TY - CONF A1 - Adam, Christian A1 - Krüger, Oliver A1 - Herzel, Hannes ED - Lederer, J. ED - Laner, D. ED - Rechberger, H. ED - Fellner, J. T1 - Phosphorus flows in German sewage sludge ashes and potential recovery technologies N2 - Phosphorus (P) is essential for all forms of life and cannot be substituted. It is one of the macro nutrients applied in form of mineral or organic fertilizers in agricultural crop production. Mineral P fertilizers are generally based on phosphate rock, a limited resource. Western Europe completely depends on imports as it has no own relevant phosphate mines. The most abundant phosphate deposits are located only in a few countries such as Morocco, China, South Africa and the United States of America. Furthermore, phosphate rock and as a consequence mineral P fertilizers are often contaminated with the toxic elements cadmium and uranium. In Order to substitute phosphate rock P-bearing waste streams are investigated for their potential to be recyded as fertilizers. Wastewater is one of the important P-bearing waste streams that were in the focus of research in the last 10 years. German wastewater is e.g. a carrier of approx. 70,000 t of phosphorus per year. T2 - International workshop on technospheric mining - Mining the technosphere - drivers and barriers, challenges and opportunities CY - Vienna, Austria DA - 01.10.2015 KW - Phosphorus recovery KW - Sewage sludge ash PY - 2015 SN - 978-3-85234-132-3 SP - 77 EP - 80 AN - OPUS4-34542 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - RPRT A1 - Adam, Christian A1 - Eicher, N. A1 - Hermann, L. A1 - Herzel, Hannes A1 - Mallon, J. A1 - Schaaf, M. A1 - Stemann, J. T1 - Comparative review of ash processes N2 - This report gives technological information about processes for the recovery of phosphorus from sewage sludge ash including mass- and energy balance, process conditions and product quality. The information in this report aim at giving an overview on different concepts for the recovery of phosphorus from sewage sludge ash and are intended to allow a general qualitative comparison between the different technical approaches. This report also describes the technological backgrounds of the processes that were furthermore investigated by life cycle assessment (LCA) and life cycle cost (LCC) analysis. However, most process data stated in this report are site specific data. The LCA/LCC study includes the definition of a common base line for all processes, detailed process modeling and plausibility assessments. Results of the LCA/LCC-studies are reported in deliverables D9.2 und D10.1. PY - 2015 UR - http://p-rex.eu/uploads/media/P-REX_D4_1_Comparative_review_of_ash_processes.pdf SP - 1 EP - 30 AN - OPUS4-34858 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Adam, Christian A1 - Herzel, Hannes A1 - Krüger, Oliver ED - Schuhmann, R. T1 - Technische Prozesse zur Phosphorrückgewinnung aus Klärschlammaschen N2 - Klärschlammaschen weisen hohe Gehalte an Phosphor auf, dieser ist allerdings schlecht für Pflanzen verfügbar. Des Weiteren enthalten sie Schwermetalle die vor dem Einsatz als Düngemittel entfernt werden müssen. Vor diesem Hintergrund wurden in den letzten Jahren nasschemische und thermochemische Verfahren entwickelt und zum Teil bereits in Demonstrationsanlagen getestet. Ein thermochemischer Verfahrensansatz wird in diesem Beitrag näher vorgestellt. Klärschlammaschen werden mit Klärschlamm als Reduktionsmittel und Natriumsulfat als Aufschlussmittel im Drehrohrofen thermisch behandelt. Bei diesem Prozess wird pflanzenverfügbares NaCaPÜ4 gebildet, unerwünschte Elemente wie As, Cd, Hg und Pb werden zum Teil über die Gasphase separiert. Die Ergebnisse eines Demonstrationsversuchs werden vorgestellt. N2 - Sewage sludge ashes exhibit high phosphorus mass fractions. However, the availability of phosphorus to plants is poor. Furthermore, sewage sludge ashes contain eco-toxicologically relevant heavy metals that have to be removed prior to agricultural application. ln front of this background several wet-chemical and thermo-chemical processes were developed in the last years and some of them were already successfully demonstrated in large scale. A thermo-chemical approach is presented in this article. Sewage sludge ashes are mixed with dry sewage sludge as reductant and sodium sulfate. Düring thermal treatment in a rotary kiln at approx. 950°C plant available NaCaPCU is formed. Furthermore undesired elements such as As, Cd, Hg and Pb are separated via the gas phase. Results of demonstration trials are presented. T2 - 8. CMM-Tagung 2015 - Innovative Feuchtemessung in Forschung und Praxis - Material - Prozesse - Systeme CY - Karlsruhe, Germany DA - 07.10.2015 KW - Klärschlammasche KW - Phoshorrückgewinnung PY - 2015 N1 - Serientitel: Innovative Feuchtemessung in Forschung und Praxis – Series title: Innovative Feuchtemessung in Forschung und Praxis SP - 251 EP - 262 AN - OPUS4-34859 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Herzel, Hannes A1 - Krüger, Oliver A1 - Adam, Christian T1 - Phosphorus fertilizer from sewage sludge ashes by thermochemical treatment - Benefits and challenges N2 - Mineral phosphorus (P) fertilizers are solely produced from phosphate rock. Europe completely depends on imports since there are no relevant phosphate rock deposits on the continent. Furthermore, phosphate rock is contaminated with heavy metals such as Cd and U that pollute the farmlands and pose environmental risks. Sewage sludge ash (SSA) might be a promising source for recycling fertilizer since it contains large amounts of P (up to 13 %). However, fertilizer from SSA has to comply with the respective ordinances, particularly the heavy metal limit values stated in the fertilizer ordinance, and requires sufficient P bioavailability. Thus, we conducted a complete survey of SSA from German mono-incineration facilities and developed a thermochemical treatment for SSA to reduce toxic elements and increase P bioavailability. T2 - RAMIRAN 2015 - 16th International conference Rural-Urban Symbiosis CY - Hamburg, Germany DA - 08.09.2015 PY - 2015 SN - 978-3-941492-95-0 SP - TA EP - O_20, 33 AN - OPUS4-34311 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Herzel, Hannes A1 - Krüger, Oliver A1 - Adam, Christian T1 - Phosphorus Fertilizer from Sewage Sludge Ashes by thermochemical treatment - Benefits and Challenges T2 - RAMIRAN 2015 - 16th International Conference Rural-Urban Symbiosis CY - Hamburg, Germany DA - 2015-09-08 PY - 2015 AN - OPUS4-34359 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Herzel, Hannes A1 - Adam, Christian A1 - ext. Stemann, Jan A1 - ext. Nättorp, Anders T1 - P-Recovery Technologies and Products T2 - P-REX workshop CY - Amsterdam, Netherlands DA - 2015-06-11 PY - 2015 AN - OPUS4-34360 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Herzel, Hannes A1 - Krüger, Oliver A1 - Hermann, L. A1 - Adam, Christian T1 - Sewage sludge ash - A promising secondary phosphorus source for fertilizer production N2 - Sewage sludge incineration is extensively practiced in some European countries such as the Netherlands, Switzerland, Austria and Germany. A survey of German sewage sludge ash showed that the recovery potential is high, approx. 19,000 t of phosphorus per year. However, the survey also discovered that the bioavailability of phosphorus in the sewage sludge ash is poor and that more than half of the ashes cannot be used as fertilizers due to high heavy metal content. A new thermochemical process for sewage sludge ash treatment was developed that transforms the ash into marketable fertilizer products. Sewage sludge ash was thermochemically treated with sodium and potassium additives under reducing conditions, whereby the phosphate-bearing mineral phases were transformed into plant available phosphates. High P-bioavailability was achieved with a molar Na/P ratio > 1.75 in the starting materials. Sodium sulfate, carbonate and hydroxide performed comparably as additives for this calcination process. Potassium carbonate and -hydroxide have to be added in a molar K/P ratio > 2.5 to achieve comparable P-solubility. The findings of the laboratory scale investigations were confirmed by an industrial demonstration trial for an ash treatment with sodium sulfate. Simultaneously, the volatile transition metal arsenic (61% removal) as well as volatile heavy metals such as cadmium (80%), mercury (68%), lead (39%) and zinc (9%) were removed via the off-gas treatment system. The product of the demonstration trial is characterized by high bioavailability and a toxic trace element mass fraction below the limit values of the German fertilizer ordinance, thus fulfilling the quality parameters for a P-fertilizer. KW - Sewage sludge ash KW - Phosphorus recovery KW - Thermochemical treatment KW - Reducing conditions KW - Heavy metal evaporation KW - Bioavailability KW - Sodium sulfate PY - 2016 U6 - https://doi.org/10.1016/j.scitotenv.2015.08.059 SN - 0048-9697 SN - 1879-1026 IS - 542 SP - 1136 EP - 1143 PB - Elsevier CY - Amsterdam AN - OPUS4-34165 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Herzel, Hannes A1 - Krüger, Oliver A1 - Adam, Christian T1 - Thermochemical treatment of sewage sludge ash for P-fertilizer production T2 - European Sustainable Phosphorus Conference 2015 CY - Berlin, Germany DA - 2015-03-05 PY - 2015 AN - OPUS4-32725 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - CONF A1 - Herzel, Hannes T1 - Phasenreaktionen bei der thermochemischen Behandlung von Klärschlammaschen mit Natrium- oder Kaliumverbindungen - Versuche mit Aschen und Modellsubstanzen T2 - DMG Workshop Sektion Angewandte Mineralogie in Umwelt und Technik CY - Bad Windsheim, Germany DA - 2015-02-25 PY - 2015 AN - OPUS4-32724 LA - deu AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER - TY - JOUR A1 - Huber, F. A1 - Herzel, Hannes A1 - Adam, Christian A1 - Mallow, O. A1 - Blasenbauer, D. A1 - Fellner, J. T1 - Combined disc pelletisation and thermal treatment of MSWI fly ash N2 - An environmentally friendly and cost efficient way for the management of municipal solid waste incineration (MSWI) fly ash represents its thermal co-treatment together with combustible waste. However, the safe introduction and storage of MSWI fly ash in the waste bunker is challenging and associated with severe problems (e.g. dust emissions, generation of undefined lumps and heat in case of moistened MSWI fly ash). Therefore, the aim of this study is to investigate the suitability of pelletisation as a pretreatment of MSWI fly ash. In particular, MSWI fly ash was characterised after sampling, pelletisation and thermal treatment and the transfer of constituents to secondary fly ash and flue gas was investigated. For this purpose, MSWI fly ash pellets with a water content of about 0.15 kg/kg and a diameter of about 8 mm have been produced by disc pelletiser and treated in an electrically heated pilot-scale rotary kiln at different temperatures, ranging from 450°C to 1050°C. The total contents of selected elements in the MSWI fly ash before and after thermal treatment and in the generated secondary fly ash have been analysed in order to understand the fate of each element. Furthermore, leachable contents of selected elements and total content of persistent organic pollutants of the thermally treated MSWI fly ash were determined. Due to the low total content of Hg (0.7 mg/kg) and the low leachate content of Pb (<0.36 mg/kg), even at the lowest treatment temperature of 450°C, thermally treated MSWI fly ash pellets can be classified as nonhazardous waste. However, temperatures of at least 650°C are necessary to decrease the toxic equivalency of PCDD/F and DL-PCB. The removal of toxic heavy metals like Cd and Pb is significantly improved at temperatures of 850°C, 950°C or even 1050°C. The observed metal removal led to relatively high contents of e.g. Cu (up to 11,000 mg/kg), Pb (up to 91,000 mg/kg) and Zn (up to 21,000 mg/kg) in the secondary fly ash. This metal enriched secondary fly ash might represent a potential raw material for metal recovery (e.g. via acidic leaching). Due to the high content of total dissolved solids observed in the leachate of thermally treated MSWI fly ash pellets, a wet extraction procedure is suggested to enable its safe disposal at non-hazardous waste landfills. KW - MSWI fly ash KW - Thermal treatment PY - 2018 U6 - https://doi.org/10.1016/j.wasman.2017.12.020 SN - 0956-053X VL - 73 SP - 381 EP - 391 PB - Elsevier Ltd. CY - Rotterdam AN - OPUS4-44481 LA - eng AD - Bundesanstalt fuer Materialforschung und -pruefung (BAM), Berlin, Germany ER -