Zusammenfassung
Die Vergasung ist als thermochemischer Konversionsprozess sehr komplex. Neben chemischen Reaktionen, die endotherm und exotherm, homogen und heterogen sein können, sind Stoff‐ und Wämetransportvorgäge entscheidend fü den Vergasungsfortschritt. Die heterogenen Reaktionen zur Umsetzung des Kokses spielen dabei eine besondere Rolle, da sie relativ langsam ablaufen. Ausgehend von der Vorstellung grundlegender Vergasungsmodelle und der experimentellen Ermittlung reaktionskinetischer Parameter werden Zusammenhäge zwischen Porenstrukturveränderungen wärend der Koksvergasung und der Reaktionskinetik betrachtet. Ein weiterer behandelter Aspekt ist die experimentelle Untersuchung der Co‐Vergasung von biogenen Energierohstoffen mit Braunkohlen sowie des Vergasungsverhaltens von Zwischenprodukten einer thermochemischen Veredlungskette, in vorliegenden Fall von Koks aus der katalytischen Pyrolyse. Abschließend wird ein fortschrittliches kinetisches Modell zur Beschreibung der Koksumsetzung vorgestellt und Möglichkeiten zur Kopplung dieses Modells mit CFD-Anwendungen präsentiert. Mittels numerischen Untersuchungen wird der Einfluss von Wärme‐ und Stofftransportprozessen in der Grenzschicht und den Partikelporen bzw. die Wechselwirkungen zwischen Gasströmung und reaktivem Partikel analysiert.
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Notes
- 1.
1 Der Fehler bezüglich der Reaktionsgeschwindigkeit r‘‘(U=0,5) beträgt ± 1,57E-04 1/s
- 2.
2 Der Fehler bezüglich dem Reaktivitätsindex RS0,5 beträgt ± 0,18 1/h (Die aufgeführten Fehler wurden anhand von 10 Wiederholungsmessungen in der METTLER-TGA ermittelt)
- 3.
3 Für die folgenden Betrachtungen werden für die Standard- bzw. Vergleichsprobe A Mittelwerte aus den Proben A.1 und A.2 (WDH) verwendet
- 4.
4 Das Verhältnis zwischen SiO2 und Al2O3 wird allgemein als Modul bezeichnet [47]
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Rußig, S. et al. (2018). Vergasung. In: Krzack, S., Gutte, H., Meyer, B. (eds) Stoffliche Nutzung von Braunkohle. Springer Vieweg, Berlin, Heidelberg. https://doi.org/10.1007/978-3-662-46251-5_20
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