1) stirred tank
搅拌釜
1.
CFD technology of scale-up for stirred tank with three impellers on the conditions of same mixing performance;
三桨叶搅拌釜相同混合时间条件下的CFD模拟及放大研究
2.
Numerical simulation of three-dimensional flow in stirred tank with anisotropic differential Reynolds stress model;
搅拌釜三维流场的雷诺应力模型数值模拟
3.
The promoting effects of sodium sulfate, magnesium sulfate and sodium humate on limestone dissolution in flue gas desulfurization(FGD) process were studied in a stirred tank.
以双搅拌釜为实验设备,研究了烟气脱硫过程中硫酸钠、硫酸镁和腐殖酸钠对石灰石的促溶作用。
2) stirred vessel
搅拌釜
1.
Measurement of slurry concentration in stirred vessel based on AE measurement by wavelet transform;
声波的多尺度分解与搅拌釜中浆液浓度的测量
2.
The heat transfer coefficients of stirred vessel equipped with double coils were measured with water as heat transfer medium,using composite impellers.
以水为传热介质，采用组合桨，测定了装有双层蛇管的搅拌釜的传热系数。
3) Agitator
[英]['ædʒɪteɪtə(r)] [美]['ædʒə'tetɚ]
搅拌釜
1.
Development of the Measurement System for the Flow Field of Agitators;
搅拌釜流场测试系统的开发
2.
In order to avoid infecting from bacteria and disinfect thoroughly, it' s usually adopted in large and middle size agitators (such as fermenting tank) that cancel the middle and bottom bearing, install steady apparatus on the upper or lower part of the agitator shaft.
大中型搅拌釜如发酵罐等为了避免染菌和消毒彻底,常采用取消搅拌轴中间轴承和底部轴承,而在搅拌桨上方或下方加装稳定器的方法。
3.
By means of three dimensional flow field measured by two component laser Doppler anemometer,the three dimensional total pumping capacity coefficient was defined and caculated,which should be more accurate for agitators design.
简要分析了圆盘涡轮搅拌釜中泵送能力系数的研究情况及存在的问题。
5) Rushton stirred tank
Rushton搅拌釜
1.
Calculation for Rushton stirred tank with SST k-ω turbulence model;
应用SSTk-ω湍流模型计算Rushton搅拌釜流场
6) double-stirred cell
双搅拌釜
1.
Mass transfer and reaction kinetics of NO absorption with aqueous ferrous cysteine solution in double-stirred cell;
双搅拌釜中半胱氨酸亚铁溶液吸收NO的传质-反应动力学
补充资料：连续搅拌反应釜
分子式：
CAS号：
性质：又称连续搅拌反应釜。操作方式为连续进料、连续反应、连续出料，为带有搅拌桨叶的槽式反应设备。在稳态操作时，反应器同一部位的操作参数不随时间而变，有利于产品质量控制和过程自动控制。与间歇反应器操作方式不同，没有装料、卸料、升温等不发生化学反应的辅助时间，因而生产能力较大，辅助劳动少。适用于反应速度慢的液相反应，使用时可用单个反应槽(釜)，也可把几个反应槽(釜)串联成一组。
CAS号：
性质：又称连续搅拌反应釜。操作方式为连续进料、连续反应、连续出料，为带有搅拌桨叶的槽式反应设备。在稳态操作时，反应器同一部位的操作参数不随时间而变，有利于产品质量控制和过程自动控制。与间歇反应器操作方式不同，没有装料、卸料、升温等不发生化学反应的辅助时间，因而生产能力较大，辅助劳动少。适用于反应速度慢的液相反应，使用时可用单个反应槽(釜)，也可把几个反应槽(釜)串联成一组。
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