Thermogravimetric study of Chlorella vulgaris for syngas production

被引:31
作者
Raheem, Abdul [1 ]
Sivasangar, S. [2 ]
Azlina, W. A. K. G. Wan [1 ]
Yap, Y. H. Taufiq [2 ]
Danquah, Michael K. [3 ]
Harun, Razif [1 ]
机构
[1] Univ Putra Malaysia, Dept Chem & Environm Engn, Serdang 43400, Malaysia
[2] Univ Putra Malaysia, Fac Sci, Catalysis Sci & Technol Res Ctr, Serdang 43400, Malaysia
[3] Curtin Univ, Dept Chem Engn, Sarawak, Malaysia
来源
ALGAL RESEARCH-BIOMASS BIOFUELS AND BIOPRODUCTS | 2015年 / 12卷
关键词
Chlorella vulgaris; Microalgae; Biomass; Thermogravimetric analysis; Gasification; Syngas; STEAM GASIFICATION; KINETIC-ANALYSIS; PYROLYTIC CHARACTERISTICS; MICROALGAE COMBUSTION; THERMAL-DECOMPOSITION; TETRASELMIS-SUECICA; HEATING RATE; BIOMASS; COAL; TEMPERATURE;
D O I
10.1016/j.algal.2015.08.003
中图分类号
Q81 [生物工程学(生物技术)]; Q93 [微生物学];
学科分类号
071005 ; 0836 ; 090102 ; 100705 ;
摘要
The present study investigates the thermal degradation behavior of Chlorella vulgaris using a thermogravimetric analyzer (TGA) to explore application as feedstock for syngas production. The biomass was heated continuously from room temperature to 1000 degrees C at different heating rates (5, 10 and 20 degrees C min(-1)) under N-2/air conditions at a constant flow rate of 25 mL min(-1). Experimental results showed that the combustion process of C. vulgaris can be divided into three major phases; (1) moisture removal, (2) devolatilization of carbohydrates, protein and lipids and (3) degradation of carbonaceous material. A degradation rate of 80% was obtained at the second phase of the combustion process in the presence of air whilst a degradation rate of 60% was obtained under N-2 atmosphere at the same phase. The biomass was further gasified for syngas production using a Temperature Programmed Gasifier (TPG). The effect of three different process variables, temperature, microalgal loading, and heating rate was investigated. The maximum H-2 production was found at 800 degrees C temperature with a biomass loading of 0.5 g. No significant effect of heating rate was observed on H-2 production. The activation energy values, based on the Kissinger method, were evaluated to be 45.38 +/- 0.5 kJ mol(-1) (1st stage), 61.20 +/- 0.5 kJ mol(-1) (2nd stage) and 97.22 +/- 0.5 kJ mol(-1) (3rd stage). The results demonstrate a significant potential for the utilization of the microalgae biomass as feedstock for large-scale production of syngas via gasification. (C) 2015 Elsevier B. V. All rights reserved.
引用
收藏
页码:52 / 59
页数:8
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