Syngas and a separate nitrogen/argon stream via chemical looping reforming - A 140 kW pilot plant study

被引:115
作者
Proell, Tobias [1 ]
Bolhar-Nordenkampf, Johannes [1 ]
Kolbitsch, Philipp [1 ]
Hofbauer, Hermann [1 ]
机构
[1] Vienna Univ Technol, Inst Chem Engn, A-1060 Vienna, Austria
关键词
Chemical looping; Reforming; Hydrogen production; Carbon capture; Fluidization; NATURAL-GAS; OXYGEN CARRIERS; COMBUSTION; FUEL;
D O I
10.1016/j.fuel.2009.09.033
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
A dual circulating fluidized bed pilot plant was operated in chemical looping reforming conditions at a scale of 140 kW fuel power with natural gas as fuel. A nickel-based oxygen carrier was used as bed material. The pilot plant is equipped with an adjustable cooling system. Three experimental campaigns have been carried out at 747 degrees C (1020 K), 798 degrees C (1071 K) and 903 degrees C (1176 K), respectively. In each campaign, the global stoichiometric air/fuel ratio was varied step-wise between 1.1 and the minimum value possible to keep the desired operating temperature when the cooling is finally switched off. The results show that the fuel reactor exhaust gas approaches thermodynamic equilibrium. The residual amount of methane left decreases with increasing fuel reactor temperature. Further, the oxygen in the air reactor can be completely absorbed by the solids as soon as the air reactor operating temperature is higher than 900 degrees C (1173 K). Even though no steam was added to the natural gas feed no carbon formation was found for global excess air ratios larger than 0.4. (C) 2009 Elsevier Ltd. All rights reserved.
引用
收藏
页码:1249 / 1256
页数:8
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