Determination of Elemental Selenium Production by a Facultative Anaerobe Grown Under Sequential Anaerobic/Aerobic Conditions Suminda Hapuarachchi, Jerry Swearingen, Jr, and Thomas G. Chasteen Department of Chemistry Sam Houston State University What happens to toxic metalloids bioprocessed by metalloid-resistant bacteria? What happens to toxic metalloids bioprocessed by metalloid-resistant bacteria? Soluble forms remain in solution. What happens to toxic metalloids bioprocessed by metalloid-resistant bacteria? Soluble forms remain in solution. Bioreduction also produces methylated, volatile forms. What happens to toxic metalloids bioprocessed by metalloid-resistant bacteria? Soluble forms remain in solution. Bioreduction also produces methylated, volatile forms. Metalloids are converted to elemental (solid) form. Phototropic Bacteria 0 Se and 0 Te from Strict Anaerobes Headspace yield from 6 phototrophs •dimethyl sulfide •dimethyl selenide •dimethyl diselenide (also dimethyl selenenyl sulfide) The fluorine-induced chemiluminescence GC chromatogram of the headspace above Se-resistant bacteria. Amended with SeO32- Dimethyl telluride production by Pseudomonas fluorescens K27 Amended with TeO32- DMTe Trimethyl stibine Dimethyl disulfide Dimethyl trisulfide (CH3)3Sb production by K27 amended with an inorganic-Sb salt Amended with KSb(OH)6 Methanethiol Dimethyl sulfide Can a mass balance be determined for metalloids distributed among solid, liquid, and gas phases in bacterial cultures? Use 3 L batch cultures amended with Se oxyanions. Incubate culture far into the stationary phases. Determine metalloid content in each phase. 3 L bioreactor • Temperature controlled QuickTime™ and a None decompressor are needed to see this picture. 3 L bioreactor • Temperature controlled • pH control additions acid QuickTime™ and a None decompressor are needed to see this picture. base 3 L bioreactor • Temperature controlled • pH control • Dissolved Oxygen gas N2/O2 purge QuickTime™ and a None decompressor are needed to see this picture. D.O.probe 3 L bioreactor • Temperature controlled • pH control • Dissolved Oxygen • Nutrient addition QuickTime™ and a None decompressor are needed to see this picture. 3 L bioreactor • Temperature controlled • pH control • Dissolved Oxygen • Nutrient addition QuickTime™ and a None decompressor are needed to see this picture. • Gas harvest bubbler(s) 3 L bioreactor • Temperature controlled • pH control • Dissolved Oxygen • Nutrient addition QuickTime™ and a None decompressor are needed to see this picture. • Gas harvest • Liquid harvest Bacterial Culture Conditions Bacterial Culture Conditions Pseudomonas fluorescens K27 Isolated by Ray Fall at CU Boulder Facultative anaerobe (grows with or without oxygen) Grown on tryptic soy broth with 3% nitrate added Bacterial Culture Conditions Pseudomonas fluorescens K27 Isolated by Ray Fall at CU Boulder Facultative anaerobe (grows with or without oxygen) Grown on tryptic soy broth with 3% nitrate added Selenium Amendments 1–10 mM SeO42- or SeO32- along with 10%/vol. inoculum Bacterial Culture Conditions Pseudomonas fluorescens K27 Isolated by Ray Fall at CU Boulder Facultative anaerobe (grows with or without oxygen) Grown on tryptic soy broth with 3% nitrate added Selenium Amendments 1–10 mM SeO42- or SeO32- along with 10%/vol. inoculum Tellurium Amendments 0.01 to 1 mM TeO42- or TeO32- along with 10%/vol. inoculum Bacterial Culture Conditions Pseudomonas fluorescens K27 Isolated by Ray Fall at CU Boulder Facultative anaerobe (grows with or without oxygen) Grown on tryptic soy broth with 3% nitrate added Selenium Amendments 1–10 mM SeO42- or SeO32- along with 10%/vol. inoculum Tellurium Amendments 0.01 to 1 mM TeO42- or TeO32- along with 10%/vol. inoculum Batch cultures at 30˚C 15 hr to 72 hr bacterial cultures; ~ 3 L liquid volume Se Determination Liquid phase selenium Inductively coupled plasma spectrometry (ICP) Se Determination Liquid phase selenium Inductively coupled plasma spectrometry (ICP) Solid phase selenium (Se0 and cells) ICP following centrifugation and dissolution with HNO3 Se Determination Liquid phase selenium Inductively coupled plasma spectrometry (ICP) Solid phase selenium (Se0 and cells) ICP following centrifugation and dissolution with HNO3 Gas phase selenium (volatile organo-Se compounds) Species identified via GC/fluorine-induced chemiluminescence Trapping in serial HNO3 bubblers Analysis via ICP Simultaneous ICP ICP Analysis Te Determination Liquid phase tellurium Hydride generation atomic absorption spectrometry (HGAAS) Te Determination Liquid phase tellurium Hydride generation atomic absorption spectrometry (HGAAS) Solid phase tellurium (Te0 and cells) HGAAS following centrifugation and dissolution with HNO3 Te Determination Liquid phase tellurium Hydride generation atomic absorption spectrometry (HGAAS) Solid phase tellurium (Te0 and cells) HGAAS following centrifugation and dissolution with HNO3 Gas phase tellurium Capillary gas chromatography/F2-induced chemiluminescence Hydride Generation AAS Movie not available Te Amendments Distribution of Te among supernatant and collected solids in four duplicate bioreactor runs Run Distribution between solid/liq uid Solid phase Te Solution phase Te S.D. (n=4 aliquots from each r un) 1 2 3 4 Averag e (4 runs) 42 18 33 43 34% 58 82 67 57 66% % Recovery of added Te 6.5 1.1 18.1 5.4 7.8% 107 84 111 87 97% Anaerobic cultures of Pseudomonas fluorescens K27 were amended with 0.1 mM sodium tellurite, maintained at 30°C for 92 h, and then 1) spun-down cells and solids and 2) liquid medium were analyzed for tellurium by HGAAS. Four samples harvested at the same time from each run were analyzed. Se Amendments Gas trapping efficiencies Run 1 2 3 Averag e Trap-1 Se µg 276.21 271.32 291.04 279.52 Trap-2 Se µg 25.58 23.84 24.74 24.72 Trap-3 Se µg 22.28 22.56 19.95 21.60 Total Se µg 324.07 317.72 335.73 325.84 % Recovery 102.6 100.6 106.3 103.17 Se % recovery observed for 50% HNO3 trapping solution, followed by ICP analysis. Se added as dimethyl diselenide to Trap-1 then purged continuously for 24 h with N2, 50 mL/min. Mass Balance of anaerobic, Se-amended bioreactors 1 mM of SeO32- (n=5 runs ) Phase % Recovery (± SD) Liqu id 66.68 (±18.29) Soli d 32.44 (±19.81) Gas 0.04 (±0.07) Total Recove ry 99.16% (±0.62) Phase Liqu id Soli d Gas 10 mM of SeO32- (n=3) % Recovery 92.17 (±8.13) 6.90 (±1.32) 0.004 (±0.002) Total Recove ry 99.071 (±8.07) Phase Liqu id Soli d Gas 10 mM of SeO42- (n=3) % Recovery 95.07 (±6.98) 0.73 (±0.06) 0.001 (±0.001) Total Recove ry 95.80 ( ±6.93) Strictly anaerobic (but N2 purged) 72 hour batch experiments with P. fluorescens Does shifting between aerobic/anaerobic growth effect Se0 production for K27? Does shifting between aerobic/anaerobic growth effect Se0 production for K27? Alternate between anaerobic and aerobic growth. Does shifting between aerobic/anaerobic growth effect Se0 production for K27? Alternate between anaerobic and aerobic growth. Alternate N2 with air purging over relatively long times. Does shifting between aerobic/anaerobic growth effect Se0 production for K27? Alternate between anaerobic and aerobic growth. Alternate N2 with air purging over relatively long times. Compare Se0 yield between anaerobic and aerobic runs. Alternating anaerobic/aerobic purge cycles experiments with P. fluorescens Phase Liqu id Soli d Gas 1 mM of SeO32- (n=3 ) 16 h N2 /8 h air@ 50 mL/mi n % Recovery (± SD) 52.31 (±4.43) 37.58 (±7.99) 0.04 (±0.07) Total Recove ry 89 .89% (±11.22) Phase Liqu id Soli d Gas 10 mM of SeO32- (n=3) 12 h N2/6 h air @50 mL/mi n % Recovery 83.05 (± 3.04) 8.53 (±1.90) 0.002 (±0.001) Total Recove ry 91 .58 (±4.43) Phase Liqu id Soli d Gas 1 mM of SeO32- (n= 3) 12 h N2/6 h air @ 50 mL/mi n % Recovery 59.47(±19.65) 32.99(±18.71) 0.011(±0.014) Total Recove ry 92 .50 (±0.99) Phase Liqu id Soli d Gas 1 mM of SeO32- (n= 3) 12 h N 2/6 h air @ 250 mL/min % Recovery 45.759 (±10.80) 43.152 (±10.86) NA due to air purge rate Total Recove ry 88 .91 (±4.37) Comparison of strictly anaerobic to mixed anaerobic/aerobic conditions 1 mM of SeO32- (n=5 runs ) Phase % Recovery (± SD) Liqu id 66.68 (±18.29) Soli d 32.44 (±19.81) Gas 0.04 (±0.07) Total Recove ry 99.16% (±0.62) Phase Liqu id Soli d Gas 10 mM of SeO32- (n=3) % Recovery 92.17 (±8.13) 6.90 (±1.32) 0.004 (±0.002) Total Recove ry 99.071 (±8.07) Phase Liqu id Soli d Gas 10 mM of SeO42- (n=3) % Recovery 95.07 (±6.98) 0.73 (±0.06) 0.001 (±0.001) Total Recove ry 95.80 ( ±6.93) 1 mM of SeO32- (n=3 ) air 50 mL/mi n Phase % Recovery (± SD) Liqu id 52.31 (±4.43) Soli d 37.58 (±7.99) Gas 0.04 (±0.07) Total Recove ry 89 .89% (±11.22) 10 mM of SeO32- (n=3) air 50 mL/mi n Phase % Recovery Liqu id 83.05 (± 3.04) Soli d 8.53 (±1.90) Gas 0.002 (±0.001) Total Recove ry 91 .58 (±4.43) 1 mM of SeO32- (n= 3) air 50 mL/mi n Phase % Recovery Liqu id 59.47(±19.65) Soli d 32.99(±18.71) Gas 0.011(±0.014) Total Recove ry 92 .50 (±0.99) 1 mM of SeO32- (n= 3) air 250 mL/m in Phase % Recovery Liqu id 45.759 (±10.80) Soli d 43.152 (±10.86) Gas NA due to air purge rate Total Recove ry 88 .91 (±4.37) Alternating anaerobic/aerobic cycling in a 1 mM selenite amended culture of P. fluorescens K27. The alternating cycles were 12 h N2 then 6 h air purging at 50 mL. Alternating anaerobic/aerobic cycling in a 1 mM selenite-amended culture of P. fluorescens K27. The alternating cycles were 12 h N2 then 6 h air purging at 250 mL. 72-hour Anaerobic Experiment 1 mM selenite amendment Pseudomonas fluorescens K27 tryptic soy broth (with 3% nitrate), 30°C QuickTime Time Lapse Movie Movie not available QuickTime™ and a None decompressor are needed to see this picture. QuickTime™ and a None decompressor are needed to see this picture. QuickTime™ and a None decompressor are needed to see this picture. Acknowledgements • Suminda Hapuarachchi and Jerry Swearingen Jr. • Verena Van Fleet-Stalder • Hakan Gürleyük, Rui Yu, Mehmet Akpolat • • • • Robert A. Welch Foundation SHSU Faculty Enhancement Grants Ruth Hathaway/ACS Environmental Division Richard Courtney “Cajun Support” • Dr. John W. Birks above and beyond everyone else Thank you John for 16 years of friendship, support, and love.