Wądrzyk, Mariusz
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inżynieria chemiczna
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Item type:Article, Access status: Open Access , Benefits from co-pyrolysis of biomass and refuse derived fuel for biofuels production: experimental investigations(2024) Magdziarz, Aneta; Jerzak, Wojciech; Wądrzyk, Mariusz; Sieradzka, Małgorzata
Wydział Inżynierii Metali i Informatyki PrzemysłowejThe application of renewable fuels and waste for energy production is crucial environmentally and economically. Co-pyrolysis of biomass and refuse derived fuel (RDF) offers a promising pathway for valuable products that combine various benefits including enhanced energy recovery, waste valorisation, improved product quality, and environmental sustainability. Consideration of specific feedstocks and optimization of process parameters are necessary to maximise the efficiency and effectiveness of the co-pyrolysis process. This work presents investigations of the co-pyrolysis process of lignocellulosic biomass wastes (rye straw and agriculture grass) and RDF. These biomasses ensure efficient decomposition. The RDF, high in carbon (78.5 %) and hydrogen (11.8 %), was predominantly plastic based. Based on Py-GC-MS studies at 600°C, it was observed that the addition of RDF to biomass caused a significant decrease in the share of organic oxygen compounds among the released decomposition products. Laboratory tests were performed in a fixed-bed reactor for raw biomass and RDF and 1:1 and 3:1 biomass to RDF mass ratio. The results demonstrated that the yield of char production decreased with the addition of RDF, which promoted the bio-oil yield. Despite, RDF pyrolysis meets problems, it was proved that co-pyrolysis of biomass and RDF is a good solution for their utilization.Item type:Article, Access status: Open Access , The application of a drop-tube reactor for fast pyrolysis of agricultural biomass: an effective way to valuable products(2024) Bieniek, Artur; Sieradzka, Małgorzata; Wądrzyk, Mariusz; Jerzak, Wojciech; Magdziarz, Aneta
Wydział Inżynierii Metali i Informatyki PrzemysłowejThis paper presents experimental investigations of the fast pyrolysis of three agricultural biomass feedstocks in a drop-tube reactor (DTR) focusing on the production of bio-oil. Studying oat straw, corn straw, and rape straw allowed to optimize the use of diverse agricultural waste streams. The application of DTR with specially designed geometry and sample feeder gave information about pyrolysis conditions that can be helpful in the design of industrial-scale pyrolysis. The physical and chemical properties of feedstocks and received products using advanced instrumental techniques were determined. The yields of bio-oil were the highest during fast pyrolysis of studied biomass and were as follows: 53.2%, 51.28% and 49.11% for oat straw, corn straw and rape straw, respectively. The bio-oils were composed mainly of oxygen-containing compounds, with a dominant share of acids and phenols. It means that obtained bio-oils require upgrading their properties such as energy density and storage stability. The bio-chars were characterised by a high-energy density containing 60-70 wt.% carbon content giving carbon materials with a wide range of possible applications such as energy storage, absorbents and catalysts. The received pyrolytic gas was mostly composed of CO and CO2, and around 10% of hydrogen proving that it is possible to obtain pyrolysis-derived syngas as a source of energy. This research demonstrates the potential of using DTR for fast pyrolysis of agriculture residues aligning with the circular economy concept and contributing valuable knowledge for industrial applications.Item type:Article, Access status: Open Access , Valorisation of tyre waste from a vulcanisation plant by catalytic pyrolysis – Experimental investigations using pyrolysis–gas chromatography–mass spectrometry and drop-tube–fixed-bed reactor(2024) Jerzak, Wojciech; Wądrzyk, Mariusz; Sieradzka, Małgorzata; Magdziarz, Aneta
Wydział Inżynierii Metali i Informatyki PrzemysłowejThis study focuses on the use of car tyre waste collected at a tyre repair station in Krakow (Poland). Waste from damaged tyres is disposed of as municipal solid waste. Therefore, the management of waste tyres already shredded by pyrolysis at 500 °C has been proposed. Tyre waste was hypothesised to be converted into valuable chemical products by pyrolysis in a hybrid reactor (drop-tube–fixed-bed reactor). On a micro scale, pyrolysis–gas chromatography–mass spectrometry was used to analyse the pyrolysis process. It has been shown that the formation of aromatic hydrocarbons during pyrolysis clearly depends on whether the catalyst and tyre waste are mixed together or arranged in layers. Since the layered arrangement favoured the formation of hydrocarbons, such a system was used in the drop-tube–fixed-bed reactor. The high heating rate (500 °C/s) of tyre particles in the drop-tube–fixed-bed reactor at 500 °C allowed for the obtained a raw carbon black yield of 40.8 %. A similar yield of raw carbon black determined by thermogravimetric analysis for a heating rate of 0.17 °C/s) was observed at 800 °C. However, before commercial use, raw carbon black requires demineralisation because of its high ash content (approximately 50 %). The raw carbon black ash contained up to 90 % $SiO_{2}$, indicating that it could be a valuable catalyst material. Pyrolysis of tyre waste over the catalyst reduced the oxygen content in the oil and yield. The oil yields of tyre pyrolysis without a catalyst and over zeolite Y were 38 wt% and 35 wt%, respectively. The main components identified in the tyre pyrolysis gas were methane (27.6%), ethene (28.8%), and hydrogen (15.6%). The gas from catalytic pyrolysis was richer in CO and $CO_{2}$.Item type:Article, Access status: Open Access , Comparative study of grass pyrolysis over regenerated catalysts: Tyre ash, zeolite, and nickel-supported ash and zeolite(2024) Jerzak, Wojciech; Sieradzka, Małgorzata; Wądrzyk, Mariusz; Magdziarz, Aneta
Wydział Inżynierii Metali i Informatyki PrzemysłowejThis paper presents investigations on catalytic and non-catalytic grass pyrolysis conducted at 500 °C using two reactor scales: a micro-scale reactor and a laboratory fixed-bed reactor. Four catalysts were employed in the catalytic pyrolysis process: car tyre ash, commercial zeolite mordenite-sodium, nickel supported on ash, and nickel supported on zeolite. The use of catalysts reduced the production of oxygenates and promoted the formation of gaseous compounds, with the most pronounced effect observed for nickel supported on zeolite. Catalytic pyrolysis produced chars with yields that were higher than those of the non-catalytic process. The coking behaviour of the spent catalysts was evaluated by analysing carbon content, with the highest content (3 wt% C) obtained for ash after the first cycle. In the second cycle, the deposited carbon content decreased for all catalysts. Furthermore, the employment of catalysts was shown to promote the production of hydrogen, methane, and other hydrocarbons in pyrolysis gas. The higher heating value of the pyrolysis gas was the highest at 21.1 MJ/m³ when the ash catalyst was first used for pyrolysis. Reusing the pyrolysis catalysts slightly reduced the heating value of the gas to 20.3 MJ/m³ over ash and 20.6 MJ/m³ over zeolite.