Published January 2019 | Version v1
Journal article

Chemical looping reforming of biomass based pyrolysis gas coupling with chemical looping hydrogen by using Fe/Ni/Al oxygen carriers derived from LDH precursors

  • 1. Guangdong Provincial Key Laboratory of New and Renewable Energy Research and Development, Guangzhou 510640 (China)
  • 2. CAS Key Laboratory of Renewable Energy, Guangzhou 510640 (China)
  • 3. Guangzhou Institute of Energy Conversion, Chinese Academy of Sciences (CAS), Guangzhou 510640 (China)
  • 4. State Key Laboratory of Clean Energy Utilization, Zhejiang University, Hangzhou 310027 (China)

Description

Highlights: • Chemical looping coupling process were proposed to reform biomass based pyrolysis gas and achieve high purity hydrogen. • Reaction performance of Fe/Ni/Al mixed oxygen carriers derived from layered double hydroxide precursors was evaluated. • 98.26% CH4 conversion, 71.92% CO2 conversion and 96.56% H2 purity were achieved. • High disperse Ni0.6Fe2.4Al1.1O4 was generated in the regeneration stage. -- Abstract: Chemical looping reforming (CLR) coupling with chemical looping hydrogen (CLH) was proposed to reform biomass based pyrolysis gas and achieve high purity H2 by using Fe/Ni/Al oxygen carriers derived from layered double hydroxide (LDH) precursors. The crystal form, morphology and reactivity of oxygen carriers were characterized by various analysis methods. The chemical looping reaction process was investigated in a fixed bed reactor. The experimental results exhibited that Fe0.99Ni0.6Al1.1O4 high dispersed oxygen carrier was synthesized. Moderate lattice oxygen releasing rate 0.00175 wt%/s and escape ratio 95.14% were achieved by the mixed oxygen carrier with Fe/Ni ratio of 3/1. Ni had positive effect on lattice oxygen escape ratio of oxygen carrier while Fe contributed to improve the instantaneous lattice oxygen releasing rate. Furthermore, the CH4/CO2 in biomass based pyrolysis gas was eliminated via CLR process based on the metal catalytic effect of oxygen carrier. The highest CH4 conversion 98.26% and CO2 conversion 71.92% were obtained in CLR process accompanying with the reduction of Fe0.99Ni0.6Al1.1O4 to Fe/Ni alloy. Additionally, H2 with 96.56% purity was achieved in CLH process with the conversion of Fe/Ni alloy to Fe3O4. The H2 instantaneous generation rate increased sharply to the maximum value 34.70 ml/min and then declined gradually. Ni0.6Fe2.4Al1.1O4 new high dispersed compound was generated in the regeneration stage with similar structure to fresh sample and more active Fe species content. Though the particle size of oxygen carrier tended to decline after whole reaction process, the porous structure was still reserved.

Additional details

Identifiers

DOI
10.1016/j.enconman.2018.10.065;
PII
S0196890418311932;

Publishing Information

Journal Title
Energy Conversion and Management
Journal Volume
179
Journal Page Range
p. 304-313
ISSN
0196-8904
CODEN
ECMADL

Optional Information

Copyright
Copyright (c) 2018 Elsevier Ltd. All rights reserved.