1) Fluidized air ve locity
流化气速
2) Fluidization varying gas velocity
变气速流态化
3) air current speed
气流流速
1.
The problems in the design of smoke prevention compartmentalization,air current speed,tube discharge of smoke in each compartmentalized zone,and natural air replenishment were discussed through the introduction and analysis of the designing principles,criteria,and the operational mode on the occasion of fire.
通过对地铁防排烟设计原则、设计标准、火灾工况下防排烟系统运行模式等方面的分析和介绍,对地铁车站在防烟分区划分、气流流速、区间隧道排烟、自然补风设计方面存在的问题进行了探讨。
4) vaporized fuel flow
气化燃料流动[量，速]
5) air velocity
气流速度
1.
The scrap absorbing system was introduced in details,such as the constituent,determination of air velocity,pipeline arrangement,layout of scrap absorbing unit and the control and interlock between principal machines for edge cutting.
介绍了碎边吸收系统的组成、气流速度的确定、管道布置、碎边吸收风机的选择布置、与切边主机之间的控制连锁。
2.
This paper analyzes the influence of indoor air velocity and the effects of setting of exterior shade,direction of glass curtain wall,glass types and glasses filled different gas on energy consumption in glass curtain buildings.
本文分析了室内气流速度、设置外遮阳、幕墙朝向、玻璃类型和玻璃夹层的填充气体等因素对玻璃幕墙建筑能耗的影响。
3.
CFD software Fluent was applied to simulate the air velocity of fire arresters, and the relation was analyzed between structure parameters, temperature and air velocity.
应用Fluent软件模拟空气在防爆格栅中气流速度,定性分析了平板阻火单元不同结构和温度与气流速度的关系。
6) flow velocity
气流速度
1.
That was accomplished through a series of experiments at different flow velocity,with the same smoldering cottons put directly at the entrance of the FE/DE and in box,respectively.
实验结果表明,在烟颗粒生成过程不受气流影响的情况下,两种感烟探测器的响应灵敏度均随气流速度增大而下降。
2.
To study the phenomena occurring in plasma aerodynamic actuation and the mechanism of plasma flow control,the induced flow velocity of the plasma aerodynamic actuator is experimentally investigated under a variety of parameter conditions.
为了探索等离子体流动控制的内在机理,在不同的参数条件下,对等离子体气动激励的诱导气流速度进行了实验研究。
补充资料：流化床煤气化
分子式：
CAS号：
性质：煤在流化床中进行气化的方法。采用细粒度煤(小于10mm)为原料，吹入气化炉内的气化剂为富氧空气和水蒸气，气流速度高到使炉内煤粒悬浮，处于流化状态，进行煤与气化剂的反应而制得煤气。解决了固定床气化需要块煤的限制。缺点是碳转化率较低，热效率不高，该法适用于气化活性较高的煤种，如褐煤。
CAS号：
性质：煤在流化床中进行气化的方法。采用细粒度煤(小于10mm)为原料，吹入气化炉内的气化剂为富氧空气和水蒸气，气流速度高到使炉内煤粒悬浮，处于流化状态，进行煤与气化剂的反应而制得煤气。解决了固定床气化需要块煤的限制。缺点是碳转化率较低，热效率不高，该法适用于气化活性较高的煤种，如褐煤。
说明：补充资料仅用于学习参考，请勿用于其它任何用途。
参考词条