge is due primarily to C2 and CH emission bands. Figure 20b is the picture o f the plasma when pure methanol is being nebulized through the membrane desolvator and the Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 479 Figure 18. 480 481 Wavelength (nm) 482 483 Five hundred ppm Cl signal from 2,6 dichlorobenzamide in methanol without membrane desolvator. No Cl signal is seen. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 479 Figure 19. 480 481 Wavelength (nm) 482 483 Five hundred ppm Cl spectrum from 2 ,6 dichlorobenzamide in methanol. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 56 a Figure 20. b e (a) Image of the original plasma (nothing is being nebulized), ( b) image o f the plasma when methanol is being nebulized with the membrane desolvator, and ( c) image o f the plasma when methanol is being nebulized without the membrane desolvator. A 500-watt generator was used for this study. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 57 desolvator temperature is set at the 50°C optimum temperature for organic analytes. A slight increase in intensity of the blue outline coloration seen due to emission from the methanol that is not eliminated by the desolvator. But the picture o f this plasma appears similar to the original plasma, indicating that the desolvator efficiently removes most of the organic solvent, even when operated at 50°C. Figure 20c is a picture of the plasma as methanol is nebulized directly without the membrane desolvator. The plasma color turned from pink to an intense blue. The plasma became unstable under these conditions and the plasma torch was coated with carbon immediately. This simple set o f studies implied effective removal of organic solvents by the MDX-100 desolvator, even at the lower temperatures necessary for semivolatile organic analytes. To further corroborate the effectiveness the membrane desolvator, background emission spectra from the plasma were analyzed. Figure 21 depicts the 200*600 run spectrum during pure methanol nebulization with and without the membrane desolvator “in-line.” The spectra are similarly scaled but have been offset on the yaxis for visual clarity. Without the desolvator, intense solvent-related molecular emission is seen from C2, CN, and OH. Additionally, intense C(I) line emission is observed at 247 nm. With the membrane desolvator in place and the temperature set at 50°C as dictated by organic analyte considerations, the molecular emission bands are reduced considerably and the only prominent features are those ofHe(I) lines at 501 and 587 nm. To examine the effects of temperature on the spectral background, methanol was nebulized and 200-600 nm spectra were obtained with the desolvation Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 58 120 512.9 (C2) 100- WrthMD 473.7 (C2) 436.5 306 (OH) 20 IC2) 388 (CN) {CN) - 200 250 300 350 400 450 500 550 600 Wavelength (nm) Figure 21. Methanol background with and without membrane desolvator. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. temperature set at SO, 100, and 150°C. These plots are shown in Figure 22. It should be noted that, compared to Figure 21, the gain is greatly increased to accentuate the spectral detail. All the plots in Figure 22 are normalized to the most intense 587-nm He signal at a membrane desolvator temperature o f 150° C (Figure 22b). Figure 22a is the emission spectrum from the plasma with no solution nebulization. The most prominent features in this spectrum are emission lines from the He plasma gas. Figure 22b, 22c, and 22d show the methanol background spectra collected as the desolvator temperature is varied. As the temperature is decreased from ISO to SOX, all carbonbased molecular emission bands from the solvent increase only slightly in intensity as a result of reduced transport through the membrane. (C2and OH arise directly from the solvent. It appears that CN arises from the combination o f carbon from the solvent with N2either from atmospheric entrainment or helium contamination.) It is important to note that, while decreasing the desolvation temperature somewhat decreases the He(I) line emission intensities, the changes in He(I) line intensities are only slight. This observation indicates that the changes in solvent transport from S0° to 150°C may not significantly affect the “excitation chemistry” o f the plasma. The required lower desolvation temperature does not appear to have a deleterious effect on analyte excitation. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 60 100 Spccmm origan) p b s m 517 n it 4471 " 200 300 1 C(,) 495.7 400 WavMngtfi(nm) 600 500 22(a) 100 MOH iptcm m « MO tamp. 150 He 517 80 He 501.5 He 388.8 60 40 20 i OH 306 a 01 388 CN m -4 200 22(b) Figure 22. 250 300 He 447.1 436.5 a H(l) 186 cm 495.7 473.7 C2 5119 Cl 563.6 -J 350 400 Wavelength (nm) 450 500 550 600 (Continued on following page) Plasma background spectrum at different membrane desolvator temperatures while methanol is being nebulized, (a) Original plasma (nothing nebulized), (b) Membrane desolvator temperature 150°C. (c) Membrane desolvator temperature 100°C. (d) Membrane desolvator temperature S0°C. The plots are normalized to the He peak at 587 nm at membrane desolvator temperature of 150°C. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. Figure 22 (continued) 100 MeOH background at M> tamp. 100 He 587 80 I I He 60 501.5 He 388.8 40 He 447.1 OH 306 20 CN 388 l 200 250 300 H(l) 486 C2 4365 CN 421 ■- ji 350 400 Wavelength (nm) 1 C2 j 512.9 C(l) 495.7 Cl 473.7 ! M 450 C2 563 6 1 600 550 500 22(c) 100 MeOH backgound M MOtemp. 50 He 587 80 60 He 5015 40 He 512.9 H(l) 486 388.8 OH 20 i 306 He 447.1 CN 388 Cl O CN C2 CCD 495.7 473.7 C2 563.6 —— I ^1 200 250 300 350 400 Wavelength (nm) 450 500 550 600 22(d) Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 62 2.7 Examination of a 500 W Plasma for Detection The low-power plasma (100 W) was used for the purpose o f preliminary characterization of the membrane desolvator. Compared to low-power plasmas, highpower plasmas are more tolerant to solvents and provide higher thermal energy for analyte excitation. Hence, a 500 W maximum power generator was used to investigate the possible enhancement o f the analytical detection limits and sensitivities. For these experiments, the 1-m Spex monochromator was used. A series o f tests similar to those performed with the 100 W plasma were carried out to optimize the USN carrier gas flow, membrane desolvator counter current gas flow, and plasma power. A 500 ppm Cl solution of DCB in methanol was used to study the effects o f these parameters on the S/B ratios. For this experiment, the optimum USN flow (1.8 L/min) and countercurrent flow (3 L/min) from the lowpower plasma experiments were used. The minimum gas flow required to sustain the plasma was about 11 L/min. However, at this flow rate, a heavy carbon deposition from methanol was seen on the plasma torch, which led to arcing in the torch and torch melting. This problem was resolved by increasing the flow rate to 15 L/min. Figure 23 is a plot of Cl S/B ratio as a function of plasma gas flow rates. As the flow rate was increased above 15 L/min, the Cl S/B ratio decreased steadily. A 10% decrease in S/B was observed as flow rate was increased from 15 to 19 L/min. This Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 15 Figure 23. 16 17 Plasma gas flow (L/min) 18 19 Plasma gas vs Cl S/B. 500 ppm Cl as DCB in methanol used. Five hundred W maximum power generator operated at 400 W. USN gas flow was set at 1.8 L/min and the membrane desolvator countercurrent flow at 3 L/min. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 64 decrease can be attributed to lower analyte residence time and analyte dilution with increases in flow rates. Figure 24 depicts USN gas flow rate optimization at various plasma gas flows. The USN gas flow was varied with plasma gas flow rates o f IS, 16, and 17 L/min. The optimum S/B ratio was observed at a USN gas flow o f 1.8 L/min for all of the plasma gas flow rates investigated. This optimum USN flow rate was the same as that observed for the 100 W plasma. The membrane desolvator countercurrent flow was set at 3 L/min. Countercurrent gas flow optimization was also done for different plasma gas flows. Results are shown in Figure 25. Again, the optimum rate (3 L/min) was found to be the same as what was obtained for the lower power plasma. The high-power plasma generator gave an opportunity to vary the plasma power over a large range (170 - 520 W) and maintain a stable plasma. The effect of plasma power on the Cl S/B ratio is shown in Figure 26. It was expected that the S/B ratio will increase with increase in plasma power as more thermal energy is generated. As per expectation, the Cl S/B ratio increased (53%) as the plasma power was increased from 170 to 520 W. Detection limits for DCB and CB calculated under these optimum conditions were 1.2 and 1 ppm respectively. These detection limits were very similar to those obtained with the 100 W plasma (2 and 1.5 ppm for DCB and CB respectively). Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 1 Figure 24. 1.5 2 USN gas flow (L/min) 2.5 3 USN gas flow vs Cl S/B. Five hundred ppm Cl as DCB used in methanol. Plasma was operated at 400 W. Membrane desolvator counter-current flow was set at 3 L/min. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 66 Plasma gas flow rate S/B 15 -v - 16 ■17 O' 0 Figure 25. 1 2 Counter current gas (L/min) 3 Membrane desolvator countercurrent gas flow vs Cl signal. Five hundred ppm Cl as DCB in methanol was used. Plasma operated at 400 W. USN gas flow was set at 1.8 L/min. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 100 Figure 26. 200 300 400 Plasma power (W) 500 600 Plasma power vs Cl S/B. Five hundred ppm Cl as DCB in methanol was used. Plasma gas was set at IS L/min, USN gas at 1.8 L/min, and membrane desolvator countercurrent flow at 3 L/min. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 2.8 Summary The membrane desolvator operated efficiently for both aqueous and organic solvent desolvation. Results o f the background studies and the similar detection limits achieved with aqueous and organic solvents support this conclusion. Plasma gas, carrier gas, membrane desolvator countercurrent flow rates, and plasma power conditions were key factors in obtaining maximum nonmetal emission signal. For volatile organic analytes, operation o f the membrane desolvator at a lower temperature was critical. Enhancement o f the signal using a 500 W generator was investigated. Detection limits for DCB and CB were not significantly enhanced with the higher power plasmas. These results indicate that enhancement of analyte throughput and transport to the plasma and even better desolvation of the analyte call for further investigation. Some o f these aspects are discussed in Chapter 3. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. CHAPTER 3 INTERFACING HPLC WITH THE MIP AES USING USN AND MEMBRANE DESOLVATION 3.1 Introduction As the toxicity and mobility, and hence the environmental and biomedical importance, of an element is strongly dependent on the chemical form in which it occurs, there is a growing interest for elemental speciation rather than total elemental analyses. Typically, speciation involves two complementary analytical techniques: isolation o f various species or forms o f the analyte and detection o f those individual species. For separation, various techniques are available. However, chromatographybased procedures like GC, LC, SFC, and capillary zone electrophoresis (CZE) are effective and commonly used. For detection, plasma-based mass spectrometric and atomic emission techniques have been successfully used in conjunction with chromatography. Plasma-based detectors exhibit superior sensitivity compared to other types of detectors commonly used with chromatography. Also, as discussed in section 1.2, plasma-based spectrometries provide additional selectivity to the separation process. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 70 Various workers have interfaced plasma AES and MS systems with chromatographic techniques for speciation and detection. Kim et al.120,12' coupled a GC with Ar ICPMS for determination o f alkyl lead compounds (tetraethyllead, trimethylethyllead, dimethyldiethyllead, methyltriethyllead, and tetraethyllead) in fuel. Various mixtures o f organomercury, organotin compounds,122and metalloporphyrins123have also been separated and quantified using this technique. MIPs have also been used with GC for nonmetal selective detection, and GC-MIP AES systems are commercially available. Bradley and Carnahan124 have used such a system for oxygen selective detection for petroleum samples. Haloorganics in drinking water were assayed by Quimby et al.l2s Becker and Colmsjo126used GC-MIP-AES to determine 34 tri-, tetra-, penta-, and hexacyclic aromatic sulfur heterocycles. ICPs have also been used with LC for separation of ionic, polar, nonpolar, neutral compounds with low volatility, and low thermal stability. Houk and colleagues127,12s successfully separated phosphorous-containing compounds (ortho, pyro, and tripolyphosphate), organolead (trimethyllead, triethyllead) and organomercury (methylmercury, ethylmercury, and phenylmercury) mixtures using reverse-phase ion pairing LC-ICPMS. Dauchy et al.129have used reverse-phase HPLC-ICP MS to separate mixtures o f organotin (di, mono, and tributyltin). Camara and coworkers130 used a similar approach to separate four selenium species (selenocystine, selenomethionine, selenite, and selanate). Ion exchange chromatography has also been used with ICPs for speciation o f Chromium (Cr [HI] and Cr [VI], Vanadium [IV]131 and Vanadium (V)) and rare earth elements.132 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 71 In this chapter, characterization o f a reverse-phase HPLC - MIP AES system is discussed. Akinbo and Carnahan36 used a similar system for nonmetal selective detection o f organics with reasonable success. However, they experienced transportrelated problems with low-boiling-point organic analytes. Also, the USN failed to nebulize certain LC solvent mixtures, which limited the mobile phase options. These problems and their solutions are addressed in this discussion. 3J Experimental The schematic o f the HPLC-MIP AES is shown in Figure 27. This set-up is similar to that shown in Figure 5, except a Rainin Dynamax HPLC was used for solvent introduction instead of a peristaltic pump. A peristaltic pump (not shown) was used to drain the excess solvent from the USN aerosol chamber. The specifications for the HPLC system are provided in section 2.3.2. The solvent from the HPLC was directed to the USN using a 0.01 inch PEEK tubing. Aerosol exiting the USN nebulization/desolvation system was then transported to the plasma via the membrane desolvator. The monochromator was set to detect the wavelength o f interest. Data were collected throughout the chromatographic run. Typically, 20 |xL of sample were injected into the LC column. Chromatograms were obtained by monitoring the element-selective emission as the separated analytes exited the column and passed through the plasma. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 72 Analyte Flow Gas Flow • He Microwave Generator *•••••• Carrier Gas Figure 27. System schematic for the HPLC-MIP AES. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 73 For the HPLC experiments, the areas under the peaks were calculated by summation of the difference between the baseline and each point on the peak. Twenty five points on each side o f the peaks were averaged to calculate the signal at baseline. Noise was calculated by taking the standard deviation of the baseline values from three or more replicate runs. The detection limit was calculated by dividing the amount of analyte by the width o f the peak. The width at half the height of the peak was multiplied by 2 to calculate the peak width. 33 Separation Using HPLC-MIP AES For preliminary studies, 20 microliters o f a methanol solution containing 5000 ppm of Cl in methanol as DCB was injected into the column. One hundred percent methanol was used as the mobile-phase. The mobile phase flow rate was set at 1 L/min. At this flow rate the pressure developed in the LC system wasl.5 kpsi. The monochromator was set to detect the 479.5-nm Cl emission line. The chromatogram is shown in Figure 28. The retention time for the peak was 1.9 min and the peak width 0.41 minutes. As shown in Figure 29, a Cl calibration plot was obtained by injecting DCB solutions in the mass range o f 20 to 120 pg. Areas under the peaks were calculated as described in section 3.2. The plot is linear with a r value o f0.995 and the slope o f the plot was 655.9 counts/ jig. However, the plot showed a significant Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. Figure 28. Chromatogram of DCB. Twenty [iL of 5000 ppm Cl as DCB in methanol used. One hundred percent methanol at a flow rate of 1 L/min was used as mobile phase. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 Figure 29. 20 40 60 80 100 Mass of Cl in micrograms 120 DCB calibration plot using HPLC-MIP AES. One hundred percent methanol at a flow rate o f 1 L/min used as mobile phase. Injection volume was 20 |iL. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 76 negative y-axis intercept (-17812 counts, which corresponded to 27.4 micrograms of Cl). Similar negative y-axis intercept behavior was also observed from the Cl calibration plot o f CB obtained under the same conditions. The calibration plot from CB is shown in Figure 30. The r2 value for this plot was 0.991. The slope was calculated to be 433.4 counts/ |lg. The intercept was -14184.72 counts (corresponds to 33 micrograms o f Cl). The detection limits obtained for Cl obtained from DCB and CB were 2.9 |ig (14S.3 ppm) and 1.5 fig (78.8 ppm) respectively. The corresponding relative detection limits calculated for DCB and CB were 96.9 and 35 ng/s. The problem o f the substantial negative y-axis intercept was believed to be caused by one or both o f the following reasons. Firstly the baseline drops when the analyte elutes, which results in an erroneous reading when the analytical signal is subtracted from the baseline (signal due to the solvent). Secondly a constant amount o f analyte is lost in the system. To investigate these issues specific tests were designed. 3.3.1 Effects o f Anlyte on Background The monochromator was set at 479.5 Cl emission line and a chromatogram was obtained by injecting 20 }iL o f 1500 ppm DCB solution. The other conditions described in the previous section were maintained. To observe the effect o f the analyte on the base line, the monochromator was set at 479.6 nm, away from the Cl Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 77 40000- 30000 — 0000 - 10000 0 Figure 30. 20 40 60 80 Mass of Cl (micrograms) 100 120 CB calibration plot using HPLC-MIP AES. One hundred percent methanol at a flow rate o f 1 L/min used as mobile phase. Injection volume was 20 |iL. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 78 emission line, and another DCB chromatogram was obtained. Figure 31 shows an overlay of the two chromatograms. The chromatogram, shown in black (a) was obtained from DCB when the monochromator was set at the 479.5-nm Cl emission line and one shown in red (b) was obtained when the monochromator was o ff the Cl line. As seen in chromatogram (a), DCB eluted between 1.8 and 2.2 minutes. During the same time interval no decline in signal was observed compared to the baseline signal in chromatogram (b). A decrease in signal between 1.8 and 2.2 minutes when the monochromator was off the Cl line would have suggested baseline shift when the analyte elutes. Hence, the possibility o f analyte interference with the background signal being the cause for negative y-axis intercept in the calibration plots can logically be eliminated. 3.3.2 Investigation o f Analyte Loss in the System To investigate possible analyte loss in the system, the HPLC was replaced with the peristaltic pump for solvent introduction. A number o f Cl calibration plots were obtained using SO to 400 ppm Cl as DCB solutions in methanol. The plot is shown in Figure 32. The plot was linear with a correlation coefficient (r2) o f0.9993. However, consistent with HPLC-MIP calibration plots, these also showed a significantly negative y-axis intercept. Similar behavior was observed with CB calibration plots. This behavior suggested analyte loss either at the USN or in the membrane desolvator. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 79 On Cl line (a) _9000 <0 «# c 3 * 2 !t£ € Off Cl line (b) §7000 5000 Time (min) Figure 31. (a) DCB chromatogram when monochromator is set for 479.5 Cl emission line and (b) DCB chromatogram when the monochromator is set at479.6 nm, off the Cl emission line. One hundred percent methanol at flow rates of 1 L/min was used. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 80 Cl signal in arbitrary units 500000 400000 • 300000 • 200000 100000 o • 0 Figure 32. 100 200 300 Concentration (ppm) 400 Cl calibration plot using DCB with direct solution nebulization. Conditions for organic analyte listed in Table 2 were used. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. After the aerosol is generated in the aerosol chamber, it passes through a heated “IT’ tube (maintained at a temperature of 140° C) to a condenser. It was suspected that at high “U” tube temperatures some o f the analyte might pass into the vapor form and remain in that form even after passing through the condenser and, hence, be lost through the semipermeable membrane in the desolvator. A series o f calibration plots were obtained at different USN “U” tube temperatures. For all these measurements the membrane desolvator was maintained at S0°C. The temperatures were varied between 50° and 100°C. At temperatures above 70°C the plots obtained were very similar to the ones obtained at the “U” tube temperatures of 140°C (Figure 32). The plot showed a response o f zero at about 40 ppm at these temperatures. Improvement in the calibration plot behavior was observed when the USN was operated at “U” temperatures between 50° and 70°C, the calibration plots are shown in Figure 33. The r2values were 0.991 and 0.9995 for the plots at 50° and 70°C respectively. Understandably, due to better aerosol transport at higher temperatures, the sensitivities observed during operation at 70°C were about 3 times higher than what was observed at 50°C. The plots showed a response o f zero at 26 and 18 ppm at 50° and 70°C, respectively. Although not significant, this was an improvement over what was observed at a “U” tube temperature of 140°C. However, operation with “U” tube temperatures below 100°C resulted in severe condensation problems. After about 20 minutes o f operation, the connecting tube between the USN and the membrane desolvator was filled with condensed solvent, which resulted in plasma Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 82 Signal intensity (arbitrary units) 120000 100000 SO degree Celsius 80000 70 degree Celsius 60000 40000 20000 0 0 Figure 33. 50 100 150 200 250 Concentration in ppm 300 350 400 Cl calibration plot using DCB at reduced USN “U” tube temperature. Solvent was introduced by direct solution nebulization. Other conditions for organic analytes listed in Table 2 were used. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. flicker and poor measurement reproducibility. Hence, operation at lower “U” tube temperatures was not a plausible solution to the nonideal calibration problem. Akinbo and Carnahan3*noted similar behavior for organic analytes and utilized 0.125 M NaOH in methanol to enhance analyte transport and linearize the calibration plot to a near-zero intercept. As discussed in section 2.S.3, the excess NaOH was believed to encapsulate the analyte within desolvated NaOH particulates to avoid volatilization as the analyte passed through the heated membrane desolvator. However, large quantities of NaOH led to other problems such as significant background emissions and reduced plasma torch lifetimes. To enhance analyte transport, but avoid NaOH complications, solutions of a number of other modifiers were characterized. Solutions containing 1% HN03, CH3COOH, and H2S04 in methanol were examined and DCB calibration plots were obtained. Results are shown on Figure 34. As with the pure methanol solvent, a linear calibration plot was not obtained with the addition o f 1% HN03or CH3COOH. However, the addition o f 1% H2S04 produced a linear plot with a correlation coefficient o f0.9992 and an x-intercept corresponding to 1.3 ppm. The enhanced calibration behavior with H2S04can be explained by improved analyte transport. Sulfuric acid protonates the amine group of DCB to form less volatile species. Additionally, low vapor pressure o f H,S04depresses the volatility o f the analyte. Nitric and acetic acids have significantly higher vapor pressures. The minimum H2S04 concentration necessary was determined by preparing calibration plots with varying Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 84 1400001— 1 1200004tI -T 1% H2S04 - S joooo-^ 3 e* 4- a ^ooooi 7 •- 1%HN03 1% Acetic Acid $0000+ SC it |oooo35 I 20000+ ▼ ▼ 50 Figure 34. 100 150 200 250 300 Concentration (ppm) 350 400 450 Cl calibration plot from 2 ,6-dichlorobenzamide dissolved in methanolic 1% H2S 04, 1% CH3COOH, and 1% HN03. Other conditions are described in Table 2. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 85 amounts o f H2S04; 0.01% H2S 04 was found to be the minimum necessary concentration to maintain the behavior. Calibration plots o f CB in 0.01% H2S04 also yielded near-zero calibration intercepts. Additionally, calibration plots o f DCB in various methanofrwater mixtures (80:20,70:30,60:40 [v/v]) with 0.01% H2S 04 exhibited near-zero intercepts. Temperature optimization o f the membrane desolvator was performed for the modified solvent. The membrane desolvator temperature was varied between 50° and 110°C and the Cl S/B was observed from 500 ppm DCB in 0.1 and 0.01% H2S04 in methanol solutions. The results are shown in Figure 35. The S/B at 50° C was not significantly different from that seen at 70°C. At these temperatures the S/B from the 0.01% H2S04-modifred solution was 33% higher than that o f the 0.1% H2S04modified solution. That 0.01% H,S04 in methanol is less viscous compared to the 0.1% H2S04 solution, leading to better nebulization, could be the reason for the enhanced S/B with the dilute H2S04. Since there was no noticeable difference in the signal between 50° and 70°C operation, the previously optimized membrane desolvator temperature of 50°C was used for future experiments. Detection limits were obtained with 0.01% H2S04 in methanol and the optimized plasma parameters are listed in the bottom row o f Table 2. Detection limits as CB and DCB were found to be 1.0 and 1.1 ppm Cl, respectively. These values were not very different from those obtained from Cl solutions with pure methanol (see section 2.7) and are comparable to those obtained by Akinbo and Carnahan36 using a flat-sheet membrane desolvator. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. SO 60 70 80 90 Temperature in degrees Celsius 100 110 0.01% H2S04 -m - 0.1% H2S04 Figure 35. Cl S/B from 500 ppm of DCB in 0.01 and 0.1% H,S04 in methanol solution. Solvent was introduced by direct solution nebulization. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 87 3.4 Nebulization of LC Solvents with USN Following attainment of calibration plot linearity, the peristaltic pump was replaced by the HPLC and the separation of a mixture of DCB and CB was attempted. The HPLC-MIP AES system was set up as described in section 3.3. Equal portions of 5000-ppm Cl solution as DCB and 5000-ppm Cl solution as CB were mixed. The sample solvent was HPLC-grade methanol. Twenty |XL samples were injected into the HPLC. One hundred percent methanol at flow rates o f 0.8 mL/min was used as the mobile phase. The chromatogram obtained is shown in Figure 36a. The retention times for DCB and CB were 3.1 and 3.3 minutes, respectively. The peak widths were 30 s for DCB and 45 s for CB. The detection limits calculated for the two compounds were 2.9 }ig (150 ppm) for DCB and 1.5 jig (79 ppm) for CB. With 100% methanol as the mobile phase, complete baseline resolution could not be obtained. To achieve complete separation o f the two peaks, a 70:30 mixture o f methanolrwater was used. The resultant chromatogram is shown in Figure 36 b. However, the peaks were much less intense compared to what was obtained with 100% methanol as mobile phase. The detection limits obtained were 646 and 540 (ig for DCB and CB respectively, two orders o f magnitude higher than those obtained with pure methanol as mobile phase. The loss in signal intensity was due to inability of the USN to effectively nebulize the 70% methanol mobile phase. The decline in USN efficiency for this was noticeable by Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 88 40000 30000 20000 10000 •10000 4 Tme(min) 5 40000 30000 jg 20000 9 1 10000 3 o 0 -10000 0 1 2 3 4 5 6 7 Time((nin) b Figure 36. (a) Chromatogram o f DCB and CB using 100 % methanol as mobile phase and ( b) separation of DCB and CB using 70% methanol as mobile phase. Flow rate was 0.8 mL/min. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 89 visual inspection of the mist within the aerosol chamber. Akinbo and Carnahan36had experienced similar problems. The USN (CETAC U500AT with automatic transducer) failed to nebulize certain water, methanol, and acetonitrile binary and ternary mixtures that are used as HPLC mobile phases. This problem severely impaired the ability to perform determinations requiring certain solvent mixtures for separation. The USN transducer consists o f a LiNb03 piezoelectric ceramic crystal. When the oscillating voltage (at a frequency typically near 1 MHz) is applied, the crystal alternately expands and contracts. This oscillation of the crystal induces a standing wave on the crystal. This wave is transmitted to any liquid film that comes in contact with the crystal. Systematic instabilities in the liquid surface cause it to break up into fine aerosol. Most current commercial USNs are supplied with automatic transducer controllers. These automatic controllers typically monitor the transducer at a fixed frequency (1.4 MHz in the CETAC U50t vT USN) but automatically adjust the input power for efficient nebulization of various liquids. Transducer operation at a fixed frequency o f 1.4 MHz is effective for nebulization o f aqueous and pure organic solutions. However, difficulties arise with mixed solution nebulization, as experienced by Akinbo and Carnahan.36 This problem is illustrated in Table 3, as based upon visual inspection o f the aerosol density in the aerosol chamber. As noted in the “automatic transducer” column, 100% aqueous, methanol, acetonitrile, and isopropyl alcohol solutions could be nebulized efficiently. Ninety and 80% solutions o f the organic Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. * Table 3. USN Nebulization Efficiency o f Binary Solvent Mixtures (v/v) with Automatic and Manual Transducer Controllers. Water:Methanol Water:Acetonitrile Water:Isopropyl alcohol Automatic transducer controller (Fixed frequency) Manual transducer controller 100:0 Nebulized Nebulized 90:10 Not nebulized Nebulized 80:20 Not nebulized Nebulized 70:30 Not nebulized Nebulized 60:40 Not nebulized Nebulized 50:50 Not nebulized Nebulized 40:60 Not nebulized Nebulized 30:70 Inefficient nebulization Nebulized 20:80 Nebulized Nebulized 90:10 Nebulized Nebulized 0:100 Nebulized Nebulized Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. solvents in water were also effectively nebulized. However, the other solvent mixtures were either not nebulized at all or were poorly nebulized. The automatic transducer controller o f the USN did not allow the transducer frequency to be changed. However, a CETAC U5000 USN with manual frequency and input power control was available and utilized. Various methanol, acetonitrile, and isopropyl alcohol solutions in water were introduced to this USN and the frequency was manually adjusted until aerosol formation was visibly noticed. By adjusting the transducer frequency, all the solutions listed in Table 3 could be nebulized. A frequency counter (Hewlett Packard, model S38S A) was connected to the transducer power supply in parallel to monitor the frequency at which each solvent was efficiently nebulized. The observations are listed in Table 4. The solvents that could not be nebulized by the automatic transducer (10 to 70% methanol) required a higher frequency (1.39 MHz) than the solvents that could be nebulized (1.33 MHz). The frequency supplied to the transducer by the automatic controller was measured to be 1.33 MHz, indicating that the frequency supplied by the automatic controller is not appropriate for nebulization o f the 10 to 70% methanol mixtures. Thus, to accomplish aerosol formation from all the solvent mixtures, the transducer frequency was set at 1.39 MHz with the help o f the manual controller. Cl S/B were measured as 500-ppm Cl as DCB in 20 to 100% methanol solutions were introduced to the USN. The results are shown in Figure 37. The Cl S/B gradually increased with increasing amounts o f methanol in the solvent, even though the background emissions were Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 92 Table 4. Nebulization Frequency o f Water:Metiianol and WatenAcetonitrile Mixtures Using USN with Manual Transducer. Water:methanol Watenacetonitrile Manual transducer frequency (MHz) 100:0 1.33 90:10 1.39 80:20 1.39 70:30 1.39 60:40 1.39 50:50 1.39 40:60 1.39 30:70 1.38 20:80 1.33 90:10 1.33 0:100 1.33 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 20 Figure 37. 40 60 Percent MeOH 80 100 Plot of percent methanol in the solvent versus Cl S/B from solutions of500-ppm Cl as DCB solution. Direct solution nebulization was used for solvent introduction. « Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 94 higher with the organic solvents. This shows superior nebulization o f the higher methanol-containing solutions even after transducer frequency optimization. However, approximately two times higher S/B with pure methanol compared to 20% Cl solution translated to only a 2 ppm improvement (1 ppm versus 3 ppm) in the detection limits of the two solutions. However, the capability to nebulize all mobilephase solvents provided an opportunity for a large variety of HPLC applications. 3.5 Assessment of Fixed-Frequency Transducer Behavior To further investigate the behavior of the fixed-frequency transducer, physical properties o f solutions such as the surface tension, density, and viscosity were analyzed. Values for these parameters were obtained from the CRC Handbook of Chemistry and Physics.133,134 Figure 38 is a plot o f density (kg/L) for the full range of water/methanol (v/v) mixtures.133 The density was calculated by using equation 3.1. (Cs + Cw) 1000 (3.1) where D = density at 20°C (kg/L), Cs - anhydrous solute concentration (g/L), and Cw = total water concentration (g/L). The density gradually decreases from 1 kg/L for pure water to 0.8 kg/L for pure methanol. No unusual density profile for the 10 to Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 20 40 60 80 100 Volume % of MeOH Figure 38. Plot o f percent methanol versus density with respect to water. All density values were taken from Weast and Astle.133 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 96 70% solutions o f methanol is observed, which would have indicated that density could be a contributing factor for the inability o f the fixed-frequency USN to nebulize these solvent mixtures. Hence, no correlation between the density and the USN’s peculiar behavior can be drawn from the density plot o f water/methanol mixtures. A plot of surface tension134(dynes/cm) versus percent methanol is shown in Figure 39. The surface tension gradually decreases from 72.25 for pure water to 22.65 dynes/cm for pure methanol. Again, like the density plot, no extraordinary surface tension profiles for the unnebulizable solvent mixtures were observed. Conversely, the viscosity133profile showed more interesting characteristics. Figure 40 is a plot o f relative viscosity versus percent methanol in water. Relative viscosity is calculated as the ratio o f the absolute viscosity of a solution at 20“C to the absolute viscosity of water at 20°C. The relative viscosity increases from l(for pure water) to 1.8 (for 40% methanol) and then gradually decreases to 0.6 for pure methanol. The line perpendicular to the y-axis that extends from 10 to 70% methanol shows that all the solvent mixtures with a relative viscosity o f 1.3 or greater were not nebulized by the fixed-frequency USN. Hence, viscosity appears to be one o f the contributing factors for the USN behavior. The viscosity profile o f isopropyl alcohol (IPA):water mixtures was also examined. The plot is shown in Figure 41. Again, the viscosity curve rises to a maximum and then decreases. The relative viscosity increases from 1 (pure water) to 3.2 for 50% 1PA and then decreases to a relative viscosity value o f 2.2 for 100% IPA. The solutions above the straight line connecting Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 Figure 39. 20 40 60 Volume % MeOH 80 100 Plot o f percent methanol versus corresponding surface tensions. All surface tension values were taken from Weast and Astle.m Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 Figure 40. 20 40 60 80 Volume % of MeOH in water 100 Plot o f percent methanol versus corresponding viscosity relative to water. All viscosity values were taken from Weast and Astle.133 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 Figure 41. 20 40 60 Percent IPA 80 100 Plot of percent IPA versus corresponding viscosity with respect to water. All viscosity values were taken from Weast and Astle.133 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 100 10 and 70% IPA solution in Figure 41 could not be nebulized (refer to Table 3). This observation is consistent with the H20:methanoI studies. The higher viscosity solutions required alternate nebulization conditions. However, while the trend is consistent for both sets o f solutions, the viscosity “cut-offs” vary. The viscosity trend correlates well with the behavior, but the absolute viscosity does not. Obviously, another factor is needed for a complete explanation. 3.6 HPLC-MIP AES Using Solvent Modifiers A number of solvent compositions were examined for the separation o f DCB and CB. Baseline resolution was achieved with a 60:40 (v/v) mixture of methanol and water. The 0.SS mL/minute chromatographic eluate was post-column mixed with 0.55 mL/minute of 0.1% H2S04 in methanol and directed to the USN. A schematic of the HPLC-MIP AES is shown in Figure 42. The plasma gas, the carrier gas, and countercurrent gas flow rates were those listed in Table 1 for organic analytes. Figure 43 shows the two Cl peaks obtained from the separation of a mixture containing 30 |ig each of DCB and CB. Calibration plots were obtained (Figure 44). The correlation coefficient calculated for DCB was 0.9996 and 0.997 with CB. The relative standard deviations (RSD) calculated for Cl with the system were between 5 and 8% for both DCB and CB. The sensitivities were found to be 1227 counts/jig for DCB and 1045 counts/jlg Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 101 Analyte Flow Gas Flow .•*’ **• G ultrGrantQb »• DUe | tUnnac N h te • a a a a a a a • a.*i *•••••* O nirQ i 1 1 Modnk Curator Vf t ; H bbO b Figure 42. System schematic o f the HPLC- MIP AES showing post column addition of dilute H,S04. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 102 7000 — 6000 i DCB 1 5000 i £ §1000 ! 1 Sooo Q> CO 2000 1000 0 — 0 Figure 43. 1 2 3 4 5 6 7 8 Time (min) 9 10 11 12 13 Chromatogram showing Cl peaks from 30 |ig 2,6dichlorobenzamide and 30 |ig 4-chlorobenzamide. Sixty:forty (v/v) methanokwater was used as the mobile phase. The mobile-phase flow rate was 0.55 mL/min. Mobile-phase modifier, 0.1% H,S04, was pumped at a rate o f 0.5 mL/min. Other conditions are as described in Table 2. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 35000 30000 & 2.6 DCB 1 25000 £* 2 | a 4CB 20000 Z 15000 2 sa. 10000 •* 5000 2 Figure 44. 4 6 8 10 12 14 16 18 Mass of Cl in micrograms 20 22 24 26 Calibration plots from 2,6-dichlorobenzamide and 4-chlorobenzamide. Sixtyrforty (v/v) methanol:water was used as the mobile phase. The mobile-phase flow rate was 0.5S ml/min. Mobile-phase modifier, 0.1% H2S04, was pumped at rate o f 0.5 mL/min. Other conditions are as described in Table 2. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 104 for CB. It is likely that the 14.8% higher sensitivity for DCB was due to its higher boiling point and reduced diffusion losses through the desolvator membrane, compared to CB. Chlorine detection limits for DCB and CB were 110 ppm (36 ng/s) and 127 ppm (47 ng/s), respectively. These mass-flow detection limits were about 4 to 5 times higher than those obtained with direct solution nebulization (10 ng/s) described in this manuscript. The major contributions to increase in detection limits with HPLC are onand off-column dilutions as well as dilution due to post column addition o f H2S04 Using membrane desolvation with NaOH os the transport salt, Cl detection limits obtained by Akinbo and Carnahan36 were between 74 to 200 ng/s, which are comparable to detection limits presented in this study. However, detection limits reported with LC-He-MIP using the moving-band interface were lower by about 2 orders o f magnitude (between 0.22 and 0.77 ng/s).3S With a moving-band interface almost 100% of the analyte is transported to the plasma, whereas a much smaller fraction is transported with the ultrasonic nebulizer.36 Additionally, superior desolvation o f the analyte is achieved with the moving-band interface. However, the membrane desolvation system provides better performance in terms o f ease of operation and reproducibility. 3.7 Summary Linearization o f the calibration plot was achieved using H2S04 as the solvent Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 105 modifier. Detection limits and precision obtained using this system were comparable and in some cases better than those obtained by Akinbo and Carnahan.36 All HPLC solvent combinations could be nebulized through the USN by using a manual transducer control. This will provide unlimited mobile-phase choices for HPLC separations. However, improvement is necessary to obtain detection limits comparable to those obtained from GC-MIP systems. Enhancement o f analyte throughput by utilizing other types o f nebulizers is one area that needs further investigation. A detailed scheme for enhancement o f analyte throughput to the plasma is provided in Chapter 5. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. CHAPTER 4 HPLC-MIP AES APPLICATIONS 4.1 Introduction As discussed in Chapters 2 and 3, the MIP AES system combined with appropriate optimized conditions for membrane desolvation, mixed solvent nebulization, and solvent modifiers performed satisfactorily with chlorinated organic compounds. With these positive results for the model chlorinated compounds, it is appropriate to examine the potential of the system for a breadth o f sample types. In this chapter, investigations are initiated with studies of other elemental analytes and “real-world” type samples. Emissions from some o f the other nonmetals (Br, I, S, and P) are detailed. Comparisons with MIP AES and UV-Vis detectors for HPLC applications are discussed. The performance o f the HPLC-MIP AES with biological and pharmaceutical samples is demonstrated. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 107 4 2 Examination of Br, I, S, and P Emission As discussed in Chapter 2, Cl line emission signals were used to optimize the MIP AES system. Line emission from other nonmetals (Br, I, S, and P) was also examined using the optimized conditions listed in Table 2. One part per thousand (ppt) aqueous solutions of Br, I, S, and P as inorganic salts were introduced to the plasma and the corresponding emission signals were observed. Figure 45 is a Br spectrum of the 468 to 483 nm region using a solution of KBr03. Three distinct Br ion lines were observed at 470.7,478.8, and 481.9 nm. The peak at 471.4 nm is emission from helium and the molecular band at 473.7 is from C2. Characteristic iodine peaks from the KI03-containing aqueous solution are shown in Figure 46. Three iodine ion lines were seen at 516.3,534.0, and 534.7 nm. Figure 47 is a sulfur spectrum from the (NH4)2S04-containing solution. Sulfur ion emission lines at 543.1, 543.5,545.6, and 547.6 nm are seen. Figure 48 and 49 show phosphorus atom emission lines in the spectral regions o f 231 to 216 and 252 to 257 nm. A H3P04containing solution was used to acquire the P spectra. Characteristic P lines were observed at 213.7,213.8,215.1,215.5,215.6,253.6,253.7,255.5, and 255.7 nm. Table 5 shows the detection limits obtained for Br, I, S, and P using their most intense emission lines. Br, I, and S detection limits were between land 3 ppm. These limits of detection were similar to that observed for Cl. However, a P detection limit Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 108 100 , ----------------------------- 470.7 80 > 478.8 I 60 (0 § 40 o i 481.9 Z 20 468 Figure 45. 470 472 474 476 478 Wavelength (nm) 480 482 484 One ppt Br, MIP AES spectrum from aqueous KBr03. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 510 Figure 46. 515 520 525 Wavelength (nm) 530 535 One ppt I, MIP AES spectrum from aqueous KI03. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 110 100 545.6 Normalized signal 80 60 40 1543.5 543.1 20 •20 542 Figure 47. 547.6 543 544 545 Wavelength (nm) 546 547 One ppt S, MIP AES spectrum from aqueous (NH^SO.,. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 213.72 ,: 1 215.48 :I ; .215.60 0 213 Figure 48. 213.5 214 214.5 215 Wavelength (nm) 215.5 216 One ppt P, MIP AES spectrum (213-216 nm) from aqueous H3P04 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 255.68 20 253.58 1 ;1 I 0 252 Figure 49. 253 254 255 Wavelength (nm) 256 257 One ppt P, MIP AES spectrum (252-257 nm) from aqueous H3P 04. Reproduced with permission o f the copyright owner. Further reproduction prohibited without permission. 113 Table 5. Nonmetal Detection Limits Using MIP AES Nonmetal Analyte used Wavelength (nm) Detection Limit (ppm) Br (II) KBrOj 470.7 2 1(H) KIOj 516.3 3 S(H) (NH4),_S04 545.6 2 P(I) h 3po 4 253.7 0.02 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 114 o f 20 ppb was observed. The lower detection limits obtained with P provided an opportunity to perform some interesting LC-MIP AES applications using P-containing compounds. 43 Sensitivity of MIP-AES Detectors As discussed in section 1.2, one o f the attractive traits of MIP AES detectors is its sensitivity to a myriad o f compounds, even when present in complex matrices. This section compares the sensitivity o f the MIP AES to the commonly used UV-Vis spectrophotometry for LC detection. The separation of a mixture of (3glycerophosphate (GP) and triphenylphosphene (TPP) is demonstrated. These samples were obtained from Aldrich (Milwaukee, WI). Twenty |XL of a methanol mixture containing 500 ppm P as GP and TPP in methanol was injected into the LC column. The monochromator was set at the 253.7 nm P emission line. Eighty:twenty methanokwater (v/v) was used as the mobile phase. The flow rate was maintained at 0.8 mL/min. Using a peristaltic pump, 0.1% H2S04 was post-column added to the mobile phase through a “T” junction at a flow rate o f 0.8 mL/min. The resultant 0.05% H2S04 post-column solution was directed to the USN using a 0.01-inch PEEK tube. The plasma, USN, and the membrane desolvator conditions were set in accordance with the optimized conditions listed in Table 2. The resultant chromatogram is shown in Figure 50. GP and TPP eluted at 1.6 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 115 70000 , -----------------------------------------60000 j [ ' I \ f 50000 I 3 fc* I 240000 ; ' .« p o o o o i s 120000 _ I ■ * 10000 0 0 1 2 3 4 5 ---------6 Time (min) Figure 50. LC-MIP AES chromatogram o f P-glycerophosphate (500 ppm P) and triphenyl phosphene (500 ppm P). Twenty |iL injections were made. Retention times were 1.6 and 2.8 minutes for GP and TPP respectively. Eighty:twenty mixture o f water and methanol at a flow rate o f 0.8 mL/min was used. The P line at 253.7 nm was monitored. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 116 and 2.8 minutes respectively. The peak width at half height for GP was 6s and that for TPP was 9s. The absolute detection limits were calculated to be 38 ng (1.9 ppm) and 30 ng (1.5 ppm) for GP and TPP, respectively. Relative detection limits calculated by dividing the absolute detection limits by twice the peak width at half height were 6.3 and 3.3 ng/s for GP and TPP, respectively. Calibration plots for both phosphorus containing compounds were obtained using 200 - 600 ng P solution mixtures (Figure 51). The calibration plots were linear with lv alu es ofO.9994 for GP and 0.9998 for TPP. The plots showed near-zero intercepts. The sensitivities for GP and TPP were 85.9 and 153.8 counts/ng respectively. A chromatogram for this mixture was also obtained using a UV-Vis detector and is shown in Figure 52. The detector was set at 254 nm. Only one o f the two compounds (TPP) is detected. Glycerophosphate does not contain any strong UV absorbing chromophores; hence, it is not detected by the UV-Vis detector. A glycerophosphate spectrum from 200 to 400 nm taken using a UV-Vis spectrometer revealed very weak absorbance in the UV region. Usually, laborious and timeconsuming derivatization is necessary to make UV-inactive eluates compatible for UVVis detection. However, as shown, appropriate element selective detection with plasma AES detection may allow many compounds to be easily and reliably detected. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 117 7000--------------------------------- Peak area (arbitrary units) 6000— ■ GP • TPP 5000I 4000 3000T 2000 — 1000 0 ------------0 100 200 300 400 500 600 Mass of P (nanograms) Figure 51. LC-MIP AES calibration plots for GP and TPP. The r values for the plots were 0.9994 and 0.9998 for GP and TPP respectively. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 0 1 2 3 4 5 6 Time (min) Figure 52. Chromatogram of GP (500 ppm P) and TPP (500 ppm P) using the UV-Vis detector. Only the peak from TPP is observed (retention time 2.2 minutes). GP is UV inactive, hence is not detected by the detector. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 119 4.4 HPLC-MIP AES Applications 4.4.1 Detection ofDNA High molecular weight compounds such as proteins, peptides, and nucleic acids pose significant analysis difficulties for mass spectrometrists. Most mass spectrometers do not possess high resolving power at higher mass ranges. With plasma AES, the potential to obtain total elemental content information exists. The performance o f the plasma system with a high molecular weight DNA sample from salmon testes was examined. The primary structure of a nucleic acid is a sequence of nucleotide residues connected by 3-5' phosphodiester linkages. A tetranucleotide representing a segment of single-stranded DNA is shown in Figure 53.I3S A DNA double helix is formed from two antiparallel polynucleotide strands as shown in Figure S4.l3s Bases on opposite strands are connected through hydrogen bonding forming a series o f base pairs. Commonly, the length o f long DNA structures is measured in thousands of base pairs or kilobase pairs (kb). For detection o f the sample containing salmon DNA (Sigma Chemical Co., S t Louis, MO) with MIP AES, the presence o f P atoms in the sugar-phosphate backbone was utilized. A 500-ppm sample was prepared by dissolving 5 mg o f the DNA sample Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 120 5 ' end '0—P=0 NH i Adenine (A) = CH — P=0 Guanine (G) —p = o >CH SH O—P=0 OH H 3 'end Figure 53. Structure of a tetranucleotide. The nucleotide residues are connected by 3-5' phosphodiester linkage. Figure taken from Moran etal.135 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 121 Figure 54. Diagram o f a double-stranded DNA. Figure taken from Moran etal.l3s Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 122 in 10 mL o f tris-ethylene diamine tetraacetate ( EDTA) (10 mM tris +1 mM EDTA, pH 8.0) buffer. Twenty |iL o f this solution was injected into the C „ HPLC column and the 253.7 nm P emission line was observed. The mobile phase used was 80:20 methanokwater (v/v) at a flow rate o f 0.8 mL/min. The chromatogram obtained is shown in Figure 55. The retention time for the peak was 1.6 minutes. Despite the presence o f a large number o f carbon atoms in DNA samples, the plasma behaved ideally. No plasma flicker or extinguishment was observed. To determine the length o f the DNA strands present in the sample, gel electrophoresis was performed. The agarose (SeaKem Leagarose, FMC Bioproducts) and the buffer (tris-borate electrophoretic buffer, pH 8.0) solution was heated in a 125-ml Erlenmeyer flask until the agarose dissolved. The solution was then cooled to 60°C and 2 }lL o f 10-ppm ethidium bromide in water solution was added. The gel was immediately poured into a mold. A 12-tooth comb was placed on the mold and the solution was allowed to cool for an hour until a gel was formed. The gel contained 0.9% (w/v) of agarose. Molecular weight standards were prepared by adding 1 (XL of Promega, lkb DNA ladder with 1 }iL o f Promega loading dye and 4 pL o f water.136 The samples were prepared by adding 1,2, and 3 [XL of a 5-ppm solution o f DNA to 1 |lL o f the loading dye. Water was added to make the total volume 6 |iL . The comb was removed from the gel and the framework from the gel mold was set in the electrophoresis tank. The tris-borate buffer was added to the tank until the gel was Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 123 9000 , Signal (arbitrary units) 8000 ; 7000 | i ; i 6000 ! 5000 • 4000 3000 2000 2 3 Time (min) Figure 55. LC-MIP AES chromatogram obtained from 500 ppm DNA, extracted from salmon testes. Injection volume was 20 |iL. Mobile phase used was 80:20 mixture o f methanohwater at a flow rate of 0.8 mL/min. P emission line at 253.7 nm was monitored. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 124 completely submerged. Using a micropipette, 4 }lL o f each sample and the standard were added to the wells in the gel. Eighty volts were applied across the 8 cm gel for 80 minutes, using a Bio-Rad (model 500/200) power supply. Once the separation was complete, a photograph of the gel was taken under UV light. The photograph is shown in Figure 56. Slots 2,3, and 12 were used for the standards. Sample was loaded into slots 5, 9, and 10. The samples and the standards migrated from left to right under the influence of the applied voltage. The molecular weight standard used was a 14fragment DNA ladder, ranging from 0.25 tolO kb. Clearly separated bands across slots 2 and 3 are seen in Figure 56. The bands seen closest to the slots 2 and 3 are the 10-kb fragments and the faint bands seen farthest away from the slots are the 0.25-kb fragments. All the other fragments fall between the 10- and the 0.25-kb bands. The sample bands across slots 5,9, and 10 are not well defined. The smear of bands suggest the sample contains DNA strands o f various lengths. A heavy concentration is seen closer to the slots, indicating significant presence o f greater than 10 kb pair fragments. 4.4.2 Detection o f Vitamin Bn Chromatographic detection schemes often lack selectivity, which may result in overlapping chromatographic peaks. Often, separation and quantification o f only Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. Figure 56. UV picture o f electrophoretic bands from the molecular weight standards (in slots 2,3, and 12) and the DNA sample from salmon testes (in slots 5,7,9,10) on the agarose gel. The direction of migration o f the bands is from left to right. The lower molecular weight fractions move further to the right compared to the high molecular weight fractions. No band separation is observed with the samples. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 126 selected species in a mixture are necessary. However, extraneous components may overlap with the chromatographic peaks o f the analyte. An example where one such complication occurs is the analysis of vitamin B,2 in multivitamin tablets. Multivitamins usually contain vitamins Bt, B6, BI2, and excipients. Since the human body needs only 1 to 2 fig of BI2 aday, B,2 is typically present in ratios betweenlrlOO to 1:1000, with respect to other vitamins in these formulations. The most common chromatographic technique used for these separations is reverse-phase HPLC.137 In isocratic modes, the peaks are not well separated. Gradient elution methods are time consuming and may be less reproducible. In . situations such as this, a detector that can selectively detect the analyte o f interest is desirable. The MIP AES system was examined for the separation o f related mixtures. Of the three vitamins under discussion, only vitamin BI2 contains a phosphate group. The reader is referred to Figure 57. Phosphorus selective detection by the MIP AES detector was exploited. Chromatograms were obtained using both UV-Vis and MIP AES. The solvent after exiting the UV detection system was directed to the MIP AES. UV detection was done at 361 nm and the 253.7 nm P line was monitored with MIP AES. Figure 58 shows vitamin BI2 chromatograms when 20 |iL o f 886 ppm vitamin B12 (20 ppm P) in a 50:50 mixture o f methanokwater. The mobile phase was a 1% acetic acid solution in methanol at a flow rate o f I mL/min. Since the solvent goes through the UV detector to the AES detector, the retention time with the latter is Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 127 NHj «m yCHg *cr y _ HO. CH90H CH2OH • HCI IJ V ^C W H CHjV HCI CH,V Cl^ - C -N H , C % C H ,- C - W , H^-C-Ofe 0 CH, HjM-C-CHOfc1 tyi-c-c* 4 II 0 CH, 0 CH, C * C H ,- C - N * p r t) I CH, CH , „ I CH I H p CI^OH CH, Figure 57. Molecular structure of (a) vitamin B„ (b) vitamin B6and (c) vitamin B,z. Figures were taken from Moran et al.135 Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. -1000 --------------------------------------------------------------------------------0 1 2 3 4 5 Time(min) b Figure 58. Chromatograms obtained from vitamin B,2 (10 ppm P) using (a) UV-Vis detector and (b) MIP AES. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 129 about 40 s longer. The P detection limit calculated with the MIP AES was 1.2 ppm (53 ppm vitamin B12). Under the same conditions, 20 |lL of a mixture containing 10 ppm vitamin B, and B6 and 20 ppm P as vitamin Bl2 in 50:50 water:methanol was injected. The chromatograms obtained with the two detectors are shown in Figure 59. With the UV detector the three co-eluting peaks are not resolved. The elution sequence was vitamins B„ BI2, and B6by increasing order of retention. However, with the MIP AES detector, only the P-containing vitamin B,2 is observed. Thus, the high selectivity of the MIP AES detector is demonstrated. From the absorption bands shown for the three vitamins in Figure 60, it is clearly seen that selective detection o f vitamin Bl2 is not possible with UV-Vis detection. Unlike the atomic emission lines, the absorption bands are broad and not conducive for selective detection. However, for the MIP AES detector to be applicable for the analysis of real multivitamin tablets (typically a 500-mg tablet contains 100 |lg o f vitamin BI2), at least a 10-fold improvement in P detection limits is essential. With the current P detection limits, a large number o f tablets must be dissolved in small amounts of solvent for the resultant B,2 analyte concentration to be detectable. As an example, a solution must contain approximately 25% multivitamin tablets by weight for the phosphorous concentration from vitamin B,2 to be at the detection limit. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 130 35 B6 A ! \ 30 i \ £25 s Bi £ 20 B 121 h A i ' ! I 15 1 10 I 1 : ’■ ! ; ; i 5 i 0 ---------2 3 Time(min) 5000 ----------------------------------------------------------------- I 4000 1 I 3000 |! 2000 1 3 £* a i s. i.9 10 1000 .1000 i.fc — -------------------------------------------------------------------------------- 1 2 3 Time (min) b Figure 59. Chromatogram from a mixture of vitamin B, (10 ppm), vitamin B6(10 ppm), and vitamin B12(10 ppm P) using (a) UV-Vis detector and (b) MIP AES. Three co-eluting peaks are shown with the UV-Vis detection. With MIP AES, only P-containing vitamin B12is detected. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 131 0.75--------------- - - ---------- ---------- Absorbance (AU) VrtB1 VitB6 Vit B12 0 .5 - 0.25 — 0 250 Figure 60. 300 Wavelength (nm) 350 400 UV-Vis spectrum o f vitamins (250-400 nm) B„ B6, and B12. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 132 4.4.3 Detection o f Nucleotides Ion-pair chromatography is used to separate ionic compounds using a reversephase column. A counter-ion o f a charge opposite to that of the analyte is used in the mobile phase. The counter-ion is thought to associate with the analyte to fonn an ion pair. The counter-ion may contain a hydrophobic moiety which interacts with the hydrophobic stationary phase o f the column to enhance analyte retention. Ion-pair chromatographic methods are fast, reliable, and simple. The ion-pair reverse-phase mode is routinely used for the separation o f bases and acids, pharmaceuticals, amino acids, peptides, proteins, nucleic acid compounds, and for separations of chiral analytes.13* Combes et al.139successfully used ion-pair reversephase HPLC to separate many fundamental biological compounds such as nucleotides and nucleotide sugars. The nucleotides play a vital role in many biochemical reactions in prokaryotic and eukaryotic cells and are important as energy storage molecules. Both anion exchange and ion-pair chromatography have been used for the separation o f these compounds. In this section, the application o f the MIP AES detection for ion-pair chromatography is examined. The separation of cytidine S' monophosphate (CMP), uridine S' monophosphate (UMP), and guanosine S' monophosphate (GMP) is examined. The Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 133 molecular structures o f these compounds are shown in Figure 61. Pure samples o f these nucleotides were obtained from Sigma Chemical Co. (St. Louis, MO). Before attempting the separation, aqueous solutions o f the nucleotides were introduced to the plasma through direct solution nebulization and the P signal at 253.7 nm was observed. The P detection limits obtained were 20,34, and 47 ppb for CMP, UMP, and GMP respectively. For the LC separation, a solution of CMP, UMP, and GMP was prepared in water. The final solution contained 50 ppm P from each o f the aforementioned monophosphates. The mobile phase used was a 95:5 mixture of water and methanol with a flow rate o f 0.55 mL/inin. The pH o f the mobile phase was adjusted to 4.8 using 100-mM solutions o f CH3COOH and CH3COONa. Since the signal from P was monitored, commonly used phosphate buffers were avoided. Tetrabutylammonium hydrogen sulfate (TBAHS) (Aldrich Chemical Company, Inc., Milwaukee, WI) was used as the counter-ion. The concentration of TBAHS in the mobile phase was 8 mmol/L, about 5 times in excess o f the stoichiometric requirement. The tetrabutyl portion of TBAHS provided the hydrophobic interaction with the C „ column and the ammonium ion formed the ion pair with the anionic nucleotide. The separation is shown in Figure 62, with the UV detector set at 254 nm. Three well-separated peaks from CMP, UMP, and GMP were observed. The retention times for the analytes were 5.7,7.5, and 9.4 minutes for CMP, UMP, and GMP respectively. This separation was conducted with the MIP AES under the optimized Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. ONa L / \ vOH rOH c Figure 61. Molecular structures o f (a) cytidine S' monophosphate disodium salt, (b) uridine S' monophosphate in free acid form, and (c) guanosine S' monophosphate disodium salt. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. I I 0.0 Figure 62. I r " I ■ i ■ » i i i i i ■' i — i i i 1 i i i Tine (nm) 20.0 Chromatogram of a mixture of CMP, UMP, and GMP using the UV-Vis detector at 254 nm. Retention times for CMP, UMP, and GMP were 5.7,7.5, and 9.4 minutes, respectively. Mobile phase used was 95:5 MeOH:H20 at a flow rate o f 0.55 mL/min. pH of the mobile phase was 4.8. TBAHS was used as the counter-ion. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 136 conditions listed in Table 2. Phosphorus emission at 2S3.7 nm was monitored. However, no signals from the nucleotides were observed with the plasma detector. The plasma turned intense yellow due to the Na emissions from the CH3COONa in the mobile phase. As discussed in section 3.3.2, excess Na could have perturbed the plasma chemistry, and no signal was observed as a result. In future, different buffer systems and their compatibility with the MIP detection system must be investigated. 4.5 Summary Superior selectivity and sensitivity of the MIP AES over UV-Vis detection systems were demonstrated. The ability o f the plasma system to handle high molecular weight compounds such as DNA has also been shown. However, the inability of the plasma system to produce signal from the nucleotides in the presence o f the acetic acid/sodium acetate buffer is a concern. Systematic studies o f plasma performance in the presence o f different buffer systems warrants further investigation. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. CHAPTER 5 CONCLUSIONS AND FUTURE DIRECTIONS In this dissertation, characterization o f an MIP AES system for nonmetal selective detection and possible applications as a detector for reverse-phase liquid chromatography have been discussed. MIP AES with ultrasonic nebulization and membrane desolvation was successfully used for nonmetal (Cl, Br, I, S, and P) detection in organic analytes. Membrane desolvator temperature was successfully optimized for maximum nonmetal signal from semivolatile organic analytes. Linearization of the calibration plots was achieved through use of dilute H2S04 as a solvent modifier. The inability o f USN with a fixed-fiequency (1.4 MHz) automatic transducer to nebulize certain HPLC solvents (aqueous solutions of 10 -70% methanolrwater and acetonitrilerwater) was remedied by frequency optimization using a manual transducer controller. Coupling o f MIP AES in this configuration to a reverse-phase LC system was accomplished for separation o f various biologically active and pharmaceutically important mixtures. However, for LC applications, MIP AES detection limits must be significantly enhanced for it to compete with the already existing LC detectors. As discussed in Chapter 2, despite optimization of various plasma, USN, and Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 138 membrane desolvator conditions, the detection limits did not improve significantly. It appears that enhancement o f analyte throughput to the plasma using other types of nebulizers could affect the MIP AES sensitivity. Akinbo and Carnahan34 have done extensive research on analyte transport through USN-mebrane desolvator systems. The USN has a high solvent uptake rate (0.S -1 mL/min) and it transports 5 to 10% analyte into the plasma. At these flow rates the solvent effects in the plasma are significant. To minimize these effects, a membrane desolvator is necessary. The use of a membrane desolvator causes further loss of analyte and broadens chromatographic peaks. However, if a high-throughput microflow nebulizer (uptake rate 20-50 |iL/min)140were used, reduced solvent effects might obviate the need for a membrane desolvator. These nebulizers transport 50-60% of the total analyte. Hence, significant improvements in detection limits can be achieved. The MIP AES with low-flow nebulizers can be easily interfaced to micro-LC columns for separation and detection. For LC applications, compatibility of the MIP system with different buffer systems should also be assessed. As discussed in Chapter 4, the plasma system failed to produce signal from the nucleotide samples in the presence o f the acetic acid/sodium acetate buffer system. Also, the phosphate buffer could not be used for phosphorus selective detection. Alternative buffer systems more compatible with MIPs should be investigated to obtain the requisite pH for the separation. Finally, for simultaneous elemental analysis, a CCD array detector or a Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. 139 polychiomator should be used with the LC-MIP AES. Simultaneous elemental detection would provide a quicker means to examine multi-element analysis for empirical formula determinations and structure elucidation. Reproduced with permission of the copyright owner. Further reproduction prohibited without permission. REFERENCES 1. L. Ebdon, S. Hill, R. W. Ward, Analyst 111, 1113 (1986). 2. D. L. Haas and J. A. Caruso, Anal. Chem. 56,2014 (1984). 3. J. P. Matousek, B. J. Orr, M. Selby, Prog. Anal. At. Spectrosc. 7,275 (1984). 4. P. C. Uden, Chromatogr. Forum 1 ,17 (1986). 5. P. C. Uden, Trends Anal. Chem. 6,238 (1987). 6. K. Tanabe, H. Haraguchi, and K. Fuwa, Spectrochim. 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