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1)  inner flowing
内流化
2)  internal circulating fluidized bed
内旋流流化床
1.
And the particle diffusion coefficients of particles in different areas of this internal circulating fluidized bed are calculated.
通过实验得到了非均匀布风流化床内示踪颗粒在床层内的运动历程,以及床层内颗粒的浓度分布随时间的变化,并归纳得到颗粒在非均匀布风的内旋流流化床中不同区域的扩散系数。
2.
Based on the calorific value of municipal solid waste, its physical composition analysis and the cold state test results of fluidized bed air distribution the authors have conducted the study of an internal circulating fluidized bed (ICFB) combustion system.
根据垃圾的热值和物理成分分析,结合流化床布风的冷态实验结果,对内旋流流化床燃烧系统进行了研究,设计出热态试验装置并成功地进行了生活垃圾焚烧试验。
3.
In this paper, The combustion temperature stability in the dense phase bed zone and temperature distributions in the incinerator have been studied by adjusting mass of processed waste, types of waste and particles thickness of bed in the internal circulating fluidized bed (ICFB).
采用内旋流流化床进行了垃圾焚烧实验,通过改变垃圾处理量、垃圾种类和流化床浓相床区高度,研究了浓相床区温度的稳定性和焚烧炉内温度分布。
3)  inner heating fluid bed dryer
内热式的流化床
4)  internal flow changes
内部流速变化
5)  internally circulating fluidized bed
内循环流化床
1.
Study on an internally circulating fluidized bed for flue gas desulfurization process;
内循环流化床烟气脱硫装置研究
2.
Experimental research on an internally circulating fluidized bed for flue gas desulfurization process;
内循环流化床烟气脱硫技术的实验研究
3.
An internally circulating fluidized bed for FGD process was developed on the basis of modification and optimization of conventional fluidized bed flue gas absorber.
在改进和优化传统流态化烟气脱硫装置结构的基础上,开发了内循环流化床烟气脱硫装置。
6)  internally circulating fluidized bed gasifier
内循环流化床
1.
Study on gasification experiment of wood powder and rice husk in internally circulating fluidized bed gasifier;
稻壳和木粉在内循环流化床气化炉中气化实验研究
2.
Gasification experiment of wood powder and rice husk has been studied in internally circulating fluidized bed gasifier in this paper.
本文主要以稻壳和木粉为原料在内循环流化床气化炉中进行气化实验的研究,测试了温度对当量比的反影响,及对气体成分、气体热值等的影响,并比较内循环流化床气化炉中气化效率与碳转化率的影响。
补充资料:流化床煤气化
分子式:
CAS号:

性质:煤在流化床中进行气化的方法。采用细粒度煤(小于10mm)为原料,吹入气化炉内的气化剂为富氧空气和水蒸气,气流速度高到使炉内煤粒悬浮,处于流化状态,进行煤与气化剂的反应而制得煤气。解决了固定床气化需要块煤的限制。缺点是碳转化率较低,热效率不高,该法适用于气化活性较高的煤种,如褐煤。   

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