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Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2024, Vol. 18 Issue (11): 121   https://doi.org/10.1007/s11705-024-2472-7
  本期目录
Comparison of CO2 with H2O as the transport medium in a biomass supercritical water gasification system
Weizuo Wang, Bingru Lu, Jinwen Shi, Qiuyang Zhao, Hui Jin()
State Key Laboratory of Multiphase Flow in Power Engineering, Xi’an Jiaotong University, Xi’an 710049, China
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Abstract

Supercritical water gasification is a clean technology for biomass conversion and utilization. In supercritical water gasification systems, H2O is often used as the transport medium. Decreases in the reaction temperature at the gasification area and in the heating rate of biomass may limit the gasification rate and efficiency. In this paper, CO2 is used as the transport medium due to its relatively low critical point and specific heat capacity. Moreover, a corn stalk gasification system with different transport media is established in this paper, and the influences of various operating parameters, such as temperature, pressure and feedstock concentration, are investigated. The results show that the gas yield in the CO2-transport system decreases by no more than 5 wt %. In addition, thermodynamic analysis reveals that a system with CO2 as transport medium consumes approximately 25% less electricity than a system with H2O as the transport medium. In addition, the reaction heat absorption decreases. The results show the superiority of CO2 to H2O as a transport medium.

Key wordsbiomass supercritical water gasification    hydrogen production    CO2 transport    energy and exergy analyses
收稿日期: 2024-02-11      出版日期: 2024-08-06
Corresponding Author(s): Hui Jin   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2024, 18(11): 121.
Weizuo Wang, Bingru Lu, Jinwen Shi, Qiuyang Zhao, Hui Jin. Comparison of CO2 with H2O as the transport medium in a biomass supercritical water gasification system. Front. Chem. Sci. Eng., 2024, 18(11): 121.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-024-2472-7
https://academic.hep.com.cn/fcse/CN/Y2024/V18/I11/121
Feedstock Elemental analysis/wt % Proximate analysis/wt % Lower heating value/(106 J·kg?1)
Cad Had Nad Sad Oad Mad Aad Vad FCad
Corn stalks 41.18 4.96 0.78 0.19 30.90 8.02 6.46 67.55 17.97 15.58
Tab.1  
Fig.1  
Fig.2  
System Changes in parameters Changes in production yields/(kg·kg?1 feedstock)
Temperature/°C Pressure/MPa H2 yield CH4 yield CO yield CO2 yield
CO2-transport system 550–800 23 0.094–0.131 (increase) 0.082–0.000 (decrease) 0.020–0.082 (increase) 5.249–5.377 (increase)
650 23–29 0.129–0.125 (decrease) 0.010–0.017 (increase) 0.046–0.047 (increase) 1.406–1.386 (decrease)
H2O-transport system 550–800 23 0.114–0.132 (increase) 0.038–0.000 (decrease) 0.006–0.021 (increase) 1.394–1.475 (increase)
650 23–29 0.132–0.130 (decrease) 0.002–0.004 (increase) 0.012–0.012 (increase) 1.483–1.376 (decrease)
Tab.2  
Fig.3  
Fig.4  
Fig.5  
Fig.6  
Fig.7  
Fig.8  
Fig.9  
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