4 Material und Umwelt
Filtern
Dokumenttyp
- Vortrag (440) (entfernen)
Sprache
- Englisch (279)
- Deutsch (155)
- Spanisch (4)
- Französisch (2)
Referierte Publikation
- nein (440)
Schlagworte
- Biocides (20)
- Antimicrobial resistance (19)
- Nano (18)
- Recycling (17)
- Ink (16)
- MIC (14)
- Biofilms (12)
- Phosphor (12)
- XRF (12)
- Klärschlamm (11)
Organisationseinheit der BAM
- 4 Material und Umwelt (440)
- 4.4 Thermochemische Reststoffbehandlung und Wertstoffrückgewinnung (93)
- 4.1 Biologische Materialschädigung und Referenzorganismen (91)
- 4.3 Schadstofftransfer und Umwelttechnologien (81)
- 4.2 Material-Mikrobiom Wechselwirkungen (77)
- 4.5 Kunst- und Kulturgutanalyse (66)
- 4.0 Abteilungsleitung und andere (46)
- 6 Materialchemie (30)
- 1 Analytische Chemie; Referenzmaterialien (27)
- 6.1 Oberflächen- und Dünnschichtanalyse (16)
Per- and polyfluoroalkyl substances (PFAS) are anionic, cationic and zwitterionic synthetic products, in which the hydrogen atoms on the carbon skeleton of at least one carbon atom have been completely replaced by fluorine atoms (see Figure 1) and which include more than 4730 compounds, depending on the definition. As a result of continuous and prolific use, mainly in aviation firefighting foams, thousands of industrial and military installations have been found to contain contaminated soil, groundwater and surface water. Furthermore, because of the continuous contamination through PFAS containing commercial products, effluents and sewage sludge from WWTPs have been shown to be an important source of PFAS discharge into the aquatic environment. In the last few years, legacy PFAS (≥C4) have been found in various environments, including soil, water and wastewater, and their environmental pathways have been partly described. To get a better
overview of the amount of “total PFAS,” sum parameter methods like total oxidizable precursor (TOP) assay and methods based on combustion ion chromatography (CIC) are in development. CIC results in data regarding the sum of absorbable organic fluorine (AOF) or extractable
organic fluorine (EOF), which can also quantify other organically bound fluorine compounds such as fluorinated pesticides and pharmaceutical. Additionally, for research purpose several spectroscopical methods like X-ray photoelectron spectroscopy (XPS), fluorine K-edge X-ray absorption near-edge structure (XANES) spectroscopy, particular induced gamma-ray emission (PIGE) spectroscopy and 19F nuclear magnetic resonance (NMR) spectroscopy are available. Therefore, an overview is given on various analytical techniques for PFAS in environmental samples and their application possibilities discussed for different kind of PFAS compounds
Recycling-Düngemittel auf Basis von sekundären Ressourcen (Gülle, Gärreste, Klärschlamm, Tiermehl etc.) gewinnen in den letzten Jahren zunehmend an Bedeutung in der Landwirtschaft. Die in den Recycling-Düngemitteln enthaltenen P-Spezies weichen oft stark von denen in konventionell hergestellten Düngemitteln aus Rohphosphat ab, zudem enthalten Recyclingdünger oft mehrere verschiedene P-Formen. Die Pflanzenverfügbarkeit des P in ist ganz wesentlich von der enthaltenen P-Form abhängig. Derzeit gibt es außer zeitaufwendigen und kostspieligen Gefäß- und Feldversuchen keine zufriedenstellende Testmethode zur Analyse der P-Pflanzenverfügbarkeit von unterschiedlichen Recycling P-Düngemitteln. Die im europäischen Düngemittelrecht normierten chemischen Extraktionsmethoden (Wasser, Zitronensäure, Ameisensäure, neutral Ammoniumcitrat etc.) zeigen oftmals keine oder nur sehr geringe Korrelation zu der P-Aufnahme von Pflanzen in Gefäßversuchen mit Recycling-Düngemitteln (Kratz et al. 2010, Steckenmesser et al. 2017, Vogel et al. 2017). Eine grundlegende Schwäche chemischer Extraktionsmethoden liegt darin, dass es sich dabei um statische Methoden handelt, die nicht in der Lage sind, die im System Boden/Düngemittel-Bodenlösung-Pflanze stattfindenden dynamischen Prozesse wie P-Freisetzung und Entzug durch die Pflanzenwurzeln abzubilden.
Einen Lösungsansatz bieten hier sog. P-Senken-Methoden. Bereits in den 1950er Jahren wurden erstmals P-Senken zur Analyse des Boden-P angewendet (Chardon et al. 1996). In den darauffolgenden Jahrzehnten wurden verschiedene P-Senken auf der Basis von Eisenoxid-Papier entwickelt (Chardon et al. 1996). Jedoch konnten diese Ansätze auch nur begrenzt zur Bestimmung der P-Pflanzenverfügbarkeit des Boden-P eingesetzt werden. Mitte der 1990er Jahre wurde die DGT (engl. diffusive gradients in thin films) Methode entwickelt (Zhang et al. 1998). Bei der DGT Methode diffundiert P aus der Bodenlösung des angefeuchteten Bodens durch einen Membranfilter und die Diffusionsschicht und wird anschließend an einer Bindungsschicht absorbiert. Durch den Diffusionsgradienten wird das Gleichgewicht in der Bodenlösung permanent gestört, wodurch auch labiles P im Boden gelöst wird. Die stetige Entnahme von P aus der Bodenlösung über die Diffusions-/Bindungsschicht simuliert dabei den Entzug von P durch die Pflanzenwurzel. Die an die Bindungsschicht adsorbierte Menge an P korreliert stark mit der P-Aufnahme von Pflanzen (u.a. Mason et al. 2005, 2013; Menzies et al. 2005, Six et al. 2012). Im Gegensatz zu chemischen Extraktionsmethoden werden bei der DGT Methode Mischungen an Düngemittel und Boden für mehrere Tage inkubiert (Vogel et al. 2017; Duboc et al. 2017), da ansonsten wasserlösliche P-Dünger den DGT Adsorber sättigen und wasserunlösliche P-Dünger unterschätzt werden. Ein bis zwei Wochen Inkubation sind ausreichend, damit sich pflanzenverfügbares P in die Mischungen bildet.
In letzter Zeit haben verschiedene Forschungsgruppen gezeigt, dass die DGT Methode auch eine sehr gute Korrelation mit der Pflanzenverfügbarkeit verschiedener Typen von (Recycling-)P-Düngemitteln aufweist (Vogel et al. 2017; Duboc et al. 2017; Foereid 2017; Haarstad and Bavor 2017; Lemming et al. 2017). Bei Gefäßversuchen mit verschiedenen Recycling P-Düngemitteln konnte die DGT Methode den Ertrag bzw. die P-Aufnahme von Mais deutlich besser vorhersagen als herkömmliche chemische Extraktionsmethoden (Vogel et al. 2017; Duboc et al. 2017).
Daher kann die DGT Methode im Vorfeld der Zulassung von neuen Düngermitteltypen als zuverlässige und robuste Methode zum Screening von Produktvarianten eines Düngemittelherstellers verwendet werden. Um dieses Messverfahren im Rahmen des Düngemittelrechts als Bewertungsinstrument für die Abschätzung der Pflanzenverfügbarkeit unterschiedlicher Düngemittel zu verwenden, muss es allerdings zunächst standardisiert werden. Zu diesem Zweck bietet sich der Einsatz eines „standardisierten“ Bodens bzw. Bodenrezepts an. Zur Kalibrierung der Methode im jeweiligen Labor könnten auch chemisch definierte P-Verbindungen mit bekannter Löslichkeit/Pflanzenverfügbarkeit als Referenz-substanzen verwendet werden.
Previous research shows that analytical methods based on Diffusive Gradients in Thin films (DGT) provide very good correlations to the amount of bioavailable nutrients and pollutants in the environmental samples. However, these DGT results do not identify which compound of the specific element has the high bioavailability. Using various spectroscopic techniques (infrared, XANES and NMR spectroscopy) to analyze the dried DGT binding layers after deployment could allow us to determine the specific elements or compounds. Nutrients such as phosphorus and nitrogen are often, together with other elements, present as molecules in the environment. These ions are detectable and distinguishable by infrared and NMR spectroscopy, respectively. In addition, XANES spectroscopy allows for the specification of nutrients and pollutants (e.g. chromium) on the DGT binding layer. Furthermore, microspectroscopic techniques make it also possible to analyze compounds on the DGT binding layer with a lateral resolution down to 5 µm2. Therefore, species of elements and compounds of e.g. a spatial soil segment can be mapped and analyzed, providing valuable insight to understand the dynamics of nutrients and pollutants in the environment. Here we will present the advantages and limitations of this novel combination of techniques.
Phosphorus (P) plays an essential role in the global food security. However, the global P reservoirs have a statistic lifetime of about 385 years only. Due to the scarcity of P and the increasing world population an efficient and sustainable recycling management is required. A few biogenic waste materials are high in P contents such as sewage sludge and meat and bone meal. Thus, they are suitable for P recycling and fertilizer production. But besides the high P content sewage sludge is often highly contaminated with organic pollutants and toxic heavy metals which have to be eliminated before agricultural field application. In this presentation we show the potential of sewage sludge as secondary resource for fertilizers. This includes our developments in thermochemical processes for the production of novel P-fertilizers from recycled materials. Furthermore, for these novel P-fertilizers common extraction tests to determine the plant-available P are often unusable. Therefore, we successfully applied the Diffusive gradients in thin-films (DGT) techniques to analyse the plant-availability of P-fertilizers from recycled materials.
Per- and polyfluoroalkyl substances (PFAS) are a large group of more than 10,000 anionic, cationic, zwitterionic or neutral organofluorine surfactants. As a result of continuous and prolific use, mainly in aviation firefighting foams, thousands of industrial and military installations have been found to contain contaminated soil, groundwater and surface water. While liquid chromatography tandem mass spectrometry (LC-MS/MS) is commonly used technique to characterize targeted PFAS in environmental samples, there are more than 10,000 different PFAS known, which have various headgroups and properties. Therefore, several analytical techniques are available to analyse various groups or pools of PFAS or “all” PFAS as a sum parameter. Current decontamination strategies of PFAS-burdened soils mainly consist of adsorption methods using adsorbents for fixation of PFAS in the ground. A second option is the utilization of a “pump and treat” process, cycling polluted soils through a washing plant leading to the concentration of the pollutants in the fine fraction. Both approaches are cost-intensive and not intended for the direct decomposition of all PFAS contaminants. Hence, there is a great demand for innovative developments and chemical treatment technologies, dealing with new strategies of tackling the PFAS problem. Previously, mechanochemical treatment of polychlorinated organic compounds in soils showed an efficient dechlorination. Thus, we investigated mechanochemical treatment of PFAS contaminated soils with various additives in a ball mill and analyzed the PFAS defluorination with gas chromatography mass spectrometry (GC-MS) and liquid chromatography tandem mass spectrometry (LC-MS/MS), respectively, as well es the fluoride mineralization by ion chromatography (IC) and fluorine K-edge X-ray absorption near-edge structure (XANES) spectroscopy.
Current decontamination strategies of PFAS-burdened soils mainly consist of adsorption methods using adsorbents for fixation of PFAS in the ground. A second option is the utilization of a “pump and treat” process, cycling polluted soils through a washing plant leading to the concentration of the pollutants in the fine fraction. Only a subsequent, high-energy consuming pyrolysis process guarantees the total destruction of all fluorinated organic contaminants. These approaches are cost-intensive and not intended for the direct decomposition of all PFAS contaminants. Hence, there is a great demand for innovative developments and chemical treatment technologies, dealing with new strategies of tackling the PFAS problem. Thus, we investigated mechanochemical treatment of PFAS contaminated soils with various additives in a ball mill and analyzed the PFAS defluorination with gas chromatography mass spectrometry (GC-MS) and liquid chromatography tandem mass spectrometry (LC-MS/MS), respectively, as well as the fluoride mineralization by ion chromatography (IC) and fluorine K-edge X-ray absorption near-edge structure (XANES) spectroscopy.
Per- and polyfluoroalkyl substances (PFAS) are a group of anionic, cationic and zwitterionic synthetic products, in which the hydrogen atoms on the carbon skeleton of at least one carbon atom have been completely replaced by fluorine atoms and which include more than 4730 compounds, depending on the definition. As a result of continuous and prolific use, mainly in aviation firefighting foams, thousands of industrial and military installations have been found to contain contaminated soil, groundwater and surface water. Furthermore, current decontamination strategies of PFAS-burdened soils mainly consist of adsorption methods using adsorbents for fixation of PFAS in the ground. Hence, there is a great demand for innovative developments and chemical treatment technologies, dealing with new strategies of tackling the PFAS problem. Thus, we investigated mechanochemical treatment of PFAS contaminated soils with various additives in a ball mill and analyzed the PFAS defluorination. In this presentation the advantages of fluorine K-edge X-ray absorption near-edge structure (XANES) spectroscopy for various environment samples are shown.
Per- and polyfluoroalkyl substances (PFAS) have been used extensively in the past because of their inert chemical character and resistance to degradation by environmental influences. Since the beginning of their commercial use, PFAS have been widely exposed to the environment by application of PFAS in consumer products or as foaming agent in firefighting foams, thus several cases of contaminated soils sites have been reported. Since the number of known PFAS already exceeds 4700, their characterization and direct analysis is challenging given the current available techniques. Here, we introduce the novel fluorine (F) K-edge X-ray absorption near-edge structure (XANES) spectroscopy as a tool to analyze PFAS and inorganic fluorine compounds in contaminated soils and sewage sludges. While F K-edge bulk-XANES spectroscopy provide us information on the overall fluorine bonding in a sample micro X-ray fluorescence (XRF) in combination with F K-edge micro-XANES spectroscopy can also detect minor fluorine compounds and PFAS hotspots in investigated soils and sludges. Additionally, we used the combustion ion chromatography (CIC) to analyze the total amount of all PFAS as a sum parameter (extractable organic fluoride: EOF) in soils and sewage sludges. During combustion in the CIC, the PFAS in the sample get destroyed at temperatures of approx. 1000 °C and converted in inorganic fluorides that subsequently gets quantified by ion chromatography. Thus, for the first time we successfully combined F K-edge XANES spectroscopy and CIC as analytical tools to detect and quantify PFAS contaminants in soils and sewage sludges.
Per- and polyfluoroalkyl substances (PFAS) are a group of anionic, cationic and zwitterionic synthetic products, in which the hydrogen atoms on the carbon skeleton of at least one carbon atom have been completely replaced by fluorine atoms and which include more than 4730 compounds, depending on the definition. As a result of continuous and prolific use, mainly in aviation firefighting foams, thousands of industrial and military installations have been found to contain contaminated soil, groundwater and surface water. As a result of the perpetual use of PFAS containing products, effluents and sewage sludge from wastewater treatment plants (WWTPs) have been observed to be an important pathway for PFAS into the environment. In Germany, phosphorus and other nutrients from sewage sludge and wastewater should be recycled in WWTPs of cities with a large population. However, it is not clear if PFAS contamination from wastewater and sewage sludge end up in novel wastewater-based fertilizers. Normally, PFAS are analyzed using PFAS protocols typically with liquid chromatography tandem mass spectrometry (LC-MS/MS) quantification. To get a better overview of the amount of “total PFAS,” we applied sum parameter methods based on combustion ion chromatography (CIC) to screen the PFAS contaminations in various sewage sludge and wastewater-based fertilizers. Furthermore, current decontamination strategies of PFAS-burdened soils mainly consist of adsorption methods using adsorbents for fixation of PFAS in the ground. A second option is the utilization of a “pump and treat” process, cycling polluted soils through a washing plant leading to the concentration of the pollutants in the fine fraction. Only a subsequent, high-energy consuming pyrolysis process guarantees the total destruction of all fluorinated organic contaminants. Both approaches are cost-intensive and not intended for the direct decomposition of all PFAS contaminants. Hence, there is a great demand for innovative developments and chemical treatment technologies, dealing with new strategies of tackling the PFAS problem.
Per- and polyfluoroalkyl substances (PFAS) are chemicals which were developed to improve humanity’s quality of life. Due to their high chemical stability and resistance to degradation by heat or acids, PFAS were used in a variety of consumer products. The continuous use of PFAS in household products and the discharge of PFAS from industrial plants into the sewer system resulted in the contamination of effluents and sewage sludge from wastewater treatment plants (WWTPs) (Roesch et al. 2022). Since sewage sludge is often used as fertilizer, its application on agricultural soils has been observed as a significant entry path for PFAS into the environment, specifically in our food chain. In Germany the sewage sludge/biosolid application on agricultural land was banned with the amendment of the German Sewage Sludge Ordinance and by 2029 sewage sludge application will be totally prohibited. However, phosphorus (P) from sewage sludge should still be recycled in WWTPs of cities with a population larger than 50,000 residents. To produce high-quality P-fertilizers for a circular economy, PFAS and other pollutants (e.g. pesticides and pharmaceuticals) must be separated from sewage sludge. Due to the strong diversity of industrial PFAS usage it is not clear if a safe application of novel recycled P-fertilizers from WWTPs can be guaranteed. Therefore, we analyzed various sewage sludges and wastewater-based fertilizers. Sewage sludge (SL) samples from various WWTPs in Germany and Switzerland, six sewage sludge ashes (SSA) from Germany, six thermally treated SL and SSA samples with different additives (temperatures: 700-1050 °C), two pyrolyzed SL samples (temperature: 400 °C) and two struvite samples from Germany and Canada were analyzed. The goal was to quantify PFAS in sewage sludges and wastewater-based P-fertilizers with the sum parameter extractable organic fluorine (EOF) by combustion ion chromatography (CIC). The results were compared with data from classical LC-MS/MS target analysis as well as selected samples by HR-MS suspect screening. The EOF values of the SLs mainly range between 154 and 538 µg/kg except for one SL which showed an elevated EOF value of 7209 µg/kg due to high organofluorine contamination. For the SSA samples the EOF values were lower and values between LOQ (approx. 60 µg/kg) and 121 µg/kg could be detected. For the pyrolyzed SLs no EOF values above the LOQ were detected. Moreover, the two wastewater-based struvite fertilizers contain 96 and 112 µg/kg EOF, respectively. In contrast to the EOF values, the sum of PFAS target values were relatively low for all SLs. Additional applied PFAS HR-MS suspect screening aimed to tentatively identify PFAS that could contribute to the hitherto unknown part of the EOF value. The majority of the detected fluorinated compounds are legacy PFAS such as short- and long-chain perfluorocarboxylic acids (PFCA), perfluorosulfonic acids (PFSA), polyfluoroalkyl phosphate esters (PAPs) and perfluorophosphonic acids (PFPA). Moreover, fluorinated pesticides, pharmaceutical as well as aromatic compounds were also identified, which are all included in the EOF parameter. Our research revealed that the current PFAS limit of 100 µg/kg for the sum of PFOS + PFOA in the German Fertilizer Ordinance is no longer up to date. Since the number of known PFAS already exceeds 10,000, the ordinance limit should be updated accordingly. Recent regulations and restrictions on using long-chain PFAS (≥C8) have resulted in a significant shift in the industry towards (ultra-)short-chain alternatives, and other, partly unknown, emerging PFAS. Ultimately, also fluorinated pesticides and pharmaceuticals, which end up as ultrashort PFAS in the WWTPs, have to be considered as possible pollutants in fertilizers from wastewater, too.
Per- and polyfluoroalkyl substances (PFAS) are a large group of organofluorine surfactants used in the formulations of thousands of consumer goods. The continuous use of PFAS in household products and the discharge of PFAS from industrial plants into the sewer system have been resulted in contaminated effluents and sewage sludge from wastewater treatment plants (WWTPs) which became an important pathway for PFAS into the environment. Because sewage sludge is often used as fertilizer its application on agricultural soils has been observed as significant input path for PFAS into our food chain. To produce high-quality phosphorus fertilizers for a circular economy from sewage sludge, PFAS and other pollutants (e.g. pesticides and pharmaceuticals) must be separated from sewage sludge. Normally, PFAS are analyzed using PFAS protocols typically with time-consuming extraction steps and LC-MS/MS target quantification. However, for screening of PFAS contaminations in wastewater-based fertilizers also the DGT technique can be used for the PFAS extraction. Afterwards, combustion ion chromatography (CIC) can be applied to analyze the “total” amount of PFAS on the DGT binding layer. The DGT method was less sensitive and only comparable to the extractable organic fluorine (EOF) method values of the fertilizers in samples with >150 µg/kg, because of different diffusion properties for various PFAS, but also kinetic exchange limitations. However, the DGT approach has the advantage that almost no sample preparation is necessary. Moreover, the PFAS adsorption on the DGT binding layer was investigated via surface sensitive spectroscopical methods, such as Fourier-transform infrared (FT-IR) and fluorine K-edge X-ray absorption near-edge structure (XANES) spectroscopy.
Per- und polyfluorierte Alkylsubstanzen (PFAS) im Klärschlamm - Analytische Methoden und Grenzwerte
(2022)
Per- und Polyfluoralkylsubstanzen (PFAS) sind eine Gruppe von mehr als 4700 anionischen und kationischen anthrophonen Stoffen, die aufgrund ihrer inerten chemischen Stabilität und ihrer Widerstandsfähigkeit gegen den Abbau durch Hitze oder Säuren in einer Vielzahl von Produkten verwendet werden. Infolge der ständigen Verwendung, vor allem in Feuerlöschschäumen für die Luftfahrt, wurden in Tausenden von Industrie- und Militäranlagen kontaminierte Böden und Grundwasservorkommen gefunden. Aufgrund der ständigen Verwendung von fluorierten Konsumgütern haben sich jedoch auch Abwässer und Klärschlamm aus Kläranlagen als Quelle für die Kontamination der aquatischen Umwelt mit PFAS erwiesen. Infolge der strengeren Vorschriften und Beschränkungen, die in den letzten Jahren für die Verwendung langkettiger (≥C8) PFAS erlassen wurden, findet in der chemischen Industrie eine deutliche Verlagerung hin zur Herstellung kurz- (C4-C7) und ultrakurzkettiger (C1-C3) Alternativen statt. Mit der Novellierung der Klärschlammverordnung im Jahr 2017 hat der deutsche Gesetzgeber die Ausbringung von Klärschlamm auf landwirtschaftlichen Flächen verboten, und bis 2029/2032 wird die Ausbringung von Klärschlamm in der Landwirtschaft vollständig verboten sein. Während die Belastung der Umwelt mit organischen Schadstoffen wie PFAS, Pestiziden und Arzneimitteln nicht mehr erwünscht ist, muss Phosphor (P) aus Klärschlamm weiterhin zur Herstellung hochwertiger P-Dünger für eine Kreislaufwirtschaft genutzt werden. Derzeit können pflanzenverfügbare P-Düngemittel aus Klärschlamm/Abwasser mit verschiedenen Behandlungsmethoden hergestellt werden, darunter Fällung, Auslaugung und thermische Behandlung. Der Verbleib von PFAS bei der Auslaugung, Ausfällung und Behandlung von Klärschlamm und Abwasser ist jedoch noch weitgehend unbekannt.
Per- and polyfluoroalkyl substances (PFAS) are a large group of anionic, cationic, or zwitterionic organofluorine surfactants used in the formulations of thousands of products and consumer goods, including aqueous film-forming foams (AFFF) used to suppress aviation fires in training scenarios, non-stick cookware, fast-food wrappers, water-repellent fabrics, medical equipment. Because PFAS have been extensively used in a variety of AFFF products they can be found in soils from industrial and military installations. Current decontamination strategies of PFAS-burdened soils mainly consist of adsorption methods using adsorbents for fixation of PFAS in the ground. A second option is the utilization of a “pump and treat” process, cycling polluted soils through a washing plant leading to the concentration of the pollutants in the fine fraction. Only a subsequent, high-energy consuming pyrolysis process guarantees the total destruction of all fluorinated organic contaminants. Both approaches are cost-intensive and not intended for the direct decomposition of all PFAS contaminants. Hence, there is a great demand for innovative developments and chemical treatment technologies, dealing with new strategies of tackling the PFAS problem. Previously, mechanochemical treatment of polychlorinated organic compounds in soils showed an efficient dechlorination. Thus, we investigated mechanochemical treatment of PFAS contaminated soils with various additives in a ball mill and analyzed the PFAS defluorination with gas chromatography mass spectrometry (GCMS) and liquid chromatography tandem mass spectrometry (LC-MS/MS), respectively, as well es the fluoride mineralization by ion chromatography (IC) and fluorine K-edge X-ray absorption near-edge structure (XANES) spectroscopy.
Lightweighting as a cross-cutting technology contributes significantly to achieve the European Green Deal goals. Based on, but not limited to, advanced materials and production technologies, the demand for natural resources and CO2 emmissions are reduced by lightweighting during production, as well as use phase. Therefore, lightweighting is a crucial transformation technology assisting in decoupling economic growth from resource consumption. In this manner, lightweighting contributes significantly as a key technology of relevance for many industrial sectors such as energy, mobility, and infrastructure, towards resource efficiency, climate action and economic strength, as well as a resilient Europe. To strengthen international partnerships, addressing global issues of today at the edge of science with high performance lightweight material based on carbon fibers, an overview about the BAM expertise in carbon fiber reinforced materials is given.
Ammoniakemissionen in die Umwelt erfolgen insbesondere durch die Landwirtschaft (93,6 %), aber auch durch Verbrennungsprozesse in der die Abfallwirtschaft (2,3 %) und den Straßenverkehr (1,8 %). Dieser Stoff ist selbst in geringen Konzentrationen nicht nur eine Geruchsbelästigung, sondern auch eine Substanz mit ökologischer und klimatischer Relevanz.
Die Bestimmung von Ammoniak in relevanten Konzentrationen von kleiner 25 μg m-3 erfolgt im Allgemeinen über NH4+ als Analyten, spektralfotometrisch oder mit der Ionenchromatographie nach Überführung in die flüssige Phase. Wegen der niedrigen Konzentrationen an Ammoniak in der Außenluft wird meist eine gesammelte Probe verwendet oder die Bestimmung erfolgt nach einer aktiven, anreichernden Probenahme.
Die eigenen Arbeiten sollen dazu beitragen, die Ammoniak-Bestimmung in der Außenluft präziser, sowie schneller und kostengünstiger zu machen.
Die BAM prüfte daher kommerzielle elektrochemische und Metalloxid-basierte Sensoren, die für diesen Konzentrationsbereich aber nur bedingt geeignet sind. Deshalb wurden alternativ eigene Entwicklungen zum Nachweis von Ammoniak im Spurenbereich aufgenommen, wobei der Analyt über die Änderung der Fluoreszenz eines BODIPY-Farbstoffs bei 550 nm mittels eines portablen Fluoreszenz-Sensors direkt aus der Gasphase gemessen wird.
Zur Kalibrierung von Ammoniak-Sensoren und -Messgeräten steht ein stationäres System basierend auf der Mischung von zertifizierten Prüfgasen aus Druckflaschen mit kalibrierten Massendurchfluss-regler (MFC) zur Verfügung. Darüber hinaus erfolgt eine chemische Analyse der verwendeten Gasgemische mittels eines Massenspektrometers.
Für die Kalibrierung und Prüfung von Sensoren und Messgeräten vor Ort wurde ein mobiles Prüfsystem entwickelt. Die Generierung von Ammoniak-haltigen Gasen im Spurenbereich von 0,5 nmol/mol bis 500 nmol/mol erfolgt durch das Permeationsverfahren nach ISO 6145-10.
Für die Realisierung der Rückführbarkeit der Ammoniakbestimmung werden von den Nationalen Metrologischen Instituten sowie designierten Instituten Standards bereitgestellt und auch weiterentwickelt. Die primären metrologischen Standards beruhen auf SI-Einheiten und sind die Basis für eine Rückführbarkeit der Sensoren bzw. Analysengeräte.
Optimierung eines pyrometallurgischen Tantal- und Niob- Recyclingprozesses mithilfe von On-Line LIBS
(2018)
Die Entwicklung von Hochleistungselektronik zu immer kleineren Bauformen ohne Leistungseinbußen ist ohne den Einsatz von Technologiemetallen wie Niob und Tantal heute praktisch nicht mehr realisierbar. Besonders in technischen Geräten wie Smartphones und Tablets sind Tantal- und Niobkondensatoren aufgrund ihrer hohen Leistungsdichten bereits unverzichtbar geworden. Für die nachhaltige Produktion von Elektronik stellt jedoch vor allem das Tantalerz Coltan als sogenanntes „conflict mineral” ein großes Problem dar.
Um den Wirtschaftsstandort Europa unabhängiger von Primärrohstoffimporten aus Krisenregionen zu machen, ist die Entwicklung von effizienten Recyclingverfahren heute wichtiger denn je. An der Bundesanstalt für Materialforschung und -prüfung (BAM) findet daher zurzeit die Optimierung eines pyrometallurgischen Industrieprozesses zur Niob- und Tantalrückgewinnung statt, welchem hauptsächlich niedrigkonzentrierte metallurgische Rückstände aus der Tantal- und Niob- bzw. der Zinngewinnung als Einsatzstoffe dienen.
Zu diesem Zweck werden im kleintechnischen Lichtbogenofen der BAM (480 kVA, max. Materialdurchsatz ca. 150 kg/h) Versuche mit einem neuen innovativen Messgerät durchgeführt, welches eine On-Line Analyse von Hochtemperaturprozessen ermöglicht. Der eingesetzte Prototyp nutzt das Verfahren der laserinduzierten Plasmaspektroskopie (LIBS), um die chemische Zusammensetzung der Schlackephase noch im Schmelzbad und während eines Schlackeabgusses zu bestimmen. Nach einer Kalibrierung auf das vorliegende Stoffsystem ermöglicht dieser On-Line-LIBS Prototyp der BAM daher eine in-situ Bestimmung der Elementverteilung in der Schmelze. Die hier gewonnenen Daten sollen helfen, die aktuelle Prozessführung zu verbessern und die Tantal- und Niobausbeute noch weiter zu erhöhen.
Tantalum and niobium are essential for the development of electronics towards a more and more compact design, but without reducing their performance today. Especially in smart phones and tablets, tantalum and niobium capacitors with high charge densities have already become almost indispensable. However, tantalum as a critical raw material is still a problem for the sustainable production of electronics. Due to this fact, the existence of efficient recycling processes especially in Europe is becoming even more important nowadays.
The Bundesanstalt für Materialforschung und -prüfung (BAM) is currently working on the optimisation of an existing pyrometallurgical tantalum recycling process. Optimisation of this industrial process is carried out in a small-scale electric arc furnace (480 kVA, capacity approx. 150 kg/h) at BAM using a new and innovative equipment for on-line analysis of high temperature processes.
The aim of this project is to identify the best timing for an optimum slag tapping, when the slag is lower than minimum targeted tantalum concentration. Hence, LIBS (Laser induced breakdown spectroscopy) is used to identify the chemical composition of the slag layer and during slag tapping. The on-line-LIBS prototype of BAM enables an in-situ measurement of the element distribution in the melt after calibration on the slag system.
First results of this joint research project will be presented including on-line-LIBS-measurements and thermodynamic and kinetic aspects of the process.
An existing pyrometallurgical process for tantalum and niobium recovery, mainly from low grade pyrometallurgical residues, was investigated. Series of melting experiments were carried out in a pilot-scale electric arc furnace to study how the amount, the grain size and the way of feeding affect the activity of carbon as a reducing agent. During the pyrometallurgical treatment refractory metals such as tantalum and niobium are reduced to their carbide form and enriched in the molten iron-based metal phase. The cooled down slag and metal phase were analysed to investigate thermodynamic and kinetic conditions of the carbide formation. FACT Sage simulations were also used to investigate the material system in state of thermodynamic equilibrium. Results show that mass transfer and kinetics may play an important role if compared to equilibrium analyses using FACT Sage.
Since the recycling of tantalum bearing post-consumer waste is practically not existent, metallurgical residues are the most important feed for the tantalum recycling. Most tin ores naturally contain significant quantities of refractory metals. During the smelting process in primary tin production these elements are enriched in the slag phase. This slag is a highly valuable raw material for tantalum production due to its considerable concentration of tantalum and its functioning as an additional slag former in further pyrometallurgical treatment.
In this paper the first process stage of an existing pyrometallurgical process for tantalum recovery, mainly from low grade pyrometallurgical residues, is discussed. Smelting trials were carried out in a pilot-scale electric arc furnace to analyse the effect of feeding on the activity of carbon as a reducing agent. Therefore, blowing petroleum coke through an iron lance and the manual adding of coke into the melting bath were tested. During the pyrometallurgical treatment elements with a high affinity to carbon were reduced to their carbide form and enriched in the molten iron-based metal phase. The objective of the process was to reduce the oxidic tantalum completely and to enrich it into the metal phase. Furthermore, the transfer of unwanted elements such as titanium into the metal phase was aimed to be avoided.
Spoon test specimens were taken from the liquid mineral melt to follow the evolution of the reduction process. The cooled down solidified melting bath was investigated by using the XRD and EDX method to characterise the slag system and to identify relevant mineral phases.
Fused filament fabrication (FFF) on desktop 3D printers is a material extrusion-based technique often used by educational institutions, small enterprises and private households. Polymeric filaments are melted and extruded through a heated nozzle to form a 3D object in layers. The extrusion temperature is therefore a key parameter for a successful print job, but also one of the main driving factors for the emission of harmful air pollutants, namely ultrafine particles and volatile organic gases, which are formed by thermal stress on the polymeric feedstock. The awareness of potential health risks has increased the number of emission studies in the past years. However, the multiplicity of study designs makes an objective comparison of emission data challenging because printer hardware factors such as the actual extruder temperature (TE) and also feedstockspecific emissions are not considered. We assume that across the market of commercial low- and mid-price FFF printers substantial deviations between actual and set extruder temperatures exist, which have a strong effect on the emissions and hence may bias the findings of exposure studies. In our last publication, we presented a standardized feedstock-specific emission test method and showed that for each investigated feedstock an increase in actual extruder temperature was accompanied by an increase in particle emissions (Tang and Seeger, 2022). Therefore, any systematic discrepancy between set and actual extruder temperature matters. In this study, we used a thermocouple and an infrared camera to measure the actual extruder temperatures at different heights. We found significant under- and overestimation of the actual extruder temperatures by the respective set temperatures in three commercial printers. This caused a broad variation of the measured total numbers of emitted particles (TP), even when the same feedstock was operated. For the determination of TP, we followed the DE-UZ 219 test guideline. In a second round we repeated the tests with all printers adjusted to exactly the same extruder temperatures, i.e., to TE=230°C for ABS and TE=210°C for PLA. All measurements were conducted in a 1 m³ emission test chamber. Particle emissions in the size range between 4 nm and 20 μm were detected. Printing on three different printer models without temperature adjustment resulted for each of the investigated feedstocks in a variation in TP of around two orders of magnitude. After temperature adjustment, this was substantially reduced to approx. one order of magnitude and hence minimizes the bias of printer hardware on the emissions. Our findings suggest that adjustment of the extruder temperature should be mandatory in emission testing standards. It also poses a more accurate benchmark and provides more reliable emission data for evaluation of indoor air quality or for health risk assessments. In addition, a proper temperature setting is in the interest of the user. Some commercial FFF printers may have a higher actual extruder temperature than displayed and unintended overheating may not only impair the print quality but may cause unnecessarily increased exposure to particle emissions.