对烟气循环流化床脱硫工艺和脱硫塔设计进行详细的介绍，为设计提供参考。
The desulfurization process and absorber design of flue gas circulating fluidized bed were described in detail to supply reference for design.
本文对烟气中二氧化硫污染与控制技术进行了综述，在参考大量文献的基础上，提出了烟气循环流化床脱硫工艺。
A review on pollution and control for SO2 in flue gas is carried out in the dissertation, CFB FGD process is brought forward on the base of large number of literatures.
提出了由两级分离系统组成的循环流化床烟气脱硫工艺。
Flue gas desulfurization technology is proposed on the basis of a circulating fluidized bed composed of a two-stage separation system.
建立了基于热平衡法、烟气分析法和烟气量法的循环流化床锅炉燃烧室密相区燃烧份额计算数学模型，并分析比较了各种模型的特点。
The model of combustion fraction for dense phase in circulating fluidized bed combustor has been built up, based on thermal balance, gas analysis and total gas amount.
循环流化床锅炉的烟气和烟尘性质与常规煤粉炉相比有较大差异。
There are greater differences for gas and dust characters between the circulating fluidized-bed(CFB) and normal boiler.
重点叙述了循环流化床烟气脱硫技术和微生物脱硫技术。
It emphasizes on the technology of circulating fluidized bed for flue gas desulfurization and the technology of flue gas desulfurization by micro-organism.
循环流化床烟气脱硫技术是近年来国内外正在研究开发的一种先进技术。
Flue gas desulfurization technology with circulating fluidized bed (CFB) has been developed in the world recently.
用到循环流化床锅炉启动，可以任意调整出口烟气温度、出口烟气射流长度。
Exit flue gas temperature, flue gas quantity and length of flue gas jet could be control conveniently according to requirement of the boiler start up process.
给出了循环流化床烟气脱硫数学模型中的各个参数或相应的计算公式。
Values of parameters, or relevant formulae, for determining the parameters of the mathematical desulfurization model for circulating fluidized bed boilers, are here presented.
给出了循环流化床烟气脱硫数学模型中的各个参数或相应的计算公式。
Values of parameters, or relevant formulae, for determining the parameters of the mathematical desulfurization model for circulating fluidized bed boilers, are here presented.
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