4.4 Thermochemische Reststoffbehandlung und Wertstoffrückgewinnung
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- 4.4 Thermochemische Reststoffbehandlung und Wertstoffrückgewinnung (93) (entfernen)
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In Deutschland ist ab 2029 eine Phosphorrückgewinnung aus Klärschlamm verpflichtend. Ausgenommen sind Klärschlämme mit weniger als 20 g P/kg TM. Für die Phosphorbestimmung sind verschiedene Methoden nach Klärschlammverordnung als gleichwertig zugelassen: Der Königswasseraufschluss in der Mikrowelle und am Rückfluss sowie die Messung an ICP-OES, ICP-MS und die photometrische Bestimmung mittels Ammoniummolybdaten. An der BAM wurden die unterschiedlichen Methodenkombinationen aus Aufschluss- und Messmethode an 15 Klärschlämmen überprüft und in einem Ringversuch mit einem Klärschlamm getestet. Die Ergebnisse werden in diesem Vortrag zusammengefasst. Als Folge der Untersuchungen wird für die Phosphorbestimmung in Klärschlamm die ICP-OES-Messung nach Königswasseraufschluss in der Mikrowelle empfohlen.
Der Vortrag liefert eine Zusammenfassung der wichtigsten Ergebnisse des extraWERT-Vorhabens mit Schwerpunkt auf den Umsetzungsfragen zur Klärschlammverordnung. Bei diesen Punkten handelt es sich um die Untersuchung von monatlichen Phosphorschwankungen in kommunalem Klärschlamm und die Gleichwertigkeit verschiedener Verfahren zur Phosphorbestimmung in Klärschlamm.
Die Zementindustrie und weitere energieintensive Industrien wie etwa die Stahlindustrie stehen vor dem Hintergrund der Transformation unserer Gesellschaft zur Klimaneutralität vor erheblichen Herausforderungen. Ziel dieser Branchen ist perspektivisch die vollständige Vermeidung klimaschädlicher Emissionen – mit besonderem Fokus auf Kohlendioxid. Neben der Umstellung auf regenerative Energieträger, sind im Speziellen für die Zementindustrie die erheblichen Anteile an CO2-Emissionen durch die Entsäuerung von Kalkstein zukünftig zu vermeiden. Da die hervorragenden Bindemitteleigenschaften des bisher hauptsächlich in Zementen eingesetzten Portlandklinkers jedoch auf Calciumverbindungen wie Tri- und Di-calciumsilikaten basieren, stellt die Substitution des Kalks derzeit für die Zementindustrie die größte Herausforderung dar. Neben vollständig neuen Bindemittelsystemen ohne Verwendung von Kalk und CCS/CCU-Technologien zur Vermeidung der CO2-Emissionen bei Verwendung von Kalk, können Abfälle und Nebenprodukte wie etwa Betonbrechsand, verschiedene Schlacken und weitere Massenreststoffe sinnvoll zur Einsparung von Rohstoffen und zur Vermeidung von CO2-Emissionen eingesetzt werden. Es gilt diese Potentiale von Sekundärrohstoffen branchenübergreifend zu identifizieren und Synergien zwischen den Branchen nutzbar zu machen. Hierbei werden neben der chemischen Zusammensetzung der Abfälle und Nebenprodukte auch die Verfügbarkeit und der Massenstrom relevante Kriterien sein. Die potenziellen Sekundärrohstoffe und deren Gemische mit chemisch ähnlicher Zusammensetzung wie die bisher verwendeten Bindemittel, können durch verschiedene technische Ansätze wieder in reaktive Bindemittel umgewandelt und damit nutzbar gemacht werden. Eine gezielte Umwandlung der nicht reaktiven mineralischen Phasen in neue mineralische Phasen mit guten Bindemitteleigenschaften, kann u. a. durch Schmelzprozesse erzielt werden. In Schmelzen können bei hohen Temperaturen die bestehenden, nicht reaktiven mineralischen Phasen zerstört und neue mineralische Phasen mit guten Bindemitteleigenschaften erzeugt werden. Hohe Freiheitsgrade durch gezielte Einstellung der stofflichen Zusammensetzung der Schmelze, durch Stoffseparationen und durch geregelte Abkühlregimes können eine maßgeschneiderte Erzeugung neuer Bindemitteltypen ermöglichen. Aufgrund der hohen erforderlichen Temperaturen von Schmelzprozessen ist die Umsetzung dieser neuen Verfahren nach Möglichkeit in bestehenden pyrometallurgischen Produktionsrouten wie etwa der Stahlproduktion vorzunehmen. So kann etwa der Einsatz von Betonbrechsand als Schlackebildner in der Stahlproduktion zielführend sein, wenn die Schlacke wieder zu einem Bindemittel prozessiert wird und in Zementen Verwendung findet. Eine stoffliche Kreislaufführung wäre hiermit gegeben, wobei der Einsatz von Kalkstein als Schlackebildner oder Rohstoff für die Zementproduktion, und damit die entsprechenden CO2-Emissionen, vermieden werden. Die Entwicklung neuartiger Bindemittelsysteme auf Basis von Sekundärrohstoffen sollte von erforderlichen Anpassungen und neuen Entwicklungen in der Regelsetzung und Normung begleitet werden. Vor allem muss gewährleistet sein, dass die mit neuen Bindemitteln hergestellten Betone den hohen Anforderungen an Dauerhaftigkeit und Umweltverträglichkeit genügen. Des Weiteren sollte mit den etablierten Methoden, wie etwa der Lebenszyklusanalyse, untersucht werden, inwiefern und in welchem Umfang die neuen technischen Entwicklungen zu Nachhaltigkeit und Klimaschutz beitragen.
Klärschlammaschen können eine hohe Phosphatkonzentration aufweisen und stellen damit einen geeigneten Sekundärrohstoff für die Produktion von Phosphatdüngemitteln dar. Bisher wird dieses Potential der Klärschlammaschen für die Phosphor-Rückgewinnung jedoch kaum genutzt, da die in den Aschen enthaltenen Phosphate für Pflanzen kaum verfügbar und die Aschen teilweise mit toxischen Schwermetallen belastet sind.
Im AshDec®-Verfahren wird die Klärschlammaschen im Drehrohrofen im Temperaturbereich 800-1000°C unter Zugabe von Alkali-Additiven (bsp. Na2CO3) thermochemisch behandelt, um ein wirksames und schadstoffarmes Phosphatdüngemittel herzustellen. Aktuell bereitet die Firma Emter GmbH den Bau der ersten großtechnischen AshDec®-Anlage mit einer Kapazität von 30.000 Jahrestonnen Klärschlammasche am Standort ihrer Klärschlammverbrennungsanlage (Altenstadt / Oberbayern) vor. Die erste Ausbaustufe dieser Anlage wird durch das BMBF-Projekt R-Rhenania im Rahmen der Förderinitiative RePhoR begleitet.
Dust deposition is an important source of phosphorus (P) to many ecosystems. However, there is little evidence of dust-derived P-containing minerals in soils. Here we studied P forms along a well-described climatic gradient on Hawaii, which is also a dust deposition gradient. Soil mineralogy and soil P forms from six sites along the climatic gradient were analyzed with bulk (X-ray diffraction and P K-edge X-ray absorption near edge structure)
and microscale (X-ray fluorescence, P K-edge X-ray absorption near edge structure, and Raman) analysis methods. In the wettest soils, apatite grains ranging from 5 to 30 μm in size were co-located at the micro-scale with quartz, a known continental dust indicator suggesting recent atmospheric deposition. In addition to colocation with quartz, further evidence of dust-derived P included backward trajectory modeling indicating that dust particles could be brought to Hawaii from the major global dust-loading areas in central Asia and northern Africa. Although it is not certain whether the individual observed apatite grains were derived from long-distance transport of dust, or from local dust sources such as volcanic ash or windblown fertilizer, these observations offer direct evidence that P-containing minerals have reached surface layers of highly-weathered grassland soils
through atmospheric deposition.
Thermochemische Behandlung von Klärschlammaschen - Phosphorrückgewinnung mit dem AshDec Prozess
(2021)
Klärschlammaschen können eine hohe Phosphatkonzentration aufweisen und stellen damit einen geeigneten Sekundärrohstoff für die Produktion von Phosphatdüngemitteln dar. Bisher wird dieses Potential der Klärschlammaschen für die Phosphor-Rückgewinnung jedoch kaum genutzt, da die in den Aschen enthaltenen Phosphate für Pflanzen kaum verfügbar und die Aschen teilweise mit toxischen Schwermetallen belastet sind.
Im AshDec®-Verfahren wird die Klärschlammaschen im Drehrohrofen im Temperaturbereich 800-1000°C unter Zugabe von Alkali-Additiven (bsp. Na2CO3) thermochemisch behandelt, um ein wirksames und schadstoffarmes Phosphatdüngemittel herzustellen. Aktuell bereitet die Firma Emter GmbH den Bau der ersten großtechnischen AshDec®-Anlage mit einer Kapazität von 30.000 Jahrestonnen Klärschlammasche am Standort ihrer Klärschlammverbrennungsanlage (Altenstadt / Oberbayern) vor. Die erste Ausbaustufe dieser Anlage wird durch das BMBF-Projekt R-Rhenania im Rahmen der Förderinitiative RePhoR begleitet.
Gleichwertigkeit der nach AbfKlärV zulässigen Verfahren zur Phosphorbestimmung in Klärschlamm
(2021)
In dem Meeting wurde den Notifizierern und Ausrichtern des jährlichen länderübergreifenden Ringversuchs Klärschlamm die Ergebnisse zu Untersuchungen hinsichtlich der Gleichwertigkeit verschiedener nach AbfKlärV zulässiger Verfahren zur Phosphorbestimmung in Klärschlamm vorgestellt. Die Untersuchungen an 15 Klärschlammproben ergaben die höchsten Ergebnisse für das Messverfahren ICP-OES und das Aufschlussverfahren in der Mikrowelle. Diese Ergebnisse wurden im Ringversuch bestätigt.
Die Ergebnisse des extraWERT-Vorhabens wurden Vertreter*innen des Umweltministeriums von Bund und Ländern vorgestellt und im Zusammenhang mit dem Vollzug der AbfKlärV diskutiert. Es ging um die Phosphorschwankungen in kommunalem Klärschlamm und eine Empfehlung der Untersuchungshäufigkeit, um den Phosphorgehalt rechtssicher festzustellen. Des weiteren wurde die Performance verschiedener nach Verordnung gleichwertiger Analyseverfahren für Phosphor in Klärschlamm diskutiert anhand von Ringversuchsergebnissen und Eigenuntersuchungen an 15 Klärschlammproben.
Agricultural sewage sludge utilization becomes less important in Germany. In 2017, new fertilizer and waste laws caused the agricultural sewage sludge utilization to collapse by more than a quarter. From 2029, in German wastewater treatment plants (WWTPs) phosphorus (P) must be recovered from sewage sludge ifit contains more than 2 wt % P. Agricultural utilization will be prohibited for large WWTPs > 100,000 population equivalents (pe) from 2029 and > 50,000 pe from 2032. In Germany, each federal state must annually report amounts and quality of agriculturally utilized sewage sludge which was 17 % of the total disposal in 2019. The reports of 10 States were evaluated for 2016 and 2017 representing approx. 60 % ofthe total agriculturallyused sludge volume. Whereas phosphorus recovery is mandatory this does not apply to other nutrients. However, many P recovery processes recover other nutrients, too. Considering three differentscenariosfor future German sewage sludge disposal shows that 70 - 77 % ofthe P load in sewage sludge will probably be recovered in the future. At the same time, this applies for about 0 - 16 % of nitrogen, 36 - 52 % of calcium, 31-53 % of potassium, and 40 - 52 % of magnesium. However, these recovered nut rient loads can substitute only 1 % or less ofthe commercial fertilizer demand except from phosphorus which is about 45 % ofthe demand.
Phosphorus (P) fertilizers from secondary resources became increasingly important in the last years. However, these novel P-fertilizers can also contain toxic pollutants. Chromium in its hexavalent state (Cr(VI)) is regulated with low limit values for agricultural products due to its high toxicity, but the determination of Cr(VI) in these novel fertilizer matrices can be hampered by redox processes that lead to false results. Thus, we applied the passive sampler technique Diffusive Gradients in Thin-films (DGT) for the determination of Cr(VI) in fertilizers and compared the results with the standard wet chemical extraction method (German norm DIN EN 15192) and Cr K-edge X-ray absorption near-edge structure (XANES) spectroscopy. We determined an overall good correlation between the wet chemical extraction and the DGT method. DGT was very sensitive and in most cases selective for the analysis of Cr(VI) in P-fertilizers. However, hardly soluble Cr(VI) compounds cannot be detected with the DGT method since only mobile Cr(VI) is analyzed. Furthermore, Cr K-edge XANES spectroscopy showed that the DGT binding layer also adsorbs small amounts of mobile Cr(III) compounds which leads to overestimated Cr(VI) values. The results of certain types of P-fertilizers containing mobile Cr(III) or partly immobile Cr(VI), showed that optimization of the DGT method is required to avoid over- or underestimation of Cr(VI).
The aim of this study was to investigate the passive sampler method Diffusive Gradients in Thin-films (DGT) for ammonium and nitrate in amended soils. Therefore, we used soils from a pot experiment with maize where nitrogen (N) was supplied as ammonium sulfate nitrate (ASN), without and with a nitrification inhibitor (NI). The additional use of a NI can delay the nitrification in the soil and making the ammonium available for a longer period in the soil solution after its application. Homogenized soil samples were collected directly from each pot after one week of incubation before sowing and after harvesting the maize. Nitrate and ammonium in these soil samples were extracted using DGT devices equipped with a Putolite A520E (for nitrate) and Microlite PrCH (for ammonium) binding layer. Ammonium DGT which determined the mobile and labile ammonium forms based on diffusion and the resupplies from the solid soil phase, only showed a significantly higher amount of extractable ammonium with NI compared to that without NI for some samples. However, significantly lower values were found for nitrate of treatments with NI compared to without NI after harvest. Thus, the lower nitrate amounts for treatments with NI compared to the treatments without NI after harvest indicated the delay of the nitrification process by the NI. Furthermore, we compared also the ammonium and nitrate
DGT results to chemical extraction with KCl solutions. The results demonstrated that the trends of DGT results and chemical extraction were complimentary through all the treatments.
Gypsum is widely used in the construction sector, and its worldwide consumption has been increasing now for several decades. Currently, the gypsum demand is met up to 60% by FGD gypsum (a by-product from coal-fired power plants) in Germany. The natural gypsum deposits cover the remaining gypsum demand. Due to national climate protection goals and the related shutdown of coal-fired power plants, the FGD gypsum supply will decrease significantly in the coming years and, therefore, other gypsum sources must be found.
Depending on the lifetime of the used gypsum products in the construction sector, an increase of gypsum in construction and demolition waste is to be expected. With regard to an upcoming shortage of gypsum, several approaches are being tested to recover gypsum from construction and demolition waste. Gypsum plasterboard recycling is already implemented on an industrial scale. Furthermore, new processes to recycle different types of gypsum products from construction and demolition waste are being examined. Of particular interest are different types of gypsum boards because they are well suited for selective dismantling. Therefore, they can be recovered comparatively free of impurities which is most important for the gypsum recycling.
In the research project “GipsRec 2.0”, funded by the Federal Ministry of Education and Research, recycling methods for gypsum fiberboards are being investigated. Additionally, the suitability of different types of synthetic gypsum as substitutes for FGD gypsum is being considered. Currently, the quantities of recycled gypsum are not sufficient with regard to the reduction of FGD gypsum. An increase of gypsum recycling should be achieved to narrow the future gypsum gap that will occur in the near future.
CF Pyro: Stofflich-energetische Verwertung von carbonfaserhaltigen Abfällen in der Pyrometallurgie
(2021)
Despite its contribution to tackling climate change by lightweight design, growing CFRP production also results in a global waste generation of 62 kt/a. Accordingly, the energy-intensive production process of carbon fibers (CF) necessitates sustainable recycling solutions.
Herein we will give an overview of current recycling processes, discuss their limitations and present a novel approach for safe treatment of CF unsuitable for material recovery . Our project CF Pyro examines feedstock recycling in pyrometallurgical processes, focusing on reactivity of CF, process stability and prevention of hazardous WHO fiber release. Besides fundamental experimental breakthroughs, their broader impact on circular economy will be presented.
Basic oxygen furnace slag (BOFS) is a by-product of the steelmaking process, of which about 10.4 Mt are produced annually in the European Union. Besides its predominant use in road construction, earthwork, and hydraulic engineering, it is also possible to use BOFS as a source material for Portland cement clinker.
The main difference in the chemical composition of BOFS from the chemical composition of Portland cement clinker is its high content of iron oxides (7-50 wt.%). In recent decades, many researchers have investigated the production of both Portland cement clinker and crude iron from BOFS via thermochemical reductive treatment. Carbothermal treatment of liquid BOFS causes reduction of iron oxides to metallic iron, which separates from the mineral phase due to its higher density.
In this study, German BOFS was reduced in a small-scale electric arc furnace using petrol coke as reducing agent. The produced low-iron mineral product was chemically similar to Portland cement clinker and contained the most important Portland cement mineral alite (Ca3SiO5) as main component. Besides alite, the mineral product contained other Portland cement clinker constituents such as belite (β-Ca2SiO4) and tricalcium aluminate (Ca3Al2O6).
The production of Portland cement clinker and crude iron from BOFS has economic and ecological benefits for both the cement and steel industry. Cement clinker from reduced BOFS may be used as a substitute for cement clinker from conventional cement production, thereby CO2 emissions will be reduced. The steel industry benefits from a high-value application for its by-products that avoids cost expensive landfilling and may even bring economic advantages. However, reductive treatment requires high temperatures and, for economic reasons, has to be carried out immediately after casting of the liquid BOFS, which is a logistical challenge for most steel plants. A cost-benefit analysis is therefore essential.
Basic oxygen furnace slags (BOFS) are a by-product of steel production. In 2016, 10.4 Mt of BOFS were produced in the European Union (EU). The main part of BOFS is used in road construction, earthwork and hydraulic engineering. A smaller part is returned to the metallurgical circle, used as fertilizer or landfilled. However, it is also possible to produce higher value products from BOFS. For example, many researchers have investigated the possibility of producing Portland cement clinker and crude iron from BOFS by a carbothermal post-treatment.
In this study, German BOFS was reduced in a small-scale electric arc furnace using petrol coke as reducing agent. The carbothermal treatment reduces the iron oxides in the BOFS to metallic iron, which accumulates at the bottom of the furnace by density separation. In addition to metallic iron, the process generates a mineral product rich in the tricalcium silicate solid solution alite. As the main constituent of Portland cement clinker, the hydraulic reactive mineral alite is of high economic importance.
In previous studies, the hydraulic reactivity of the mineral product was investigated by testing the compressive strength of blends with 70 wt.% ordinary Portland cement (OPC). Recent investigations focused on the hydraulic properties of the pure mineral product from the reduced BOFS. The heat of hydration of the mineral product was measured by isothermal calorimetry and compared with the heat of hydration of a synthetic low-iron slag and OPC. In addition, the formation of hydration products was investigated with differential scanning calorimetry (DSC) and x-ray diffraction analysis (XRD) on freeze-dried samples after defined curing times. The results of the calorimetric measurements indicate that the mineral product produced less heat of hydration and its reaction was delayed compared to the synthetic low-iron slag and OPC. Hydration products such as portlandite and calcium silicate hydrates (C-S-H) formed later and in lower amounts.
The production of a hydraulic material from BOFS by reductive treatment is of great interest to both the cement and steel industries. The substitution of cement clinker in OPC with a hydraulic material such as reduced BOFS leads to a reduction in greenhouse gas emissions from cement production. The steel industry benefits from an application for its by-products that avoids cost expensive landfilling and may even bring economic advantages. Furthermore, it may be possible to return the recovered crude iron to production.
During iron and steel production, several by-products such as slags, dusts and sludges are generated in addition to pig iron and steel as primary products. While established recycling routes exist for slags, there are still considerable recycling problems for other residual materials, especially for filter dusts and sludges containing zinc and lead from waste gas purification. However, the high heavy metal contents make landfilling these dusts and sludges cost-intensive and ecologically problematic. In addition, the relatively high zinc and iron loads represent a valuable material potential, which can make reprocessing of the material with recovery of the zinc and iron loads as secondary raw materials ecologically as well as economically attractive. Against this background, a process is being developed in a cooperative project between Ferro Duo GmbH and the Federal Institute for Materials Research and Testing (BAM), in which the heavy metals (zinc, lead, cadmium, etc.) contained in the filter dusts and sludges are selectively converted into chlorides in a thermochemical process after the addition of a chlorine donor and evaporated at temperatures between 650 and 1100 °C. This process can be used to recover zinc and iron as secondary raw materials.
Experiments to date in a batch reactor show that >99% of the zinc and lead can be removed from the treated material. However, a continuous process is necessary for an economical process, which is why this process is transferred to a rotary kiln and relevant process parameters are identified and optimized. The results of these investigations will be presented here.
Despite its contribution to tackling climate change by lightweight design, growing CFRP production also results in a global waste generation of 62 kt/a. Accordingly, the energy-intensive production process of carbon fibers (CF) necessitates sustainable recycling solutions.
Herein we will give an overview of current recycling processes, discuss their limitations and present a novel approach for safe treatment of CF unsuitable for material recovery . Our project CF Pyro examines feedstock recycling in pyrometallurgical processes, focusing on reactivity of CF, process stability and prevention of hazardous WHO fiber release. Besides fundamental experimental breakthroughs, their broader impact on circular economy will be presented.
Recycled fertilizers produced using processes for the recovery of phosphate from residual materials such as wastewater, sewage sludge and sewage sludge ashes show very good bioavailability, but it is still a product largely unknown to the market. The aim of CLOOP is therefore to document the properties and effects of such fertilizers through chemical, mineralogical and ecological analyses as well as analytical method development and pot and field plant growth trials.
Outotec focused on 3 points in CLOOP: Experimental campaigns, process simulations as well as economic analyses with focus on the AshDec process, respectively the design of a large-scale AshDec plant for phosphorus recovery. The laboratory scale trials as well as the semi-industrial scale campaign provided valuable insights into the operating parameters of the process and the plant. As a result, for example, the temperature range could be significantly lowered, and the additive addition reduced by approx. 20 %. They have further shown that the AshDec process is not susceptible to operating fluctuations and that the product can be consistently produced at high quality. With the selection of suitable operating parameters, heavy metals (As, Pb, Cd, (Zn)) can be removed. Within the campaign, about 1.5 t of fertilizer for the plant trials in CLOOP could be produced. An AshDec plant process was digitally created in simulation software, allowing valuable process parameters to be simulated at various operating parameters. On this basis, a full-scale plant was designed. The data obtained in the project were used for a detailed economic analysis including a sensitivity analysis. It was possible to show under which conditions this plant can be operated economically.
At BAM, the AshDec fertilizer was synthesized with different additives and then applied to plant experiments at Uni Bonn. The goal hereby was to check differences in plant uptake. Because of the promising results of AshDec synthesized with sodium-carbonate and because this AshDec version does not require special off gas treatment for sulfur recovery (compared to AshDec synthesized with sodium-sulfate), all project partners agreed on continuing working with this AshDec variation. It was then used as a raw P-source for formulating it into NPK-fertilizers, by granulation with ammonium-sulfate and straw ash as potassium source. These recycling fertilizers were applied to plant- and field experiments by project partners in Brazil (University of Sao Paulo) and Australia (University of Queensland). Furthermore, in leaching experiments, the solubility of phosphorus in AshDec was compared to triple super phosphate. The experiments were carried out on soils with a varying phosphorus buffering index. Results show, that the phosphorus form in AshDec is way less soluble in water. This indicates that AshDec has the potential for a so-called next generation fertilizer – a fertilizer which’s nutrients remain in the soil and supply the plant according to its needs. At the moment, this behavior gets examined more in depth in lysimeter experiments in cooperation with University of Technology Berlin.
The focus of KWB is the Life Cycle Assessment (LCA) of different NextGen fertilizers to evaluate the entire process chain from recovery to fertilizer application. The NextGen fertilizer is credited by the amount of plant available nutrients in the product, which replace nutrients from conventional fertilizer. The LCA covers N-struvite precipitation from municipal wastewater, K-struvite precipitation from industrial wastewater and the AshDec-product from sewage sludge. The LCA task is almost complete. It could be shown that struvite precipitation has comprehensive environmental benefits, mainly since positive side effects occur in sewage sludge treatment (e.g. reduced sludge volume). In principle, the energetic and ecological profile of the AshDec process compared to direct use of sewage sludge ash cannot be assessed as being generally beneficial or negative. Regarding the global warming potential, the Ashdec process shows that the expenses (e.g. energy, chemicals) cannot be covered by the P fertilizer credit. In contrast, the impact categories “terrestrial acidification potential”, and “freshwater eutrophication potential” show positive results as the credits for conventional fertilizer are higher than the burdens for the process.
At University Bonn, the standardized pot experiments were conducted with several AshDec variations, using ryegrass, soybean, and spinach on a slightly acidic sandy soil and an organic-free standard substrate. P-uptake and biomass production of different AshDec variations were generally like those of triple super phosphate and struvite, and clearly outperformed untreated sewage sludge ash and rock phosphate. Field trials in Australia and Brazil with sugarcane on acidic soils are still ongoing and results are expected by the end of 2021.