TY - CONF A1 - Adolphs, Jürgen A1 - Rübner, Katrin A1 - Schnell, A. A1 - Prinz, Carsten A1 - Peplinski, Burkhard A1 - Hempel, S. ED - Ludwig, H.-M. T1 - Porenstruktur hydrothermal erhärteter Granulate aus Mauerwerkbruch N2 - Die Herstellung hydrothermal erhärteter Granulate ist eine Möglichkeit zur Wiederverwertung von ziegelhaltigem Mauerwerkbruch, der derzeit aufgrund der heterogenen Zusammensetzung und hoher Feinanteile ein besonders hohes Verwertungsdefizit aufweist. Dabei ist die hydrothermale Erhärtung in einem Autoklav bei 200 °C und 1.6 MPa in gesättigter Wasserdampfatmosphäre eine Alternative mit geringerem Energieverbrauch im Vergleich zur thermischen Herstellung von Leichtgranulaten aus mineralischen Abfällen (Blähgranulate) oder Tonen und Schiefer (kommerzieller Blähton bzw. Blähschiefer), die bei Temperaturen von 1200-1300 °C im Drehrohrofen erfolgt. Die Festigkeit der Hydrothermalgranulate entwickelt sich bei diesem Prozess durch die Ausbildung von Calciumsilicathydrat-Phasen (CSH), die durch die Reaktion zwischen Quarzpartikeln und hydratisiertem Kalk entstehen. Die so erzeugten Hydrothermalgranulate haben Rohdichten zwischen 1500 kg/m3 und 2000 kg/m3. Damit und auch durch andere Eigenschaften unterscheiden sie sich von den thermisch erhärteten Blähgranulaten bzw. Blähtonen. Ursache dafür ist letztendlich eine sehr unterschiedliche Gefüge- und Porenstruktur. Im vorliegenden Beitrag wird hauptsächlich über die Ergebnisse der Mikrostrukturuntersuchungen an Hydrothermalgranulaten zusammen mit ihren technologischen Eigenschaften, wie Kornfestigkeit, Rohdichte und Wasseraufnahme, berichtet. T2 - 19. Ibausil - Internationale Baustofftagung CY - Weimar, Germany DA - 16.09.2015 KW - Leichtgranulat KW - Mauerwerkbruch KW - Hydrothermale Herstellung KW - Mikrostruktur KW - Porenstruktur PY - 2015 SN - 978-3-00-050225-5 VL - 2 SP - 2-291 EP - 2-298 AN - OPUS4-34878 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - GEN A1 - Adam, Christian A1 - Peplinski, Burkhard A1 - Kley, Gerd A1 - Simon, Franz-Georg ED - Hilty, L. M. T1 - Thermo-chemical treatment of sewage sludge ashes aiming at marketable P-fertiliser products T2 - R'07 World Congress "Recovery of Materials and Energy for Resource Efficiency" CY - Davos, Switzerland DA - 2007-09-03 KW - P-recovery KW - Sewage sludge KW - Thermo-chemical treatment KW - Mineral phases KW - XRD PY - 2007 SN - 978-3-905594-49-2 SP - 14/1 EP - 14/7 PB - EMPA CY - Davos AN - OPUS4-16469 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Adam, Christian A1 - Peplinski, Burkhard A1 - Michaelis, Matthias A1 - Kley, Gerd A1 - Simon, Franz-Georg T1 - Thermochemical treatment of sewage sludge ashes for phosphorus recovery N2 - Phosphorus (P) is an essential element for all living organisms and cannot be replaced. Municipal sewage sludge is a carrier of phosphorus, but also contains organic pollutants and heavy metals. A two-step thermal treatment is suggested, including mono-incineration of sewage sludge and subsequent thermochemical treatment of the ashes. Organic pollutants are completely destroyed by mono-incineration. The resulting sewage sludge ashes contain P, but also heavy metals. P in the ashes exhibits low bioavailability, a disadvantage in farming. Therefore, in a second thermochemical step, P is transferred into mineral phases available for plants, and heavy metals are removed as well. The thermochemical treatment was investigated in a laboratory-scale rotary furnace by treating seven different sewage sludge ashes under systematic variation of operational parameters. Heavy metal removal and the increase of the P-bioavailability were the focus of the investigation. The present experimental study shows that these objectives have been achieved with the proposed process. The P-bioavailability was significantly increased due to the formation of new mineral phases such as chlorapatite, farringtonite and stanfieldite during thermochemical treatment. KW - P-recovery KW - Sewage sludge ash KW - Thermochemical treatment KW - Mineral phases KW - X-ray diffraction PY - 2009 DO - https://doi.org/10.1016/j.wasman.2008.09.011 SN - 0956-053X VL - 29 IS - 3 SP - 1122 EP - 1128 PB - Pergamon Press CY - New York, NY AN - OPUS4-18605 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Adam, Christian A1 - Peplinski, Burkhard A1 - Kley, Gerd A1 - Kratz, S. A1 - Schick, J. A1 - Schnug, E. T1 - Phosphorrückgewinnung aus Klärschlammaschen - Ergebnisse aus dem EU-Projekt SUSAN N2 - Phosphor ist ein für alle Lebewesen essenzielles Element und kann in seinen Funktionen z. B. als Bestandteil der DNS und RNS sowie als Schlüsselelement beim Energiestoffwechsel (ADP/ATP) nicht ersetzt werden. Klärschlammaschen sind aufgrund ihrer hohen Gehalte an Phosphor (15–25 % P2O5) geeignete Sekundärrohstoffe für die Herstellung von P-Düngemitteln. Aufgrund der schlechten Pflanzenverfügbarkeit des Phosphors und der Gehalte an umweltrelevanten Schwermetallen sollten diese allerdings nicht direkt in der Landwirtschaft eingesetzt werden. Im Mittelpunkt des EU-Projekts SUSAN steht die Entwicklung und Optimierung einer thermochemischen Behandlung von Klärschlammaschen, mit der die Düngewirkung der Aschen auf das Niveau konventioneller Mineraldünger (Thomaskali und Superphosphat SSP) angehoben wird und die Schwermetallkonzentrationen unter die Grenzwerte nach Düngemittelverordnungen europäischer Länder abgesenkt werden. Die sehr positiven Ergebnisse, die bisher im SUSAN-Projekt erzielt wurden, und die darauf basierenden ökonomischen Betrachtungen legen eine großtechnische Umsetzung des Verfahrens nahe. KW - Klärschlamm KW - Phosphor KW - Ressource KW - Klärschlammasche KW - P-Düngemittel KW - Mineralische Phasen PY - 2008 DO - https://doi.org/10.1007/s00506-008-0152-3 SN - 0945-358X SN - 1613-7566 VL - 60 IS - 3-4 SP - 55 EP - 64 PB - Springer CY - Wien AN - OPUS4-17449 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Vogel, Christian A1 - Adam, Christian A1 - Peplinski, Burkhard A1 - Wellendorf, Stephan T1 - Chemical reactions during the preparation of P and NPK fertilizers from thermochemically treated sewage sludge ashes KW - NPK fertilizer KW - P fertilizer KW - Phosphorus recycling KW - Sewage sludge ash KW - Urban mining PY - 2010 DO - https://doi.org/10.1111/j.1747-0765.2010.00485.x SN - 0038-0768 SN - 1747-0765 VL - 56 IS - 4 SP - 627 EP - 635 PB - Blackwell Publ. Asia CY - Tokyo, Japan AN - OPUS4-21924 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Donėlienė, J. A1 - Rudzikas, M. A1 - Rades, Steffi A1 - Dörfel, Ilona A1 - Peplinski, Burkhard A1 - Sahre, Mario A1 - Pellegrino, F. A1 - Maurino, V. A1 - Ulbikas, J. A1 - Galdikas, A. A1 - Hodoroaba, Vasile-Dan T1 - Electron Microscopy and X-Ray Diffraction Analysis of Titanium Oxide Nanoparticles Synthesized by Pulsed Laser Ablation in Liquid N2 - A femto-second pulsed laser ablation in liquid (PLAL) procedure for the generation of titanium oxide nanoparticles (NP) is reported with the purpose of understanding morphology and structure of the newly generated NPs. Ablation duration was varied for optimization of NP generation processes between 10 and 90 min. Surface morphology of NPs as well as their size and shape (distribution) were analysed by various complementary electron microscopy techniques, i.e. SEM, TSEM and TEM. The crystalline structure of titanium oxide particles was investigated by XRD(two instruments operated in different geometries) and HR-TEM. Concentration of generated titanium oxide NPs in liquid was analysed by ICP-MS. A mix of crystalline (mainly anatase), partly crystalline and amorphous spherical titanium oxide NPs can be reported having a mean size between 10 and 20 nm, which is rather independent of the laser ablation (LA) duration. A second component consisting of irregularly shaped, but crystalline titanium oxide nanostructures is co-generated in the LA water, with more pronounced occurrence at longer LA times. The provenance of this component is assigned to those spherical particles generated in suspension and passing through the converging laser beam, being hence subject to secondary irradiation effects, e. g. fragmentation. KW - Laser ablation in liquid KW - Nanoparticles KW - Titanium oxide KW - Particle morphology PY - 2018 UR - https://www.cambridge.org/core/journals/microscopy-and-microanalysis/article/electron-microscopy-and-xray-diffraction-analysis-of-titanium-oxide-nanoparticles-synthesized-by-pulsed-laser-ablation-in-liquid/AE368446FAC70E08C514F9AEABFD131B DO - https://doi.org/10.1017/S1431927618009030 VL - 24 IS - S1 (August) SP - 1710 EP - 1711 PB - Cambridge University Press CY - New York, NY, U.S.A. AN - OPUS4-45949 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Donėlienė, J. A1 - Rudzikas, M. A1 - Rades, Steffi A1 - Dörfel, Ilona A1 - Peplinski, Burkhard A1 - Sahre, Mario A1 - Pellegrino, F. A1 - Maurino, V. A1 - Ulbikas, J. A1 - Galdikas, A. A1 - Hodoroaba, Vasile-Dan T1 - Morphology and structure of TixOy nanoparticles generated by femtosecond laser ablation in water N2 - In this work femto-second pulsed laser ablation in liquid (PLAL) procedure for the generation of titanium oxide nanoparticles (NP) is reported with the purpose of understanding morphology and structure of the newly generated NPs. Ablation duration was varied for optimization of NP generation processes between 10 and 90 min. Surface morphology of NPs as well as their size and shape (distribution) were analysed by various complementary electron microscopy techniques, i.e. SEM, TSEM and TEM. The crystalline structure of titanium oxide particles was investigated byXRD(two instruments operated in different geometries) and HR-TEM. Concentration of generated titanium oxide NPs in liquid was analysed by ICP-MS. A mix of crystalline (mainly anatase), partly crystalline and amorphous spherical titanium oxide NPs can be reported having a mean size between 10 and 20 nm, which is rather independent of the laser ablation (LA) duration. A second component consisting of irregularly shaped, but crystalline titanium oxide nanostructures is co-generated in the LA water, with more pronounced occurrence at longer LA times. The provenance of this component is assigned to those spherical particles generated in suspension and passing through the converging laser beam, being hence subject to secondary irradiation effects, e. g. fragmentation. KW - Titanium oxide KW - Nanoparticles KW - Laser ablation in liquid KW - Particle morphology KW - Nanoparticle structure PY - 2018 DO - https://doi.org/10.1088/2053-1591/aaba56 SN - 2053-1591 VL - 5 IS - 4 SP - 045015-1 EP - 045015-12 PB - IOP Publishing CY - London, UK AN - OPUS4-44678 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Petzet, S. A1 - Peplinski, Burkhard A1 - Cornel, P. T1 - On wet chemical phosphorus recovery from sewage sludge ash by acidic or alkaline leaching and an optimized combination of both N2 - The advantages and drawbacks of existing wet chemical phosphorus (P) recovery technologies, their applicability to different types of sewage sludge ash (SSA) and the role of the decay products of detergent zeolites as a source of reactive Al in SSA are analyzed. Since neither a purely acidic nor a purely alkaline treatment are able to provide satisfactory technical solutions a wet chemical phosphorus (P) recovery process for sewage sludge ashes (SSAs) is investigated in detail that is based on a sequential treatment of SSA with an acid and a base. As a result of an acidic pre-treatment, the P fraction of the raw SSA that was bound as – alkaline-insoluble – calcium phosphate (Ca–P) is converted into aluminum phosphate (Al–P). This newly formed Al–P can be easily dissolved via alkaline treatment and then easily separated from the alkaline leachate via precipitation of Ca–P. The Al-component can be reused as precipitant for P-removal in waste water treatment plants (WWTPs). The investigated process requires fewer chemicals than the direct acidic dissolution of all P-compounds contained in the SSA. This is due to the described rearrangement of the P component from Ca–P to Al–P. That such a rearrangement of P occurs indeed was confirmed through a combination of XRD, ICP and XRF analyses together with mass balance calculations. The present investigation proves that the process works for very different types of SSAs: For Al-rich SSAs that come from WWTPs where Al-salt is used for chemical P-removal the described sequential treatment process works best and yields P-recovery rates as high as 70–77%. But even for SSAs from WWTPs where only iron salt is used for chemical P-removal, a considerable amount of the reactive Al necessary for the described P-rearrangement is supplied by decay products of detergent zeolites, a hidden Al-source present in most SSAs produced in Europe. KW - Phosphorus recovery KW - Sewage sludge ash KW - Alkaline and acidic leaching KW - Calcium phosphate KW - Aluminum phosphate KW - Detergent zeolites KW - XRD analysis PY - 2012 DO - https://doi.org/10.1016/j.watres.2012.03.068 SN - 0043-1354 VL - 46 IS - 12 SP - 3769 EP - 3780 PB - Elsevier CY - Amsterdam AN - OPUS4-26005 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Peplinski, Burkhard A1 - Adamczyk, Burkart T1 - New horizons for the structural characterization of stainless steel slags by X-ray powder diffraction T2 - 10. European Powder Diffraction Conference (EPDIC-10) CY - Geneva, Switzerland DA - 2006-09-01 PY - 2006 AN - OPUS4-13787 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Peplinski, Burkhard A1 - Adam, Christian A1 - Michaelis, Matthias A1 - Kley, Gerd A1 - Emmerling, Franziska A1 - Simon, Franz-Georg T1 - Reaction sequences in the thermochemical treatment of sewage sludge ashes revealed by X-ray powder diffraction - A contribution to the European project SUSAN N2 - The sequence of reactions accompanying the thermochemical treatment of an iron- and aluminium-bearing sewage sludge ash was ascertained by investigating two systematic series of samples. The ash was thermochemically treated in a lab-scale rotary furnace after mixing it with a chlorine-donor, either CaCl2 or MgCl2. Within each of these two sample series only a single process parameter, the reaction temperature, was varied, namely between 350 and 1050°C. It was found, that among the numerous crystalline phases present in the raw ash only quartz and hematite continue to exist after thermochemical treatments carried out at 1050°C, whereas all other components undergo at least one decomposition-recrystallization cycle. Some of the components re-crystallize even several times. It was proved that the restructuring of the calcium- and phosphorus-bearing mineral phases proceeds via the formation of chlorspodioside, Ca2PO4Cl. The influence of the type of chlorine-donor on the final product was elucidated in detail and - to the best of our knowledge - for the first time crystalline AlPO4 was found in a sewage sludge ash and its decomposition was investigated, too. KW - XRD KW - Phosphorus recovery KW - Sewage sludge ash KW - Urban mining KW - Fertilizers PY - 2009 DO - https://doi.org/10.1524/zksu.2009.0068 SN - 0930-486X VL - 30 EPDIC 2008 SP - 459 EP - 464 PB - Oldenbourg CY - München AN - OPUS4-20562 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -