A study of black liquor and pyrolysis oil co-gasification in pilot scale

被引:19
|
作者
Jafri, Yawer [1 ]
Furusjo, Erik [1 ]
Kirtania, Kawnish [1 ]
Gebart, Rikard [1 ]
Granberg, Fredrik [2 ]
机构
[1] Lulea Univ Technol, Div Energy Sci, SE-97187 Lulea, Sweden
[2] Lulea Univ Technol, Green Fuels Operat, Ind Gatan 1, S-94138 Pitea, Sweden
关键词
Black liquor; Pyrolysis oil; Gasification; Pilot-scale; Co-gasification; Thermochemical conversion; PRODUCT GAS-COMPOSITION; METHANOL PRODUCTION; PARAMETERS; COMPONENTS; CONVERSION; OPERATION; CHAR; WOOD;
D O I
10.1007/s13399-016-0235-5
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
The effect of the blend ratio and reactor temperature on the gasification characteristics of pyrolysis oil (PO) and black liquor (BL) blends with up to 20 wt% PO was studied in a pilot-scale entrained-flow gasifier. In addition to unblended BL, three blends with PO/BL ratios of 10/90, 15/85, and 20/80 wt% were gasified at a constant load of 2.75 MWth. The 15/85 PO/BL blend was used to investigate the effect of temperature in the range 1000-1100 degrees C. The decrease in fuel inorganic content with increasing PO fraction resulted in more dilute green liquor (GL), and a greater portion of the feedstock carbon ended up in syngas as CO. As a consequence, the cold gas efficiency increased by about 5%-units. Carbon conversion was in the range 98.8-99.5% and did not vary systematically with either fuel composition or temperature. Although the measured reactor temperatures increased slightly with increasing PO fraction, both unblended BL and the 15% PO blend exhibited largely similar behavior in response to temperature variations. The results from this study show that blending BL with the more energy-rich PO can increase the cold gas efficiency and improve the process carbon distribution without adversely affecting either carbon conversion or the general process performance.
引用
收藏
页码:113 / 124
页数:12
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