1) bubbling
[英]['bʌbl] [美]['bʌbḷ]
鼓泡
1.
Study on the Bubbling Enhancement of Microfiltration in Submerged Hollow Fiber Membrane Module;
鼓泡对浸没式中空纤维膜微滤过程强化作用的研究
2.
Reasons of ionic membrane bubbling and its preventive measures
离子膜鼓泡的原因及预防措施
3.
Factors of bubbling in operation process of ionic membrane were analysed and enumerated.
分析并列举了离子交换膜在使用过程中鼓泡的原因,阳极液质量浓度;pH值;阴极液质量浓度;电流密度;开停车及盐水质量等因素都可以造成膜鼓泡,形成针孔。
2) bubble
[英]['bʌbl] [美]['bʌbḷ]
鼓泡
1.
The number of bubble after first heat treatment is reduced by CIP processing which can improve the uniformity of Jr along the longitudinal direction to be more suitable for the fabrication of long Bi-2223/Ag tapes.
结果表明:采用压棒装管工艺提高了带材芯丝的填充系统,有利于提高带材的工程电流密度;第一次热处理后带材表面的鼓泡明显比松装带材少,有利于提高电流沿长度方向上的均匀性,更适合制备长带。
2.
In order to predigest experiment and save energy, material and time, bubble factors of Bi-2212 tape were studied systematically by grey theory.
为了简化实验,达到节能、节材及节时的目的,利用灰色理论系统地研究了Bi-2212带材鼓泡的影响因素。
3.
Through the Analysis of the bubble generation while pressing the"sandwich structure"panel,a solution was brought forward.
对"三明治"结构厢板在压制时产生鼓泡的原因进行了分析,并提出了解决办法。
3) Blister
[英]['blɪstə(r)] [美]['blɪstɚ]
鼓泡
1.
Blister were observed in the surface of square pipe after being hot zinc-plated.
方管表面热镀锌后出现不同程度的鼓泡现象。
4) bubble column
鼓泡床
1.
Experiment and CFD simulation of bubble size distribution in 2D gas-liquid bubble column;
二维鼓泡床内气泡尺寸分布的实验与CFD模拟
2.
Modeling of liquid circulation in gas-liquid bubble columns;
气液鼓泡床内的液体流速分布
3.
Comparison of bubble behavior between single orifice and porous spargers air-water bubble columns;
单孔及微孔曝气低气速鼓泡床内气泡行为比较
5) critical bubbling
临界鼓泡
1.
This paper introduces a new iodine addition process after fluid bed dryer in which amount of powder salt is greatly reduced by adopting a critical bubbling facility,resulting in the reduction of iodine loss.
本文介绍了一种新型的床后加碘工艺,采用临界鼓泡装置大大降低了粉盐的产生,从而减少了碘剂的损失。
6) bubbling tower
鼓泡塔
1.
Taking the bubbling tower of the flue gas desulfurization(FGD) system for 600 MW units in Taishan Power Plant and the spray tower of the FGD system for 660 MW units in Shajiao C Power Station for instance,this paper makes a comparative analysis of the bubbling tower and the spray tower in terms of their process,equipment parameters and operation features.
以台山发电厂600MW机组烟气脱硫装置的鼓泡塔和沙角C电厂660MW机组烟气脱硫装置的喷淋塔为例,从工艺技术、设备参数、运行特性等方面对鼓泡塔和喷淋塔进行了分析、比较。
2.
In the recent years,a lot of limestone-gypsum wet method flue gas desulfurization (FGD) facilities have been built up,commissioned or under construction,but over whelming majority of them employ the familiar spraying towers, while the people’s under standing of GT-121(bubbling tower) FGD technology is very limited.
而对CT121鼓泡塔脱硫技术了解并不多。
3.
Lime/Lime stone wet flue Gas Desulfurization(FGD) is a common proce ss to control SO2 emission,At the present home 600 MW and above 600 MW unit newly built all use Lime/Lime stone wet FGD process,and absorbed towers in wet desulfu rization process all use sprinkling tower and bubbling tower.
石灰石/石膏湿法烟气脱硫是控制SO2排放最常用的方法,目前国内新建的600MW及以上机组几乎全部运用石灰石/石膏湿法脱硫,而且湿法脱硫中的吸收塔基本采用喷淋塔和鼓泡塔2种塔型。
补充资料：鼓泡
分子式：
CAS号：
性质：聚式流化床在一定的气速范围内，床内出现颗粒密度接近临界流化状态的乳化相，和大量在乳化相中上升的气泡群。鼓泡床的流动模型(图暂缺)可简述为。(1)在分布板上方形成的气泡浮起时，就在自己的尾部拖曳了一部分颗粒，随之上升，称之为尾涡。尾涡上升过程中与乳化相中的颗粒不断交换。在床顶部气泡崩破，尾涡中颗粒重新进入乳化相，乳化相中的颗粒则处于向下环流运动中。(2)气泡中颗粒含量稀少，气泡中固体颗粒分率仅为0.002到0.01左右。(3)气泡的周围有一个气体环流层，称之为气泡云，气泡与气泡云之间、气泡云与乳化相之间有气体交换。(4)在乳化相中向上渗透的气体速度和向下流动的固体速度之间的相对速变由临界流化条件所决定。如果气泡尾涡总携带量很大，固体颗粒在乳化相中向下速度相当高时，乳化相中气体流动方向可能倒转，改为向下流动。
CAS号：
性质：聚式流化床在一定的气速范围内，床内出现颗粒密度接近临界流化状态的乳化相，和大量在乳化相中上升的气泡群。鼓泡床的流动模型(图暂缺)可简述为。(1)在分布板上方形成的气泡浮起时，就在自己的尾部拖曳了一部分颗粒，随之上升，称之为尾涡。尾涡上升过程中与乳化相中的颗粒不断交换。在床顶部气泡崩破，尾涡中颗粒重新进入乳化相，乳化相中的颗粒则处于向下环流运动中。(2)气泡中颗粒含量稀少，气泡中固体颗粒分率仅为0.002到0.01左右。(3)气泡的周围有一个气体环流层，称之为气泡云，气泡与气泡云之间、气泡云与乳化相之间有气体交换。(4)在乳化相中向上渗透的气体速度和向下流动的固体速度之间的相对速变由临界流化条件所决定。如果气泡尾涡总携带量很大，固体颗粒在乳化相中向下速度相当高时，乳化相中气体流动方向可能倒转，改为向下流动。
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