reactor height

The drive is characterized by simplicity in structure, high reliability, in-herent safety, reduction in reactor height, economy, etc.

这种传动具有结构简单、可靠性高、固有安全、降低反应堆高度、经济等优点。

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Stable operation of the reactor after the separation of different height of the DGGE profiles showed that the reactor there is room for differences in microbial community structure, for the loss of different positions between the quality of PBS to provide proof of the microbial level.

反应器稳定运行后，不同高度处的DGGE分离图谱表明，反应器内微生物群落结构存在空间差异，为不同位置PBS的质量损耗差异提供了微生物层面的证明。

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Revamping schemes of parallel regenerator and reactor with same height in FCCU

同高并列催化裂化装置再生器改造方案分析

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The temperature of gaseous oil, catalysts and the concentration distribution of products along the riser reactor height are predicted by applying the mathematical model developed in this paper.

运用建立的数学模型预测了不同工况条件下反应油气和催化剂颗粒温度沿提升管高度的分布和反应产物的浓度沿提升管高度的分布。

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The construction parameters are similar with the industrial reactor, and the height of the reactor is 1000 mm and the diameter is 250 mm.

采用与工业反应器类似的结构，反应器直径为250mm，高度为1000mm。

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Revamping schemes of parallel regenerator and reactor with same height in FCCU are introduced.

介绍了如何确定同高并列催化裂化装置再生器的改造方案.

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Especially, the advent of focused microwave synthesized reactor reach new height in the way of microwave energy of intension, the ratio of utilization, the control and repetition of reaction.

特别是聚焦微波合成反应器的出现，在微波能的强度，利用率，反应的可控性和可重复性方面都达到了新的高度。

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Influence of height and diameter ratio, downcomer and riser area ratio, and reactor bottom gap height to reactor performance is analyzed, in addition, span of reactor bottom gap height is optimized.

分析了反应器高径比、降流区与升流区面积比及反应器底隙高度对反应器性能的影响，确定了反应器底隙高度的取值范围。

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The diameter of a fixed-bed adiabatic reactor, height of catalyst bed and catalyst loading were calculated by using Runge-Kutta numerical solution method.

采用龙格－库塔数值解法，计算了不同设计方案时，固定床绝热反应器的直径、催化剂床层高度及装量；

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The circulation and mixing state in the reactor were shown to relate with the gas flow rate, the gap between the board and the bottom of reactor and the liquid height above the board.

反应器中液体的循环混合状态与供气量、导流板和反应器底部的距离、挡板上方的液面高度以及提升区和回落区的面积之比有关。

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Through application of mathematic model for flow and atomization within Y-Jet nozzle, the authors designed and verified nozzles required for spray water humidifying desulfurization experiment to be made in humidification activation reactor with 6 meter height and square cross section 590 × 425.

通过应用Y型喷嘴内流动和雾化的数学模型，对高6m，方形截面590×425mm的增湿活化反应器上进行喷水增湿脱硫试验所需喷嘴进行了设计和校核。

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The sludge bed in the bottom of the reactor was the main reaction field for VFA production, and the height of the reactor for stable VFA production increased with the increase of OLR.

反应器底部的污泥床层是VFA生成的主要反应区，随着OLR的升高，达到稳定VFA浓度的反应器高度逐渐增加。

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The paper studied the influences of structural and operating factors on pulp suspension and power consumption in a modified Pachuca ( pneumaticagitating) reactor with a height/ diameter ratio 7.5. The experiments showed that both of the aeration and agitation affect suspension status mutually.

研究了高径比为7.5的充气搅拌反应器中结构因素和操作因素对矿浆悬浮和能耗的影响。

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