首页> 外文会议>International Conference on Fluidized Bed Combustion; 20050522-25; Toronto(CA) >COAL GASIFICATION CHARACTERISTICS IN A 2MWth SECOND-GENERATION PFB GASIFIER
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COAL GASIFICATION CHARACTERISTICS IN A 2MWth SECOND-GENERATION PFB GASIFIER

机译:2MWth第二代PFB气化炉的煤气化特性

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Coal gasification process and equipment feasibility research were carried out in a 2 MW thermal input pressurized spout-fluid bed pilot-scale gasifier and a long-time-run test was performed to study the effects of operating parameters on coal partial gasification behaviors. The test results have demonstrated the feasibility of the gasifier to provide suitable fuel gas and residual char for downstream system of 2G PFBC-CC. The concentration of methane decreased at higher gasification temperature due to the secondary cracking of methane while the carbon conversion increased, and the concentration of hydrogen increased with an increase of steam flow rate. The main experimental results were compared with those of pilot-scale facilities in the world.
机译:在2 MW热输入加压喷流床中试规模气化炉中进行了煤气化工艺和设备可行性研究,并进行了长期运行试验,以研究运行参数对煤部分气化行为的影响。测试结果证明了该气化炉为2G PFBC-CC下游系统提供合适的燃料气体和残留焦炭的可行性。甲烷的浓度在较高的气化温度下由于甲烷的二次裂化而降低,而碳的转化率增加,并且氢的浓度随着蒸汽流量的增加而增加。将主要实验结果与世界上中试规模的设施进行了比较。

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