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1)  fluidized bed
流化床
1.
Summary on the running of converter with circulating fluidized bed for the synthesis of 3000 t/a vinyl chloride;
3000t/a氯乙烯循环流化床转化器运行小结
2.
Thermal fragmentation of quartzite particles in fluidized bed and gray forecasting model;
流化床内石英砂的热破碎及其灰色预测模型
3.
Study on the parameter of fluidization characteristics in the fluidized bed;
流化床内介质主要流化特性参数的研究
2)  fluid bed
流化床
1.
Discussions on the consolidated heat transfer of fluid bed;
流化床的强化传热途径探讨
2.
Experimental study on sodium chloride crystallization dynamics in fluid bed;
流化床中氯化钠结晶动力学实验研究
3.
A summary on acceptance of a model for commercialization of circulated fluid bed gasification of pulverized caol;
循环流化床粉煤气化工业示范装置考核小结
3)  fluidized-bed
流化床
1.
Influencial factors on fluidized-bed pelletization during installation and trial run;
从安装调试看影响流化床制粒的因素
2.
Modification of Fluidized-bed Exhaust System for Copper Sulfate Drying;
硫酸铜干燥用流化床尾气系统的改造
3.
Arsenic emission characteristics during fluidized-bed coal combustion;
流化床煤燃烧过程中砷析出特性研究
4)  Fluidized bed reactor
流化床
1.
Hydrogen production from methane decomposition and catalyst regeneration by air in a fluidized bed reactor;
流化床中甲烷裂解制氢与催化剂再生过程研究
2.
Catalytic performance of Ni/SiO2 in converting methane to syngas using fluidized bed reactor;
流化床上甲烷催化转化制合成气Ni/SiO_2催化剂性能研究
3.
Process of biofilm colonization of a hydrophilic porous carrier in fluidized bed reactor;
亲水性多孔载体在流化床中的生物膜形成过程分析
5)  CFB
流化床
1.
Wear of flash hydrated and agglomerated CFB fly ash;
飞灰快速水化团聚颗粒在流化床中的冷态磨耗研究
2.
Comprehensive Utilization of CFB Ashes After Desulfurization;
流化床脱硫灰渣的特性与综合利用研究
3.
CFB Boiler for Handling High Consistency Organic Waste Water;
处理高浓度有机废水流化床焚烧炉
6)  fluidization bed
流化床
1.
Firstly, to better operate and design a fluidization bed to convert biomass such as wheat stalk, corn stalk and wood powder into activated carbon, the minimum fluidization velocity of biomass mixing with sand is obtained by experiment.
为了更好的设计和操作流化床,通过实验确定了小麦秸秆—石英砂混合物、玉米秸秆—石英砂混合物和木粉—石英砂混合物的最小流化速度。
2.
Glucose used as a biomass model compound was gasified for hydrogen production in the new supercritical water fluidization bed system with temperature of 500-600℃and pressure of 23-27MPa.
以生物质模型化合物葡萄糖为原料,在温度500~600℃,压力23~37MPa范围内,利用新研制的超临界水流化床系统对其气化制氢特性进行研究,讨论了过程主要参数温度、压力、物料浓度以及催化剂添加对气化制氢的影响。
3.
A fluidization bed reactor was proposed to be used in supercritical water gasification of biomass in order to reduce reactor plugging.
本文提出在生物质超临界水气化制氢过程中采用流化床反应器防止反应器结渣堵塞。
补充资料:流化床
      见流态化。
  

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