Evaluation of Sugar Beet Waste in the Production of Hydrogen-Rich Gas

被引:0
|
作者
Cakan, Alattin [1 ]
Kiren, Burcu [1 ]
Duran, Fatma [1 ]
Cinar, Baris [1 ]
Ayas, Nezihe [2 ]
机构
[1] Anadolu Univ, Fac Engn, Dept Chem Engn, TR-26470 Eskisehir, Turkey
[2] Eskisehir Tech Univ, Fac Engn, Dept Chem Engn, TR-26470 Eskisehir, Turkey
来源
INTERNATIONAL JOURNAL OF RENEWABLE ENERGY RESEARCH | 2019年 / 9卷 / 03期
关键词
Sugar beet; waste material; gasification; hydrogen; alkali catalyst; BIOMASS GASIFICATION; AIR GASIFICATION; PYROLYSIS; TAR; CONVERSION; PULP;
D O I
暂无
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
Among renewable energy sources, biomass is increasingly gaining tremendous attention due to its feedstock diversity and the way for waste management. The objective of this work is to explore the potential of the pulp, which is the waste of the sugar factory, as alternative energy for conventional energy sources through gasification technologies. Dry air was used as an oxidizing agent for the production of producer gas. Gasification experiments were carried out using different operating parameters including various temperatures (650 degrees C, 750 degrees C and 850 degrees C), without catalyst and with alkali catalysts (K2CO3 , Na2CO3). The producer gas generated from the gasification process was identified through Micro Gas Chromatography (mu-GC) system. From the results obtained, the highest hydrogen yield is found to be 5.730 mol H-2/kg biomass in the absence of a catalyst, at 850 degrees C with 2 L/h dry air flow rate and 15 min. reaction time. Besides, it also revealed that K2CO3 is more effective than Na2CO3, and the maximum hydrogen yield (5.199 mol H-2/kg biomass) was achieved when K2CO3 used at 650 degrees C with 2 L/h dry air flow rate and 15 min. reaction time.
引用
收藏
页码:1214 / 1223
页数:10
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