TY - JOUR
T1 - Mono-dimensional and two-dimensional models for chemical looping reforming with packed bed reactors and validation under real process conditions
AU - Argyris, Panagiotis Alexandros
AU - de Leeuwe, Christopher
AU - Abbas, Syed Zaheer
AU - Spallina, Vincenzo
N1 - Funding Information:
The authors acknowledge the EPSRC project (BREINSTORM – EP/S030654/1) and the Department of BEIS in the framework of the Low Carbon Hydrogen Supply 2: Stream 1 Phase 1 Competition (TRN 5044/04/2021) (RECYCLE, HYS2137) for providing funding and support for development of this study. For the purpose of open access, the author has applied a Creative Commons Attribution (CC BY) licence to any Author Accepted Manuscript version arising.
Publisher Copyright:
© 2022 The Royal Society of Chemistry
PY - 2022/4/20
Y1 - 2022/4/20
N2 - Chemical looping reforming (CLR) is an emerging hydrogen/syngas production technology, integrated with CO2 capture. Packed bed reactors are widely used in the hydrogen production industry as they are preferred for high pressure operation and the mathematical modelling describing their operation is very important for their design. In this study, a one-dimensional (1-D) and a two-dimensional (2-D) model have been developed to describe the dynamic operation of chemical looping reforming processes in packed bed reactors (CLR-PB). The reactor under study (L: 400 mm ID: 35 mm) contains an axially placed thermowell (OD: 6.35 mm) to monitor the temperature across the reactor bed at 6 points and 440 g of NiO/CaAl2O4 oxygen carrier (OC). Both models have been validated presenting very good agreement with the experimental results. The comparison between modelling and experimental results has been carried out in terms of thermowell temperature and the gas composition breakthroughs, with the 2-D model capturing the thermowell temperature recordings with high accuracy, while the 1-D model delivered results that underestimated it by 2.5%. Nonetheless, the predicted average bed temperature presented a difference limited to 1% lower estimation of the 1-D to the 2-D model. The temperature difference between the bed and the thermowell has achieved a value of >180 °C thus resulting also problematic in terms of safe operation if not properly considered. with temperatures during oxidation being higher even by 181 °C inside the bed, emphasizing the importance of the model in the proper design and safe operation of the reactor. The 1-D model, due to the significantly lower computation time (∼21 times faster than 2-D), has been selected to be tested against a range of operating conditions for oxidation (500-600 °C, 1-5 bar, 10-40 NLPM, 10-20% O2), reduction (600-900 °C, 1-5 bar) with H2, syngas and CH4-rich reducing agents and dry reforming (700-900 °C, 1-5 bar), delivering results with good agreement especially under high temperature conditions where solid conversion is high and under conditions which resemble the expected industrial ones.
AB - Chemical looping reforming (CLR) is an emerging hydrogen/syngas production technology, integrated with CO2 capture. Packed bed reactors are widely used in the hydrogen production industry as they are preferred for high pressure operation and the mathematical modelling describing their operation is very important for their design. In this study, a one-dimensional (1-D) and a two-dimensional (2-D) model have been developed to describe the dynamic operation of chemical looping reforming processes in packed bed reactors (CLR-PB). The reactor under study (L: 400 mm ID: 35 mm) contains an axially placed thermowell (OD: 6.35 mm) to monitor the temperature across the reactor bed at 6 points and 440 g of NiO/CaAl2O4 oxygen carrier (OC). Both models have been validated presenting very good agreement with the experimental results. The comparison between modelling and experimental results has been carried out in terms of thermowell temperature and the gas composition breakthroughs, with the 2-D model capturing the thermowell temperature recordings with high accuracy, while the 1-D model delivered results that underestimated it by 2.5%. Nonetheless, the predicted average bed temperature presented a difference limited to 1% lower estimation of the 1-D to the 2-D model. The temperature difference between the bed and the thermowell has achieved a value of >180 °C thus resulting also problematic in terms of safe operation if not properly considered. with temperatures during oxidation being higher even by 181 °C inside the bed, emphasizing the importance of the model in the proper design and safe operation of the reactor. The 1-D model, due to the significantly lower computation time (∼21 times faster than 2-D), has been selected to be tested against a range of operating conditions for oxidation (500-600 °C, 1-5 bar, 10-40 NLPM, 10-20% O2), reduction (600-900 °C, 1-5 bar) with H2, syngas and CH4-rich reducing agents and dry reforming (700-900 °C, 1-5 bar), delivering results with good agreement especially under high temperature conditions where solid conversion is high and under conditions which resemble the expected industrial ones.
UR - http://www.scopus.com/inward/record.url?scp=85132113981&partnerID=8YFLogxK
U2 - 10.1039/d2se00351a
DO - 10.1039/d2se00351a
M3 - Article
AN - SCOPUS:85132113981
SN - 2398-4902
VL - 6
SP - 2755
EP - 2770
JO - Sustainable Energy and Fuels
JF - Sustainable Energy and Fuels
IS - 11
ER -
