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1)  industrial turbulent fluidized bed
工业湍动流化床
1.
Based on the calculation of flow parameters in a fluidized bed and modeling study, a mathematical model for the industrial turbulent fluidized bed reactor was developed, and was verified by commercial data and proved to be suitable for describing the characteristics of industrial turbulent fluidized bed reactor in different load
但是对于这些模型都缺少更多的工业数据去检验它们应用于工业模拟时的可靠性[1,3] ,对于具有垂直内构件的工业湍动流化床的模型化文献中未见报道 。
2)  turbulent fluidized bed
湍动流化床
1.
The axial bed voidage distribution of FCC catalyst particles and the pressure fluctuation in a large two-dimensional turbulent fluidized bed(500 mm×30 mm×6000 mm) were investigated.
详细研究了在500mm×30mm×6000mm大型二维湍动流化床中FCC催化剂颗粒的床层轴向空隙率分布和床层的压力脉动。
2.
Flow behavior of gas and particles was simulated in the turbulent fluidized bed using the k-εturbulent model for gas phase,and kinetic theory of granular flow for particles in combination with interactions between phases.
采用欧拉-欧拉双流体模型,颗粒动理学方法模拟颗粒脉动流动和k-ε双方程模型模拟气相湍流流动,考虑气固两相间耦合作用,数值模拟湍动流化床内气固两相流动行为,获得颗粒浓度和颗粒速度分布。
3)  turbulent fluidized bed
湍动流化床<冶>
4)  turbulent fluidized bed
湍流流化床,湍动流(态)化床
5)  turbulent fluidized beds
湍流流化床
1.
The two phase flow in the dense phase region of FCC turbulent fluidized beds hasbeen studied in a cold model fluidized bed made of plexiglass with a diameter-variable pipe ofφ 710mm X 4000mm/φ870mm X 11000mm and also in a commercial RFCC regenerator (800kt/a ).
分别在φ710mm×4000mm/φ870mm×11000mm有机玻璃流化床和800kt/a重油流化催化裂化装置的再生器中对湍流流化床密相区的两相流动规律进行了研究。
2.
It is shown that the dense density of turbulent fluidized beds along bed radius has an obvious distribution.
在一套710/4000×870/11000mm大型有机玻璃流化床中,测定了大比重的FCC催化剂在湍流流化床密相密度沿径向的分布规律。
6)  commercial turbulent fluidized bed
工业流化床
1.
Based on the calculation of flow parameters in a fluidized bed and its modeling, a mathematical model applied to the industrial turbulent fluidized bed reactor was developed, which is demonstrated by a series of commercial data and proved to be able to describe the characteristics of the commercial turbulent fluidized bed reactor with various loads correctly.
在对已有的流化床的流动参数和反应器模型化研究成果的基础上 ,提出了一个适用于有内构件的丙烯氨氧化制丙烯腈工业流化床反应器两相流动数学模型 ,在模型中的晕相采用平推流模型 ,乳浊相采用全混釜串联模型。
补充资料:悬湍
1.瀑布,从高处下注的水流。
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