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.
运用几种热力计算方法，对某型船用增压锅炉低负荷工况的炉膛出口烟气温度进行了计算。
Use several kinds of thermal calculation methods of boiler's furnace, and calculate the outlet flue gas temperature of a low load of some supercharged boiler.
该模型只利用进出口烟气温度、空气预热器管壁温度和烟气压降等易测参数来监测积灰情况。
The model is based on the easy measurable parameters, such as the inlet and outlet temperature of flue gas, the wall temperature of air preheater, and the pressure difference of the air preheater.
提高进口烟气温度、降低蒸汽压力或减小节点温差，均可显著降低设计出口烟气温度，从而增大蒸发量，提高热效率；
Higher gas inlet temperature, lower steam pressure or pinch point temperature difference lead to lower exhaust gas temperature, larger evaporation and higher efficiency;
计算采用典型F GD入口烟气参数，应用烟气湿度和定压容积热容的概念计算了吸收塔出口烟气温度及塔内蒸发水量，并分析了其变化规律。
With adoption of the typical flue gas inlet parameter for FGD, this article completes above calculation with humidity and pressure volume heat concept, and analyzes the relative changing rules.
结果表明：一次风率对煤粉气流的着火影响较大，而对出口处烟气温度、氧量以及飞灰含碳量影响较小。
The results illustrate that primary air ratio has a major effect on pulverized coal ignition and minor effects on gas temperature, oxygen concentration and unburned carbon at furnace exit.
这将导致燃烧器出口处热量局部聚集，烟气温度非常高，造成炉内温度分布不均及喷嘴的损坏。
These will result in local heat accumulation at the outlet of burner, very high temperature of flue gas, uneven distribution of temperature in furnace and damage of nozzles.
这将导致燃烧器出口处热量局部聚集，烟气温度非常高，造成炉内温度分布不均及喷嘴的损坏。
These will result in local heat accumulation at the outlet of burner, very high temperature of flue gas, uneven distribution of temperature in furnace and damage of nozzles.
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