Las cookies nos ayudan a ofrecer nuestros servicios. Al utilizar nuestros servicios, aceptas el uso de cookies.

Editorial Cuvillier

Publicaciones, tesis doctorales, capacitaciónes para acceder a una cátedra de universidad & prospectos.
Su editorial internacional especializado en ciencias y economia

Editorial Cuvillier

De En Es
Dynamic Simulation of the Chemical Looping Combustion Process

Impresion
EUR 49,90

E-Book
EUR 34,99

Dynamic Simulation of the Chemical Looping Combustion Process (Volumen 17) (Tienda española)

Johannes Haus (Autor)

Previo

Indice, PDF (160 KB)
Lectura de prueba, PDF (900 KB)

ISBN-13 (Impresion) 9783736973350
ISBN-13 (E-Book) 9783736963351
Idioma Inglés
Numero de paginas 140
Laminacion de la cubierta mate
Edicion 1
Serie SPE-Schriftenreihe
Volumen 17
Lugar de publicacion Göttingen
Lugar de la disertacion TU Hamburg
Fecha de publicacion 09.12.2020
Clasificacion simple Tesis doctoral
Area Ingeniería mecánica y de proceso
Allgemeine Verfahrenstechnik
Descripcion

In this Ph.D. thesis a system of coupled fluidized bed reactors is modelled and simulated dynamically. Chemical Looping Combustion was used as an exemplary process in both the numerical and the experimental part of this work. For the simulation purpose a novel flowsheeting software was used and models for the needed process units developed and integrated into this software. The needed unit models were three interconnected fluidized bed reactors in circulating and bubbling operation conditions, a cyclone for gas-solid separation and loop seals, which ensured solids transport and gas separation between the reactors. Additionally, lab scale experiments on the reactivity of the used solids, oxygen carrier and solid fuels, were conducted and kinetic parameters extracted.
All unit models were connected to a process flowsheet and simulated dynamically. The simulation results were compared to experimental data from a 25 kWth pilot plant operated at the university by the author. It could be shown that a detailed and dynamic simulation of the whole process can be carried out over a time period of more than 45 minutes and the experimental results from start-up, steady state operation and shutdown of the plant were predicted accurately.