Process improvement analysis of pyrolysis/gasification of biomass and waste plastics with carbon capture and utilisation through process simulation

被引:24
作者
Chai, Yue [1 ]
Packham, Nicholas [1 ]
Wang, Meihong [1 ]
机构
[1] Univ Sheffield, Dept Chem & Biol Engn, Sheffield S1 3JD, England
关键词
Pyrolysis; Gasification; Biomass; Plastics; CO2 capture and utilisation; Process Simulation; GAS-PRODUCTION; ASPEN PLUS; GASIFICATION; PYROLYSIS; MODEL; CO2;
D O I
10.1016/j.fuel.2022.124571
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
Excessive utilisation of fossil fuels to meet increasing energy demand results in increasing global CO2 emissions. It is a promising solution to apply carbon capture and utilisation (CCU) for pyrolysis/gasification of biomass and waste plastics, which recycles captured CO2 from pyrolysis/gasification to the reforming stage to serve as the second gasification agent. This paper aims to analyse the potential of combining the pyrolysis/gasification process with CCU and to investigate how to improve this process through process simulation using Aspen Plus (R). Process analysis is carried out based on the validated model to investigate the impact of recycling captured CO2 on the product gas production and CO2 conversion when changing various operating conditions (i.e. the amount of recycled CO2, reforming temperature and steam-to-feed ratio). The target is to ensure high H-2 production and to promote CO2 conversion. Simulation results indicated that: (i) Applying CCU for pyrolysis/gasification can inhibit the production of H-2 andCO(2), but it can promote the production of CO; (ii) The H-2/CO ratio of gas products can be adjusted flexibly after recycling CO2 to the reforming stage; (iii) Increase of CO2 recycle amount and steam-to-feed ratio results in lower CO2 conversion while the increase of reforming temperature improves the CO2 conversion; (iv) It is suggested to add solid carbon (e.g. bio-char or carbon-based catalyst) in the reforming stage together with adjusting the operating conditions (i.e. relatively high reforming temperature (e.g. 600 similar to 700 degrees C) and low steam-to-feed ratio (e.g. 3 similar to 4)) simultaneously to protect H-2 production and achieve high CO2 conversion. The findings in this paper will be very useful for future large-scale commercial deployment of applying CCU for pyrolysis/gasification.
引用
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页数:14
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