In freshwater, there is more opportunity for silver (Ag) to interact with organic ligands than in seawater. Triclosan is an antibiotic agent which resembles thyroid hormone T3 and is finding its way into aquatic systems. Preliminary toxicology studies for the frogSCOPE program suggest that triclosan and nanosilver (nanoAg), also used as an antibiotic agent, may be chemically interacting, as they seem to synergistically increase the endocrine-disrupting abilities already observed independently in each chemical. Ag speciation methods can be used to determine if triclosan or thyroid hormone T3 are interacting with Ag ion (Ag+), which gets released over time by nanoAg. To fully utilize Ag speciation methods, however, total Ag in the sample must also be independently analyzed. Here we investigated a new total Ag analysis using cadmium sulfide quantum dots (CdS QDs) as fluorescence probes in solution. This method promises results in a fraction of the time of the established competitive ligand equilibration-solvent extraction (CLE-SE) technique utilizing PDC- and DDC- to bind Ag and bring it out of solution. Following this investigation were a series of experiments using CLE-SE for total Ag and Ag speciation in well water used to house bullfrog tadpoles in frogSCOPE Ag exposure studies. CLE-SE for Ag speciation was also applied to well water samples containing the two levels of nanoAg or Ag+ used in frogSCOPE Ag exposures, and used in ligand competition experiments to examine the potential of triclosan or T3 to act as strong Ag-binding ligands, as compared to glutathione and EDTA, two known Ag-binding ligands. The results of the latter experiments could be used to determine if either of these could be forming complexes with Ag which increase or decrease their delivery to amphibian cells. The fluorometric method using CdS QDs showed no ideal analytical response to nanomolar Ag+, even when commercial QDs were modified and used, so it could not be applied to our samples. Using CLE-SE for total Ag, the well water used as a base for toxicity studies in frogSCOPE contained Ag below the method detection limit of 5 pM. Using the speciation variation of the CLE-SE method, no evidence of naturally-occurring ligands which could produce extractable (hydrophobic) or non-extractable (hydrophilic) Ag complexes was found in this well water. EDTA and glutathione responded as model Ag-binding ligands to form non-extractable hydrophilic Ag complexes in fresh water. T3 behaved like these model ligands, while triclosan enhanced the extractability of Ag in the presence of certain concentrations of the added ligand, DDC-. In another set of experiments, coordination of Ag by triclosan or T3 was not detectable within that analytical window. These results suggest that ionic Ag released over time by nanoAg may be binding T3 and preventing it from reaching its receptor, but confirming the interaction of triclosan and Ag+ will require additional experiments using different analytical windows.

The continuous microreactor-assisted solution deposition (MASD) process was used for the deposition of CdS thin films on fluorine-doped tin oxide (FTO) glass. The MASD system, including a T-junction micromixer and a microchannel heat exchanger is capable of isolating the homogeneous particle precipitation from the heterogeneous surface reaction. The results show a dense nanocrystallite CdS thin films with a preferred orientation at (111) plane. Focused-ion-beam was used for TEM specimen preparation to characterize the interfacial microstructure of CdS and FTO layers. The band gap of the microreactor-assisted deposited CdS film was determined at 2.44 eV. X-ray Photon Spectroscopy show the bindings of energies of Cd 3d₃/₂, Cd 3d₅/₂, S 2p₃/₂ and S 2p₁/₂ at 411.7 eV, 404.8 eV, 162.1 eV, and 163.4 eV, respectively. The film growth kinetics was studied by measuring the film thickness deposited from 1 minute to 15 minutes in physical (FIB-TEM) and optical (reflectance spectroscopy) approaches. A growth model that accounts for the residence time in the microchannel using empirical factor (η) obtained from previous reported experimental data. Applying this factor in the proposed modified growth model gives a surface reaction rate of 1.61*10⁶ cm⁴ mole⁻¹s⁻¹, which is considerable higher than the surface reaction rates obtained from the batch CBD process. With the feature of separating homogeneous and heterogeneous surface reaction, the MASD process provides the capability to tailor the surface film growth rate and avoid the saturation growth regime in the batch process. An in situ spectroscopy technique was used to measure the UV-Vis absorption spectra of CdS nanoparticles formed within the continuous flow microreactor. The spectra were analyzed by fitting the sum of three Gaussian functions and one exponential function in order to calculate the nanoparticle size. This deconvolution analysis shows the formation of CdS nanoparticles range from 1.13 nm to 1.26 nm using a residence time from 0.26 s to 3.96 s. Barrier controlled coalescence mechanism seems to be a reasonable model to explain the experimental UV-Vis data obtained from the continuous flow microreactor, with a rate constant k' value of 2.872 s⁻¹. Using CFD, low skewness value of the RTD curve at high flow rate (short τ) suggests good radial mixing at high flow rate is responsible for the formation of smaller CdS nanoparticles with a narrower size distribution. The combination of CdS nanoparticle solution with MASD process resulted in the hindrance of CdS thin film deposition. It is hypothesized that the pre-existing sulfide (S²⁻) ions and CdS nanoparticles changes the chemical species equilibrium of thiourea hydrolysis reaction. Consequently, the lack of thiourea slows down the heterogeneous surface reaction. To test the scalability of the MASD process, a flow cell and reel-to-reel (R2R)-MASD system were setup and demonstrated for the deposition of CdS films on the FTO glass (6" x 6") substrate. The film deposition kinetics was found to be sensitive to the flow conditions within the heat exchanger and the substrate flow cell. The growth kinetics of the CdS films deposited by R2R-MASD process was investigated by with a deposition time of 2.5 min, 6.3 min, and 9 min. In comparison with the continuous MASD process, the growth rate in R2R-MASD is higher, however more difficult to obtain a linear relationship with the deposition time. / Graduation date: 2012 / Access restricted to the OSU Community at author's request from Jan. 13, 2012 - Jan. 13, 2013

Im Rahmen der vorliegenden Arbeit wurden Metallchalkogenid-Nanopartikel bzw. Quantum Dots größenselektiv mittels kontinuierlicher MicroJet-Reaktor-Technologie in wässrigem Medium erzeugt. Aufgrund der sehr kurzen Mischzeiten im µs- bis ms-Bereich können Keimbildung und -wachstum im MicroJet-Reaktor zeitlich voneinander separiert werden. Die Begrenzung des Partikelwachstum durch den Einsatz von Stabilisatoren oder geringer Präkursorkonzentrationen ermöglichten die Synthese von monodispersen, nanokristallinen Produkten mit sehr schmaler Partikelgrößenverteilung. Ausgehend von den wasserlöslichen Präkursoren Cadmiumnitrat und Natriumsulfid wurde sowohl eine Synthesestrategie für elektrostatisch- als auch Liganden-stabilisierte CdS-Nanopartikel entwickelt. Es wurden zahlreiche Reaktionsparameter wie Temperatur, Präkursorverhältnis, Konzentration oder Fällungsmittel variiert und der Einfluss auf die Partikelgröße überprüft. In weiteren Untersuchungen konnte die Übertragbarkeit der MicroJet-Reaktor-Synthese auf die Metallchalkogenide Cadmiumzinksulfid, Silbersulfid und Silberindiumsulfid validiert werden. Auch komplexere Systeme wie Core/Shell Partikel sind mittels postsynthetischer Beschichtung der im MicroJet-Reaktor hergestellten Nanopartikel möglich. Erste Experimente zur Synthese von CdSe bestätigten die Eignung des kontinuierlichen Verfahrens zur Fällung höherer Chalkogenide.:1 Einleitung 1 1.1 Halbleiternanopartikel 3 1.1.1 Bandstruktur des Festkörpers 3 1.1.2 Interbandübergänge in direkten und indirekten Halbleitern 7 1.1.3 Quantum Confinement 15 1.2 Fällung von Nanopartikeln im MicroJet-Reaktor 20 1.2.1 Partikelbildung durch Kristallisation 20 1.2.2 Funktionsprinzip des MicroJet-Reaktors 22 1.2.3 State of the Art 25 1.3 Nanoskalige Metallchalkogenide 29 1.3.1 Cadmiumchalkogenide 29 1.3.2 Near-Infrared Quantum Dots 31 1.3.3 Core/Shell-Partikel 34 1.4 Zielsetzung 37 2 Ergebnisse und Diskussion 39 2.1 Allgemeines 39 2.2 Cadmiumchalkogenide 47 2.2.1 Hydrothermalsynthese von CdS im Laborautoklaven 47 2.2.1.1 Wiederholbarkeit 48 2.2.1.2 Einfluss des Präkursorverhältnis 50 2.2.1.3 Versuchsplanung zur Untersuchung ausgewählter Reaktionsparameter 51 2.2.1.4 Effektberechnung zur Untersuchung ausgewählter Einflussfaktoren 54 2.2.1.5 Beobachtungen und Charakterisierung 56 2.2.2 Kontinuierliche Synthese von CdS im MicroJet-Reaktor 62 2.2.2.1 MJR-Synthese von CdS aus Cd(NO3)2 und Na2S 62 2.2.2.2 MJR-Synthese von CdS aus Cd(NO3)2 und Thioacetamid 71 2.2.3 CdS/ZnS Core/Shell und Cd1-xZnxS Quantum Dots 76 2.2.3.1 CdS/ZnS Core/Shell Quantum Dots 77 2.2.3.2 Cd1-xZnxS Quantum Dots 88 2.2.4 Hydrothermalsynthese von CdSe im Laborautoklaven 99 2.2.4.1 Wiederholbarkeit 99 2.2.4.2 Präkursorverhältnis Cd2+:Se2- 101 2.2.4.3 Versuchsplanung zur Untersuchung ausgewählter Reaktionsparameter 104 2.2.4.4 Effektberechnung zur Untersuchung ausgewählter Einflussfaktoren 108 2.2.4.5 Beobachtungen und Charakterisierung 111 2.2.5 Kontinuierliche Synthese von CdSe im MicroJet-Reaktor 116 2.3 Near-Infrared Quantum Dots 121 2.3.1 Kontinuierliche Synthese von AgS2 im MJR-Reaktor 121 2.3.1.1 Elektrostatisch stabilisierte Ag2S Quantum Dots 121 2.3.1.2 Ag2S/ZnS Core/Shell Quantum Dots 138 2.3.1.3 Ligandenstabilisierte Ag2S Quantum Dots 143 2.3.2 Kontinuierliche Synthese von Indiumsilbersulfid im MJR-Reaktor 152 3 Experimenteller Teil 165 3.1 Synthesen 165 3.1.1 Verwendete Chemikalien 165 3.1.2 Hydrothermalsynthese im Laborautoklaven 166 3.1.2.1 Versuchsaufbau 166 3.1.2.2 Cadmiumsulfid 167 3.1.2.3 Cadmiumselenid 168 3.1.2.4 Silbersulfid 169 3.1.3 Kontinuierliche Synthese im MicroJet-Reaktor 169 3.1.3.1 Versuchsaufbau und Durchführung der MicroJet-Reaktor-Synthese 169 3.1.3.2 Synthese Liganden-stabilisierter Metallsulfide 171 3.1.3.3 Synthese elektrostatisch stabilisierter Metallsulfide 171 3.1.3.4 Synthese von Cadmiumselenid 172 3.1.3.5 Synthese von Core-Shell-Partikeln 172 3.2 Analytische Methoden 173 3.2.1 Dynamische Lichtstreuung (DLS) 173 3.2.2 Statische Lichtstreuung (SLS) 173 3.2.3 UV/Vis-Absorptionsspektroskopie 173 3.2.4 Photolumineszenz (PL)-Spektroskopie 174 3.2.5 Transmissionselektronenmikroskopie (TEM) 174 3.2.6 Rasterelektronenmikroskopie (REM) 175 3.2.7 Optische Emissionsspektroskopie mit induktiv gekoppeltem Plasma (ICP-OES) 175 3.2.8 Röntgenfluoreszenzanalyse (RFA) 176 3.2.9 Pulver-Röntgendiffraktometrie (PXRD) 176 3.2.10 RAMAN-Spektroskopie 177 3.2.11 Abgeschwächte Totalreflexions-Infrarotspektroskopie (ATR-FTIR) 177 4 Zusammenfassung und Ausblick 179 5 Literatur 182 6 Anhang 195 / In the present work, metal chalcogenide nanoparticles or Quantum Dots were obtained size-selectively using continuous MicroJet Reactor technology. Due to the short mixing times in the µs to ms range, crystallite nucleation and crystal growth are well separated and enable concentration-limited particle growth. Alternatively, particle growth can be limited by stabilizers. Starting from the water-soluble precursors Cd(NO3)2 and Na2S, a synthesis strategy for both electrostatic and ligand stabilized CdS nanoparticles in aqueous medium was developed. The nanocrystalline products obtained were characterized by a narrow, monodisperse particle size distribution. Examining the influence of the particle size, numerous reaction parameters e. g. temperature, ratio of precursors, concentration or precipitant were varied. In further investigations, the transferability of the MicroJet Reactor synthesis to the metal chalcogenides (Cd,Zn)S, Ag2S and AgInS2 was validated. By means of post-synthetic coating of the nanoparticles produced in the MicroJet Reactor, more complex systems such as CdS/ZnS or Ag2S/ZnS core/shell particles are accessible. Initial experiments on the synthesis of CdSe confirmed the suitability of the continuous process for precipitation of selenides.:1 Einleitung 1 1.1 Halbleiternanopartikel 3 1.1.1 Bandstruktur des Festkörpers 3 1.1.2 Interbandübergänge in direkten und indirekten Halbleitern 7 1.1.3 Quantum Confinement 15 1.2 Fällung von Nanopartikeln im MicroJet-Reaktor 20 1.2.1 Partikelbildung durch Kristallisation 20 1.2.2 Funktionsprinzip des MicroJet-Reaktors 22 1.2.3 State of the Art 25 1.3 Nanoskalige Metallchalkogenide 29 1.3.1 Cadmiumchalkogenide 29 1.3.2 Near-Infrared Quantum Dots 31 1.3.3 Core/Shell-Partikel 34 1.4 Zielsetzung 37 2 Ergebnisse und Diskussion 39 2.1 Allgemeines 39 2.2 Cadmiumchalkogenide 47 2.2.1 Hydrothermalsynthese von CdS im Laborautoklaven 47 2.2.1.1 Wiederholbarkeit 48 2.2.1.2 Einfluss des Präkursorverhältnis 50 2.2.1.3 Versuchsplanung zur Untersuchung ausgewählter Reaktionsparameter 51 2.2.1.4 Effektberechnung zur Untersuchung ausgewählter Einflussfaktoren 54 2.2.1.5 Beobachtungen und Charakterisierung 56 2.2.2 Kontinuierliche Synthese von CdS im MicroJet-Reaktor 62 2.2.2.1 MJR-Synthese von CdS aus Cd(NO3)2 und Na2S 62 2.2.2.2 MJR-Synthese von CdS aus Cd(NO3)2 und Thioacetamid 71 2.2.3 CdS/ZnS Core/Shell und Cd1-xZnxS Quantum Dots 76 2.2.3.1 CdS/ZnS Core/Shell Quantum Dots 77 2.2.3.2 Cd1-xZnxS Quantum Dots 88 2.2.4 Hydrothermalsynthese von CdSe im Laborautoklaven 99 2.2.4.1 Wiederholbarkeit 99 2.2.4.2 Präkursorverhältnis Cd2+:Se2- 101 2.2.4.3 Versuchsplanung zur Untersuchung ausgewählter Reaktionsparameter 104 2.2.4.4 Effektberechnung zur Untersuchung ausgewählter Einflussfaktoren 108 2.2.4.5 Beobachtungen und Charakterisierung 111 2.2.5 Kontinuierliche Synthese von CdSe im MicroJet-Reaktor 116 2.3 Near-Infrared Quantum Dots 121 2.3.1 Kontinuierliche Synthese von AgS2 im MJR-Reaktor 121 2.3.1.1 Elektrostatisch stabilisierte Ag2S Quantum Dots 121 2.3.1.2 Ag2S/ZnS Core/Shell Quantum Dots 138 2.3.1.3 Ligandenstabilisierte Ag2S Quantum Dots 143 2.3.2 Kontinuierliche Synthese von Indiumsilbersulfid im MJR-Reaktor 152 3 Experimenteller Teil 165 3.1 Synthesen 165 3.1.1 Verwendete Chemikalien 165 3.1.2 Hydrothermalsynthese im Laborautoklaven 166 3.1.2.1 Versuchsaufbau 166 3.1.2.2 Cadmiumsulfid 167 3.1.2.3 Cadmiumselenid 168 3.1.2.4 Silbersulfid 169 3.1.3 Kontinuierliche Synthese im MicroJet-Reaktor 169 3.1.3.1 Versuchsaufbau und Durchführung der MicroJet-Reaktor-Synthese 169 3.1.3.2 Synthese Liganden-stabilisierter Metallsulfide 171 3.1.3.3 Synthese elektrostatisch stabilisierter Metallsulfide 171 3.1.3.4 Synthese von Cadmiumselenid 172 3.1.3.5 Synthese von Core-Shell-Partikeln 172 3.2 Analytische Methoden 173 3.2.1 Dynamische Lichtstreuung (DLS) 173 3.2.2 Statische Lichtstreuung (SLS) 173 3.2.3 UV/Vis-Absorptionsspektroskopie 173 3.2.4 Photolumineszenz (PL)-Spektroskopie 174 3.2.5 Transmissionselektronenmikroskopie (TEM) 174 3.2.6 Rasterelektronenmikroskopie (REM) 175 3.2.7 Optische Emissionsspektroskopie mit induktiv gekoppeltem Plasma (ICP-OES) 175 3.2.8 Röntgenfluoreszenzanalyse (RFA) 176 3.2.9 Pulver-Röntgendiffraktometrie (PXRD) 176 3.2.10 RAMAN-Spektroskopie 177 3.2.11 Abgeschwächte Totalreflexions-Infrarotspektroskopie (ATR-FTIR) 177 4 Zusammenfassung und Ausblick 179 5 Literatur 182 6 Anhang 195