Modelling of sorption-enhanced steam reforming (SE-SR) process in fluidised bed reactors for low-carbon hydrogen production: A review

被引:17
作者
Udemu, Chinonyelum [1 ]
Font-Palma, Carolina [1 ]
机构
[1] Univ Hull, Sch Engn, Kingston Upon Hull HU6 7RX, England
关键词
Sorption-enhanced steam reforming; CO2; capture; Hydrogen; Modelling; CFD; SE-SMR; DIMENSIONAL 2-FLUID MODEL; HIGH-PURITY HYDROGEN; CO2; CAPTURE; SMR PROCESS; PROCESS PERFORMANCE; CATALYST MATERIAL; COMBINED SORBENT; DESIGN ANALYSIS; SOLID SORBENTS; H-2; PRODUCTION;
D O I
10.1016/j.fuel.2023.127588
中图分类号
TE [石油、天然气工业]; TK [能源与动力工程];
学科分类号
0807 ; 0820 ;
摘要
Sorption-enhanced steam reforming (SE-SR) offers lower capital costs than conventional steam reforming with carbon capture, which arises from the compact makeup that allows reforming and CO2 capture to occur in a single reactor. However, the technology readiness level (TRL) of SE-SR technology is currently low and large-scale deployment can be expedited by ramping up activities in reactor modelling and validation at pilot scale. This work first explores the concept of SE-SR technology, then the experimental activities and pilot tests performed for this technology, followed by the review of progress made on SE-SR modelling. It was found that the Eulerian-Eulerian two-fluid model is the most popular approach widely adopted for modelling SE-SR in fluidised bed reactors. However, the averaging method used to close equations ignores flow details at particle level and simplifies the particle system. Moreover, while hydrogen purity and yield have been predicted within an acceptable error, larger errors for CO2 gas output relative to experimental data have been reported for this model type. Limitations and future perspectives for reactor designs and the various models and modelling approaches are also analysed, to provide guidance and advance research, modelling and scaleup of SE-SR technology.
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页数:21
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