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inner circulation fluidized bed
相关语句
  内循环流化床
     Design of Reaction Area in Air-lift Inner Circulation Fluidized Bed
     气提内循环流化床反应区的设计
短句来源
     Experimental Research on Inner Circulation Fluidized Bed with Lower Dissolved Oxygen to Treat Municipal Wastewater
     微氧内循环流化床处理城市污水的试验研究
短句来源
     The macroscopical and microcosmic kinetics model of degrading organic in the wastewater with low contaminant concentration in the inner circulation fluidized bed biofilm reactor were deduced.
     提出了内循环流化床处理低浓度污水的宏观、微观动力学模型。
短句来源
     Based on Bernoulli equation,a trial calculation model for design of reaction area in an integrated air-lift inner circulation fluidized bed reactor is put forward.
     基于伯努利能量方程,提出了一体化气提内循环流化床反应器反应区设计的试算模型。
短句来源
  气提内循环流化床
     Design of Reaction Area in Air-lift Inner Circulation Fluidized Bed
     气提内循环流化床反应区的设计
短句来源
     Based on Bernoulli equation,a trial calculation model for design of reaction area in an integrated air-lift inner circulation fluidized bed reactor is put forward.
     基于伯努利能量方程,提出了一体化气提内循环流化床反应器反应区设计的试算模型。
短句来源
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Based on Bernoulli equation,a trial calculation model for design of reaction area in an integrated air-lift inner circulation fluidized bed reactor is put forward.Curves of raising velocity against up-flow area diameter developed based on the model can describe response rules with the change of parameters,such as substrate concentration,air-lift distance and hydraulic retention time,etc.in reactor.Results show that the proper inner diameter of up-flow area is 65 mm for a reaction area with the height...

Based on Bernoulli equation,a trial calculation model for design of reaction area in an integrated air-lift inner circulation fluidized bed reactor is put forward.Curves of raising velocity against up-flow area diameter developed based on the model can describe response rules with the change of parameters,such as substrate concentration,air-lift distance and hydraulic retention time,etc.in reactor.Results show that the proper inner diameter of up-flow area is 65 mm for a reaction area with the height of 2 m and the outer diameter of 150 mm.

基于伯努利能量方程,提出了一体化气提内循环流化床反应器反应区设计的试算模型。根据该模型绘制的升流速度随升流管内径变化的曲线可描述反应器在底物浓度、气提距离以及反应器水力停留时间等参数变化时的响应规律。依据该模型得出,当反应区外筒尺寸为H=2m、D=150 mm时升流筒内径宜为65 mm。

 
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