English   español  
Por favor, use este identificador para citar o enlazar a este item: http://hdl.handle.net/10261/156819
logo share SHARE   Add this article to your Mendeley library MendeleyBASE
Visualizar otros formatos: MARC | Dublin Core | RDF | ORE | MODS | METS | DIDL
Exportar a otros formatos:

Producción de bio-hidrógeno mediante gasificación catalítica de biomasa con captura integrada de CO2

AutorEsteban Díez, Gonzalo
DirectorPevida García, Covadonga ; Rubiera González, Fernando
Fecha de publicación2017
EditorUniversidad de Oviedo
Resumen[EN]Hydrogen has been proposed as the energy carrier of the future. How-ever, for the Hydrogen Economy to be feasible, hydrogen production must be cheap, accessible and sustainable. Nowadays, more than 96% of H₂ is produced from fossil fuels, contributing to increase the CO₂ con‑centration in the atmosphere and leading to a progressive Climate Change. The most widespread method for hydrogen production con-sists in the steam reforming of methane (SMR), which employs several catalytic reactors at different temperatures to produce gas with a 70% H₂ content that should be later purified. In this context, integration of steam reforming and CO₂ capture in a sin‑gle step process called Sorption Enhanced Steam Reforming (SESR) is considered a promising technology. This process allows to reduce the number of required reactors and the reaction temperature, increasing yield and H₂ purity at the same time. The ultimate consequence is to achieve lower costs of installation and operation. Additionally, if a re-newable fuel like biomass is fed to the reactor, production of cheaper, accessible and sustainable hydrogen is possible, as biomass has zero net impact in the atmospheric CO₂ concentration, thus reducing the contri‑bution of hydrogen to Climate Change.
To optimize the SESR process, an appropriate selection of catalyst and sorbent for CO₂ must be made, together with a proper optimization of the operating conditions. A Pd/Ni-Co-hydrotalcite derived material has been chosen as catalyst, while dolomite has been selected as CO₂ sorbent. All experiments were preceded by thermodynamic equilibrium calculations to estimate the maximum limits of yield, selectivity and concentration of products. This results were later compared with the ex-perimental results obtained. A fluidized bed reactor was employed to assess the optimal conditions for the SESR process. The three main variables modified during these experiments were temperature, steam to carbon ratio (S/C) and weight hourly space velocity (WHSV). Acetone was employed as model com-pound to simulate the behaviour of biomass pyrolysis derived bio-oil.
The fluidized bed reactor was also employed to investigate the effect of bio-oil composition on the performance of the SESR process. The behav-iour of blends with different proportions of acetic acid and acetone was tested along a wide range of temperatures. The values of steam propor-tion and WHSV were chosen from the optimized parameters obtained in the previous work. Thereafter, to reach a deeper knowledge of the influence of composition, several blends of phenol, acetic acid and ace-tone were prepared at similar proportions to those found in pyrolysis bio-oil, and tested for the SESR process. Sorption Enhanced Catalytic Steam Gasification (SECSG) was carried out employing two solid lignocellulosic biomasses. During these exper-iments, a fixed bed reactor was fed semi‑continuously with the bio‑masses in order to evaluate the effect of temperature and biomass composition on yield and H₂ production. The present work has demonstrated that temperature is the most influ-ent factor in the SESR process, followed by S/C and WHSV. It is possible to achieve a H₂ purity higher than 99.5% between 525 and 625 °C, for both the model compounds and the lignocellulosic biomass. However, other process variables such as H₂ yield and selectivity are greatly af‑fected by the nature of the fuel and the reactor employed, needing higher temperatures to reach the same values. The concentration of some by-products, like CO and CH₄, is also very sensitive to changes in temperature and feed, increasing when the process moves away from the optimal conditions.
DescripciónTesis doctoral presentada en el Departamento de Energía de la Universidad de Oviedo, 2017.
Aparece en las colecciones: (INCAR) Tesis
Ficheros en este ítem:
Fichero Descripción Tamaño Formato  
TD_Esteban_Díez_Gonzalo.pdf9,62 MBAdobe PDFVista previa
Mostrar el registro completo

NOTA: Los ítems de Digital.CSIC están protegidos por copyright, con todos los derechos reservados, a menos que se indique lo contrario.